anexo a-201
TRANSCRIPT
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-SFluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.1240
26.00 *
19.00 *
3.500 *
197.2
2292
-6.112e+004
26.36
-2.349e+007
2213 *
Vapour Phase
0.1240
26.00
19.00
0.4339
15.32
229.3
-4.177e+004
39.78
-1.990e+006
---
Liquid Phase
0.8115
26.00
19.00
2.840
177.0
2032
-5.916e+004
25.38
-1.845e+007
1970
Aqueous Phase
0.0645
26.00
19.00
0.2259
4.872
30.73
-1.229e+005
12.93
-3.048e+006
30.20
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
Overall
47.14
0.2935
221.7
5597
-3.015
0.5592
28.34
0.6011
---
---
0.1000
7.767e-002
-0.2246
0.0000
---
0.7166
28.34
3.493
33.78
59.90
---
14.15
---
-2.128e-002
1.075
1.026
1.234e+004
---
35.00
2213
0.8760
3.407
261.8
0.1240
---
---
---
26.35
Vapour Phase
29.53
5.748e-002
27.19
3543
-3.289
1.347
13.91
0.4710
---
---
0.1000
7.767e-002
---
0.0000
13.82
0.8883
13.91
0.4331
26.23
---
0.8578
16.12
---
---
1.167
1.334
---
0.4081
---
---
0.0000
17.40
---
0.1240
---
1.497e-002
1.110e-002
11.92
Liquid Phase
52.15
0.6589
550.4
2023
-2.639
0.4867
31.32
0.6006
---
---
0.8866
0.8976
---
0.0000
---
0.6559
31.32
2.835
34.20
59.01
7.483e-002
14.00
---
---
1.068
1.068
---
0.2485
35.29
1970
1.000
1.518
---
0.8115
8.979
5.276e-002
0.1368
29.34
Aqueous Phase
18.04
3.484
1007
30.43
-15.84
0.7167
18.54
1.028
280.5
15.55
1.341e-002
2.470e-002
---
0.0000
---
3.450
18.54
0.2255
62.25
0.8876
1.415e-002
9.031
---
---
1.120
1.148
---
0.8836
63.34
30.20
1.000
0.2870
---
0.0645
71.83
0.3534
0.8898
16.56
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 1 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.5590
27.63
0.5861
---
---
---
17.18
33.19
2000
Vapour Phase
0.4037
10.43
0.3530
10.43
0.3530
1.334
---
106.9
0.0000
Liquid Phase
0.5625
29.34
0.5625
---
---
---
12.84
22.38
1970
Aqueous Phase
0.9176
16.15
0.8952
---
---
---
42.13
2.244
30.20
COMPOSITION
Overall Phase Vapour Fraction 0.1240
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
MOLAR FLOW (lbmole/hr)
33.8729 *
62.6067 *
90.8735 *
19.6436 *
61.4099 *
16.9583 *
21.1416 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
28.9267 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0881 *
0.1629 *
0.2365 *
0.0511 *
0.1598 *
0.0441 *
0.0550 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0753 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
543.4193 *
1882.5767 *
4007.2505 *
1141.7626 *
3569.3903 *
1223.5617 *
1525.3898 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
2492.8448 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0300 *
0.1039 *
0.2212 *
0.0630 *
0.1970 *
0.0675 *
0.0842 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1376 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
124.2826 *
362.4164 *
541.5427 *
139.1182 *
419.0614 *
134.3842 *
165.8614 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
257.5847 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0542 *
0.1581 *
0.2362 *
0.0607 *
0.1828 *
0.0586 *
0.0724 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1124 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 2 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.1240
COMPONENTS
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
5.1418 *
12.3177 *
0.0000 *
0.3140 *
25.0267 *
0.4612 *
0.6349 *
0.6103 *
0.5626 *
0.6395 *
1.4458 *
1.0819 *
0.4777 *
0.0942 *
0.0638 *
0.0104 *
0.0008 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0134 *
0.0321 *
0.0000 *
0.0008 *
0.0651 *
0.0012 *
0.0017 *
0.0016 *
0.0015 *
0.0017 *
0.0038 *
0.0028 *
0.0012 *
0.0002 *
0.0002 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
226.2877 *
419.7388 *
0.0000 *
8.7957 *
450.8583 *
35.3771 *
51.4071 *
51.7164 *
53.9515 *
64.5514 *
153.1101 *
125.3216 *
63.3055 *
14.2470 *
10.7223 *
2.0146 *
0.1809 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0125 *
0.0232 *
0.0000 *
0.0005 *
0.0249 *
0.0020 *
0.0028 *
0.0029 *
0.0030 *
0.0036 *
0.0085 *
0.0069 *
0.0035 *
0.0008 *
0.0006 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
18.7737 *
36.4541 *
0.0000 *
0.7469 *
30.9338 *
3.7834 *
5.4230 *
5.3681 *
5.5086 *
6.4504 *
14.9663 *
11.7468 *
5.6979 *
1.2513 *
0.9236 *
0.1699 *
0.0148 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0082 *
0.0159 *
0.0000 *
0.0003 *
0.0135 *
0.0017 *
0.0024 *
0.0023 *
0.0024 *
0.0028 *
0.0065 *
0.0051 *
0.0025 *
0.0005 *
0.0004 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 3 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.1240
COMPONENTS
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Total 384.3164 1.0000 18117.7817 1.0000 2292.4642 1.0000
Vapour Phase Phase Fraction 0.1240
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
MOLAR FLOW (lbmole/hr)
18.7957
13.5374
7.5274
0.7648
1.7854
0.2264
0.2205
0.0000
0.0000
0.0000
0.0000
0.0000
0.1112
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.3945
0.2841
0.1580
0.0161
0.0375
0.0048
0.0046
0.0000
0.0000
0.0000
0.0000
0.0000
0.0023
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
301.5373
407.0672
331.9379
44.4510
103.7758
16.3342
15.9115
0.0000
0.0000
0.0000
0.0000
0.0000
9.5802
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.2143
0.2893
0.2359
0.0316
0.0737
0.0116
0.0113
0.0000
0.0000
0.0000
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
68.9630
78.3648
44.8583
5.4161
12.1837
1.7940
1.7301
0.0000
0.0000
0.0000
0.0000
0.0000
0.9899
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.3008
0.3418
0.1956
0.0236
0.0531
0.0078
0.0075
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.1240
COMPONENTS
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
1.9233
2.4069
0.0000
0.2444
0.0876
0.0040
0.0038
0.0027
0.0018
0.0015
0.0024
0.0009
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0404
0.0505
0.0000
0.0051
0.0018
0.0001
0.0001
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
84.6444
82.0167
0.0000
6.8452
1.5789
0.3063
0.3103
0.2291
0.1741
0.1507
0.2570
0.1065
0.0174
0.0012
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0601
0.0583
0.0000
0.0049
0.0011
0.0002
0.0002
0.0002
0.0001
0.0001
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
7.0224
7.1231
0.0000
0.5813
0.1083
0.0328
0.0327
0.0238
0.0178
0.0151
0.0251
0.0100
0.0016
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0306
0.0311
0.0000
0.0025
0.0005
0.0001
0.0001
0.0001
0.0001
0.0001
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.1240
COMPONENTS
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 47.6483 1.0000 1407.2332 1.0000 229.2941 1.0000
Liquid Phase Phase Fraction 0.8115
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
MOLAR FLOW (lbmole/hr)
15.0772
49.0693
83.3461
18.8788
59.6245
16.7320
20.9211
0.0000
0.0000
0.0000
0.0000
0.0000
28.8156
0.0000
0.0000
0.0000
MOLE FRACTION
0.0483
0.1573
0.2673
0.0605
0.1912
0.0537
0.0671
0.0000
0.0000
0.0000
0.0000
0.0000
0.0924
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
241.8820
1475.5095
3675.3127
1097.3116
3465.6146
1207.2275
1509.4784
0.0000
0.0000
0.0000
0.0000
0.0000
2483.2646
0.0000
0.0000
0.0000
MASS FRACTION
0.0149
0.0907
0.2260
0.0675
0.2131
0.0742
0.0928
0.0000
0.0000
0.0000
0.0000
0.0000
0.1527
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
55.3196
284.0516
496.6844
133.7021
406.8777
132.5902
164.1313
0.0000
0.0000
0.0000
0.0000
0.0000
256.5948
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0272
0.1398
0.2444
0.0658
0.2002
0.0652
0.0808
0.0000
0.0000
0.0000
0.0000
0.0000
0.1262
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.8115
COMPONENTS
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
3.2100
9.8796
0.0000
0.0696
0.1749
0.4572
0.6311
0.6076
0.5608
0.6380
1.4434
1.0809
0.4776
0.0941
0.0638
0.0104
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0103
0.0317
0.0000
0.0002
0.0006
0.0015
0.0020
0.0019
0.0018
0.0020
0.0046
0.0035
0.0015
0.0003
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
141.2696
336.6575
0.0000
1.9496
3.1516
35.0708
51.0968
51.4873
53.7774
64.4006
152.8531
125.2151
63.2881
14.2457
10.7219
2.0146
0.1809
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0087
0.0207
0.0000
0.0001
0.0002
0.0022
0.0031
0.0032
0.0033
0.0040
0.0094
0.0077
0.0039
0.0009
0.0007
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
11.7202
29.2385
0.0000
0.1655
0.2162
3.7506
5.3903
5.3443
5.4909
6.4353
14.9412
11.7368
5.6964
1.2512
0.9235
0.1699
0.0148
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0058
0.0144
0.0000
0.0001
0.0001
0.0018
0.0027
0.0026
0.0027
0.0032
0.0074
0.0058
0.0028
0.0006
0.0005
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.8115
COMPONENTS
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 311.8643 1.0000 16262.9815 1.0000 2032.4373 1.0000
Aqueous Phase Phase Fraction 6.454e-002
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 8 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 6.454e-002
COMPONENTS
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0085
0.0312
0.0000
0.0000
24.7641
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0013
0.0000
0.0000
0.9984
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3737
1.0647
0.0000
0.0009
446.1277
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0008
0.0024
0.0000
0.0000
0.9968
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0310
0.0925
0.0000
0.0001
30.6093
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0010
0.0030
0.0000
0.0000
0.9960
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 9 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Litoral-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 6.454e-002
COMPONENTS
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 24.8039 1.0000 447.5670 1.0000 30.7328 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 10 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-SFluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.7448
90.00 *
19.00 *
3.500 *
197.2
2292
-5.407e+004
38.08
-2.078e+007
2213 *
Vapour Phase
0.7448
90.00
19.00
2.607
135.8
1660
-4.776e+004
41.10
-1.367e+007
1620
Liquid Phase
0.2181
90.00
19.00
0.7634
58.63
614.6
-6.428e+004
31.44
-5.388e+006
601.2
Aqueous Phase
0.0371
90.00
19.00
0.1300
2.801
17.66
-1.208e+005
16.51
-1.725e+006
17.36
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
Overall
47.14
6.530e-002
49.31
2.516e+004
-2.668
0.8077
27.29
0.5788
---
---
0.7242
0.6886
-0.6901
0.0000
---
0.7166
27.29
3.493
33.78
21.29
---
14.15
---
-0.2471
1.078
1.140
1.234e+004
---
35.00
2213
0.2552
15.31
261.8
0.7448
---
---
---
25.30
Vapour Phase
43.59
5.008e-002
34.97
2.443e+004
-2.549
0.9429
22.88
0.5249
---
---
0.7242
0.6886
---
0.0000
95.25
0.7370
22.88
2.602
32.12
---
0.8110
14.52
---
---
1.095
1.235
---
0.3348
32.92
1620
0.0000
19.97
---
0.7448
---
1.592e-002
1.171e-002
20.89
Liquid Phase
64.25
0.5037
518.3
711.4
-2.327
0.4894
43.78
0.6814
---
---
0.2681
0.2972
---
0.0000
---
0.5830
43.78
0.7619
37.45
20.75
8.065e-002
13.35
---
---
1.048
1.048
---
0.2155
38.29
601.2
1.000
1.985
---
0.2181
6.498
4.431e-002
0.1117
41.79
Aqueous Phase
18.02
3.314
956.9
18.41
-15.59
0.9161
18.81
1.043
103.0
5.712
7.702e-003
1.420e-002
---
0.0000
---
3.456
18.81
0.1298
62.29
0.5370
1.226e-002
9.110
---
---
1.118
1.172
---
0.3253
63.35
17.36
1.000
0.3017
---
0.0371
60.46
0.3905
0.3113
16.82
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 11 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.5367
23.94
0.5077
---
---
---
17.18
33.19
2239
Vapour Phase
0.4793
18.53
0.4251
18.53
0.4251
1.235
22.21
40.56
1620
Liquid Phase
0.6505
41.79
0.6505
---
---
---
4.894
8.188
601.2
Aqueous Phase
0.9333
16.04
0.8901
---
---
---
35.60
115.2
17.36
COMPOSITION
Overall Phase Vapour Fraction 0.7448
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
MOLAR FLOW (lbmole/hr)
33.8729 *
62.6067 *
90.8735 *
19.6436 *
61.4099 *
16.9583 *
21.1416 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
28.9267 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0881 *
0.1629 *
0.2365 *
0.0511 *
0.1598 *
0.0441 *
0.0550 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0753 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
543.4192 *
1882.5767 *
4007.2505 *
1141.7626 *
3569.3903 *
1223.5617 *
1525.3898 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
2492.8448 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0300 *
0.1039 *
0.2212 *
0.0630 *
0.1970 *
0.0675 *
0.0842 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1376 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
124.2826 *
362.4164 *
541.5427 *
139.1182 *
419.0614 *
134.3842 *
165.8614 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
257.5847 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0542 *
0.1581 *
0.2362 *
0.0607 *
0.1828 *
0.0586 *
0.0724 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1124 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 12 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.7448
COMPONENTS
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
5.1418 *
12.3177 *
0.0000 *
0.3140 *
25.0267 *
0.4612 *
0.6349 *
0.6103 *
0.5626 *
0.6395 *
1.4458 *
1.0819 *
0.4777 *
0.0942 *
0.0638 *
0.0104 *
0.0008 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0134 *
0.0321 *
0.0000 *
0.0008 *
0.0651 *
0.0012 *
0.0017 *
0.0016 *
0.0015 *
0.0017 *
0.0038 *
0.0028 *
0.0012 *
0.0002 *
0.0002 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
226.2877 *
419.7388 *
0.0000 *
8.7957 *
450.8583 *
35.3771 *
51.4071 *
51.7164 *
53.9515 *
64.5514 *
153.1101 *
125.3216 *
63.3055 *
14.2470 *
10.7223 *
2.0146 *
0.1809 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0125 *
0.0232 *
0.0000 *
0.0005 *
0.0249 *
0.0020 *
0.0028 *
0.0029 *
0.0030 *
0.0036 *
0.0085 *
0.0069 *
0.0035 *
0.0008 *
0.0006 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
18.7737 *
36.4541 *
0.0000 *
0.7469 *
30.9338 *
3.7834 *
5.4230 *
5.3681 *
5.5086 *
6.4504 *
14.9663 *
11.7468 *
5.6979 *
1.2513 *
0.9236 *
0.1699 *
0.0148 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0082 *
0.0159 *
0.0000 *
0.0003 *
0.0135 *
0.0017 *
0.0024 *
0.0023 *
0.0024 *
0.0028 *
0.0065 *
0.0051 *
0.0025 *
0.0005 *
0.0004 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.7448
COMPONENTS
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Total 384.3164 1.0000 18117.7817 1.0000 2292.4642 1.0000
Vapour Phase Phase Fraction 0.7448
