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Forty-five hundred kilograms per hour of a solution that is 33.33% K2CrO4 (1) by mass and the rest water (2) is joined by a recycle stream containing 36.36% K2CrO4 by mass. The combined stream fed into the evaporator. The concentrated stream that leaves the evaporator contains 49.4 % K2CrO4 by mass. This stream is fed into a crystallizer, in which it is cooled, causing crystals of K2CrO4 to precipitate as well as then filtered. The filter cake consists of K2CrO4 crystals as well as a solution that contains 36.36% K2CrO4 by mass. The crystals account for 95% of the total mass of the filter cake. The solution that passes through the filter is sent back to the process as a recycle stream.
Compute
2.1 Determine the amount of water removed in the evaporator.
2.2 Determine the rate of production of crystalline K2CrO4
2.3 Determine the ratio [kg recycle/kg fresh feed]
2.4 Feed rates that the evaporator as well as crystallizer must be designed to handle.
Show all the steps in the mechanism for the following reaction, When benzene is mixed with deuterated sulfuric acid, deuterium is slowly incorporated onto the ring. Show the mechanism for this reaction and explain how this relates the sulfonation of ..
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