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1.6 1.4 1.2 1 0.8 0.6 0.4 0.2 00 5 10 15 20 25 30 pi [bar] Figure 2: Adsorption isotherm for CO2 (red) and H2O (blue) (Boon et al., 2014) pCO =0 2 400 °C CO2 H2O pCO = 5 bar pH O = 0 2 2 pH O = 20 bar 2 pCO = 20 bar 2 Intraparticle mass balance LDF mass transfer coefficient Multicomponent isotherm d⟨ci⟩ = k dt LDF,i c − ⟨c ⟩ E kLDF,i = 15Dp,i int,i i F ⟨qi⟩= f(⟨c1...N⟩) G rp2(εp + ρp ∂qi ) ∂ci Table 2: Intraparticle equations 9 qi [mol kg 1]PDF Image | High-temperature pressure swing adsorption cycle design for sorption
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