The temperature of a catalysed exothermic reaction is being maintained at T1°C as it promotes generation of a particular product. It is proposed to control the temperature with a proportional only controller of gain Kc. The temperature dynamics of the reactor can be modelled as a mixture o a CSTR (1st order) and PFR (dead time) to changes either in inlet temperature, or in the heating/cooling jacket flowrate via
The temperature of a catalysed exothermic reaction is being maintained at T1°C as it promotes generation of a particular product. It is proposed to control the temperature with a proportional only controller of gain Kc. The temperature dynamics of the reactor can be modelled as a mixture o a CSTR (1st order) and PFR (dead time) to changes either in inlet temperature, or in the heating/cooling jacket flowrate via
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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![The temperature of a catalysed exothermic reaction is being maintained at T1°C as it promotes
generation of a particular product. It is proposed to control the temperature with a proportional
only controller of gain Kc. The temperature dynamics of the reactor can be modelled as a mixture of
a CSTR (1st order) and PFR (dead time) to changes either in inlet temperature, or in the
heating/cooling jacket flowrate via
Ke-tas
Ts+1
i)
Considering a change in inlet temperature show why a 1st order model for a
CSTR and a dead time model for a PFR are appropriate.
CSTR - continuous stirred tank reactor
PFR - plug flow reactor](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F4b64215b-4814-4c42-ac09-5462a69f6986%2F4c94ed3e-eb39-4f0a-a2d0-fb645013dc2f%2Frbk6xki_processed.png&w=3840&q=75)
Transcribed Image Text:The temperature of a catalysed exothermic reaction is being maintained at T1°C as it promotes
generation of a particular product. It is proposed to control the temperature with a proportional
only controller of gain Kc. The temperature dynamics of the reactor can be modelled as a mixture of
a CSTR (1st order) and PFR (dead time) to changes either in inlet temperature, or in the
heating/cooling jacket flowrate via
Ke-tas
Ts+1
i)
Considering a change in inlet temperature show why a 1st order model for a
CSTR and a dead time model for a PFR are appropriate.
CSTR - continuous stirred tank reactor
PFR - plug flow reactor
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