8.4-12. Concentration of Cane Sugar Solution. A single-effect evaporator is being used to concentrate a feed of 10000 lb/h of a cane sugar solution at 80°F and containing a sugar content of 15° Brix (degrees Brix is wt % sugar) to 30° Brix for use in a food process. Saturated steam at 240°F is available for heating. The vapor space in the evaporator will be at 1 atm abs pressure. The overall U=350 btu/h ft2.°F and the heat capacity of the feed is c, = 0.91 btu/lb °F. The boiling-point rise can be estimated from Example 8.5-1. The heat of solution can be considered negligible and neglected. Calculate the area required for the evaporator and the amount of steam used per hour.

Introduction to Chemical Engineering Thermodynamics
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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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8.4-12. Concentration of Cane Sugar Solution. A single-effect evaporator is being used to
concentrate a feed of 10000 lb/h of a cane sugar solution at 80°F and containing
a sugar content of 15° Brix (degrees Brix is wt % sugar) to 30° Brix for use in a
food process. Saturated steam at 240°F is available for heating. The vapor space
in the evaporator will be at 1 atm abs pressure. The overall U=350 btu/h ft2.°F
and the heat capacity of the feed is c, = 0.91 btu/lb °F. The boiling-point rise
can be estimated from Example 8.5-1. The heat of solution can be considered
negligible and neglected. Calculate the area required for the evaporator and the
amount of steam used per hour.
Transcribed Image Text:8.4-12. Concentration of Cane Sugar Solution. A single-effect evaporator is being used to concentrate a feed of 10000 lb/h of a cane sugar solution at 80°F and containing a sugar content of 15° Brix (degrees Brix is wt % sugar) to 30° Brix for use in a food process. Saturated steam at 240°F is available for heating. The vapor space in the evaporator will be at 1 atm abs pressure. The overall U=350 btu/h ft2.°F and the heat capacity of the feed is c, = 0.91 btu/lb °F. The boiling-point rise can be estimated from Example 8.5-1. The heat of solution can be considered negligible and neglected. Calculate the area required for the evaporator and the amount of steam used per hour.
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