3004 heat ex stream conditions

COLD IN HOT INStream Name Rich to L/R Regen Bttms

124.20 Temperature [C] 59.48 124.8690.90 Pressure [kPa] 620.53 217.1843650.00 Molar Flow [kgmole/h] 1954.27 1853.75

Mass Flow [kg/h] 47228.84 43695.43Rich Amine Std Ideal Liq Vol Flow [m3/h] 47.13 42.65

60.00 Molar Enthalpy [kJ/kgmole] -297666.14 -289915.5493.30 Heat Flow [kJ/h] -581720995.31 ###47070.00 Fraction vapour 0.00 0.000002

Heat Capacity [kJ/kgmole-C] 82.39 98.14Equipment Mass Heat Capacity [kJ/kg-C 3.41 4.16F Heat of Vap. [kJ/kgmole] 53265.453918 46212.32948UA1 W/mK 0.5778 Btu/hr.ft.F

U (Btu/h.ft2.F0 U (W/m.K75 13080 13885 14790 156

Lean AmineTl, I (oC)

Tl, o (oC)

Fl (kg/hr)

Cp, l

Tr,I (oC)

Tr, o (oC)

Fr (kg/hr)

Cp, r

HOT OUT COLD OUTLean from L/R Regen Feed COUNTER Data COCURRENT

92.20 93.33 qh (kJ/hr -5942185.19 -5830014.11

148.24 551.58 qh (kJ/s -1650.607 -1619.44836

1853.75 1954.27 qc (kJ/h 5450745.85 5830011.42

43695.43 47228.84 qc (kJ/s 1514.09607 1619.4476242.65 47.13 dT 1 30.90 -65.39

-293060.52 -294682.92 dT 2 30.90 1.13

-543262052.66 ### dT LM #DIV/0!

0.00 0.002244

94.44 87.93 Q (J/s -16506074.01 3.64

46876.16802 53630.27168

A (m2803.2753.0708.7669.3

65.3850427

1.13

15.8331147

Rich to L/R (COLD IN)

Stream Name Rich to L/R Vapour Phase Aqueous PhaseVapour / Phase Fraction 0 0 1Temperature [C] 59.4795075817648 59.4795075818 59.47950758176Pressure [kPa] 620.528317809783 620.52831781 620.5283178098Molar Flow [kgmole/h] 1954.27334159473 0 1954.273341595Mass Flow [kg/h] 47228.8390520017 0 47228.839052Std Ideal Liq Vol Flow [m3/h] 47.1254678287494 0 47.12546782875Molar Enthalpy [kJ/kgmole] -297666.13652576 -117048.53272 -297666.1365258Molar Entropy [kJ/kgmole-C] -188.256160384732 -74.008645737 -188.2561603847Heat Flow [kJ/h] -581720995.307791 0 -581720995.3078Liq Vol Flow @Std Cond [m3/h] 44.1268652257702 0 44.12686522577Fluid Package Converted Basis-1 Utility Type

