Determine the amount of steam to be consumed, the economy, and the heating area required, for the production of 10,000 Ib/hr of 50 % NaOH solution from 10 % NaOH feed entering at 100 °F. Evaporation is to be carried out in a single body, standard evaporator for which an over-all coefficient of 500 Btu/hr sq. ft. °F is expected. Saturated steam is available at 50 psig and the evaporator can be operated at 10 psi vacuum relative to a barometric pressure of 14.7 psia.
Determine the amount of steam to be consumed, the economy, and the heating area required, for the production of 10,000 Ib/hr of 50 % NaOH solution from 10 % NaOH feed entering at 100 °F. Evaporation is to be carried out in a single body, standard evaporator for which an over-all coefficient of 500 Btu/hr sq. ft. °F is expected. Saturated steam is available at 50 psig and the evaporator can be operated at 10 psi vacuum relative to a barometric pressure of 14.7 psia.
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:Determine the amount of steam to be
consumed, the economy, and the heating area
required, for the production of 10,000 Ib/hr of
50 % NaOH solution from 10 % NaOH feed
entering at 100 °F. Evaporation is to be
carried out in a single body, standard
evaporator for which an over-all coefficient of
500 Btu/hr sq. ft. °F is expected. Saturated
steam is available at 50 psig and the
evaporator can be operated at 10 psi vacuum
relative to a barometric pressure of 14.7 psia.
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