Determine the bare module, total module, and grassroots cost of the following: Toluene hydrodealkylation plant described in

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Determine the bare module, total module, and grassroots cost of the following:

Toluene hydrodealkylation plant described in Chapter 1 (see Figures 1.3 and 1.5 and Tables 1.5 and 1.7)V-101 P-101A/B E-101 H-101 R-101 C-101A/B Toluene Toluene Feed Feed Reactor Recycle Gas Storage Feed Pumps

Figures 1.5

V-101 Toluene Feed Drum Toluene KEY Temperature (C) Pressure (bar) Mass Flow (1000 kg/h) Hydrogen 3 10.0 25

Table 1.5 Flow Summary Table for the Benzene Process Shown in Figure 1.3 (and Figure 1.5) Stream Number

Hydrogen 0.0 Methane 0.0 Benzene Toluene 108.7 143.2 0.0 0.0 0.0 1.0 286.0 735.4 449.4 735.4 15.0 0.0 0.0

Table 1.6 Equipment Descriptions for PFD and P&IDs Equipment Type Description of Equipment Towers Size

Actual Inlet Flowrate, Temperature, Pressure Inlet and Outlet, Driver Type, Shaft Power, Materials of

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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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