tabel sifat-sifat thermodinamika uap air

20
Table A.1 Thermodynamic Properties of Steamu Table A.1 .1 Saturated Steam: TemBerature Table Specific Volume Internal Energy Enthalpy Iinropy T Press kPa P Sat. l,iquid uf Sat. Sat. Vapor Liquid Ile U1 Sat. Sat. Evap. Vapor Liquid L[s u' ht Sat. Sat. Sat. Evap. Vapor Liquid Evap. VaPor hrn h,t .r/ .!r" Jo A (tl 0.0l 5 10 l5 20 25 30 .13 40 z+ t) 50 5l) 60 o3 70 BO 85 90 95 0.61 13 0.001 000 206.14 0.8721 0.001 000 147 .t2 1.2276 0.001 000 106.38 1.7051 0.001 001 77 .93 2.339 0.001 002 57 .7s 3.169 0.001 003 43.36 4.246 0.001 004 32.89 5.628 0.001 006 25.22 7.384 0.001 008 19.52 9.593 0.001 010 15.26 12.349 0.001 012 12.03 15.758 0.001 015 9.568 19.940 0.00i 017 7.671 25.03 X 0.001 020 6.197 31.19 0.001 023 5.042 38.58 0,001 026 4. l3l 47.39 0.001 029 3.407 57.83 0.001 033 2.828 70.14 0.001 036 2.361 84.55 0.001 040 1.982 .00 2375.3 2375.3 '10.97 236 i .3 2382.3 42.00 2347 .2 2389.2 6 2.99 2333 .r 2 396. i 83.95 2319.0 2402.9 tB4-88 2304.9 2409,8 1?5.78 2290.8 2416.6 146.67 2276.1 2423.4 167.56 2262.6 2430.1 188.44 2248.4 2436.8 209.32 2234.2 2443.5 :30.21 2219.9 2450.1 251.1 I 2205.5 2456.6 272.02 2l9l.l 2463.1 292.95 2r76.6 2469.6 313.90 2162.0 2475.9 334.86 2147.4 2482.2 355.84 2132.6 2488.4 376.85 21t7.7 2494.5 397.88 2102.7 2500.6 .01 2501.3 250r .4 20.98 2489.6 2510.6 42.01 2477 .7 2519.8 62.9S 2465.9 2528.9 83.96 2454.1 2538.1 i04.89 2442.3 2547.2 r25.79 2430.5 2556.3 r46.68 2418.6 2565.3 167.57 2406.7 2s74.:\ 188.45 2394.8 2583.2 209.33 2382.7 2592.1 230.23 2370.7 2600.9 251 .13 2958.5 2609.6 272.06 2346.2 2618.3 292.98 2333.8 2626.8 313.93 232r.4 2635.3 334.9 I 2308.8 264:\.7 355.90 2296.0 2651.9 376.92 2283.2 2660.1 397.96 2270.2 266tt.l .0000 9. I l-r62 9.1562 .0761 tt.9496 9.0257 . l5 l0 8.7498 8.9008 .2245 8.5569 8.78 i 4 .2966 8.3 706 8.6672 .3674.8.1905 8.5580 .4369 8.0164 8.4533 .5053 7 .8478 8.3531 .s725 7.684s 8.2570 .6387 7 .5261 8.1648 .7038 7 .3725 8.0763 .7675 k2234 7.9913 .8312 7 .0784 7.9096 .tj935 {i 9375 7.8310 .9549 6.8004 7.7553 I .() t55 6.6669 7.6824 1.07s3 6.5369 7.6122 I . l:]43 6.41 02 7 .5445 1.1925 6.2866 7.4791 1.2500 6. 1659 7.4159 ,,Aclapted f r.orn .|oseph H. I(eenan, l.rederick (i. l(e,ves, Philip G. Hill, ancl Joan G. Moore, Stuam rn,les, (New Yot'k:.lolrn wiley & sons' Inc..1969).

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Page 1: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1

Thermodynamic Properties of SteamuTable A.1 .1

Saturated Steam: TemBerature Table

Specific Volume Internal Energy Enthalpy Iinropy

T

PresskPaP

Sat.l,iquid

uf

Sat. Sat.Vapor Liquid

Ile U1

Sat. Sat.Evap. Vapor LiquidL[s u' ht

Sat. Sat. Sat.Evap. Vapor Liquid Evap. VaPor

hrn h,t .r/ .!r" Jo

A(tl

0.0l5

10l5202530.13

40z+ t)

505l)60o370

BO

859095

0.61 13 0.001 000 206.140.8721 0.001 000 147 .t21.2276 0.001 000 106.381.7051 0.001 001 77 .93

2.339 0.001 002 57 .7s3.169 0.001 003 43.364.246 0.001 004 32.895.628 0.001 006 25.227.384 0.001 008 19.529.593 0.001 010 15.26

12.349 0.001 012 12.0315.758 0.001 015 9.56819.940 0.00i 017 7.67125.03 X 0.001 020 6.19731.19 0.001 023 5.04238.58 0,001 026 4. l3l47.39 0.001 029 3.40757.83 0.001 033 2.82870.14 0.001 036 2.36184.55 0.001 040 1.982

.00 2375.3 2375.3'10.97 236 i .3 2382.342.00 2347 .2 2389.26 2.99 2333 .r 2 396. i83.95 2319.0 2402.9

tB4-88 2304.9 2409,81?5.78 2290.8 2416.6146.67 2276.1 2423.4167.56 2262.6 2430.1188.44 2248.4 2436.8209.32 2234.2 2443.5:30.21 2219.9 2450.1251.1 I 2205.5 2456.6272.02 2l9l.l 2463.1292.95 2r76.6 2469.6313.90 2162.0 2475.9334.86 2147.4 2482.2355.84 2132.6 2488.4376.85 21t7.7 2494.5397.88 2102.7 2500.6

.01 2501.3 250r .420.98 2489.6 2510.642.01 2477 .7 2519.862.9S 2465.9 2528.983.96 2454.1 2538.1

i04.89 2442.3 2547.2r25.79 2430.5 2556.3r46.68 2418.6 2565.3167.57 2406.7 2s74.:\188.45 2394.8 2583.2209.33 2382.7 2592.1230.23 2370.7 2600.9251 .13 2958.5 2609.6272.06 2346.2 2618.3292.98 2333.8 2626.8313.93 232r.4 2635.3334.9 I 2308.8 264:\.7355.90 2296.0 2651.9376.92 2283.2 2660.1397.96 2270.2 266tt.l

.0000 9. I l-r62 9.1562

.0761 tt.9496 9.0257

. l5 l0 8.7498 8.9008

.2245 8.5569 8.78 i 4

.2966 8.3 706 8.6672

.3674.8.1905 8.5580

.4369 8.0164 8.4533

.5053 7 .8478 8.3531

.s725 7.684s 8.2570

.6387 7 .5261 8.1648

.7038 7 .3725 8.0763

.7675 k2234 7.9913

.8312 7 .0784 7.9096

.tj935 {i 9375 7.8310

.9549 6.8004 7.7553I .() t55 6.6669 7.68241.07s3 6.5369 7.6122I . l:]43 6.41 02 7 .54451.1925 6.2866 7.47911.2500 6. 1659 7.4159

,,Aclapted f r.orn .|oseph H. I(eenan, l.rederick (i. l(e,ves, Philip G. Hill, ancl Joan G. Moore, Stuam rn,les, (New Yot'k:.lolrn wiley & sons'

Inc..1969).

Page 2: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1 .1 (Continued)Saturated Steam: Temperature Table

Specific Volume Internal Ener.gy Iinthalpy Entropy

L,

T

Press.NIPa

P

Sat.Liquid

U1

Sat.Vapor

Tg

Sat.Liquid

Uy

Evapufs

Sat.Vapor

us

Sat.Liquid

hr

Sat.Vaptir

t,,

Sat.Liquid

.t/

Sat.Vapor

.t9

Evap.h,,,

EvapJn,

100105I l0t 15120t25130135140t45150155160t65170r/5rB0185190r95200205210

0.101 350.120 8?0.143 270.169 060.198 530.23210.27010.313i)0.36130.41510.47 580.54310.61 780.70050.7 s 170.89201,00211 . t2271.25441.39781.55381.7230r.9062

|.67291.4 t 941.2102l 03660.89190.7 7 060.66850.58220.50890.44630.39280.34680.30710.27270.24280.21680.194 050.174 090.156 540.141 050.127 360.115 2l0.104 4I

4I8.94440.02461.14482.30503.50524.7 4546.02567.35588.7 4610. t 8631.68653.24674.87696.56718.337 40.17762.09784. I 0806. t9828.37850.6587i3.04895.53

2087.62072.32057.0204t.42025.82009.9r 993.9t977.7r 961 .3t914.7\927.9r-9 I 0.81893.5I876.0I 858. Ir 840.0l82l .6l 802.9r 783.81764.417 44.71724.51703.9

2506.52512.42518.12523.72529.32531.62539.92545.02550.02554.92559.52564.r2568.42572.52576.52580.22583.72587.02590.02592.896q6 C

2s97.s2599.5

2ii76. i2683.82691.52699.02706.327 13.52720.52727.3.6-!)-.n

t4lJJ.V\2710.32746.527 52.42758. I2763.52768.7tt t.).o2778.22782.42786.42790.097q\,)2796.02798.5

306936304 185

t.47345276

l 581.31.6344| .6870

0.001 0440.001 0480.001 0520.001 0560.001 0600.001 0650.001 0700.00 i 0750.001 0800.00r 0u50.001 0910.001 0960.001 1020.001 t 0B0.001 1140.00r 12t0.001 1270.001 1340.001 I4t0.001 1490.001 1570.00 I 1640.00I 173

4t9.04 2257.0440.15 2243.746 I .3 0 2230 .2482.48 22 t 6.5503.71 2202.6524.99 2188.5546.31 2174.2567.69 2159.65rJ9.l3 2144.7610.63 2129.6632.20 2t14,3653.84 2098.6675.55 2082.6697.34 2066.2719.21 2049.5741.17 2032.4763.22 2015.0785.37 1997. I807.62 1978.8829.98 1960.0852.45 1940.7875.04 1921.0,897.76 1900.7

6.0480 7.35495.9328 7,29585.8202 7.23875.7100 7.18335.6020 7.12965.4962 7.07755.3925 7.0269s.2907 6.97775.I908 6.92995.0926 6.88334.9960 6.83794.9010 6.79354.8075 6.75024.7153 6.70784.6244 6.66634.5347 6.62564.4461 6.58574.3586 6.54654.2720 6.50794. t863 6.46984.r014 6.43231.0r72 6.39523.9337 6.3585

).73911.7507

84r8892594279925

2.04192.09092. 1 3962, I 8792.23592.28352.3 3 092.3 7802.4248

215 2.10,1220 2.318225 2.548230 2.795235 3.060240 3.344245 3.648250 3.973255 4.3 19260 4.688265 5.081270 5.49!l27 5 5.942280 6.4t2285 6.909290 7 .436295 7.993300 8.58 r305 9.202310 9.8563 I 5 10.547320 rr.271330 12.845340 14.586350 16.5 I 3360 I8.65 r

':J70 21.03374.14 22.09

0.001 l8l0.001 1900.00 r 1990.00 r 2090.001 2190.001 2290.00r ?400.00 t ?510.001 2630.001 2760.001 2890.001 3020.00r 3r70.001 3320.001 3480-aql 3660.001 3840.001 4040.001 4250.00 r 4470.001 4720.001 4990.001 5610.001 6380.001 7400.001 8930.002 2130.003 155

0.094 790.086 190.078 490.07 r 580.065 370.059 760.051 710.050 130.045 980.042 210.038 770.035 640.032 790.030 170.027 770.025 570.023 rt40.021 670.0 r 9 9480.018 3500.0 r 6 8670.015 4880.012 9960.0 r 0 7970.008 8130.006 9450.004 9250.003 i 55

1879.9 2800.51858.5 ?802.r1836.5 2803.31813.8 2804.01790.5 2804.21766.5 2803.8174t.7 2803.0t716.2 2U01.51689.8 2799.5r662.5 2796.91634.4 2793.61 605. ? 27 89 .7r574.9 2785.0r543.6 2779.6I5t1.0 2773.1J1477.1 2766.21441.8 2758. I

1404.9 2749.01366.4 2738.71 3 26.0 27 27 .t\1283.5 27 14.5r 238.6 2700. r

i 140.6 2665.9t027 .9 2622.0893.4 2563.!)720.5 248r.044t .6 233 2. 1

0 2099.3

l 04.28r 28.39| 52.7 4t77 .36

109.73134.37159.28184.5 i

918. r4940.87963.73986.74

1009.891033.2 r1056.71I 080.39

r 682.9166 I .51639.616t7.2r594.21570.8r546.71522.01496.71470.61443.91416.31387.91358.7r328.41297 .l1264.71231.0

195.9159.4121.1

260 1. I2602.42603.32603.92604.12604.02603.42602.42600.92599.02596.62593.72590.22586. r

258 r.42576.02569.92563.02555.22516.42536.62525.52498.92464.62418.4235 I .52228.52029.6

920.62943.62966.78990. I 2

1013.621037.32106r.231085.36

2.47t4 3.8507 6.32212.5r78 3.7683 6.28612.q639 3.6r.163 6.25032.6099 3.6047 6.21462.6558'3.5233 6.179r2.701b 3.4422 6.14372.7472 3.3ii r2 6.10832.7 927 3.2 802 6.07302.8383 3.1992 6.03752.8838 3.llBl 6.00192.9294 3.0368 5.96622.9751 2.955i 5.9301 *3.0208 2.8730 5.89383.0668 2.7903 5.85713.1130 2.7070 5.81993.1594 2.6227 5.78213.2062 2.537 5 5.7 4373.2534 2.15t t 5.7 0453.30r0 2.3633 5.66433.3493 2.27 37 5.62 303.3982 2. r 82 l 5.58043.4480 2.0882 5.53623.5507 1.8909 5.44173.6594 1.6763 5.33573.7777 1.4335 5.21123.9147 1. r379 5.05264. n06 .6865 4.79714.4298 0 4.4298

1202.251227.461253.00t278.921305.21332.0I 359.3I387.11415.51444.61505.31570.3r 6'1r.917 25 .2I 844. 02029.6

1080.9993.7894.3/ /o.o626.3384.5

0

1210.071235.991262.311289.0713 r 6.31344.0r372.1r40r.3r431.01461.5t525.31554.21670.61760.5r 890.52099.3

