Asymptotic rejection of nonvanishing disturbances despite plant-model mismatch

2012 ◽  
Vol 26 (12) ◽  
pp. 1090-1110 ◽  
Author(s):  
Ph. Mullhaupt ◽  
S. Valentinotti ◽  
B. Srinivasan ◽  
D. Bonvin
Keyword(s):  
Author(s):  
W Feng ◽  
I Postlethwaite

In robotics, despite considerable effort to minimize system modelling errors, uncertainties are always present and sometimes significant. In this paper, modelling errors are first represented by a class of bounded disturbances in the input channels (torques) of the robot. A measure of the robot system's ability to reject these disturbances is formulated in an L2 gain sense and a control design is subsequently proposed to achieve optimal disturbance rejection. If more detailed information is available on the plant-model mismatch, then the control design can be modified to incorporate an adaptive scheme (with explicit parameter updating laws) in order to reduce the conservativeness of the original design and to improve robust performance of the overall system.


Author(s):  
Jodie M. Simkoff ◽  
Siyun Wang ◽  
Michael Baldea ◽  
Leo H. Chiang ◽  
Ivan Castillo ◽  
...  

2018 ◽  
Vol 51 (18) ◽  
pp. 833-838
Author(s):  
Martand Singhal ◽  
Timm Faulwasser ◽  
Dominique Bonvin

2020 ◽  
Vol 30 (17) ◽  
pp. 7103-7129
Author(s):  
Xiaodong Xu ◽  
Jodie M. Simkoff ◽  
Michael Baldea ◽  
Leo H. Chiang ◽  
Ivan Castillo ◽  
...  

2016 ◽  
Vol 49 (7) ◽  
pp. 25-30 ◽  
Author(s):  
Siyun Wang ◽  
Jodie M. Simkoff ◽  
Michael Baldea ◽  
Leo H. Chiang ◽  
Ivan Castillo ◽  
...  

2016 ◽  
Author(s):  
Maxim Stuckert

This thesis deals with the nonlinear full state observer for distillation processes first introduced by Lang and Gilles in 1990. The observer is very attractive in practice as it requires only few temperature measurements in each section of a distillation column and only few observer parameters need to be tuned. We provide conditions under which this observer converges and derive a simple rule for the tuning of the observer parameters. We also give a method for the on-line estimation of the Murphree tray efficiency. Such on-line methods are rarely found in ­literature. In a sequence of simulation studies, we investigate the capabilities of the observer for the estimation of the tray efficiency and for model-predictive control. The simulation studies are based on distillation processes for separation of multicomponent mixtures and one of the studies introduces a plant-model mismatch. ...


2004 ◽  
Vol 43 (21) ◽  
pp. 6680-6693
Author(s):  
Anthony H. Kamphausen ◽  
John A. O'Donnell
Keyword(s):  

2017 ◽  
Vol 104 ◽  
pp. 5-14 ◽  
Author(s):  
Siyun Wang ◽  
Jodie M. Simkoff ◽  
Michael Baldea ◽  
Leo H. Chiang ◽  
Ivan Castillo ◽  
...  

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