Adaptation of methanol synthesis reactor mathematical model

Authors

  • Марина Геннадьевна Лория the Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400, Ukraine
  • Джабран Абдалхамид Technological Institute of East-Ukrainian National University named after Vladimir Dal (c. Severodonetsk) Prospect Soviet 59a, c. Severodonetsk, 93400, Ukraine
  • Алексей Борисович Целищев Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400, Ukraine
  • Петр Иосифович Елисеев Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400, Ukraine
  • Иван Иванович Захаров Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400, Ukraine

DOI:

https://doi.org/10.15587/1729-4061.2013.18863

Keywords:

adaptation, mathematical model, methanol synthesis column, optimal process parameters

Abstract

The development of the adaptation algorithm of the model of complex object on the example of methanol synthesis column is

discussed in the paper. The main objective of the paper is to develop experimental-statistical models. To create such models it is necessary to have the ability of careful research of the control object, as well as collect quite a large amount of experimental material. For complex control objects, it is sometimes difficult to determine the number of influencing factors and their mutual influence. It is not always possible to use active experiment on the working equipment of continuous and large-scale productions. However, this model has a very simple form. It is easy to use in solving the optimization problems. The paper proposes to use a control system with the combined model for managing multi-shelf gas reactor (e.g. methanol synthesis reactor)

Author Biographies

Марина Геннадьевна Лория, the Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400

associate Professor of department of electronic vehicles, k.t.n.

Джабран Абдалхамид, Technological Institute of East-Ukrainian National University named after Vladimir Dal (c. Severodonetsk) Prospect Soviet 59a, c. Severodonetsk, 93400

Postgraduate student of the Department of electronic vehicles

Алексей Борисович Целищев, Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400

associate Professor of department computer - computer-integrated control system, k.t.n.

Петр Иосифович Елисеев, Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400

associate Professor of department of equipment of chemical productions, k.t.n.

Иван Иванович Захаров, Technological institute of the Vostochnoukrainskogo national university of the name of V. Dalya ( Severodonetsk) pr. Soviet, 59a, Severodonetsk, Ukraine, 93400

Professor of department of technology of inorganics, d.t.s.

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Published

2013-12-18

How to Cite

Лория, М. Г., Абдалхамид, Д., Целищев, А. Б., Елисеев, П. И., & Захаров, И. И. (2013). Adaptation of methanol synthesis reactor mathematical model. Eastern-European Journal of Enterprise Technologies, 6(3(66), 4–6. https://doi.org/10.15587/1729-4061.2013.18863

Issue

Vol. 6 No. 3(66) (2013): Control processec

Section

Control processes

License

Copyright (c) 2014 Марина Геннадьевна Лория, Джабран Абдалхамид, Алексей Борисович Целищев, Петр Иосифович Елисеев, Иван Иванович Захаров

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