Abstract
Mathematical modeling is conducted to determine optimal solutions for systems controlling processes with distributed parameters in an example of the operation of tube furnaces at oil refineries. A mathematical model is proposed for nonstationary combustion with one-dimensional movement of flows. The efficiency function is formulated as the minimum deviation of the temperature of the flow from the assigned value. Numerical modeling is performed for one meter of actual volume of tube furnace. Linear approximation is selected as a mathematical approach.
This is a preview of subscription content, log in via an institution to check access.
Similar content being viewed by others
References
N. D. Demidenko, V. I. Potapov, and Yu. I. Shokin, Modeling and Optimization of Systems with Distributed Parameters [in Russian], Nauka, Novosibirsk (2006).
N. D. Demidenko and L. V. Kulagina, Modeling and Optimization of Technical Systems with Distributed Parameters [in Russian], IPTs Krasnoyarskogo Gosudarstvennogo Tekhnicheskogo Universiteta, Krasnoyarsk (2006).
Author information
Authors and Affiliations
Additional information
__________
Translated from Khimicheskoe i Neftegazovoe Mashinostroenie, No. 6, pp. 15–16, June, 2007.
Rights and permissions
About this article
Cite this article
Kulagina, L.V. Mathematical modeling of control systems for production processes with distributed parameters. Chem Petrol Eng 43, 319–322 (2007). https://doi.org/10.1007/s10556-007-0057-1
Issue Date:
DOI: https://doi.org/10.1007/s10556-007-0057-1