Figure (1) shows a distillation column (C1) treats a mixture consisting of 58 mole% Ortho, 4 mol% Meta and 38 mol% Para mono-nitro-toluene using a reflux ratio of 4.8. The mixture is to be distilled at a temperature of 415 K requiring a pressure in the boiler of about 0.06 bar. Select the light key and more volatility component, then find the composition of liquid and vapor in the 3rd stage if the relative volatility of Ortha to Para is 1.69 and Meta to Para is 1.159 at range of (288 to 418 K). Fig. [1] Q RECY-2 98 mol% Ortho 0.58 mol % Meta 0.58 Ortho TOP 0.38 Para 0.04 Meta R-4.8 TOPI PUMP BTM2 HEX BITM 8.2 mol% Meta 80 mol% Para
Figure (1) shows a distillation column (C1) treats a mixture consisting of 58 mole% Ortho, 4 mol% Meta and 38 mol% Para mono-nitro-toluene using a reflux ratio of 4.8. The mixture is to be distilled at a temperature of 415 K requiring a pressure in the boiler of about 0.06 bar. Select the light key and more volatility component, then find the composition of liquid and vapor in the 3rd stage if the relative volatility of Ortha to Para is 1.69 and Meta to Para is 1.159 at range of (288 to 418 K). Fig. [1] Q RECY-2 98 mol% Ortho 0.58 mol % Meta 0.58 Ortho TOP 0.38 Para 0.04 Meta R-4.8 TOPI PUMP BTM2 HEX BITM 8.2 mol% Meta 80 mol% Para
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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Question
A3
![[Q1]
Figure (1) shows a distillation column (C1) treats a mixture consisting of 58 mole% Ortho, 4 mol % Meta
and 38 mol % Para mono-nitro-toluene using a reflux ratio of 4.8. The mixture is to be distilled at a
temperature of 415 K requiring a pressure in the boiler of about 0.06 bar. Select the light key and more
volatility component, then find the composition of liquid and vapor in the 3rd stage if the relative volatility
of Ortha to Para is 1.69 and Meta to Para is 1.159 at range of (288 to 418 K).
RECY-2
98 mol% Ortho
0.58 mol % Meta
TOP2
0.58 Ortho
0.38 Para
0.04 Meta
R-4.8
FI
PULP
BTMZ
Fig. [1] Q
C1
TOPI
DTMI
8.2 mol% Meta
80 mot% Para
HEX](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Ff6d7fadc-5e53-45a8-9fdc-0362cdca95f3%2F0fd11eac-794d-4631-830d-04ef048c5f02%2Fcr18y3i_processed.jpeg&w=3840&q=75)
Transcribed Image Text:[Q1]
Figure (1) shows a distillation column (C1) treats a mixture consisting of 58 mole% Ortho, 4 mol % Meta
and 38 mol % Para mono-nitro-toluene using a reflux ratio of 4.8. The mixture is to be distilled at a
temperature of 415 K requiring a pressure in the boiler of about 0.06 bar. Select the light key and more
volatility component, then find the composition of liquid and vapor in the 3rd stage if the relative volatility
of Ortha to Para is 1.69 and Meta to Para is 1.159 at range of (288 to 418 K).
RECY-2
98 mol% Ortho
0.58 mol % Meta
TOP2
0.58 Ortho
0.38 Para
0.04 Meta
R-4.8
FI
PULP
BTMZ
Fig. [1] Q
C1
TOPI
DTMI
8.2 mol% Meta
80 mot% Para
HEX
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