TABLE P12-6, FEED CONDITIONS AND PROPERTIES Component Feed (Ib-mol/hr) 10.0 10.0 Feed temperature (F) Specific heat (Btu/lb-mol - °F) Molecular weight Density (Ib/ft) 80 80 51.0 44.0 47.5 128 94 111 63.0 67.2 65.0
TABLE P12-6, FEED CONDITIONS AND PROPERTIES Component Feed (Ib-mol/hr) 10.0 10.0 Feed temperature (F) Specific heat (Btu/lb-mol - °F) Molecular weight Density (Ib/ft) 80 80 51.0 44.0 47.5 128 94 111 63.0 67.2 65.0
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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Question
The endothermic liquid-phase elementary reaction
A+B→2C
proceeds, substantially, to completion in a single steam-jacketed, continuous-stirred reactor(Table P12-6B). From the following data, calculate the steady-state reactor temperature:
Reactor volume: 125 gal
Steam jacket area:10ft2
Jacket steam: 150 psig (365.9oF saturation temperature)
Overall heat-transfer coefficient of jacket,U: 150 Btu/h.ft2.oF
Agitator shaft horsepower: 25 hp
Heat of reaction,∆HoRX=+20,000
Btu/lb-mol of A (independent of temperature)
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