A robustness study for chemical process control.
スポンサーリンク
概要
- 論文の詳細を見る
Generally, chemical processes behave nonlinearly. But existing well-developed controller design techniques are based on linearized models of nonlinear processes. The neglected nonlinear effects affect the stability of control systems. Robustness degree, a new measure for robust control, is introduced and studied from the engineering point of view. The concept of robustness degree, proposed by applying the semigroup theory of functional analysis, can play a role in analysis and design of control systems. It is a sufficient and quantitative measure of the margin of stability within which certain nonlinear functions and modelling errors can be tolerated. Robustness degree of an open-loop or closed-loop system is linked with system matrix measure as an estimation that is straightforward and easy to calculate. A chemical reactor is studied as an example of robust control system design by this approach.
- The Society of Chemical Engineers, Japanの論文
著者
-
Hashimoto Iori
Department Of Chemical Engineering Kyoto University
-
Ohshima Masahiro
Department Of Chemical Engineering Graduate School Of Engineering Kyoto University
-
Chu Jian
Department of Chemical Engineering, Kyoto University
-
Wang JiCheng
Department of Chemical Engineering, Kyoto University
-
Tanamatsu Takeichiro
Department of Chemical Engineering, Kyoto University
関連論文
- Fabrication of Hollow TiO_2 Fibers Templated by Electrospun Aqueous Poly(ethylene oxide) (PEO) Solution
- SIMULTANEOUS SEPARATION OF LIGHT AND HEAVY IMPURITIES BY A COMPLEX BATCH DISTILLATION COLUMN
- Product Quality Estimation and Operating Condition Monitoring for Industrial Ethylene Fractionator
- Energy Conservation by Multi-Effect Batch Distillation System
- Improvement of Distillation Composition Control by Using Predictive Inferential Control Technique
- SA-Based Scheduling Algorithm for Increasing Probability of Selecting Promising Schedules
- A FLEXIBLE SIMULATION SYSTEM FOR SCHEDULING WITH VARIOUS CONSTRAINTS
- Lactide Bubble Nucleation Rate Model for Degassing in Polylactic Acid Synthesis
- PID Temperature Control of an Unstable Gas-phase Polyolefin Reactor
- Thoracoscopic Findings and Surgical Management of Catamenial Hemopneumothorax
- Stress-Induced Expression of Genes for Pathogenesis-Related Proteins in Plants : ENVIRONMENTAL AND STRESS RESPONSES : GENE STRUCTURE AND EXPRESSION
- Fabrication of hollow N-doped TiO2 photocatalyst by sprayinduced hydrolysis
- Optimization Aspects for Reactive Batch Distillation
- Dielectric Behavior of cis-Polyisoprene in Carbon Dioxide under High Pressure
- Study of energy efficiency of a wetted-wall distillation column with internal heat integration.
- A design method for a class of robust nonlinear observers.
- General Reordering Algorithm for Scheduling of Batch Processes
- ON DESIGN MARGIN FOR PROCESS SYSTEM WITH PARAMETER UNCERTAINTY
- Analyses of the characteristics of a binary packed distillation column with internal heat integration.
- A robustness study for chemical process control.