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A new Lyapunov design method for nonlinear process control
dc.creator | Dubljevic, Stevan | |
dc.date.accessioned | 2012-06-07T23:03:52Z | |
dc.date.available | 2012-06-07T23:03:52Z | |
dc.date.created | 2001 | |
dc.date.issued | 2001 | |
dc.identifier.uri | https://hdl.handle.net/1969.1/ETD-TAMU-2001-THESIS-D82 | |
dc.description | Due to the character of the original source materials and the nature of batch digitization, quality control issues may be present in this document. Please report any quality issues you encounter to digital@library.tamu.edu, referencing the URI of the item. | en |
dc.description | Includes bibliographical references (leaves 42-47). | en |
dc.description | Issued also on microfiche from Lange Micrographics. | en |
dc.description.abstract | The present research work proposes a new nonlinear controller synthesis approach that is based on the methodological principles of Lyapunov design. In particular, it introduces a notion of short-horizon model-based prediction and optimization of the rate of ``energy dissipation'' of the system, as it is realized through the derivative of an appropriately selected control Lyapunov function. The latter is computed by solving Zubov's partial differential equation based on the system's drift vector field. A nonlinear state feedback control law with two adjustable parameters is derived as the solution of an optimization problem, that is formulated on the basis of the aforementioned control Lyapunov function and closed-loop performance characteristics. A set of key properties of the proposed control law is examined. Key properties include continuity, unity static (steady-state) gain in closed-loop, closed-loop internal stability and enlargement of the quadratic closed-loop stability region estimates. The proposed Laypunov design method is evaluated in a representative chemical reactor example which exhibits nonminimum-phase behaviour, and the main design aspects are illustrated through simulation studies. | en |
dc.format.medium | electronic | en |
dc.format.mimetype | application/pdf | |
dc.language.iso | en_US | |
dc.publisher | Texas A&M University | |
dc.rights | This thesis was part of a retrospective digitization project authorized by the Texas A&M University Libraries in 2008. Copyright remains vested with the author(s). It is the user's responsibility to secure permission from the copyright holder(s) for re-use of the work beyond the provision of Fair Use. | en |
dc.subject | chemical engineering. | en |
dc.subject | Major chemical engineering. | en |
dc.title | A new Lyapunov design method for nonlinear process control | en |
dc.type | Thesis | en |
thesis.degree.discipline | chemical engineering | en |
thesis.degree.name | M.S. | en |
thesis.degree.level | Masters | en |
dc.type.genre | thesis | en |
dc.type.material | text | en |
dc.format.digitalOrigin | reformatted digital | en |
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