Single – stage leaching of flaked soybeans. In a single – stage of soybean oil from flaked soybeans with hexane, feed slurry of soybeans 200 kg containing 150 kg inert solid and 25 kg solution (25% oil and 75% hexene). Oil is leached with 150 kg of fresh hexane solvent. The value of N for the slurry underflow is essentially constant at 1,5 kg insoluble solid/kg solution retained. Calculate the amounts and compositions of the overflow V1 and the underflow slurry L1 leaving the stage. The process flow diagram is the same as given in fig 12.9-2a. The known process variables are as follows
Single – stage leaching of flaked soybeans. In a single – stage of soybean oil from flaked soybeans with hexane, feed slurry of soybeans 200 kg containing 150 kg inert solid and 25 kg solution (25% oil and 75% hexene). Oil is leached with 150 kg of fresh hexane solvent. The value of N for the slurry underflow is essentially constant at 1,5 kg insoluble solid/kg solution retained. Calculate the amounts and compositions of the overflow V1 and the underflow slurry L1 leaving the stage. The process flow diagram is the same as given in fig 12.9-2a. The known process variables are as follows
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
Problem 1.1P
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Single – stage leaching of flaked soybeans. In a single – stage of soybean oil from flaked soybeans with hexane, feed slurry of soybeans 200 kg containing 150 kg inert solid and 25 kg solution (25% oil and 75% hexene). Oil is leached with 150 kg of fresh hexane solvent. The value of N for the slurry underflow is essentially constant at 1,5 kg insoluble solid/kg solution retained. Calculate the amounts and compositions of the overflow V1 and the underflow slurry L1 leaving the stage.
The process flow diagram is the same as given in fig 12.9-2a. The known process variables are as follows
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