In this dissertation, the design procedures of four typical decentralized PI/PID controller design methods: the biggest log modulus tuning (BLT) method, the gain and phase margin (GPM) method, the internal model control (IMC) method and the effective relative gain array (ERGA) method, are revisited first, and then implemented to ten different distillation systems that vary from two-input two-output systems up to four-input four-output systems.Master of Science (Computer Control and Automation
Detailed dynamic simulations of three industrial distillation columns (a propylene/propane splitter,...
New methods of designing Fractional Order PID (FOPID) controllers are developed for regulating produ...
Distillation column is a multi-input multi-output system, used especially in petrochemical industrie...
In this dissertation, the design procedures of four typical decentralized PI/PID controller design m...
This dissertation presents three decentralized control systems for the three distillation systems in...
Control methodologies to cope with multivariable process systems are studied in this thesis. Topics ...
its remarkable effectiveness and simplicity of This paper presents one of the simplest method to tun...
86 p.PID controllers are the most widely used controllers in today's industrial control applications...
This dissertation presents sparse control system design method which is based on the concept of ener...
The rapid growth in the complexity of modern process plants both in terms of material flow and energ...
Decentralized PID control has been extensively used in process industry due to its functional simpli...
The reversed frame normalizing design technique of Y.S. Hung and A.G.F. Mac Farlane (1982) is modifi...
A new method of centralized PI/PID control system synthesis for TITO processes using the non-convent...
Detailed dynamic simulations of three industrial columns (a propylene/propane splitter, a xylene/tol...
This thesis presents a decentralized PI/PID controller design scheme for Multi-Input Multi-Output (M...
Detailed dynamic simulations of three industrial distillation columns (a propylene/propane splitter,...
New methods of designing Fractional Order PID (FOPID) controllers are developed for regulating produ...
Distillation column is a multi-input multi-output system, used especially in petrochemical industrie...
In this dissertation, the design procedures of four typical decentralized PI/PID controller design m...
This dissertation presents three decentralized control systems for the three distillation systems in...
Control methodologies to cope with multivariable process systems are studied in this thesis. Topics ...
its remarkable effectiveness and simplicity of This paper presents one of the simplest method to tun...
86 p.PID controllers are the most widely used controllers in today's industrial control applications...
This dissertation presents sparse control system design method which is based on the concept of ener...
The rapid growth in the complexity of modern process plants both in terms of material flow and energ...
Decentralized PID control has been extensively used in process industry due to its functional simpli...
The reversed frame normalizing design technique of Y.S. Hung and A.G.F. Mac Farlane (1982) is modifi...
A new method of centralized PI/PID control system synthesis for TITO processes using the non-convent...
Detailed dynamic simulations of three industrial columns (a propylene/propane splitter, a xylene/tol...
This thesis presents a decentralized PI/PID controller design scheme for Multi-Input Multi-Output (M...
Detailed dynamic simulations of three industrial distillation columns (a propylene/propane splitter,...
New methods of designing Fractional Order PID (FOPID) controllers are developed for regulating produ...
Distillation column is a multi-input multi-output system, used especially in petrochemical industrie...