Stream Name Rich to L/R Vapour Phase Aqueous PhaseMolecular Weight 24.1669566108198 22.304768685 24.16695661082Molar Density [kgmole/m3] 43.7124001367255 0.22785087262 43.71240013673Mass Density [kg/m3] 1056.39567745904 5.08216100836 1056.395677459Act. Volume Flow [m3/h] 44.7075277377146 0 44.70752773771Mass Enthalpy [kJ/kg] -12317.0716660488 -5247.6909477 -12317.07166605Mass Entropy [kJ/kg-C] -7.78981662508748 -3.3180638088 -7.789816625087Heat Capacity [kJ/kgmole-C] 82.3877932657263 40.1368473784 82.38779326573Mass Heat Capacity [kJ/kg-C] 3.40910916473614 1.79947382308 3.409109164736LHV Molar Basis (Std) [kJ/kgmole] 152347.177131352 723590.056493 152347.1771314HHV Molar Basis (Std) [kJ/kgmole] 203447.855206357 795668.841527 203447.8552064HHV Mass Basis (Std) [kJ/kg] 8418.43093785634 35672.5887977 8418.430937856CO2 Loading 0.45170036197941 <empty> 0.451700361979CO2 Apparent Mole Conc. [kgmole/m3] 1.18726867490958 <empty> 1.18726867491CO2 Apparent Wt. Conc. [kgmol/kg] 1.12E-03 <empty> 1.12E-03LHV Mass Basis (Std) [kJ/kg] 6303.94548989859 32441.0473255 6303.945489899Phase Fraction [Vol. Basis] <empty> <empty> 1Phase Fraction [Mass Basis] 0 0 1Phase Fraction [Act. Vol. Basis] 0 0 1Partial Pressure of CO2 [kPa] 0 <empty> <empty>Cost Based on Flow [Cost/s] 0 0 0Act. Gas Flow [ACT_m3/h] <empty> <empty> <empty>Avg. Liq. Density [kgmole/m3] 41.4695796484487 18.2905715386 41.46957964845Specific Heat [kJ/kgmole-C] 82.3877932657263 40.1368473784 82.38779326573Std. Gas Flow [STD_m3/h] 46207.6918002433 0 46207.69180024Std. Ideal Liq. Mass Density [kg/m3] 1002.193532033 407.966967285 1002.193532033Act. Liq. Flow [m3/s] 1.24E-02 <empty> 1.24E-02Z Factor <empty> 0.9847441301 5.13E-03Watson K 8.98584485244405 15.5020770495 8.985844852444User Property <empty> <empty> <empty>Partial Pressure of H2S [kPa] 0 <empty> <empty>Cp/(Cp - R) 1.11224423040315 1.26127151691 1.112244230403Cp/Cv 1.07336606479157 1.28532427701 1.073366064792Heat of Vap. [kJ/kgmole] 53265.4539180445 <empty> <empty>Kinematic Viscosity [cSt] 1.33454334846111 2.59897558118 1.334543348461Liq. Mass Density (Std. Cond) [kg/m3] 1070.2967185718 255.935942546 1070.296718572Liq. Vol. Flow (Std. Cond) [m3/h] 44.1268652257702 0 44.12686522577

Liquid Fraction 1 0 1Molar Volume [m3/kgmole] 2.29E-02 4.38883550684 2.29E-02Mass Heat of Vap. [kJ/kg] 2204.0613046906 <empty> <empty>Phase Fraction [Molar Basis] 0 0 1Surface Tension [dyne/cm] 38.0849600194402 <empty> 38.08496001944Thermal Conductivity [W/m-K] 0.49802367744216 3.27E-02 0.498023677442Viscosity [cP] 1.40980582469602 1.32E-02 1.409805824696Cv (Semi-Ideal) [kJ/kgmole-C] 74.0734732657263 31.8225273784 74.07347326573Mass Cv (Semi-Ideal) [kJ/kg-C] 3.06507246479529 1.42671407303 3.065072464795Cv [kJ/kgmole-C] 76.7564729016514 31.2270203686 76.75647290165Mass Cv [kJ/kg-C] 3.17609180740974 1.40001543211 3.17609180741Cv (Ent. Method) [kJ/kgmole-C] <empty> <empty> <empty>Mass Cv (Ent. Method) [kJ/kg-C] <empty> <empty> <empty>Cp/Cv (Ent. Method) <empty> <empty> <empty>Reid VP at 37.8 C [kPa] 1670.6958456258 18086.2733301 1670.695845626True VP at 37.8 C [kPa] 349.506303350271 <empty> 349.5063033503Liq. Vol. Flow - Sum(Std. Cond) [m3/h] 44.12686522577 0 44.12686522577Viscosity Index 6.95197980597474 <empty> <empty>Mass Exergy [kJ/kg] 6.96312151423272 <empty> <empty>

