For the styrene process shown in Appendix B, check the design specifications for the following three pieces of equipment against the appropriate heuristics: E-401, C-401, T-402. Comment on any significant differences that you find.

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Heat Exchangers E-401 Carbon steel A = 541 m² Boiling in shell, condensing in tubes 1 shell-2 tube passes Q=29695 MJ/h Compressors and Drives C-401 Carbon steel W = 364.2 kW 80% adiabatic efficiency T-402 Carbon steel Total condenser (E-409) Feed at location equivalent to tray 36 Reflux ratio = 25.8 Structured packing C=1 Diameter = 4.1 m HETP = 0.3 m Height = 34.5 m