Consider the idealized scheme shown below in which 100.0 mol/min of a reactive species A is fed to the process along with 20.0 mol/min of inserts. That stream is mixed with a recycle stream and fed to a reactor in which the single-pass conversion of A to P according to the reaction 1A-1Pis0.100 (that is, 1 molecule of A produces 1 of P). The reactor products are fed to a separator in which all of the Pis removed and sent to a product stream as pure P. The other output of the separator consists solely of A and inserts; it is split into a recycle stream that feeds the mixer and a purge stream that is further processed elsewhere. The overall conversion of A in the process is 0.95. a (mol A/min) (mol P/min) u (mol In/min) a7 (mol A/min) ip (mol P/min) (mol in/min) Purge MIXER SPLIT Feed (mol A/min) a (mol P/min) hns (mol in/min) n (mol A/min) a (mol P/min) na (mol In/min) as (mol A/min) s (mol P/min) as (mol in/min) Product REACTOR SEPARATOR a, (mol A/min) ia (mol P/min) Au (mol in/min) (mol A/min) a (mol P/min) na (mol In/min) Calculate the flow rate of each species in each stream of the process and enter the results into the table below. Stream \ Component Flow (mol/min) (mol/min) (mol/min) 1 4 5 7
Consider the idealized scheme shown below in which 100.0 mol/min of a reactive species A is fed to the process along with 20.0 mol/min of inserts. That stream is mixed with a recycle stream and fed to a reactor in which the single-pass conversion of A to P according to the reaction 1A-1Pis0.100 (that is, 1 molecule of A produces 1 of P). The reactor products are fed to a separator in which all of the Pis removed and sent to a product stream as pure P. The other output of the separator consists solely of A and inserts; it is split into a recycle stream that feeds the mixer and a purge stream that is further processed elsewhere. The overall conversion of A in the process is 0.95. a (mol A/min) (mol P/min) u (mol In/min) a7 (mol A/min) ip (mol P/min) (mol in/min) Purge MIXER SPLIT Feed (mol A/min) a (mol P/min) hns (mol in/min) n (mol A/min) a (mol P/min) na (mol In/min) as (mol A/min) s (mol P/min) as (mol in/min) Product REACTOR SEPARATOR a, (mol A/min) ia (mol P/min) Au (mol in/min) (mol A/min) a (mol P/min) na (mol In/min) Calculate the flow rate of each species in each stream of the process and enter the results into the table below. Stream \ Component Flow (mol/min) (mol/min) (mol/min) 1 4 5 7
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:Consider the idealized scheme shown below in which 100.0 mol/min of a reactive species A is fed to the process along with 20.0
mol/min of inserts. That stream is mixed with a recycle stream and fed to a reactor in which the single-pass conversion of A to P
according to the reaction 1A-1Pis0.100 (that is, 1 molecule of A produces 1 of P). The reactor products are fed to a separator in
which all of the Pis removed and sent to a product stream as pure P. The other output of the separator consists solely of A and inserts;
it is split into a recycle stream that feeds the mixer and a purge stream that is further processed elsewhere.
The overall conversion of A in the process is 0.95.
a (mol A/min)
a (mol P/min)
h (mol In/min)
a, (mol A/min)
ie (mol P/min)
(mol in/min)
Purge
MIXER
SPLIT
as (mol A/min)
i (mol P/min)
na (mol In/min)
Feed
na (mol A/min)
nia (mol P/min)
nia (mol In/min)
as (mol A/min)
es (mol P/min)
as (mol In/min)
Product
REACTOR
SEPARATOR
As (mol A/min)
iea (mol P/min)
(mol in/min)
a (mol A/min)
a (mol P/min)
Ana (mol In/min)
Calculate the flow rate of each species in each stream of the process and enter the results into the table below.
Pin,i
(mol/min)
Stream \ Component Flow
(mol/min)
(mol/min)
2
3
4
5
7
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