#1: Part A. The diagram below shows a simplified chemical process where component A reacts to become B in the reactor, with reaction stoichiometry of A→ 2B, followed by partial separation of A&B in a distillation tower. Fill in the blank cells (?) in the stream table to complete the mole stream flows (total and component) for all streams 1-4. PRODUCTS FEED A UNREACTED A Distilacion Tower Process Stream Table (no recycle) Stream Number Parameter 1 2. 3. 4. Total Mole Flow (kgmol/hr) 60 110 92 Component Flow (kgmol/hr) 60 10 8 90
#1: Part A. The diagram below shows a simplified chemical process where component A reacts to become B in the reactor, with reaction stoichiometry of A→ 2B, followed by partial separation of A&B in a distillation tower. Fill in the blank cells (?) in the stream table to complete the mole stream flows (total and component) for all streams 1-4. PRODUCTS FEED A UNREACTED A Distilacion Tower Process Stream Table (no recycle) Stream Number Parameter 1 2. 3. 4. Total Mole Flow (kgmol/hr) 60 110 92 Component Flow (kgmol/hr) 60 10 8 90
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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Transcribed Image Text:#1: Part A. The diagram below shows a simplified chemical process where component A reacts to become B in
the reactor, with reaction stoichiometry of A→2B, followed by partial separation ofA &B in a distillation tower.
Fill in the blank cells (?) in the stream table to complete the mole stream flows (total and component) for all
streams 1-4.
PRODUCT B
FEED A
Reactor
UNREACTED A
Distilation
Tower
Process Stream Table (no recycle)
Stream Number
Parameter
1
2.
4.
Total Mole Flow (kgmol/hr)
60
110
92
Component Flow (kgmol/hr)
A
60
10
8
B
90
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