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
MOLAR FLOW (lbmole/hr)
32.8591
57.6238
76.5365
14.7719
43.7735
9.9021
11.5531
0.0000
0.0000
0.0000
0.0000
0.0000
10.8362
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.1148
0.2013
0.2674
0.0516
0.1529
0.0346
0.0404
0.0000
0.0000
0.0000
0.0000
0.0000
0.0379
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
527.1553
1732.7423
3375.0299
858.6040
2544.2923
714.4450
833.5654
0.0000
0.0000
0.0000
0.0000
0.0000
933.8437
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0423
0.1389
0.2705
0.0688
0.2039
0.0573
0.0668
0.0000
0.0000
0.0000
0.0000
0.0000
0.0749
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
120.5629
333.5716
456.1040
104.6167
298.7106
78.4677
90.6367
0.0000
0.0000
0.0000
0.0000
0.0000
96.4937
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0726
0.2009
0.2747
0.0630
0.1799
0.0473
0.0546
0.0000
0.0000
0.0000
0.0000
0.0000
0.0581
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 14 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.7448
COMPONENTS
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
4.9029
11.2315
0.0000
0.3094
10.1888
0.2348
0.2836
0.2407
0.1931
0.1884
0.3605
0.1846
0.0412
0.0038
0.0013
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0171
0.0392
0.0000
0.0011
0.0356
0.0008
0.0010
0.0008
0.0007
0.0007
0.0013
0.0006
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
215.7765
382.7231
0.0000
8.6678
183.5531
18.0114
22.9593
20.3931
18.5188
19.0170
38.1763
21.3797
5.4654
0.5785
0.2223
0.0154
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0173
0.0307
0.0000
0.0007
0.0147
0.0014
0.0018
0.0016
0.0015
0.0015
0.0031
0.0017
0.0004
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17.9016
33.2393
0.0000
0.7360
12.5938
1.9262
2.4220
2.1168
1.8908
1.9003
3.7317
2.0040
0.4919
0.0508
0.0191
0.0013
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0108
0.0200
0.0000
0.0004
0.0076
0.0012
0.0015
0.0013
0.0011
0.0011
0.0022
0.0012
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 15 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.7448
COMPONENTS
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 286.2210 1.0000 12475.1360 1.0000 1660.1897 1.0000
Liquid Phase Phase Fraction 0.2181
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
MOLAR FLOW (lbmole/hr)
1.0138
4.9829
14.3370
4.8716
17.6364
7.0563
9.5886
0.0000
0.0000
0.0000
0.0000
0.0000
18.0905
0.0000
0.0000
0.0000
MOLE FRACTION
0.0121
0.0594
0.1710
0.0581
0.2104
0.0842
0.1144
0.0000
0.0000
0.0000
0.0000
0.0000
0.2158
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
16.2639
149.8345
632.2206
283.1586
1025.0980
509.1167
691.8244
0.0000
0.0000
0.0000
0.0000
0.0000
1559.0011
0.0000
0.0000
0.0000
MASS FRACTION
0.0030
0.0278
0.1174
0.0526
0.1903
0.0945
0.1285
0.0000
0.0000
0.0000
0.0000
0.0000
0.2895
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
3.7196
28.8448
85.4387
34.5015
120.3508
55.9164
75.2247
0.0000
0.0000
0.0000
0.0000
0.0000
161.0910
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0061
0.0469
0.1390
0.0561
0.1958
0.0910
0.1224
0.0000
0.0000
0.0000
0.0000
0.0000
0.2621
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 16 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.2181
COMPONENTS
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.2380
1.0797
0.0000
0.0046
0.5707
0.2264
0.3513
0.3696
0.3695
0.4511
1.0853
0.8973
0.4365
0.0903
0.0625
0.0103
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0028
0.0129
0.0000
0.0001
0.0068
0.0027
0.0042
0.0044
0.0044
0.0054
0.0129
0.0107
0.0052
0.0011
0.0007
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
10.4723
36.7911
0.0000
0.1278
10.2809
17.3657
28.4478
31.3233
35.4326
45.5344
114.9338
103.9419
57.8401
13.6685
10.5000
1.9992
0.1806
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0019
0.0068
0.0000
0.0000
0.0019
0.0032
0.0053
0.0058
0.0066
0.0085
0.0213
0.0193
0.0107
0.0025
0.0019
0.0004
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.8688
3.1953
0.0000
0.0109
0.7054
1.8572
3.0010
3.2513
3.6178
4.5501
11.2346
9.7428
5.2060
1.2005
0.9044
0.1686
0.0147
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0014
0.0052
0.0000
0.0000
0.0011
0.0030
0.0049
0.0053
0.0059
0.0074
0.0183
0.0159
0.0085
0.0020
0.0015
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 17 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.2181
COMPONENTS
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 83.8208 1.0000 5385.3577 1.0000 614.6170 1.0000
Aqueous Phase Phase Fraction 3.714e-002
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 18 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 3.714e-002
COMPONENTS
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0009
0.0066
0.0000
0.0000
14.2672
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0005
0.0000
0.0000
0.9995
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0389
0.2246
0.0000
0.0001
257.0243
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0009
0.0000
0.0000
0.9990
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0032
0.0195
0.0000
0.0000
17.6347
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0011
0.0000
0.0000
0.9987
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 19 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Pto-Ceiba-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 3.714e-002
COMPONENTS
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 14.2746 1.0000 257.2880 1.0000 17.6575 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 20 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Dulce-SFluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
56.00 *
16.50 *
1.030 *
31.28
516.6
-3.553e+004
40.61
-4.019e+006
---
Vapour Phase
1.0000
56.00
16.50
1.030
31.28
516.6
-3.553e+004
40.61
-4.019e+006
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
Overall
25.40
4.213e-002
17.14
1.148e+004
-3.254
1.599
12.99
0.5114
5.150e+005
2.028e+004
---
4.941e-324
-1.019
0.0000
44.74
0.9359
12.99
1.028
23.77
---
0.9310
17.11
---
-1.033
1.180
1.258
7379
0.7093
---
---
0.0000
23.74
290.5
1.0000
---
1.874e-002
1.216e-002
11.00
Vapour Phase
25.40
4.213e-002
17.14
1.148e+004
-3.254
1.599
12.99
0.5114
5.150e+005
2.028e+004
1.000
1.000
---
0.0000
44.74
0.9359
12.99
1.028
23.77
---
0.9310
17.11
---
---
1.180
1.258
---
0.7093
---
---
0.0000
23.74
---
1.0000
---
1.874e-002
1.216e-002
11.00
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 21 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Dulce-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.4332
10.32
0.4064
10.32
0.4064
1.258
---
---
0.0000
Vapour Phase
0.4332
10.32
0.4064
10.32
0.4064
1.258
---
---
0.0000
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
MOLAR FLOW (lbmole/hr)
69.7933 *
21.8394 *
11.9093 *
1.3911 *
3.4948 *
0.9274 *
1.1310 *
0.0113 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.6899 *
0.0000 *
0.0679 *
0.0226 *
0.0000 *
0.0565 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1244 *
0.0000 *
0.0000 *
0.0000 *
0.0226 *
0.0113 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0339 *
0.0000 *
0.0000 *
MOLE FRACTION
0.6171 *
0.1931 *
0.1053 *
0.0123 *
0.0309 *
0.0082 *
0.0100 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0061 *
0.0000 *
0.0006 *
0.0002 *
0.0000 *
0.0005 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0011 *
0.0000 *
0.0000 *
0.0000 *
0.0002 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0003 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
1119.6868 *
656.7081 *
525.1647 *
80.8572 *
203.1291 *
66.9136 *
81.6019 *
0.8160 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
59.4544 *
0.0000 *
5.7112 *
1.7668 *
0.0000 *
4.7592 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
12.4664 *
0.0000 *
0.0000 *
0.0000 *
2.2210 *
1.0421 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
3.8759 *
0.0000 *
0.0000 *
MASS FRACTION
0.3897 *
0.2286 *
0.1828 *
0.0281 *
0.0707 *
0.0233 *
0.0284 *
0.0003 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0207 *
0.0000 *
0.0020 *
0.0006 *
0.0000 *
0.0017 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0043 *
0.0000 *
0.0000 *
0.0000 *
0.0008 *
0.0004 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0013 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
256.0777 *
126.4234 *
70.9711 *
9.8521 *
23.8482 *
7.3491 *
8.8729 *
0.0938 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
6.1434 *
0.0000 *
0.5200 *
0.1371 *
0.0000 *
0.4168 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
1.2428 *
0.0000 *
0.0000 *
0.0000 *
0.1969 *
0.0820 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.3762 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.4957 *
0.2447 *
0.1374 *
0.0191 *
0.0462 *
0.0142 *
0.0172 *
0.0002 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0119 *
0.0000 *
0.0010 *
0.0003 *
0.0000 *
0.0008 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0024 *
0.0000 *
0.0000 *
0.0000 *
0.0004 *
0.0002 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0007 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 22 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Dulce-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0113 *
0.0000 *
0.0000 *
0.0905 *
0.0000 *
0.0000 *
1.4703 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0001 *
0.0000 *
0.0000 *
0.0008 *
0.0000 *
0.0000 *
0.0130 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
1.6092 *
0.0000 *
0.0000 *
3.9820 *
0.0000 *
0.0000 *
41.1871 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0006 *
0.0000 *
0.0000 *
0.0014 *
0.0000 *
0.0000 *
0.0143 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.1504 *
0.0000 *
0.0000 *
0.3304 *
0.0000 *
0.0000 *
3.4974 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0003 *
0.0000 *
0.0000 *
0.0006 *
0.0000 *
0.0000 *
0.0068 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 23 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Dulce-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Total 113.0988 1.0000 2872.9527 1.0000 516.5818 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
MOLAR FLOW (lbmole/hr)
69.7933
21.8394
11.9093
1.3911
3.4948
0.9274
1.1310
0.0113
0.0000
0.0000
0.0000
0.0000
0.6899
0.0000
0.0679
0.0226
0.0000
0.0565
0.0000
0.0000
0.0000
0.0000
0.0000
0.1244
0.0000
0.0000
MOLE FRACTION
0.6171
0.1931
0.1053
0.0123
0.0309
0.0082
0.0100
0.0001
0.0000
0.0000
0.0000
0.0000
0.0061
0.0000
0.0006
0.0002
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0011
0.0000
0.0000
MASS FLOW (lb/hr)
1119.6868
656.7081
525.1647
80.8572
203.1291
66.9136
81.6019
0.8160
0.0000
0.0000
0.0000
0.0000
59.4544
0.0000
5.7112
1.7668
0.0000
4.7592
0.0000
0.0000
0.0000
0.0000
0.0000
12.4664
0.0000
0.0000
MASS FRACTION
0.3897
0.2286
0.1828
0.0281
0.0707
0.0233
0.0284
0.0003
0.0000
0.0000
0.0000
0.0000
0.0207
0.0000
0.0020
0.0006
0.0000
0.0017
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
256.0777
126.4234
70.9711
9.8521
23.8482
7.3491
8.8729
0.0938
0.0000
0.0000
0.0000
0.0000
6.1434
0.0000
0.5200
0.1371
0.0000
0.4168
0.0000
0.0000
0.0000
0.0000
0.0000
1.2428
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.4957
0.2447
0.1374
0.0191
0.0462
0.0142
0.0172
0.0002
0.0000
0.0000
0.0000
0.0000
0.0119
0.0000
0.0010
0.0003
0.0000
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
0.0024
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 24 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Dulce-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0226
0.0113
0.0000
0.0000
0.0000
0.0000
0.0339
0.0000
0.0000
0.0000
0.0000
0.0000
0.0113
0.0000
0.0000
0.0905
0.0000
0.0000
1.4703
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0008
0.0000
0.0000
0.0130
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
2.2210
1.0421
0.0000
0.0000
0.0000
0.0000
3.8759
0.0000
0.0000
0.0000
0.0000
0.0000
1.6092
0.0000
0.0000
3.9820
0.0000
0.0000
41.1871
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0008
0.0004
0.0000
0.0000
0.0000
0.0000
0.0013
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
0.0000
0.0014
0.0000
0.0000
0.0143
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.1969
0.0820
0.0000
0.0000
0.0000
0.0000
0.3762
0.0000
0.0000
0.0000
0.0000
0.0000
0.1504
0.0000
0.0000
0.3304
0.0000
0.0000
3.4974
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0004
0.0002
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0006
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Dulce-S (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 113.0988 1.0000 2872.9527 1.0000 516.5818 1.0000
Material Stream: Gas-a-PilotosFluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
60.00 *
16.50 *
0.9485
28.80 *
475.7
-3.544e+004
40.77
-3.691e+006
---
Vapour Phase
1.0000
60.00
16.50
0.9485
28.80
475.7
-3.544e+004
40.77
-3.691e+006
---
PROPERTIES
Molecular Weight
Overall
25.40
Vapour Phase
25.40
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Gas-a-Pilotos (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
4.150e-002
16.89
1.073e+004
-3.245
1.605
13.05
0.5138
5.150e+005
2.028e+004
---
4.941e-324
-1.019
0.0000
41.82
0.9359
13.05
0.9467
23.77
---
0.9337
17.11
---
-1.033
1.179
1.254
7379
0.7276
---
---
0.0000
24.09
290.5
1.0000
---
1.903e-002
1.229e-002
11.07
0.4356
10.41
0.4098
10.41
0.4098
1.254
---
---
0.0000
Vapour Phase
4.150e-002
16.89
1.073e+004
-3.245
1.605
13.05
0.5138
5.150e+005
2.028e+004
1.000
1.000
---
0.0000
41.82
0.9359
13.05
0.9467
23.77
---
0.9337
17.11
---
---
1.179
1.254
---
0.7276
---
---
0.0000
24.09
---
1.0000
---
1.903e-002
1.229e-002
11.07
0.4356
10.41
0.4098
10.41
0.4098
1.254
---
---
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Gas-a-Pilotos (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
MOLAR FLOW (lbmole/hr)
64.2682 *
20.1105 *
10.9665 *
1.2810 *
3.2181 *
0.8540 *
1.0415 *
0.0104 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.6353 *
0.0000 *
0.0625 *
0.0208 *
0.0000 *
0.0521 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1146 *
0.0000 *
0.0000 *
0.0000 *
0.0208 *
0.0104 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0312 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0104 *
0.0000 *
0.0000 *
0.0833 *
0.0000 *
0.0000 *
1.3539 *
0.0000 *
0.0000 *
MOLE FRACTION
0.6171 *
0.1931 *
0.1053 *
0.0123 *
0.0309 *
0.0082 *
0.0100 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0061 *
