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The following empirical equation correlates the values of variables ina system in which solid particles are suspended in a flowing ga 1/3 1/2 = 2.00 + 0,.600 D Pue are dimensionless groups; k, is a coefficient that expresses the rate at which a particular species transfers from Both the gas to the solid particles; and the coefficients 2.00 and 0.600 are dimensionless constants obtained by fitting experimental data covering a wide range of values of the equation variables. Estimate the values of k. for the following data

The following empirical equation correlates the values of variables ina system in which solid particles are suspended in a flowing ga 1/3 1/2 = 2.00 + 0,.600 D Pue are dimensionless groups; k, is a coefficient that expresses the rate at which a particular species transfers from Both the gas to the solid particles; and the coefficients 2.00 and 0.600 are dimensionless constants obtained by fitting experimental data covering a wide range of values of the equation variables. Estimate the values of k. for the following data

Introduction to Chemical Engineering Thermodynamics
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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The following empirical equation correlates the values of variables in a system in which solid particles are suspended in a flowing gas 1/2 kg dpy 1/3 (dp u p = 2.00 + 0.600 D Both pD andp - are dimensionless groups; k, is a coefficient that expresses the rate at which a particular species transfers from the gas to the solid particles; and the coefficients 2.00 and 0.600 are dimensionless constants obtained by fitting experimental data covering a wide range of values of the equation variables. Estimate the values of k, for the following data: Case dp D. (dimensionless) 1.00 x 10-5 (N-s)/m? 5.00 1.250 x 10 0.200 0.170 cm2/s 20.0 m/s m/s g/cm mm 1.05 x 10-4 ft2/s 3.00 x 10-7 (Ibr-s) /ft? 0.300 in 0.100 0.3000 Ib/ft 42.0 ft/s ft/s 0.250 2.60 x 10-5 4.00 x 104 1.30 kg/m 1000.0 cm/s 3 0.200 m2/s g/(cm-s) cm/s cm
Transcribed Image Text:The following empirical equation correlates the values of variables in a system in which solid particles are suspended in a flowing gas 1/2 kg dpy 1/3 (dp u p = 2.00 + 0.600 D Both pD andp - are dimensionless groups; k, is a coefficient that expresses the rate at which a particular species transfers from the gas to the solid particles; and the coefficients 2.00 and 0.600 are dimensionless constants obtained by fitting experimental data covering a wide range of values of the equation variables. Estimate the values of k, for the following data: Case dp D. (dimensionless) 1.00 x 10-5 (N-s)/m? 5.00 1.250 x 10 0.200 0.170 cm2/s 20.0 m/s m/s g/cm mm 1.05 x 10-4 ft2/s 3.00 x 10-7 (Ibr-s) /ft? 0.300 in 0.100 0.3000 Ib/ft 42.0 ft/s ft/s 0.250 2.60 x 10-5 4.00 x 104 1.30 kg/m 1000.0 cm/s 3 0.200 m2/s g/(cm-s) cm/s cm
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