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Control Structures Fixing Reactor-Inlet Stream

Control Structures Fixing Reactor-Inlet Stream [Pg.112]

The system is still described by Eqs. (4.1) to (4.6). However, the control structure now fixes the values of Fu V, k, z3 and z4. Therefore, the model can be solved for 6 unknowns F0, F2, F3, F4, zh z2. Among them, the production rate is given by  [Pg.112]

Dividing the numerator and denominator by F0, the following dimensionless form is obtained  [Pg.112]

Figu re 4.4 First-order reaction in a CSTR/separation/recycle system. [Pg.113]

Production-rate changes can be implemented in several ways, depending on the reactor design  [Pg.113]

Control Structures Fixing Reactor-Inlet Stream... [Pg.112]

See other pages where Control Structures Fixing Reactor-Inlet Stream is mentioned: [Pg.360]   


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Inlet streams

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Structural controllability

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