0.0000 *
0.0006 *
0.0002 *
0.0000 *
0.0005 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0011 *
0.0000 *
0.0000 *
0.0000 *
0.0002 *
0.0001 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0003 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0001 *
0.0000 *
0.0000 *
0.0008 *
0.0000 *
0.0000 *
0.0130 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
1031.0486 *
604.7209 *
483.5909 *
74.4563 *
187.0487 *
61.6165 *
75.1421 *
0.7514 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
54.7478 *
0.0000 *
5.2591 *
1.6270 *
0.0000 *
4.3824 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
11.4795 *
0.0000 *
0.0000 *
0.0000 *
2.0452 *
0.9596 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
3.5690 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
1.4818 *
0.0000 *
0.0000 *
3.6667 *
0.0000 *
0.0000 *
37.9266 *
0.0000 *
0.0000 *
MASS FRACTION
0.3897 *
0.2286 *
0.1828 *
0.0281 *
0.0707 *
0.0233 *
0.0284 *
0.0003 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0207 *
0.0000 *
0.0020 *
0.0006 *
0.0000 *
0.0017 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0043 *
0.0000 *
0.0000 *
0.0000 *
0.0008 *
0.0004 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0013 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0006 *
0.0000 *
0.0000 *
0.0014 *
0.0000 *
0.0000 *
0.0143 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
235.8057 *
116.4153 *
65.3528 *
9.0721 *
21.9603 *
6.7674 *
8.1705 *
0.0864 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
5.6571 *
0.0000 *
0.4788 *
0.1263 *
0.0000 *
0.3838 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
1.1445 *
0.0000 *
0.0000 *
0.0000 *
0.1813 *
0.0755 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.3465 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.1385 *
0.0000 *
0.0000 *
0.3042 *
0.0000 *
0.0000 *
3.2205 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.4957 *
0.2447 *
0.1374 *
0.0191 *
0.0462 *
0.0142 *
0.0172 *
0.0002 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0119 *
0.0000 *
0.0010 *
0.0003 *
0.0000 *
0.0008 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0024 *
0.0000 *
0.0000 *
0.0000 *
0.0004 *
0.0002 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0007 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0003 *
0.0000 *
0.0000 *
0.0006 *
0.0000 *
0.0000 *
0.0068 *
0.0000 *
0.0000 *
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Gas-a-Pilotos (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 29 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Gas-a-Pilotos (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Total 104.1455 1.0000 2645.5200 1.0000 475.6874 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
MOLAR FLOW (lbmole/hr)
64.2682
20.1105
10.9665
1.2810
3.2181
0.8540
1.0415
0.0104
0.0000
0.0000
0.0000
0.0000
0.6353
0.0000
0.0625
0.0208
0.0000
0.0521
0.0000
0.0000
0.0000
0.0000
0.0000
0.1146
0.0000
0.0000
0.0000
0.0208
0.0104
0.0000
0.0000
0.0000
0.0000
0.0312
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.6171
0.1931
0.1053
0.0123
0.0309
0.0082
0.0100
0.0001
0.0000
0.0000
0.0000
0.0000
0.0061
0.0000
0.0006
0.0002
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0011
0.0000
0.0000
0.0000
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
1031.0486
604.7209
483.5909
74.4563
187.0487
61.6165
75.1421
0.7514
0.0000
0.0000
0.0000
0.0000
54.7478
0.0000
5.2591
1.6270
0.0000
4.3824
0.0000
0.0000
0.0000
0.0000
0.0000
11.4795
0.0000
0.0000
0.0000
2.0452
0.9596
0.0000
0.0000
0.0000
0.0000
3.5690
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.3897
0.2286
0.1828
0.0281
0.0707
0.0233
0.0284
0.0003
0.0000
0.0000
0.0000
0.0000
0.0207
0.0000
0.0020
0.0006
0.0000
0.0017
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
0.0000
0.0008
0.0004
0.0000
0.0000
0.0000
0.0000
0.0013
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
235.8057
116.4153
65.3528
9.0721
21.9603
6.7674
8.1705
0.0864
0.0000
0.0000
0.0000
0.0000
5.6571
0.0000
0.4788
0.1263
0.0000
0.3838
0.0000
0.0000
0.0000
0.0000
0.0000
1.1445
0.0000
0.0000
0.0000
0.1813
0.0755
0.0000
0.0000
0.0000
0.0000
0.3465
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.4957
0.2447
0.1374
0.0191
0.0462
0.0142
0.0172
0.0002
0.0000
0.0000
0.0000
0.0000
0.0119
0.0000
0.0010
0.0003
0.0000
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
0.0024
0.0000
0.0000
0.0000
0.0004
0.0002
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 30 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Gas-a-Pilotos (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0104
0.0000
0.0000
0.0833
0.0000
0.0000
1.3539
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0001
0.0000
0.0000
0.0008
0.0000
0.0000
0.0130
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
1.4818
0.0000
0.0000
3.6667
0.0000
0.0000
37.9266
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0006
0.0000
0.0000
0.0014
0.0000
0.0000
0.0143
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.1385
0.0000
0.0000
0.3042
0.0000
0.0000
3.2205
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0003
0.0000
0.0000
0.0006
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 31 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Gas-a-Pilotos (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 104.1455 1.0000 2645.5200 1.0000 475.6874 1.0000
Material Stream: G-Relevo-CompresoresFluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.9753
32.00 *
0.1055 *
10.00 *
563.5
6550
-5.364e+004
43.53
-5.891e+007
6321 *
Vapour Phase
0.9753
32.00
0.1055
9.753
557.8
6512
-5.190e+004
44.28
-5.559e+007
6307
Liquid Phase
0.0004
32.00
0.1055
4.201e-003
0.5460
4.802
-1.037e+005
45.81
-4.785e+004
4.746
Aqueous Phase
0.0242
32.00
0.1055
0.2425
5.222
32.91
-1.228e+005
13.26
-3.270e+006
32.37
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
Overall
47.14
2.873e-003
2.169
1.634e+006
-2.647
0.9233
19.67
0.4173
---
---
0.9942
0.9898
-1.018
Vapour Phase
47.84
2.802e-003
2.147
1.634e+006
-2.524
0.9255
19.69
0.4115
---
---
0.9942
0.9898
---
Liquid Phase
108.7
0.4069
708.6
4.846
-2.219
0.4214
53.97
0.4964
---
---
7.331e-004
9.689e-004
---
Aqueous Phase
18.02
3.472
1002
32.78
-15.86
0.7360
18.56
1.030
10.67
0.5920
5.025e-003
9.267e-003
---
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.0000
---
0.7166
19.67
9.981
33.78
1.097
---
14.15
---
-0.9958
1.112
1.118
1.530e+004
---
35.00
6321
2.467e-002
348.1
324.5
0.9753
---
---
---
17.69
0.3752
17.60
0.3734
---
---
---
17.18
33.19
6344
Vapour Phase
0.0000
6371
0.7030
19.69
9.735
33.63
---
0.9807
14.15
---
---
1.112
1.121
---
3.978
34.73
6307
0.0000
356.9
---
0.9753
---
1.063e-002
8.540e-003
17.70
0.3700
17.56
0.3671
17.55
0.3669
1.121
17.19
33.20
6307
Liquid Phase
0.0000
---
0.4107
53.97
4.193e-003
44.65
0.1413
6.753e-003
12.29
---
---
1.038
1.038
---
0.6685
45.18
4.746
1.000
2.458
---
0.0004
18.51
6.755e-002
0.4737
51.98
0.4781
51.98
0.4781
---
---
---
-9.649e-002
0.2632
4.746
Aqueous Phase
0.0000
---
3.458
18.56
0.2420
62.30
0.9561
7.913e-004
9.108
---
---
1.120
1.151
---
0.7626
63.35
32.37
1.000
0.2880
---
0.0242
70.88
0.3588
0.7642
16.57
0.9200
16.12
0.8948
---
---
---
35.33
-0.4482
32.37
COMPOSITION
Overall Phase Vapour Fraction 0.9753
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
MOLAR FLOW (lbmole/hr)
96.7797 *
178.8762 *
259.6387 *
56.1245 *
175.4569 *
48.4524 *
60.4047 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0881 *
0.1629 *
0.2365 *
0.0511 *
0.1598 *
0.0441 *
0.0550 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
1552.6264 *
5378.7907 *
11449.2873 *
3262.1789 *
10198.2581 *
3495.8905 *
4358.2567 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0300 *
0.1039 *
0.2212 *
0.0630 *
0.1970 *
0.0675 *
0.0842 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
355.0930 *
1035.4754 *
1547.2649 *
397.4807 *
1197.3183 *
383.9547 *
473.8898 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0542 *
0.1581 *
0.2362 *
0.0607 *
0.1828 *
0.0586 *
0.0724 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 33 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.9753
COMPONENTS
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
MOLAR FLOW (lbmole/hr)
0.0000 *
82.6478 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
14.6908 *
35.1935 *
0.0000 *
0.8971 *
71.5048 *
1.3177 *
1.8140 *
1.7437 *
1.6075 *
1.8272 *
4.1309 *
3.0910 *
1.3649 *
0.2690 *
0.1823 *
0.0296 *
0.0022 *
MOLE FRACTION
0.0000 *
0.0753 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0134 *
0.0321 *
0.0000 *
0.0008 *
0.0651 *
0.0012 *
0.0017 *
0.0016 *
0.0015 *
0.0017 *
0.0038 *
0.0028 *
0.0012 *
0.0002 *
0.0002 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
7122.4137 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
646.5364 *
1199.2538 *
0.0000 *
25.1306 *
1288.1665 *
101.0774 *
146.8774 *
147.7610 *
154.1471 *
184.4325 *
437.4573 *
358.0617 *
180.8729 *
40.7056 *
30.6351 *
5.7560 *
0.5170 *
MASS FRACTION
0.0000 *
0.1376 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0125 *
0.0232 *
0.0000 *
0.0005 *
0.0249 *
0.0020 *
0.0028 *
0.0029 *
0.0030 *
0.0036 *
0.0085 *
0.0069 *
0.0035 *
0.0008 *
0.0006 *
0.0001 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
735.9564 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
53.6390 *
104.1546 *
0.0000 *
2.1340 *
88.3824 *
10.8096 *
15.4944 *
15.3374 *
15.7390 *
18.4298 *
42.7608 *
33.5622 *
16.2798 *
3.5752 *
2.6388 *
0.4855 *
0.0422 *
LIQUID VOLUMEFRACTION
0.0000 *
0.1124 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0082 *
0.0159 *
0.0000 *
0.0003 *
0.0135 *
0.0017 *
0.0024 *
0.0023 *
0.0024 *
0.0028 *
0.0065 *
0.0051 *
0.0025 *
0.0005 *
0.0004 *
0.0001 *
0.0000 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 34 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.9753
COMPONENTS
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
MASS FRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUMEFRACTION
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Total 1098.0469 1.0000 51765.0906 1.0000 6549.8977 1.0000
Vapour Phase Phase Fraction 0.9753
COMPONENTS
Methane
MOLAR FLOW (lbmole/hr)
96.7794
MOLE FRACTION
0.0904
MASS FLOW (lb/hr)
1552.6228
MASS FRACTION
0.0303
LIQUID VOLUMEFLOW (barrel/day)
355.0922
LIQUID VOLUMEFRACTION
0.0545
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 35 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.9753
COMPONENTS
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
MOLAR FLOW (lbmole/hr)
178.8739
259.6269
56.1181
175.4289
48.4331
60.3726
0.0000
0.0000
0.0000
0.0000
0.0000
82.5083
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
14.6905
35.1916
0.0000
0.8971
44.8793
1.3168
1.8122
MOLE FRACTION
0.1670
0.2424
0.0524
0.1638
0.0452
0.0564
0.0000
0.0000
0.0000
0.0000
0.0000
0.0770
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0137
0.0329
0.0000
0.0008
0.0419
0.0012
0.0017
MASS FLOW (lb/hr)
5378.7217
11448.7673
3261.8072
10196.6275
3494.4941
4355.9461
0.0000
0.0000
0.0000
0.0000
0.0000
7110.3951
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
646.5250
1199.1896
0.0000
25.1306
808.5052
101.0109
146.7305
MASS FRACTION
0.1050
0.2235
0.0637
0.1990
0.0682
0.0850
0.0000
0.0000
0.0000
0.0000
0.0000
0.1388
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0126
0.0234
0.0000
0.0005
0.0158
0.0020
0.0029
LIQUID VOLUMEFLOW (barrel/day)
1035.4621
1547.1946
397.4354
1197.1268
383.8014
473.6386
0.0000
0.0000
0.0000
0.0000
0.0000
734.7145
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53.6381
104.1490
0.0000
2.1339
55.4724
10.8025
15.4789
LIQUID VOLUMEFRACTION
0.1590
0.2376
0.0610
0.1838
0.0589
0.0727
0.0000
0.0000
0.0000
0.0000
0.0000
0.1128
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0082
0.0160
0.0000
0.0003
0.0085
0.0017
0.0024
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 36 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.9753
COMPONENTS
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
MOLAR FLOW (lbmole/hr)
1.7412
1.6042
1.8217
4.1127
3.0612
1.3174
0.2364
0.1267
0.0088
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0016
0.0015
0.0017
0.0038
0.0029
0.0012
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
147.5494
153.8285
183.8783
435.5305
354.6063
174.5820
35.7671
21.2900
1.7079
0.0173
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0029
0.0030
0.0036
0.0085
0.0069
0.0034
0.0007
0.0004
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
15.3154
15.7065
18.3744
42.5725
33.2383
15.7136
3.1414
1.8338
0.1441
0.0014
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0024
0.0024
0.0028
0.0065
0.0051
0.0024
0.0005
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 37 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.9753
COMPONENTS
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
Total 1070.9590 1.0000 51235.2309 1.0000 6512.1817 1.0000
Liquid Phase Phase Fraction 4.201e-004
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
MOLAR FLOW (lbmole/hr)
0.0002
0.0023
0.0118
0.0064
0.0281
0.0194
0.0320
0.0000
0.0000
0.0000
0.0000
0.0000
0.1395
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0005
0.0050
0.0256
0.0139
0.0608
0.0420
0.0694
0.0000
0.0000
0.0000
0.0000
0.0000
0.3023
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0037
0.0690
0.5200
0.3717
1.6306
1.3964
2.3106
0.0000
0.0000
0.0000
0.0000
0.0000
12.0187
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0001
0.0014
0.0104
0.0074
0.0325
0.0278
0.0461
0.0000
0.0000
0.0000
0.0000
0.0000
0.2396
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0008
0.0133
0.0703
0.0453
0.1914
0.1534
0.2512
0.0000
0.0000
0.0000
0.0000
0.0000
1.2419
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0002
0.0028
0.0146
0.0094
0.0399
0.0319
0.0523
0.0000
0.0000
0.0000
0.0000
0.0000
0.2586
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 38 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 4.201e-004
COMPONENTS
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0001
0.0006
0.0000
0.0000
0.0003
0.0009
0.0018
0.0025
0.0033
0.0055
0.0182
0.0298
0.0475
0.0326
0.0556
0.0209
0.0021
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0002
0.0013
0.0000
0.0000
0.0007
0.0019
0.0039
0.0054
0.0072
0.0119
0.0394
0.0647
0.1029
0.0708
0.1205
0.0452
0.0046
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0040
0.0207
0.0000
0.0000
0.0054
