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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 Input Equations Output This table shows the calculation of all differential variables using a backward differencing scheme with implicit time stepping method for the microchannel node. Ct  22.69 [kg m-3] g,CH4,j Ct  27.74 [kg m-3] g,CO2,j t  0.005 [s] utt 1.83[ms-1] j Ctt 18.30 [kg m-3] g,CH4,j1 Ctt  22.51 [kg m-3 ] g,CO2,j1 z  0.01 [m] Dtt 0.012[m2 s-1] A,G,j Dtt  2.23109 [m2 s-1] A,L,j Ctt g,CH4,j2 Ctt g,CO2,j2 16.21[kg m-3]  20.31 [kg m-3 ] 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 76001[m-2 s] 90133[m-2 s] 2.72106 [m-2 s] 2.73106 [m-2 s] Ctt  23.68 [kg m-3] w,CH4,j Ctt  29.18 [kg m-3] w,CO2 , j Ag 1.735107 [m2] Microchannel species conservation equation Cg,i uCg,i  t z S S X S X S D  2C  ads LDG G GDL G purge A,G  g,i  S XS S S XD z 2 LDG L deso cool GDL L A,L S S X S X S  1  ads LDG G GDL G   purge R CC eq,Mass,G,i  g,i w,i 0 S XS S S X 1  Ag  LDG L deso  cool GDL L  Req,Mass,L,i  Discretized form Ctt Ct g,i,j g,i,j utt Ctt Ctt g,i,j g,i,j1  t j z S S X S X S Dtt  Ctt 2Ctt Ctt  ads LDG G GDL G purge A,G,i,j  g,i,j2 g,i,j1 g,i,j S XS S S XDtt  z2  Sads  SLDG  XG  SGDL  XG  Spurge Rtt  Ctt Ctt   eq,Mass,G,i,j  g,i, j w,i, j S XS S S X 1  A g  LDG L deso cool GDL L A,L,i,j  1 Ctt  20.49 [kg m-3] g,CH4,j Ctt  25.12 [kg m-3] g,CH4,j (After iterations and implementing the switch procedure)  LDG L deso  R t   t  cool GDL L eq,Mass,L,i,j  0 185

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