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 tt 0.3178[kgm-3] j t  0.1 [s] yt g,He,j yt g,N2,j  0.5437  0.3056  0.1871 utt 10.726[ms-1] yt g,CO2,j j ytt 0.5056 g,He,j1 ytt 0.3030 g,N2,j1 ytt 0.2204 g,CO2,j1 ytt 0.5041 g,He,j1 ytt 0.3006 g,N2,j1 ytt 0.2212 g,CO2,j1 z  0.0003 [m] Ctt g,He,j Ctt g,N2,j Ctt g,CO2,j Ctt w,He,j Ctt w,N2,j Ctt w,CO2 , j R R R Mass , He Mass,N2 Mass,CO2  6834 [s m-2 ]  0.1604 [kg m-3]  0.0955 [kg m-3]  0.1605 [kg m-3]  0.0955 [kg m-3]  0.0703 [kg m-3]  0.1605 [kg m-3]  0.0955 [kg m-3]  0.05894 [kg m-3]  4411 [s m-2 ]  5748 [s m-2 ] Ag 1.735107 [m2] Ctt g,He,j1 Ctt g,N2,j1 Ctt g,CO2,j1 Ctt g,He,j1 Ctt g,N2,j1 Ctt g,CO2,j1  0.0706 [kg m-3]  0.16056 [kg m-3]  0.9556 [kg m-3]  0.0703 [kg m-3] Microchannel species conservation equation yg,iuyg,iy Cg,iCw,i D Cg,iCg,iCw,i A,i   tzg,iAR zzAR ytt  yt g,i, j g,i, j tt j g,i, j1 Dispersion coefficient Pei  uDh DAB ,i t Ctt  ttutt j j g,i,j g,i, j w,i, j  A Rtt i g Mass,i,j i g Mass,i ytt  ytt g,i, j1 g,i, j1 2z   ytt  g Mass,i Ctt Ctt Dtt A,i,j g,i, j z2 g,i, j1  2Ctt Ctt Ctt Ctt g,i, j w,i, j A Rtt g Mass,i, j D D 1Pe2 A,i AB,i i  192 ytt g,He, j ytt g,N2 , j ytt g ,CO2 , j Dtt A,He,j Dtt A,N2,j  0.5049  0.3006  0.2212 0.006[m2 s-1] 0.009[m2 s-1] 0.010[m2 s-1] Dtt A,CO2 , j 204

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