0.0665
0.1469
0.2116
0.3185
0.5543
1.9268
3.4553
6.2909
4.9385
9.3451
4.0481
0.4997
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0013
0.0029
0.0042
0.0064
0.0111
0.0384
0.0689
0.1254
0.0985
0.1863
0.0807
0.0100
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0003
0.0018
0.0000
0.0000
0.0004
0.0071
0.0155
0.0220
0.0325
0.0554
0.1883
0.3239
0.5662
0.4337
0.8049
0.3414
0.0407
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0015
0.0032
0.0046
0.0068
0.0115
0.0392
0.0674
0.1179
0.0903
0.1676
0.0711
0.0085
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 4.201e-004
COMPONENTS
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 0.4613 1.0000 50.1530 1.0000 4.8019 1.0000
Aqueous Phase Phase Fraction 2.425e-002
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 2.425e-002
COMPONENTS
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0013
0.0000
0.0000
26.6252
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0074
0.0435
0.0000
0.0000
479.6558
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0038
0.0000
0.0000
32.9097
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: G-Relevo-Compresores (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 2.425e-002
COMPONENTS
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 26.6267 1.0000 479.7066 1.0000 32.9141 1.0000
Material Stream: CondensadosFluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
32.00 *
1.500 *
2.580
418.1
3429 *
-1.262e+005
64.37
-3.575e+007
3396 *
Liquid Phase
0.9995
32.00
1.500
2.579
418.1
3428
-1.262e+005
64.40
-3.573e+007
3396
Aqueous Phase
0.0005
32.00
1.500
1.229e-003
2.646e-002
0.1668
-1.228e+005
13.26
-1.657e+004
0.1640
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
(lbmole/ft3)
(kg/m3)
(barrel/day)
Overall
135.6
0.3503
760.8
3457
Liquid Phase
135.6
0.3502
760.8
3457
Aqueous Phase
18.02
3.472
1002
0.1661
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
-2.165
0.4748
64.23
0.4738
---
---
---
2.122e-314
-1.033
0.0000
---
0.3532
64.23
2.575
47.89
100.8
---
11.94
---
-1.033
1.032
1.145
3.834e+004
1.132
48.35
3396
1.000
2.854
282.8
0.0000
---
7.365e-002
0.8614
62.24
0.4591
56.08
0.4137
---
---
---
-0.4525
2.982e-002
3396
Liquid Phase
-2.164
0.4748
64.25
0.4737
---
---
1.000
0.9999
---
0.0000
---
0.3531
64.25
2.574
47.89
100.8
1.746e-002
11.94
---
---
1.032
1.145
---
1.132
48.35
3396
1.000
2.856
---
0.9995
21.51
7.364e-002
0.8612
62.26
0.4591
56.10
0.4136
---
---
---
-0.4525
1.149e-002
3396
Aqueous Phase
-15.86
0.7360
18.56
1.030
11.78
0.6538
4.864e-005
6.328e-005
---
0.0000
---
3.458
18.56
1.226e-003
62.30
4.844e-003
1.760e-003
9.076
---
---
1.120
1.151
---
0.7626
63.35
0.1640
1.000
0.2880
---
0.0005
70.88
0.3588
0.7642
16.57
0.9200
16.12
0.8948
---
---
---
38.17
-0.4572
0.1640
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methane
Ethane
MOLAR FLOW (lbmole/hr)
0.2595 *
1.4589 *
MOLE FRACTION
0.0009 *
0.0051 *
MASS FLOW (lb/hr)
4.1636 *
43.8676 *
MASS FRACTION
0.0001 *
0.0011 *
LIQUID VOLUMEFLOW (barrel/day)
0.9522 *
8.4450 *
LIQUID VOLUMEFRACTION
0.0003 *
0.0025 *
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 43 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
MOLAR FLOW (lbmole/hr)
4.6656 *
1.9595 *
8.0932 *
3.6702 *
5.4617 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
19.6955 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0887 *
0.4207 *
0.0000 *
0.0006 *
0.3173 *
2.7743 *
4.0640 *
4.1176 *
MOLE FRACTION
0.0165 *
0.0069 *
0.0286 *
0.0130 *
0.0193 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0695 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0003 *
0.0015 *
0.0000 *
0.0000 *
0.0011 *
0.0098 *
0.0143 *
0.0145 *
MASS FLOW (lb/hr)
205.7369 *
113.8936 *
470.4120 *
264.8103 *
394.0674 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
1697.3176 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
3.9028 *
14.3372 *
0.0000 *
0.0159 *
5.7167 *
212.8198 *
329.0661 *
348.9252 *
MASS FRACTION
0.0054 *
0.0030 *
0.0122 *
0.0069 *
0.0103 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0442 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0001 *
0.0004 *
0.0000 *
0.0000 *
0.0001 *
0.0055 *
0.0086 *
0.0091 *
LIQUID VOLUMEFLOW (barrel/day)
27.8034 *
13.8774 *
55.2283 *
29.0842 *
42.8484 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
175.3832 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.3238 *
1.2452 *
0.0000 *
0.0013 *
0.3922 *
22.7597 *
34.7139 *
36.2180 *
LIQUID VOLUMEFRACTION
0.0081 *
0.0040 *
0.0161 *
0.0085 *
0.0125 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0512 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0001 *
0.0004 *
0.0000 *
0.0000 *
0.0001 *
0.0066 *
0.0101 *
0.0106 *
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
MOLAR FLOW (lbmole/hr)
4.0261 *
4.9106 *
12.1332 *
11.9088 *
10.6336 *
5.6419 *
10.0536 *
7.1299 *
3.9754 *
1.3399 *
0.1317 *
0.0068 *
0.0006 *
0.0000 *
6.2474 *
9.3521 *
8.0329 *
8.2006 *
7.5399 *
4.4927 *
4.4389 *
9.1302 *
4.8814 *
7.3784 *
4.0099 *
2.4692 *
4.0094 *
3.3090 *
2.3182 *
14.6426 *
1.1276 *
1.8609 *
1.2092 *
0.9797 *
4.0281 *
0.7021 *
0.7556 *
1.1257 *
1.1806 *
1.4759 *
4.6333 *
4.7778 *
4.6772 *
3.0829 *
7.4388 *
6.2842 *
5.9541 *
2.3836 *
MOLE FRACTION
0.0142 *
0.0173 *
0.0428 *
0.0420 *
0.0375 *
0.0199 *
0.0355 *
0.0252 *
0.0140 *
0.0047 *
0.0005 *
0.0000 *
0.0000 *
0.0000 *
0.0221 *
0.0330 *
0.0284 *
0.0289 *
0.0266 *
0.0159 *
0.0157 *
0.0322 *
0.0172 *
0.0260 *
0.0142 *
0.0087 *
0.0142 *
0.0117 *
0.0082 *
0.0517 *
0.0040 *
0.0066 *
0.0043 *
0.0035 *
0.0142 *
0.0025 *
0.0027 *
0.0040 *
0.0042 *
0.0052 *
0.0164 *
0.0169 *
0.0165 *
0.0109 *
0.0263 *
0.0222 *
0.0210 *
0.0084 *
MASS FLOW (lb/hr)
386.0611 *
495.6792 *
1284.9075 *
1379.5177 *
1409.1598 *
853.6758 *
1689.7072 *
1384.2770 *
935.8015 *
379.8491 *
44.1643 *
2.6692 *
0.2581 *
0.0000 *
618.4897 *
1028.7280 *
1004.1125 *
1131.6869 *
1161.1462 *
741.2994 *
799.0004 *
1789.5246 *
1015.3414 *
1638.0079 *
938.3245 *
604.9537 *
384.8992 *
357.3700 *
278.1822 *
2108.5411 *
202.9758 *
187.9504 *
145.1090 *
131.2860 *
604.2100 *
53.8570 *
61.1837 *
95.3884 *
113.0213 *
148.7069 *
488.9473 *
542.1792 *
613.4576 *
463.2653 *
1247.2573 *
1210.5261 *
1394.0397 *
667.0600 *
MASS FRACTION
0.0101 *
0.0129 *
0.0335 *
0.0359 *
0.0367 *
0.0222 *
0.0440 *
0.0360 *
0.0244 *
0.0099 *
0.0011 *
0.0001 *
0.0000 *
0.0000 *
0.0161 *
0.0268 *
0.0261 *
0.0295 *
0.0302 *
0.0193 *
0.0208 *
0.0466 *
0.0264 *
0.0426 *
0.0244 *
0.0157 *
0.0100 *
0.0093 *
0.0072 *
0.0549 *
0.0053 *
0.0049 *
0.0038 *
0.0034 *
0.0157 *
0.0014 *
0.0016 *
0.0025 *
0.0029 *
0.0039 *
0.0127 *
0.0141 *
0.0160 *
0.0121 *
0.0325 *
0.0315 *
0.0363 *
0.0174 *
LIQUID VOLUMEFLOW (barrel/day)
39.4183 *
49.5316 *
125.5978 *
129.3062 *
126.8343 *
74.9780 *
145.5444 *
116.7566 *
76.3039 *
30.2737 *
3.4194 *
0.2024 *
0.0193 *
0.0000 *
59.2586 *
94.9760 *
90.0281 *
99.5476 *
100.5081 *
62.5865 *
66.9553 *
146.2322 *
81.3461 *
130.2811 *
73.6302 *
46.7971 *
36.3184 *
32.9706 *
24.7016 *
184.2446 *
15.7570 *
17.9917 *
13.4256 *
11.8366 *
52.8492 *
5.7987 *
6.4100 *
9.9104 *
11.5126 *
14.8239 *
47.5576 *
49.3245 *
54.3545 *
40.2399 *
107.0109 *
100.7550 *
112.6552 *
52.0993 *
LIQUID VOLUMEFRACTION
0.0115 *
0.0144 *
0.0366 *
0.0377 *
0.0370 *
0.0219 *
0.0425 *
0.0341 *
0.0223 *
0.0088 *
0.0010 *
0.0001 *
0.0000 *
0.0000 *
0.0173 *
0.0277 *
0.0263 *
0.0290 *
0.0293 *
0.0183 *
0.0195 *
0.0427 *
0.0237 *
0.0380 *
0.0215 *
0.0136 *
0.0106 *
0.0096 *
0.0072 *
0.0537 *
0.0046 *
0.0052 *
0.0039 *
0.0035 *
0.0154 *
0.0017 *
0.0019 *
0.0029 *
0.0034 *
0.0043 *
0.0139 *
0.0144 *
0.0159 *
0.0117 *
0.0312 *
0.0294 *
0.0329 *
0.0152 *
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.2465 *
0.0102 *
0.0011 *
MOLE FRACTION
0.0009 *
0.0000 *
0.0000 *
MASS FLOW (lb/hr)
80.9711 *
3.8993 *
0.4988 *
MASS FRACTION
0.0021 *
0.0001 *
0.0000 *
LIQUID VOLUMEFLOW (barrel/day)
6.0929 *
0.2859 *
0.0358 *
LIQUID VOLUMEFRACTION
0.0018 *
0.0001 *
0.0000 *
Total 283.3275 1.0000 38410.1780 1.0000 3428.5714 1.0000
Liquid Phase Phase Fraction 0.9995
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
MOLAR FLOW (lbmole/hr)
0.2595
1.4589
4.6656
1.9595
8.0932
3.6702
5.4617
0.0000
0.0000
0.0000
0.0000
0.0000
19.6955
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0009
0.0052
0.0165
0.0069
0.0286
0.0130
0.0193
0.0000
0.0000
0.0000
0.0000
0.0000
0.0695
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
4.1636
43.8676
205.7369
113.8936
470.4120
264.8103
394.0674
0.0000
0.0000
0.0000
0.0000
0.0000
1697.3176
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0001
0.0011
0.0054
0.0030
0.0122
0.0069
0.0103
0.0000
0.0000
0.0000
0.0000
0.0000
0.0442
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.9522
8.4450
27.8034
13.8774
55.2283
29.0842
42.8484
0.0000
0.0000
0.0000
0.0000
0.0000
175.3832
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0003
0.0025
0.0081
0.0040
0.0161
0.0085
0.0125
0.0000
0.0000
0.0000
0.0000
0.0000
0.0512
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 46 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.9995
COMPONENTS
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0887
0.4207
0.0000
0.0006
0.1824
2.7743
4.0640
4.1176
4.0261
4.9106
12.1332
11.9088
10.6336
5.6419
10.0536
7.1299
3.9754
1.3399
0.1317
0.0068
0.0006
0.0000
6.2474
9.3521
8.0329
8.2006
7.5399
4.4927
4.4389
9.1302
4.8814
7.3784
4.0099
2.4692
4.0094
3.3090
2.3182
14.6426
1.1276
1.8609
1.2092
0.9797
4.0281
0.7021
0.7556
1.1257
MOLE FRACTION
0.0000
0.0000
0.0003
0.0015
0.0000
0.0000
0.0006
0.0098
0.0144
0.0145
0.0142
0.0173
0.0428
0.0421
0.0375
0.0199
0.0355
0.0252
0.0140
0.0047
0.0005
0.0000
0.0000
0.0000
0.0221
0.0330
0.0284
0.0290
0.0266
0.0159
0.0157
0.0322
0.0172
0.0261
0.0142
0.0087
0.0142
0.0117
0.0082
0.0517
0.0040
0.0066
0.0043
0.0035
0.0142
0.0025
0.0027
0.0040
MASS FLOW (lb/hr)
0.0000
0.0000
3.9028
14.3369
0.0000
0.0159
3.2864
212.8198
329.0661
348.9252
386.0611
495.6792
1284.9075
1379.5177
1409.1598
853.6758
1689.7072
1384.2770
935.8015
379.8491
44.1643
2.6692
0.2581
0.0000
618.4897
1028.7280
1004.1125
1131.6869
1161.1462
741.2994
799.0004
1789.5246
1015.3414
1638.0079
938.3245
604.9537
384.8992
357.3700
278.1822
2108.5411
202.9758
187.9504
145.1090
131.2860
604.2100
53.8570
61.1837
95.3884
MASS FRACTION
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0055
0.0086
0.0091
0.0101
0.0129
0.0335
0.0359
0.0367
0.0222
0.0440
0.0360
0.0244
0.0099
0.0011
0.0001
0.0000
0.0000
0.0161
0.0268
0.0261
0.0295
0.0302
0.0193
0.0208
0.0466
0.0264
0.0426
0.0244
0.0158
0.0100
0.0093
0.0072
0.0549
0.0053
0.0049
0.0038
0.0034
0.0157
0.0014
0.0016
0.0025
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.3238
1.2452
0.0000
0.0013
0.2255
22.7597
34.7139
36.2180
39.4183
49.5316
125.5978
129.3062
126.8343
74.9780
145.5444
116.7566
76.3039
30.2737
3.4194
0.2024
0.0193
0.0000
59.2586
94.9760
90.0281
99.5476
100.5081
62.5865
66.9553
146.2322
81.3461
130.2811
73.6302
46.7971
36.3184
32.9706
24.7016
184.2446
15.7570
17.9917
13.4256
11.8366
52.8492
5.7987
6.4100
9.9104
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0066
0.0101
0.0106
0.0115
0.0144
0.0366
0.0377
0.0370
0.0219
0.0425
0.0341
0.0223
0.0088
0.0010
0.0001
0.0000
0.0000
0.0173
0.0277
0.0263
0.0290
0.0293
0.0183
0.0195
0.0427
0.0237
0.0380
0.0215
0.0136
0.0106
0.0096
0.0072
0.0537
0.0046
0.0052
0.0039
0.0035
0.0154
0.0017
0.0019
0.0029
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 47 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.9995
COMPONENTS
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
1.1806
1.4759
4.6333
4.7778
4.6772
3.0829
7.4388
6.2842
5.9541
2.3836
0.2465
0.0102
0.0011
MOLE FRACTION
0.0042
0.0052
0.0164
0.0169
0.0165
0.0109
0.0263
0.0222
0.0210
0.0084
0.0009
0.0000
0.0000
MASS FLOW (lb/hr)
113.0213
148.7069
488.9473
542.1792
613.4576
463.2653
1247.2573
1210.5261
1394.0397
667.0600
80.9711
3.8993
0.4988
MASS FRACTION
0.0029
0.0039
0.0127
0.0141
0.0160
0.0121
0.0325
0.0315
0.0363
0.0174
0.0021
0.0001
0.0000
LIQUID VOLUMEFLOW (barrel/day)
11.5126
14.8239
47.5576
49.3245
54.3545
40.2399
107.0109
100.7550
112.6552
52.0993
6.0929
0.2859
0.0358
LIQUID VOLUMEFRACTION
0.0034
0.0043
0.0139
0.0144
0.0159
0.0117
0.0312
0.0294
0.0329
0.0152
0.0018
0.0001
0.0000
Total 283.1926 1.0000 38407.7474 1.0000 3428.4047 1.0000
Aqueous Phase Phase Fraction 4.762e-004
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 4.762e-004
COMPONENTS
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1349
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0002
0.0000
0.0000
2.4303
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1667
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9998
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 49 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: Condensados (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 4.762e-004
COMPONENTS
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 0.1349 1.0000 2.4306 1.0000 0.1668 1.0000
Material Stream: 1300Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.6203
43.47
9.725
8.030
425.7
5102
-5.476e+004
34.26
-4.829e+007
5000 *
Vapour Phase
0.6203
43.47
9.725
4.981
219.7
2951
-4.329e+004
40.72
-2.368e+007
3096
Liquid Phase
0.3285
43.47
9.725
2.638
197.2
2095
-6.590e+004
25.21
-1.909e+007
2052
Aqueous Phase
0.0511
43.47
9.725
0.4107
8.848
55.78
-1.224e+005
13.96
-5.519e+006
54.84
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
Overall
44.35
4.382e-002
31.13
8.601e+004
-2.872
Vapour Phase
36.90
2.791e-002
16.49
8.378e+004
-2.729
Liquid Phase
62.53
0.5701
571.1
2172
-2.451
Aqueous Phase
18.02
3.441
993.5
56.01
-15.79
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.7723
23.53
0.5306
---
---
0.5784
0.5161
-0.8412
0.0000
---
0.7388
23.53
8.015
32.77
64.98
---
14.36
---
-0.6135
1.092
1.087
1.383e+004
---
33.43
5000
0.3797
22.82
311.8
0.6203
---
---
---
21.55
0.4858
21.65
0.4882
---
---
---
23.00
48.48
5202
Vapour Phase
1.104
16.83
0.4560
---
---
0.5784
0.5161
---
0.0000
326.7
0.7923
16.83
4.972
29.23
---
0.8965
15.25
---
---
1.134
1.213
---
0.6325
27.87
3096
0.0000
35.83
---
0.6203
---
1.382e-002
1.043e-002
14.84
0.4022
13.88
0.3761
13.83
0.3747
1.217
38.50
67.29
3096
Liquid Phase
0.4032
36.97
0.5912
---
---
0.4106
0.4632
---
0.0000
---
0.5911
36.97
2.633
36.96
63.35
4.388e-002
13.44
---
---
1.057
1.057
---
