Using the data from Table 1.7, estimate the footprints of all the equipment in the toluene HDA

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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 mTable 1.7 Equipment Summary for Toluene Hydrodealkylation PFD Heat Exchangers E-101 E-103 MDP Fl.H. 36 11

Height/Length (m) Diameter (m) Internals Pumps/Compressors Flow (kg/h) Fluid Density (kg/m) Power (shaft)

MOC 316SS CS Materials of construction Stainless steel type Par 316 F.H. Carbon steel Fl.H. Partial Fixed

Vap Cond Recipr. Centrf. Stream being vaporized Stream being condensed Reciprocating Centrifugal Rbl s.p. 1

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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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