1. Reverse feed double-effect evaporator is used to concentrate a feed of 10% solids to 20%. The heat-transfer coefficients are U₁ = 300 and U₂ = 600 btu/hr-ft2-°F for each evaporator, each of which has a surface area of 800 ft².

Introduction to Chemical Engineering Thermodynamics
8th Edition
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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1. Reverse feed double-effect evaporator is used to concentrate a feed of 10% solids to
20%. The heat-transfer coefficients are U₁ = 300 and U₂ = 600 btu/hr-ft2-°F for each
evaporator, each of which has a surface area of 800 ft².
Both the rise in boiling point and the heat of solution may be regarded as insignificant.
The feed enters the 2nd evaporator at 100°F, and steam enters the
first evaporator number 1 at 100 psi. The 2nd evaporator's vapor space is under
2 psia of pressure. Assume that liquid water has the same thermal capacity as all other
liquid solutions. Determine the solution's feed rate (F) and product rate (L1) for a
20% solids solution. Initial assumptions for feed rate and inlet steam temperature are
1000 lbm/hr and 350°F.
Transcribed Image Text:1. Reverse feed double-effect evaporator is used to concentrate a feed of 10% solids to 20%. The heat-transfer coefficients are U₁ = 300 and U₂ = 600 btu/hr-ft2-°F for each evaporator, each of which has a surface area of 800 ft². Both the rise in boiling point and the heat of solution may be regarded as insignificant. The feed enters the 2nd evaporator at 100°F, and steam enters the first evaporator number 1 at 100 psi. The 2nd evaporator's vapor space is under 2 psia of pressure. Assume that liquid water has the same thermal capacity as all other liquid solutions. Determine the solution's feed rate (F) and product rate (L1) for a 20% solids solution. Initial assumptions for feed rate and inlet steam temperature are 1000 lbm/hr and 350°F.
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