A single-effect evaporator is being used to concentrate 200 kg/hour of liquor from 10 wt% solids to 50wt% solids. Steam is available at 5 bar (absolute) and the liquor-side of the evaporator is open to atmosphere. If the feed stream enters the evaporator at 35°C, calculate: i) the amount of steam (in kg/hour) required ii) the heat transfer area required Assume: the overall heat transfer coefficient is 1 kW m² K' the specific heat capacity of the feed is 4 kJ kg' K' heat loss from the unit is 4 kW • boiling point elevation is 3 °C

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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A single-effect evaporator is being used to concentrate 200 kg/hour of liquor from 10 wt% solids to 50wt% solids. Steam is available at 5 bar (absolute) and the liquor-side of the evaporator is open to atmosphere. If the feed stream enters the evaporator at 35°C, calculate:
i) the amount of steam (in kg/hour) required
ii) the heat transfer area required
Assume:
● the overall heat transfer coefficient is 1 kW m-2 K-1
● the specific heat capacity of the feed is 4 kJ kg-1 K-1
● heat loss from the unit is 4 kW
● boiling point elevation is 3 °C

A single-effect evaporator is being used to concentrate 200 kg/hour of liquor from 10 wt%
solids to 50wt% solids. Steam is available at 5 bar (absolute) and the liquor-side of the
evaporator is open to atmosphere. If the feed stream enters the evaporator at 35°C, calculate:
i) the amount of steam (in kg/hour) required
ii) the heat transfer area required
Assume:
the overall heat transfer coefficient is 1 kW m² K'
the specific heat capacity of the feed is 4 kJ kg' K'
heat loss from the unit is 4 kW
• boiling point elevation is 3 °C
Transcribed Image Text:A single-effect evaporator is being used to concentrate 200 kg/hour of liquor from 10 wt% solids to 50wt% solids. Steam is available at 5 bar (absolute) and the liquor-side of the evaporator is open to atmosphere. If the feed stream enters the evaporator at 35°C, calculate: i) the amount of steam (in kg/hour) required ii) the heat transfer area required Assume: the overall heat transfer coefficient is 1 kW m² K' the specific heat capacity of the feed is 4 kJ kg' K' heat loss from the unit is 4 kW • boiling point elevation is 3 °C
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