Inlet CompositionMol Frac Vapour Phase Aqueous Phase

Nitrogen 1.02E-07 6.32E-04 1.02E-07CO2 2.72E-02 0.12696787103 2.72E-02H2S 1.10E-02 6.36E-02 1.10E-02Methane 6.40E-05 0.72712827917 6.40E-05Ethane 3.09E-06 3.35E-02 3.09E-06Propane 4.52E-07 6.14E-03 4.52E-07i-Butane 2.46E-08 2.83E-04 2.46E-08n-Butane 8.31E-08 5.20E-04 8.31E-08i-Pentane 8.45E-06 1.47E-03 8.45E-06n-Pentane 9.35E-06 1.32E-03 9.35E-06n-Hexane 3.70E-05 1.75E-03 3.70E-05n-Heptane 3.21E-04 6.42E-03 3.21E-04H2O 0.90123568730343 3.02E-02 0.901235687303DEAmine 6.01E-02 2.93E-08 6.01E-02

Mixed Light HeavyNitrogen 6210.17579739056 <empty> 6210.175797391CO2 4.67465410331062 <empty> 4.674654103311H2S 5.76978409418703 <empty> 5.769784094187Methane 11358.7814389936 <empty> 11358.78143899Ethane 10839.3910840049 <empty> 10839.391084Propane 13585.6451612398 <empty> 13585.64516124i-Butane 11489.1681279315 <empty> 11489.16812793n-Butane 6259.2508029698 <empty> 6259.25080297i-Pentane 174.163423792197 <empty> 174.1634237922n-Pentane 141.104146254235 <empty> 141.1041462542n-Hexane 47.3625526783086 <empty> 47.36255267831n-Heptane 20.0152154576785 <empty> 20.01521545768H2O 3.35E-02 <empty> 3.35E-02DEAmine 4.88E-07 <empty> 4.88E-07

pH 8.0258964785806

Osmotic Pressure 13952.5888045324Ionic Strength 2.44E-03Heat Capacity 82.3877932657263Viscosity 1.40981168950039

H2S Loading 0.18342939073136H2S [Grains/US Gal] 910.235709379572H2S Composition [ppm] 11029.6781879963H2S Composition [Grains/100 SCF] 693.006162970924CO2 Loading 0.45170036197941CO2 Composition (Mole %) 2.71609124915582Acid Gas Loading 0.63512975271077Amine Strength [wt %] 26.1593555251192Recirculation Rate [m3/h] 47.1254678287494Temperature [C] 59.4795075817648Pressure [kPa] 620.528317809783Molar Flow Rate [MMSCFD] 39.2368565705746

Regen Bttms (HOT IN)

Stream Name Regen Bttms Vapour PhaseVapour / Phase Fraction 1.58E-06 1.58E-06Temperature [C] 124.864550263284 124.864550263Pressure [kPa] 217.184911233424 217.184911233Molar Flow [kgmole/h] 1853.75379413246 2.93E-03Mass Flow [kg/h] 43695.4257651884 5.34E-02Std Ideal Liq Vol Flow [m3/h] 42.653010471758 5.38E-05Molar Enthalpy [kJ/kgmole] -289915.543395584 -239449.88096Molar Entropy [kJ/kgmole-C] -173.533259316532 -40.281241744Heat Flow [kJ/h] -537432038.547539 -700.50864539Liq Vol Flow @Std Cond [m3/h] 42.2157567323394 5.36E-05Fluid Package Converted Basis-1 Utility Type