0.2714
37.74
2052
1.000
1.754
---
0.3285
10.10
5.277e-002
0.1550
34.99
0.5595
34.99
0.5595
---
---
---
5.313
8.820
2052
Aqueous Phase
0.7743
18.57
1.030
93.28
5.176
1.093e-002
2.078e-002
---
0.0000
---
3.456
18.57
0.4099
62.29
1.634
7.270e-003
9.099
---
---
1.120
1.157
---
0.6146
63.35
54.84
1.000
0.2906
---
0.0511
68.86
0.3673
0.6106
16.58
0.9201
16.05
0.8903
---
---
---
36.15
18.27
54.84
COMPOSITION
Overall Phase Vapour Fraction 0.6203
COMPONENTS
Methane
Ethane
Propane
MOLAR FLOW (lbmole/hr)
137.5391
147.0528
193.6564
MOLE FRACTION
0.1560
0.1668
0.2196
MASS FLOW (lb/hr)
2206.5253
4421.8616
8539.6658
MASS FRACTION
0.0564
0.1131
0.2184
LIQUID VOLUMEFLOW (barrel/day)
504.6428
851.2562
1154.0566
LIQUID VOLUMEFRACTION
0.0989
0.1669
0.2262
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.6203
COMPONENTS
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
MOLAR FLOW (lbmole/hr)
40.6782
126.3146
34.8441
43.4143
0.0113
0.0000
0.0000
0.0000
0.0000
58.5434
0.0000
0.0679
0.0226
0.0000
0.0565
0.0000
0.0000
0.0000
0.0000
0.0000
0.1244
0.0000
0.0000
0.0000
0.0226
0.0113
0.0000
0.0000
0.0000
0.0000
0.0339
0.0000
0.0000
0.0000
0.0000
0.0000
0.0113
0.0000
0.0000
10.3740
24.6355
0.0000
2.0983
50.0534
0.9224
1.2698
1.2206
1.1253
MOLE FRACTION
0.0461
0.1433
0.0395
0.0492
0.0000
0.0000
0.0000
0.0000
0.0000
0.0664
0.0000
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.0279
0.0000
0.0024
0.0568
0.0010
0.0014
0.0014
0.0013
MASS FLOW (lb/hr)
2364.3824
7341.9097
2514.0370
3132.3816
0.8160
0.0000
0.0000
0.0000
0.0000
5045.1440
0.0000
5.7112
1.7668
0.0000
4.7592
0.0000
0.0000
0.0000
0.0000
0.0000
12.4664
0.0000
0.0000
0.0000
2.2210
1.0421
0.0000
0.0000
0.0000
0.0000
3.8759
0.0000
0.0000
0.0000
0.0000
0.0000
1.6092
0.0000
0.0000
456.5574
839.4777
0.0000
58.7785
901.7165
70.7542
102.8142
103.4327
107.9030
MASS FRACTION
0.0605
0.1877
0.0643
0.0801
0.0000
0.0000
0.0000
0.0000
0.0000
0.1290
0.0000
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0117
0.0215
0.0000
0.0015
0.0231
0.0018
0.0026
0.0026
0.0028
LIQUID VOLUMEFLOW (barrel/day)
288.0885
861.9710
276.1175
340.5958
0.0938
0.0000
0.0000
0.0000
0.0000
521.3129
0.0000
0.5200
0.1371
0.0000
0.4168
0.0000
0.0000
0.0000
0.0000
0.0000
1.2428
0.0000
0.0000
0.0000
0.1969
0.0820
0.0000
0.0000
0.0000
0.0000
0.3762
0.0000
0.0000
0.0000
0.0000
0.0000
0.1504
0.0000
0.0000
37.8777
72.9082
0.0000
4.9911
61.8677
7.5667
10.8461
10.7362
11.0173
LIQUID VOLUMEFRACTION
0.0565
0.1690
0.0541
0.0668
0.0000
0.0000
0.0000
0.0000
0.0000
0.1022
0.0000
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0074
0.0143
0.0000
0.0010
0.0121
0.0015
0.0021
0.0021
0.0022
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.6203
COMPONENTS
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
MOLAR FLOW (lbmole/hr)
1.2790
2.8916
2.1637
0.9554
0.1883
0.1276
0.0208
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0015
0.0033
0.0025
0.0011
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
129.1028
306.2201
250.6432
126.6110
28.4939
21.4446
4.0292
0.3619
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0033
0.0078
0.0064
0.0032
0.0007
0.0005
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
12.9008
29.9326
23.4935
11.3959
2.5026
1.8471
0.3398
0.0295
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0025
0.0059
0.0046
0.0022
0.0005
0.0004
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.6203
COMPONENTS
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
Total 881.7317 1.0000 39108.5161 1.0000 5101.5102 1.0000
Vapour Phase Phase Fraction 0.6203
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
MOLAR FLOW (lbmole/hr)
133.3788
129.6759
138.6575
21.7630
58.4523
9.8447
10.3094
0.0045
0.0000
0.0000
0.0000
0.0000
6.1222
0.0000
0.0068
0.0024
0.0000
0.0049
0.0000
0.0000
0.0000
0.0000
0.0000
0.0054
0.0000
0.0000
0.0000
0.0011
0.0004
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.2438
0.2371
0.2535
0.0398
0.1069
0.0180
0.0188
0.0000
0.0000
0.0000
0.0000
0.0000
0.0112
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
2139.7826
3899.3413
6114.3810
1264.9515
3397.4798
710.3079
743.8329
0.3241
0.0000
0.0000
0.0000
0.0000
527.6014
0.0000
0.5743
0.1854
0.0000
0.4098
0.0000
0.0000
0.0000
0.0000
0.0000
0.5431
0.0000
0.0000
0.0000
0.1041
0.0413
0.0000
0.0000
0.0000
0.0000
0.0684
0.0000
0.0000
0.0000
0.0000
0.0000
0.0050
0.0000
MASS FRACTION
0.1060
0.1932
0.3030
0.0627
0.1683
0.0352
0.0369
0.0000
0.0000
0.0000
0.0000
0.0000
0.0261
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
489.3784
750.6654
826.3018
154.1282
398.8784
78.0133
80.8798
0.0373
0.0000
0.0000
0.0000
0.0000
54.5169
0.0000
0.0523
0.0144
0.0000
0.0359
0.0000
0.0000
0.0000
0.0000
0.0000
0.0541
0.0000
0.0000
0.0000
0.0092
0.0032
0.0000
0.0000
0.0000
0.0000
0.0066
0.0000
0.0000
0.0000
0.0000
0.0000
0.0005
0.0000
LIQUID VOLUMEFRACTION
0.1658
0.2544
0.2800
0.0522
0.1352
0.0264
0.0274
0.0000
0.0000
0.0000
0.0000
0.0000
0.0185
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.6203
COMPONENTS
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
MOLAR FLOW (lbmole/hr)
0.0000
9.7620
21.3417
0.0000
2.0749
4.6441
0.1890
0.1945
0.1439
0.1004
0.0853
0.1422
0.0560
0.0084
0.0005
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0178
0.0390
0.0000
0.0038
0.0085
0.0003
0.0004
0.0003
0.0002
0.0002
0.0003
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
429.6211
727.2381
0.0000
58.1236
83.6645
14.5003
15.7513
12.1912
9.6319
8.6076
15.0600
6.4845
1.1107
0.0816
0.0234
0.0011
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0213
0.0360
0.0000
0.0029
0.0041
0.0007
0.0008
0.0006
0.0005
0.0004
0.0007
0.0003
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
35.6429
63.1603
0.0000
4.9355
5.7403
1.5507
1.6616
1.2654
0.9835
0.8601
1.4721
0.6078
0.1000
0.0072
0.0020
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0121
0.0214
0.0000
0.0017
0.0019
0.0005
0.0006
0.0004
0.0003
0.0003
0.0005
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 55 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.6203
COMPONENTS
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 546.9730 1.0000 20182.0248 1.0000 2950.9653 1.0000
Liquid Phase Phase Fraction 0.3285
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
MOLAR FLOW (lbmole/hr)
4.1603
17.3769
54.9989
18.9153
67.8623
24.9994
33.1049
0.0068
0.0000
0.0000
0.0000
0.0000
52.4211
0.0000
0.0610
0.0202
0.0000
0.0517
0.0000
0.0000
0.0000
0.0000
0.0000
0.1190
0.0000
0.0000
0.0000
0.0216
0.0109
0.0000
0.0000
MOLE FRACTION
0.0144
0.0600
0.1899
0.0653
0.2343
0.0863
0.1143
0.0000
0.0000
0.0000
0.0000
0.0000
0.1810
0.0000
0.0002
0.0001
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0004
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
66.7427
522.5203
2425.2848
1099.4309
3944.4299
1803.7291
2388.5487
0.4919
0.0000
0.0000
0.0000
0.0000
4517.5426
0.0000
5.1369
1.5814
0.0000
4.3494
0.0000
0.0000
0.0000
0.0000
0.0000
11.9233
0.0000
0.0000
0.0000
2.1169
1.0008
0.0000
0.0000
MASS FRACTION
0.0037
0.0288
0.1339
0.0607
0.2178
0.0996
0.1319
0.0000
0.0000
0.0000
0.0000
0.0000
0.2494
0.0000
0.0003
0.0001
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0001
0.0001
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
15.2644
100.5908
327.7547
133.9603
463.0926
198.1041
259.7160
0.0566
0.0000
0.0000
0.0000
0.0000
466.7960
0.0000
0.4677
0.1227
0.0000
0.3809
0.0000
0.0000
0.0000
0.0000
0.0000
1.1887
0.0000
0.0000
0.0000
0.1877
0.0788
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0073
0.0480
0.1565
0.0639
0.2211
0.0946
0.1240
0.0000
0.0000
0.0000
0.0000
0.0000
0.2228
0.0000
0.0002
0.0001
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 56 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.3285
COMPONENTS
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0333
0.0000
0.0000
0.0000
0.0000
0.0000
0.0113
0.0000
0.0000
0.6093
3.2749
0.0000
0.0234
0.3365
0.7333
1.0752
1.0767
1.0248
1.1937
2.7494
2.1077
0.9470
0.1878
0.1275
0.0207
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0021
0.0113
0.0000
0.0001
0.0012
0.0025
0.0037
0.0037
0.0035
0.0041
0.0095
0.0073
0.0033
0.0006
0.0004
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
3.8075
0.0000
0.0000
0.0000
0.0000
0.0000
1.6042
0.0000
0.0000
26.8165
111.5960
0.0000
0.6544
6.0613
56.2539
87.0629
91.2415
98.2711
120.4951
291.1601
244.1586
125.5003
28.4123
21.4212
4.0281
0.3619
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0015
0.0062
0.0000
0.0000
0.0003
0.0031
0.0048
0.0050
0.0054
0.0067
0.0161
0.0135
0.0069
0.0016
0.0012
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.3696
0.0000
0.0000
0.0000
0.0000
0.0000
0.1499
0.0000
0.0000
2.2248
9.6921
0.0000
0.0556
0.4159
6.0160
9.1844
9.4707
10.0338
12.0407
28.4605
22.8857
11.2959
2.4954
1.8451
0.3398
0.0295
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0011
0.0046
0.0000
0.0000
0.0002
0.0029
0.0044
0.0045
0.0048
0.0057
0.0136
0.0109
0.0054
0.0012
0.0009
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.3285
COMPONENTS
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 289.6643 1.0000 18113.7366 1.0000 2094.7675 1.0000
Aqueous Phase Phase Fraction 5.114e-002
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 5.114e-002
COMPONENTS
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0027
0.0189
0.0000
0.0000
45.0728
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.9995
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1199
0.6435
0.0000
0.0005
811.9907
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0008
0.0000
0.0000
0.9991
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0099
0.0559
0.0000
0.0000
55.7115
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0010
0.0000
0.0000
0.9988
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1300 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 5.114e-002
COMPONENTS
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 45.0944 1.0000 812.7546 1.0000 55.7774 1.0000
Material Stream: 1304Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Overall
0.6936
28.08
4.500 *
8.030
425.7
5102
-5.476e+004
35.07
-4.829e+007
Vapour Phase
0.6936
28.08
4.500
5.570
254.5
3362
-4.411e+004
41.13
-2.698e+007
Liquid Phase
0.2546
28.08
4.500
2.044
162.3
1683
-6.992e+004
23.04
-1.569e+007
Aqueous Phase
0.0518
28.08
4.500
0.4161
8.963
56.50
-1.229e+005
13.03
-5.616e+006
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Liq Vol Flow @Std Cond (barrel/day)
Overall
5000 *
Vapour Phase
3471
Liquid Phase
1655
Aqueous Phase
55.55
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
44.35
2.065e-002
14.67
1.826e+005
-2.872
0.7907
21.65
0.4882
---
---
0.6590
0.5977
-0.9418
0.0000
---
0.7388
21.65
8.015
32.77
51.05
---
14.36
---
-0.8252
1.101
1.088
1.434e+004
---
33.43
5000
0.3064
48.44
323.4
0.6936
---
---
---
19.67
0.4434
19.89
0.4485
---
---
---
23.00
48.48
5181
Vapour Phase
38.22
1.446e-002
8.852
1.808e+005
-2.684
1.076
16.32
0.4269
---
---
0.6590
0.5977
---
0.0000
705.0
0.7777
16.32
5.559
29.72
---
0.9355
15.11
---
---
1.139
1.182
---
1.081
28.79
3471
0.0000
69.16
---
0.6936
---
1.229e-002
9.570e-003
14.33
0.3750
13.80
0.3612
14.68
0.3842
1.111
34.76
62.46
3471
Liquid Phase
66.43
0.5663
602.6
1694
-2.448
0.3469
36.82
0.5543
---
---
0.3300
0.3812
---
0.0000
---
0.5700
36.82
2.040
37.86
49.41
2.388e-002
13.28
---
---
1.057
1.057
---
0.3249
38.51
1655
1.000
1.766
---
0.2546
12.65
5.725e-002
0.1958
34.83
0.5244
34.83
0.5244
---
---
---
3.570
5.571
1655
Aqueous Phase
18.02
3.482
1005
56.09
-15.87
0.7229
18.56
1.030
61.88
3.434
1.107e-002
2.105e-002
---
0.0000
---
3.457
18.56
0.4153
62.29
1.636
3.885e-003
9.100
---
---
1.120
1.149
---
0.8269
63.35
55.55
1.000
0.2872
---
0.0518
71.55
0.3556
0.8312
16.57
0.9195
16.15
0.8962
---
---
---
36.02
1.361
55.55
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase Vapour Fraction 0.6936
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
MOLAR FLOW (lbmole/hr)
137.5391
147.0528
193.6564
40.6782
126.3146
34.8441
43.4143
0.0113
0.0000
0.0000
0.0000
0.0000
58.5434
0.0000
0.0679
0.0226
0.0000
0.0565
0.0000
0.0000
0.0000
0.0000
0.0000
0.1244
0.0000
0.0000
0.0000
0.0226
0.0113
0.0000
0.0000
0.0000
0.0000
0.0339
0.0000
0.0000
0.0000
0.0000
0.0000
0.0113
0.0000
0.0000
10.3740
24.6355
0.0000
2.0983
50.0534
0.9224
MOLE FRACTION
0.1560
0.1668
0.2196
0.0461
0.1433
0.0395
0.0492
0.0000
0.0000
0.0000
0.0000
0.0000
0.0664
0.0000
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0118
0.0279
0.0000
0.0024
0.0568
0.0010
MASS FLOW (lb/hr)
2206.5253
4421.8616
8539.6658
2364.3824
7341.9097
2514.0370
3132.3816
0.8160
0.0000
0.0000
0.0000
0.0000
5045.1440
0.0000
5.7112
1.7668
0.0000
4.7592
0.0000
0.0000
0.0000
0.0000
0.0000
12.4664
0.0000
0.0000
0.0000
2.2210
1.0421
0.0000
0.0000
0.0000
0.0000
3.8759
0.0000
0.0000
0.0000
0.0000
0.0000
1.6092
0.0000
0.0000
456.5574
839.4777
0.0000
58.7785
901.7165
70.7542
MASS FRACTION
0.0564
0.1131
0.2184
0.0605
0.1877
0.0643
0.0801
0.0000
0.0000
0.0000
0.0000
0.0000
0.1290
0.0000
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0117
0.0215
0.0000
0.0015
0.0231
0.0018
LIQUID VOLUMEFLOW (barrel/day)
504.6428
851.2562
1154.0566
288.0885
861.9710
276.1175
340.5958
0.0938
0.0000
0.0000
0.0000
0.0000
521.3129
0.0000
0.5200
0.1371
0.0000
0.4168
0.0000
0.0000
0.0000
0.0000
0.0000
1.2428
0.0000
0.0000
0.0000
0.1969
0.0820
0.0000
0.0000
0.0000
0.0000
0.3762
0.0000
0.0000
0.0000
0.0000
0.0000
0.1504
0.0000
0.0000
37.8777
72.9082
0.0000
4.9911
61.8677
7.5667
LIQUID VOLUMEFRACTION
0.0989
0.1669
0.2262
0.0565
0.1690
0.0541
0.0668
0.0000
0.0000
0.0000
0.0000
0.0000
0.1022
0.0000
0.0001
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0074
0.0143
0.0000
0.0010
0.0121
0.0015
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 62 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.6936
COMPONENTS
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
MOLAR FLOW (lbmole/hr)
1.2698
1.2206
1.1253
1.2790
2.8916
2.1637
0.9554
0.1883
0.1276
0.0208
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0014
0.0014
0.0013
0.0015
0.0033
0.0025
0.0011
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
102.8142
103.4327
107.9030
129.1028
306.2201
250.6432
126.6110
28.4939
21.4446
4.0292
0.3619
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0026
0.0026
0.0028
0.0033
0.0078
0.0064
0.0032
0.0007
0.0005
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
