2006 AIChE Annual Meeting
(146f) Output Feedback Control of Nonlinear Systems Subject to Constraints and Asynchronous Measurements
Authors
When explicitly considered, this problem of intermittent availability of measurements (asynchronous measurements) can be analyzed as a robustness property. Specifically, for a given stabilizing control law, a bound on the sensor data loss rate is computed such that if the sensor data loss rate is within this bound, closed-loop stability is preserved. For unconstrained systems, such a bound for the data loss rate can be defined over an infinite time interval (e.g., see [4,5] and the references therein). For constrained systems, however, a data loss rate defined over an infinite time interval does not allow for the computation of such a bound. The robustness characterization is further complicated when not all the states are measured. Even with continuous measurements, the unavailability of some of the states as measurements necessitates the design of appropriate state estimators and analyzing the closed-loop system comprising the system, the state estimates and the controller to establish closed-loop stability. The intermittent loss of measurements necessitates redesigning the state estimation scheme and accounting for the asynchronous nature of the measurements in analyzing the closed-loop system.
Motivated by the above, in this work we consider the problem of output-feedback control of constrained nonlinear systems under asynchronous measurements. To clearly elucidate our approach, we first consider the state-feedback problem and characterize the robustness property of the closed-loop system under asynchronous measurements. Then, we devise an estimation scheme under asynchronous measurements and characterize the stability properties of the closed-loop system, quantifying the relationship between the controller and the estimation parameters and the maximum allowable data-loss rate that the closed-loop system can tolerate for the time over which the data-loss rate is defined. The proposed approach is illustrated using a chemical process example and then demonstrated on a polyethylene reactor.
References
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