Selection of system boundaries and organisation of the solution. The diagram shows the main steps in a process for producing a polymer. From the following data, calculate the stream flows for a production rate of 10,000 kg/h. Reactor, yield on polymer 100 per cent slurry polymerisation 20 per cent monomer/water conversion 90 per cent catalyst 1 kg/1000 kg monomer short stopping agent 0.5 kg/1000 kg unreacted monomer Filter, wash water approx. 1 kg/1 kg polymer Recovery column, yield 98 per cent (percentage recovered) Dryer, feed ¾5 per cent water, product specification 0.5 per cent H2O Polymer losses in filter and dryer =1 per cent

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
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Selection of system boundaries and organisation of the solution.
The diagram shows the main steps in a process for producing a polymer. From the
following data, calculate the stream flows for a production rate of 10,000 kg/h.
Reactor, yield on polymer 100 per cent
slurry polymerisation 20 per cent monomer/water
conversion 90 per cent
catalyst 1 kg/1000 kg monomer
short stopping agent 0.5 kg/1000 kg unreacted monomer
Filter, wash water approx. 1 kg/1 kg polymer
Recovery column, yield 98 per cent (percentage recovered)
Dryer, feed ¾5 per cent water, product specification 0.5 per cent H2O
Polymer losses in filter and dryer =1 per cent

Monomer
water
catalyst
Reactor
Recycle
monomer
Short stop
Filter
Recovery
column
Effluent
Dryer
Polymer
Transcribed Image Text:Monomer water catalyst Reactor Recycle monomer Short stop Filter Recovery column Effluent Dryer Polymer
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