Modeling Of Multicomponent Rectification Under Uncertainty

Authors

Nodirbek Rustambekovich Yusupbekov, Tashkent State Technical University, Address: 2 Universitetskaya st., 100095, Tashkent city, Republic of UzbekistanFollow
Djalol Patxiddinovich Mukhitdinov, Tashkent State Technical University, Address: 2 Universitetskaya st., 100095, Tashkent city, Republic of Uzbekistan
Yorkin Bakhodirovich Kadirov, Doctor of Philosophy of Technical Sciences (PhD), Department of Automation and Control, Navoi State Mining Institute, Navoiy city, Republic of Uzbekistan, Тел:+998913382922.Follow

Abstract

This paper presents a complete computer model for an industrial distillation column, which considers the input, output and model (nonlinearity and high-frequency dynamics of the process) uncertainties. The proposed model has a great advantage of covering the entire working range of the distillation column. This model can be used as a main tool for the analysis and synthesis of distillation process control systems.

First Page

37

Last Page

42

References

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Recommended Citation

Yusupbekov, Nodirbek Rustambekovich; Mukhitdinov, Djalol Patxiddinovich; and Kadirov, Yorkin Bakhodirovich (2019) "Modeling Of Multicomponent Rectification Under Uncertainty," Chemical Technology, Control and Management: Vol. 2019: Iss. 5, Article 5.
DOI: https://doi.org/10.34920/2019.6.37-42