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.1 Calculation of geometrical parameters (not iterative variables) Input Equations Output Dh = 530 ×10-6 [m] th = 30 ×10-6 [m] thFS = 25 ×10-6 [m] Rh Dh th 2 R0 Dh th 22 R  Dh 12 R  R  thFS 212 R3  R2  thFS 2 Rh = 235×10-6 [m] R0 = 250×10-6 [m] R1 = 265×10-6 [m] R2 = 277×10-6 [m] R3 = 290×10-6 [m] Inlet pressure, P = 55×10-6 [Pa] Average molecular size, d = 3.8495 × 10-10 [m] Collision integral, Ω = 1.12 Inlet temperature, T = 298 [K] CH4 Molecular weight, MWCH4 = 16.043 CO2 Molecular weight MWCO2 = 44.01 A (D 2th)2 g4h A (D2 (D 2th)2) w4hh Peri(Dh 2th) Peri 2R Channel Cross sectional area, Ag = 1.735 × 10-7 [m2] Adsorbent layer cross sectional area, Aw = 4.712 × 10-8 FS 1 A (R2R2) FS 3 1 [m2]Channel perimeter, Peri = 1477×10-6 [m] Fused silica cover inner perimeter, PeriFS =1665×10-6[m] AFS = 4.359 × 10-8 [m2] 178

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