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T2-45 °C 11-25 °C TI-45°C 12-40°C design condenser-inlet temperature of the process stream T1 =45 °C. -Outlet temperature of the process stream T2-45 °C. -Inlet temperature of the water t1= 25 °C. -Outlet temperature of the water 12-40 °C. -Mass flow rate of the process stream m'-8060 Kg/hr -Enthalpy of vapors of process stream removed 1940 KJ/kg. -CP- 4.2 KJ/Kg.K. -Assumed value of overall coefficient U-1000 W/m.°C. -Calculate number of tubes.

T2-45 °C 11-25 °C TI-45°C 12-40°C design condenser-inlet temperature of the process stream T1 =45 °C. -Outlet temperature of the process stream T2-45 °C. -Inlet temperature of the water t1= 25 °C. -Outlet temperature of the water 12-40 °C. -Mass flow rate of the process stream m'-8060 Kg/hr -Enthalpy of vapors of process stream removed 1940 KJ/kg. -CP- 4.2 KJ/Kg.K. -Assumed value of overall coefficient U-1000 W/m.°C. -Calculate number of tubes.

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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T2-45 °C 11-25 °C TI-45°C 12-40°C design condenser-inlet temperature of the process stream T1 =45 °C. -Outlet temperature of the process stream T2-45 °C. -Inlet temperature of the water t1= 25 °C. -Outlet temperature of the water 12-40 °C. -Mass flow rate of the process stream m'-8060 Kg/hr -Enthalpy of vapors of process stream removed 1940 KJ/kg. -CP- 4.2 KJ/Kg.K. -Assumed value of overall coefficient U-1000 W/m.°C. -Calculate number of tubes.
Transcribed Image Text:T2-45 °C 11-25 °C TI-45°C 12-40°C design condenser-inlet temperature of the process stream T1 =45 °C. -Outlet temperature of the process stream T2-45 °C. -Inlet temperature of the water t1= 25 °C. -Outlet temperature of the water 12-40 °C. -Mass flow rate of the process stream m'-8060 Kg/hr -Enthalpy of vapors of process stream removed 1940 KJ/kg. -CP- 4.2 KJ/Kg.K. -Assumed value of overall coefficient U-1000 W/m.°C. -Calculate number of tubes.
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