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Extream )s used to oxiidize CO to CO, at 100 atm absoute pressure in a steady-state process A stoichiometrie amoun of impure oxygen (98% mol O, and 2 mol N:) in the fresh feed rate must be s o chosen that the mole fraction of N; in the stream entering the reactor is 0,I. ). Calculate the flow rates and compositions of streams 1, 3, and 6. Choose as a basis of calculation one mole gas mixture in the stream entering the reactor (stream Preblem#: is removed completely by with reeycle and purge. condensation via a scparator placed after the reacto from the separator The CO, produced in the reactor No CO, O, or N. exits the bottom stream he single-pass conyersion in the reastor is specified to be 25%. The purge Steam 6 Steam 7 Steam 5 Steam 8 Steam 1 Steam 2 Steam 3 Reactor pure Oxygen Steam 4

Extream )s used to oxiidize CO to CO, at 100 atm absoute pressure in a steady-state process A stoichiometrie amoun of impure oxygen (98% mol O, and 2 mol N:) in the fresh feed rate must be s o chosen that the mole fraction of N; in the stream entering the reactor is 0,I. ). Calculate the flow rates and compositions of streams 1, 3, and 6. Choose as a basis of calculation one mole gas mixture in the stream entering the reactor (stream Preblem#: is removed completely by with reeycle and purge. condensation via a scparator placed after the reacto from the separator The CO, produced in the reactor No CO, O, or N. exits the bottom stream he single-pass conyersion in the reastor is specified to be 25%. The purge Steam 6 Steam 7 Steam 5 Steam 8 Steam 1 Steam 2 Steam 3 Reactor pure Oxygen Steam 4

Introduction to Chemical Engineering Thermodynamics
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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A stoichiometrie amounr of impre oxygen (98% mol Oy and 2 mo% N2) in the fresh feed condensation via a separator placed after the reactor. No CO, O, or N. exits the bottom stream rate must be so chosen that the mole fraction of N in the stream entering the reactor is 0.1. (stream )is used to oxidize CO to CO at 100 atm absotute pressure in a steady-state process Choose as a basis of calculation one mole gas mixture in the stream entering the reactor (stream Problem with reeycle and purge. The CO, produced in the reactor is removed completely by from the separator. Single-pass converssion in the reactor is specified to be 25%. The purge 2). Calculate the flow rates and compositions of streams 1.3. and Steam 6 Steam 7 Steam 5 Steam 8 Steam 1 Steam 2 Steam 3 Reactor Co mpure Oxygen Steam 4
Transcribed Image Text:A stoichiometrie amounr of impre oxygen (98% mol Oy and 2 mo% N2) in the fresh feed condensation via a separator placed after the reactor. No CO, O, or N. exits the bottom stream rate must be so chosen that the mole fraction of N in the stream entering the reactor is 0.1. (stream )is used to oxidize CO to CO at 100 atm absotute pressure in a steady-state process Choose as a basis of calculation one mole gas mixture in the stream entering the reactor (stream Problem with reeycle and purge. The CO, produced in the reactor is removed completely by from the separator. Single-pass converssion in the reactor is specified to be 25%. The purge 2). Calculate the flow rates and compositions of streams 1.3. and Steam 6 Steam 7 Steam 5 Steam 8 Steam 1 Steam 2 Steam 3 Reactor Co mpure Oxygen Steam 4
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