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.4. Sample calculations for fluid property and process performance parameters – continued  20.50 [kg m-3 ]  25.12 [kg m-3 ] C 45.61[kgm-3] C C g,CH4 g,CO2 g,i i  995.2[kgm-3] L Effective gas mass fraction in the microchannel y S S X S X S  Cg,i i,g ads LDG G GDL G purge Cg,i S LDG X S L deso S cool S GDL X  L C C tt g,i,j S S X S X S  Ctt y S g,i,j ads LDG G GDL G purge Ctt g,i,j i g,i g,i L i LDG X S L deso S cool S X  GDL L i Ctt g,i,j Ctt  tt g,i,j L,j i Mass fractions of component gases in liquid HTF, yg,CH4 0.019 yg,CO2 0.024 c 1853[Jkg-1 K-1] P,G c 3867[Jkg-1 K-1] P,L Effective fluid specific heat in the microchannel cp,g SadsSLDGXGSGDLXGSpurgeCp,G SLDG XL Sdeso Scool SGDL XLCp,L Ctt S S X S X S Ctt p,g,j ads LDG G GDL G purge p,G,j S X S S S X Ctt LDG L deso cool GDL L p,L,j Fluid specific heat for the microchannel node, c 3867[Jkg-1 K-1] P,g k 0.035[Wm-1 K-1] G k 0.621[Wm-1 K-1] L Effective fluid thermal conductivity in the microchannel kg Sads SLDG XG SGDL XG Spurge kG SLDG XL Sdeso Scool SGDL XL kL ktt S S X S X S ktt g, j ads LDG G GDL G purge G, j S X S S S X ktt LDG L deso cool GDL L L, j Fluid thermal conductivity for the microchannel node, k 0.621[Wm-1 K-1] g G 1.5105 [kg m-1 s-1] L  7.3104 [kg m-1 s-1] Effective fluid viscosity in the microchannel g SadsSLDGXGSGDLXGSpurgeG SLDG XL Sdeso Scool SGDL XLL tt S S X S X S tt g,j ads LDG G GDL G purge G,j S X S S S X tt LDG L deso cool GDL L L,j Fluid viscosity for the microchannel node, g 7.3104 [kgm-1 s-1] 192

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