Page 3: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1.2Saturated Steam: Pressure Table

Specific Volume Internal Energy Entl'ralpy Entropy

Press. Te m p.kPa / oC

lrT

Sat. Sat.Vapor l-iquid

us ul

Sat. Sat.Evap. Vapor Liquidulg ut, hI

Sat.Liquid

U1

Sat. Sat. Sat.Evap. Vapor Liquid livap. Vapor

hto h,, J1 stu .re

0.61 13 0.0 IL0 6,981.5 13.032.0 17.502.5 2 1.083.0 24.084.0 28.965.0 32.8rJ7.5 40.29

10 45.8I15 53.9720 60.0625 64.9730 69.1040 7 5.8750 B 1.3375 91.78

0.00 r 0000.001 0000.001 0010.00 r 0010.001 0020.00 t 0030.001 0040.001 0050.00I 00ti0.001 0100.00r 0i40.001 0170.001 0200.001 0220.001 0270.00 r 0300.00I 037

206.14 .00r 29.21 29.3087.98 54.7167.00 73,4854.25 88.4845.67 101.0434.80 12r.4528.19 \ i37.8119.24 r68.7814.67 i 91.8210.02 225.92

7 .649 251.386.204 27 i.905,229 289.203.993 317.533.240 340.442.217 :r8+.31

2375.3 237s.32355.7 2385.02338.6 2393.32326.0 2399.52315.9 2404.42307.5 2408.52293.7 2415.22282.7 2420.52261.7 2430.52246.1 2437.92222.8 2448.72205.4 2456.72191.2 2463.12179.2 2468.42159.5 2477 .02143.4 2483.92r12.4 2496.7

.0 r 2501.329.30 2484.954.7 | 2470.673.48 2460.088.49 245r.6

101.05 2444.5121.46 2432.9137.82 2423.7168.79 2406.0

-19 l .83 2392.8225.94 2373.1251.40 2358.327r.93 2346.3289.23 2336.1317.58 2319.2340.49 2305.4384.39 227 8.6

250 1.4 .000025t4.2 . r 0592521t.3 .19572533.5 .26072540.0 .31202545.5 .35452554,4 .422625ii 1.5 .47642574.8 .57642584.7 .64932599.1 ./ .75492009.7 .83202618.2 .89312625.3 .94392636.8 1.025926115.9 l 09102663.0 r.2r30

9.1562 9.15628.8697 8.97568.6322 8.82798.4629 8.72378.331 1 8.64328.2 23 1 8.57 7 68.0520 8.47467 .9187 8.39517 .67 50 8.25157.5009 8.15027.2Pfi6 B.oo857.0766 7.90856.9383 7.83146.8247 7.76866.6441 7.67006.5029 7.59396.2.134 7.1561

Mlta0. 100 99.630. i 25 105.990.150 I I 1.370. 175 l 16.060.200 120.23O.?2ir 12.1.()o

0.0010.0010.0010.00 r

0.(x) Io o{) |

043048trI).)0s70(i I( )( t.l

1.6940t.37 49t. l 593r.00360.8857o.7!):l:l

2675.52685.42693.62700.62706.7!7 r2. r

1.3026| .37 40

417.36 2088.7 2s06.1144.t9 2069.3 !5 r3.5466.94 2052.7 2519.7186.80 2038. r 2524.950.1.49 2O25.0 2lt2!t.b',J':o..ti :.to l:1. i ?r:ttt.r)

4r7.46 2258.0444.32 2241.0467 .l | 2226.5486.99 2213.650,1.70 !20r.()t-'2O.72 : l1) l.:l

535.37 2181.5548.89 2r72.456r.47 2r63.8573.25 2155.8584.33 2l48.l594.81 2140.8604.74 2133.8623.25 2120.7640.23 2 r 08.5655.93 2097.0670.56 2086.3684.18 2076.0697.22 2066.3709.47 2057.t)72r.rt 2048.0732.22 2039.4742.83 2031.I753.02 2023.1762.8I 2015.3781.34 2000.4798.65 1986.2814.93 r972.7830.30 1959.7844.89 t947.3878.50 1917.9908.79 1890.7936.49 t865.2962.1I 184r.0

1 00 8.42 t7 95 .7

6.0568 7.35945.9104 7.28445 .7 897 7 .22335.6868 7.17175.5970 7.127 I5.lt I7ll 7.(l!l7tl

-.!i!#.' .*'.-.'.. \*11W

5.4455 7.05275.3801 7.02095.3201 6.99195.2646 6.96525.2130 6.94055.1647 6.91755. I 193 6.89595.0359 6.85654.9606 6.82134.8920 6.78934.8288 6.76004.7 7 03 6.733 l"4.7158 6.70804.6647 6.68474.6166 6.66284,5711 6.6421,1.5280 6.62264.4869 6.60411.4478 6.58654.3744 6.55364.3067 6.52334.2438 6.49534. 1850 6.46934. r 298 6.44484.0044 6.38963.8935 6.3409i\.7937 6.29723.7028 6.25753.5412 6.1869

.4336484\)5:to Ii7 0(;

0.2500.27 50.3000.3250.3500.3750.400.450.500.550.600.650.700.7 50.800.850.900.!151.001.10 r1,20 )1.301.40I .50l./52.002.252.53.0

127.41130.60I .).1.3 )136.30138.88t4r.32143.63r47.93l5r.86155.4tJ158.85r 62.01164.97167.78170.43172:9617 5.38177.69179.9118.1.09187.99191.64195.07198.32205.76212.42218.,r5223.99233.90

0.001 0670.00 r 0700.00 r 0730.00 r 0760.001 0790.001 0810.00I 0840.001 0880.001 0930.001 0970.001 r 0l0.00 r r 04'0.001 108

0.7 1870.65730.60580.56200.52430.49 i40.46250.4 r 400.37490.34270.3 r 570.2927{).27290.2556().24040.22700.2 1500.20420.r94 440.177 530.163 330.151 250.140 840.r3r 770. n3 490.099 630.088 750.079 980.066 68

27 i6.9272r.32725.32729.02732.427 35.62738.62743.927 48.727 53.02756.r12760.32763.52766.42769, I2771.62773.927 7 6.12778.12781.72784.82787.62790.02792.22796.42799.5280r.72803. l2804.2

1.6408r.67rB

6072

.7006

.7275

.7 528

.77 66r.8207

535.10 2002.1 2537.2548.59 1991.9 2540.5561.15 1982.4 2543.6572.90 1973.5 2546.4583.95 1965.0 2548.9594.40 r956.9 255 t.3604.31 1949.3 2553.6622.77 1934.9 2557.6639.68 192 1.6 256r.2655.32 1909.2 2564.5669.90 i897.5 2567.4683.56 1886.5 2570.r696.44 1876. I 2572.5708.64 1866.1 2574.7720.22 1856.6 2576.873r.27 1847.4 2578.77 4r.83 1838.6 2580.5751.95 r830.2 2582.1761.68 r822.0 2583.6780.09 1806.3 2586.4797 .29 r 79l.5 2588.88I3.44 1777 .5 2591.0828.70 1764.1 2592.8843.16 175r.3 2594.5876.46 ' 172t.4 2597.8906.44 r693.8 2600.3933.83 1668.2 2602.0959.rr 1644.0 2603.1

r004.78 1599.3 2604.1

.8607

.8973

.93r2:9627.9C22

0.001 I l20.001 I l50.00 t I l80.001 l2 l0.001 1240.001 1270.001 1330.001 r 390.00 l 1440.00r 1490.001 1540.001 1660.001 1770.00I I B70.0t) I 1970.00 i 2 l7

2.02002.0462z.0z r o2.09462.t 172.2.t3872.17922.21662.25152.28422.31502.38512.447 42.50352.55472.6457

Page 4: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.'1.2 (Continued)

SaiurateO Steam: Pressure TableEnthalPY EnttopY

Specific Volume lnternal EnergY

Pt'essNIPa

P

^ ''_'r"CT

Sat.Liquid

uJ

Sat.Vapor

ug

Sat.Liquid

uJ

Sat.Liquid

hlEvap

hr,,

Sat.Virpot"

hu

S:rt.Liquid

J/

Evap..)tu

Sat.Vapor

Js

- Sat'Evap. VaPoru1s uq

3.51I'r

67

dI

l01l1213l4l5t6T7

l819202l22

2 2.0!l

242.60250.40263.9927 5.64285.88295.06303.4031 1.06318. 15

324.75330.93336.75

"19 94

347.44352.37357.06361.54365.81369.89373.8037 4.t1

1045.431082.31I 147.8 I1205.441257.551305.571350.5 t1393.041433.7t473.01511.1r 548.61585.61622.7r 660.21698.91739.91785.6I 842. 1

196 1 ,9

2029.6

r 558.31520.01449.31384.31323.0t264.21207.31 151.41096.01040.7985.0o9R 9

869.8809.07 44.8o/).4598:1507 .5388.5194 2

0

2603.72602.32597.12589.72580.52569.82557.82544.4e(9q R

2513.72496.12476.82455.52431.72405.02374.32338.12293.02230.62087. I

2029.6

1049.75i 087.3 1

tr54.231213.351267.001316.641363.261407.561450. I1491.3153 1 .5

1571.11610.51650. I1 690.3t732.0I / /O.51826.31888.49n.9.) <)

2099.3

t'i 53.71714.r1640. I1571 .0I 505.11441.31378.91317.11255.5l193.6I 130.71066.51000.0930.6856.9

688.0583.4446.2r43.4

0

2803.42801.42794.3.2784.3.)Ft a t) 1

2758.0e1 L') 1

2724.72',705.6

2684.92662.22637.62610.52580.62547.22509. I

2464.52409.72334.62 I ti5.62099.3

e ?96'1

2.79642.92023.02673.12113.20683.28583.35963.42953.49623.56063.62323.68483,7 4613.80793.87153.93884.01394.107 54.31 l04.4298

3.400i)3.27 373.05322.86252.69222.53642.39159'14442. I 2331.99621.87181 .7 4851.62491.49941.3698I ,)q9q

1.0839.9130.6938.22t6

0

6.12536.07015.51345.8 89 2

5.81335.7 432b.67725.61415.55z t

^ 4A94

5.4323c.J / r ,

5.3098h.24555.ll t t

5.1 0445.02284.92694.80134.53274.4298

0.001 2:15 0.057 07

0.001 252 0.049 78

0.001 286 0.039 44

0.001 319 0-032 44

0.001 35i 0.027 37

o.oo1 384 0".j'23-520.001 418 0.020 48

0.001 452 0.018 026

0.001 489 0.015 987

0.001 527 0.014 263

0.00 I 567 0.012 780

0.001 6l 1 0.01 I 485

0.001 658 0.010 337

0.001 71 I 0.009 306

0.001 770 0.008 364

0.001 840 0.007 489

0.001 924 0.006 657

0.002 036 0.005 834

0.002 207 0.004 952

0.002 7420.003 155

0.003 5680.003 155

Table A.1 .3Superheated Vapor

P: .010 MPa (45.81) P : .050 MPa (81.33) P: .10 MPa 199.63)

T

Sat. 14.67 450 14.869

100 17.196150 19.5 l2200 21.825250 24.126300 26.145400 31.063500 35.679600 40.295700 44.9 t r800 49.526900 54.l4l

1000 58.7 57r 100 63.372r 200 67 .9871300 72.602

2437.9 2584.72443.9 2592.62515,5 2687.52587.9 2783.02661.3 2879.52736.0 2977.328 1 2. 1 307 6.52968.9 3279.63t32.:J 3489. t3 302.5 37 05.43479.6 3928.73663.8 4159.03855.0 4396.44053.0 4640.64257 .5 4891.24467.9 5147 .84683.7 5409.7

P : .20 MPa (120.23)

3.240 2483.9 2645.9 7.5g3g

3.418 251 1.6 2682.5 7 .69473.889 2585.6 2780.1 7 .94014.356 2659.9 2871 .1 8.15804.820 2735.0 2976.0 8.35565.284 28 l I .3 307 5.5 8.53 736.209 2968.5 327 8.9 8.86427 .r34 3132.0 3488.7 9.15468.057 3302.2 3705.1 9.4178B.9B 1 3479.4 3928.5 9.65999.904 3663.6 4158.9 9.8852

10.828 3854.9 4396.3 r0.096711.751 4052.9 4640.5 10.296412.674 4257.4 489r.1 10.485913.597 4467.8 5147.7 10.666214.521 4683.6 5409.6 10.8382

P : .30 MPa (133.55)

1.6940 2506. l 267 5.5 7 .3594

L6958 2506.7 2676.2 7.3614r.9364 2582.8 2776.4 7.6t342.t72 2658. i 2875.3 7.83432.406 2733.7 2974.3 8.03332.639 28 r 0.4 307 4.3 8.21583.103 2967.9 3278.2 8.54353.565 313r.6 3488,r 8.83424.028 330i.9 3704.7 9.09761.490 3479.2 3928.2 9.33984.952 3663.5 4 r 58.6 9.56525.4r4 3854.8 4396. r 9.77675.875 4052.8 4640.3 9.97646.337 4257.3 489r.0 10.r6596.799 4467 .7 5147 .6 10.34637.260 .1683.5 5409.5 10.5183

P : .4() MPa (143.63)

8. l 5028.r7 498.44798.68828.90389. 1 0029.2s1 3

9.60779.8978

10.r60810.402810.6281r 0.8396

1.0393t.22871.40911.581 I

Sat. .8857150 .959ti200 r.0803250 1. r988300 1.3162.100 1.5493

2529.5 2706.7 7.12722576.9 2768.8 7.27952654.4 2870.5 7.5066273r.2 297r.0 7.70862808.6 3071.8 7.89262966.7 327 6.6 8. 2 2 I 8

.6058 2543.6 2725.3

.6339 2570,8 276r.0

.7 163 2650.7 2865.6

.7964 2728.7 2967.6

.8753 2806.7 3069.3I .03 1 5 2965.6 327 5.0

6.99197.07787.3rt5/.5IOO7.70228.0330

.4625 2553.6 2738.6 6.8959

.4708 2564.5 2752.8 6.9299

.5342 2646.8 2860.5 7.1706

.595 i 2726.1 2564.2 7.3789

.6548 2804.8 3066.8 7.5662

.7726 2964.4 3273.4 7.8985

Page 5: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1.3 (Continued)Superheated Vapor

