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  637[kgm-3] w c 1131[Jkg-1 K-1] P,w T t  306 [K] w,j t  0.005 [s]  0.2941 [W m-1 K-1] w,j2 k Ttt 307.5[K] w Ttt 306.9[K] w,j1 z  0.01 [m] Aw 4.71108 [m2] Ttt 308[K] g,j Rtt  0.89 [W-1m K] eq,Heat,j   0.1991 H H Ct A,CH4,j  20400 [J mol-1]  25000 [J mol-1] ads ,CH 4 ads,CO2 = 1659 [mol m-3 ] Ct = 5205 [mol m-3 ] A,CO2 , j R  0.0369 W1m K eq,FS    2200[kgm-3] FS c 740[Jkg-1 K-1] P,FS T t  306 [K] FS,j 1.3 [W m-1 K-1] FS,j2 k T t  t  307.2 [K] FS T t  t  306.6 [K] FS,j1 A =4.35910-8 [m2] FS Energy conservation for adsorbent layer CTwk2TwTgTw  w p,w t h w z2 Aw Req,heat CA,i  Tw TFS ads,i i t Aw Req,FS Discretized form Ttt Tt Ttt 2Ttt Ttt Cw,j w,jkw,j2 w,j1w,j wp,wtw 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 ads,i Energy conservation for fused silica monolith wall T 2T TT C FSk FSw FS A R w eq,Heat, j i t A R w eq,FS FS p,FS t FS z2 Discretized form Ttt Tt C FS,j FS,j FS p,FS t Ttt 2Ttt k FS,j2 FS,j1 FS z2 AFS Req,FS Ttt Ttt Ttt FS,j  w,j FS,j AFS Req,FS Ttt 306.5[K] w,j Ttt 306.3[K] FS,j (After iterations and implementing the switch procedure) 188

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