Stream Name Regen Bttms Vapour PhaseMolecular Weight 23.5713210154952 18.2432192499Molar Density [kgmole/m3] 41.1375205756306 6.67E-02Mass Density [kg/m3] 969.665703269725 1.21632353129Act. Volume Flow [m3/h] 45.0623607887201 4.39E-02Mass Enthalpy [kJ/kg] -12299.503417946 -13125.418145Mass Entropy [kJ/kg-C] -7.36205065479597 -2.2080117107Heat Capacity [kJ/kgmole-C] 98.144257950093 34.8285179257Mass Heat Capacity [kJ/kg-C] 4.16371479076525 1.90912127123LHV Molar Basis (Std) [kJ/kgmole] 152892.090959075 865.680282772HHV Molar Basis (Std) [kJ/kgmole] 205552.320388904 41572.2197054HHV Mass Basis (Std) [kJ/kg] 8720.44126223469 2278.77652162CO2 Loading 1.86E-02 <empty>CO2 Apparent Mole Conc. [kgmole/m3] 4.84E-02 <empty>CO2 Apparent Wt. Conc. [kgmol/kg] 4.99E-05 <empty>LHV Mass Basis (Std) [kJ/kg] 6486.36072872486 47.4521667976Phase Fraction [Vol. Basis] 1.26E-06 1.26E-06Phase Fraction [Mass Basis] 1.22E-06 1.22E-06Phase Fraction [Act. Vol. Basis] 9.74E-04 9.74E-04Partial Pressure of CO2 [kPa] 1.67312746339964 <empty>Cost Based on Flow [Cost/s] 0 0Act. Gas Flow [ACT_m3/h] 4.39E-02 4.39E-02Avg. Liq. Density [kgmole/m3] 43.4612650696695 54.4159857867Specific Heat [kJ/kgmole-C] 98.144257950093 34.8285179257Std. Gas Flow [STD_m3/h] 43830.9637498846 6.92E-02Std. Ideal Liq. Mass Density [kg/m3] 1024.43943069671 992.722759407Act. Liq. Flow [m3/s] 1.25E-02 <empty>Z Factor <empty> 0.98436538631Watson K 8.98450996029372 8.89982149798User Property <empty> <empty>Partial Pressure of H2S [kPa] 0.29467667060475 <empty>Cp/(Cp - R) 1.09255622557169 1.31357991757Cp/Cv 1.01579540667303 1.33674013734Heat of Vap. [kJ/kgmole] 46212.3294754637 <empty>Kinematic Viscosity [cSt] <empty> 11.2288146106Liq. Mass Density (Std. Cond) [kg/m3] 1035.05016011511 995.005201037Liq. Vol. Flow (Std. Cond) [m3/h] 42.2157567323394 5.36E-05

Liquid Fraction 0.9999984218553 0Molar Volume [m3/kgmole] 2.43E-02 14.9986568381Mass Heat of Vap. [kJ/kg] 1960.53201452243 <empty>Phase Fraction [Molar Basis] 1.58E-06 1.58E-06Surface Tension [dyne/cm] 49.2528171398218 <empty>Thermal Conductivity [W/m-K] 0.36784410807697 2.66E-02Viscosity [cP] 0.37972471658337 1.37E-02Cv (Semi-Ideal) [kJ/kgmole-C] 89.8299379500931 26.5141979257Mass Cv (Semi-Ideal) [kJ/kg-C] 3.81098445399141 1.45337276072Cv [kJ/kgmole-C] 96.6181352124229 26.0548157064Mass Cv [kJ/kg-C] 4.09896989434358 1.42819177632Cv (Ent. Method) [kJ/kgmole-C] <empty> <empty>Mass Cv (Ent. Method) [kJ/kg-C] <empty> <empty>Cp/Cv (Ent. Method) <empty> <empty>Reid VP at 37.8 C [kPa] 71.8028272308636 <empty>True VP at 37.8 C [kPa] 6.10289410994641 2164.12934928Liq. Vol. Flow - Sum(Std. Cond) [m3/h] 42.2157576311752 5.36E-05Viscosity Index -14.3612746633619 <empty>Mass Exergy [kJ/kg] 61.5922650755442 <empty>

Mol Frac Vapour PhaseNitrogen 1.25E-38 0CO2 1.18E-03 7.70E-03H2S 1.70E-04 1.36E-03Methane 1.07E-32 0Ethane 2.56E-33 0Propane 1.04E-35 0i-Butane 1.78E-47 0n-Butane 1.42E-40 0i-Pentane 4.25E-32 0n-Pentane 7.10E-31 0n-Hexane 6.83E-26 0n-Heptane 5.56E-25 0H2O 0.93526215287619 0.99087193718DEAmine 6.34E-02 6.76E-05