"l

I' : .20 MPa (120.23) P : .30 MPa (133.55) P:.40 MPa (143.63)

ir00 L78t4 3l30.tJ 3187.1 8.5133600 2.013 3301.4 3704.0 8.7770700 2.244 3478.8 3927.6 9.0194800 2.475 3663. r 4158.2 9.2449900 2.7 06 3 854.5 4395.8 9.4566

i000 2.937 4052.5 4640.0 9.6563l 100 3. r 68 4257.0 4890.7 9.84581200 3.399 4467.5 5147.3 10.0262r 300 3.630 4683.1 5409.3 I0.1982

P : .50 MPa (151 .86)

l. 1867 3130.0 3486.0 8.325 r

1.3414 3300.8 3703.2 8.5892r.4957 3478.4 3927.1 8.83191.6499 3662.9 4t57 .8 9.05761.8041 3854.2 4395.4 9.2692t.9581 4052.3 4639.7 9.46902.lt2t 4256.8 4890.4 9.65852.2661 4467 .2 5147 .t 9.83892.4201 4683.0 5409.0 10.01l0

P:.60 MPa (158.85)

.8893 3 t29.2 3484.9 8.19131.0055 3300.2 3702.4 8.4558l.l2l5 3477 .9 3926.5 8.6987t.2372 3662.1 4157.3 8.92441.3529 3853.9 4395. l 9. r3621.4685 4052.0 4639.4 9.33601.5840 425b.5 4890.2 9.52561.6996 4467.0 5146.8 9.7060r.8l5 r 4682.8 5408.8 9.8780

P:.80 MPa (170.43)

Sat.200250300350400500600700800900

I(XX)

6.82137.05927.27097.45997.63297.79388.08737.35228.59528.821 1

9.03299.2328

.37 49 2561.2 27 48.7

.4249 2642.9 2855.4

.4744 2723.5 2960.7

.5226 2802.9 3064.2

.5701 2882.6 3167 .7

.6173 2963.2 321 t.9

.7109 3128.4 3483.9

.8041 3299.6 3701.7

.8969 3.177.5 3925.9

.9896 3662. 1 4156.91.0822 3853.6 4394.71 .17,47 405 LI .1639. I

.3157 2567.4 2756.8 6.7600

.3520 2638.9 2850.I 6.9665

.3938 2720.9 2957 .2 7.1816

.4344 2801 ,0 3061.6 7 .3721

.4742 2881.2 3165.7 7.5464

.5137 2962.1 3270.3 7.7079

.5920 3127 .6 3482.8 8.002 r

.6697 3299.r 3700.9 8.2674

.7 472 3477 .0 3925.3 8.5107

.8245 3661.8 4156.5 8.7367

.9017 3853.4 4394.4 8.9486

.9788 405 I .5 4638.8 9. l4fi.5

2769. r 6.66282839.3 6.81582950.0 7.03843056.5 7.23283i61.7 7.40893267 .t 7.57163480.6 7.867336ee:4 8. r3333924.2 8.377041 55 .6 8.60 3 343s3.7 8.8 I 53.1{t3ft.? 9.015.?

.2404 2576.8

.2608 2630.6

.2931 2715.5

.3241 2797.2

.3514 2878.2

.3843 2959.7

.4433 3126.0

.50 r 8 3297.S

.5601 347 6.2

.6t8r 3661.r

.676 r 3852.8

.7340 405 l,()

l100 r.2672r200 1.35961300 |.4521

4256.3 4889.94466.8 5146.64682.5 5408.6

P: 1.00 MPa (179.91)

1.0559 4256.r 4889.61.1330 4466.5 5146.31.2101 4682.3 5408.3

P : 1.20 MPa (187.99)

.79 19 4255.6 4889. I 9.2050

.8497 4466.1 5145.9 9.3855

.9076 4681.8 5407.9 9.5575

P : 1.40 MPa (195.07)

9.42249.60299.7749

9.338I9.51859.6906

Saf. .194 44 2583.6 2778.1200 .2060 2621.9 2827.9250 .2327 2709.9 2942.6300 .2575 2793.2 3051.2350 .2825 2875.2 3157.7400 .3066 2957.3 3263.9500 .3541 3124.4 3478.5600 .401 I 3296.8 3697.9700 .447 B 347 5.3 3923. I800 .4943 3660.4 4154.7900 .5407 3852.2 4392.9r000 .5871 4050.5 4637 .6I i00 .6335 4255.1 4888.6r200 .6798 4465.6 5145.41300 .7261 .1681.3 5407 .4

6.5865 .163 33 2588.86.6940 .169 30 2612.86.924? .r92 34 2704.27.1225 .2138 2789.27.3011 .2345 2872.27.465r .2548 2954.97 .7622 .2946 3 122.88.0290 .3339 3295.68.273 r .3729 3474.48.4996 .41 l8 3659.7B.7l 18 .4505 3851 .6B.9l l9 .4892 4050.09.1017 .5278 1254.69.2822 .5665 4465.19.4543 .6051 4680.9

2784.8 6.52332815.9 6.58982935.0 ^ 6.82943045.8 7 .03173153.6 7 .2r2r3260.7 7.37743476.3 7.67593696.3 .7.94353922.0 8.18814 153.8 8.4 l484392.2 8.62724637.0 8.82744888.0 9.01725144.9 9.19775407.0 9.3698

.140 84 2592.8

.t43 02 2603.I

.163 50 2698.3

.182 2B 2785.2

.2003 2869.2

.2178 2952.5

.2521 3 l2 1. 1

.2860 325y.4

.3191r 3473.6

.3528 3659.0

.3861 3851. I

.4192 4049.5

.4524 4254.1

.4855 4464.7

.5186 4680.4

2790.0 6.46932803.3 6.497 5

2927.2 6.74673040.4 6.95343 r 49.5 7.13603257 .5 7.3026 "3474.1 1.e,C2i3694.8 7.87l03920.8 8. I 1604 r53.0 8.34314391 .5 8.55564636.1 8.75594887.5 8.94575t44.4 9. 12625406.5 9.2984

P: 1.60 MPa (201.41) P: 1.80 MPa (207.15) P : 2.00 MPa (212.42)

Sat. .123 80225 .r32 87250 .l4l 84300 .158 62350 .174 56

r400 .190 05

. 500 .2203600 .2500700 .2794

2596.0 2794.02644.7 2857.32692.3 2919.22781.1 3034.82866.1 3145.42950.1 3254.23119.5 3472.03293.3 3653.23472.7 3919.7

6.42t8 .ll0 426.5518 .116 736.6732 .t24 976.8844 .140 2r7.0691 .154 577.2374 .-.168 477.5390 - .195 507.8080 .22208.0535 .2482

2598.4 2797.r2636.6 2846.72686.0 2911.02776.9 3029.22863.0 3141.22947.7 3250.931 17.9 3469.83292.r 3691.7347r.8 3918.5

6.379'4 .099 636.4808 .1.03 776.6066 .r11 446.8226 .t25 177.0100 .138 577 .t794 .15l 207 .4825 . 125_687 .7 523 . 199 60? qoR'l 99\,)

2600.3 2799.5 6.34092628.3 2 83 5.8 6.41472679.6 2902.5 6.54532772.6 3023.5 6.76642859.8 3137.0 6.95632945 2 3247.6 7 .r27 |3r16.2 346? .6 7.43173290.9 3690. I 7.70243470.9 3917 .4 7.9487

Page 6: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1.3 (Continued)Superheated Vapor

P: 1.60 MPa (201.41) P : 1.80 MPa i207. I51 P : 2100 MPa (212.42)

800 .3086 3658.3 4152.1900 .337 7 3 85 0.5 4390.8

1000 .3668 4049.0 4635.8I 100 .3958 4253.i 4887.01200 .4248 4464.2 5143.91300 .4538 4679.9 5406.0

8.2258 .2467 3657.08.43 86 .27 00 3 849.38.6391 .2933 4048.08.8290 .3166 4252.79.0096 .3398 4463.39.18r8 .3631 4679.0

4 r 50.3 B. 17654389.4 8.38954634.6 8.59014885.9 8.78005142.9 8.96075405. r 9.1329

P :2.50 MPa (223.99)

8.2808 .2742 3657.6 4151.28.4935 .3001 3849.9 4390.18.6938 .3260 4048.5 4635.28.8837 .3518 4253.2 4886.49.0643 .3776 4463.7 5143.49.2364 .4034 4679.5 5405.6

P: 3.00 MPa (233.90) P: 3.50 MPa 1242.60)

Sat. .079 98225 .080 27250 .087 00300 .098 90350 .109 76400 .120 10450 .130 14

500 .139 98600 .1 59 30700 .r7B 32800 .197 16

900 .215 901000 .23461100 .25321200 .27 r 8l 300 .2905

2603.1 2803.1 6.25752605.6 2806.3 6.26392662.6 2880.1 6.40852761.6 3008.8 6.64382851.9 3126.3 6.84032939.1 3239,.3 7.01483025.5 3350.8 7,17463l 12.1 3462.t 7.32343288.0 3686.3 7.59603468.7 3914.5 7.84353655.3 4148.2 8.07203847.9 4387.6 8.28534046.7 4633.1 8.4861425r.5 4884.6 8.67621462.1 514t.7 8.85694677.8 5404.0 9.0291

.066 68 2604.1 2804.2

.070 58 2644.0 2855.8

.081 l4 2750.1 2993.5

.09053 2843.7 3115.3

.099 36 2932.8 3230.9

. 1 07 87 3020.4 3344.0

.116 19 3108.0 3456.5

.t32 43 3285.0 3682.3

.148 38 3466.5 3911.7

.164 14 3653.5 4145.9

.179 80 3846.5 4385.9

.195 41 4045.4 4631.6

.210 98 4250.3 4883.3

.226 52 4460.9 5140.5

.242 06 4676.6 5402.8

6.1869 .057 07

6.2872 .058 726.5390 .068 426.7428 .076 786.9212 .084 537 .0834 .091 967.2338 .099 r 8

7.5085 .l 13 247.7571 .126 997.9862 .140 568.1999 .154 028.4009 .167 438.5912 . 180 808.7720 .194 15

8.9442 .207 4tl

2603.7 2803.4 6.1253

2623.7 2829.2 6.17492738.0 2977.5 6.446r2835.3 3104.0 6.Orzs2926.4 3222.'3 6.840530i5.3 3337.2 7,00523103.0 3450.9 7.r5723282.1 3678.4 7.43393464.s 3908.8 7.6837stsr.s 414J.7 7.gtz43845.0 4384.r 8.12764044.1 4630.1 8.32884249.2 4881 .9 8.51924459.8 5139.3 8.70004675.lt lt'lo l.l U.8723

P : 4.0 MPa (250.40) P :4 5 ue\gz.+ot l'J : 5.0 MPa (263.99)

S:rt. .049 78 ?602.3 2801 .4275 .054 57 2667.9 2886.2300 .058 8,1 2725.3 2960.7350 .066 45 28?6.7 3092.5400 .073 4l 2919.9 3213.6450 .080 02 3010.2 3330.3500 .086 43 3099.5 3445)'600 .098 85r 3279.I 3674.4700 . 1 l0 95 3462.1 3905.9800 .122 87 3650.0 4141.5900 . i 34 69 3843.6 4382.3

1000 .t46 45 1042.9 4628.7r 100 . l5B 17 4248.0 4880.61200 .169 87 4458.6 5 i 38. i1300 . 18 r 56 4671.3 5400.5

P:6.0 MPa (275.64)

2600.1 2798.32650.3 2863.227 r2.0 2943.12B 17.8 3080.62913.3 3204.73005.0 3323.33095_3 3439.63 2 76.0 367 0.53459.9 3903.03648.3 4139.33842.2 4380.64041.6 4627 .24246.8 4879.34457 .5 5136.94673.1 5399.4

P : 7.0 MPa (285.88)

6.0 t 98 .039 .14 2597 .l6. t40 r .04r 11 263 t.36.2828 .045 32 2698.06.513 I .051 94 2808.76.7047 .0578r 2906.66.8746 .063 30 2999.77.030L_--O68 57 3091.07.3110 .07869 3273.07.563r .0BB 49 3457.67.7942 .098i1 3646.68.009r .r07 62 3840.78.2 108 .t t7 07 4040.48.4015 .126 48 4245.68.5825 . 135 87 4456.38.7549 .145 26 4672.0

6.07016.22856.36156.58216.76906.93637.09017.36887.61987.85028.06478.26628.45678.63768.8100

.044 06

.047 30

.051 35

.058 40

.064 7 b

.070 74

.076 5l

.087 65

.098 47

.r09 1l

.119 65

.130 l3

.140 56

.150 98

. 161 39

2794.3 5.97342838.3 6.05442924.5 6.20843068.4 6.44933 r 95.7 6.64593316.2 6.81863433.8 6.97593666.5 7.25893900.1 7.51224137 .l 7 .7 440 *4378.8 7.95934625 .7 B. l6 r 24878.0 8.35205135.7 8.53315398.2 8.7055

P : 8.0 MPa (295.06)

Sat. .032 44 2589.7 2784.3300 .036 lri 2667.2 2884.2350 .042 23 2789.6 3043.0400 .047 39 2892.9 3t77.2450 .05214 2988.9 3301.8500 .056 65 3082.2 3422.2550 .061 0r 3174.6 3540.6t600 .065 25 3266.9 3658.4.700 .07i1 52 3453.1 3894.2800 .081 60 3643. r 4132.7900 .089 58 3837.8 4375.3

1000 .097 49 4037.8 4622.11100 .105 36 4243.3 4875.4

5.8892 .027 376.0674 .029 476.3335 .035 246.5408 .039 936.7193 .044 166.8803 .048 147 .0288.. .05 I 95I.roI / .tr55 r)57.4234 .062 837.6566 .069 8 t7.8727 .076 698.0751 .083 508.266 r .090 27

5.8133 .023 525.9305 .024 266.2283 .029 956.4478 .034 326.6327 .038 17

6.7975 .04t 756.9486 .045 r ri7.0894 .048 ,{5

7.3476 .054 r.il7.5822 .060 1)7

7.7591 .067 028.0020 .073 0 r

8.1933 .078 96

2569.8 2 75 8.0 5.7 4322590.9 2785.0 5.79062747.7 2987.3 6.13012U63.8 3138.3 6.36342966.7 3272.0 6.555 r3064.3 3398.3 6.72403159.8 3521.0 6.8778!\254.4 3642.0 7.02063443.9 3882.4 7.28123636.0 4123.8 7.5r733832. l 4368.3 7.73514032.8 4616.9 7.93844238.6 4870.3 8.r300

