This paper presents the development of a simple model which describes the product quality and production over time of an experimental batch distillation column, including start-up. The model structure is based on a simple physical framework, which is augmented with fuzzy logic. This provides a way to use prior knowledge about the dynamics, which have a general validity, while additional information about the specific column behavior is derived from measured process data. The model framework is applicable for a wide range of columns operating under a certain control policy. The model framework for the particular column under study makes a priori assumptions about the specific behavior superfluous. In addition, a detailed description of the i...
Process modeling with limited experimental data is always a dicult task. It becomes even more dicult...
Takagi-Sugeno fuzzy model is presented as an alternative modeling tool for the molecular distillatio...
The aim of this work is to compare several of the commercial dynamic models for batch distillation a...
This paper presents the development of a simple model which describes the product quality and produc...
This paper presents the development of a simple model which describes the product quality and produc...
The present work describes the development and implementation of fuzzy control algorithms in order t...
Distillation is the process most commonly used in industry to separate chemical mixtures; its applic...
The simulation of batch distillation columns during start-up operations is a very challenging modell...
In this chapter, the analysis and design of a fuzzy observer based on a Takagi-Sugeno model of a bat...
This paper proposes the combined use of a conceptual modeling method and a referential control strat...
Abstract-The dynamic behavior of distillation columns during startup operations have been studied an...
One feature of batch processes that is typically ignored, in the formulation of monitoring and contr...
A robust nonlinear control law is designed to reject unknown feed composition disturbances with over...
Industrial interest in batch distillation has increased significantly in recent years as more batch ...
Automatic control of the flotation process is a difficult task due to the large number of variables ...
Process modeling with limited experimental data is always a dicult task. It becomes even more dicult...
Takagi-Sugeno fuzzy model is presented as an alternative modeling tool for the molecular distillatio...
The aim of this work is to compare several of the commercial dynamic models for batch distillation a...
This paper presents the development of a simple model which describes the product quality and produc...
This paper presents the development of a simple model which describes the product quality and produc...
The present work describes the development and implementation of fuzzy control algorithms in order t...
Distillation is the process most commonly used in industry to separate chemical mixtures; its applic...
The simulation of batch distillation columns during start-up operations is a very challenging modell...
In this chapter, the analysis and design of a fuzzy observer based on a Takagi-Sugeno model of a bat...
This paper proposes the combined use of a conceptual modeling method and a referential control strat...
Abstract-The dynamic behavior of distillation columns during startup operations have been studied an...
One feature of batch processes that is typically ignored, in the formulation of monitoring and contr...
A robust nonlinear control law is designed to reject unknown feed composition disturbances with over...
Industrial interest in batch distillation has increased significantly in recent years as more batch ...
Automatic control of the flotation process is a difficult task due to the large number of variables ...
Process modeling with limited experimental data is always a dicult task. It becomes even more dicult...
Takagi-Sugeno fuzzy model is presented as an alternative modeling tool for the molecular distillatio...
The aim of this work is to compare several of the commercial dynamic models for batch distillation a...