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Ethylene glycol 90 10 80 20 70 30 60 Plait point7 40 50 P/ 50 40 60 30 70 20 80 R 90 10 Tie lines Water Furfural 50 40 30 20 10 B A 90 80 70 60 100 Furfural 0 Water 0- 100 0- 0- 100 Water Glycol 100 Raffinate' 0. 100 Furfural- Glycol. Extract 0.

Ethylene glycol 90 10 80 20 70 30 60 Plait point7 40 50 P/ 50 40 60 30 70 20 80 R 90 10 Tie lines Water Furfural 50 40 30 20 10 B A 90 80 70 60 100 Furfural 0 Water 0- 100 0- 0- 100 Water Glycol 100 Raffinate' 0. 100 Furfural- Glycol. Extract 0.

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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counter current partially miscible liquid liquid extraction an aqueous 20 wt% ethylene glycol mixture is extracted using pure furfural as a solvent the concetration of ethylene glycol should be effectively zero; XEt<0.025, in the resultant raffinate. The total mass flow rates of feed and solvent are 300 and 100 kg/hr respectively find the mad flow rates of extract and raffinate leaving (b) number of stages required for separation (c) concentration of extract leaving the second stage

Ethylene glycol 90 10 80 20 70 30 60 Plait point7 40 50 P/ 50 40 60 30 70 20 80 R 90 10 Tie lines Water Furfural 50 40 30 20 10 B A 90 80 70 60 100 Furfural 0 Water 0- 100 0- 0- 100 Water Glycol 100 Raffinate' 0. 100 Furfural- Glycol. Extract 0.
Transcribed Image Text:Ethylene glycol 90 10 80 20 70 30 60 Plait point7 40 50 P/ 50 40 60 30 70 20 80 R 90 10 Tie lines Water Furfural 50 40 30 20 10 B A 90 80 70 60 100 Furfural 0 Water 0- 100 0- 0- 100 Water Glycol 100 Raffinate' 0. 100 Furfural- Glycol. Extract 0.
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