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 Input Equations Output t 0.302[kgm-3] j t  0.1 [s] tt 0.3175[kgm-3] j1 utt 10.728[ms-1] j1 tt 0.3181[kgm-3] j1 utt 10.724[ms-1] 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 Mass , He Mass,N2 Mass,CO2  6834 [s m-2 ]  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 ] R R R Ag 1.735107 [m2] Microchannel total mass conservation equation uCg,i Cw,i t z i Ag RMass,i tt  t ttutt  ttutt Ctt Ctt j jj1j1j1j1g,i,jw,i,j t 2z Real gas equation of state PRT a Vb V22bVb2 i A Rtt g Mass,i, j mmm a0.457235R2T2 b0.077796RT cc T T PPrT  11T0.52 r   0.37464 1.54226  0.269922 ccc tt 0.3178[kgm-3] j utt 10.726[ms-1] j 203

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