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 D.2. Sample calculations for governing equations in the laboratory scale models – continued   0.688 Ct w,He,j Ct w,N2,j  0.1642 [kg m-3 ]  0.0923 [kg m-3 ]  0.0394 [kg m-3 ] t  0.1 [s]   0.3012 Ct w,CO2 , j Ct A,He,j Ct A,N2,j Ct A,CO2 , j = 0 [mol m-3 ] = 13.825 [mol m-3 ] = 2018.695 [mol m-3 ] Dtt He,mix,eff ,total, j Dtt N2 ,mix,eff ,total, j Dtt CO2 ,mix,eff ,total, j 1.62105 [m2 s-1] 1.28105 [m2 s-1] Ctt w,He,j1 Ctt w,N2,j1 1.11105 [m2 s-1]  0.1641 [kg m-3 ] Ctt w,CO2,j1 Ctt w,He,j1 Ctt w,N2,j1 Ctt w,CO2,j1  0.0923 [kg m-3]  0.0393 [kg m-3]  0.1643 [kg m-3]  0.0923 [kg m-3]  0.03938 [kg m-3] z  0.0003 [m]  4411 [s m-2 ]  5748 [s m-2 ]  6834 [s m-2 ]  0.1604 [kg m-3]  0.0955 [kg m-3]  0.07033 [kg m-3] Aw 4.712108 [m2] R R R Mass , He Mass,N2 Mass,CO2 Ctt g,He,j Ctt g,N2,j Ctt g,CO2,j Adsorbent layer species conservation equation Cw,i  CA,i   D Cw,i  Cg,i Cw,i t t zeff,i zAR Ctt Ct  Ctt Ct   w,i,j w,i,j  A,i,j A,i,j    w Mass,i t Dtt i,mix,eff ,total, j t Ctt 2Ctt Ctt w,i,j1 w,i,j w,i,j1  z2 Ctt Ctt  g,i,j w,i,j 0 A Rtt w eq,Mass,i, j Ctt w,He,j Ctt w,N2 , j Ctt w,CO2 , j Ctt A,He,j Ctt A,N2,j Ctt A,CO2 , j  0.1604 [kg m-3]  0.0955 [kg m-3]  0.0589 [kg m-3]  0 [mol m-3] 12.35 [mol m-3]  2347 [mol m-3] 207

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