Effect of the Composition of the Medium on the Selectivity of Deactivation of Skeletal Nickel Catalyst

被引:0
|
作者
A. F. Afineevskii
M. V. Lukin
D. A. Prozorov
机构
[1] Ivanovo State University of Chemical Technology,Research Institute of Chemical Thermodynamics and Kinetics
来源
关键词
liquid-phase hydrogenation; adsorption complex; catalytic activity; catalytic poison;
D O I
暂无
中图分类号
学科分类号
摘要
The effect of the composition of the catalytic system (the nature and composition of the solvent, specifically, aqueous solutions of sodium hydroxide and their mixtures with aliphatic alcohols with the alcohol concentration of 0.11 mole fractions) and additions of a catalyst poison (sodium sulfide) on the catalytic activity of skeletal nickel in the liquid-phase hydrogenation of the carbon‒carbon double bond in sodium maleate was studied. The assumption was made on the decisive role of the solvent in changing the activity of skeletal nickel in the hydrogenation reaction of sodium maleate, which is primarily associated with the redistribution of individual forms of adsorbed hydrogen. In was found that in the water‒sodium hydroxide‒monohydric alcohol solvent skeletal nickel undergoes selective deactivation at the NaOH concentration of 0.01 M, antiselective deactivation at the NaOH concentration of 0.10 M, and variable deactivation at the NaOH concentration of 1.0 M. It is shown that in some cases sodium sulfide additions exert a promoting effect on skeletal nickel in the hydrogenation of sodium maleate.
引用
收藏
页码:1976 / 1980
页数:4
相关论文
共 50 条
  • [41] Deactivation and selectivity: The effect of hydrogen concentration in propyne hydrogenation over a silica-supported palladium catalyst.
    Lennon, D
    Kennedy, DR
    Webb, G
    Jackson, SD
    CATALYST DEACTIVATION 1999, 1999, 126 : 341 - 348
  • [42] Deactivation of industrial alumina catalyst for the skeletal isomerization of n-butenes
    Lamberov A.A.
    Mukhambetov I.N.
    Zalyaliev R.F.
    Catalysis in Industry, 2014, 6 (2) : 128 - 133
  • [43] Selectivity and deactivation of diffusion-limited reactions in a pore-fractal catalyst
    Sheintuch, M
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (09) : 3261 - 3269
  • [44] Selectivity and deactivation of diffusion-limited reactions in a pore- fractal catalyst
    Sheintuch, Moshe
    Industrial and Engineering Chemistry Research, 1999, 38 (09): : 3261 - 3269
  • [45] EFFECT OF TEMPERATURE OF THE DEACTIVATION OF PLATINUM CATALYST BY LEAD
    LAMYPITARA, E
    ALFATIMI, B
    BARBIER, J
    JOURNAL DE CHIMIE PHYSIQUE ET DE PHYSICO-CHIMIE BIOLOGIQUE, 1992, 89 (10) : 2045 - 2055
  • [46] THE EFFECT OF FEEDSTOCK ADDITIVES ON FCC CATALYST DEACTIVATION
    HUGHES, R
    HUTCHINGS, G
    KOON, CL
    MCGHEE, B
    SNAPE, CE
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1995, 210 : 50 - PETR
  • [47] Effect of catalyst deactivation on mild hydrocracking reactions
    Tailleur, RG
    COMPUTERS & CHEMICAL ENGINEERING, 2005, 29 (11-12) : 2404 - 2419
  • [48] Catalyst Deactivation of a Monoligated CyJohnPhos-Bound Nickel(0) Complex
    Newman-Stonebraker, Samuel H.
    Raab, T. Judah
    Doyle, Abigail G.
    ORGANOMETALLICS, 2023, 42 (24) : 3438 - 3441
  • [49] DEACTIVATION OF BIMODAL NICKEL-CATALYST FOR STEAM METHANE REFORMING REACTION
    NUMAGUCHI, T
    KIKUCHI, K
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (03) : 447 - 453
  • [50] Microkinetic deactivation studies on nickel supported catalyst for dry reforming of methane
    Fu, P. R. K.
    Twaiq, F.
    Chung, W. L.
    INTERNATIONAL CONFERENCE ON ADVANCED MANUFACTURING AND INDUSTRY APPLICATIONS, 2018, 429