Part B. The diagram below shows a simplified chemical proce reactor, with reaction stoichiometry of A→ 2B, followed by E recycle of stream 4 (high in unreacted A) back to stream 1. F complete the mole stream flows for all streams 1a/b-4 (tota PRODUCT B FEED A Reactor Distillation Tower RECYCLE OF UNREACTED A Process Stream Table (with recycle) Stream Number Parameter 1a 1b 2 Total Mole Flow (kgmol/hr) 100 144 Component Flow (kgmol/hr) A 100 44 8. 192
Part B. The diagram below shows a simplified chemical proce reactor, with reaction stoichiometry of A→ 2B, followed by E recycle of stream 4 (high in unreacted A) back to stream 1. F complete the mole stream flows for all streams 1a/b-4 (tota PRODUCT B FEED A Reactor Distillation Tower RECYCLE OF UNREACTED A Process Stream Table (with recycle) Stream Number Parameter 1a 1b 2 Total Mole Flow (kgmol/hr) 100 144 Component Flow (kgmol/hr) A 100 44 8. 192
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:Part B. The diagram below shows a simplified chemical process for where component À reacts to become B in the
reactor, with reaction stoichiometry of A 2B, followed by partial separation of A & B in a distillation tower, and
recycle of stream 4 (high in unreacted A) back to stream 1. Fill in the blank cells (?) in the stream table to
complete the mole stream flows for all streams 1a/b-4 (total and component).
PRODUCT B
FEED A
Reactor
Distillation
RECYCLE OF
Tower
UNREACTED A
Process Stream Table (with recycle)
Stream Number
Parameter
1a
1b
3.
4.
Total Mole Flow (kgmol/hr)
100
144
192
Component Flow (kgmol/hr)
A
100
44
8
8.
192
184
8.
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