Transhydrogenation of pentane with 1,5- and 2,4-hexadiene over CrOx/Al2O3

IF 0.125
Mustapha D. Garba, S. David Jackson
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引用次数: 2

Abstract

Transhydrogenation of pentane (P) and 1,5-hexadiene (1,5HD) and pentane and 2,4-hexadiene (2,4HD) was studied over a CrOx/alumina catalyst at 523–773?K. Thermodynamic stability differences between the conjugated (2,4-hexadiene) and non-conjugated (1,5-hexadiene) isomers indicated that transhydrogenation was favoured between pentane and 1,5-hexadiene but not pentane and 2,4-hexadiene (+?ve ?G). At 773?K a significantly enhanced alkene yield was observed for the P/1,5HD system, clearly showing the effect of transhydrogenation. The yield of alkenes was?~?50% and included alkylated and isomerized alkenes. Alkylation and isomerization were significant reactions under reaction conditions. Pentane was shown to affect the chemistry of 1,5HD and vice versa with the conversion of pentane significantly enhanced at all reaction temperatures, indicating a molecular interaction between the reactants even when transhydrogenation was not obvious. In contrast, no effect on the conversion of pentane was observed when the co-feed was 2,4HD. An unexpected effect of pentane on 2,4HD conversion was observed, with all reactions of cis-2,4-hexadiene (including alkylation and isomerization) being completely inhibited at low reaction temperatures (573?K and 523?K) by the presence of pentane, suggesting that pentane competes for the same sites as cis-2,4-hexadiene. Transhydrogenation activity between pentane and 1,5-hexadiene was less obvious at the lower reaction temperature, which appeared to be a kinetic effect. Direct hydrogenation of 1,5-hexadiene revealed that 1,5HD sampled the same hydrogen population for hydrogenation and transhydrogenation. Comparisons of transhydrogenation of 1-hexyne, 1,5-hexadiene, and 2,4-hexadiene with pentane have revealed significant differences in the adsorption and reaction chemistry of the three isomers.

Abstract Image

戊烷与1,5-和2,4-己二烯在CrOx/Al2O3上的转氢化反应
研究了戊烷(P)和1,5-己二烯(1,5hd)以及戊烷和2,4-己二烯(2,4hd)在CrOx/氧化铝催化剂上在523 - 773k下的转氢化反应。共轭(2,4-己二烯)和非共轭(1,5-己二烯)异构体的热力学稳定性差异表明,戊烷和1,5-己二烯之间容易发生转氢化反应,而戊烷和2,4-己二烯(+?ve ? G)。在773年?P/ 1,5hd体系的烯烃产率显著提高,表明了转氢化反应的作用。烯烃产率为?~?50%,包括烷基化和异构化烯烃。烷基化和异构化是反应条件下的重要反应。戊烷会影响1,5hd的化学性质,反之亦然,在所有反应温度下,戊烷的转化率都显著提高,表明即使在转氢化不明显的情况下,反应物之间也存在分子相互作用。相比之下,共进料为2,4hd时,对戊烷的转化率没有影响。戊烷对2,4hd转化有意想不到的影响,在低反应温度下(573?K和523?K)的存在,表明戊烷与顺式2,4-己二烯竞争相同的位点。在较低的反应温度下,戊烷与1,5-己二烯的转氢化反应活性不明显,这可能是一种动力学效应。1,5-己二烯的直接加氢表明,1,5hd在加氢和转氢化过程中获得了相同的氢族。比较了1-己炔、1,5-己二烯和2,4-己二烯与戊烷的转氢化反应,揭示了三种异构体在吸附和反应化学上的显著差异。
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来源期刊
Applied Petrochemical Research
Applied Petrochemical Research ENGINEERING, CHEMICAL-
自引率
0.00%
发文量
0
审稿时长
13 weeks
期刊介绍: Applied Petrochemical Research is a quarterly Open Access journal supported by King Abdulaziz City for Science and Technology and all the manuscripts are single-blind peer-reviewed for scientific quality and acceptance. The article-processing charge (APC) for all authors is covered by KACST. Publication of original applied research on all aspects of the petrochemical industry focusing on new and smart technologies that allow the production of value-added end products in a cost-effective way. Topics of interest include: • Review of Petrochemical Processes • Reaction Engineering • Design • Catalysis • Pilot Plant and Production Studies • Synthesis As Applied to any of the following aspects of Petrochemical Research: -Feedstock Petrochemicals: Ethylene Production, Propylene Production, Butylene Production, Aromatics Production (Benzene, Toluene, Xylene etc...), Oxygenate Production (Methanol, Ethanol, Propanol etc…), Paraffins and Waxes. -Petrochemical Refining Processes: Cracking (Steam Cracking, Hydrocracking, Fluid Catalytic Cracking), Reforming and Aromatisation, Isomerisation Processes, Dimerization and Polymerization, Aromatic Alkylation, Oxidation Processes, Hydrogenation and Dehydrogenation. -Products: Polymers and Plastics, Lubricants, Speciality and Fine Chemicals (Adhesives, Fragrances, Flavours etc...), Fibres, Pharmaceuticals.
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