Heat Balance Updated
Heat Balance Updated
Heat Balance Updated
Mol
Component Weight weight fractions kg/hr kmol/hr
Carbon Dioxide, CO2 44.010 0.065 2340 53.170
Water, H2O 18.015 0 0 0
Nitrogen, N2 28.013 0.03 1080 38.55298
Propane, C3H8 44.0956 0.07 2520 57.149
Methane, CH4 16.042 0.67 24120 1503.510
Ethane, C2H6 30.069 0.08 2880 95.780
i-Butane, C4H10 58.1222 0.02 720 12.388
n-Butane, C4H10 58.1222 0.025 900 15.485
i-Pentane, C5H12 72.1488 0.01 360 4.990
n-Pentane, C5H12 72.1488 0.03 1080 14.969
K2CO3 138.204 0 0 0
weight fractions kg/hr kmol/hr mol fractions weight fractions kg/hr kmol/hr
0.001 34.034 0.773 0.0004 0.13 9140.75 207.6971
0.01 340.344 18.892 0.0107 0.63670923149 44769.23 2485.108
0.032 1080 38.553 0.0219 0 0 0
0.074 2520 57.149 0.0324 0 0 0
0.709 24120 1503.51 0.8531 0 0 0
0.085 2880 95.78 0.0543 0 0 0
0.021 720 12.388 0.0070 0 0 0
0.026 900 15.485 0.0088 0 0 0
0.011 360 4.99 0.0028 0 0 0
0.032 1080 14.969 0.0085 0 0 0
0 0 0 0 0.23329076851 16403.48 118.6903
mol fractions same as 3 same as 6 weight fractions kg/hr kmol/hr mol fractions
0.073874 2305.966 52.39641
0.88391
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0 0 0 0 0
0.042216 0 0 0 0
9 10
0 0 0
0 0 0
0 0 0
0 0 0
0 0 0
0 0 0
0 0 0
0 0 0
mol fractions
0
0
0
0
0
0
0
0
Ho298.15
Component kJ/mol a0 a1 a2 a3
Carbon Dioxide, CO2 -393.52 -801.7822 671.9651 -226.1366 38.3798
Water, H2O -285.83 -303.0362 303.2388 -120.4019 23.71084
Nitrogen, N2 0.00 -251.0632 227.4529 -83.12737 15.31465
Propane, C3H8 -104.70 -971.3423 738.7186 -232.1411 38.91159
Methane, CH4 -74.87 -862.9417 779.5988 -285.281 52.89228
Ethane, C2H6 -84.00 -449.4331 329.0602 -102.4507 17.86233
i-Butane, C4H10 -134.20 -1647.677 1273.327 -401.6721 66.21702
n-Butane, C4H10 -125.60 -1417.123 1092.492 -345.8766 57.73653
i-Pentane, C5H12 -153.70 -1851.93 1406.955 -438.6186 72.256
n-Pentane, C5H12 -146.80 -2063.867 1581.974 -495.3197 81.19351
K2CO3 -1130.61 n/a n/a n/a n/a
use nist values Steam, H20 -241.83 n/a n/a n/a n/a
Temperature
ln(T+100)
T/1000
Energy (H0)
a4 a5 A B C D E F H
-3.307295 0.116944 24.99735 55.18696 -33.69137 7.948387 -0.136638 -403.6075 -393.5224
-2.3221 0.091101 -203.606 1523.29 -3196.413 2474.455 3.855326 -256.5478 -285.8304
-1.425871 0.054139 n/a n/a n/a n/a n/a n/a n/a
-3.577449 0.145414 n/a n/a n/a n/a n/a n/a n/a
-4.971868 0.189893 n/a n/a n/a n/a n/a n/a n/a
-1.788649 0.080465 n/a n/a n/a n/a n/a n/a n/a
-5.850431 0.225181 n/a n/a n/a n/a n/a n/a n/a
-5.213445 0.206197 n/a n/a n/a n/a n/a n/a n/a
-6.475149 0.255874 n/a n/a n/a n/a n/a n/a n/a
-7.152359 0.275257 n/a n/a n/a n/a n/a n/a n/a
n/a n/a 97.08093 94.22326 -2.053291 0.709644 -0.94786 -1186.499 -1150.182
n/a n/a 30.092 6.832514 6.793435 -2.53448 0.082139 -250.881 -241.8264
[1] enthalpy (kJ/mol) [1] enthalpy (kJ/hr)
Correction factor [1] kmol/hr
402.66162834419 53.170 -392.951674012329 -20893240.5072356
295.821880424254 0 -285.327604946932 0
