A modified two-phase model is presented to describe the process of gas phase propylene and ethylene copolymerization in a fluidized bed reactor (FBR). Entrainment of solid particles in the FBR is considered in the model, as an improvement to the original two-phase model. Non-linearity of this process makes it difficult to control only by the conventional controllers, such as PID. A hybrid control strategy (a simple designed fuzzy logic controller (FLC) integrated with generic model control (GMC)) was designed to control the reactor temperature. This advanced control system was compared with the GMC and conventional PID controllers. The simulation results showed that the hybrid controller (Fuzzy-GMC) performs better than either GMC or PID fo...
The present work is concerned with the design and experimental testing of a fuzzy control algorithm ...
Two models for the copolymerization of propylene and ethylene in a fluidized bed reactor (FBR) were ...
Butene-1 is produced from ethylene by dimerization reaction in a CSTR. Due to the exothermic reactio...
A modified two-phase model for gas phase propylene and ethylene copolymerization was chosen to repre...
In order to explore the dynamic behavior and process control of reactor temperature, a modified two-...
The control of a gas phase propylene polymerization model in a fluidized bed reactor was studied, wh...
A two-phase dynamic model, describing gas phase propylene polymerization in a fluidized bed reactor,...
Two-phase dynamic model describing gas phase propylene polymerization in a fluidized bed reactor was...
BACKGROUND: Polyethylene (PE) is the most extensively consumed plastic in the world, and gas phase‐...
This paper presents a fuzzy model-based predictive hybrid controller (FMPHC) for polymerization proc...
This work presents the development of a predictive hybrid controller (PHC) based in fuzzy systems fo...
The performances of three advanced non-linear controllers are analyzed for the optimal set point tra...
This study describes the development of a rule-based fuzzy controller for regulating the copolymer c...
Polymer reactors are ideal candidates for the application of fuzzy control. Many polymerization reac...
The worldwide demand for polyolefins has reached more than 140 million tons per year and low-pressur...
The present work is concerned with the design and experimental testing of a fuzzy control algorithm ...
Two models for the copolymerization of propylene and ethylene in a fluidized bed reactor (FBR) were ...
Butene-1 is produced from ethylene by dimerization reaction in a CSTR. Due to the exothermic reactio...
A modified two-phase model for gas phase propylene and ethylene copolymerization was chosen to repre...
In order to explore the dynamic behavior and process control of reactor temperature, a modified two-...
The control of a gas phase propylene polymerization model in a fluidized bed reactor was studied, wh...
A two-phase dynamic model, describing gas phase propylene polymerization in a fluidized bed reactor,...
Two-phase dynamic model describing gas phase propylene polymerization in a fluidized bed reactor was...
BACKGROUND: Polyethylene (PE) is the most extensively consumed plastic in the world, and gas phase‐...
This paper presents a fuzzy model-based predictive hybrid controller (FMPHC) for polymerization proc...
This work presents the development of a predictive hybrid controller (PHC) based in fuzzy systems fo...
The performances of three advanced non-linear controllers are analyzed for the optimal set point tra...
This study describes the development of a rule-based fuzzy controller for regulating the copolymer c...
Polymer reactors are ideal candidates for the application of fuzzy control. Many polymerization reac...
The worldwide demand for polyolefins has reached more than 140 million tons per year and low-pressur...
The present work is concerned with the design and experimental testing of a fuzzy control algorithm ...
Two models for the copolymerization of propylene and ethylene in a fluidized bed reactor (FBR) were ...
Butene-1 is produced from ethylene by dimerization reaction in a CSTR. Due to the exothermic reactio...