2580.5 2772.r2632,2 2838.42769.4 3016.02878.6 3158.I2978.0 3287.r3073.4 3410.33167.2 3530.93260.7 3650.33448.5 3888.33639.5 4128.2383 5.0 437 r.84035.3 4619.84240.9 4872.8

Page 7: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1.3 (Continued)Superheated Vapor

7-

P : 6.0 MPa (275.64) P : 7.0 MPa (285.U8) P:8.0 MPa (295.06)

1200 .113 2l 4454.0 5133.3 8.4474r 300 . t 2 1 06 4669.6 5396.0 8.6199

P : 9.0 MPa (303.40)

.097 03 445r.7 5130.9 8.3747

.103 77 4667.3 5353.7 8.5473

P : 10.0 MPa (31 1.06)

.084 89 1449.5 5 128.5 8.31 15

.090 B0 4665.0 5391.5 8.4842

P - r2.5 MPa (327.89)

Sat. .020 48325 .023 27350 .025 80400 .029 93450 .033 50500 .036 77550 .039 87600 .042 85650 .045 74700 .048 57800 .054 09900 .059 50

r 000 .064 85I 100 .070 16r200 .075 441300 .080 72

2557 .B 27 42.r2646.6 2856.02724.4 2956.62848.4 31 17.82955.2 3256.63055.2 3386.13152.2 351 1.03248. l 3633.73343.6 3755.33439.3 3876.53632.5 4119.33829.2 4364.84030.3 4614.04236.3 1867.74447.2 5126.24662.7 5389.2

5.6772 .018 026 2544.4 2724.75.8712 .019 861 2610.4 2809.16.0361 .022 42 2699.2 2923.46.2854 .026 41 2832.4 3096,56.4844 .029 75 2943.4 3240.96.6576 .032 79 3045.8 3373.76.8142 .035 64 3144.6 3500.96.9589 .038 37 324t.7 3625.37.0943 .041 0r 3338.2 3748.27.2221 .043 58 3434.7 3870.57.4596 .048 59 3628.9 4rt4.87.6783 .053 49 3826.3 436r.27.882r .058 32 4027.8 4611.08.0740 .063 l2 4234.0 4865.18.2556 .067 89 4444.9 5123.88.4284 .072 65 4460.5 5387.0

5.6r4r .013 495 2505.1 2673.8 5.46245, / 5Crd

5.9443 .016 126 2624.6 2826.2 5.71l86.2120 .020 00 2789.3 3039.3 6.04176.4190 .022 99 2912.5 3199.8 6.27196.5966 .025 60 302r.7 3341 .8 6.461B6.7561 .028 0l 3125.0 3475.2 6.62906.9029 .030 29 3225.4 3604.0 6.78107.0398 .032 48 3324.4 3730.4 6.92187.1687 .034 60 3422.9 3855.3 7.05367.4077 .038 69 3620.0 4103.6 7.29657.6272 .042 61 3819.1 4352.5 7.51827.8315 .046 58 4021.6 4603.8 7.12378.0237 .050 4:5 4228.2 4858.8 7.91658.2055 .054 30 4439.3 5l I8.0 8.09878.3783 .058 t 3 4654.8 538 r.4 8.27 t7

1']: 15.0 MPa (342.24) P : 17.5 MPa (354.75) P:20.0 MPa (365.81)

Sat. .010 337 2455.5 2610.5350 .011 470 2520.4 2692.4400 .015 649 2740.7 2975.5450 .018 445 2879,5 3156.2500 .020 80 2996.6 3308.6550 .022 93 3104.7 3448.6600 .024 91 3208.6 3582.3650 .026 80 3310.3 37 t2.3700 .028 6r 3410.9 3840.1800 .032 10 3610.9 4092.4900 .035 46 3811.9 4343.8

1000 .038 75 1015.4 4596.61100 .042 00 4222.6 4852.6r 200 .04b 23 4433.8 5rr2.31300 .048 45 4649.1 5376.0

P :25.0 MPa

5.3098 .007 920 2390.2 2528.85.442r5.88 r 1 .0r2 447 2685.0 2902.96.1404 .0r5 174 2844.2 3109.76.3443 .017 358 2970.3 3274.16.5199 .019 288 3083.9 342r.46.6776 .021 06 3191.5 3560.16.8224 .022 74 3296.0 3693.96.9572 .024 34 3398.7 3824.67 .2040 .027 38 3601.8 4081.17 .4275 .030 3l 3804.7 4335.17.6348 .033 16 4009.3 4589.57.8283 .035 97 4216.9 4846.48.0108 .038 76 4428.3 5106.68.1840 .041 b4 4643.5 5370.5

5. r419 .005 834 2293.0 2409.7 4.9269

5.7213 .009 9426.0184 .012 6956.2383 .014 7686.4230 .016 5556.5866 .018 1786.7357 .0r9 6936.8736 .021 r 3

7.1244 .023 857.3507 .026 457.5589 .028 977 .7 53r .03 1 457.9360 .033 9l8.1093 .036 36

2619.3 2818. l 5.55402806.2 3060.1 5.90172542.9 3238.2 6. l40l3062.4 3393.5 6.33483 r 74.0 3537.6 6.5048328r.4 3675.3 6.65823386.4 3809.0 6.79933592.7 4069.7 7.0544*3797.5 4326.4 7.28304003.1 4582.5 7.492542r | .3 4840 .2 7 .687 44422.8 5r01.0 7.87074638.0 5365. r 8.0442

P :35.0 MPaP :30.0 MPa

375 .001 973 1

400 .006 004425 .007 88 r

450 .009 162500 .01 l 123550 .0r2 724600 .014 137650 .0t5 433700 .016 646800 .018 912900 .021 045

1000 .023 i 0ll00 .025 12

t798.7 1848.02430.1 2580.22609.2 2806.32720.7 2949.72884.3 3162.43017.5 3335.63137 .9 3491.43251.6 3637 .4

3361.3 3777.53574.3 4047.r3783.0 4309.13990.9 4568.54200.2 4828.2

4.0320 .001 789 25.1418 .002 7905.4723 .005 3035.6744 .006 7355.9592 .008 6786.1765 .010 1686.3602 .011 4466.5229 .012 5966.6707 .013 6616.9345 .015 6237.1680 .0r7 4487.3802 .019 1967.5765 .020 903

1737.8 179r.52067.4 2l5l.l2455.1 26r4.22619.3 2821.42820.7 3081.12970.3 3275.43 r 00.5 3443.93221.0 3598.933 35. B 37 45.63555.5 4024.23768.5 4291.93978.8 4554.74i89.2 4816.3

3.9305 .001 700 3

4.4728 .002 r 005.1504 .003 4285.4424 .004 96r5.7905 .006 9276.0342 .008 3456.2331 .009 5276.4058 .010 5756.5606 .0ii 5336.8332 .013 2787 .07 tB .0 14 BB37.2867 .016 4r07 .4845 .017 895

1762.4 3.87221987.6 4.21262373.4 4.77472672.4 5.19622994.4 5.628232 13.0 5.90263395.5 6. r 1793559.9 6.30 i 037 13.5 6.463 I400 r.5 6.74501274.9 6.9886454t.t 7 .20644804.6 7.4057

r702.9i 914. I2253.42498.727 51.9292 t.03062.03189.83309.83536.737 54.03966.74r78.3

Page 8: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1.3 (Continued)

Superheated VaPor

P:30.0 MPa P : 35,0 MPaP :25.0 MPa

1200 .027 rr1300 .029 10

4412.0 5089.9 7.1605 .022 589

4626.s 5354.4 7.9342 .024 266

P :40.0 MPa

4401.3 5079.0 7.6692 .0193604616.0 5344.0 7.8432 .020 815

P:50.0 MPa

4390.7 5068.3 7.59104605.1 5333.6 7.7653

P:60.0 MPa

375400425450500l)5u600650700800900

I 000I i00I 200I 300

IOi /. r

1854.62096.92365.12678.42869.73022.63158.03283.63517.83739.439b4.64167.44380. r

4594.3

.001 640 7

.001 907 7

.002 532

.003 693

.005 622

.006 984

.008 094

.009 063

.009 941

.01 1 523

.012 962

.014 324,0t5 642.016 940.018 229

1742.8 3.82901930.9 4.r1352198.1 4.50292512.8 4.94592903.3 5.47003149.r 5.77853346.4 6.01l43520.6 6.2054368 r.2 6.37503978.7 6.66624257.9 6.91504527 .6 7.13564793,r 7 .33645057.7 7.52245323.5 7.6969

.001 559 4

.00r 730 I

.002 007

.002 486

.003 892

.005 I l8

.006 I 12

.006 966

.007 727

.009 076

.010 283

.011 411

.012 496

.013 561

.014 616

.001 502 B

.001 633 5

.001 B16 5

.002 085

.002 956

.003 956

.004 834,005 595.0p6 272,007 459.008 508.009 480.010 409.01 1 317.012 215

1699.5 3.7 r4r1843.4 3.93182001.7 4.16262r79.0 4.412\2567.9 4.932r2896.2 5.344r3151.2 5.64523364.5 5.88293553.5 6.08243889. 1 6.4109419 r.5 6.68054475.2 6.91274748.6 7.1 195

50t7 .2 7.30835284.3 7.4837

r638.6 17 16.6 3.7639r7B8. r 1874.6 4.003.1959,7 2060.0 4.27342159.6 2284.0 4.58842525.5 2720.t 5.17262763.6 3019.5 5.54852942.0 3247 .6 5.81783093.5 3441.8 6.03423230.5 3616.8 6.21893479.8 3933.6 6.52903710.3 4224.4 6.78823930.5 450r.1 7.01464t45.7 4770.5 7.21844359.1 5037.2 7.40584572.8 5303.6 7.5808

1609.4t745.41892.72053.92390.62658.8286 l. I3028.83t77.23441.53681.03906.44124.14338.24551.4

Table A.1 .4Compressed Liquid

1':5N4Pa(263.99) P : l0 MPa (31 1.06) P: 15 MPa (342.24)

't

Sat. .00 I 285 90 .000 997 7

20 .000 999 540 .001 005 660 .001 014 !)

80 .001 026 8100 .001 041 0r20 .001 057 6r40 .001 076 8160 .001 098 B

r 80 .001 124 0200 .001 r53 0220 .001 186 6240 .001 226 4260 .001 274 I280300320340

1147.8 1t54.2.04 5.04

83.65 88.65166.95 17 L97250.23 255.30t\33.72 338.85417.52 422.72501.80 507.09586.76 592. l5672.62 678. r 2

759.63 765.25848.1 853.9938.4 944.4

t031.4 1037.5r 127.9 1134.3

2.9202 .00t 452 4.0001 .000 995 2.2956 .000 997 2.5705 .001 003 4.8285 .001 012 7

1.0720 .001 024 51.3030 .00r 038 51.5233 .001 054I1.7343 .00r 073 7t.9375 .001 095 32.1341 .001 119 92.3255 .001 148 02.5128 .001 180 5

2.6979 .001 218 7

2.8830 .001 264 5.001 321 6.001 397 2

1393.0 1407.6.09 10.04

83.36 93.33166.35 176.38249.36 259.49332.59 342.834t6.r2 426.50500.08 510.64584.68 595.42670.r3 681.08756.65 767.84844.5 856.0934.1 945.9

1026.0 1038. rll2l.l t133.71220.9 1234.11328.4 1342.3

3.3596 .001 658 I.0002 .000 992 8.2945 .000 995 0.5686 .001 001 3.8258 .001 010 5

1.0688 .001 022 2

1.2992 .001 036 I1.5189 .001 052 21.7292 .001 070 71.9317 .001 091 B

2.1275 .001 r15I2.3178 .001 r43 3

2.5039 .00r 174 8

2.6872 .001 2ll42.8699 .001 255 03.0548 .001 308 43.2469 .001 377 0

.001 472 4..001 631 1

1585.6 1610.5.15 15.05

83.06 97.99165.76 r 80.782 48.5 i 263.6733 r.48 346.814t4.7 4 430.28498.40 514.19582.66 598.72667.7r .684.09753.76 770.50841.0 858.2929.9 947.5

1020.8 r039.0il r4,6 1 133.4t212.5 1232.113 r 6.6 1337 .3t43t.1 1453.21567 .5 159 r.9

3.6848.0004.2934.5666 *.8232

1.0656t.2955t.5t45| 1r4,)1.92602.12r02.3t042.4953

4.677 r

4.85763.03933.2260z+2473.6546

Page 9: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.1.4 (Continued)

Compressed Liquid

P:20 MPa (365.81) P: 30 MPa P: 50 MPa

T

Sat. .002 0360 .000 990 4

20 .000 992 840 .000 999 260 .001 008 480 .001 019I

100 .001 033 7

r20 .001 049 6140 .001 067 8

160 .001088 5180 .001 I 12 0200 .001 138 8220 .001 169 3

240 .001 204 6260 .001 246 2

280 .001 296 5

300 .001 359 6320 .001 443 7

340 .001 568 4360 .00r 822 6380

1826.3 4.013920.01 .0004

102.62 .2923185.r6 .5646267.85 .8206350.80 l.0624434.06 r.29175r7 .7 6 1.5 102602 .04 | .7 r93687. r 2 1.9204773.20 2.1147860.5 2.3031949.3 2.4870

1040.0 2.66741133.5 2.84591230.6 3.02481333.3 3.20711444.6 3.39791571.0 3.60751739.3 3.8772

.25 29.8282.17 I I 1.84

164.04 193.89246.06 276.r9328.30 358.77410.78 44r.66493.59 524.93576.88 608.75660.82 693.28745.59 778.73831.4 865.39 18.3 953. I

1006.9 1042.61097.4 l 134.3l190.7 1229.01287.9 1327 .81390.7 1432.71501.7 1546.51626.6 167 5.4l 78 I .4 1837.5

.0001 .000 976 6

.2899 .000 980 4

.5607 .000 987 2

.8r54 .000 996 21.0561 .001 007 3

t.2844 .001 020 I1.5018 .001 034 8

1.7098 .001 051 5

1.9096 .001 070 3

2.1024 .001 091 2

2.2893 .001 I l4 62.47rr .001 140 8

2.6490 .001 170 2

2.8243 .001 203 42.9986 .001 241 5

3.r74r .001 286 03.3539 .001 338 8

3.5426 .001 403 23.7494 .001 483 84.0012 .001 588 4

.20 49.03 -.0014B 1.00 130.02 .2848

r61.86 211.21 .5527242.98 292.79 .8052324.34 374.70 1.0440405.88 456.89 r.2703487.65 539.39 r.4857569.77 622.35 1.6915652.4t 705.92 1.8891735.69 790.25 2.0794819.7 875.5 2.2634904.7 961.7 2.4419990.7 1049.2 2.6158

