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Q1. Considera Shell and tube heat exchanger constructed from a 0.0254m OD tube to cool 6.93 kg/sec. of 95% ethyl alcohol Solution (cp=36 J/kg from 66% to 42°C, using water available at in 10 C (cp=41873/kg. k) at a flow rate of 6.30kg/s in The heat exchanger, 72 tubes will be used. Assume that the overall Coefficient of heat transfer based on the outer-tive area is 568 W/m²K. Calculate Surface area and the length exchanger for each of the following arrangements. of the heat kg k

Q1. Considera Shell and tube heat exchanger constructed from a 0.0254m OD tube to cool 6.93 kg/sec. of 95% ethyl alcohol Solution (cp=36 J/kg from 66% to 42°C, using water available at in 10 C (cp=41873/kg. k) at a flow rate of 6.30kg/s in The heat exchanger, 72 tubes will be used. Assume that the overall Coefficient of heat transfer based on the outer-tive area is 568 W/m²K. Calculate Surface area and the length exchanger for each of the following arrangements. of the heat kg k

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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Q1. Considera Shell and tube heat exchanger constructed from a 0.0254m OD tube to cool 6.93 kg/sec of 95% ethyl alcohol Solution (cp=36 J/kg from 66% to 42°C, using water available at in 10 C (cp=41873/kg. k) at a flow rate of 6.30kg/s in The heat exchanger, 72 tubes will be used. Assume that the overall Coefficient of heat transfer based on the outer-tive area is 568 W/m²K. Calculate Surface area and the length exchanger for each of the following arrangements. of the heat kg k
Transcribed Image Text:Q1. Considera Shell and tube heat exchanger constructed from a 0.0254m OD tube to cool 6.93 kg/sec of 95% ethyl alcohol Solution (cp=36 J/kg from 66% to 42°C, using water available at in 10 C (cp=41873/kg. k) at a flow rate of 6.30kg/s in The heat exchanger, 72 tubes will be used. Assume that the overall Coefficient of heat transfer based on the outer-tive area is 568 W/m²K. Calculate Surface area and the length exchanger for each of the following arrangements. of the heat kg k
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