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  474[kgm-3] w c 802[Jkg-1 K-1] P,w T t  299.72 [K] w,j t  0.1 [s]  0.3765 [W m-1 K-1] w,j1 k Ttt  300.333 [K] w Ttt  300.301 [K] w,j1 z  0.0003 [m] Aw 4.71108 [m2] Ttt 300.3787[K] g,j Rtt  0.928 [W-1m K] eq,Heat,j   0.3012 H H  0 [J mol-1]  17.14 [J mol-1 ]  30790 [J mol-1 ] = 0 [mol m-3 ] = 13.825 [mol m-3 ] = 2018.695 [mol m-3 ] R  0.049 W1m K  2200[kgm-3] FS c 740[Jkg-1 K-1] P,FS T t  299.635 [K] FS,j H Ct ads,CO2 A,He,j Ct A,N2,j Ct ads,He ads,N2 A,CO2 , j eq,FS   1.3 [W m-1 K-1] FS,j1 k T t  t  300.278 [K] FS Ttt  300.244 [K] FS,j1 A =1.11210-7 [m2] FS Adsorbent layer energy conservation equation T 1 c w 1k 2T w  Tg Tw A R h ads,i TFS Tw A R w p,w t w z2 CA,i  t w p,w t w z2 Ttt Ttt  Ctt Ct  Ttt Ttt g,j w,j   H A,i,j A,i,j  w,j FS,j i  c w,j w,j k w,j1 w,j w,j1  w Heat,gw Ttt Tt w Heat,wFS Ttt 2Ttt Ttt ads,i 1Aw Req,Heat,j i 1 t Fused silica energy conservation equation 1Aw Req,FS T T T 2T T T c FSk FS w FS   FS FS p,FS t FS z2 AFS RHeat,wFS AFS RHeat,FS Ttt Tt c FS,j FS,j FS p,FS t Ttt 2Ttt Ttt Ttt Ttt T Ttt k FS,j1 FS,j FS,j1  w,j FS,j   FS,j FS z2 AFS Req,wFS AFS RHeat,FS Ttt 300.3177[K] w,j Ttt 300.2615[K] FS,j 208

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