The cthanol dehyd rogenation reaction is carried out with the fead entering at 300°C, The feed contains 90% mal ethanol abd the balance acetaldehyde and enters the reactor at a rate of 150mol/so To heep the femperature from dropping too much ard there by decreasing the reaction rate to an unaliep tably Jow levelj heat is translered to the reautor. When the addition rate is 2440kW, the ouflet tonpera ture is d53%a Calulate the hactional oYNEYS İOn of ethano) achieved by the reactora

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
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The ethanol dehyd rogenation reactiun is carried out with the feed.
entering at 300°C. The feed contains 90% mal ethangl and the balance.
acetaldehyde and enters the reactor at a rate of I5omol ba To heep
the temperature from diopping too much and there by decreasing the
reaction rate to an unaliep tably low levelj heat is transfened to the
reautor. When the addition rate is 2440KW, the outlet tempera ture
is a53%. Calculate the fractional LONNAYS İon of ethano) achieved by
the reactora
Transcribed Image Text:The ethanol dehyd rogenation reactiun is carried out with the feed. entering at 300°C. The feed contains 90% mal ethangl and the balance. acetaldehyde and enters the reactor at a rate of I5omol ba To heep the temperature from diopping too much and there by decreasing the reaction rate to an unaliep tably low levelj heat is transfened to the reautor. When the addition rate is 2440KW, the outlet tempera ture is a53%. Calculate the fractional LONNAYS İon of ethano) achieved by the reactora
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