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Conditions for the bottoms at 229°F and 282 psia from a depro- panizer 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 Ib/ft’, lb/gal, Ib/bbl (42 gal), and kg/m². Component Flow rate, Ibmol/h Liquid density, g/cm' Propane 2.2 0.20 Isobutane 171.1 0.40 n-butane 226.6 0.43 Isopentane 28.1 0.515 n-pentane 17.5 0.525

Conditions for the bottoms at 229°F and 282 psia from a depro- panizer 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 Ib/ft’, lb/gal, Ib/bbl (42 gal), and kg/m². Component Flow rate, Ibmol/h Liquid density, g/cm' Propane 2.2 0.20 Isobutane 171.1 0.40 n-butane 226.6 0.43 Isopentane 28.1 0.515 n-pentane 17.5 0.525

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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Conditions for the bottoms at 229°F and 282 psia from a depro- panizer 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/ft', Ib/gal, Ib/bbl (42 gal), and kg/m³. Component Flow rate, Ibmol/h Liquid density, g/cm³ Propane 2.2 0.20 Isobutane 171.1 0.40 n-butane 226.6 0.43 Isopentane 28.1 0.515 n-pentane 17.5 0.525
Transcribed Image Text:Conditions for the bottoms at 229°F and 282 psia from a depro- panizer 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/ft', Ib/gal, Ib/bbl (42 gal), and kg/m³. Component Flow rate, Ibmol/h Liquid density, g/cm³ Propane 2.2 0.20 Isobutane 171.1 0.40 n-butane 226.6 0.43 Isopentane 28.1 0.515 n-pentane 17.5 0.525
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