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<article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" article-type="research-article" dtd-version="1.1d1" xml:lang="ru"><front><journal-meta><journal-id journal-id-type="publisher">Вестник нефтегазовой отрасли Казахстана</journal-id><journal-title-group><journal-title>Вестник нефтегазовой отрасли Казахстана</journal-title></journal-title-group><issn publication-format="print">2707-4226</issn><issn publication-format="electronic">2957-806X</issn><publisher><publisher-name>KMG Engineering</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="publisher-id">108984</article-id><article-id pub-id-type="doi">10.54859/kjogi108984</article-id><article-categories><subj-group subj-group-type="heading"><subject></subject></subj-group></article-categories><title-group><article-title>CATALYTIC ISOMERIZATION OF LIGHT ALKANES: THERMODYNAMIC, KINETIC, AND TECHNOLOGICAL ASPECTS</article-title></title-group><contrib-group><contrib contrib-type="author"><name name-style="eastern" xml:lang="kk"><surname>Orazbayev</surname><given-names>Nurkhan Samatuly</given-names></name><bio>&lt;p&gt;магистрант&lt;/p&gt;</bio><email>nurkhan7allmight@gmail.com</email><uri content-type="orcid">https://orcid.org/0009-0000-7097-989X</uri><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author"><name name-style="eastern" xml:lang="kk"><surname>Seitenova</surname><given-names>Gaini Zhumagaliyevna</given-names></name><bio>&lt;p&gt;Candidate of chemical sciences, professor&lt;/p&gt;</bio><email>gainiseitenova@gmail.com</email><uri content-type="orcid">https://orcid.org/0000-0001-6202-3951</uri><xref ref-type="aff" rid="aff-2"/></contrib></contrib-group><aff id="aff-1">Л.Н.Гумилев атындағы Еуразия ұлттық университеті</aff><aff id="aff-2">L.N. Gumilyov Eurasian National University</aff><volume>8</volume><issue>2</issue><history><pub-date date-type="received" iso-8601-date="2026-05-06"><day>06</day><month>05</month><year>2026</year></pub-date><pub-date date-type="accepted" iso-8601-date="2026-05-25"><day>25</day><month>05</month><year>2026</year></pub-date></history><permissions><copyright-statement>Copyright © , Orazbayev N., Seitenova G.</copyright-statement></permissions><abstract>&lt;p&gt;&lt;em&gt;The gradual tightening of environmental standards, combined with growing global demand for environmentally friendly fuels, has significantly increased the importance of cutting-edge technologies in oil refining. In this context, the catalytic isomerization of light alkanes (C&lt;/em&gt;&lt;em&gt;&lt;sub&gt;4&lt;/sub&gt;&lt;/em&gt;&lt;em&gt;-&lt;/em&gt;&lt;em&gt;C&lt;/em&gt;&lt;em&gt;&lt;sub&gt;6&lt;/sub&gt;&lt;/em&gt;&lt;em&gt; fraction) is one of the most strategic processes for improving gasoline quality without increasing the concentration of aromatic hydrocarbons or adding hazardous additives. From a chemical standpoint, this process promotes the structural rearrangement of linear paraffins into corresponding branched isomers, which possess a higher octane rating. This results in a significant improvement in the fuel’s combustion characteristics, while reducing the formation of environmentally harmful emissions.&lt;/em&gt;&lt;/p&gt;&#13;
&lt;p&gt;&lt;em&gt;This review systematically examines the fundamental principles underlying the isomerization of alkanes. Particular attention is given to the reaction mechanism, which proceeds via carbocationic intermediates at acidic catalytic centers, reflecting the classic scheme of acid-catalyzed hydrocarbon transformations. Furthermore, the thermodynamic constraints determining the equilibrium distribution of isomers, as well as the kinetic parameters that determine the reaction rate, product selectivity, and overall process efficiency, are critically analyzed. Particular attention is given to bifunctional catalytic systems, which combine metal and acid functional groups, thereby enabling the simultaneous execution of the hydrogenation-dehydrogenation and backbone isomerization steps. The role of competing side reactions, notably hydrocracking and aromatization, is also addressed due to their influence on product yield and catalyst stability.&lt;/em&gt;&lt;/p&gt;&#13;
&lt;p&gt;&lt;em&gt;Beyond theoretical considerations, this review examines the complexities inherent in real industrial systems. In practice, the attainment of thermodynamic equilibrium is often limited by kinetic constraints, resistance to mass transfer within particles and between phases, as well as by the gradual deactivation of the catalyst due to coke formation or poisoning. These factors require a more detailed understanding of process behavior under industrial operating conditions.&lt;/em&gt;&lt;/p&gt;</abstract><kwd-group xml:lang="en"><kwd>catalytic isomerization, light alkanes, hydroisomerization, bifunctional catalysts, carbocation mechanism, thermodynamic equilibrium, reaction kinetics, zeolite catalysts, catalyst deactivation, octane number enhancement.</kwd></kwd-group></article-meta></front><body></body><back><ref-list><ref id="B1"><label>1.</label><mixed-citation>1.	Wei C. et al. 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