Mixed LightNitrogen <empty> <empty>CO2 6.5476574709392 <empty>H2S 7.96527330307301 <empty>Methane <empty> <empty>Ethane <empty> <empty>Propane <empty> <empty>i-Butane <empty> <empty>n-Butane <empty> <empty>i-Pentane <empty> <empty>n-Pentane <empty> <empty>n-Hexane <empty> <empty>n-Heptane <empty> <empty>H2O 1.05945913358397 <empty>DEAmine 1.07E-03 <empty>

pH 8.7881700352959


H2S Loading 2.69E-03H2S [Grains/US Gal] 14.7327546043009H2S Composition [ppm] 170.341393874613H2S Composition [Grains/100 SCF] 10.7027271106275CO2 Loading 1.86E-02CO2 Composition (Mole %) 0.11765685314132Acid Gas Loading 2.12E-02Amine Strength [wt %] 28.2747214419921Recirculation Rate [m3/h] 42.653010471758Temperature [C] 124.864550263284Pressure [kPa] 217.184911233424Molar Flow Rate [MMSCFD] 37.2186787740655

Regen Bttms (HOT IN) Lean from L/R (HOT OUT)

Aqueous Phase Stream Na Lean from Aqueous Phase0.999998421855 Vapour / Ph 0 1124.8645502633 Temperatur92.20357 92.20357217.1849112334 Pressure [k 148.2373 148.23731853.750868641 Molar Flow 1853.754 1853.754

43695.3723948 Mass Flow 43695.43 43695.4342.65295671013 Std Ideal L 42.65301 42.65301

-289915.6230378 Molar Enth -293061 -293061-173.5334696078 Molar Entr -181.6328 -181.6328-537431338.0389 Heat Flow [-5.43E+08 -5.43E+0842.21570399288 Liq Vol Fl 42.21576 42.21576

Fluid PackaConverted Utility Type

Aqueous Phase Stream Na Lean from Aqueous Phase23.57132942402 Molecular 23.57132 23.5713241.17755135652 Molar Dens 42.23336 42.23336970.6096278993 Mass Densi 995.496 995.49645.01848234225 Act. Volum 43.89312 43.89312

-12299.50240916 Mass Enthal-12432.93 -12432.93-7.36205695004 Mass Entrop-7.705669 -7.70566998.14435787165 Heat Capaci94.43572 94.43572

4.16371754457 Mass Heat C4.006382 4.006382152892.3308791 LHV Molar B152892.1 152892.1205552.5791736 HHV Molar B205552.3 205552.38720.449130211 HHV Mass Ba8720.441 8720.441

1.86E-02 CO2 Loadin 1.86E-02 1.86E-024.84E-02 CO2 Appare 4.97E-02 4.97E-024.99E-05 CO2 Appare 4.99E-05 4.99E-05

6486.368593334 LHV Mass Ba6486.361 6486.3610.999998739559 Phase Fract 0 10.999998778582 Phase Fract 0 10.999026272798 Phase Fract 0 1

<empty> Partial Pre 0 <empty>0 Cost Based 0 0

<empty> Act. Gas F <empty> <empty>43.46125126187 Avg. Liq. D 43.46127 43.4612798.14435787165 Specific He 94.43572 94.4357243830.89457828 Std. Gas F 43830.96 43830.961024.439470674 Std. Ideal 1024.439 1024.439

1.25E-02 Act. Liq. F 1.22E-02 1.22E-021.59E-03 Z Factor 1.16E-03 1.16E-03

8.984510017589 Watson K 8.98451 8.98451<empty> User Prope<empty> <empty><empty> Partial Pre 0 <empty>1.092556122618 Cp/(Cp - R) 1.096542 1.0965421.092556122618 Cp/Cv 1.143883 1.143883

