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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 – continued P105 [Pa] L  1 [m] tt 951[kgm-3] j ut 1.838[ms-1] j utt 1.838[ms-1] j1 utt 1.838[ms-1] j1 z  0.5 [m] Ctt g,CH4,j Ctt g,CH4,j Ctt w,CH4,j Ctt w,CO2 , j  20.49 [kg m-3]  25.12 [kg m-3]  23.61 [kg m-3 ]  29.13 [kg m-3] Ag 1.73107 [m2] 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] tt 7.3104 [kgm-1 s-1] j ftt 0.057 j Rh 235106 [m] ftt 0.057 L,j tt 951[kgm-3] L,j zIF  0.5 [m] Overall momentum equation P tz   S S S S  C C  z ads purge deso cool  g,i w,i u2uf u2  AR z2 2D  u2 du zIF    u2  fL L L S  2Dh  GDL  u2 du  LzIF fL L L  2Dh dt  dt     u  u u    i cs eq,Mass,i h  S Discretized and overall form used in the process model P Sads Spurge Sdeso Scool  L   tt tt tt tt tt tt tt 2   Cg,i,j Cw,i,j utt tt uj1 2uj uj1  ftt j uj   LDG  u2 fGLz fGz du   h    h   du  G 2D G dt  IF   G 2D G dt  IF  utt ut utt utt  tt j j ttutt j1 j1    j t j j 2z j AR z 2D tt j j  i g eq,Mass,i,j h  2  tt tt2 tt t  fttL,j uj ttuj ujz    L,j 2D L,j t  IF  S h   LDG2  tt utt  utt ut ftt G,j j Lz  tttt2 ttt  j tt j h  G,j 2D G,j t IF  fttL,j uj ttuj ujLz L,j 2D L,j tIF S  GDL  ftt G,j  h  h   tt utt 2 utt ut   G,j  j  tt j j z 2D G,j t IF  utt 1.838 [m s-1] j (Because displacement equations without convection terms are solved, axial dependence on velocity is absent) 189

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