10.8461
10.7362
11.0173
12.9008
29.9326
23.4935
11.3959
2.5026
1.8471
0.3398
0.0295
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0021
0.0021
0.0022
0.0025
0.0059
0.0046
0.0022
0.0005
0.0004
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 63 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.6936
COMPONENTS
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
Total 881.7317 1.0000 39108.5161 1.0000 5101.5102 1.0000
Vapour Phase Phase Fraction 0.6936
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
MOLAR FLOW (lbmole/hr)
135.9732
138.6966
160.5749
27.1269
74.4901
13.0082
13.5306
0.0059
0.0000
0.0000
0.0000
0.0000
7.5839
0.0000
0.0085
0.0030
0.0000
0.0059
0.0000
0.0000
0.0000
0.0000
0.0000
0.0060
0.0000
0.0000
0.0000
0.0012
0.0005
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.2223
0.2268
0.2625
0.0444
0.1218
0.0213
0.0221
0.0000
0.0000
0.0000
0.0000
0.0000
0.0124
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
2181.4049
4170.5938
7080.8720
1576.7262
4329.6613
938.5517
976.2466
0.4223
0.0000
0.0000
0.0000
0.0000
653.5687
0.0000
0.7135
0.2307
0.0000
0.5004
0.0000
0.0000
0.0000
0.0000
0.0000
0.6056
0.0000
0.0000
0.0000
0.1196
0.0453
0.0000
0.0000
0.0000
0.0000
0.0674
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0933
0.1784
0.3029
0.0675
0.1852
0.0402
0.0418
0.0000
0.0000
0.0000
0.0000
0.0000
0.0280
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
498.8976
802.8844
956.9141
192.1164
508.3204
103.0814
106.1510
0.0485
0.0000
0.0000
0.0000
0.0000
67.5330
0.0000
0.0650
0.0179
0.0000
0.0438
0.0000
0.0000
0.0000
0.0000
0.0000
0.0604
0.0000
0.0000
0.0000
0.0106
0.0036
0.0000
0.0000
0.0000
0.0000
0.0065
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.1484
0.2388
0.2846
0.0571
0.1512
0.0307
0.0316
0.0000
0.0000
0.0000
0.0000
0.0000
0.0201
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 64 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.6936
COMPONENTS
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
10.1084
22.9967
0.0000
2.0907
4.2536
0.2484
0.2511
0.1815
0.1231
0.1010
0.1621
0.0588
0.0076
0.0004
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0165
0.0376
0.0000
0.0034
0.0070
0.0004
0.0004
0.0003
0.0002
0.0002
0.0003
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0039
0.0000
0.0000
444.8684
783.6365
0.0000
58.5654
76.6296
19.0535
20.3285
15.3766
11.7997
10.1905
17.1613
6.8090
1.0047
0.0634
0.0160
0.0006
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0190
0.0335
0.0000
0.0025
0.0033
0.0008
0.0009
0.0007
0.0005
0.0004
0.0007
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0004
0.0000
0.0000
36.9079
68.0584
0.0000
4.9730
5.2576
2.0376
2.1445
1.5961
1.2048
1.0183
1.6775
0.6382
0.0904
0.0056
0.0014
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0110
0.0202
0.0000
0.0015
0.0016
0.0006
0.0006
0.0005
0.0004
0.0003
0.0005
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 65 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.6936
COMPONENTS
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 611.5994 1.0000 23375.8376 1.0000 3361.7667 1.0000
Liquid Phase Phase Fraction 0.2546
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
MOLAR FLOW (lbmole/hr)
1.5658
8.3561
33.0815
13.5513
51.8245
21.8359
29.8836
0.0055
0.0000
0.0000
0.0000
0.0000
50.9594
0.0000
0.0594
0.0197
0.0000
0.0506
0.0000
0.0000
0.0000
0.0000
0.0000
0.1184
0.0000
0.0000
0.0000
0.0214
MOLE FRACTION
0.0070
0.0372
0.1474
0.0604
0.2309
0.0973
0.1331
0.0000
0.0000
0.0000
0.0000
0.0000
0.2270
0.0000
0.0003
0.0001
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0005
0.0000
0.0000
0.0000
0.0001
MASS FLOW (lb/hr)
25.1204
251.2678
1458.7938
787.6563
3012.2485
1575.4853
2156.1350
0.3937
0.0000
0.0000
0.0000
0.0000
4391.5753
0.0000
4.9977
1.5361
0.0000
4.2588
0.0000
0.0000
0.0000
0.0000
0.0000
11.8608
0.0000
0.0000
0.0000
2.1014
MASS FRACTION
0.0017
0.0169
0.0978
0.0528
0.2020
0.1057
0.1446
0.0000
0.0000
0.0000
0.0000
0.0000
0.2946
0.0000
0.0003
0.0001
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0008
0.0000
0.0000
0.0000
0.0001
LIQUID VOLUMEFLOW (barrel/day)
5.7451
48.3718
197.1424
95.9721
353.6506
173.0360
234.4448
0.0453
0.0000
0.0000
0.0000
0.0000
453.7799
0.0000
0.4550
0.1192
0.0000
0.3730
0.0000
0.0000
0.0000
0.0000
0.0000
1.1825
0.0000
0.0000
0.0000
0.1863
LIQUID VOLUMEFRACTION
0.0034
0.0287
0.1171
0.0570
0.2101
0.1028
0.1393
0.0000
0.0000
0.0000
0.0000
0.0000
0.2696
0.0000
0.0003
0.0001
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0001
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 66 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.2546
COMPONENTS
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
MOLAR FLOW (lbmole/hr)
0.0108
0.0000
0.0000
0.0000
0.0000
0.0333
0.0000
0.0000
0.0000
0.0000
0.0000
0.0113
0.0000
0.0000
0.2638
1.6260
0.0000
0.0076
0.1277
0.6740
1.0187
1.0391
1.0022
1.1780
2.7295
2.1049
0.9478
0.1879
0.1275
0.0207
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0012
0.0072
0.0000
0.0000
0.0006
0.0030
0.0045
0.0046
0.0045
0.0052
0.0122
0.0094
0.0042
0.0008
0.0006
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.9968
0.0000
0.0000
0.0000
0.0000
3.8085
0.0000
0.0000
0.0000
0.0000
0.0000
1.6054
0.0000
0.0000
11.6094
55.4085
0.0000
0.2128
2.3002
51.7007
82.4857
88.0561
96.1033
118.9123
289.0588
243.8342
125.6064
28.4306
21.4286
4.0286
0.3619
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0001
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0008
0.0037
0.0000
0.0000
0.0002
0.0035
0.0055
0.0059
0.0064
0.0080
0.0194
0.0164
0.0084
0.0019
0.0014
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0785
0.0000
0.0000
0.0000
0.0000
0.3697
0.0000
0.0000
0.0000
0.0000
0.0000
0.1500
0.0000
0.0000
0.9632
4.8122
0.0000
0.0181
0.1578
5.5291
8.7016
9.1401
9.8125
11.8825
28.2551
22.8553
11.3055
2.4970
1.8458
0.3398
0.0295
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0006
0.0029
0.0000
0.0000
0.0001
0.0033
0.0052
0.0054
0.0058
0.0071
0.0168
0.0136
0.0067
0.0015
0.0011
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 67 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.2546
COMPONENTS
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 224.4457 1.0000 14909.3792 1.0000 1683.2471 1.0000
Aqueous Phase Phase Fraction 5.181e-002
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 5.181e-002
COMPONENTS
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0018
0.0127
0.0000
0.0000
45.6721
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.9997
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0796
0.4326
0.0000
0.0003
822.7867
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0005
0.0000
0.0000
0.9994
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0066
0.0376
0.0000
0.0000
56.4522
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0007
0.0000
0.0000
0.9992
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 69 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1304 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 5.181e-002
COMPONENTS
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 45.6866 1.0000 823.2993 1.0000 56.4964 1.0000
Material Stream: 1404Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Overall
0.9757
31.79
8.318e-002
10.00
563.5
6550
Vapour Phase
0.9757
31.79
8.318e-002
9.757
557.9
6513
Liquid Phase
0.0004
31.79
8.318e-002
3.786e-003
0.4957
4.350
Aqueous Phase
0.0239
31.79
8.318e-002
0.2391
5.149
32.45
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
-5.364e+004
43.56
-5.890e+007
6321 *
Vapour Phase
-5.193e+004
44.31
-5.564e+007
6307
Liquid Phase
-1.044e+005
46.26
-4.341e+004
4.299
Aqueous Phase
-1.228e+005
13.25
-3.224e+006
31.91
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
Overall
47.14
2.816e-003
2.127
1.667e+006
-2.647
0.9241
19.66
0.4170
---
---
0.9944
0.9900
-1.018
0.0000
---
0.7166
19.66
9.981
33.78
1.070
---
14.15
---
-0.9966
1.112
1.118
1.530e+004
---
35.00
6321
2.429e-002
355.1
324.6
0.9757
---
---
---
17.67
0.3748
17.59
0.3730
---
---
---
Vapour Phase
47.83
2.748e-003
2.105
1.667e+006
-2.525
0.9263
19.67
0.4112
---
---
0.9944
0.9900
---
0.0000
6498
0.7032
19.67
9.739
33.63
---
0.9810
14.15
---
---
1.112
1.121
---
4.053
34.73
6307
0.0000
363.9
---
0.9757
---
1.062e-002
8.533e-003
17.68
0.3697
17.55
0.3669
17.21
0.3597
1.143
Liquid Phase
109.5
0.4049
710.4
4.389
-2.218
0.4224
54.27
0.4955
---
---
6.642e-004
8.795e-004
---
0.0000
---
0.4085
54.27
3.779e-003
44.74
0.1280
6.658e-003
12.28
---
---
1.038
1.038
---
0.6801
45.27
4.299
1.000
2.470
---
0.0004
18.61
6.776e-002
0.4831
52.28
0.4773
52.28
0.4773
---
---
---
Aqueous Phase
18.02
3.473
1002
32.31
-15.86
0.7353
18.56
1.030
10.49
0.5824
4.955e-003
9.137e-003
---
0.0000
---
3.458
18.56
0.2386
62.30
0.9425
7.762e-004
9.108
---
---
1.120
1.151
---
0.7658
63.35
31.91
1.000
0.2879
---
0.0239
70.92
0.3587
0.7675
16.57
0.9200
16.12
0.8949
---
---
---
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 71 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
17.18
33.19
6344
Vapour Phase
17.19
33.20
6307
Liquid Phase
-0.1112
0.2452
4.299
Aqueous Phase
35.33
-0.4693
31.91
COMPOSITION
Overall Phase Vapour Fraction 0.9757
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
MOLAR FLOW (lbmole/hr)
96.7797
178.8762
259.6387
56.1245
175.4569
48.4524
60.4047
0.0000
0.0000
0.0000
0.0000
0.0000
82.6478
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0881
0.1629
0.2365
0.0511
0.1598
0.0441
0.0550
0.0000
0.0000
0.0000
0.0000
0.0000
0.0753
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
1552.6264
5378.7907
11449.2873
3262.1789
10198.2581
3495.8905
4358.2567
0.0000
0.0000
0.0000
0.0000
0.0000
7122.4137
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0300
0.1039
0.2212
0.0630
0.1970
0.0675
0.0842
0.0000
0.0000
0.0000
0.0000
0.0000
0.1376
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
355.0930
1035.4754
1547.2649
397.4807
1197.3183
383.9547
473.8898
0.0000
0.0000
0.0000
0.0000
0.0000
735.9564
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0542
0.1581
0.2362
0.0607
0.1828
0.0586
0.0724
0.0000
0.0000
0.0000
0.0000
0.0000
0.1124
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.9757
COMPONENTS
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
MOLAR FLOW (lbmole/hr)
14.6908
35.1935
0.0000
0.8971
71.5048
1.3177
1.8140
1.7437
1.6075
1.8272
4.1309
3.0910
1.3649
0.2690
0.1823
0.0296
0.0022
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0134
0.0321
0.0000
0.0008
0.0651
0.0012
0.0017
0.0016
0.0015
0.0017
0.0038
0.0028
0.0012
0.0002
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
646.5364
1199.2538
0.0000
25.1306
1288.1665
101.0774
146.8774
147.7610
154.1471
184.4325
437.4573
358.0617
180.8729
40.7056
30.6351
5.7560
0.5170
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0125
0.0232
0.0000
0.0005
0.0249
0.0020
0.0028
0.0029
0.0030
0.0036
0.0085
0.0069
0.0035
0.0008
0.0006
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
53.6390
104.1546
0.0000
2.1340
88.3824
10.8096
15.4944
15.3374
15.7390
18.4298
42.7608
33.5622
16.2798
3.5752
2.6388
0.4855
0.0422
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0082
0.0159
0.0000
0.0003
0.0135
0.0017
0.0024
0.0023
0.0024
0.0028
0.0065
0.0051
0.0025
0.0005
0.0004
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 73 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.9757
COMPONENTS
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 1098.0469 1.0000 51765.0906 1.0000 6549.8977 1.0000
Vapour Phase Phase Fraction 0.9757
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
MOLAR FLOW (lbmole/hr)
96.7795
178.8742
259.6282
56.1188
175.4320
48.4352
60.3762
0.0000
0.0000
0.0000
0.0000
0.0000
82.5235
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0903
0.1670
0.2423
0.0524
0.1637
0.0452
0.0564
0.0000
0.0000
0.0000
0.0000
0.0000
0.0770
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
1552.6232
5378.7296
11448.8266
3261.8491
10196.8109
3494.6495
4356.2021
0.0000
0.0000
0.0000
0.0000
0.0000
7111.7054
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0303
0.1050
0.2234
0.0637
0.1990
0.0682
0.0850
0.0000
0.0000
0.0000
0.0000
0.0000
0.1388
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
355.0923
1035.4637
1547.2026
397.4405
1197.1484
383.8184
473.6664
0.0000
0.0000
0.0000
0.0000
0.0000
734.8499
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0545
0.1590
0.2376
0.0610
0.1838
0.0589
0.0727
0.0000
0.0000
0.0000
0.0000
0.0000
0.1128
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 74 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.9757
COMPONENTS
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
14.6905
35.1917
0.0000
0.8971
45.2532
1.3169
1.8124
1.7415
1.6046
1.8223
4.1146
3.0643
1.3222
0.2394
0.1307
0.0094
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0137
0.0328
0.0000
0.0008
0.0422
0.0012
0.0017
0.0016
0.0015
0.0017
0.0038
0.0029
0.0012
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
646.5257
1199.1933
0.0000
25.1306
815.2403
101.0182
146.7466
147.5726
153.8632
183.9382
435.7374
354.9718
175.2202
36.2179
21.9648
1.8341
0.0190
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0126
0.0234
0.0000
0.0005
0.0159
0.0020
0.0029
0.0029
0.0030
0.0036
0.0085
0.0069
0.0034
0.0007
0.0004
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
53.6381
104.1493
0.0000
2.1339
55.9345
10.8033
15.4806
15.3178
15.7100
18.3804
42.5927
33.2725
15.7710
3.1810
1.8920
0.1547
0.0015
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0082
0.0160
0.0000
0.0003
0.0086
0.0017
0.0024
0.0024
0.0024
0.0028
0.0065
0.0051
0.0024
0.0005
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 0.9757
COMPONENTS
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 1071.3785 1.0000 51246.5901 1.0000 6513.0956 1.0000
Liquid Phase Phase Fraction 3.786e-004
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
MOLAR FLOW (lbmole/hr)
0.0002
0.0020
0.0104
0.0057
0.0249
0.0172
0.0285
0.0000
0.0000
0.0000
0.0000
0.0000
0.1243
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0005
0.0049
0.0251
0.0136
0.0599
0.0414
0.0685
0.0000
0.0000
0.0000
0.0000
0.0000
0.2989
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0032
0.0610
0.4607
0.3298
1.4472
1.2411
2.0546
0.0000
0.0000
0.0000
0.0000
0.0000
10.7083
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0001
