The approaches to concentrating orange juice include evaporation, freeze concentration, and reverse osmosis. Here we examine the evaporation process by focusing only on two constituents in the juice: solids and water. Fresh orange juice contains approximately 10 wt% solids (sugar, citric acid, and other ingredients) and frozen concentrate contains approximately 42 wt% solids. The frozen concen- trate is obtained by evaporating water from the fresh juice to produce a mixture that is approximately 65 wt% solids. However, so that the flavor of the concentrate will closely approximate that of fresh juice, the concentrate from the evaporator is blended with fresh orange juice (and other additives) to produce a final concentrate that is approximately 42 wt% solids. (a) Draw and label a flowchart of this process, neglecting the vaporization of everything in the juice but water. First prove that the subsystem containing the point where the bypass stream splits off from the evaporator feed has one degree of freedom. (If you think it has zero degrees, try determining the unknown variables associated with this system.) Then perform the degree-of- freedom analysis for the overall system, the evaporator, and the bypass-evaporator product mixing point, and write in order the equations you would solve to determine all unknown stream variables. In each equation, circle the variable for which you would solve, but don't do any calculations. (b) Calculate the amount of product (42% concentrate) produced per 100 kg fresh juice fed to the process and the fraction of the feed that bypasses the evaporator. (c) Most of the volatile ingredients that provide the taste of the concentrate are contained in the fresh juice that bypasses the evaporator. You could get more of these ingredients in the final product by evaporating to (say) 90% solids instead of 65%; you could then bypass a greater fraction of the fresh juice and thereby obtain an even better tasting product. Suggest possible drawbacks to this proposal.

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
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4.43. The popularity of orange juice, especially as a breakfast drink, makes this beverage an important factor
in the economy of orange-growing regions. Most marketed juice is concentrated and frozen and then
reconstituted before consumption, and some is “not-from-concentrate." Although concentrated juices
are less popular in the United States than they were at one time, they still have a major segment of the
market for orange juice.
The approaches to concentrating orange juice include evaporation, freeze concentration, and
reverse osmosis. Here we examine the evaporation process by focusing only on two constituents in the
juice: solids and water. Fresh orange juice contains approximately 10 wt% solids (sugar, citric acid, and
other ingredients) and frozen concentrate contains approximately 42 wt% solids. The frozen concen-
trate is obtained by evaporating water from the fresh juice to produce a mixture that is approximately
65 wt% solids. However, so that the flavor of the concentrate will closely approximate that of fresh
juice, the concentrate from the evaporator is blended with fresh orange juice (and other additives) to
produce a final concentrate that is approximately 42 wt% solids.
(a) Draw and label a flowchart of this process, neglecting the vaporization of everything in the juice
but water. First prove that the subsystem containing the point where the bypass stream splits off
from the evaporator feed has one degree of freedom. (If you think it has zero degrees, try
determining the unknown variables associated with this system.) Then perform the degree-of-
freedom analysis for the overall system, the evaporator, and the bypass-evaporator product
mixing point, and write in order the equations you would solve to determine all unknown stream
variables. In each equation, circle the variable for which you would solve, but don't do any
calculations.
(b) Calculate the amount of product (42% concentrate) produced per 100 kg fresh juice fed to the
process and the fraction of the feed that bypasses the evaporator.
(c) Most of the volatile ingredients that provide the taste of the concentrate are contained in the fresh juice
that bypasses the evaporator. You could get more of these ingredients in the final product by
evaporating to (say) 90% solids instead of 65%; you could then bypass a greater fraction of the fresh
juice and thereby obtain an even better tasting product. Suggest possible drawbacks to this proposal.
Transcribed Image Text:4.43. The popularity of orange juice, especially as a breakfast drink, makes this beverage an important factor in the economy of orange-growing regions. Most marketed juice is concentrated and frozen and then reconstituted before consumption, and some is “not-from-concentrate." Although concentrated juices are less popular in the United States than they were at one time, they still have a major segment of the market for orange juice. The approaches to concentrating orange juice include evaporation, freeze concentration, and reverse osmosis. Here we examine the evaporation process by focusing only on two constituents in the juice: solids and water. Fresh orange juice contains approximately 10 wt% solids (sugar, citric acid, and other ingredients) and frozen concentrate contains approximately 42 wt% solids. The frozen concen- trate is obtained by evaporating water from the fresh juice to produce a mixture that is approximately 65 wt% solids. However, so that the flavor of the concentrate will closely approximate that of fresh juice, the concentrate from the evaporator is blended with fresh orange juice (and other additives) to produce a final concentrate that is approximately 42 wt% solids. (a) Draw and label a flowchart of this process, neglecting the vaporization of everything in the juice but water. First prove that the subsystem containing the point where the bypass stream splits off from the evaporator feed has one degree of freedom. (If you think it has zero degrees, try determining the unknown variables associated with this system.) Then perform the degree-of- freedom analysis for the overall system, the evaporator, and the bypass-evaporator product mixing point, and write in order the equations you would solve to determine all unknown stream variables. In each equation, circle the variable for which you would solve, but don't do any calculations. (b) Calculate the amount of product (42% concentrate) produced per 100 kg fresh juice fed to the process and the fraction of the feed that bypasses the evaporator. (c) Most of the volatile ingredients that provide the taste of the concentrate are contained in the fresh juice that bypasses the evaporator. You could get more of these ingredients in the final product by evaporating to (say) 90% solids instead of 65%; you could then bypass a greater fraction of the fresh juice and thereby obtain an even better tasting product. Suggest possible drawbacks to this proposal.
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