The life-time performance of chemical processes is limited due to changes in the plant dynamics and disturbance characteristics over time. Such systems often make use of model-based controllers. When a dynamic change arises over time, a difference occurs between the dynamic models contained in the controller and the true system dynamics. The difference in dynamics could deteriorate the performance of a model-based control system. Monitoring the performance on-line is therefore of importance. Detection of a dynamic plant or disturbance change occurs by a classical performance monitoring method, which estimates the variance of the controlled outputs. A change is detected at the moment that a maximum performance bound is violated. An important...
This paper illustrates the results of the off-line application of an advanced performance monitoring...
Process Control Modeling and Analysis of a Binary Packed Distillation Column using structured packin...
A detailed dynamic simulator of a propylene/propane (C{sub 3}) splitter, which was bench-marked agai...
The inherent time-varying nature of dynamics in chemical processes often limits the lifetime perform...
As the sophistication of systems used in chemical processing industries increases and demands for hi...
A sieve plate distillation column has been constructed and interfaced to a minicomputer with the nec...
Model Predictive Control (MPC) is a powerful tool in the control of large scale chemical processes a...
Model Predictive Control (MPC) is a powerful tool in the control of large scale chemical processes a...
Model predictive control (MPC) is a control technique that is frequently used in the process industr...
The profitability of any industrial process is closely related to its ability to maintain near optim...
Abstract: Model Predictive Control (MPC) is an advanced process control technique used in process re...
Distillation column units present special safety hazards because of their large inventories, which o...
Modern control techniques have been applied to a distillation column. Three control techniques were ...
Plant-wide disturbance; control loop performance; principal components; diagnosis; non-linearity; mu...
This paper presents a methodology to detect the origin of closed-loop performance degradation of mod...
This paper illustrates the results of the off-line application of an advanced performance monitoring...
Process Control Modeling and Analysis of a Binary Packed Distillation Column using structured packin...
A detailed dynamic simulator of a propylene/propane (C{sub 3}) splitter, which was bench-marked agai...
The inherent time-varying nature of dynamics in chemical processes often limits the lifetime perform...
As the sophistication of systems used in chemical processing industries increases and demands for hi...
A sieve plate distillation column has been constructed and interfaced to a minicomputer with the nec...
Model Predictive Control (MPC) is a powerful tool in the control of large scale chemical processes a...
Model Predictive Control (MPC) is a powerful tool in the control of large scale chemical processes a...
Model predictive control (MPC) is a control technique that is frequently used in the process industr...
The profitability of any industrial process is closely related to its ability to maintain near optim...
Abstract: Model Predictive Control (MPC) is an advanced process control technique used in process re...
Distillation column units present special safety hazards because of their large inventories, which o...
Modern control techniques have been applied to a distillation column. Three control techniques were ...
Plant-wide disturbance; control loop performance; principal components; diagnosis; non-linearity; mu...
This paper presents a methodology to detect the origin of closed-loop performance degradation of mod...
This paper illustrates the results of the off-line application of an advanced performance monitoring...
Process Control Modeling and Analysis of a Binary Packed Distillation Column using structured packin...
A detailed dynamic simulator of a propylene/propane (C{sub 3}) splitter, which was bench-marked agai...