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A still mill desires to cool 3000 gal/hr of an inorganic liquid from 250oF to 180oF by Lehigh River water flowing through a shell-and-tube exchanger at a rate of 5000 gal/hr. The liquid is somewhat acidic in nature and so an alloy exchanger is probably required.
Within the plant is an unused S-and-T, floating-head exchanger have one shell pass and two tube passes. The shell is mild steel, and the tubes are type 304 stainless. Specifications of the surplus exchanger revel a 20-in I.D. shell with 158 1-in 14 BWG tubes 16 ft long laid out on a 1.25 in square pitch. Baffles are placed 6-in apart.
Will the surplus exchanger be suitable for the cooling requirements? Assume the inorganic
liquid has the physical properties of water.
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