Abstract
AbstractTranshydrogenation 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.
Publisher
Springer Science and Business Media LLC
Reference24 articles.
1. Givens EN, Charles PJ, Rosinski EJ (1976) Converting low molecular weight olefins over zeolites. US 3960978
2. Coleman ST (2014) Process for cracking heavy hydrocarbon feed. US 8658023
3. Ward AM, Oprins AM, Housmans THM (2015) Process for the production of light olefins and aromatics from a hydrocarbon feedstock. WO 2015000842
4. OSHA (2014) Petroleum refining process. In: Labor U (ed). OSHA, USA. http://www.osha.gov/dts/osta/otm/otm_iv/otm_iv_2.html
5. Garba MD, Galadima A (2015) Efficiencies of green chemistry metrics in the activities of petroleum refinery process. Int Sci Invest J 4:65–87
Cited by
2 articles.
订阅此论文施引文献
订阅此论文施引文献,注册后可以免费订阅5篇论文的施引文献,订阅后可以查看论文全部施引文献