8.60511998373868 38.553 0.432426247528101 16671.3291209509
117.560531078179 57.149 -103.623746802225 -5921993.50600036
84.4695340912869 1503.510 -74.3371580952286 -111766660.567757
94.5196312193412 95.780 -83.2450718881759 -7973212.98544949
149.678019996392 12.388 -132.769060735504 -1644743.12439142
142.378672498282 15.485 -124.145221099886 -1922388.74873173
172.853070816186 4.990 -152.013767573813 -758548.700193327
168.004000390373 14.969 -145.060344240921 -2171408.29294234
0.000 0
0.000 0
298.15 313.15
5.98682881870345 6.02381072314719
0.29815 0.31315
-153035525.103568
[2] kmol/hr [2] enthalpy (kJ/mol) [2] enthalpy (kJ/hr) [3] kmol/hr [3] enthalpy (kJ/mol)
0.773 -391.579023373225 -302690.585067506 207.697 -392.00123757745
18.892 -284.154714055137 -5368250.85792965 2485.11 -282.816482008315
38.553 1.44606218373795 55750.0353696493 0 n/a
57.149 -100.843638914415 -5763113.12031989 0 n/a
1503.51 -73.0342616893575 -109807742.792566 0 n/a
95.78 -81.3036877452889 -7787267.21224377 0 n/a
12.388 -129.069279792946 -1598910.23807501 0 n/a
15.485 -120.404000788486 -1864455.95220971 0 n/a
4.99 -147.617332016549 -736610.486762578 0 n/a
14.969 -140.557590909688 -2104006.57832713 0 n/a
0 n/a n/a 118.69 -1125.93315321653
0 n/a n/a 0 n/a
348.15 338.15
6.10512799780337 6.08256131750186
0.34815 0.33815
-135277297.788124 -917884554.600076
[3] enthalpy (kJ/hr) [6] kmol/hr [6] enthalpy (kJ/mol) [6] enthalpy (kJ/hr) [10] kmol/hr
-81417481.0411237 155.30069984 -391.609959066242 -60817300.7073011 155.301
-702830067.603683 2504.00 -282.061941373226 -706283305.975526 2504.001
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
-133637005.955269 118.6903499 -1124.72166140103 -133493607.531797 118.6903
n/a 0 n/a n/a 0
348.15
0.34815
-900594214.214625
[10] enthalpy (kJ/mol) [10] enthalpy (kJ/hr) [7] kmol/hr [7] enthalpy (kJ/mol)
-390.614006138766 -60662745.7673565 207.697 -391.015322728298
-280.168437595119 -701542047.906616 2485.11 -280.927190799063
n/a n/a 0 n/a
n/a n/a 0 n/a
n/a n/a 0 n/a
n/a n/a 0 n/a
n/a n/a 0 n/a
n/a n/a 0 n/a
n/a n/a 0 n/a
n/a n/a 0 n/a
-1121.63334784518 -133126998.545749 118.69 -1122.87852384135
n/a n/a 0 n/a
373.15 363.151125347236
0.37315 0.363151125347236
-895331792.219722 -912622132.605173000000
[7] enthalpy (kJ/hr) [9] kmol/hr [9] enthalpy (kJ/mol) [9] enthalpy (kJ/hr) [13] kmol/hr
-81212709.4846994 157.974635 -389.963830679028 -61604393.8147213 0
-698134971.126658 2437.65336 -278.949353761968 -679981829.467689 109.460728
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
-133274451.99473 120.732188 -1119.61402547238 -135173451.010768 0
n/a 0 n/a n/a 0
293.15
0.29315
-31328281.0844565
[8] enthalpy (kJ/hr) [11] kmol/hr [11] enthalpy (kJ/mol) [11] enthalpy (kJ/hr) [12] kmol/hr
0 n/a n/a 0
n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
n/a 0 n/a n/a 0
[12] enthalpy (kJ/mol) [12] enthalpy (kJ/hr)
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
n/a n/a
Stream No.
