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Table C.3 Sample calculations for the governing conservation equations – continued tt 651[kgm-3] j ctt 3867[kgm-3] P,j T t 306.7 [K] g,j t 0.005 [s] utt 1.83[ms-1] j Ttt 308.4[K] g,j1 z 0.01 [m] ktt 0.035[Wm-1 K-1] G,j ktt 0.621[Wm-1 K-1] L,j Ttt 309.4[K] g,j2 Rtt 0.89 [W-1m K] eq,Heat,G,j Rtt 0.15 [W-1m K] eq,Heat,L,j Ttt 306.4[K] w,j Ag 1.735107 [m2] Microchannel energy conservation equation hg u hg t z S S X S X S k 2T ads LDG G GDL G purge G g S X S S S X k LDG L deso cool GDL L L Req,Heat,L,i Discretized form S S X S X S ktt Ttt 2Ttt Ttt ads LDG G GDL G purge G,j g,j2 g,j1 g,j S XS S S X 1 A g z S S X S X S 1 eq,Heat,G 2 ads LDG G GDL G purgeR S XS S S X 1 T T g w 0 Ag LDG L deso cool GDL L Ttt Tt ttctt g,j g,j ttcttutt g,j g,j1 Ttt Ttt jP,jtjP,jj z S XS S S Xktt z2 Sads SLDG XG SGDL XG Spurge Rtt Ttt Ttt LDG L deso cool GDL L L,j 1 e q,Heat ,G , j g , j w, j 0 LDG L deso R t t cool GDL L eq,Heat,L,j T t 307.5 [K] g,j (After iterations and implementing the switch procedure) 186PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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