Using the data from Table 1.7, estimate the footprints of all the equipment in the toluene HDA process. For the shell-and-tube exchangers, assume 12 ft, 1.25-in tubes on a 1.5-in square pitch, and assume 2 ft additional length at either end of the exchanger for tube return and feed header.

For double pipe exchangers, assume an 8-in schedule-20 OD and a 6-in schedule-40 ID pipe with a length of 12 ft including ubend.

For the footprints of pumps, compressors, and fired heater, assume the following:

P-101 use 2 m by 1 m, P-102 use 2 m by 1 m

C-101 (+D-101) use 4 m by 2 m

H-101 use 5 m by 5 m

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Table 1.7 Equipment Summary for Toluene Hydrodealkylation PFD Heat Exchangers E-101 E-103 MDP Fl.H. 36 11 15,190 1055 Type Area (m²) Duty (MJ/h) Shell Temp. (°C) Pres. (bar) Phase MOC Tube Temp. (°C) Pres. (bar) Phase MOC Vessels/Tower/Reactors Temperature (°C) Pressure (bar) Orientation MOC Size 225 26 Vap. 316SS 258 42 Cond. 316SS V-101 55 2.0 Horizontal CS E-102 F1.H. 763 46.660 654 24 Par. Cond. 316SS 40 3 1 316SS V-102 38 24 Vertical CS 160 6 Cond. CS 90 3 1 CS V-103 38 3.0 Vertical CS E-104 Fl.H. 35 8335 112 3 Cond. CS 40 3 1 CS V-104 112 2.5 E-105 MDP 12 1085 112 3 1 CS 40 3 1 CS T-101 147 3.0 Horizontal Vertical CS CS E-106 Fl.H. 80 9045 185 11 Cond. CS 147 3 Vap. CS R-101 660 25 Vertical 316SS