A dilute solution of solute A in solvent B is passed through a tubular membrane separator, where the feed flows through the tubes. At a certain location, solute concentrations on the feed and permeate sides are 5.0x10-2 kmol/m3 and 1.5 x 10-2 kmol/m3, respectively.The permeance of the membrane for solute A is given by the membrane vendor as 7.3 x10-5 m/s. If the tube-side Reynolds number is 15,000, the feed-side solute Schmidt number is 500, the diffusivity of the feed-side solute is 6.5 x 10-5 cm2/s, and the inside diameter of the tube is 0.5 cm, estimate the solute flux through the membrane if the mass-transfer resistance on the permeate side of the membrane is negligible.
A dilute solution of solute A in solvent B is passed through a tubular membrane separator, where the feed flows through the tubes. At a certain location, solute concentrations on the feed and permeate sides are 5.0x10-2 kmol/m3 and 1.5 x 10-2 kmol/m3, respectively.The permeance of the membrane for solute A is given by the membrane vendor as 7.3 x10-5 m/s. If the tube-side Reynolds number is 15,000, the feed-side solute Schmidt number is 500, the diffusivity of the feed-side solute is 6.5 x 10-5 cm2/s, and the inside diameter of the tube is 0.5 cm, estimate the solute flux through the membrane if the mass-transfer resistance on the permeate side of the membrane is negligible.
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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A dilute solution of solute A in solvent B is passed through a tubular membrane separator, where the feed flows through the tubes. At a certain location, solute concentrations on the feed and permeate sides are 5.0x10-2 kmol/m3 and 1.5 x 10-2 kmol/m3, respectively.The permeance of the membrane for solute A is given by the membrane vendor as 7.3 x10-5 m/s. If the tube-side Reynolds number is 15,000, the feed-side solute Schmidt number is 500, the diffusivity of the feed-side solute is 6.5 x 10-5 cm2/s, and the inside diameter of the tube is 0.5 cm, estimate the solute flux through the membrane if the mass-transfer resistance on the permeate side of the membrane is negligible.
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