For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The inputs are the ingoing concentration of a certain component in the fluid, and the reaction rate. The output is the outgoing concentration. The realisation makes use of a first-order reaction equation, and the residence time distribution of the fluid particles inside the reactor. Also dead time is incorporated in the modelling. The method is tested on two non-linear models for which the residence time distributions are known analytically. The first model is a series of mixed tanks, and it is shown by simulation that the method gives an accurate approximation of the original model. The second model is a UV disinfection reactor, which has a dead t...
The paper provides a procedure for the design of adaptive control of a nonlinear distributed paramet...
Abstract The efficiency of chemical reactors can be analysed using the residence time distribution. ...
This paper deals with the design of adaptive linearizing controllers of process components at the ou...
For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The in...
For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The in...
For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The in...
In practice, feedback control design consists of three steps: modelling, model reduction and control...
Reactor engineering generally uses distributed parameter models for design purpose. These models are...
The Residence-Time Distribution (RTD) is a chemical engineering concept introduced by Danckwerts in ...
Two recent extensions of the residence time distribution concept are developed. The first one concer...
This work is a mathematical study of the effect of dispersion on the optimum residence times of seve...
International audienceThe Residence-Time Distribution (RTD) is a chemical engineering concept introd...
This paper studies the application of proper orthogonal decomposition (POD) to reduce the order of d...
In this paper, we propose a 2D approach in order to create a mathematical model for the determinatio...
The continuous operation of a stirred tank reactor for styrene polymerization was modeled. The propo...
The paper provides a procedure for the design of adaptive control of a nonlinear distributed paramet...
Abstract The efficiency of chemical reactors can be analysed using the residence time distribution. ...
This paper deals with the design of adaptive linearizing controllers of process components at the ou...
For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The in...
For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The in...
For chemical reactors with non-linear fluid dynamics, a linear model realisation is proposed. The in...
In practice, feedback control design consists of three steps: modelling, model reduction and control...
Reactor engineering generally uses distributed parameter models for design purpose. These models are...
The Residence-Time Distribution (RTD) is a chemical engineering concept introduced by Danckwerts in ...
Two recent extensions of the residence time distribution concept are developed. The first one concer...
This work is a mathematical study of the effect of dispersion on the optimum residence times of seve...
International audienceThe Residence-Time Distribution (RTD) is a chemical engineering concept introd...
This paper studies the application of proper orthogonal decomposition (POD) to reduce the order of d...
In this paper, we propose a 2D approach in order to create a mathematical model for the determinatio...
The continuous operation of a stirred tank reactor for styrene polymerization was modeled. The propo...
The paper provides a procedure for the design of adaptive control of a nonlinear distributed paramet...
Abstract The efficiency of chemical reactors can be analysed using the residence time distribution. ...
This paper deals with the design of adaptive linearizing controllers of process components at the ou...