TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION

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TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION ( temperature-swing-adsorption-processes-for-gas-separation )

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Table C.5. Sample calculations for energy requirement for the process operation – continued Ncyc 17.7 [cycles hr-1]  75500 [channels kg-1 ] A = 1.7310-7 [m2 ] N ch w L  1 [m]   0.1991 H H  20400[Jmol-1] C C  25000[Jmol-1]  3600 [mol m-3 ]  4900 [mol m-3 ] ads ,CH 4 ads,CO2 A,CH4 A,CO2 Heat of desorption EDeso NcycNchAw LHads,i CA,i i EDeso  2457 [kJ kg-1 hr-1] N cyc  17.7 [cycles hr-1 ]  75500 [channels kg-1 ] N M HTF ,cyc  1.12 103 [kg cycle-1 ] ch  0.0011[m3 kg-1] v P  100 [kPa] HTF HTF recirculation energy EHTF,recir  NcycNch MHTF,cyc vHTF P EHTF,recir 172 [kJ kg-1 hr-1] Ncyc 17.7[cycleshr-1] N  75500 [channels kg-1 ]  0.0229 [kJ cycle-1 ] ch H com Purge gas recirculation energy Epurge  NcycNch HCom Epurge 30600[kJkg-1hr-1] 196

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