<empty> Heat of Vap46876.17 <empty>0.391222903285 Kinematic V0.616098 0.6160981035.050188958 Liq. Mass D 1035.05 1035.0542.21570399288 Liq. Vol. F 42.21576 42.21576

1 Liquid Frac 1 12.43E-02 Molar Volu 2.37E-02 2.37E-02

<empty> Mass Heat o1988.695 <empty>0.999998421855 Phase Fract 0 149.25281713982 Surface Te 54.4077 54.40770.367844108077 Thermal Co 0.366811 0.3668110.379724716583 Viscosity [c 0.613323 0.61332389.83003787165 Cv (Semi-Id 86.1214 86.12143.810987333625 Mass Cv (Se3.653652 3.65365289.83003787165 Cv [kJ/kgmo82.55713 82.557133.810987333625 Mass Cv [kJ 3.50244 3.50244

<empty> Cv (Ent. Me<empty> <empty><empty> Mass Cv (En<empty> <empty><empty> Cp/Cv (Ent <empty> <empty>71.80208964343 Reid VP at 71.80283 71.802836.102893191878 True VP at 6.102894 6.10289442.21570399288 Liq. Vol. F 42.21576 42.21576

<empty> Viscosity I -4.372016 <empty><empty> Mass Exergy30.61811 <empty>

Aqueous Phase Mol Frac Aqueous Phase0 Nitrogen 1.25E-38 0

1.18E-03 CO2 1.18E-03 1.18E-031.70E-04 H2S 1.70E-04 1.70E-04

0 Methane 1.07E-32 00 Ethane 2.56E-33 00 Propane 1.04E-35 00 i-Butane 1.78E-47 00 n-Butane 1.42E-40 00 i-Pentane 4.25E-32 00 n-Pentane 7.10E-31 00 n-Hexane 6.83E-26 00 n-Heptane 5.56E-25 0

0.935262065116 H2O 0.935262 0.9352626.34E-02 DEAmine 6.34E-02 6.34E-02

Heavy Mixed Light Heavy<empty> Nitrogen <empty> <empty> <empty>6.547657470939 CO2 0 <empty> 07.965273303073 H2S 0 <empty> 0

<empty> Methane <empty> <empty> <empty><empty> Ethane <empty> <empty> <empty><empty> Propane <empty> <empty> <empty><empty> i-Butane <empty> <empty> <empty><empty> n-Butane <empty> <empty> <empty><empty> i-Pentane <empty> <empty> <empty><empty> n-Pentane <empty> <empty> <empty><empty> n-Hexane <empty> <empty> <empty><empty> n-Heptane <empty> <empty> <empty>1.059459133584 H2O 0 <empty> 0

1.07E-03 DEAmine 0 <empty> 0

pH 9.305483

M76

Emily Rowe: This guy only has aqueous phase but I checked this is the right phase

Osmotic Pr 11362.72Ionic Stren 8.65E-05Heat Capac 94.43572Viscosity 0.613323

H2S Loadin 2.69E-03H2S [Grains 14.73275H2S Compos170.3414H2S Compos10.70273CO2 Loadin 1.86E-02CO2 Compos0.117657Acid Gas L 2.12E-02Amine Stre 28.27472Recirculati 42.65301Temperatur92.20357Pressure [k 148.2373Molar Flow 37.21868

Regen Feed (COLD OUT)

