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.4. Sample calculations for fluid property and process performance parameters – continued Feed gas supplied dMFeed,inlet,i  N S C A u dt Mtt Mt Feed,inlet,i Feed,inlet,i t z0 chads g,ig  N   g,i g g z0 S ch ads Ct A ut Feed gas entering the channel in 0.19 s, M tt  0.3708 [kg kg-1] Feed ,inlet ,CH 4 M tt  0.4532 [kg kg-1] Feed ,inlet ,CO2 Product gas collected Mtt Mt  N S S  ads collection S Ct Purge g,i Aut  g g  zL   Prod,net t Prod,net chS S CtAut t Sads  Scollection  SPurge Cg,i Agu  dMProd,net N  zL dt chS S Ct Au   GDL Purge g,i g z0    GDL Purge g,i g g z0   Product gas collected M tt  0.8708 [kg kg-1] Prod,net,CH4 M tt  0.0061 [kg kg-1] Prod,net,CO2 Mass and molar purities of product gas Purity  kg Mtt Mtt PurityMole     MW  Puritytt  kg,i Mtt i Mtt Mtt CH4 CH4 Puritytt  Mtt Prod,net,CH4 Prod,net,CH4 Prod,net,CO2  Puritykg ,i   Purity ii  kg,i MW Puritytt   i  i  kg,i MW   Mole Puritytt   kg,i MW ii Puritytt kg,CH4 Puritytt kg,CO2  0.993  0.007 Puritytt mole,CH4  0.997 Puritytt  0.003 mole,CO2 193

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