Development of a Pressure Swing Adsorption (PSA) Cycle for CO2 Capture

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Development of a Pressure Swing Adsorption (PSA) Cycle for CO2 Capture ( development-pressure-swing-adsorption-psa-cycle-co2-capture )

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Table 2.1 Initial and boundary conditions for different steps of the PSA process Step Time and Bed Location z/L = 0 z/L = 1 z/L = 0 z/L = 1 z/L=0 z/L=1 z/L=0 z/L=1 z/L=0 z/L=1 z/L = 0 z/L = 1 z/L=0 z/L=1 Initial, Boundary conditions and balances !"#$=0,&== ,& ! Where,Y=yi,qi,v,T,P,and i=1,2........n Boundary Conditions y=yi,F,F=FF,OSIMPM,T=TF,M.B.,P=PF,v=vF (at all t) C.M.B., O.M.B., OSIMPM, E.B. (To = TF), V.E. (Po=PH) (at all t) y = yi,HR, F = FHR, OSIMPM, T = THR, M.B., P=PHR, v = vHR (at all t) C.M.B., O.M.B., OSIMPM, E.B. (To = TF), V.E. (Po=PH) (at all t) C.M.B., v = 0, OSIMPM, E.B. (To = TF) (at all t) C.M.B., O.M.B., OSIMPM, E.B. (To = TF), V.E. (Po=PH) (at all t) C.M.B., O.M.B., OSIMPM, E.B. (To = TF), V.E. (at all t) C.M.B., v = 0, OSIMPM, E.B. (To = TF) (at all t) C.M.B., O.M.B., OSIMPM, E.B. (To = TF), V.E. (at all t) y = yi,LR, F = -FLR, OSIMPM, T = TF, M.B. (at all t) C.M.B., O.M.B., OSIMPM, E.B. (To = TF), v = 0 (at all t) y = yi,E1D,z/L=1, F = -FE1D,z/L=1, OSIMPM, T = TF, M.B. (at all t) C.M.B., v = 0, OSIMPM, E.B. (To = TF) (at all t) y = yi,LPP, F = -FLPP, OSIMPM, T = TF, M.B. (at all t) Initial Condition Feed (F) Heavy Reflux (HR) Equalization (E) Counter-current depressurization (CnD) Light reflux (LR) Equalization (E*) Light Product pressurization (LPP) F (= εbAbv(P/P*)(T*/T)): Flow in SLPM; C.M.B: Component mass balance; O.M.B: Overall mass balance; O.S.I.M.P.M. One Step Isothermal Macropore Model; E.B.: Energy balance; M.B.: Momentum balance; V. E.: Valve equation 10

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