Component Flow rate, Ibmol/h Liquid density, g/cm³ 2.2 Propane Isobutane n-butane Isopentane n-pentane 0.20 0.40 0.40 0.43 171.1 226.6 28.1 0.515 17.5 0.525
Component Flow rate, Ibmol/h Liquid density, g/cm³ 2.2 Propane Isobutane n-butane Isopentane n-pentane 0.20 0.40 0.40 0.43 171.1 226.6 28.1 0.515 17.5 0.525
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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Liquid density of a mixture.
Conditions for the bottoms at 229oF and 282 psia from a depropanizer distillation unit in a refinery are given below, including the pure-component liquid densities. Assuming an ideal-liquid solution (volume of mixing= 0), compute the liquid density in lb/ft3, lb/gal, lb/bbl (42 gal), and kg/m3.
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