Derive the operating equation for the middle section of Figure 4-17. Show that the equations are equivalent

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Derive the operating equation for the middle section of Figure 4-17. Show that the equations are equivalent whether the mass balance envelope is drawn around the top of the column or the bottom of the column.

Figure 4-17

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Separation Process Engineering Includes Mass Transfer Analysis

ISBN: 9780137468041

5th Edition

Authors: Phillip Wankat

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Question Posted: May 12, 2024 07:02 AM

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Derive the operating equation for the middle section of Figure 4-17. Show that the equations are equivalent

Question:

N **0.72 L/D=1.0 Saturated Liquid F =300- 22=0.4 Feed condenses I mole vapor/4 moles V L' Fix F = 200 2 = 0.3 Sat'd Vapori feed p=101.3 kPa Optimum Feeds B *B=0.02

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Separation Process Engineering Includes Mass Transfer Analysis

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