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Multistability control in periodically forced catalytic reactor.
| Content Provider | CiteSeerX |
|---|---|
| Author | Gol'Dshtein, Vladimir Panfilov, Vadim |
| Abstract | A novel approach of the chemical reactor stabilization is proposed by using a multistability control. A creation of an additional stable steady state by changing the reactor multiplicity features is a main idea of the multistability control. Proposed approach employs a special type of periodic forced operation, called mediating operation. Mediating operation is able to change a qualitative character of the reactor dynamic behavior, particularly, to produce additional stable steady states in an intermediate temperature area. Feed flow rate is considered as a manipulated variable. Changing of CSTR multiplicity is investigated for two--step control inputs. It is shown that CSTR under two--step control can exhibit at most five steady states having stable intermediate steady state. Two constructive procedures are proposed for finding out control parameters which provide a creation of the stable steady state in selected intermediate area. 1. INTRODUCTION Chemically reacting systems are an ... |
| File Format | |
| Access Restriction | Open |
| Subject Keyword | Multistability Control Periodically Forced Catalytic Reactor Mediating Operation Step Control Additional Stable Steady State Qualitative Character Constructive Procedure Manipulated Variable Reactor Multiplicity Feature Intermediate Area Novel Approach Stable Intermediate Steady State Feed Flow Rate Reactor Dynamic Behavior Stable Steady State Chemical Reactor Stabilization Main Idea Introduction Chemically Cstr Multiplicity Steady State Control Parameter Periodic Forced Operation Special Type Intermediate Temperature Area |
| Content Type | Text |
