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Example 5.4. Redo the Example 5.2. once again, but consider the case that there is no recycle of the filtrate to be mixed with the fresh feed. Determine (a) the amount of K,Cro, produced per hour and (b) the rate that we need to evaporate water. Without the recycle of the filtrate, we can re-draw the flow chart as shown on the next page. We then try performing the balances around the whole process, as done previously. water vapour m2 kg 100% w Feed m -4,500 kg 33.3% 66.7 W FIlter cake m. kg K crystals (100%) makg 36.4% K 63.6% w makg 49 50.6% w Crystalliser & Fater Evaporator Filtrate me kg 36.4%K 63.6% w

Example 5.4. Redo the Example 5.2. once again, but consider the case that there is no recycle of the filtrate to be mixed with the fresh feed. Determine (a) the amount of K,Cro, produced per hour and (b) the rate that we need to evaporate water. Without the recycle of the filtrate, we can re-draw the flow chart as shown on the next page. We then try performing the balances around the whole process, as done previously. water vapour m2 kg 100% w Feed m -4,500 kg 33.3% 66.7 W FIlter cake m. kg K crystals (100%) makg 36.4% K 63.6% w makg 49 50.6% w Crystalliser & Fater Evaporator Filtrate me kg 36.4%K 63.6% w

Introduction to Chemical Engineering Thermodynamics
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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Example 5.4. Redo the Example 5.2. once again, but consider the case that there is no recycle of the filtrate to be mixed with the fresh feed. Determine (a) the amount of K2Cro, produced per hour and (b) the rate that we need to evaporate water. Without the recycle of the filtrate, we can re-draw the flow chart as shown on the next page. We then try performing the balances around the whole process, as done previously. water vapour mz kg FIlter cake me kg K crystals (100%) makg 36.4% K 63.6% w 100% w Feed m -4.500 kg 33.3% makg 4941 50.6% w Crystalliser & Fater Evaporator Filtrate me kg 36.4%K 63.6% w
Transcribed Image Text:Example 5.4. Redo the Example 5.2. once again, but consider the case that there is no recycle of the filtrate to be mixed with the fresh feed. Determine (a) the amount of K2Cro, produced per hour and (b) the rate that we need to evaporate water. Without the recycle of the filtrate, we can re-draw the flow chart as shown on the next page. We then try performing the balances around the whole process, as done previously. water vapour mz kg FIlter cake me kg K crystals (100%) makg 36.4% K 63.6% w 100% w Feed m -4.500 kg 33.3% makg 4941 50.6% w Crystalliser & Fater Evaporator Filtrate me kg 36.4%K 63.6% w
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