A continuous stirred tank reactor operating under direct digital control has been constructed, commissioned and used for the practical evaluation of estimation and control techniques of interest to chemical engineers. Several increasingly complex algorithms, based on the Kalman filter, were applied to estimate process states and/or unmeasurable parameters under a variety of simulated and practical conditions. A number of multivariable suboptimal control algorithms were also investigated and, by combination with the Kalman-type estimators, on-line adaptive control was realised. The simulation studies showed that for single input- single output systems, a most useful technique for process identification was the summed sine wave method; howeve...
parameter estimation, control simulation. The paper deals with continuous-time nonlinear adaptive co...
The goal of this paper is to compare two identification methods continuous-time and discrete-time. T...
Abstract: Model Predictive Control (MPC) schemes are now widely used in process industries for the c...
A continuous stirred tank reactor operating under direct digital control has been constructed, commi...
In the past decade a large number of studies concerning the application of modern state estimation t...
In the past decade a large number of studies concerning the application of modern state estimation t...
A continuous stirred tank reactor operating under digital computer control has been designed and bui...
The control implementation loops for the chemical process require measurements and variable estimati...
The control implementation loops for the chemical process require measurements and variable estimati...
The control implementation loops for the chemical process require measurements and variable estimati...
State and parameter estimation are cornerstone problems in Chemical Process Control. When the proble...
The goal of this paper is to compare two identification methods – continuous-time and discrete-time....
Effective monitoring and tight control of chemical, petrochemical and biochemical processes are ofte...
The paper deals with adaptive control of a continuous stirred tank reactor (CSTR). A nonlinear model...
Chemical reactors are often characterized by highly nonlinear behaviour. In such a case the use of t...
parameter estimation, control simulation. The paper deals with continuous-time nonlinear adaptive co...
The goal of this paper is to compare two identification methods continuous-time and discrete-time. T...
Abstract: Model Predictive Control (MPC) schemes are now widely used in process industries for the c...
A continuous stirred tank reactor operating under direct digital control has been constructed, commi...
In the past decade a large number of studies concerning the application of modern state estimation t...
In the past decade a large number of studies concerning the application of modern state estimation t...
A continuous stirred tank reactor operating under digital computer control has been designed and bui...
The control implementation loops for the chemical process require measurements and variable estimati...
The control implementation loops for the chemical process require measurements and variable estimati...
The control implementation loops for the chemical process require measurements and variable estimati...
State and parameter estimation are cornerstone problems in Chemical Process Control. When the proble...
The goal of this paper is to compare two identification methods – continuous-time and discrete-time....
Effective monitoring and tight control of chemical, petrochemical and biochemical processes are ofte...
The paper deals with adaptive control of a continuous stirred tank reactor (CSTR). A nonlinear model...
Chemical reactors are often characterized by highly nonlinear behaviour. In such a case the use of t...
parameter estimation, control simulation. The paper deals with continuous-time nonlinear adaptive co...
The goal of this paper is to compare two identification methods continuous-time and discrete-time. T...
Abstract: Model Predictive Control (MPC) schemes are now widely used in process industries for the c...