2.13. Condenser duty for two-liquid-phase distillate. Isopropanol, with 13 wt% water, can be dehydrated to obtain almost pure isopropanol at a 90% recovery by azeotropic distillation with benzene. When condensed, the overhead vapor from the column forms two immiscible liquid phases. Use a process simulator to compute the heat-transfer rate in Btu/h and kJ/h for the condenser. Organic-Rich Phase Water-Rich Overhead Phase Phase Vapor Liquid Liquid Temperature, °C Pressure, bar Flow rate, kg/h: 76 40 40 1.4 1.4 1.4 5,870 1,790 Isopropanol 6,800 930 Water 2,350 560 Benzene 24,600 30 24,570
2.13. Condenser duty for two-liquid-phase distillate. Isopropanol, with 13 wt% water, can be dehydrated to obtain almost pure isopropanol at a 90% recovery by azeotropic distillation with benzene. When condensed, the overhead vapor from the column forms two immiscible liquid phases. Use a process simulator to compute the heat-transfer rate in Btu/h and kJ/h for the condenser. Organic-Rich Phase Water-Rich Overhead Phase Phase Vapor Liquid Liquid Temperature, °C Pressure, bar Flow rate, kg/h: 76 40 40 1.4 1.4 1.4 5,870 1,790 Isopropanol 6,800 930 Water 2,350 560 Benzene 24,600 30 24,570
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
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