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Download Solutions Manual for Analysis, Synthesis, and Design of by Jessica W. Castillo, Richard Turton, Richard C. Bailie, PDF

By Jessica W. Castillo, Richard Turton, Richard C. Bailie, Wallace Whiting, Joseph A. Shaeiwitz

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E. 14/b Heat and Compress Cost E\lUip. No. Name 1st Stream. dp aan 1st Stream. c Ht Duty MJ/h LMTD Corr Factor 1st Stream. 41/b Heat and Compression is slightly more expensive than pump and heat. The fact that the two answers are so close is in part due to the low cost of electricity relative to the heating utility used in this problem. 11 Production of high purity oxygen via cryogenic distillation. a. 7 K b. Assuming nearly pure compositions of products, nitrogen at the top (~78 K) and oxygen at the bottom (~90 K) c.

This mixture is then pumped via P-501A/B to the Feed Fired Heater, H-501, where the temperature is raised to 380°C. The hot liquid stream, Stream 4, leaving the heater is then fed to the Drying Oil Reactor, R-501, that contains inert packing. The reactor provides residence time for the cracking reaction to take place. The two-phase mixture leaving the reactor is cooled in the Reactor Effluent Cooler, E-501, where low-pressure steam is generated. The liquid stream leaving the exchanger is at a temperature of 175°C and is passed through one of two filter vessels, V-502A/B, that removes any gum produced in the reactor.

05 Floating Head 5 ,. ol 919 $ lSI,OOO $ 994,000 r . 000 $ 154,000 $ 174,000 ". 48 Stainlo. 5 Stainle. 5 $ 6,810 $ 33,800 ... 2 Trays !

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