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.3 Sample calculations for the governing conservation equations – continued This table shows the calculation of all differential variables using a backward differencing scheme with implicit time stepping method for the adsorbent layer node.   0.55 Ct  23.68 [kg m-3] w,CH4,j Ct  29.18 [kg m-3] w,CO2 , j t  0.005 [s]   0.1991 Ct A,CH4,j Ct A,CO2 , j Dtt eff ,G, j Dtt eff ,L, j = 1659 [mol m-3 ] = 5205 [mol m-3 ] 8.39108 [m2 s-1] 6.131010 [m2 s-1] Ctt w,CH4,j2 Ctt w,CO2,j2 Ctt w,CH4,j1 Rtt eq,Mass,G,CH4,j Rtt eq,Mass,G,CO2,j Rtt eq,Mass,L,CH4,j Rtt eq,Mass,L,CO2,j  23.17 [kg m-3]  28.76 [kg m-3]  23.41 [kg m-3 ]  28.96 [kg m-3] z  0.01 [m] Ctt w,CO2,j1 76001[m-2 s] 90133[m-2 s] 2.72106 [m-2 s] 2.73106 [m-2 s] Ctt  20.49 [kg m-3] g,CH4,j Ctt  25.12 [kg m-3] g,CO2,j Aw 4.712108 [m2] Adsorbent layer species conservation equations Cw,i CA,i  t t SSXSXSD 2C ads LDG G GDL G purge eff,G,iw,i S XS S S XD LDG L deso cool GDL L eff ,L,i  S S X S X S  1  ads LDG G GDL G  z2 purge R CC eq,Mass,G,i  g,i w,i 0 S XS S S X 1  Aw  LDG L deso cool GDL  Discretized form  t LDG L deso cool GDL L eff ,L, j  Ctt Ct  w,i, j w,i, j Ctt Ct A,i, j A,i, j L  Req,Mass,L,i   S S X S X S Dtt  Ctt 2Ctt Ctt    ads LDG G GDL G purge eff,G,j  w,i,j2 w,i,j1  S XS S S XDtt  t z2 SSXSXS1   w,i,j   0   ads LDG G GDL G purge Rtt  Ctt Ctt  eq,Mass,G,i, j   g,i, j w,i, j SXSSSX1  Aw  LDG L deso cool GDL  L Rtt  eq,Mass,L,i, j  Ctt w,CH4 , j Ctt w,CO2 , j Ctt A,CH4 , j Ctt A,CO2 , j  23.61 [kg m-3 ]  29.13 [kg m-3] 1654 [mol m-3]  5200 [mol m-3] (After iterations and implementing the switch procedure) 187

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