کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
688750 | 1460368 | 2015 | 9 صفحه PDF | دانلود رایگان |
• A virtual output that is a linear combination of reaction rates should be maximized.
• A bank of super-twisting observers carry out the estimation of the virtual output.
• A weighted super-twisting observer with constant gains is proposed.
• A two-level output feedback controller is proposed to maximize the output.
• The resulting output-feedback controller is tested with simulations of a bioreactor.
In biotechnological processes such as fed-batch reactors the lack of reliable and robust on-line sensors and the limited number of actuators make the task of operating at optimal conditions very difficult. We present a feedback controller that aims at regulating the substrate concentration at an optimum value such that biomass production is enhanced while by-product formation is not favored. We use a virtual output that is estimated using a bank of weighted super-twisting observers to drive an output-feedback extremum-seeking controller. The only online measurements needed are the biomass concentration and the oxygen and carbon dioxide mass transfer rates. Simulations on a fed-batch bioreactor model show its applicability.
Journal: Journal of Process Control - Volume 35, November 2015, Pages 41–49