Partial hydrogenation of benzene to cyclohexene

被引:155
|
作者
Nagahara, H
Ono, M
Konishi, M
Fukuoka, Y
机构
[1] ASAHI CHEM IND CO LTD,TENAC DEV DEPT,KURASHIKI,OKAYAMA 711,JAPAN
[2] ASAHI CHEM IND CO LTD,PETROCHEM INTERMEDIATES DEV DEPT,KURASHIKI,OKAYAMA 711,JAPAN
[3] ASAHI CHEM IND CO LTD,CHEM & CHEM PROC LAB,KURASHIKI,OKAYAMA 711,JAPAN
[4] NOGUCHI INST,ITABASHI KU,TOKYO 173,JAPAN
关键词
partial hydrogenation; cyclohexene; ruthenium catalyst; co-catalyst;
D O I
10.1016/S0169-4332(97)00325-5
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
We (Asahi Chemical Industy Co., Ltd.) have developed a technology for a highly selective partial hydrogenation of benzene to cyclohexene and succeeded in the commercialization of a new production process for producing cyclohexanol from benzene through cyclohexene. The process has been considered to be difficult for a long time in the industry, Several innovative technologies made the partial hydrogenation reaction possible, A catalyst that consists of specific metallic ruthenium particles exhibited excellent high selectivity of cyclohexene, The catalyst was obtained by reducing a ruthenium compound which contains a zinc compound, The use of a zinc salt of strong acid as a co-catalyst exhibited a remarkable effect to enhance selectivity. Dispersing agents of metal oxides were found to extend the life of the metallic ruthenium catalyst and some dispersing agents had the effect of enhancing the selectivity in the partial hydrogenation reaction, One of the remarkable features of the reaction was the reaction field. This comprises four phases: vapor (hydrogen), oil, aqueous and solid (ruthenium catalyst), The catalyst was used in the aqueous phase, and the reactants (benzene and hydrogen) were dissolved in the aqueous phase where the reaction proceeded. Therefore the products and reactants transfer between four phases through dissolution, diffusion and extraction, rendering quick transfer was a very important factor in enhancing reaction selectivity. The catalyst system and the reaction field described above made the selectivity for cyclohexene very high, and a yield of 60% for cyclohexene was obtained. (C) 1997 Elsevier Science B.V.
引用
收藏
页码:448 / 451
页数:4
相关论文
共 50 条
  • [21] Selective hydrogenation of benzene to cyclohexene in a monolithic reactor
    Zhao, D
    Chen, GW
    Yuan, Q
    CHINESE JOURNAL OF CATALYSIS, 2005, 26 (09) : 824 - 828
  • [22] THE SELECTIVE HYDROGENATION OF BENZENE TO CYCLOHEXENE ON PENTAAMMINEOSMIUM(II)
    HARMAN, WD
    TAUBE, H
    JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1988, 110 (23) : 7906 - 7907
  • [23] Partial Hydrogenation of Benzene to Cyclohexene on Ru@XO2 (X = Ti, Zr, or Si)
    Yu, Xue-Lian
    Li, Yan
    Xin, Shuang-Mei
    Yuan, Pei-Qing
    Yuan, Wei-Kang
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (06) : 1961 - 1967
  • [24] Partial hydrogenation of benzene to cyclohexene over supported ruthenium carbonyl cluster-derived catalysts
    Suzuki, K
    Ishida, H
    Nagahara, H
    SCIENCE AND TECHNOLOGY IN CATALYSIS 2002, 2003, 145 : 545 - 546
  • [25] CYCLOHEXENE DECOMPOSITION ON RU(001) AND THE MECHANISM OF BENZENE HYDROGENATION
    FLYNN, DK
    POLTA, JA
    THIEL, PA
    SURFACE SCIENCE, 1987, 185 (1-2) : L497 - L505
  • [26] Ruthenium supported catalysts in selective hydrogenation of benzene to cyclohexene
    Fang, L
    Jing, L
    Jie, X
    PROGRESS IN CHEMISTRY, 2003, 15 (04) : 338 - 343
  • [27] FACILE HETEROGENEOUS CATALYTIC-HYDROGENATION OF BENZENE AND CYCLOHEXENE
    HOLY, NL
    TETRAHEDRON LETTERS, 1977, (42) : 3703 - 3706
  • [28] SELECTIVE HYDROGENATION OF BENZENE TO CYCLOHEXENE WITH ZIRCONIUM HYDRIDE CATALYSTS
    PEZ, GP
    CRISSEY, RK
    JOURNAL OF MOLECULAR CATALYSIS, 1983, 21 (OCT): : 393 - 404
  • [29] Partial hydrogenation of benzene to cyclohexene on a Ru-Zn/m-ZrO2 nanocomposite catalyst
    Wang, JQ
    Wang, YZ
    Zhe, SH
    Qiao, MH
    Li, HX
    Fan, KN
    APPLIED CATALYSIS A-GENERAL, 2004, 272 (1-2) : 29 - 36
  • [30] Partial hydrogenation of benzene: A review
    Hu, SC
    Chen, YW
    JOURNAL OF THE CHINESE INSTITUTE OF CHEMICAL ENGINEERS, 1998, 29 (06): : 387 - 396