Heat Integration Improvement for Benzene Hydrocarbons Extraction from Coke-Oven Gas

dc.contributor.author	Tovazhnyanskyy, Leonid Leonidovich	en
dc.contributor.author	Kapustenko, P. O.	en
dc.contributor.author	Ulyev, L.	en
dc.contributor.author	Boldyryev, S. A.	en
dc.date.accessioned	2017-03-09T13:34:56Z
dc.date.available	2017-03-09T13:34:56Z
dc.date.issued	2011
dc.description.abstract	In present work the extraction of benzene hydrocarbons from coke-oven gas on the one column unit is studied. Energy consumption of the investigated plant is defined and disadvantages of existing heat exchangers network are shown. The integrated flexible flowsheet is proposed based on process integration method. It enables to reduce both hot and cold utilities consumption on 2,872 kW with pay back period about 9 months.	en
dc.identifier.citation	Heat Integration Improvement for Benzene Hydrocarbons Extraction from Coke-Oven Gas / L. L. Tovazhnyanskyy [et al.] // Chemical Engineering Transactions. – 2011. – Vol. 25. – P. 153-158.	en
dc.identifier.doi	https://doi.org/10.3303/CET1125026
dc.identifier.uri	https://repository.kpi.kharkov.ua/handle/KhPI-Press/27666
dc.language.iso	en
dc.publisher	The Italian Association of Chemical Engineering	en
dc.title	Heat Integration Improvement for Benzene Hydrocarbons Extraction from Coke-Oven Gas	en
dc.type	Article	en

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