1078.r 1138.2 2.78601t67.2 1229.3 2.95371258.7 1323.0 3.12001353.3 1420.2 3.28681452.0 1522.r 3.45571556.0 r630.2 3.6291t667.2 1746.6 3.8101

1785.6.19

82.77I05.l /247.68330.40413.39496.76580.69tlb5.J57 50.95

837.7925.9

t 016.01108.6t204.7I 306.114t5.71539.71702.8

.000 985 6

.000 988 6

.000 995 l

.001 004 2

.001 015 6

.001 029 0

.001 044 5

.001 062 I

.001 082 1

.00r 104 7

.001 130 2

.00i 159 0

.001 192 0

.001 230 3

.00r 275 5

.001 330 4

.001 399 7

.001 492 0

.001 626 5

.001 869 I

Table A.1 .5Saturated Solid-Vapor

Specifrc Volume lnternal Energy Enthalpy Entropy

'lemp. Press. Sat. Sat.oC kPa Solid VaporT P ziX103 7)o

Sat. Sat.Subl. Vapor Solidltis 1ls hi

Sat. Sat.Subl. Vapor Solid Subl.

hin h! .f i ris

Sat.Solid

Ui

Sat.Vapor

J9

.0i .61 130 .6108

-2 ,5t76-4 .4375

-6 .3689

-8 .3102

- l0 .2602

-12 .2176* t4 . 1815* 16 . 1510

- 1B .1252-20 .1035*22 .0853

-24 .0701

-26 .057 4

-28 .0469

-30 .038I*32 .0309

-34 .0250

-36 .0201

-38 .0i61-40 .0 I 29

1.0908 206. I1.0908 206.31.0904 241.71.0901 283.81.0898 334.21.0894 394.4l.0891 466.71.0888 553.71.0884 658.81.088I 786.01.0878 940.51.0874 1 128.61 .0871 1358.41.0868 1640.11.0864 1986.4t.0861 2413.71.0858 29431.0854 36001.0851 44191.0848 54441.0844 6731r.0841 8354

-333.40-333.43-337.62-34t.7 B

-345.91-350.02-354.09-358.14-362.15-366. r4-370.10-374.03*377.93

-381.80-385.64-389.45-393.23-396.98-400.7 t

-404.40-408.06-4tt.70

27 08.7 237 5.32 7 08.8 237 5 .32710.2 2372.6271r.6 2369.82712.9 2367 .02714.2 2364.22715.5 2361.42716.8 2358.72718.0 2355.92719.2 2353.12720.4 2350.32721.6 2347.52722.7 2344.72723.7 2342.02724.8 2339.22725,8 2336.42726.8 2333.62727.8 2330.82728.7 2328.02725.6 2325.22730.5 2322.4273r.3 2319.6

-333.40-.) 3 J. a.l

-337.62*341.78

-345.91-350.02-354.09-358.14-362.r5-366.14*370. l0-374.03-377.93-381.80-385.64-389.45-393.23-396.98-400.7 |-404.40-408.06-4t 1.7 0

2834.8 2501.42834.8 250r.32835.3 2497.72835.7 2494.02836.2 2490.32836.6 2486.62837.0 2482.92837.3 2479.22837.6 2475.52837 .9 247 r.82838.2 2468.12838.4 2464.32838.6 2460.62838.7 2456.92838.9 2453.22839.0 244s.52839.0 2445,82839.1 2442,12839.1 2438.42839.1 2434.72839.0 2430.92838.9 2427,2

9.1 56Y.L5/9.219 *9.2839.3489.4149.4819.5509.6199.6909.7629.8359.9099.985

10.062i0.l4r10.22110.30310.386r0.470r 0.556t0.644

- 1.221

-1.221- 1 .237

- 1 .253

- r.268- 1.284

- 1 .299

- 1 .315

- 1.33 r

-1.346- 1.362

-t.377- 1.393* r.408* t.424- 1.439

- r.+55

-L47|- 1,486

- I .501* | .51 I

-1.532

10.37810.37810.45610.536r 0.61610.69810.781i 0.865r 0.950

r.036l. 123r.2r21.3021.394l.486r,580r.676t.t t3t.872r.972

r2.07312.176

Page 10: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.2Thermodynamic Properties of AmmoniauTable A.2.1Saturated Ammonia

Specific Volumem'/kg

EnthalpykJ/kg

EntropykJ/kg K

Temp.OC

Abs.Press.kPa

D

Sat.Liquid

a1

Evap.ule

Evap.L

Sat.Vapor

ho

Sat.Liquid

j,

Sat. Sat.Vapor Liquid

7)s ht

Sat.Evap. Vapor

sfs Js

-5r.J*48-46_A A

-al-40-38-JO-34*32-30-28-26*24-22-20-i8-16*14-12

40.8845.96J 1.555 i.b964.42

79.8088.5498.05

108.37I 19.55131.64144.7 0158.78r73.93190.22207 .7 |226.45246.5 i267.95

0.0010.0010.0010.0010.0010.0010.00 i0.0010.0010.0010.0010.0010.0010.00 i0.0010.0010.0010.0010.0010.001

424 2.6239 2.6254429 2.3518 2.3533434 2.1 126 2.rr40439 1.9018 1.9032444 1 .7 r55 r.7 t7 0449 1.5506 i.5521454 r.4043 i.4058460 |.2742 1.2757465 1 1582 l.1597470 1.0547 1.0562476 0.9621 0.9635481 0.8790 0.8805487 0.8044 0.8059492 0.7373 0.7388498 0.6768 0.6783504 0.6222 0.6237510 0.5728 0.57 43515 0.5280 0.529652r 0.4874 0.4889528 0.4505 0.4520

-44.3 t4t6.7-35.5 1411.3

-26.6 1405.8

- r 7.8 1400.3

-8.9 t394.70.0 i 389.08.9 1383.3

17.8 1377.626.8 1371.835.7 I 365.944.7 1360.053.6 1354.062.6 1347.97r.6 1341.880.7 1335.689.7 1329.398.8 1322.9

r07.8 1316.5l r6.9 13t0.0126.0 1303.5

1372.4 -0.1942r 375.8 -0.15471379.2 -0. I 1561382.5 -0.07681385.8 *0.03821389.0 0.00001392.2 0.03801395.4 0.07571398.5 0. I I321401.6 0.15041404.6 0.1873t407.6 0.22401410.5 0.2605r4r3.4 0.29671416.2 0.3327r419.0 0.3684t42r.7 0.40401424.4 0.43931427.0 0.47441429.5 0.5093

6.3502 6. l56l6.2696 6.1.1496. 1902 6.07466. I r20 6.03526.0349 5.99675.9589 5.95895.8840 5.92205.8101 5.88585.7372 5.85045.6652 5.81565.5942 5.78155.5241 5.748r5.4548 5.7 r535.3864 5.68315.3188 5.65155.2520 5.62055.1860 5.59005.1207 5.56005.0561 5.53054.9922 5.5015

-10-8-6-+-z

02

46B

l0l214t6t82022242628303234363B404244464850

r35.2144.3I CJ.5162.7171.9181.1190.4199.6208.9218.3227.6237.0246.4255.9265.4274.9284.4294.0303.63t3.2322.9332.6342.3352.1.

361.937 r.738 r.6391.5401.54rt.5421.7

r 296.8I 290. I1283.31276.4r 269.4t262.4t255.21248.0t240.61233.21225.71218. I1210.41202.6

1432.0r434.41436.81439.1r44t.3t443.51445.61447.61449.6145I.51453.31.t55. _t

1456.81458.51460.0146 l .5r 462.9t464.31465.61466.81467.9r469.01469.91470.8r47 t.51472.2r472.81473.2t+t.).5r47 3.7r473.7

290.853r5.2534r.25368.90358.27429.44462.49497.49534.5r5/.r.oat

, 614.95658.52704.44752.79803.66857.12913.27972.r9

i 033.971098.71r 166.491237.41t3I1.551389.031469.921554.331642.351734.091829.651929. i32032.62

0.001 5340.001 5400.001 5460.001 5530.001 5590.001 5660.001 5730.001 5800.001 5870.001 5940.001 6010.00 r 6080.00i 6160.001 6230.001 6310.001 6390.001 6470.001 6550.001 6630.001 6710,001 6800.001 6890.00 r 6980.001 7070.001 7160.00 r 7260.001 7350.001 745u.t)u I / 5r)0.001 7660.001 777

194.7186.7178.5170.3162.0153.6145.0136.4127.6118.7109.71 00.5

0.4169 0.41 850.3863 0.38780.3583 0.35990.3328 0.33430.3094 0.31090.2879 0.28950.2683 0,2698 ,0.2502 0.2517.0.2335 0.235IJ0.2182 0.21980.2040 0.20560.1910 0.19260.1789 0.18050 .167 7 0. I 6930.r574_- 0. r5900.1477 0.14940.1388 0. r4050. 1305 0.t3220.1228 0.12450.1 156 0.1 1730.1089 0.1 1060.1027 0.10440.0969 0.09860.0914 0.09310.0863 0.08800.08i5 0.08330.077 | 0.07880.0728 0.07460.0689 0.07070.0652 0.06690.0617 0.0635

0.5440 4.9290 5.47300.5785 4.8664 5.44490.6128 4.8045 5.4t730.6469 4.7432 5.39010.6808 4.6825 5.36330.7 r45 4.6223 5.33690.7481 4.5627 5.31080.7815 4.5037 5.28520.8 1 48 4.4451 5. 2 5 990.8479 4.387 | 5.23500.8808 4.3295 5.2 1040.9136 4.2725 5.18610.9463 4.2159 5. 16210.9788 4.1597 5. 13851.0112 4.1039 5.lr5lt.0434 4.0486 5.09201.0755 3.9937 5.06921.1075 3.9392 5.04671.1394 3.8850 5.02441.1711 3.8312 5.00231.2028 3.7777 4.9805r.2343 3.7246 4.95891.2656 3.6718 4.9374n2969 3.6192 4.91611.328 r 3.5669 4.89501.3591 3.5148 4.87401.3901 3.4630 4.85301.4209 3.4112 4.83221.4'518 3.3595 4.81 l31.4826 3.30',19 4.79051.5135 3.2561 4.7696

1091.2108 r .7r072.01062.21052.0

"Adapted from National Bureau of Standards Circular No. 142, TabLes of Therrnotlynamic Properties oJ Ammonta.

Page 11: Tabel Sifat-Sifat Thermodinamika Uap Air

Table 4.2.2Superheated Ammonia

Abs. Press.kPa

(S:rt. Temp.)OC

Temperature, oC

1008070605U403020IO-20 - 10

50(-46.54)

75(-3e. l8)

100(-33.61)

125(*29.08)

150(-25.23)

200(- 18.86)

250(-13.67)

300(*9.23)

2.4474 2.54811435.8 1457.06.3256 6.40771.6233 1.69151433.0 1454.76.1 190 6.2028l.2ll0 1.26311430.1 1452.25.9695 6.05520.9635 1.00591427.2 1449.85.85 r 2 5.93890.7984.0.83441424.1 1447.35.7526 5.8424

0.6199t442.05.68630.491 01436.65.5609

2.6482 2.7479t47B.l 1499.26.4865 6.56251.7591 r.82631476.r 1497.56.2828 6.3597r.314b 1.3654147 4.r 1495.76. r366 6.2144r.0476 1.0889t4'72.0 1493.96.0217 6. r 0060.8697 0.90451469.8 1492.15.9266 6.00660.647 | 0.67381465.5 1488.45.7737 5.85590.5135 0.53541461.0 t484.55.6517 5.73650.4243 0.4430i456.3 r480.65.5493 5.63660.3605 0.3770

2.8473 2.9464t520.4 154t.76.6360 6.70731.8932 r.95971518.9 1540.36.4339 6.50581.4160 r.4664r5r7.3 1538.96.2894 6.36181.1297 l . 1703l5_t5./ I5J/.J6.1763 6.24940.9388 0.97291514.1 1536. l6.0831 6.15680.700r 0.726r1510.9 1533.25.9342 6.00910.5568 0.5780r 507.6 1530.35.8165 5.89280.4613 0.4192t504.2 r527.45.7186 5.75630.3929 0.40B6

3.0453 3.14411563.0 1584.56.7766 6.844r2.0?61 2.09231561.8 1583.46.5756 6.64341.5165 1.56641560.5 1582.26.432t 6.50031.2107 1.2509r 559.3 1581. l6.3201 6.38871.0068 1.04051558.0 1580.06.2280 6.29700.75r9 0.77741555.5 t5t Lt6.0813 6.15120.5989 0.61961 5 5 2.9 r57 5.45.966 r 6.03680.4968 0.5 r431550.3 r573.05.8707 5.94230.4239 0.4391

3.2427 3.34 I 3

1606. r 1627.86.9099 6.97432. 1 584 2.22441605. 1 1626.96.7096 6.7742I .6 163 r .66591604. r 1626.06.5668 6.63161.2909 r.33091603.0 1625.06.4555 6.5206| .07 40 1 .r07 41602.0 t624,16.3641 6.42950.8029 0.82821599.9 1622.26.2189 6.28490.640 r 0.66051597.8 1620.36. 1052 6.r7170.53 r 6 0.54881595.7 16r8.46.01 r 4 6.07850.45,1I 0.4689

3.4397r649.77.03722.29031648.96.83731.7155 1.81451648.0 1692.66.6950 6.8177| .37 07 t .450 I1647 .2 l69l .B

o)se+z 6.70721.1408 1.20721646.3 l69l.l6.4933 6.61670.8533 0.90351644.6 1689.66.3491 6.47320.6809 0.72121642.8 1688.26.2365 6.36130.5658 0.5997r64l.r 1686.76.1437 6.26930.4837 0.5129

uhJ

uhs

ahJ

ah.t

uhJ

u

hJ

ah

u

h,

.t

1)

\.

