A mixture of air and acetone enter a condenser at 255 ⁰C and 1.1 bar with partial pressure of acetone is 0.100 bar. A portion of the acetone is liquefied and the effluent gas leaves at 10 ⁰C and 40 bar. The air leaving the condenser at partial pressure of 0.621 bar. Assume ideal gas behavior. a. Calculate for a basis of 2.5 m3 of gas fed to the condenser the mass of acetone condensed (kg) and the volume of gas leaving the condenser (m3). b. Suppose the volumetric flow rate of the gas leaving the condenser is 35.0 m3/h. Calculate the rate (kg/h) at which acetone is vaporized in the solvent recovery unit.
A mixture of air and acetone enter a condenser at 255 ⁰C and 1.1 bar with partial pressure of acetone is 0.100 bar. A portion of the acetone is liquefied and the effluent gas leaves at 10 ⁰C and 40 bar. The air leaving the condenser at partial pressure of 0.621 bar. Assume ideal gas behavior. a. Calculate for a basis of 2.5 m3 of gas fed to the condenser the mass of acetone condensed (kg) and the volume of gas leaving the condenser (m3). b. Suppose the volumetric flow rate of the gas leaving the condenser is 35.0 m3/h. Calculate the rate (kg/h) at which acetone is vaporized in the solvent recovery unit.
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 mixture of air and acetone enter a condenser at 255 ⁰C and 1.1 bar with partial pressure of acetone is 0.100 bar. A portion of the acetone is liquefied and the effluent gas leaves at 10 ⁰C and 40 bar. The air leaving the condenser at partial pressure of 0.621 bar. Assume ideal gas behavior.
a. Calculate for a basis of 2.5 m3
of gas fed to the condenser the mass of acetone condensed (kg) and the volume of gas leaving the condenser (m3).
b. Suppose the volumetric flow rate of the gas leaving the condenser is 35.0 m3/h.
Calculate the rate (kg/h) at which acetone is vaporized in the solvent recovery unit.
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