A drier is to be designed to reduce the water content of copra om 180% to 10%. The available air is at 21.11 degree C (700F) d has an absolute humidity of 0.01 kg water per kg city solid. order to produce the desired drying conditions, the air is ated to 48.8 degreec (1200F) before it enters the drier. The it air will leave at 43.3 degree C(I 10 degree F) with 70% RH. the basis of 1 metric ton ofproduct per hour, calculate the
A drier is to be designed to reduce the water content of copra om 180% to 10%. The available air is at 21.11 degree C (700F) d has an absolute humidity of 0.01 kg water per kg city solid. order to produce the desired drying conditions, the air is ated to 48.8 degreec (1200F) before it enters the drier. The it air will leave at 43.3 degree C(I 10 degree F) with 70% RH. the basis of 1 metric ton ofproduct per hour, calculate the
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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SUBJECT: HEAT AND MASS TRANSFER
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