Question
Mass Balance Stream ID VS001 (link Section 5.1) PS001 (ADS001 inlet) CA004 (Ca0 feed) Flowrate KMOL/HR KG/HR KMOL/HR KG/HR KMOL/HR KG/HR CO 1.1285 31.6104 1.1285
Mass Balance
Stream ID | VS001 (link Section 5.1) | PS001 (ADS001 inlet) | CA004 (Ca0 feed) | |||
Flowrate | KMOL/HR | KG/HR | KMOL/HR | KG/HR | KMOL/HR | KG/HR |
CO | 1.1285 | 31.6104 | 1.1285 | 31.6104 | 0 | 0 |
CO2 | 44.6630 | 1965.619 | 44.6630 | 1965.619 | 0 | 0 |
H2 | 135.2616 | 272.6711 | 135.2616 | 272.6711 | 0 | 0 |
METHANE | 0.1754 | 2.8141 | 0.1754 | 2.8141 | 0 | 0 |
CAO | 0 | 0 | 0 | 0 | 42.4919 | 2382.8401 |
CACO3 | 0 | 0 | 0 | 0 | 0.3211 | 32.1386 |
Stream ID | PS002 (ADS001 outlet) | HG001 (H2 product) | PS006 (DES001 outlet) | |||
Flowrate | KMOL/HR | KG/HR | KMOL/HR | KG/HR | KMOL/HR | KG/HR |
CO | 1.1285 | 31.6104 | 0.0564 | 1.5805 | 1.0721 | 30.0299 |
CO2 | 2.1712 | 95.5554 | 0.1086 | 4.7778 | 44.4476 | 1956.131 |
H2 | 135.2616 | 272.6711 | 121.7354 | 245.4041 | 13.5261 | 27.2671 |
METHANE | 0.1754 | 2.8141 | 0.0087 | 0.1407 | 0.1666 | 2.6734 |
CAO | 0 | 0 | 0 | 0 | 42.3849 | 2376.8380 |
CACO3 | 42.8130 | 4285.0420 | 0 | 0 | 0.4281 | 42.8504 |
Energy Balance
Stream ID | VS001 | PS001 | PS002 | PS003 | PS004 | PS005 | PS006 | CA004 | HG001 | ||||||
Temperature (C) | 55.88 | 657.05 | 25 | 25.05 | -14.59 | 750 | 750 | 574.2 | 25.05 | ||||||
Pressure (atm) | 1 | 50 | 50 | 50 | 1 | 1 | 1 | 1 | 50 | ||||||
Enthalpy (M*KJ/HR) | 0.82 | 4.52 | -20.77 | -20.81 | -20.97 | -17.34 | 2.42 | -0.37 | 0.046 | ||||||
Unit ID | COM001 | EXP001 | H003 | ADS001 | PSA001 | DES001 | |||||||||
Duty (M*KJ/HR) | 3.7002 | -0.1525 | 3.6271 | -12.6469 | 0 | 7.5473 | |||||||||
Streams | VS001/ PS001 | PS003/ PS004 | PS004/ PS004 | PS001/ PS002 | PS002/ PS003+HG001 | PS005/ PS006 |
Design pressure swing adsorption unit to obtain pure Hydrogen stream.
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