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)

Figures 1.5

Transcribed Image Text:

V-101 P-101A/B E-101 H-101 R-101 C-101A/B Toluene Toluene Feed Feed Reactor Recycle Gas Storage Feed Pumps Preheater Heater Compressor Drum Toluene Hydrogen V-101 P-101A/B E-101 hps Air H-101 V-103 E-102 V-102 Reactor High-Pres. Low-Pres Effluent Phase Sep. Phase Sep, Cooler Combustion Products Fuel Gas R-101 C-101A/B CW E-102 E-103 E-106 T-101 E-104 V-104 P-102A/B E-105 Tower Benzene Benzene Benzene Reflux Reflux Product Feed Reboiler Column Condenser Drum Pumps Cooler Heater Fuel Gas V-102 V-103 T-101 78-103 Ips E-106 mps E-104 CW V-104 P-102A/B CW E-105 Benzene Figure 1.3 Skeleton Process Flow Diagram (PFD) for the Production of Benzene via the Hydrodealkylation of Toluene