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Where: VF2 = volume of the feed piston at the beginning of Step 2-3 {m3} e = void fraction of the bed {-} A = total cross sectional area of the bed {m2} Upon substituting in Equation (3.6), we find: Where: VB = AL B = volume of the adsorbent bed {m3} V= PA (3.8) Now we can calculate the number of moles of feed, using the ideal gas law with P=PH andV=VF2. N =Z3L£ZB_ (3.9) Where: NF = number of moles of feed {mol} PH = high pressure limit of the cycle {Pa} This can be divided up into moles of heavy component and moles of light component by multiplying by the feed mole fraction of each component. yOPH £ V B (3.10) RT BA N FA 48PDF Image | Energy Efficiency of Gas Separation Pressure Swing Adsorption
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