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02: A single-effect evaporator is concentrating a feed solution of organic colloids from (5 to 50wt%). The solution has a negligible boiling point elevation. The heat capacity of the feed is 4.06kJ/kg.K and the feed enters at 15.6°C. Saturated steam at 101.32kPa. A total of 4536kg/h of water is to be evaporated. The overall heat transfer coefficient is 1988 W/m².K. What is the required surface area and the steam consumption?

02: A single-effect evaporator is concentrating a feed solution of organic colloids from (5 to 50wt%). The solution has a negligible boiling point elevation. The heat capacity of the feed is 4.06kJ/kg.K and the feed enters at 15.6°C. Saturated steam at 101.32kPa. A total of 4536kg/h of water is to be evaporated. The overall heat transfer coefficient is 1988 W/m².K. What is the required surface area and the steam consumption?

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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02: A single -effect evaporator is concentrating a feed solution of organic colloids from (5 to 50w1%). The solution has a negligible boiling point elevation. The heat capacity of the feed is 4.06kJ/kg.K and the feed enters at 15.6°C. Saturated steam at 101.32kPa. A total of 4536kg/h of water is to be evaporated. The overall heat transfer coefficient is 1988 W/m².K. What is the required surface area and the steam consumption?
Transcribed Image Text:02: A single -effect evaporator is concentrating a feed solution of organic colloids from (5 to 50w1%). The solution has a negligible boiling point elevation. The heat capacity of the feed is 4.06kJ/kg.K and the feed enters at 15.6°C. Saturated steam at 101.32kPa. A total of 4536kg/h of water is to be evaporated. The overall heat transfer coefficient is 1988 W/m².K. What is the required surface area and the steam consumption?
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