6. A gas mixture of mass flowrate 140 kg/hr contains 10 mol% propane (C;Hg), 20 mol% n-butane(n-C4H10), 70 mol% n-pentane (n-C,H12). The mixture are evaporated completely in a pipestill (tubular furnace) and the exit conditions for temperature, pressure are 540 K, 4.1 Mpa respectively. Calculate the velocity of the vapor on the outlet stream of pipestill if the internal diameter of pipe is 5.08 cm. Note: use the second Virial coefficient equations method.
6. A gas mixture of mass flowrate 140 kg/hr contains 10 mol% propane (C;Hg), 20 mol% n-butane(n-C4H10), 70 mol% n-pentane (n-C,H12). The mixture are evaporated completely in a pipestill (tubular furnace) and the exit conditions for temperature, pressure are 540 K, 4.1 Mpa respectively. Calculate the velocity of the vapor on the outlet stream of pipestill if the internal diameter of pipe is 5.08 cm. Note: use the second Virial coefficient equations method.
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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Transcribed Image Text:6. A gas mixture of mass flowrate 140 kg/hr contains 10 mol% propane (C;H3),
20 mol% n-butane(n-C,H10), 70 mol% n-pentane (n-C,H12). The mixture are
evaporated completely in a pipestill (tubular furnace) and the exit conditions
for temperature, pressure are 540 K, 4.1 Mpa respectively. Calculate the
velocity of the vapor on the outlet stream of pipestill if the internal diameter of
pipe is 5.08 cm.
Note: use the second Virial coefficient equations method.
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