(a)
Interpretation:
The response of the tank temperature for the given process is to be simulated for a step change in the heat input of the heater from
Concept introduction:
For chemical processes, dynamic models consisting ordinary differential equations are derived through unsteady-state conservation laws. These laws generally include mass and energy balances.
The process models generally include algebraic relationships which commence from
For a function
Here,
The difference in the actual variable
In steady-state process, the accumulation in the process is taken as zero.
(b)
Interpretation:
The overall transfer function for the given heating system including tank and the heater is to be determined.
Concept introduction:
For chemical processes, dynamic models consisting ordinary differential equations are derived through unsteady-state conservation laws. These laws generally include mass and energy balances.
The process models generally include algebraic relationships which commence from thermodynamics, transport phenomena, chemical kinetics, and physical properties of the processes.
For a function
Here,
The difference in the actual variable
In steady-state process, the accumulation in the process is taken as zero.
(c)
Interpretation:
The response of the tank temperature for the given process is to be simulated for a step change in the heat input for the transfer function derived in part (b).
Concept introduction:
For chemical processes, dynamic models consisting ordinary differential equations are derived through unsteady-state conservation laws. These laws generally include mass and energy balances.
The process models generally include algebraic relationships which commence from thermodynamics, transport phenomena, chemical kinetics, and physical properties of the processes.
For a function
Here,
The difference in the actual variable
In steady-state process, the accumulation in the process is taken as zero.
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Process Dynamics and Control, 4e
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