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Figure 1 shows the Heat Exchanger Network (HEN) that has been designed based on stream data and heat cascade information for ATmin= 10°C. The pinch temperature is 165°C. Analyze whether this HEN is feasible or vice versa, by showing detail calculation. of feasibility for all heat exchangers involved. 100 °C 190°C 3 420 kW 210°C e 3250 KW 1000 kW 2240 kW 240 °C 220 °C H 1240 KW H 1520 KW 160 °C 760 kW Figure 1 Heat Exchanger Network 40 °C 80 °C

Figure 1 shows the Heat Exchanger Network (HEN) that has been designed based on stream data and heat cascade information for ATmin= 10°C. The pinch temperature is 165°C. Analyze whether this HEN is feasible or vice versa, by showing detail calculation. of feasibility for all heat exchangers involved. 100 °C 190°C 3 420 kW 210°C e 3250 KW 1000 kW 2240 kW 240 °C 220 °C H 1240 KW H 1520 KW 160 °C 760 kW Figure 1 Heat Exchanger Network 40 °C 80 °C

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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CPE614: PROCESS INTEGRATION

 

b) Figure 1 shows the Heat Exchanger Network (HEN) that has been designed based on stream data and heat cascade information for ATmin= 10°C. The pinch temperature is 165°C. Analyze whether this HEN is feasible or vice versa, by showing detail calculation of feasibility for all heat exchangers involved. 100 °C 190°C 420 kW 210°C € 3250 kW 1000 kW 240 °C 220 °C H 1240 kW CH 1520 kW 2240 kW 160 °C 760 kW Figure 1 Heat Exchanger Network 40 °C 80 °C
Transcribed Image Text:b) Figure 1 shows the Heat Exchanger Network (HEN) that has been designed based on stream data and heat cascade information for ATmin= 10°C. The pinch temperature is 165°C. Analyze whether this HEN is feasible or vice versa, by showing detail calculation of feasibility for all heat exchangers involved. 100 °C 190°C 420 kW 210°C € 3250 kW 1000 kW 240 °C 220 °C H 1240 kW CH 1520 kW 2240 kW 160 °C 760 kW Figure 1 Heat Exchanger Network 40 °C 80 °C
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