A chemical company propose to build an ammonia production plant using Haber process method to produce pure liquid ammonia. As a group of engineers in the company, you are assigned to write a material balance proposal for the plant. b) Propose a simple flow diagram of the process with complete labelling, which consists of feed mixer, reactor and separator as the main equipment. For optimum production, the unreacted reactants should be recycled and purging is introduced to prevent accumulation of recycled reactants in the system. (non-CPS)

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
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A chemical company propose to build an ammonia production plant using Haber process method to
produce pure liquid ammonia. As a group of engineers in the company, you are assigned to write a
material balance proposal for the plant.
b) Propose a simple flow diagram of the process with complete labelling, which consists of feed mixer,
reactor and separator as the main equipment. For optimum production, the unreacted reactants
should be recycled and purging is introduced to prevent accumulation of recycled reactants in the
system. (non-CPS)
c) State basis of calculation and solve the material balance when overall conversion of process is
within 80-90 %. Several suitable assumptions should be introduced in solving the material balance,
such as basis of calculation, single pass conversion (50-60)% and compound ratio in the fresh feed
stream.
Transcribed Image Text:A chemical company propose to build an ammonia production plant using Haber process method to produce pure liquid ammonia. As a group of engineers in the company, you are assigned to write a material balance proposal for the plant. b) Propose a simple flow diagram of the process with complete labelling, which consists of feed mixer, reactor and separator as the main equipment. For optimum production, the unreacted reactants should be recycled and purging is introduced to prevent accumulation of recycled reactants in the system. (non-CPS) c) State basis of calculation and solve the material balance when overall conversion of process is within 80-90 %. Several suitable assumptions should be introduced in solving the material balance, such as basis of calculation, single pass conversion (50-60)% and compound ratio in the fresh feed stream.
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