0.0013
0.0101
0.0072
0.0318
0.0273
0.0451
0.0000
0.0000
0.0000
0.0000
0.0000
0.2352
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0007
0.0117
0.0623
0.0402
0.1699
0.1363
0.2234
0.0000
0.0000
0.0000
0.0000
0.0000
1.1065
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0002
0.0027
0.0143
0.0092
0.0391
0.0313
0.0514
0.0000
0.0000
0.0000
0.0000
0.0000
0.2544
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 3.786e-004
COMPONENTS
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0005
0.0000
0.0000
0.0003
0.0008
0.0016
0.0022
0.0030
0.0049
0.0162
0.0267
0.0427
0.0297
0.0516
0.0202
0.0021
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0013
0.0000
0.0000
0.0006
0.0019
0.0039
0.0053
0.0071
0.0118
0.0391
0.0642
0.1026
0.0714
0.1241
0.0486
0.0051
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0036
0.0184
0.0000
0.0000
0.0049
0.0592
0.1308
0.1884
0.2839
0.4944
1.7199
3.0899
5.6527
4.4878
8.6703
3.9220
0.4980
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0013
0.0029
0.0041
0.0062
0.0109
0.0378
0.0679
0.1242
0.0986
0.1904
0.0861
0.0109
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0016
0.0000
0.0000
0.0003
0.0063
0.0138
0.0196
0.0290
0.0494
0.1681
0.2896
0.5088
0.3942
0.7468
0.3308
0.0406
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0015
0.0032
0.0045
0.0067
0.0114
0.0386
0.0666
0.1170
0.0906
0.1717
0.0760
0.0093
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 3.786e-004
COMPONENTS
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 0.4157 1.0000 45.5298 1.0000 4.3502 1.0000
Aqueous Phase Phase Fraction 2.391e-002
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 2.391e-002
COMPONENTS
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0012
0.0000
0.0000
26.2514
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0072
0.0421
0.0000
0.0000
472.9213
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0037
0.0000
0.0000
32.4476
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1404 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 2.391e-002
COMPONENTS
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 26.2528 1.0000 472.9706 1.0000 32.4519 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 80 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
0.0000
32.42
11.54
2.580
418.1
3429
-1.261e+005
64.43
-3.572e+007
3396 *
Liquid Phase
0.9995
32.42
11.54
2.579
418.1
3428
-1.261e+005
64.45
-3.570e+007
3396
Aqueous Phase
0.0005
32.42
11.54
1.210e-003
2.607e-002
0.1643
-1.228e+005
13.28
-1.632e+004
0.1616
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
Overall
135.6
0.3508
761.8
3452
-2.163
0.4752
64.23
0.4738
---
---
---
2.122e-314
-1.033
0.0000
---
0.3532
64.23
2.575
47.89
100.7
---
11.94
---
-1.033
1.032
1.144
2.931e+004
1.125
48.35
3396
1.000
2.850
216.2
0.0000
---
7.359e-002
0.8572
62.25
Liquid Phase
135.6
0.3507
761.8
3452
-2.162
0.4752
64.25
0.4738
---
---
1.000
0.9999
---
0.0000
---
0.3531
64.25
2.574
47.89
100.7
8.641e-002
11.94
---
---
1.032
1.144
---
1.125
48.35
3396
1.000
2.852
---
0.9995
21.47
7.358e-002
0.8571
62.27
Aqueous Phase
18.02
3.472
1002
0.1636
-15.85
0.7372
18.56
1.030
11.84
0.6573
4.792e-005
6.234e-005
---
0.0000
---
3.458
18.56
1.208e-003
62.30
4.772e-003
8.726e-003
9.076
---
---
1.120
1.151
---
0.7560
63.35
0.1616
1.000
0.2880
---
0.0005
70.81
0.3591
0.7576
16.57
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.4591
56.14
0.4141
---
---
---
-0.4525
2.982e-002
3396
Liquid Phase
0.4591
56.15
0.4140
---
---
---
-0.4525
1.204e-002
3396
Aqueous Phase
0.9197
16.12
0.8945
---
---
---
38.15
-0.4359
0.1616
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
MOLAR FLOW (lbmole/hr)
0.2595
1.4589
4.6656
1.9595
8.0932
3.6702
5.4617
0.0000
0.0000
0.0000
0.0000
0.0000
19.6955
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0009
0.0051
0.0165
0.0069
0.0286
0.0130
0.0193
0.0000
0.0000
0.0000
0.0000
0.0000
0.0695
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
4.1636
43.8676
205.7369
113.8936
470.4120
264.8103
394.0674
0.0000
0.0000
0.0000
0.0000
0.0000
1697.3176
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0001
0.0011
0.0054
0.0030
0.0122
0.0069
0.0103
0.0000
0.0000
0.0000
0.0000
0.0000
0.0442
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.9522
8.4450
27.8034
13.8774
55.2283
29.0842
42.8484
0.0000
0.0000
0.0000
0.0000
0.0000
175.3832
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0003
0.0025
0.0081
0.0040
0.0161
0.0085
0.0125
0.0000
0.0000
0.0000
0.0000
0.0000
0.0512
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0887
0.4207
0.0000
0.0006
0.3173
2.7743
4.0640
4.1176
4.0261
4.9106
12.1332
11.9088
10.6336
5.6419
10.0536
7.1299
3.9754
1.3399
0.1317
0.0068
0.0006
0.0000
6.2474
9.3521
8.0329
8.2006
7.5399
4.4927
4.4389
9.1302
4.8814
7.3784
4.0099
2.4692
4.0094
3.3090
2.3182
14.6426
1.1276
1.8609
1.2092
0.9797
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0015
0.0000
0.0000
0.0011
0.0098
0.0143
0.0145
0.0142
0.0173
0.0428
0.0420
0.0375
0.0199
0.0355
0.0252
0.0140
0.0047
0.0005
0.0000
0.0000
0.0000
0.0221
0.0330
0.0284
0.0289
0.0266
0.0159
0.0157
0.0322
0.0172
0.0260
0.0142
0.0087
0.0142
0.0117
0.0082
0.0517
0.0040
0.0066
0.0043
0.0035
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
3.9028
14.3372
0.0000
0.0159
5.7167
212.8198
329.0661
348.9252
386.0611
495.6792
1284.9075
1379.5177
1409.1598
853.6758
1689.7072
1384.2770
935.8015
379.8491
44.1643
2.6692
0.2581
0.0000
618.4897
1028.7280
1004.1125
1131.6869
1161.1462
741.2994
799.0004
1789.5246
1015.3414
1638.0079
938.3245
604.9537
384.8992
357.3700
278.1822
2108.5411
202.9758
187.9504
145.1090
131.2860
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0055
0.0086
0.0091
0.0101
0.0129
0.0335
0.0359
0.0367
0.0222
0.0440
0.0360
0.0244
0.0099
0.0011
0.0001
0.0000
0.0000
0.0161
0.0268
0.0261
0.0295
0.0302
0.0193
0.0208
0.0466
0.0264
0.0426
0.0244
0.0157
0.0100
0.0093
0.0072
0.0549
0.0053
0.0049
0.0038
0.0034
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3238
1.2452
0.0000
0.0013
0.3922
22.7597
34.7139
36.2180
39.4183
49.5316
125.5978
129.3062
126.8343
74.9780
145.5444
116.7566
76.3039
30.2737
3.4194
0.2024
0.0193
0.0000
59.2586
94.9760
90.0281
99.5476
100.5081
62.5865
66.9553
146.2322
81.3461
130.2811
73.6302
46.7971
36.3184
32.9706
24.7016
184.2446
15.7570
17.9917
13.4256
11.8366
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0066
0.0101
0.0106
0.0115
0.0144
0.0366
0.0377
0.0370
0.0219
0.0425
0.0341
0.0223
0.0088
0.0010
0.0001
0.0000
0.0000
0.0173
0.0277
0.0263
0.0290
0.0293
0.0183
0.0195
0.0427
0.0237
0.0380
0.0215
0.0136
0.0106
0.0096
0.0072
0.0537
0.0046
0.0052
0.0039
0.0035
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
4.0281
0.7021
0.7556
1.1257
1.1806
1.4759
4.6333
4.7778
4.6772
3.0829
7.4388
6.2842
5.9541
2.3836
0.2465
0.0102
0.0011
MOLE FRACTION
0.0142
0.0025
0.0027
0.0040
0.0042
0.0052
0.0164
0.0169
0.0165
0.0109
0.0263
0.0222
0.0210
0.0084
0.0009
0.0000
0.0000
MASS FLOW (lb/hr)
604.2100
53.8570
61.1837
95.3884
113.0213
148.7069
488.9473
542.1792
613.4576
463.2653
1247.2573
1210.5261
1394.0397
667.0600
80.9711
3.8993
0.4988
MASS FRACTION
0.0157
0.0014
0.0016
0.0025
0.0029
0.0039
0.0127
0.0141
0.0160
0.0121
0.0325
0.0315
0.0363
0.0174
0.0021
0.0001
0.0000
LIQUID VOLUMEFLOW (barrel/day)
52.8492
5.7987
6.4100
9.9104
11.5126
14.8239
47.5576
49.3245
54.3545
40.2399
107.0109
100.7550
112.6552
52.0993
6.0929
0.2859
0.0358
LIQUID VOLUMEFRACTION
0.0154
0.0017
0.0019
0.0029
0.0034
0.0043
0.0139
0.0144
0.0159
0.0117
0.0312
0.0294
0.0329
0.0152
0.0018
0.0001
0.0000
Total 283.3275 1.0000 38410.1780 1.0000 3428.5714 1.0000
Liquid Phase Phase Fraction 0.9995
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
MOLAR FLOW (lbmole/hr)
0.2595
1.4589
4.6656
1.9595
8.0932
3.6702
5.4617
0.0000
0.0000
0.0000
0.0000
0.0000
19.6955
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0009
0.0052
0.0165
0.0069
0.0286
0.0130
0.0193
0.0000
0.0000
0.0000
0.0000
0.0000
0.0695
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
4.1636
43.8676
205.7369
113.8936
470.4120
264.8103
394.0674
0.0000
0.0000
0.0000
0.0000
0.0000
1697.3176
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0001
0.0011
0.0054
0.0030
0.0122
0.0069
0.0103
0.0000
0.0000
0.0000
0.0000
0.0000
0.0442
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.9522
8.4450
27.8034
13.8774
55.2283
29.0842
42.8484
0.0000
0.0000
0.0000
0.0000
0.0000
175.3832
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0003
0.0025
0.0081
0.0040
0.0161
0.0085
0.0125
0.0000
0.0000
0.0000
0.0000
0.0000
0.0512
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 84 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.9995
COMPONENTS
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0887
0.4207
0.0000
0.0006
0.1844
2.7743
4.0640
4.1176
4.0261
4.9106
12.1332
11.9088
10.6336
5.6419
10.0536
7.1299
3.9754
1.3399
0.1317
0.0068
0.0006
0.0000
6.2474
9.3521
8.0329
8.2006
7.5399
4.4927
4.4389
9.1302
4.8814
7.3784
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0015
0.0000
0.0000
0.0007
0.0098
0.0144
0.0145
0.0142
0.0173
0.0428
0.0421
0.0375
0.0199
0.0355
0.0252
0.0140
0.0047
0.0005
0.0000
0.0000
0.0000
0.0221
0.0330
0.0284
0.0290
0.0266
0.0159
0.0157
0.0322
0.0172
0.0261
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
3.9028
14.3369
0.0000
0.0159
3.3225
212.8198
329.0661
348.9252
386.0611
495.6792
1284.9075
1379.5177
1409.1598
853.6758
1689.7072
1384.2770
935.8015
379.8491
44.1643
2.6692
0.2581
0.0000
618.4897
1028.7280
1004.1125
1131.6869
1161.1462
741.2994
799.0004
1789.5246
1015.3414
1638.0079
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0055
0.0086
0.0091
0.0101
0.0129
0.0335
0.0359
0.0367
0.0222
0.0440
0.0360
0.0244
0.0099
0.0011
0.0001
0.0000
0.0000
0.0161
0.0268
0.0261
0.0295
0.0302
0.0193
0.0208
0.0466
0.0264
0.0426
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3238
1.2452
0.0000
0.0013
0.2280
22.7597
34.7139
36.2180
39.4183
49.5316
125.5978
129.3062
126.8343
74.9780
145.5444
116.7566
76.3039
30.2737
3.4194
0.2024
0.0193
0.0000
59.2586
94.9760
90.0281
99.5476
100.5081
62.5865
66.9553
146.2322
81.3461
130.2811
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0004
0.0000
0.0000
0.0001
0.0066
0.0101
0.0106
0.0115
0.0144
0.0366
0.0377
0.0370
0.0219
0.0425
0.0341
0.0223
0.0088
0.0010
0.0001
0.0000
0.0000
0.0173
0.0277
0.0263
0.0290
0.0293
0.0183
0.0195
0.0427
0.0237
0.0380
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Liquid Phase (continued) Phase Fraction 0.9995
COMPONENTS
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
4.0099
2.4692
4.0094
3.3090
2.3182
14.6426
1.1276
1.8609
1.2092
0.9797
4.0281
0.7021
0.7556
1.1257
1.1806
1.4759
4.6333
4.7778
4.6772
3.0829
7.4388
6.2842
5.9541
2.3836
0.2465
0.0102
0.0011
MOLE FRACTION
0.0142
0.0087
0.0142
0.0117
0.0082
0.0517
0.0040
0.0066
0.0043
0.0035
0.0142
0.0025
0.0027
0.0040
0.0042
0.0052
0.0164
0.0169
0.0165
0.0109
0.0263
0.0222
0.0210
0.0084
0.0009
0.0000
0.0000
MASS FLOW (lb/hr)
938.3245
604.9537
384.8992
357.3700
278.1822
2108.5411
202.9758
187.9504
145.1090
131.2860
604.2100
53.8570
61.1837
95.3884
113.0213
148.7069
488.9473
542.1792
613.4576
463.2653
1247.2573
1210.5261
1394.0397
667.0600
80.9711
3.8993
0.4988
MASS FRACTION
0.0244
0.0158
0.0100
0.0093
0.0072
0.0549
0.0053
0.0049
0.0038
0.0034
0.0157
0.0014
0.0016
0.0025
0.0029
0.0039
0.0127
0.0141
0.0160
0.0121
0.0325
0.0315
0.0363
0.0174
0.0021
0.0001
0.0000
LIQUID VOLUMEFLOW (barrel/day)
73.6302
46.7971
36.3184
32.9706
24.7016
184.2446
15.7570
17.9917
13.4256
11.8366
52.8492
5.7987
6.4100
9.9104
11.5126
14.8239
47.5576
49.3245
54.3545
40.2399
107.0109
100.7550
112.6552
52.0993
6.0929
0.2859
0.0358
LIQUID VOLUMEFRACTION
0.0215
0.0136
0.0106
0.0096
0.0072
0.0537
0.0046
0.0052
0.0039
0.0035
0.0154
0.0017
0.0019
0.0029
0.0034
0.0043
0.0139
0.0144
0.0159
0.0117
0.0312
0.0294
0.0329
0.0152
0.0018
0.0001
0.0000
Total 283.1946 1.0000 38407.7834 1.0000 3428.4071 1.0000
Aqueous Phase Phase Fraction 4.691e-004
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 4.691e-004
COMPONENTS
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1329
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0002
0.0000
0.0000
2.3942
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9999
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.1643
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.9998
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1501 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Aqueous Phase (continued) Phase Fraction 4.691e-004
COMPONENTS
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 0.1329 1.0000 2.3945 1.0000 0.1643 1.0000
Material Stream: 1604Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Overall
1.0000
54.50
8.000 *
0.9485
Vapour Phase
1.0000
54.50
8.000
0.9485
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1604 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
28.80
475.7
-3.544e+004
42.02
-3.691e+006
---
Vapour Phase
28.80
475.7
-3.544e+004
42.02
-3.691e+006
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
Overall
25.40
2.106e-002
8.570
2.114e+004
-3.245
1.654
12.56
0.4945
5.150e+005
2.028e+004
---
4.941e-324
-1.026
0.0000
82.42
0.9359
12.56
0.9467
23.77
---
0.9639
17.11
---
-1.033
1.188
1.226
7790
1.384
---
---
0.0000
47.48
306.7
1.0000
---
1.819e-002
1.186e-002
10.57
0.4163
10.25
0.4035
8.586
Vapour Phase
25.40
2.106e-002
8.570
2.114e+004
-3.245
1.654
12.56
0.4945
5.150e+005
2.028e+004
1.000
1.000
---
0.0000
82.42
0.9359
12.56
0.9467
23.77
---
0.9639
17.11
---
---
1.188
1.226
---
1.384
---
---
0.0000
47.48
---
1.0000
---
1.819e-002
1.186e-002
10.57
0.4163
10.25
0.4035
8.586
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1604 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
0.3380
1.463
---
---
0.0000
Vapour Phase
0.3380
1.463
---
---
0.0000
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
MOLAR FLOW (lbmole/hr)
64.2682
20.1105
10.9665
1.2810
3.2181
0.8540
1.0415
0.0104
0.0000
0.0000
0.0000
0.0000
0.6353
0.0000
0.0625
0.0208
0.0000
0.0521
0.0000
0.0000
0.0000
0.0000
0.0000
0.1146
0.0000
0.0000
0.0000
0.0208
0.0104
0.0000
0.0000
0.0000
0.0000
0.0312
0.0000
0.0000
0.0000
0.0000
0.0000
0.0104
MOLE FRACTION
0.6171
0.1931
0.1053
0.0123
0.0309
0.0082
0.0100
0.0001
0.0000
0.0000
0.0000
0.0000
0.0061
0.0000
0.0006
0.0002
