What if:
(a) the benzene feed stream in Example R1.3-1 in the PRS were not preheated by the product stream? What would be the consequences?
(b) you needed the cost of a 6000-gallon and a 15,000-gallon Pfaudler reactor? What would they be?
(c) only one operator showed up to run the nitrobenzene plant. What would be some of your first concerns?
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