2. 1 toluene. Entering the process is 0.5126 m³ of toluene (C,Hs) vapor at 124 °C. The liquid toluene exits at 82 °C. To cool the toluene, 13.5 mol/s of chilled water (H2O) at 50 °C are fed. The entire process is adiabatic and isobaric at 1 atm (1 bar). A water-toluene heat exchanger system is used to condense and recover liquid Use an energy balance to determine the final temperature of the water stream. HINT: It is not 82 °C!

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
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A water-toluene heat exchanger system is used to condense and recover liquid
2. [
toluene. Entering the process is 0.5126 m³ of toluene (C,H8) vapor at 124 °C. The liquid
toluene exits at 82 °C. To cool the toluene, 13.5 mol/s of chilled water (H2O) at 50 °C are fed.
The entire process is adiabatic and isobaric at 1 atm (1 bar).
Use an energy balance to determine the final temperature of the water stream.
HINT: It is not 82 °C!
Transcribed Image Text:A water-toluene heat exchanger system is used to condense and recover liquid 2. [ toluene. Entering the process is 0.5126 m³ of toluene (C,H8) vapor at 124 °C. The liquid toluene exits at 82 °C. To cool the toluene, 13.5 mol/s of chilled water (H2O) at 50 °C are fed. The entire process is adiabatic and isobaric at 1 atm (1 bar). Use an energy balance to determine the final temperature of the water stream. HINT: It is not 82 °C!
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