At a certain point in a spiral-wound membrane, the bulk conditions on the feed side are 1.8 wt% NaCl, 25oC, and 1,000 psia, while bulk conditions on the permeate side are 0.05 wt% NaCl, 25oC, and 50 psia. For this membrane the permeance values are 1.1x 10-5 g/cm2-s-atm for H2O and 16 x 10-6 cm/s for the salt. If mass-transfer resistances are negligible, calculate the flux of water in gal/ft2-day and the flux of salt in g/ft2-day. If ks = 0.005 cm/s, estimate thepolarization factor.
At a certain point in a spiral-wound membrane, the bulk conditions on the feed side are 1.8 wt% NaCl, 25oC, and 1,000 psia, while bulk conditions on the permeate side are 0.05 wt% NaCl, 25oC, and 50 psia. For this membrane the permeance values are 1.1x 10-5 g/cm2-s-atm for H2O and 16 x 10-6 cm/s for the salt. If mass-transfer resistances are negligible, calculate the flux of water in gal/ft2-day and the flux of salt in g/ft2-day. If ks = 0.005 cm/s, estimate thepolarization factor.
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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At a certain point in a spiral-wound membrane, the bulk conditions on the feed side are 1.8 wt% NaCl, 25oC, and 1,000 psia, while bulk conditions on the permeate side are 0.05 wt% NaCl, 25oC, and 50 psia. For this membrane the permeance values are 1.1x 10-5 g/cm2-s-atm for H2O and 16 x 10-6 cm/s for the salt. If mass-transfer resistances are negligible, calculate the flux of water in gal/ft2-day and the flux of salt in g/ft2-day. If ks = 0.005 cm/s, estimate the
polarization factor.
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