Calculate the mass of the alcohol lost in the bottoms based on the data shown in the Figure below that was collected during 1 hour of operation. Sysm Bondery Vper Heet Echrge 1000 feet F 10% EIOH P-100 kg iiete Protet 70% EFOH 30, H20 Distilation Colune uns (Wete Bs00 k 4.5 % 0.45% 3.34% 0.135% 0.35 * Untitled Question Tank A containing 90% nitrogen is mixed with Tank B containing 10 % nitrogen to get Tank C containing 60% nitrogen. You are asked to determine the ratio of the gas used from Tank A to that used from Tank B. 1.67 4.05 7.04 6.223 8.32

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
Calculate the mass of the alcohol lost in the bottoms based on the
data shown in the Figure below that was collected during 1 hour of operation.
Ssen
Boundery
Excharger
1000 feet
F 10% EIOH Cone
P-100 kg
Distiete (Profuct
70. EFOH
30, H20
Distilatige
Buons (Wate) s00 ke
ENOH
4.5 %
0.45%
3.34%
0.135%
0.35
* Untitled Question
Tank A containing 90% nitrogen is mixed with Tank B containing 10 % nitrogen to
get Tank C containing 60 % nitrogen. You are asked to determine the ratio of the gas
used from Tank A to that used from Tank B.
1.67
4.05
7.04
6.223
8.32
II
Transcribed Image Text:Calculate the mass of the alcohol lost in the bottoms based on the data shown in the Figure below that was collected during 1 hour of operation. Ssen Boundery Excharger 1000 feet F 10% EIOH Cone P-100 kg Distiete (Profuct 70. EFOH 30, H20 Distilatige Buons (Wate) s00 ke ENOH 4.5 % 0.45% 3.34% 0.135% 0.35 * Untitled Question Tank A containing 90% nitrogen is mixed with Tank B containing 10 % nitrogen to get Tank C containing 60 % nitrogen. You are asked to determine the ratio of the gas used from Tank A to that used from Tank B. 1.67 4.05 7.04 6.223 8.32 II
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