Draw a flowchart of the process, labeling the two feed streams (beans and solvent) and the leaving streams (solids and extract). The soybeans contain 14.5 wt% oil and the remainder insoluble solids, and the hexane is fed at a rate corresponding to 2.00 kg hexane per kg beans. The solids stream leaving the extraction unit contains 32.5 wt% hexane, all of the non-oil solids that entered with the beans, and 0.75% of the oil that entered with the beans.

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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In the production of soybean oil, dried and flaked soybeans are brought into contact with a solvent (often hexane) that extracts the oil
and leaves behind the residual solids and a small amount of oil.
Draw a flowchart of the process, labeling the two feed streams (beans and solvent) and the leaving streams (solids and extract).
The soybeans contain 14.5 wt% oil and the remainder insoluble solids, and the hexane is fed at a rate corresponding to 2.00 kg hexane
per kg beans. The solids stream leaving the extraction unit contains 32.5 wt% hexane, all of the non-oil solids that entered with the
beans, and 0.75% of the oil that entered with the beans.
For a feed rate of 750 kg/h of dried flaked soybeans, calculate the mass flow rates of the extract and residual solids, and the
composition of the extract.
Extract:
i
kg/h
Solids:
i
kg/h
wt% oil
%
wt% oil
i
wt% hexane
wt% hexane
%
wt% non-oil solids
i
%
Transcribed Image Text:In the production of soybean oil, dried and flaked soybeans are brought into contact with a solvent (often hexane) that extracts the oil and leaves behind the residual solids and a small amount of oil. Draw a flowchart of the process, labeling the two feed streams (beans and solvent) and the leaving streams (solids and extract). The soybeans contain 14.5 wt% oil and the remainder insoluble solids, and the hexane is fed at a rate corresponding to 2.00 kg hexane per kg beans. The solids stream leaving the extraction unit contains 32.5 wt% hexane, all of the non-oil solids that entered with the beans, and 0.75% of the oil that entered with the beans. For a feed rate of 750 kg/h of dried flaked soybeans, calculate the mass flow rates of the extract and residual solids, and the composition of the extract. Extract: i kg/h Solids: i kg/h wt% oil % wt% oil i wt% hexane wt% hexane % wt% non-oil solids i %
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