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0011
0.0000
0.0000
0.0000
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
MASS FLOW (lb/hr)
1031.0486
604.7209
483.5909
74.4563
187.0487
61.6165
75.1421
0.7514
0.0000
0.0000
0.0000
0.0000
54.7478
0.0000
5.2591
1.6270
0.0000
4.3824
0.0000
0.0000
0.0000
0.0000
0.0000
11.4795
0.0000
0.0000
0.0000
2.0452
0.9596
0.0000
0.0000
0.0000
0.0000
3.5690
0.0000
0.0000
0.0000
0.0000
0.0000
1.4818
MASS FRACTION
0.3897
0.2286
0.1828
0.0281
0.0707
0.0233
0.0284
0.0003
0.0000
0.0000
0.0000
0.0000
0.0207
0.0000
0.0020
0.0006
0.0000
0.0017
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
0.0000
0.0008
0.0004
0.0000
0.0000
0.0000
0.0000
0.0013
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
LIQUID VOLUMEFLOW (barrel/day)
235.8057
116.4153
65.3528
9.0721
21.9603
6.7674
8.1705
0.0864
0.0000
0.0000
0.0000
0.0000
5.6571
0.0000
0.4788
0.1263
0.0000
0.3838
0.0000
0.0000
0.0000
0.0000
0.0000
1.1445
0.0000
0.0000
0.0000
0.1813
0.0755
0.0000
0.0000
0.0000
0.0000
0.3465
0.0000
0.0000
0.0000
0.0000
0.0000
0.1385
LIQUID VOLUMEFRACTION
0.4957
0.2447
0.1374
0.0191
0.0462
0.0142
0.0172
0.0002
0.0000
0.0000
0.0000
0.0000
0.0119
0.0000
0.0010
0.0003
0.0000
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
0.0024
0.0000
0.0000
0.0000
0.0004
0.0002
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
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* Specified by user.Licensed to: LEGENDS
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Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1604 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0833
0.0000
0.0000
1.3539
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0008
0.0000
0.0000
0.0130
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
3.6667
0.0000
0.0000
37.9266
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0014
0.0000
0.0000
0.0143
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.3042
0.0000
0.0000
3.2205
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0006
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1604 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 104.1455 1.0000 2645.5200 1.0000 475.6874 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
MOLAR FLOW (lbmole/hr)
64.2682
20.1105
10.9665
1.2810
3.2181
0.8540
1.0415
0.0104
0.0000
0.0000
0.0000
0.0000
0.6353
0.0000
0.0625
0.0208
0.0000
0.0521
0.0000
0.0000
0.0000
0.0000
0.0000
0.1146
0.0000
0.0000
0.0000
0.0208
0.0104
0.0000
MOLE FRACTION
0.6171
0.1931
0.1053
0.0123
0.0309
0.0082
0.0100
0.0001
0.0000
0.0000
0.0000
0.0000
0.0061
0.0000
0.0006
0.0002
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0011
0.0000
0.0000
0.0000
0.0002
0.0001
0.0000
MASS FLOW (lb/hr)
1031.0486
604.7209
483.5909
74.4563
187.0487
61.6165
75.1421
0.7514
0.0000
0.0000
0.0000
0.0000
54.7478
0.0000
5.2591
1.6270
0.0000
4.3824
0.0000
0.0000
0.0000
0.0000
0.0000
11.4795
0.0000
0.0000
0.0000
2.0452
0.9596
0.0000
MASS FRACTION
0.3897
0.2286
0.1828
0.0281
0.0707
0.0233
0.0284
0.0003
0.0000
0.0000
0.0000
0.0000
0.0207
0.0000
0.0020
0.0006
0.0000
0.0017
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
0.0000
0.0008
0.0004
0.0000
LIQUID VOLUMEFLOW (barrel/day)
235.8057
116.4153
65.3528
9.0721
21.9603
6.7674
8.1705
0.0864
0.0000
0.0000
0.0000
0.0000
5.6571
0.0000
0.4788
0.1263
0.0000
0.3838
0.0000
0.0000
0.0000
0.0000
0.0000
1.1445
0.0000
0.0000
0.0000
0.1813
0.0755
0.0000
LIQUID VOLUMEFRACTION
0.4957
0.2447
0.1374
0.0191
0.0462
0.0142
0.0172
0.0002
0.0000
0.0000
0.0000
0.0000
0.0119
0.0000
0.0010
0.0003
0.0000
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
0.0024
0.0000
0.0000
0.0000
0.0004
0.0002
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 92 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1604 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0312
0.0000
0.0000
0.0000
0.0000
0.0000
0.0104
0.0000
0.0000
0.0833
0.0000
0.0000
1.3539
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0008
0.0000
0.0000
0.0130
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
3.5690
0.0000
0.0000
0.0000
0.0000
0.0000
1.4818
0.0000
0.0000
3.6667
0.0000
0.0000
37.9266
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0013
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
0.0000
0.0014
0.0000
0.0000
0.0143
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.3465
0.0000
0.0000
0.0000
0.0000
0.0000
0.1385
0.0000
0.0000
0.3042
0.0000
0.0000
3.2205
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0006
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1604 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 104.1455 1.0000 2645.5200 1.0000 475.6874 1.0000
Material Stream: 1612Fluid Package: Basis-1
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (kg/cm2_g)
Molar Flow (MMSCFD)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (barrel/day)
Molar Enthalpy (Btu/lbmole)
Molar Entropy (Btu/lbmole-F)
Heat Flow (Btu/hr)
Liq Vol Flow @Std Cond (barrel/day)
Overall
1.0000
50.37
1.800 *
0.9485
28.80
475.7
-3.544e+004
44.27
-3.691e+006
---
Vapour Phase
1.0000
50.37
1.800
0.9485
28.80
475.7
-3.544e+004
44.27
-3.691e+006
---
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
(lbmole/ft3)
(kg/m3)
(barrel/day)
(kJ/g)
Overall
25.40
6.525e-003
2.655
6.823e+004
-3.245
Vapour Phase
25.40
6.525e-003
2.655
6.823e+004
-3.245
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 94 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1612 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
PROPERTIES
Mass Entropy
Heat Capacity
Mass Heat Capacity
Lower Heating Value
Mass Lower Heating Value
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole)
(Btu/lb)
(kg/cm2_g)
(Cost/s)
(ACFM)
(lbmole/ft3)
(Btu/lbmole-F)
(MMSCFD)
(lb/ft3)
(USGPM)
(kg/cm2_g)
(Btu/lbmole)
(cSt)
(lb/ft3)
(barrel/day)
(ft3/lbmole)
(Btu/lb)
(dyne/cm)
(Btu/hr-ft-F)
(cP)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/lbmole-F)
(Btu/lb-F)
(kg/cm2_g)
(kg/cm2_g)
(barrel/day)
Overall
1.743
12.22
0.4809
5.150e+005
2.028e+004
---
4.941e-324
-1.031
0.0000
266.0
0.9359
12.22
0.9467
23.77
---
0.9882
17.11
---
-1.033
1.194
1.206
8163
4.351
---
---
0.0000
153.3
321.4
1.0000
---
1.759e-002
1.155e-002
10.23
0.4027
10.13
0.3988
10.13
0.3986
1.206
---
---
0.0000
Vapour Phase
1.743
12.22
0.4809
5.150e+005
2.028e+004
1.000
1.000
---
0.0000
266.0
0.9359
12.22
0.9467
23.77
---
0.9882
17.11
---
---
1.194
1.206
---
4.351
---
---
0.0000
153.3
---
1.0000
---
1.759e-002
1.155e-002
10.23
0.4027
10.13
0.3988
10.13
0.3986
1.206
---
---
0.0000
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methane
Ethane
Propane
MOLAR FLOW (lbmole/hr)
64.2682
20.1105
10.9665
MOLE FRACTION
0.6171
0.1931
0.1053
MASS FLOW (lb/hr)
1031.0486
604.7209
483.5909
MASS FRACTION
0.3897
0.2286
0.1828
LIQUID VOLUMEFLOW (barrel/day)
235.8057
116.4153
65.3528
LIQUID VOLUMEFRACTION
0.4957
0.2447
0.1374
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 95 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1612 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
MOLAR FLOW (lbmole/hr)
1.2810
3.2181
0.8540
1.0415
0.0104
0.0000
0.0000
0.0000
0.0000
0.6353
0.0000
0.0625
0.0208
0.0000
0.0521
0.0000
0.0000
0.0000
0.0000
0.0000
0.1146
0.0000
0.0000
0.0000
0.0208
0.0104
0.0000
0.0000
0.0000
0.0000
0.0312
0.0000
0.0000
0.0000
0.0000
0.0000
0.0104
0.0000
0.0000
0.0833
0.0000
0.0000
1.3539
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0123
0.0309
0.0082
0.0100
0.0001
0.0000
0.0000
0.0000
0.0000
0.0061
0.0000
0.0006
0.0002
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0011
0.0000
0.0000
0.0000
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
0.0000
0.0008
0.0000
0.0000
0.0130
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
74.4563
187.0487
61.6165
75.1421
0.7514
0.0000
0.0000
0.0000
0.0000
54.7478
0.0000
5.2591
1.6270
0.0000
4.3824
0.0000
0.0000
0.0000
0.0000
0.0000
11.4795
0.0000
0.0000
0.0000
2.0452
0.9596
0.0000
0.0000
0.0000
0.0000
3.5690
0.0000
0.0000
0.0000
0.0000
0.0000
1.4818
0.0000
0.0000
3.6667
0.0000
0.0000
37.9266
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0281
0.0707
0.0233
0.0284
0.0003
0.0000
0.0000
0.0000
0.0000
0.0207
0.0000
0.0020
0.0006
0.0000
0.0017
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
0.0000
0.0008
0.0004
0.0000
0.0000
0.0000
0.0000
0.0013
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
0.0000
0.0014
0.0000
0.0000
0.0143
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
9.0721
21.9603
6.7674
8.1705
0.0864
0.0000
0.0000
0.0000
0.0000
5.6571
0.0000
0.4788
0.1263
0.0000
0.3838
0.0000
0.0000
0.0000
0.0000
0.0000
1.1445
0.0000
0.0000
0.0000
0.1813
0.0755
0.0000
0.0000
0.0000
0.0000
0.3465
0.0000
0.0000
0.0000
0.0000
0.0000
0.1385
0.0000
0.0000
0.3042
0.0000
0.0000
3.2205
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0191
0.0462
0.0142
0.0172
0.0002
0.0000
0.0000
0.0000
0.0000
0.0119
0.0000
0.0010
0.0003
0.0000
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
0.0024
0.0000
0.0000
0.0000
0.0004
0.0002
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0006
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 96 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1612 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 97 of 100
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1612 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Overall Phase (continued) Vapour Fraction 1.0000
COMPONENTS
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
Total 104.1455 1.0000 2645.5200 1.0000 475.6874 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
22-Mpropane
22-Mbutane
23-Mbutane
2-Mpentane
3-Mpentane
n-Hexane
22-Mpentane
Mcyclopentan
Benzene
33-Mpentane
Cyclohexane
2-Mhexane
23-Mpentane
3-Mhexane
1-tr3-MCC5
1-ci3-MCC5
n-Heptane
24-Mhexane
1tr2ci4-MCC5
1tr2ci3-MCC5
Mcyclohexane
Toluene
2-Mheptane
4-Mheptane
3-Ehexane
3-Mheptane
n-Octane
E-Benzene
o-Xylene
m-Xylene
p-Xylene
n-Nonane
n-Decane
n-C11
MOLAR FLOW (lbmole/hr)
64.2682
20.1105
10.9665
1.2810
3.2181
0.8540
1.0415
0.0104
0.0000
0.0000
0.0000
0.0000
0.6353
0.0000
0.0625
0.0208
0.0000
0.0521
0.0000
0.0000
0.0000
0.0000
0.0000
0.1146
0.0000
0.0000
0.0000
0.0208
0.0104
0.0000
0.0000
0.0000
0.0000
0.0312
0.0000
0.0000
0.0000
0.0000
0.0000
0.0104
0.0000
MOLE FRACTION
0.6171
0.1931
0.1053
0.0123
0.0309
0.0082
0.0100
0.0001
0.0000
0.0000
0.0000
0.0000
0.0061
0.0000
0.0006
0.0002
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0011
0.0000
0.0000
0.0000
0.0002
0.0001
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0001
0.0000
MASS FLOW (lb/hr)
1031.0486
604.7209
483.5909
74.4563
187.0487
61.6165
75.1421
0.7514
0.0000
0.0000
0.0000
0.0000
54.7478
0.0000
5.2591
1.6270
0.0000
4.3824
0.0000
0.0000
0.0000
0.0000
0.0000
11.4795
0.0000
0.0000
0.0000
2.0452
0.9596
0.0000
0.0000
0.0000
0.0000
3.5690
0.0000
0.0000
0.0000
0.0000
0.0000
1.4818
0.0000
MASS FRACTION
0.3897
0.2286
0.1828
0.0281
0.0707
0.0233
0.0284
0.0003
0.0000
0.0000
0.0000
0.0000
0.0207
0.0000
0.0020
0.0006
0.0000
0.0017
0.0000
0.0000
0.0000
0.0000
0.0000
0.0043
0.0000
0.0000
0.0000
0.0008
0.0004
0.0000
0.0000
0.0000
0.0000
0.0013
0.0000
0.0000
0.0000
0.0000
0.0000
0.0006
0.0000
LIQUID VOLUMEFLOW (barrel/day)
235.8057
116.4153
65.3528
9.0721
21.9603
6.7674
8.1705
0.0864
0.0000
0.0000
0.0000
0.0000
5.6571
0.0000
0.4788
0.1263
0.0000
0.3838
0.0000
0.0000
0.0000
0.0000
0.0000
1.1445
0.0000
0.0000
0.0000
0.1813
0.0755
0.0000
0.0000
0.0000
0.0000
0.3465
0.0000
0.0000
0.0000
0.0000
0.0000
0.1385
0.0000
LIQUID VOLUMEFRACTION
0.4957
0.2447
0.1374
0.0191
0.0462
0.0142
0.0172
0.0002
0.0000
0.0000
0.0000
0.0000
0.0119
0.0000
0.0010
0.0003
0.0000
0.0008
0.0000
0.0000
0.0000
0.0000
0.0000
0.0024
0.0000
0.0000
0.0000
0.0004
0.0002
0.0000
0.0000
0.0000
0.0000
0.0007
0.0000
0.0000
0.0000
0.0000
0.0000
0.0003
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1612 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
n-C12
CO2
H2S
Oxygen
Nitrogen
H2O
LM-01 (NBP-43.03)*
LM-02 (NBP-55)*
LM-03 (NBP-65)*
LM-04 (NBP-75)*
LM-05 (NBP-85)*
LM-06 (NBP-95)*
LM-07 (NBP-115)*
LM-08 (NBP-145)*
LM-09 (NBP-175)*
LM-10 (NBP-200)*
LM-11 (NBP-235)*
LM-12 (NBP-285)*
LM-13 (NBP-335)*
LM-14 (NBP-385)*
LM-15 (NBP-435)*
LM-16 (NBP-485)*
LM-17 (NBP-546)*
MAYA-01 (NBP-99.33)*
MAYA-02 (NBP-122.79)*
MAYA-03 (NBP-151.49)*
MAYA-04 (NBP-174.66)*
MAYA-05 (NBP-195.2)*
MAYA-06 (NBP-203.37)*
MAYA-07 (NBP-220.36)*
MAYA-08 (NBP-241.54)*
MAYA-09 (NBP-258.15)*
MAYA-10 (NBP-274.6)*
MAYA-11 (NBP-289.37)*
MAYA-12 (NBP-302.96)*
LIT-01 (NBP-95.4)*
LIT-02 (NBP-119.5)*
LIT-03 (NBP-144.5)*
LIT-04 (NBP-182.8)*
LIT-05 (NBP-230.3)*
LIT-06 (NBP-103.2)*
LIT-07 (NBP-139.7)*
LIT-08 (NBP-165.3)*
LIT-09 (NBP-191.9)*
PC-01 (NBP-43.03)*
PC-02 (NBP-55)*
PC-03 (NBP-65)*
PC-04 (NBP-75)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0833
0.0000
0.0000
1.3539
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0008
0.0000
0.0000
0.0130
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
3.6667
0.0000
0.0000
37.9266
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0014
0.0000
0.0000
0.0143
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.3042
0.0000
0.0000
3.2205
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0006
0.0000
0.0000
0.0068
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
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* Specified by user.Licensed to: LEGENDS
EvyaParaíso, Tabasco
Case Name: C:\USERS\UNACAR\DOCUMENTS\DC\REV. A\PARA DAR CALIDAD\CB-500-REV-B.HSC
Unit Set: DCRI
Date/Time: Tue Jul 19 18:17:19 2011
Material Stream: 1612 (continued)Fluid Package: Basis-1
Property Package: Peng-Robinson
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
PC-05 (NBP-85)*
PC-06 (NBP-95)*
PC-07 (NBP-115)*
PC-08 (NBP-145)*
PC-09 (NBP-175)*
PC-10 (NBP-200)*
PC-11 (NBP-235)*
PC-12 (NBP-285)*
PC-13 (NBP-335)*
PC-14 (NBP-385)*
PC-15 (NBP-435)*
PC-16 (NBP-485)*
MOLAR FLOW (lbmole/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FLOW (lb/hr)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFLOW (barrel/day)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUMEFRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Total 104.1455 1.0000 2645.5200 1.0000 475.6874 1.0000
Hyprotech Ltd. Aspen HYSYS Version 2006 (20.0.0.6728) Page 100 of 100
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* Specified by user.Licensed to: LEGENDS