TY - JOUR
T1 - Data-Driven Modeling of a Pilot Plant Batch Reactor and Validation of a Nonlinear Model Predictive Controller for Dynamic Temperature Profile Tracking
AU - Yadav, Eadala Sarath
AU - Shettigar J, Prajwal
AU - Poojary, Sushmitha
AU - Chokkadi, Shreesha
AU - Jeppu, Gautham
AU - Indiran, Thirunavukkarasu
N1 - Funding Information:
The authors would like to express gratitude to the Manipal Academy of Higher Education (MAHE) for the seed money grant toward the batch reactor experimental setup under Grant ID: 00000220 dated 1/1/2020. We express our sincere gratitude to Prof. Dr. J. Prakash, Anna University, Chennai, for giving us right steering with technical inputs on the batch reactor.
Publisher Copyright:
©
PY - 2021/7/6
Y1 - 2021/7/6
N2 - Batch process plays a very crucial and important role in process industries. The increased operational flexibility and trend toward high-quality, low-volume chemical production has put more emphasis on batch processing. In this work, nonlinearities associated with the batch reactor process have been studied. ARX and NARX models have been identified using open-loop data obtained from the pilot plant batch reactor. The performance of the batch reactor with conventional linear controllers results in aggressive manipulated variable action and larger energy consumption due to its inherent nonlinearity. This issue has been addressed in the proposed work by identifying the nonlinear model and designing a nonlinear model predictive controller for a pilot plant batch reactor. The implementation of the proposed method has resulted in smooth response of the manipulated variable as well as reactor temperature on both simulation and real-time experimentation.
AB - Batch process plays a very crucial and important role in process industries. The increased operational flexibility and trend toward high-quality, low-volume chemical production has put more emphasis on batch processing. In this work, nonlinearities associated with the batch reactor process have been studied. ARX and NARX models have been identified using open-loop data obtained from the pilot plant batch reactor. The performance of the batch reactor with conventional linear controllers results in aggressive manipulated variable action and larger energy consumption due to its inherent nonlinearity. This issue has been addressed in the proposed work by identifying the nonlinear model and designing a nonlinear model predictive controller for a pilot plant batch reactor. The implementation of the proposed method has resulted in smooth response of the manipulated variable as well as reactor temperature on both simulation and real-time experimentation.
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U2 - 10.1021/acsomega.1c00087
DO - 10.1021/acsomega.1c00087
M3 - Article
AN - SCOPUS:85110949018
SN - 2470-1343
VL - 6
SP - 16714
EP - 16721
JO - ACS Omega
JF - ACS Omega
IS - 26
ER -