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检索条件"机构=Chemical Process Modeling and Control Center"
60 条 记 录,以下是31-40 订阅
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Repetitive Model Predictive control using Linear Matrix Inequalities
Repetitive Model Predictive Control using Linear Matrix Ineq...
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2008 American control Conference (ACC), vol.4
作者: Pradeep Y. Tiwari Mayuresh V. Kothare Chemical Process Modeling and Control Center Department of Chemical Engineering Lehigh University Bethlehem PA USA
Repetitive systems can be characterized by two time variables, namely, the finite time within each repeating cycle and the cycle index, each embodying a distinct connotation of time. Conventional optimal control theor... 详细信息
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The Impact of process Diversity on Distillation Column control
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IFAC Proceedings Volumes 1989年 第8期22卷 1-7页
作者: W.L. Luyben Process Modeling and Control Center Department of Chemical Engineering Lehigh University 111 Research Drive Bethlehem PA 18015 USA
The engineering science of distillation column design and control is considered by many academic visionaries to be a mature field that is not worthy of continued research. However, the economic importance of distillat...
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The Value of Simple Multivariable and Nonlinear Models in process control
The Value of Simple Multivariable and Nonlinear Models in Pr...
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American control Conference (ACC)
作者: Christos Georgakis Department of Chemical Engineering and Chemical Process Modeling and Control Research Center Lehigh University Bethlehem PA USA
Simple conceptual or mathematical models have always been used in design of linear SISO process controllers. On the other hand the design of nonlinear or MIMO controllers has always been perceived as requiring a detai... 详细信息
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Nonlinear model predictive control of end-use properties in batch reactors under uncertainty
Nonlinear model predictive control of end-use properties in ...
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European control Conference (ECC)
作者: Jaleel Valappil Christos Georgakis Chemical Process Modeling and Control Research Center and Department of Chemical Engineering Lehigh Univeristy Bethlehem PA USA
There are significant incentives in controlling the end-use properties in batch reactors to reduce the variability in the final product quality specifications. Here we define an approach for controlling the properties... 详细信息
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On-line Estimation of Reaction Rates in Batch Reactors
On-line Estimation of Reaction Rates in Batch Reactors
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American control Conference (ACC)
作者: Guillermo Elicabe Christos Georgakis Chemical Process Modeling and Control Research Center Department of Chemical Engineering Lehigh University Bethlehem PA USA
Very often one needs to know the current values of reaction rates in chemical reactors in order to control them effectively or in order to avoid unsafe operating conditions. ln this work state estimation techniques ar... 详细信息
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Identification of reduced order average linear models from nonlinear dynamic simulations
Identification of reduced order average linear models from n...
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American control Conference (ACC)
作者: W.A. Docter C. Georgakis Chemical Process Modeling and Control Research Center Department of Chemical Engineering Lehigh University Bethlehem PA USA
Presents a general methodology for the identification of average linear low order models (ALLOM) from data collected from detailed nonlinear models. While there are many methods available in the literature for identif... 详细信息
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Nonlinear control Structures for chemical Reactors
Nonlinear Control Structures for Chemical Reactors
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American control Conference (ACC)
作者: R. Donald Bartusiak Christos Georgakis Matthew J. Reilly Chemical Process Modeling and Control Research Center Department of Chemical Engineering Lehigh University Bethlehem PA USA
A nonlinear feedback controller for chemical reaction dynamic systems is examined in which the control action is a function of the deviation of the reaction rate from steady state. The motivations for this controller ... 详细信息
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State estimation and nonlinear model predictive control of end-use properties in batch reactors
State estimation and nonlinear model predictive control of e...
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American control Conference (ACC)
作者: J. Valappil C. Georgakis Chemical Process Modeling and Control Research Center Department of Chemical Engineering Lehigh University Bethlehem PA USA
There are economic incentives in controlling the end-use properties in batch reactors to reduce the variability in the final product quality specifications. Here we define an approach for controlling the properties wi... 详细信息
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Bilinear Identification of Nonlinear processes
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IFAC Proceedings Volumes 1994年 第2期27卷 47-52页
作者: James F. Bartee Christos Georgakis Chemical Process Modeling and Control Research Center Department of Chemical Engineering Lehigh University Bethlehem Pennsylvania USA 18015 Fax: (610)758-5432 Internet
Identification of nonlinear processes using bilinear models is presented. To avoid direct estimation of the bilinear model parameters, a dynamically equivalent input/output model structure is developed through an anal... 详细信息
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Optimal parameter estimation of the Izhikevich single neuron model using experimental Inter-Spike Interval (ISI) data
Optimal parameter estimation of the Izhikevich single neuron...
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作者: Kumar, Gautam Aggarwal, Vikram Thakor, Nitish V. Schieber, Marc H. Kothare, Mayuresh V. Department of Chemical Engineering Chemical Process Modeling and Control Center Lehigh University Bethlehem PA 18015 United States Department of Biomedical Engineering Johns Hopkins University Baltimore MD 21205 United States Department of Neurobiology and Anatomy University of Rochester Medical Center Rochester NY 14627 United States
We propose to use the Izhikevich single neuron model to represent a motor cortex neuron for studying a control-theoretic perspective of a neuroprosthetic system. The problem of estimating model parameters is addressed... 详细信息
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