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C.3 – Fluid property calculations and process performance parameters For this section, calculations are shown for the instant when liquid has displaced gases in the microchannel at 0.397 s after the start of the process at 0.5 m. Figure C.2 also applies here, where appropriate techniques to calculate fluid properties are shown for the final state of the considered instant. Table C.4. Sample calculations for fluid property and process performance parameters Input Equations Qualitytt i j tt L, j g,i, j Output C 45.61[kgm-3] g,i i L 995.2 [kg m-3 ] Two phase quality in the microchannel g,i Quality i C L Ctt Quality of desorbed gases in the HTF liquid present in the microchannel, Quality = 0.0458 C 45.61[kgm-3] g,i i 995.2[kgm-3] L Quality 0.0458 Effective fluid density in the microchannel g Sads SLDG XG SGDL XG Spurge Cg,i i SLDG XL Sdeso Scool SGDL XL C Quality 1Quality g,i L i tt S S X S X S Ctt g, j ads LDG G GDL G purge g,i, j i SLDG XL Sdeso Scool SGDL XL Ctt Qualitytt tt 1Qualitytt i g,i,j j L j Reduced HTF density due to suspended gases in the liquid, g 951.7 [kg m-3 ] 191PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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