In this paper we consider the robustly stabilizing control of a 10001 draft tube baffled crystallizer. When operated at high fines dissolution rates, the crystallizer exhibits sustained oscillations. A detailed population balance model for the process can be found in the literature. Based on this detailed model we develop a simpler population balance model. This, in turn, permits the derivation of an irrational transfer function from manipulated to measured variable. An H-infinity mixed sensitivity minimization problem is formulated and solved using an infinite-dimensional version of H-infinity theory. Two different controllers are designed and compared in simulation studies
Crystallization is the most important purification process in the pharmaceutical industry. In additi...
This work focuses on the application of high resolution finite volume schemes for the solution of mu...
In this article a new approach to the control of batch crystallization is presented. In batch coolin...
In this paper we consider the robustly stabilizing control of a 10001 draft tube baffled crystallize...
Robustly stabilizing control of an open loop oscillatory crystallization process is considered. The ...
Industrial crystallization plants can be operated in basically two different ways: continuous or bat...
Robustly stabilizing control of an open loop oscillatory crystallization process is considered. The ...
In industrial crystallization, fines dissolution is used to improve crystalsize distribution (CSD) p...
In this contribution, a detailed model for a continuous crystallizer with fines dissolution is deriv...
In this contribution, we investigate feedforward control synthesis for a batch cooling crystalliser ...
In this contribution, a detailed model for a continuous crystallizer with fines dissolution is deriv...
This paper presents an output feedback nonlinear model-based control approach for optimal operation ...
Batch crystallization is extensively employed in the chemical, pharmaceutical, and food industries t...
The problem of nonlinear optimal (H-infinity) control for the industrial crystallization process is ...
This article is concerned with the numerical approximations of population balance equations for mode...
Crystallization is the most important purification process in the pharmaceutical industry. In additi...
This work focuses on the application of high resolution finite volume schemes for the solution of mu...
In this article a new approach to the control of batch crystallization is presented. In batch coolin...
In this paper we consider the robustly stabilizing control of a 10001 draft tube baffled crystallize...
Robustly stabilizing control of an open loop oscillatory crystallization process is considered. The ...
Industrial crystallization plants can be operated in basically two different ways: continuous or bat...
Robustly stabilizing control of an open loop oscillatory crystallization process is considered. The ...
In industrial crystallization, fines dissolution is used to improve crystalsize distribution (CSD) p...
In this contribution, a detailed model for a continuous crystallizer with fines dissolution is deriv...
In this contribution, we investigate feedforward control synthesis for a batch cooling crystalliser ...
In this contribution, a detailed model for a continuous crystallizer with fines dissolution is deriv...
This paper presents an output feedback nonlinear model-based control approach for optimal operation ...
Batch crystallization is extensively employed in the chemical, pharmaceutical, and food industries t...
The problem of nonlinear optimal (H-infinity) control for the industrial crystallization process is ...
This article is concerned with the numerical approximations of population balance equations for mode...
Crystallization is the most important purification process in the pharmaceutical industry. In additi...
This work focuses on the application of high resolution finite volume schemes for the solution of mu...
In this article a new approach to the control of batch crystallization is presented. In batch coolin...