The study of design and performance improvement of catalysts for the stepwise production of bicyclohexane from benzene and cyclohexene

Q3 Energy 燃料化学学报 Pub Date : 2024-09-01 DOI:10.1016/S1872-5813(24)60457-3
LIU Ruilin , WANG Sen , MENG Fanchun , LI Zhuo , YANG Huimin , ZHAO Shichao , QIN Yong , ZHANG Bin
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Abstract

Bicyclohexane is a hydrogen storage reagent with high hydrogen density and low boiling point. Compared with the hydrogenation of biphenyl, the alkylation of benzene and cyclohexene to cyclohexylbenzene and hydrogenation is a promising way to prepare cyclohexane on a large scale. The research and development of high-efficiency cyclohexyl benzene hydrogenation catalyst should be further developed based on mature alkylation technology. This paper used an acidified USY molecular sieve to catalyze the alkylation of benzene and cyclohexene to cyclohexylbenzene, which achieved 100% conversion and selectivity. Furthermore, Pt/TiO2/γ-Al2O3 catalyst is prepared by pre-deposition TiO2 film of different thicknesses on γ-Al2O3 surface and then supported with platinum particles by Atomic layer deposition (ALD). The role of TiO2 film in improving the cyclohexylbenzene hydrogenation performance of the catalyst is studied. TEM, CO pulse chemisorption, CO-DRIFTs, quasi-in situ XPS, H-D exchange, and H2-TPR characterization show that compared with Pt/γ-Al2O3, TiO2 thin films on Pt/TiO2/γ-Al2O3 do not change the dispersion of Pt particles, but can form new Pt-TiO2 interactions. The hydrogenation performance of cyclohexylbenzene was improved by increasing the electron density and the proportion of planar active sites on the surface of platinum and reducing the energy barrier of hydrogen spillover. The research provides theoretical support for further bicyclohexane organic liquid hydrogen storage reagent development. The relevant metal-support interaction regulation strategy can be applied to the development of efficient catalysts for other aromatic molecules hydrogenation.

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从苯和环己烯分步生产双环己烷催化剂的设计和性能改进研究
双环己烷是一种氢密度高、沸点低的储氢试剂。与联苯加氢相比,苯和环己烯烷基化为环己基苯再加氢是一种很有前途的大规模制备环己烷的方法。应在成熟的烷基化技术基础上,进一步研发高效环己基苯加氢催化剂。本文采用酸化 USY 分子筛催化苯和环己烯烷基化为环己基苯,其转化率和选择性均达到 100%。此外,铂/TiO2/γ-Al2O3 催化剂的制备方法是在 γ-Al2O3 表面预沉积不同厚度的 TiO2 薄膜,然后用原子层沉积(ALD)法支撑铂颗粒。研究了 TiO2 膜在改善催化剂环己基苯加氢性能方面的作用。TEM、CO 脉冲化学吸附、CO-DRIFTs、准原位 XPS、H-D 交换和 H2-TPR 表征表明,与 Pt/γ-Al2O3 相比,Pt/TiO2/γ-Al2O3 上的 TiO2 薄膜不会改变铂粒子的分散性,但能形成新的 Pt-TiO2 相互作用。通过增加铂表面的电子密度和平面活性位点比例,降低氢溢出的能量势垒,环己基苯的氢化性能得到了改善。该研究为进一步开发双环己烷有机液态储氢试剂提供了理论支持。相关的金属-支撑相互作用调控策略可应用于其他芳香分子加氢的高效催化剂开发。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
燃料化学学报
燃料化学学报 Chemical Engineering-Chemical Engineering (all)
CiteScore
2.80
自引率
0.00%
发文量
5825
期刊介绍: Journal of Fuel Chemistry and Technology (Ranliao Huaxue Xuebao) is a Chinese Academy of Sciences(CAS) journal started in 1956, sponsored by the Chinese Chemical Society and the Institute of Coal Chemistry, Chinese Academy of Sciences(CAS). The journal is published bimonthly by Science Press in China and widely distributed in about 20 countries. Journal of Fuel Chemistry and Technology publishes reports of both basic and applied research in the chemistry and chemical engineering of many energy sources, including that involved in the nature, processing and utilization of coal, petroleum, oil shale, natural gas, biomass and synfuels, as well as related subjects of increasing interest such as C1 chemistry, pollutions control and new catalytic materials. Types of publications include original research articles, short communications, research notes and reviews. Both domestic and international contributors are welcome. Manuscripts written in Chinese or English will be accepted. Additional English titles, abstracts and key words should be included in Chinese manuscripts. All manuscripts are subject to critical review by the editorial committee, which is composed of about 10 foreign and 50 Chinese experts in fuel science. Journal of Fuel Chemistry and Technology has been a source of primary research work in fuel chemistry as a Chinese core scientific periodical.
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