Stream Name Regen Feed Vapour Phase Aqueous PhaseVapour / Phase Fraction 2.24E-03 2.24E-03 0.997755927371Temperature [C] 93.3333333333333 93.3333333333 93.33333333333Pressure [kPa] 551.58072694203 551.580726942 551.580726942Molar Flow [kgmole/h] 1954.27334159473 4.38553131547 1949.887810279Mass Flow [kg/h] 47228.8390520017 178.507882773 47050.33116919Std Ideal Liq Vol Flow [m3/h 47.1254678287494 0.23520114124 46.89026668745Molar Enthalpy [kJ/kgmole] -294682.924661065 -279362.09722 -294717.3830377Molar Entropy [kJ/kgmole-C -179.725878224275 -28.719524983 -180.0655096059Heat Flow [kJ/h] -575890983.888288 -1225151.2257 -574665832.6626Liq Vol Flow @Std Cond [m3 44.1268652257702 0.23150664337 44.15921626598Fluid Package Converted Basis-1 Utility Type

Stream Name Regen Feed Vapour Phase Aqueous PhaseMolecular Weight 24.1669566108198 40.703821255 24.12976322081Molar Density [kgmole/m3] 28.1948755202998 0.1854308757 42.70209711186Mass Density [kg/m3] 681.384333346551 7.54774521953 1030.391492342Act. Volume Flow [m3/h] 69.3130686172986 23.6504913164 45.66257730086Mass Enthalpy [kJ/kg] -12193.6298974912 -6863.2892098 -12213.85308843Mass Entropy [kJ/kg-C] -7.4368436671008 -0.7055731894 -7.462381953692Heat Capacity [kJ/kgmole-C] 87.9297693875904 47.724325153 88.02019624898Mass Heat Capacity [kJ/kg-C 3.63842956329153 1.17247775962 3.647785328165LHV Molar Basis (Std) [kJ/k 152347.177131352 357823.000482 151885.0373849HHV Molar Basis (Std) [kJ/k 203447.855206357 390963.075159 203026.1110089HHV Mass Basis (Std) [kJ/kg] 8418.43093785634 9605.0705586 8413.928854212CO2 Loading 0.45170036197941 <empty> 0.429577023843CO2 Apparent Mole Conc. [ 0.76579854671724 <empty> 1.105502769221CO2 Apparent Wt. Conc. [kg 1.12E-03 <empty> 1.07E-03LHV Mass Basis (Std) [kJ/kg] 6303.94548989859 8790.89455115 6294.510061907Phase Fraction [Vol. Basis] 4.99E-03 4.99E-03 0.995009043896Phase Fraction [Mass Basis] 3.78E-03 3.78E-03 0.996220362677Phase Fraction [Act. Vol. Bas 0.34121258498917 0.34121258499 0.658787415011Partial Pressure of CO2 [kPa 326.976878184503 <empty> <empty>Cost Based on Flow [Cost/s] 0 0 0Act. Gas Flow [ACT_m3/h] 23.6504913164403 23.6504913164 <empty>Avg. Liq. Density [kgmole/m 41.4695796484487 18.6458760039 41.58406313354Specific Heat [kJ/kgmole-C] 87.9297693875904 47.724325153 88.02019624898Std. Gas Flow [STD_m3/h] 46207.6918002433 103.693416418 46103.99838382Std. Ideal Liq. Mass Density 1002.193532033 758.958404008 1003.413597172Act. Liq. Flow [m3/s] 1.27E-02 <empty> 1.27E-02Z Factor <empty> 0.97621633219 4.24E-03Watson K 8.98584485244405 9.67812893429 8.979447269113User Property <empty> <empty> <empty>Partial Pressure of H2S [kPa] 103.145218366806 <empty> <empty>Cp/(Cp - R) 1.10443098750248 1.21096977703 1.104312509833Cp/Cv 1.0005518088925 1.23861535217 1.219267019248Heat of Vap. [kJ/kgmole] 53630.2716796597 <empty> <empty>Kinematic Viscosity [cSt] <empty> 2.16767855921 0.819785453174Liq. Mass Density (Std. Cond 1070.2967185718 771.070238742 1065.470249422Liq. Vol. Flow (Std. Cond) [ 44.1268652257702 0.23150664337 44.15921626598

