di, mmol/g di, mmol/g X1 0.042 0.295 0.440 0.065 0.051 0.485 0.470 0.000 0.072 0.517 0.521 -0.129 0.148 0.586 0.537 -0.362 0.160 0.669 0.610 -0.643 0.213 0.661 0.756 -1.230 0.216 0.583 0.848 -1.310 0.249 0.595 0.893 -1.180 0.286 0.532 0.920 -1.230 0.341 0.383 0.953 -0.996 0.391 0.192 0.974 -0.470
di, mmol/g di, mmol/g X1 0.042 0.295 0.440 0.065 0.051 0.485 0.470 0.000 0.072 0.517 0.521 -0.129 0.148 0.586 0.537 -0.362 0.160 0.669 0.610 -0.643 0.213 0.661 0.756 -1.230 0.216 0.583 0.848 -1.310 0.249 0.595 0.893 -1.180 0.286 0.532 0.920 -1.230 0.341 0.383 0.953 -0.996 0.391 0.192 0.974 -0.470
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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Sircar and Myers measured liquid-phase adsorption at 30C for a binary mixture of cyclohexane (1) and ethyl alcohol (2) on activated carbon. Assuming no adsorption of ethyl alcohol, gave these results: (a) Plot the data as qe1 against x1. Explain the shape of the curve. (b) In what concentration region does the Freundlich isotherm fit the data? Make the fits
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