An evaporator-crystallizer-filter process is used to obtain solid potassium sulfate from an aqueous solution of this salt. The feed to the process contains 32% by weight. The wet filter cake consists of solid potassium sulfate and adhering solution goes out of the crystallizer at 23*C at a ratio of 6.9 kg crystals per kg of solution. Of the water fed to the evaporator 52.1% is evaporated. The evaporator has a maximum capacity of 127 kg per minute. (a) Calculate the maximum production rate of bone-dry potassium sulfate and (b) the rate at which the feed must be fed to the evaporator to achieve this production rate.
An evaporator-crystallizer-filter process is used to obtain solid potassium sulfate from an aqueous solution of this salt. The feed to the process contains 32% by weight. The wet filter cake consists of solid potassium sulfate and adhering solution goes out of the crystallizer at 23*C at a ratio of 6.9 kg crystals per kg of solution. Of the water fed to the evaporator 52.1% is evaporated. The evaporator has a maximum capacity of 127 kg per minute. (a) Calculate the maximum production rate of bone-dry potassium sulfate and (b) the rate at which the feed must be fed to the evaporator to achieve this production rate.
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Transcribed Image Text:An evaporator-crystallizer-filter process is used to obtain solid potassium sulfate from an aqueous solution of this
salt. The feed to the process contains 32% by weight. The wet filter cake consists of solid potassium sulfate and
adhering solution goes out of the crystallizer at 23*C at a ratio of 6.9 kg crystals per kg of solution. Of the water fed
to the evaporator 52.1% is evaporated. The evaporator has a maximum capacity of 127 kg per minute. (a) Calculate
the maximum production rate of bone-dry potassium sulfate and (b) the rate at which the feed must be fed to the
evaporator to achieve this production rate.
Temperature
Saturated Concentration %
*C
10
20
30
40
50
60
70
80
90
100
6.9
8.5
10.0
11.5
12.9
14.2
15.4
16.5
17.6
18.6
19.4
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