Distill(alpha,EML) - Page 4 ty, Liquid tray efficiencies) f...

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281c3bd116d49c123f4ee6d9c6bf601b2493d4e4.xlsx Page 1 Distillation (Constant relative volatility by Mark Burns and James Sung Department of Chemical Engineering at the University of Example from Geankoplis, 1993, p. 656 and 660 D =  47.06  mo
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281c3bd116d49c123f4ee6d9c6bf601b2493d4e4.xlsx Page 2 Xd =  0.9 F = 100  mol/hr R =  2 alpha =  3 Xf = 0.45 q =  0 E(ML) =  1
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281c3bd116d49c123f4ee6d9c6bf601b2493d4e4.xlsx Page 3 W =  52.94  mo Xw =  0.05
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281c3bd116d49c123f4ee6d9c6bf601b2493d4e4.xlsx
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Unformatted text preview: Page 4 ty, Liquid tray efficiencies) f Michigan ol/hr 0.4 0.6 0.8 1.0 1.2 Axis Title 281c3bd116d49c123f4ee6d9c6bf601b2493d4e4.xlsx Page 5 Number of Stages Required 13 Minimum Reflux Ratio = 1.91 0.0 0.2 0.4 0.6 0.8 1 0.0 0.2 0.4 Axis Title 281c3bd116d49c123f4ee6d9c6bf601b2493d4e4.xlsx Page 6 ol/hr Minimum Number of Stages 5 (at infinite reflux and E(ML)=1)...
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This note was uploaded on 02/18/2010 for the course CHEMICAL E 121 taught by Professor Rahul during the Spring '10 term at Punjab Engineering College.

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Distill(alpha,EML) - Page 4 ty, Liquid tray efficiencies) f...

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