350(*5.35)

400(- 1 .8e)

450(r.26)

h

s

uh.\

u

h

J

1451.5 147 6.55.4600 5.55020.3 1 25 0.327 4t146.5 \472.45.3803 5.47350.2752 0.2887t441.3 1468.I5.3078 5.4042

1500.7 1524.45.6342 5.7 t350.3417 0.35561497.2 1521.35.5597 5.64050.3017 0.31431493.6 1518.25.4926 5.5752

1547.6 1570.75.7890 5.86150.3692 0.38261544.9 1568.35.7 r73 5.79070.3266 0.33871542.2 1565.95.6532 5.7275

1593.6 1616.55.93 r 4 5.99900.3959 0.4090r591.r1 1614.55.8613 5.92960.3506 0.36241589.3 1612.65.7989 5.8678

r639.3 1685.26.0647 6. 19 t 00.4220 0.4478I 637.6 I 683.75.9957 6.12280.3740 0.39711635.8 1682.25.9345 6.0623

120 140 i60 180t008070605t,403020

7/

500 h(,1. 14) .'

7)

600 h(9.29) r

7/

70() h(13.81) .'

800( 17.86)

900(21.54)

1 000(24.9 l )

1 200(30.96)

uhJ

uL

.t

ah

J

uh.\

0.2698 0.28131489.9 1515.05.43t1 5.51570.2217 0.23\71482.4 1508.65.3222 5.41020. 187,1 0. 19631474.5 1501.95.2259 5.3 I 790.1615 0.16961466.3 1495.05.1387 5.2351

0.14881488.05. I 5930.13211480.65.0889

0.2926 0.3036 0.31441539.5 1563.4 1587. I5.5950 5 6704 r.7425t\.2414 u.2508 0.26001533.8 1558.5 1582.71t.4923 5.5697 5.64360.2048 0.2 l3 I 0.22121528. i t553.4 1578.25.4029 5.4826 5.558'.0.1773 0.1848 0.19201522.2 r548.3 1573.75.3232 5.4053 5.48270.1559t 0.t627 0. 1693rsr6.2 |543.0 I569.I5.2508 5.3354 5.4r470. 1388;,.0.t450 0. l5ll1510.0 1537 .7 1564.45.1840 5.2713 5.35250.il29 0.il85 0.12381497 .1 1526.6 1554.75.0629 5. 1560 5.2416

0.3251 0.3357i610.6 1634.05.8120 5.87930.269 r. 0.278 r1606.6 1630.45.7 t44 5.78260.229r 0.23691602.6 1626.85.6303 5.69970.199 l 0.20601598.6 1623.15.5562 5.62680.r7 57 0. l 820t594.4 1619.45.4897 5.56r40. r 570 0.16271590.3 1615.65.4292 5.50210.1289 0.13381581.7 1608.05.3215 5.3970

0.3565 0.3771r 680.7 17 27 .56.0079 6. I 30 I0.2951 0.3 130),677.7 1724.95.9129 6.03630.2522 0.26721674.6 1722.45.8316 5.95620.2196 0.23291671.6 1719.85.7 603 5.886 I

0.1942 0.20611668.5 17 17 .1

5.6968 5,82370.1739 0.18471665.4 17 r4.55.6352 5.76740.1434 0.15261659.2 r 709.25.5379 5.6687

0.3975| -a A a

6.24720.33021772.4ti.l54l .

0.282117 7 0.26.07,190.2459 0.25891768.0 1816.46.0057 6.12020.2 i 78 0.2294176tt.7 1814.45.9442 6.05940.1954 0.2058 0.2162t763.4 18 t 2.4 1861.75.BBB8 6.0047 6.1 1590.16r6 0.1705 0.1792r 758.9 1808.5 1858.25.79r9 5.9091 6.0214

Page 12: Tabel Sifat-Sifat Thermodinamika Uap Air

T able 4.2.2 (Conl.inued)Superheated Ammonia

Abs. Press.kPa

(Sat. Temp.)Temperature, "C

180r60r40r201008070605(.'403020

1400(36.28)

I 600(4 r .05)

1 800(45.39)

2000(4e.38)

uh

J

U

h.t

u

h.t

uh.t

0.0944 0.09951483.4 r515.14.9534 5.0530

0.08511502.94.95840.0739i 490.04.86930.0648r47 6.r4.7834

0.1042 0.10881544.7 1573.05.1434 5.22700.0895 0.09371534.4 1564.05.0543 5.14190.0781 0.08201523.5 1554.64.97 15 5.06350.0688 0.07251512.0 1544.94.8930 4.9902

0.1 132 0.12161600.2 1652.85.3053 5.45010.0977 0.1053r 592.3 1646.45.2232 5.37220.0856 0.09261584. l I639.85.1482 5.30i80.0760 0.08241575.6 r633.25.0786 5.237 |

0,1297 0.1376r 703.9 r7 54.3

25.5836 /5.70870.1 125 0.1 1951698.5 17 49.7

j.5084 5.6355'0.0992 0.10551693.1 t745.15.4409 5.56990.0885 0.0943r687.6 1740.45.3793 5.5104

0.1452 0.15281804.5 1854.75.8273 5.94060.1263 0.13301800.5 1851.25.7555 5.86990.1 1 l6 Q.lr771796.5 1847 .75.6914 5.80690.0999 0.10541792.4 1844.15.6333 5.7499

Table A.3Thermodynamic Properties of Freon-12 (Dichlorodifluoromethane)"Table A.3.1Saturated Freon-l2

Specific Volumem3/kg

EnthalpykJ/kg

EntlopykJ/kg K

Abs.Press-I'ernp. MPa.CP

Sat.Liquid

u!Evap.

als

Sat.Vapor

ltt

Sat.Liquid

htEvap.

h,,,

Sat.Vapor

h,,

Sat.Liquicl

.S1

Sat.Evap. Vapor

r f,l rs

-90 0.0028

-85 0.0042

-80 0.0062-7 5 0.0088

-70 0.0123

-65 0.0168

-60 0.0226

-55 0.0300

-50 0.0391

-45 0.0504

-40 0.0642

-35 0.0807

-30 0. i004-25 0.1237

-20 0.1509

-15 0.1826* l0 0.2 191

-5 0.26100 0.30865 0.3626

0.000 6080.000 6120.000 6170.000 6220.000 6270.000 6320.000 6370.000 6420.000 6480.000 6540.000 6590.000 6660.000 6720.000 6790.000 6850.000 6930.000 7000.000 7080.000 7160.000 724

4.4t4 9373.036 7042.137 7281.537 030r.126 6540.840 5340.637 2740.490 3580.382 4570.302 0290.241 2510.194 7320.r58 7030.130 4870.108 1620.090 3260.075 9460.064 2550.054 6730.046 761

4.115 5453.037 3 16

2.r38 3451.537 6511.127 2800.841 1660.637 9100.491 0000.383 1050.302 6820.24 r 9100.195 3980.159 3750.131 i660.108 8470.091 0l B

0.076 6460.064 9630.055 3890.047 485

-43.243*38.968

-34.688-30,401-26. 103

-2 1.793*17.469

-13. 129

-8.772-4.396-0.000

4.4168.854

13.31517.80022.3t226.85131.42036.02240.659

-0.2084-0. 1854*0. 1630

-0.141I-0.1 197*0.0987

-0.0782-0.058I-0.0384-0.0190-0.0000

0.01870.0371

' 0.0552. 0.0730

0.09060. l 0790. I 2500.14180. I 585

1.0352 0.82680.9970 0.8I l60.9609 0.79790.9266 0.78550.8940 0.77440.8630 0.76430.83 34 0.7 5520.8051 0.74700.7779 0.73960.75 r 9 0.73290.7269 0.72690.7027 0.72140.6795 0.71650.6570 0.7 r2r0.6352 0.70820.6141 0.70460.5936 0.70140.5736 0.69860.5542 0.69600.535 r 0.6937

r 89.6 I B 146.37 5

187.608 I 48.640185.6 r 2 150.9?4183.625 r53.224r81.640 155.536179.651 157 .857177 .653 160. I 84t75.641 162.512r73.611 164.840171.558 r67.r63t69.479 169.479167.368 r7 r.784165.222 r74.076r63.037 176.352160.810 178.610158.534 180.846156.207 l83.058153.823 185.243151.376 187.397148.859 189.518

Page 13: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.3.1 (Continued)

Specific Volumern3/kg

E,nthalpyk ]/ks

Entr'opykf/ks K

Abs.Pless'fernp. MPa

"CP

Sat.t.iquicl

UJ

Evaptfs

Sat.Vapor

Tt

Sat.Liquid

hlEvap.

hr,,

Sat.Vapor

h,r

Sat..

LiquidSat.

Evap. Vaporsrq Jq

l0 0.4233r5 0.491420 0.567325 0.65 r 630 0.7 4493 5 0.847 740 0.960745 1.084y50 1.2 I 9355 1.366360 1.525965 1.698870 i.88587 5 2.087 4B0 2.304685 2:538090 2.788595 3.0569t00 3.3140

0.000 733

0.000 7430.000 7520.000 7630.000 7740.000 7860.000 7980.000 81 I0.000 8260.000 8.11

0.000 8580.000 8770.000 8970.000 9200.000 9460.000 9760.00 i 0120.001 0560.001 I 13

0.040 1800.034 67 r0.030 0280.026 09 r0.022 7340.0i9 8550.017 3730.015 2200.0r3 3440.01 1 7010.010 2530.008 97 i0.007 8280.006 8020.005 8750.005 0290.004 2460.003 5080.002 790

t46.265 191.60?143.586 193.644140.812 195.641r37 .933 197.586134.936 199.475t 3 1.805 201.299128.525 203.05 t125.074 204.722121.430 .-f0o.zsel l 7.565 207 .7 66113.443 209.109r09.024 2r0.303104.255 2l 1.32199.068 212.12693.373 212.66587.047 212.86579.907 212.6147 r.658 211.7266 r.768 209.843

0.040 914 45.3370 035 413 50.0580.030 780 54.8280.026 854 59.6530.023 508 64.5390.020 641 69.4940.018 l7l 7 4.5270.016 032 79.6470.014 170 84.8680.012 542 90.2010.011111 95.6650.009 847 I01.2790.008 725 107.0670.007 723 I13,0580.006 82r 1t9.2910.006 005 I 25.8180.005 258 132.7080.004 563 140.0680.003 903 I48.076

0.1750 0.5165 0.69160. r 914 0.4983 0.68970.2076 0.4803 0:68790.2237 0.4626 0.68630.2397 0.4451 0.68480.2557 0.4277 0.68340.27 16 0.4104 0.68200.2875 0.3931 "0.68060.3 034 0.3 758 0.67920.3194 0.3582 0.67770.3355 0.3405 0.67600.35 I8 0.:\224 0.67420.3683 0.3038 0.67210.3851 0.2845 0.66970.4023 0.2644 0.66670.420 I 0.2430 0.663 1

0.4385 0.r20() 0.65850.4579 0.1946 0.65260.4788 0. r 655 0.6444

t05t10t12

3.6509 0.001 1973.9784 0.001 3644. I 155 0.001 792

0.002 045 0.003 2420.001 098 0.002 4620.000 005 0.001 797

49.014 206.09928.425 196.4840.151 175.07r

0. I 296 0.63 l90.07 42 0.60640.0004 0.5655

I 5 /.Ud5168.05917 4.920

0.50230.53220.5651

',Copyright 1955 and 1956, E. I. du Pont de Nemours & Conrpany, Inc. Reprinted by pernlission. Adapted f rrrrn linglish unit.s

Page 14: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.3.2Suoerheated Freon-12

'I"emp..C

um,r/kg

hkJ/kg

s

kJ/kg Ku

m'/kgh

kJ/kgJ

kJikg Ka

m3/kghs

kJ/kg kf/kg K

0.05 MPa 0.10 MPa 0.15 MPa

-20.0 0.341 857

- 10.0 0.3s6 2270.0 0.370 508

10.0 0.384 71620.0 0.398 86330.0 0.412 95940,0 0.427 0r250.0 0.441 03060.0 0.455 0r770.0 0.468 97880.0 0.482 91790.0 0.496 838

181.042rt1r). t 5 /192.567198.471204.469210.5572r6.733222.997229.344235.77 4242.282248.868

0.20 MPa

0.79).20.81330.83500.85620.87700.89740.91750.93720.95650.97550.99421.0126

0.167 70r0.175 2220.182 6470.189 9940.197 2770.204 5060.211 6910.218 8390.225 9550.233 0440.240 I 11

0.247 r59

179.861r 85.707l9 I .628r 97.628203.707209.8662r6.t04222.42r228.815235.285241.829248.446

0.25 MPa

0.740r0.7628 0. l 14 7 160.7849 0.119 8660.8064 0.124 9320.8275 0.129 9300.8482 0.134 8730.8684 0.139 7680.8883 '0.144 6250.9078 0.149 4500.9269 0.154 2470.9457 0.159 0200.9642 0.163 774

r84.6r9 0.7318190.660 0.7543r96.762 0.7763202.927 0.7977209.160 0.8186215.463 0.8390221.83tt 0.8591228.277 0.8787234.789 0.898024r.37 | 0.9169248.020 0.9354

0.30 MPa

0.010.020.030.040.050.060.070.080.0

189.669195.878202.135208.4462r4.Br422r.243227.735234.291240.910

0.088 6080.092 5500.096 4180.100 2280.103 9890.107 710

0.7320 0.069 7520.7543 0.073 0240.7760 0.076 2180.7972 0.079 3500.8 r 78 0.082 43 I0.8381 0.085 4700.8578 0.088 4740.8772 0.091 4490.8962 0.094 398

188.644 0.7139r94.969 0.7366201.322 0.7587207 .7 15 0.7801214.153 0.80 t 0220.642 0.82 r4227.r85 0.U4 r 3

233.785 0.8608240.443 0.8800

0.057 1500.059 9840.062 7340.065 4180.068 0490.070 6350.073 r 850.07 5 7.050.07B 200

r 87.583 0.6984194.034 0.7216200.490 0.7 440206.969 0.7658213.480 0.7869220.030 0.8075226.627 0.8276233.273 0.8473239.97 | 0.8665

0.ur 3970.1 t5 0550.1 1 8 690

90.0 0.r22 304100.0 0. 125 901l 10.0 0. 129 483

247.593254.339261.147

0.40 MPa

0.89870.91710.9352

0.9 1 49 0 .097 327 247 .1600.9332 0.100 238 253.9360.9512 0.103 134 260.770

0.50 MPa

0.080 673 246.723 0.88530.083 127 253.530 0.90380.085 566 260.391 0.9220

0.60 MPa

20.0 0.045 83630.0 0.047 97140.0 0.050 04650.0 0.052 07260.0 0.054 05970.0 0.056 01480.0 0.057 94190.0 0.059 846

