This paper considers the problem of optimal control of the process of going from one stable regime to another in piping the hydrocarbon raw material. We have investigated the influence of the transient period on the dissipation factor of the system, the length of the part of the pipeline, and the difference between the parameters of the initial and final stable regimes with account for the technological limitations set on the control actions and phase variables. The dependence of the optimal transient period on the class and range of permissible control functions, the process parameter, and its initial and final regimes has been analyzed.
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Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 85, No. 1, pp. 123–131, January–February, 2012.
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Aidazade, K.R., Asadova, D.A. Analysis of the regimes of controlling transient processes in pipelines. J Eng Phys Thermophy 85, 131–140 (2012). https://doi.org/10.1007/s10891-012-0630-0
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DOI: https://doi.org/10.1007/s10891-012-0630-0