An examination of the problem table for this dataset indicates a minimum hot utility demand of 15 MW and a minimum cold utility demand of 26 MW. After considering a minimum temperature difference of 20°C, the pinch analysis yields the pinch at temperatures at 120°C for the hot streams and 100°C for the cold streams. Your the task is to develop a heat exchanger network that optimizes energy recovery while using the fewest possible units. Please carry out this both visually via hand calculations and also use LINGO for numberical optimization. Stream Supply Temperature (°C) Target Temperature Heat Capacity (°C) Flowrate (MWXK-¹) No. Type 1 Hot 400 60 2 Hot 210 40 3 Cold 20 160 ་ྱ་ྱ་ 0.3 0.5 0.4 4 Cold 100 300 0.6
An examination of the problem table for this dataset indicates a minimum hot utility demand of 15 MW and a minimum cold utility demand of 26 MW. After considering a minimum temperature difference of 20°C, the pinch analysis yields the pinch at temperatures at 120°C for the hot streams and 100°C for the cold streams. Your the task is to develop a heat exchanger network that optimizes energy recovery while using the fewest possible units. Please carry out this both visually via hand calculations and also use LINGO for numberical optimization. Stream Supply Temperature (°C) Target Temperature Heat Capacity (°C) Flowrate (MWXK-¹) No. Type 1 Hot 400 60 2 Hot 210 40 3 Cold 20 160 ་ྱ་ྱ་ 0.3 0.5 0.4 4 Cold 100 300 0.6
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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Please correctly and handwritten no lingo work required
Transcribed Image Text:An examination of the problem table for this dataset indicates a
minimum hot utility demand of 15 MW and a minimum cold
utility demand of 26 MW. After considering a minimum
temperature difference of 20°C, the pinch analysis yields the
pinch at temperatures at 120°C for the hot streams and 100°C
for the cold streams. Your the task is to develop a heat
exchanger network that optimizes energy recovery while using
the fewest possible units. Please carry out this both visually via
hand calculations and also
use LINGO for numberical
optimization.
Stream
Supply
Temperature (°C)
Target
Temperature
(°C)
Heat Capacity
Flowrate
(MWXK'')
No. Type
1 Hot
400
60
0.3
2 Hot
210
40
0.5
3 Cold
20
160
0.4
4 Cold
100
300
0.6
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