100.0 0.061 731r 10.0 0.063 600120.0 0.065 455130.0 0.067 298

0.7 r 99 0.035 6460.7423 0.037 4640.7639 0.039 2140.7849 0.040 91i0.8054 0.042 5650.8253 0.044 1840.8448 0.045 7740.8638 0.047 3400.8825 0.048 8860.9008 0.050 4150.9187 0.051 9290.9364 0.053 430

202.1 16 0.7063209. i54 0.7291216. 14 r 0.751 I223.104 0.7723 "230.062 0.7929237 .027 0.8129244.009 0.8324251.016 0.8514258.053 0.8700265"124 0.8882272.231 0.9061

0.90 MPa

I 98.762205.4282 I 2.0952t8.779225.488232.230239.012245.837252.707259.624266.590273.605

0.70 MPa

196.935203.8142 10.656217.484224.31523l.l6l238.031244.932251.869258.845265.862272.923

0.80 MPa

0.69990.72300.74520.76670.787 50.80770.82750.84670.86560.88400.90210.9 198

0.030 4220.031 9660.033 4500.034 8870.036 2850.037 6530.038 9950.040 3160.041 6190.042 9070.044 181

40.0 0.026 76150.0 0.028 10060.0 0.029 38770.0 0.030 63280.0 0.031 84390,0 0.033 027

100.0 0.034 189I 10.0 0.035 332120.0 0.036 458130.0 0.037 572140.0 0.038 673r 50.0 0.039 764

0.022 8300.024 0680.025 2470.026 3800.027 4770.028 5450.029 5BB0.030 6120.031 6190.032 6120.033 5920.034 563

0.019 7440.020 9120.022 0 r 20.023 0620.024 0720.025 0510.026 0050.026 9370.027 8510.028 7510.029 6390.030 515

204.t70 0.698221,r.765 0.71312r9.2r2 0.7358226.564 0.7575233.856 0.7 7 8524r.r13 0.7987248.355 0.8184255.593 0.8376262.839 0.8562270.100 0.8745277.38r 0.8923284.687 0.9098

,N

207.580214.745221.854228.931235.997243.066250.146257.247264.37 427 r.531278.720285.946

0.71480.73730.75900.77990.80020.8 I 990.83920.85790.87630.89430.91l90.9292

205.9242t3.290220.558227.766234.94r242.t01944 160256.428263.61 3

270.820278.055285.320

0.70160.72480.7 4690.76820.78880.80880.82830.84720.86570.88380.90 r 60.9 189

Page 15: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.3.2 (Continued)Suoerheated Freon-12

'fernp.C

u

m'/kgh

kJ/kg5

kJ/kg Ku

m'/kgh

k |/kg.t

kJ/kg KU

rn'r/kgi.r

kJ/kg \l/t<g x

1.00 MPa 1.20 MPa l 40 MPa

50.0 0.018 36660.0 0.019 41070.0 0.020 39780.0 0.021 34190.0 0.022 251

100.0 0.023 133I 10.0 0.023 993120.0 0.024 835r 30.0 0.025 661140.0 0.026 474i50.0 0.027 2751ii0.0 0.028 068

210. i62 0.70212 r 7.8 10 0.7254225.3r9 0.7 47 6

232.739 0.7689240.101 0.7895247.430 0.8094254.7 43 0.8287262,053 0.8475269.369 0.8659276.69s 0.8839284.047 0.901529t.4lS 0.9187

1.60 MPa

206.661 0.6812214.805 0.7060222.687 0.7293230.398 0.7 514237.995 0.7727245.518 0.7931252.993 0.8129260.44r 0.8320267.875 0.850727 5.307 0.8689282.745 0.8867290.195 0.9041

1.80 MPa

21r.457 0.6876219.822 0.7 r23227.89r 0.7355235.766 0.7575243.5r2 0.778525 1.170 0.7988258.77 0 0.8183266.334 0.8373273.877 0.8558281 .4 n 0.8738288.946 0.8914

2.00 MP:t

0.014 4830.015 4630.016 3680.0t7 2210.018 0320.018 8120.019 5670.020 3010.021 0180.02t 7210.022 4r20.023 093

0.012 5790.013 4480.014 2470.014 9970.015 7100.016 3930.017 0530.017 6950.018 3210.018 9340.019 535

70.0 0.01 I 20880.0 0.01 I 98490.0 0.012 698100.0 0.013 366r 10.0 0.014 000120.0 0.014 608130.0 0.015 195140.0 0.015 765r 50.0 0.016 320

216.650 0.6959225.r77 0.7204233.390 0.743324r.397 0.7651249.264 0.7859257.035 0.8059264.742 0.8253272.406 0.8440280.044 0.8623

218.859 0.6909228.056 0.71662 36.760 0.7 402245.r54 0.7 624253.34r 0.7835261.384 0.8037269.327 0.8232277.20t 0.8420

0.009 4060.010 i870.010 8840.011 5260.012 1260.012 6970.013 2440.0r3 7720.014 284

2r3.049222.).98230.835239. I 55247.264255.228263.094270.891278.642

0.67940.70570.72980.75240.77390.79440.81410.83320.85 t 8

0.008 7040.009 4060.010 0350.010 6150.01 1 1590.011 6760.012 1720.0r2 651

160.0 0.016 864170.9 0.017 398l80.0 0.017 923

287.669295.290302.9r4

2.50 MPa

0.8801 0.014 7840.8975 0.0r5 2720.9145 0.0r5 752

0.8698 0.013 I t60.8874 0.013 5700.9046 0.0r4 013

285.027 0.8603292.822 0.8781300.598 0.8955

3.50 MPa

286.364294.06930r .7 67

3.00 MPa

90.0 0.006 595100.0 0.007 2641 r0.0 0.007 837120.0 0.008 351130.0 0.008 827140.0 0.009 273150.0 0.009 697160.0 0.0i0 104170.0 0.010 497180.0 0.010 879190.0 0.01 l 250200.0 0.01 r 614

219.562229.852239.27 |248.192256.794265. r 80273.1142B 1.540289,589297.583305.540313.472

4.00 MPa

0.68230.7103 0.005 2310.7352 0.005 8860.7582 0.006 4190.7798 0.006 8870.8003 0.007 3130.8200 0.007 7090.8390 0.008 0830.857 4 0.008 4390.87 52 0.008 7820.8926 0.009 1140.9095 0.009 436

0.67700.7075 0.0013240.7336 0.004 9590.7573 0.005 4560.7793 0.005 8840.8001 0.006 ?700.8200 0.006 6260.8391 0.006 9610.8575 0.007 2790.8753 0.007 5840.8927 0.007 878

222.t21 0.6750234.875 0.7078245.66t 0.7349255.524 0.7591264.846 0.7814273.817 0.8023282.545 0.8222291.100 0.8413299.528 0.85973 07. il64 0.877 5

220.529232.068242.208251.632260.620269.3 I I277.8r7286.r71294.422302.597310.718

r 20.0 0.003 736130.0 0.004 325140.0 0.004 781150.0 0.005 172160.0 0.005 522170.0 0.005 845r80.0 0.006 147190.0 0.006 434200.0 0.006 7082 r 0.0 0.006 972220.0 0.007 228230.0 0.007 477

224.863 0.677 r

238.443 0.7i11249.703 0.7386259.904 0.7630269.492 0.7854278.684 0.8063287.602 0.8262296.326 0.8453304.906 0.8636313.380 0.8813321 .77 4 0.8985330.108 0.9152

Page 16: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.4Thermodynamic Properties of Oxygen'Table A.4.1Saturated Oxygen

Speci{ic Volumems/kg

EnthalpykJ/kg

Enropyk|/kg K

TempK

Press.MPa

P

Sat.Liquid

a1

Evap,uts

Sat.Vapor

us

Sat.Liquid

hlEvap

hts

Sat. Sat.Vapor Liquid

h,, J1

Sat'Evap. Vapor

.l.rs se

54.3507 0.0001560 0.0007370 0.0062380 0.0300690 0.09943

100 0.25425110 0.54339120 I .0215130 r.7478140 2.7866150 4.2190

154.57 6 5.0427

0.000 7650.000 7800.000 8080.000 8400.000 8760.000 9170.000 9660.001 0270.001 i 080.00 i 2300.001 4800.002 293

92.96582r.3461

2.90850.681 040.226 490.094 6450.045 8550.024 3360.013 4880.007 3390.003 1800.000 000

92.96662r.3469

2.90930.68I 880.227 360.095 5620.046 8210.025 3630.014 5960.008 5690.004 6600.002 293

-193.432- 184.029-167.372- 150.646

- 133.758

- r 1o.55 /

-98.829-80.219-60.093-37.045-7.03832.257

242.553 49.l2 I238.265 54.236230.527 63. I 55

222.289 7 r.6432t3A70 79.3r2202.291 85.734189.320 90.491173.310 93.091152.887 92.794125.051 88.00679.459 72.4210.000 32.257

2.0938 4.4514 6.54522.2585 3.9686 6.227 |2.5r51 3.2936 5.80872.7 382 2.7 7 79 5.5 l6 I2.9364 2.3663 5.30273.ll6r 2.0222 5.13833.2823 1.7 210 5.00333.440t 1.4445 4.88463.5948 1.1766 4.77143.7567 0.8935 4.65023.9498 0.5301 4.47994.1977 0.0000 4.1977

,'Adapted frorn L. A. Weber,rlc,zrnaL of Research oJ the National Bureau of Standard's,74Az 93 (1970).

Table A.4.2Superheated Oxygen

Temp. IK m'/kg

hkJ/kg

J

kJ/kg Ka

m3/kgh

kJ/kgJ

kJ/kg Ku

m'/kghs

kJ/kg kJ/kg K

0.10 MPa 0.20 MPa 0.50 MPa

100r25150r t5200225250275300

r25150I t5200225250275300

5.20835.424r5.5V+ I5. t 5lo5.86095.96886.06576. l 5606.2332

0.253 5030.320 7170.386 9140.452 6450.518 1270.583 4650.648 7l I0.713 8950.779 036

88.828r12.2r4135.301158.255181.r45204.007226.869249.769272.720

1.00 MPa

86.864l 10.988134.440157.609180.638203.596226.529249.483272.475

2.00 MPa

0.060 6740.075 0390.088 8420.102 3710.1 l5 7460.129 0250.142 2420.155 415

5.4016 0.123 3945.6107 0.158 2685.7787 0. r92 0165.9202 0.225 2766.0427 0.258 2826.1502 0.291 1406.2468 0.323 9066.3369 0.356 6106.4140 0.389 271

I 07.093 5. 1650131.788 5.3448155.643 5.4919l 79. I 05 5.6 175202.359 5.7268225.506 5.8246248.62t 5.9 r 5627 r..740 5.9932

4.00 MPa

0.027 8690.035 9760.043 3410.050 3940.057 2820.064 0680.070 7900.077 467

99.653r27.t12r52.269176.508200.280223.795247.185270.516

4.94315.t433 0.016 2705.2986 0.020 5445.4283 0.024 3955.540 r 0.02& 0515.6394 0.031 5975.7314 0.035 0735.8098 0.038 502

116.476 4.9130145. l l2 5.0899171.150 5.2293196.052 5.3464220.348 5.449r244.309 5.5433268.076 5.6263

81.48 r 4.5475128.61 8 4.8414159.715 5.0080187.333 5. r380213.37 4 5.2480238.560 5.3469263.234 5.4300

0.005 5260.009 0290.01 l 3760.013 4440.015 3780.0 r 7 2330.0 l9 039

Page 17: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.4.2 (Continued)Superheated Oxygen

'fernp,K

u

rn3/kgh

kJ/kgJ

kJ/ks K'(.)

m'/kBh

kJ/kgJ

kJ/kg Ku

mir/kghs

kJ/ks kJikg K

6.00 MPa 8.00 MPa 10.00 MPa

I t5200225250zl5300

r75200225250z/5300

0.005 0510.007 0270.008 5890.009 9910.01 I 3060.012 570

107.496147.232178.304206.340232.848258.464

20.00 MPa

0.003 0020.004 8640.006 l8l0.007 3160.008 3600.009 351

79.5r3 4.4384r 33.760 4.7308169.069 4.8973199.317 5.0251227.2r9 5.1344253.797 5.2240

0.002 0200.003 6030.004 7570.005 7300.006 6060.007 432

52.66 r 4.2573119 .7 67 4.6 189159.686 4.8072192.401 4.9455221.685 5.0572249.262 5. I 533

4,643r4.85655.00295.12145.22535.3 I l6

0.00 r 3430.00r 7270.002 2360.002 7550.003 2410.003 700

24.551 4.008675.318 4.2798

122.595 4.5024163.109 4.6739198.021 4.8069229.655 4.917 4

Table A.5Thermodynamic Properties of N itrogen.Table A.5.1Saturated Nitrogen

Specific Volumem'/kg

EnthalpykJ/kg

EntropykJ/kg K

'fempK

Press.MPa

D

Sat.Liquid

U1

Evap.Ufu

Sat.Vapor

us

Sat.Liquid

hrEvap.

hto

Sat. Sat.Vapor Liquid Evap.

ho ii .16

Sat.Vapor

63. r43 0.0125365 0.0174270 0.038587 5 0.0761 2

77 .347 0. 101325B0 0.1 37085 0.229190 0.360895 0.541 l

100 0.7 790r 05 1.0843l l0 1.4673I 15 1.9395120 2.5135r 25 3.2079

I 26. 1 3.4000

0.001 1520.001 1620.001 l 890.00 r ?210.001 2370.001 2560.00 i 2960.00 i 3400.001 3920.001 4520.001 5240.001 6130.001 7970.001 9040.002 3230.003 184

r.480 0601.093 r 730.525 7850.280 9700.215 5040.162 7940.100 4340.064 9500.043 5040.029 8610.020 7450.014 4020.009 6960.006 1300.002 5680.000 000

r.481 2121.094 3350.526 9740.282 l9l0.216 74r0.r64 0500.10r 7300.066 2900.044 8960.031 3130.022 2690.0 r 6 0150.011 4930.008 0340.004 8910.003 I 84

- 150.348

- r 46.691

- 136.569

-126.287- t21.433- r 15.926

- r05.461

-94.817-83.895-7 2.571

-60.691*48.027

-34.t57- 18.017+6.202

+30.791

215.188 64.8402t3.29t 66.600207 .727 7l . l5820 l .662 7 5.37 5r98.645 77.2r2195.089 79. t63r 87.892 82.43 r

r79.894 85.077r70.877 86.982160.562 87.991r48.573 87.882134.319 86.292l16.701 82.54493.092 75.07550. r 14 56.3 t 60.000 30.791

2.4310 3.4076 5.83862.4845 3.2849 5.76942.6345 2.9703 5.60482.7755 2.69 t5 5.46702.8390 2.5706 5.40962.9083 2.4409 5.34923.0339 2.2122 5.246r3. r535 2.0001 5.15363.2688 1.7995 5.06833.38 l6 I .6060 4.98763.4930 I .4150 4.90803.6054 r.2209 4.82633.7214 l.0145 4.73593.8450 0.7803 4.62534.0356 0.3989 4.43454.2269 0.0000 4.2269

Properties of Nitrogen IncludingR. Stewart, Jour. oJ Phys. and Chem.

