For Example 23.11, Part (b), rework the problem for the case when the stream leaving the first

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For Example 23.11, Part (b), rework the problem for the case when the stream leaving the first stage of the ejector is condensed using cooling water (in at 30°C and out at 40°C) with a 5°C approach (leaves the condenser at 45°C). What is the reduction in steam flow to the second stage of the condenser?

You will have to set this problem up and solve it using a process simulator; you should use ideal gas and latent heat enthalpy options.


Example 23.11Design a steam ejector system for the acrylic acid distillation tower shown in Figure 23.14 and discussed in

Overhead CW Condenser Acrylic Acid Tower Acrylic/Acetic Acid Feed Reboiler Ips T = 89C P = 15.7 kPa 30C 40C

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Analysis Synthesis And Design Of Chemical Processes

ISBN: 9780134177403

5th Edition

Authors: Richard Turton, Joseph Shaeiwitz, Debangsu Bhattacharyya, Wallace Whiting

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