Liquid Fraction 0.99775592737099 0 1Molar Volume [m3/kgmole] 3.55E-02 5.39284515721 2.34E-02Mass Heat of Vap. [kJ/kg] 2219.15703095394 <empty> <empty>Phase Fraction [Molar Basis] 2.24E-03 2.24E-03 0.997755927371Surface Tension [dyne/cm] 31.6635891260081 <empty> 31.66358912601Thermal Conductivity [W/m-<empty> 2.16E-02 0.451507743527Viscosity [cP] <empty> 1.64E-02 0.844699956496Cv (Semi-Ideal) [kJ/kgmole-C 79.6154493875903 39.410005153 79.70587624898Mass Cv (Semi-Ideal) [kJ/kg- 3.29439286335068 0.96821389093 3.303218333292Cv [kJ/kgmole-C] 87.8812757181647 38.5303840045 72.19107452219Mass Cv [kJ/kg-C] 3.63642295276929 0.94660360665 2.991785450258Cv (Ent. Method) [kJ/kgmole<empty> <empty> <empty>Mass Cv (Ent. Method) [kJ/k<empty> <empty> <empty>Cp/Cv (Ent. Method) <empty> <empty> <empty>Reid VP at 37.8 C [kPa] 1670.6958456258 6386.54908321 1601.625493793True VP at 37.8 C [kPa] 349.506303350271 <empty> 58.07500250392Liq. Vol. Flow - Sum(Std. Co 44.3907229093469 0.23150664337 44.15921626598Viscosity Index 0.49563508474442 <empty> <empty>Mass Exergy [kJ/kg] 25.1660026481295 <empty> <empty>

Mol Frac Vapour Phase Aqueous PhaseNitrogen 1.02E-07 4.44E-05 2.11E-09CO2 2.72E-02 0.59279967956 2.59E-02H2S 1.10E-02 0.18699931547 1.06E-02Methane 6.40E-05 2.72E-02 2.89E-06Ethane 3.09E-06 1.30E-03 1.76E-07Propane 4.52E-07 1.92E-04 2.09E-08i-Butane 2.46E-08 1.09E-05 1.04E-10n-Butane 8.31E-08 3.65E-05 1.24E-09i-Pentane 8.45E-06 2.79E-03 2.19E-06n-Pentane 9.35E-06 2.87E-03 2.92E-06n-Hexane 3.70E-05 7.48E-03 2.03E-05n-Heptane 3.21E-04 4.25E-02 2.26E-04H2O 0.90123568730343 0.13578565533 0.90295727614DEAmine 6.01E-02 9.35E-07 6.03E-02

Mixed Light HeavyNitrogen 21041.369228839 <empty> 21041.36922884CO2 22.8979883084657 <empty> 22.89798830847H2S 17.5852030809091 <empty> 17.58520308091Methane 9427.81683800273 <empty> 9427.816838003Ethane 7402.06605450114 <empty> 7402.066054501Propane 9168.22516020606 <empty> 9168.225160206i-Butane 104933.01688843 <empty> 104933.0168884n-Butane 29484.087926807 <empty> 29484.08792681i-Pentane 1270.98505823441 <empty> 1270.985058234n-Pentane 983.786703234619 <empty> 983.7867032346n-Hexane 368.478479499903 <empty> 368.4784794999n-Heptane 187.851539265574 <empty> 187.8515392656H2O 0.15037882623977 <empty> 0.15037882624DEAmine 1.55E-05 <empty> 1.55E-05

pH 7.64141833660849


H2S Loading 0.18342939073136H2S [Grains/US Gal] 910.235709379572H2S Composition [ppm] 11029.6781879963H2S Composition [Grains/10 693.006162970924CO2 Loading 0.45170036197941CO2 Composition (Mole %) 2.71609124915582Acid Gas Loading 0.63512975271077Amine Strength [wt %] 26.1593555251192Recirculation Rate [m3/h] 47.1254678287494Temperature [C] 93.3333333333333Pressure [kPa] 551.58072694203Molar Flow Rate [MMSCFD] 39.2368565705746

3004 heat ex stream conditions

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