For the ethylbenzene process shown in Appendix B, check the design specifications for the following three pieces of equipment against the appropriate heuristics: P-301, V-302, T-302. Comment on any significant differences that you find.

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V-301 H-301 R-301/2/3 E-301/2 R-304 E-303 E-304 E-305 V-302 T-301 E-306 E-307 V-303 P-302 A/B T-302 Benzene Feed Ethylbenzene Reactor Trans- HP LP Reactor L/V Benzene Benzene Benzene Benzene Benzene EB Feed Heater Reactors Inter- alkylation Steam Steam Effluent Separator Tower Reboiler Condenser Reflux Reflux Drum coolers Reactor Boiler Boiler Cooler Drum Pumps Tower Reboiler P-301 A/B Benzene Feed Pumps Benzene UC Ethylene °℃ /kPa V-301 3 XD+₂ FIC P-301 A/B 2 FIC 2000 H-301 23 - P-305 A/B H-301 400 4 6 R-301 500 380 8 hps TE-301 bfw R-302 11 10 hps R-304 bfw E-302 380 12 13 R-303 17 V-302 110\ E-303 E-304 E-305 A hps lps 20 ▲ bfw bfw CW 280 170 80 16 T-301 E-306 /2000 Ips 15 /110 FIC LIC cw YE-307 CW es (V-303) (LIC) X P-302 A/B 18 T-302 E-308 hps E-308 EB P-304 A/B FIC P-303 A/B EB Condenser Reflux Reflux Drum Pumps E-309 ខ្លួន EB CW (V-304) VE-309 P-303 A/B 20 V-304 EB P-304 A/B DEB Recycle Pumps P-305 A/B Benzene Recycle Pumps Fuel Gas Ethylbenzene 19