Substance A from the gas mixture A-B is pure in a packed column operated at 30 °C and 1 atm. will be absorbed with water. The gas contains 8% by mole at the inlet and 0.6% by mole at the outlet. The diameter of the filled column is 0.63 m. Pure water inlet flow rate is 47.81 kmol/h, gas flow rate is 16.75 kmol/h. (HTU)L=0.490 m, mass transfer coefficient kGa=6.06x10-7 kmol/(s.m3 as .Pa) given. The balance data of the system are below. y 0 0.0158 0.0197 0.0239 0.0328 0.0416 x 0 0.0208 0.0258 0.0309 0.0405 0.0503 According to this; a) (NTU)G value b) Column height calculate
Substance A from the gas mixture A-B is pure in a packed column operated at 30 °C and 1 atm. will be absorbed with water. The gas contains 8% by mole at the inlet and 0.6% by mole at the outlet. The diameter of the filled column is 0.63 m. Pure water inlet flow rate is 47.81 kmol/h, gas flow rate is 16.75 kmol/h. (HTU)L=0.490 m, mass transfer coefficient kGa=6.06x10-7 kmol/(s.m3 as .Pa) given. The balance data of the system are below. y 0 0.0158 0.0197 0.0239 0.0328 0.0416 x 0 0.0208 0.0258 0.0309 0.0405 0.0503 According to this; a) (NTU)G value b) Column height calculate
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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Substance A from the gas mixture A-B is pure in a packed column operated at 30 °C and 1 atm. will be absorbed with water. The gas contains 8% by mole at the inlet and 0.6% by mole at the outlet. The diameter of the filled column is 0.63 m. Pure water inlet flow rate is 47.81 kmol/h, gas flow rate is 16.75 kmol/h. (HTU)L=0.490 m,
y 0 0.0158 0.0197 0.0239 0.0328 0.0416
x 0 0.0208 0.0258 0.0309 0.0405 0.0503
According to this; a) (NTU)G value b) Column height calculate
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