Description V Order Logarithmic Polynomials Coefficients
Ho298.15
Component kJ/mol a0 a1 a2 a3
Carbon Dioxide, CO2 -393.52 -0.80178 0.67197 -0.22614 0.03838
Water, H2O -285.83 -0.30304 0.30324 -0.12040 0.02371
Nitrogen, N2 0.00 -0.25106 0.22745 -0.08313 0.01531
Propane, C3H8 -104.70 -0.97134 0.73872 -0.23214 0.03891
Methane, CH4 -74.87 -0.86294 0.77960 -0.28528 0.05289
Ethane, C2H6 -84.00 -0.44943 0.32906 -0.10245 0.01786
i-Butane, C4H10 -134.20 -1.64768 1.27333 -0.40167 0.06622
n-Butane, C4H10 -125.60 -1.41712 1.09249 -0.34588 0.05774
i-Pentane, C5H12 -153.70 -1.85193 1.40696 -0.43862 0.07226
n-Pentane, C5H12 -146.80 -2.06387 1.58197 -0.49532 0.08119
K2CO3 -1130.61
Steam, H20 -241.83
Total
Temperature, Deg C
Pressure, Barg
Molecular Weight, MW
Flow Rate, kg/hr
Density, kg/m^3
Flow Rate, m^3/h
Enthalpy, Hº, kJ/h
LN (T K+100)
1 2
olynomials Coefficients Sour Gas to Absorber Phase Seperator Inlet
25 40
21.5
20.045
36000
17.347
2075.3
-153048890
5.986828818703 6.023810723
2 3 6 7
Phase Seperator Inlet Heat Exchanger Input (Cold Rich Solvent)
Heat Exchanger to Absorber Heat Exchanger to Regenerato
75 65 75
21.5 21.3 21.3
19.310 25.009
34034.445 70313.43
15.032 19.865
2264.2 3539.5
-135277936 -7.89E+08
Mol % kJ/kmol kmol/hr Mol % kJ/kmol kmol/hr Mol % kJ/kmol kmol/hr Mol %
7.39% -392.04 52.39014 43.99% -392.04 157.9746 5.82% -391.38 155.301 5.59%
88.39% -283.65 66.7 56.01% -283.65 2437.653 89.74% -282.78 2504.001 90.14%
0.00% 1.88 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -99.54 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -72.45 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -80.40 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -127.34 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -118.66 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -145.55 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
0.00% -138.45 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
4.22% 0.00 0 0.00% 0.00 120.7322 4.44% 0.00 118.6903 4.27%
0.00% 0.00 0 0.00% 0.00 0 0.00% 0.00 0 0.00%
100.00% 119.090 100.00% 2716.360 100.00% 2777.992 100.00%
90 90 116 108
2.1 2 2.3 40.6
kJ/kmol kmol/hr Mol % kJ/kmol kmol/hr Mol % kJ/kmol kmol/hr Mol % kJ/kmol
-391.59 8.2 5.80% -391.38 155.3 5.59% -391.79 0.00 0.00% 0.00
-283.05 127.0 89.82% -282.78 2504 90.14% -283.31 85.5 100.00% -286.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 0.0 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
0.00 6.2 4.38% 0.00 118.7 4.27% 0.00 0.00% 0.00
0.00 0.00 0.00% 0.00 0.00 0.00% 0.00 0.00 0.00% 0.00
141.400 100.00% 0.00 2778.000 100.00% 85.500 100.00%
116 100 20
2.3 21 40.6