Homework Help is Here – Start Your Trial Now!
Engineering
Chemical Engineering
optimal feed stage.

optimal feed stage.

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
See similar textbooks
icon
Related questions
Question
3. We are separating a mixture of 1,2 dichloroethane and 1,1,2 trichloroethane in a distillation column. Column is at 1 atm. The feed is a saturated liquid and has 60 mol% 1,2 dichloroethane. Feed rate is 100 kmol/h. We desire a bottoms product as 1.77 mol % 1,2 dichloroethane and a distillate that is 99.15 mol % 1,2 dichloroethane. If the reflux ratio is 2.23, find the total number of stages and the optimal feed stage. Relative volatility of dichloroethane w.r.t trichloroethane is 2.4. SOA Isnoitnsv Note the equilibrium data provided below is real experimental data and therefore not perfect - you may need to "smoothen" the data to use it for Mc-Cabe Thiele plot. 101 zi menisitne frigin orj gnizooda trishoqmi won sista 29gstromu 1691 gnizua Equilibrium data from Bigg et al., Journal of Chemical & Engineering Data 9.1 (1964): 17-19. action IU GUGLEA 29AIU82 LOL E-DMC A2: Table II. Experimental x, y, and temperature data for the con system 1,2-dichloroethane-1,1,1-trichloroethane BTemp., °C. 72.40 26b91972.30 bloc62262 DO 1.000 73.00 vitam 02.2 29an9qx9 gnits19go bns Isso ni anoitub91 99619vs ert. 79.30 w noite 0.775 GUGUCC 0.610 svianstni-v199 2291 919w vriwevienotni-v30940 anied yldsm 929'0 noitellijaib 9972 A anoitzoup gniwollot srl 19waris99906l6wszu2 v9490sq berlastis 74.10 0.470 196url 75.20 obr9 16600.350 € 77.0062 916 Co 75.60 0.315 0.075 1.000 0.825 01-210109 08-atnio vitalen bns 299612 to 19dmun istoj snimet90 IS.0 = 180 SS = a00 gniwollot di jerlj bemuz26 od vám 1061990 of al no10 ed amotto 084 bet ensulot srlt to dee 1991 of r6 ,916llitzib 0800 bet enesnied 9900 80 19v0391 00'08 i 9W onemus lom OE brs angulot lom 08990000 Sent.()ansmus br6 (T) ensulot (8) enesned lliw forit bangiz 0.730 ed of ai nimulos noitellitzib AA -DMC A2¹ 0.565 0.452 0.445 (bon cours) for a better foll 0.140 (660 81.00 Kwoj\U² 290.000 AOL WORD. llow bebivib s gnizu
Transcribed Image Text:3. We are separating a mixture of 1,2 dichloroethane and 1,1,2 trichloroethane in a distillation column. Column is at 1 atm. The feed is a saturated liquid and has 60 mol% 1,2 dichloroethane. Feed rate is 100 kmol/h. We desire a bottoms product as 1.77 mol % 1,2 dichloroethane and a distillate that is 99.15 mol % 1,2 dichloroethane. If the reflux ratio is 2.23, find the total number of stages and the optimal feed stage. Relative volatility of dichloroethane w.r.t trichloroethane is 2.4. SOA Isnoitnsv Note the equilibrium data provided below is real experimental data and therefore not perfect - you may need to "smoothen" the data to use it for Mc-Cabe Thiele plot. 101 zi menisitne frigin orj gnizooda trishoqmi won sista 29gstromu 1691 gnizua Equilibrium data from Bigg et al., Journal of Chemical & Engineering Data 9.1 (1964): 17-19. action IU GUGLEA 29AIU82 LOL E-DMC A2: Table II. Experimental x, y, and temperature data for the con system 1,2-dichloroethane-1,1,1-trichloroethane BTemp., °C. 72.40 26b91972.30 bloc62262 DO 1.000 73.00 vitam 02.2 29an9qx9 gnits19go bns Isso ni anoitub91 99619vs ert. 79.30 w noite 0.775 GUGUCC 0.610 svianstni-v199 2291 919w vriwevienotni-v30940 anied yldsm 929'0 noitellijaib 9972 A anoitzoup gniwollot srl 19waris99906l6wszu2 v9490sq berlastis 74.10 0.470 196url 75.20 obr9 16600.350 € 77.0062 916 Co 75.60 0.315 0.075 1.000 0.825 01-210109 08-atnio vitalen bns 299612 to 19dmun istoj snimet90 IS.0 = 180 SS = a00 gniwollot di jerlj bemuz26 od vám 1061990 of al no10 ed amotto 084 bet ensulot srlt to dee 1991 of r6 ,916llitzib 0800 bet enesnied 9900 80 19v0391 00'08 i 9W onemus lom OE brs angulot lom 08990000 Sent.()ansmus br6 (T) ensulot (8) enesned lliw forit bangiz 0.730 ed of ai nimulos noitellitzib AA -DMC A2¹ 0.565 0.452 0.445 (bon cours) for a better foll 0.140 (660 81.00 Kwoj\U² 290.000 AOL WORD. llow bebivib s gnizu
Expert Solution
trending now

Trending now

This is a popular solution!

steps

Step by step

Solved in 4 steps with 3 images

SEE SOLUTIONCheck out a sample Q&A here
Blurred answer
Recommended textbooks for you
Introduction to Chemical Engineering Thermodynami…
Introduction to Chemical Engineering Thermodynami…
Chemical Engineering
ISBN:
9781259696527
Author:
J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:
McGraw-Hill Education
Elementary Principles of Chemical Processes, Bind…
Elementary Principles of Chemical Processes, Bind…
Chemical Engineering
ISBN:
9781118431221
Author:
Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:
WILEY
Elements of Chemical Reaction Engineering (5th Ed…
Elements of Chemical Reaction Engineering (5th Ed…
Chemical Engineering
ISBN:
9780133887518
Author:
H. Scott Fogler
Publisher:
Prentice Hall
Process Dynamics and Control, 4e
Process Dynamics and Control, 4e
Chemical Engineering
ISBN:
9781119285915
Author:
Seborg
Publisher:
WILEY
Industrial Plastics: Theory and Applications
Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:
9781285061238
Author:
Lokensgard, Erik
Publisher:
Delmar Cengage Learning
Unit Operations of Chemical Engineering
Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:
9780072848236
Author:
Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:
McGraw-Hill Companies, The
SEE MORE TEXTBOOKS