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Reactive Distillation Columns A thesis submitted to the University of Manchester Institute of Science and Technology for the degree of Doctor of Philosophy by Ramona Manuela DRAGOMIR under the supervision of Dr. Megan JOBSON and Prof. Robin SMITH Department of Process Integration Manchester, United Kingdom March File Size: 1MB This thesis addresses robust control of distillation columns in the face of model-plant mismatch caused by model uncertainty, nonlinearity and changes in operating conditions. The robust control paradigm, introduced by Doyle and coworkers, is used Author: Sigurd Skogestad Distillation Design - University of Utah
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This thesis addresses robust control of distillation columns in the face of model-plant mismatch caused by model uncertainty, nonlinearity and changes in operating conditions. The robust control paradigm, introduced by Doyle and coworkers, is used Author: Sigurd Skogestad Distillation Design - University of Utah · This thesis addresses different aspects of the dynamic behavior as well as control of distillation columns. It is shown that simple distillation columns, even with ideal vapor-liquid equilibrium, may have multiple steady- state solutions and unstable operating points. Two fundamentally different sources for the multiplicity and instability are presented. The dynamics
Reactive Distillation Columns A thesis submitted to the University of Manchester Institute of Science and Technology for the degree of Doctor of Philosophy by Ramona Manuela DRAGOMIR under the supervision of Dr. Megan JOBSON and Prof. Robin SMITH Department of Process Integration Manchester, United Kingdom March File Size: 1MB This thesis addresses robust control of distillation columns in the face of model-plant mismatch caused by model uncertainty, nonlinearity and changes in operating conditions. The robust control paradigm, introduced by Doyle and coworkers, is used Author: Sigurd Skogestad · This thesis addresses different aspects of the dynamic behavior as well as control of distillation columns. It is shown that simple distillation columns, even with ideal vapor-liquid equilibrium, may have multiple steady- state solutions and unstable operating points. Two fundamentally different sources for the multiplicity and instability are presented. The dynamics
· This thesis addresses different aspects of the dynamic behavior as well as control of distillation columns. It is shown that simple distillation columns, even with ideal vapor-liquid equilibrium, may have multiple steady- state solutions and unstable operating points. Two fundamentally different sources for the multiplicity and instability are presented. The dynamics Distillation column is where the process of distillation occurs. Kaushik () claims that in a distillation column, the more volatile or lighter components are removed from the top of the column, and the less volatile or heavier components are removed from the lower part of File Size: 2MB This thesis addresses robust control of distillation columns in the face of model-plant mismatch caused by model uncertainty, nonlinearity and changes in operating conditions. The robust control paradigm, introduced by Doyle and coworkers, is used Author: Sigurd Skogestad
· This thesis addresses different aspects of the dynamic behavior as well as control of distillation columns. It is shown that simple distillation columns, even with ideal vapor-liquid equilibrium, may have multiple steady- state solutions and unstable operating points. Two fundamentally different sources for the multiplicity and instability are presented. The dynamics Distillation column is where the process of distillation occurs. Kaushik () claims that in a distillation column, the more volatile or lighter components are removed from the top of the column, and the less volatile or heavier components are removed from the lower part of File Size: 2MB Reactive Distillation Columns A thesis submitted to the University of Manchester Institute of Science and Technology for the degree of Doctor of Philosophy by Ramona Manuela DRAGOMIR under the supervision of Dr. Megan JOBSON and Prof. Robin SMITH Department of Process Integration Manchester, United Kingdom March File Size: 1MB
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