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Separation Process Engineering.1.6. Other Resources on Separation Process Engineering 7 1.7. SummaryObjectives 10 References 10 Homework 11 Chapter 2 Flash Distillation 13 2.1. Basic Method of Flash Distillation 13 2.2. Form and Sources of Equilibrium Data 15 2.3. Graphical Representation of Binary VLE 18 2.4. Binary Flash Distillation 22 2.4.1. Sequential Solution ...
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PDF SeparationProcessEngineeringIncludesMass.From the equilibrium data if yA .40 mole fraction water, then xA 0.09 mole fraction water. Can find LA and VA by solving the two mass balances for stage A simultaneously. LA VA FA 100 and LA .09 VA .40 100 .20. The results are VA 35.48 and LA
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