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dc.contributor.authorLarissa Sassykovaen_US
dc.contributor.authorYermek Aubakiroven_US
dc.date.accessioned2019-05-07T09:59:44Z-
dc.date.available2019-05-07T09:59:44Z-
dc.date.issued2018en_US
dc.identifier.issn0125-2526en_US
dc.identifier.urihttp://it.science.cmu.ac.th/ejournal/dl.php?journal_id=8765en_US
dc.identifier.urihttp://cmuir.cmu.ac.th/jspui/handle/6653943832/64043-
dc.description.abstractThe objective of this study was the development of catalysts for catalytic liquid-phase hydrogenation of gasoline fractions of Atyrau Refinery LLP at elevated hydrogen pressure. The selective efficient catalysts on the basis of the platinum metals applied on various carriers are synthesized. The hydrogenation of two gasoline fractions Stable catalysate LH (0.37% benzene), straight-run gasoline AVT (3.18% benzene) was studied. After the catalytic hydrogenation the benzene is absent, the content of aromatic compounds is reduced from 55.12% to 32.5 (wt.). The content of olefins is reduced from 0.23 to 0.11% (wt.) and paraffins content is decreased from 12.41 to 11.99% (wt.), but the amount of isoparaffins increased from 30.08 to 34.09% (wt), naphthene content increased from 2.12 to 10.14% (wt). Octane numbers of petrol fractions after hydrogenation were practically unchanged, while the benzene content decreased from 3.18% (initial sample) to the total absence in the samples.en_US
dc.languageEngen_US
dc.publisherScience Faculty of Chiang Mai Universityen_US
dc.titleCatalytic Hydrogenation of Gasoline Fractions under Elevated Pressureen_US
dc.typeบทความวารสารen_US
article.title.sourcetitleChiang Mai Journal of Scienceen_US
article.volume45en_US
article.stream.affiliationsal-Farabi Kazakh National University, 050040, Almaty, Kazakhstan.en_US
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