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partially absorbed by the fused silica cover (brown region in Figure 4.7(b)). This heat, in turn, is lost to the ambient by conduction through the insulation and by convection and radiation simultaneously. The heat transfer resistances required for the conservation equations are calculated as shown in Equations (4.20) through (4.25). Calculation of heat transfer resistances from the microchannel node to the adsorbent layer node and that from adsorbent layer node to the fused silica node is straightforward and adapted from the work by Pahinkar et al. (2015). Heat transfer from the fused silica cover to the ambient is calculated using Equation (4.22). lnRw,mid 1R RHeat,gw h h Peri 2k (4.20) (4.21) (4.22) Tw lnRhth lnRFS,mid R Rth RHeat,wFS w,mid h 2kw 2kFS R R Heat,FS Heat,ins RR 1 11 Heat ,conv Heat ,rad Heat is assumed to flow through the insulation sheet followed by losses to the ambient by convection and radiation. The individual heat transfer resistances in Equation (4.22) are calculated using Equations (4.23) through (4.25). RHeat,conv 1 hfree Periins RHeat,rad 1 hrad Periins (4.23) (4.24) 123PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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