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ISSN 00125008, Doklady Chemistry, 2015, Vol. 461, Part 1, pp. 89–92. © Pleiades Publishing, Ltd., 2015. Original Russian Text © G.M. Ostrovskii, N.N. Ziyatdinov, I.I. Emel’yanov, 2015, published in Doklady Akademii Nauk, 2015, Vol. 461, No. 2, pp. 189–192. CHEMICAL TECHNOLOGY Synthesis of Optimal Systems of Simple Distillation Columns with Heat Recovery a b b G. M. Ostrovskii , N. N. Ziyatdinov , and I. I. Emel’yanov Presented by Academician A. Yu. Tsivadze October 27, 2014 Received May 12, 2014 DOI: 10.1134/S0012500815030052 Industrial processes of multicomponent distillation we will design the optimal system of heat exchange of are highly energyintensive, and, as a consequence, streams in the designed SDC. the total reduced cost of separation of mixtures of sub Let us assume that we have designed the optimal stances is largely determined by economic parameters SDC without taking into account heat recovery. In [1]. Moreover, the energy cost in distillation processes each of the distillation columns, we know the amount constitutes 80–90% of the total energy cost in the of heat that should be withdrawn from the stream ΔQ chemical and petrochemical industries [2]. Therefore, S from the top of the ith distillation column for this the development of
Doklady Chemistry – Springer Journals
Published: Apr 21, 2015
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