Optimization of Industrial Processes in Reactors

Abstract:

In the conditions of industrial production many processes of polymerisation are non-stationary. By processes optimization with the regard for such features as basic data it is necessary to use adaptive algorithms of identification, allowing mathematical model of process continuously to be adapted for changing conditions of operation. Use of such algorithms for process optimization demands periodic recalculation of optimum technological modes of process. Polymer reaction engineering is a discipline that deals with various problems concerning the fundamental nature of chemical and physical phenomena in polymerization processes. Mathematical modeling is a powerful tool for the development of process understanding and advanced reactor technology in the polymer industry.

• Periodical: Advanced Materials Research (Volume 717)
• Pages: 613-618
• DOI: https://doi.org/10.4028/www.scientific.net/AMR.717.613
• Online since: July 2013
• Authors: Meruyert Berdiyeva, Aiman Ospanova, Мohamed Othman
• Keywords: Chemical Reactors, Conversion, Industrial Processes, Optimization Problem, Polymerisattion, Technological Parameters - Temperature

References

[1] Shteinberg Sh.E., Shatilov S.V., etc. Continuous forecast and estimation of variable of rotating furnaces of magnesite powder production using adaptive model.-//Industrial ACS and controllers. - №1. pp.75-80,(2000).

[2] Roberts S. Dynamic programming in processes of chemical technology and management methods. М: World,(1965).

[3] Anisimov A.V. Calculation and optimization of chemical reactors. Abstract of lectures. - Moscow, MITCT,. Part 2 –p.72, (2003).

[4] Optimization of technological processes of electronic representation of information by means of a program complex "Monitor EPS". <http://www.sigma-soft.ru/production/manual/eps-common.shtml> (2012).

[5] Ospanova А.О., Identification of styrol polymerization process, Works of international conference «Mathematical methods in engineering and technologies» ММТТ-14, Smolensk, (2001).

[6] Ospanova А.О., Koketayev А.I., Identification of mathematical model of chemical technology processes, Industry of Kazakhstan Nom 3, pp.88-89, (2004).

[7] Ospanova А.О., Koshkinbayeva М.Zh., Yermekbayeva G.Y. Operating modes of chemical reactors of polymerization // Search. Series of natral and engineering sciences. Nom 1. – pp.183-187, (2009).

[8] Stepanov D., Golyandina N. Variants of the method "Gusenitsa"-SSA to forecast multivariate time series.// Works of IV International conference "Identification of systems and control tasks" SICPRO'05. - Moscow,. - pp.1831-1848. – doc (210 kb), (2005).

[9] Myshlyayev L.P. Experiment of identifying industrial objects in control systems, Myshlyayev L.P., Lvova Ye.I., Ivushkin А.А., №6. pp.65-68. (2005).

[10] Myshlyayev L.P. Peculiarities of identification in the systems of controlling industrial objects. Third International conference on issues of control: reports theses in two volumes. Volume 1. М.: Trapeznikov Institute of control issues, RAS,. p.130, (2006).

[11] Trakhtengerts E.А. Computer support of coordination of control solutions, E.А. Trakhtengerts Identification of systems and tasks of control: Works of international conference. М.: Trapeznikov Institute of control issues, RA,. pp.360-422. (2003).

[12] Won Jung Yoon, Yang Soo Kim*, In Sun Kim** and Kyu Yong Choi Recent Advances in Polymer Reaction Engineering: