A small steam condenser is designed to condense 0.76 kg/min of steam at 83 kPa with cooling water at 10°C. The exit water temperature is not to exceed 57°C. The overall heat-transfer coefficient is 3400 W/m²-°C. Calculate the area required for a double-pipe heat exchanger. Tat = 95.6°C (83 kPa), h- = 2.27x106 J/kg (enthalpy of vaporization). Calculate the following: q (Watts) = ATm = A (m?) =
A small steam condenser is designed to condense 0.76 kg/min of steam at 83 kPa with cooling water at 10°C. The exit water temperature is not to exceed 57°C. The overall heat-transfer coefficient is 3400 W/m²-°C. Calculate the area required for a double-pipe heat exchanger. Tat = 95.6°C (83 kPa), h- = 2.27x106 J/kg (enthalpy of vaporization). Calculate the following: q (Watts) = ATm = A (m?) =
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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Transcribed Image Text:3. A small steam condenser is designed to condense 0.76 kg/min of steam at 83 kPa with cooling water at 10°C. The
exit water temperature is not to exceed 57°C. The overall heat-transfer coefficient is 3400 W/m2-°C. Calculate the
area required for a double-pipe heat exchanger. Tat = 95.6°C (83 kPa), hy = 2.27x106 J/kg (enthalpy of
vaporization).
Calculate the following:
q (Watts) =
ATm =
%3D
A (m?) =
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