Liquid and Vapor Phases liom 63 l( to 2000 I( with pressures toRef. Data,21 757-922 (1973).

"Adapted from "Thermodynamic10,000 Bar'," R. 'f. Jacobsen and R.

Page 18: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.5.2Superheated Nitrogen

7)

rn3/kgh

kJ/kg.t

kJ/ks Ku

m3/kgh

kJ/kg.t

kJ/kg Ku

mt'/kghs

kf/ks kf/kg KI-ernpK

0. 1 MPa 0.2 MPa 0.5 MPa

100i25i50| /5200225250275300

r25150ll3

200225250275300

0.290 9780.367 2170.442 6 l90.5 r 7 5760.592 2880.666 5520.7413750.815 5630.890 205

r 01 .965128.505ts4.7 7I180.935207.029233.085259.122285.144311.158

1.0 MPa

0.055 5200.073 4220.090 1500.106 3940.122 3940.138 1730.154 0060.169 6420.185 346

5.6944 0.142 4755.93 13 0.181 71 1

6.1228 0.220 0146.2841 0.257 8906.4234 0.295 5316.5460 0.332 8416.6561 0.370 4186.7550 , 0.407 619 )6.8457 0.445 047

100.209 5.47 67t27 .37 | 5.7 194153.962 5.9 r 32r80.314 6.0760206.537 6.2160232.690 6.3388258.796 - 6.449r.284.876 ) 6.5485310.937 6.6393

2.0 MPa

94.345 5. 1706I23.824 5.4343151 .470 5.6361t78.434 5.8025205.063 5.944723r.459 6.0690257 .828 6. I B0l284.076 6.28003 r 0.273 6.37 15

4.0 MPa

0.033 0650.041 8840.050 i 250.058 0960.065 8750.073 6340.08I 2600.088 899

117.422141 .176I I 5.155202.596229.526256.220282.720309. i 73

5.18725.40425.57795.12375.85025.96326.06396. I 563

0.014 02r0.019 5460.024 1550.028 4360.035 6970.036 5570.040 4850.044 398

101.489137.9 l6168.709197.609225.578253.032280. r 32307.014

4.88785.15475.34495.49925.63095.74695.850 r

5.9436

0.008 2340.01 l 1860.013 6480.0 r 5 8940.018 0600.020 1330.022 r 78

l t 5.7 l6 4.8384154.85 r 5.0804187.52t 5.25532r7.757 5.3976246.793 5.5202275.056 5.6277302.848 5.7248

6.0 MPa 8,0 MPA 10.0 MPa

150rt5200225250275300

150ttD200225250275300

0.004 4130.006 9130.008 7720.010 3960.01 1 9340.013 3830.014 800

0.002 9r70.004 8630.006 3900.007 69 r0.008 9030.010 0340.0r I 133

6 r.903r25.536167.680202.867235.141265.676295.2r9

20.0 MPa

4.35 r 84.74704.97265. I 3845.27505.39105.4942

0.002 3880.003 7500.005 0160.006 r040.007 r 12

0.008 0460.008 950

87.090 4.5667140.183 4.8966177 .447 5.0961210. 139 5.2410240.806 5.3796270.222 5.4917298.907 5.5916

15.0 MPa

48.687 4.2287112.489 4.6239158.578 4.8709196.079 5.0474229.861 5.190026 I .450 5.3 103291.800 5.4163

0.001 9560.002 6030.003 3690.004 1060.004 8080.005 4610.006 091

36.922 4.079892.284 4.4213

140.886 4.6813182.034 4.8752218.710 5.0303252.465 5.1845284.523 5.2707

0.001 7810.002 r 860.002 6850.003 2080.003 7280.004 2230.004 704

33.63783.453

130.291172.3072 10.456245.640278.942

3.99564.3029+.55.1C+-/5lL4.9r27b.04675. l 629

Page 19: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.6Thermodynamic Properties of Saturated Mercurv"

Enthalpy, kJ/kg Entropy, kJ/kg K

Table A.6 (Continued)Thermodynamic Properties of Saturated Mercurv"

FG';g

;:l

i

Press., Temp., Sat.MPa oC Liquid Evap.

Sat. Sat. Sat.Vapor Liquid Evap. Vapor

SpecificVolume

Sat. Vapor,m3/kg Press.,

MPa

SpecificVolume

Sat. Vapor,m3/kg

Sat.Vapor

Enthalpy, kJikg Entropy, kJikg K

0.000 060.000 070.000 080.000 090.000 l00.00020.00040.00060.00080.00100.0020.0040.0060.0080.0100.020.040.060.080.10.20.30.40.50.60.70.80.91.0t.21.41.61.82.02.22.42.62.83.0J.54.0

109.2 3r2.33312.69313.02313.31313.58315.38317.33318.543r9.43320. l6322.5r325.07326.70327.9r328.87332.07JJ3.04337.9r339.62341.00345.64348.65350.92352.78354.37355.74356.98358. I 0359. I I360.94362.55364.04365.28366.47367.59368.62369.59370.5037 r.36J l a..t /J/5.tt)

259.6994 c,

r97.7176.8160. l83.1843.2929.5722.5718.319.57 05.0133.4382.6322.r40l. 1280.59420.41 130.31630.258I0.r3770.095 5 t

0.073 780.060 ,14

0.051 370.044 790.039 780.035 840.032 660.027 B I

0.024 290.021 6 r

0.019 490.0r7 780.016 370.015 l80.0r4 l60.0i3 290.012 520.010 960.009 78

r2.315.0r I .319.7

t34.9151.5161.8169.4r I t.5195.62r7.723r.6242.0250.3278.1309.1329.0343.9J5r). I

397.r423.8444.1460.7474.9487.3498.4508.5Jr /.d534.4549.0562.0574.0584.9595.1604.6613.5622.0630.0648.5665. r

Temp., Sat."C Liquid Evap.

Sat. Sat.Vapor Liquid Evap15.13 297.20

15.55 297.r415.93 257.0916.27 297.04i6.58 297.00t8.67 296.7120.93 296.4022.33 296.2r23.37 296.0624.21 295.9526.94 295.5?29.92 295.r531.81 294.8933.21 294.7034.33 294.5438.05 294.0242.21 293.4344.85 293.0646.84 292.7848.45 292.5553.87 29r.7757.38 291.2760.03 290.8962.20 290.5864.06 290.3r65.66 290.0867.rr 289.8768.42 289.6869.6r 289.5071.7 5 289. l973.63 288.9275.37 288.6776.83 288.4578.23 288.2479.54 288.0580.7 5 287 .878r.89 287.7082.96 287.5483.97 287.3986.33 287.0488.43 286.73

0.0466 0.7774 0.8240p.0477 0.7709 0.81860.0487 0.7654 0.814t0.0496 0.7604 0.8r000.0503 0.7560 0.80630.0556 0.727r 0.78270.06r0 0.6981 0.75910.0643 0.681 I 0.74540.0666 0.6690 0.73560.0685 0.6596 0.72810.0744 0.6305 0.70490.0806 0.6013 0.68190.0843 0.5842 0.66850.0870 0.5721 0.65910.0892 0.5627 0.65190.0961 0.5334 0.62950.1034 0.5039 0.60730.1078 0.4869 0.59470.1I l0 0.4745 0.58550. l l 36 0.4649 0.5 7850.i2t8 0.4353 0.55710.1?68 0.4t79 0.54470.1305 0.4056 0.53610.1334 0.3960 0.52940.1359 0.3881 0.52400.1380 0.3815 0.51950. t398 o.3757 0.51550.1415 0.3706 0.512t0.1429 0.3660 0.50890.1455 0.3581 0.50360.r478 0.3514 0.49920.1498 0.3456 0.49540.1515 0.3405 0.49200. r 53 l 0.3359 0.48900. r 546 0.331B 0.48640. r 559 0.3280 0.48390.t571 0.3245 0.48160. r 583 0.32 t2 0.47950. t594 0.3182 0.47760.I6 t9 0.:J 1 i5 0.47340.1641 0.3056 0.1657

4.55.05.56.0o.57.0t.3

680.3 90.35 286.44694.4 92.r I 286.18707.4 93.76 285.93719.7 95.30 285.7073r.3 96.75 285.48742.3 98.12 285.28752.7 99.42 285.08

376.79 0.1660 0.3004 0.4664378.29 0.1678 0.2958 0.4636379.69 0.1694 0.29r6 0.461038r.00 0.1709 0.2878 0.4587382.23 0.1723 0.2842 0.4565383.40 0.I736 0.2809 0.4545384.50 0.1748 0.2779 0.4527

0.008 850.008 090.007 460.006 930.006 480.006 090.005 75

.^'.O1ip::9 fromThermodlmttnric properties of Mercury Vapor,by Lucian A. Sheldon. ASME,49A,30 (l949).

Page 20: Tabel Sifat-Sifat Thermodinamika Uap Air

Table A.7Critical Constantsu

Table A.8Properties of Various ldeal Gasesu

SubstanceMolecular Temp

F-ormula Weight KChemical Molecular klFormula Weight R kg K

KI(-'-uo kg K

Pressure VolumeMPa m3/kmol Gas

KTa"oo kg K

AmmoniaArgonBromineCarbon DioxideCarbon MonoxideChlorineDeuterium (Normal)HeliumHelium3Hydrogen (Normal)KryptonNeonNitrogenNitrous OxideOxygenSulfur DioxideWaterXenonBenzenen-ButaneCarbon TetrachlorideChloroformDichlorodifl uoromethaneD ich lo rofl u o ro metha neEthaneEthyl AlcoholEthylenen-HexaneMethaneMethyl AlcoholMethyl ChloridePropanePropenePropyneTrichlorofl uoromethane

NH, t7.03Ar 39.948Br, 159.808co, 44.01co 28.01lcl, 70.906D2 4.00He 4..003He 3.00H2 2.016Kr 83.80Ne 20.183N2 28.013NrO 44.01302 31.999so,. 64.063HrO 18.015Xe 131.30cuHu 79. I t5crHro 59.124ccl4 153.82cHCl3 I19.38CC|1F2 J 120.91cHCtrF 102.92crHu 30.070crH5oH 46.07crHn 28.054cuH,n g6.l7gcHn 16.043cH3oH 32.042cHscl 50.488crH, 44.097c.Hu 42.091c.H, 40.065cclsF 137.37

r 1.28 .07244.86 .a749

10.34 .13557.39 .09433.50 .09307 .7 | .t2421.660.23 .05780. l21.30 -06495.50 .09242.73 .04173.39 .08997.27 .09615.08 .07807.88 .1217

22.09 .05685.88 .1 1864.92 .26033.80 .25474.56 .27595.47 .24034.01 .21795.r7 .r97 34.88 .14806.38 . 16735.r2 .12423.03 .36774.64 .09937 .95 .1 1806.68 .14304.26 .19984.62 .18105.J54.38 .2478

AirArgonButaneCarbon

DioxideCarbon

MonoxideEthaneEthyleneHeliumHydrogenMethaneNeon.NitrogenOctaneOxygenPropaneSteam

0.7 165 I .4000.3122 1.6671.5734 1.091

0.6529 r.289

405.5i5l584304.2IJJ

4r738.4

5.J

J..l

J J..f

209.444.5

126.2309.7r54.843Q.7647.3289.8562425.2556.4536.6384.745t.7305.55r6282,4507.9191.1513.2416.3370365401/nt q

ArCrHro

CO,

COCrHoCrH.HeH2CHnNeN2CrHrto2CrHtHrO

28.9739.94858.r24

44.01

28.0130.0728.0544.0032.016

16.0420.1 8328.013

r14.2731.99944.0971 8.0 l5

0.287 000.208 13

0.143 04

0.188 92

0.296 830.276 500.296 372.077 034.124 t80.518 350.41 I 950.296 800.072 790.259 830.188 550.46\ 52

1.00350.5203r.7164

0.8418

1.0413 0.7445 1.400r.7662 1.4897 1.186r.5482 r.2518 1.2375.1 926 3. r r 56 r .667

14.2091 10.0849 1.4092.2537 r.7354 r.2991.0299 0.6 r79 l.6671.0416 0.7448 1.4001.7113 1.6385 1.0440.92r6 0.6618 1.3931.6794 1.4909 1.1261.8723 1.4108 1.327

,/

^(Cro, C,o, and A are at 300 K).

Table A.9Constant-Pressure Soecific Heats of Various ldeal Gases'

Co,: kJ/kmol K

0: T(Kelvin)/100

Gas

N2 2,, : 39.060 - bt2.7g0-1s + 1e72.7 0*2 - 820.400-3

02 e o":37.432 +0.02010201'5 - 178.570-1 5 +236.88d-2H2 e o":56.505 -702.740-o?5 + 1165.00-r 560.70d-''5co -oo:69. t45 -0.7046300'75 -200.77 0-o 5 + 176.760-0 75

oH e o":81.546 - 59.350f 2s + 17 .32900 75 - 4.2660eNO e o.:59.283 - 1.7096fl's - 70.613 0-0 s + 74.8890-' 5

HrO e,": 143.05 - l8g.54f'2s +82.751005 -3.69899CO, eo":-3.7357 +30.529f's - 4.10340+0.024198P

Range Max.K Error

Vo

300-3500 0.43300-3500 0.30

300-3500 0.60

300-3500 0.42300-3500 0.43300-3500 0.34300-3500 0.43300-3500 0.19

"K. A. Kobe and R. E. Lynn,Jr., Chem. Rex.,52: il7-236 (t953)

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