Study of the Tungstated Alumina Catalysts Deactivation in the Process of Sorbitol Hydrodeoxygenation and Their Regeneration Efficiency Evaluation

被引:1
|
作者
Chumachenko, Yu A. [1 ]
Zotova, A. A. [1 ]
Buluchevskiy, E. A. [1 ]
Gulyaeva, T., I [1 ]
Muromtsev, I., V [1 ]
Trenikhin, M., V [1 ]
机构
[1] Ctr New Chem Technol BIC, 54 Neftezavodskaya Str, Omsk 644040, Russia
来源
关键词
SELECTIVE HYDROGENOLYSIS; HYDROGENATION; BIOMASS; 1,3-PROPANEDIOL; GLYCEROL; ALKANES;
D O I
10.1063/1.5122916
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The properties of catalysts based on tungstated aluminum oxide (WA) with different nature and content of the supported metal (Pt, Pd, Rh, Ru, Ni) in sorbitol hydrodeoxygenation in flow mode at 653 K, 4.0 MPa, weight hourly space velocity (WHSV) of raw materials 1.0 h(-1) for 8 hours were studied. The samples were characterized by N-2 physical adsorption, H-2-TPR, CO chemisorption, TEM, NH3-TPD, XRD and DTA-DTG techniques. On all catalysts, a complete transformation of the substrate is observed with the formation of C-5-C-7 hydrocarbons as main products, which include n-alkanes, cycloalkanes and iso-alkanes. After 1 h of reaction, the yield of C-5-C-7 alkanes increases from 42 to 74 mol. % in the series of catalysts: 5- Ni/WA < 0.5-Ru/WA < 0.5-Pd/WA < 0.5-Rh/WA < 0.5-Pt/WA. The value of the research octane number (RON) of the C-5-C-7 fraction increases from 62 to 80 in the series of samples: 0.5-Pt/WA < 0.5-Pd/WA < 0.5-Rh/WA < 5-Ni/WA < 0.5-Ru/WA. Stable values yield and RON C-5-C-7 fractions (not less than 57.1 mol.% and 70 points, respectively) are achieved on 0.5-Pd/WA catalyst for 8 hours. The main causes of deactivation of all WA-supported catalysts include the formation of carbonaceous deposits and phase transformations of the support in hydrothermal conditions. Oxidative regeneration at a temperature of 973 K contributes to the restoration of textural properties and phase composition of deactivated catalysts. The reduction of the regenerated catalysts at 773 K does not ensure the complete restoration of their dispersion and acidity. For 0.5-Pd/WA catalyst, which is the most stable in hydrodeoxygenation of the sorbitol, the smallest decrease in acidity and dispersion of the supported metal after oxidative regeneration and reduction is observed. The use of methods for the re-dispersion of particles of supported palladium will increase the efficiency of this catalyst.
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页数:13
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  • [1] Hydrodeoxygenation of sorbitol to gasoline-range hydrocarbons over Pt, Pd, Rh, Ru, Ni catalysts supported on tungstated alumina
    Y. A. Chumachenko
    E. A. Buluchevskiy
    E. D. Fedorova
    A. A. Nepomnyashchii
    T. I. Gulyaeva
    M. V. Trenikhin
    R. R. Izmailov
    R. M. Mironenko
    [J]. Biomass Conversion and Biorefinery, 2021, 11 : 1233 - 1243
  • [2] Hydrodeoxygenation of sorbitol to gasoline-range hydrocarbons over Pt, Pd, Rh, Ru, Ni catalysts supported on tungstated alumina
    Chumachenko, Y. A.
    Buluchevskiy, E. A.
    Fedorova, E. D.
    Nepomnyashchii, A. A.
    Gulyaeva, T., I
    Trenikhin, M., V
    Izmailov, R. R.
    Mironenko, R. M.
    [J]. BIOMASS CONVERSION AND BIOREFINERY, 2021, 11 (04) : 1233 - 1243
  • [3] DEACTIVATION AND REGENERATION OF CLAUS PROCESS CATALYSTS
    KOVALEV, VN
    CHEKHOVSKII, VG
    [J]. RUSSIAN JOURNAL OF APPLIED CHEMISTRY, 1993, 66 (11) : 1864 - 1871
  • [4] DEACTIVATION AND REGENERATION OF ALUMINA CATALYSTS FOR THE REARRANGEMENT OF CYCLOHEXANONE OXIME INTO CAPROLACTAM
    CURTIN, T
    MCMONAGLE, JB
    RUWET, M
    HODNETT, BK
    [J]. JOURNAL OF CATALYSIS, 1993, 142 (01) : 172 - 181
  • [5] STUDY OF DEACTIVATION AND REGENERATION OF NOX REDUCTION CATALYSTS
    MATSUOKA, H
    NAKAMURA, H
    TAKEDA, T
    OHSATA, K
    MORI, K
    OCHIAI, Y
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1979, (APR): : 28 - 28
  • [6] Hydrodeoxygenation of Guaiacol over Pd-Co and Pd-Fe Catalysts: Deactivation and Regeneration
    Nga Tran
    Uemura, Yoshimitsu
    Thanh Trinh
    Ramli, Anita
    [J]. PROCESSES, 2021, 9 (03) : 1 - 10
  • [7] STUDY OF THE DEACTIVATION AND REGENERATION OF COPPER CHROMITE ON GAMMA-ALUMINA AND MAGNESIUM CHROMITE ON GAMMA-ALUMINA CATALYSTS FOR FUEL COMBUSTION
    ARENDARSKII, DA
    ISMAGILOV, ZR
    BARANNIK, GB
    [J]. CATALYSIS LETTERS, 1992, 15 (04) : 347 - 351
  • [8] Spectroscopic study on the irreversible deactivation of chromia/alumina dehydrogenation catalysts
    Puurunen, RL
    Weckhuysen, BM
    [J]. JOURNAL OF CATALYSIS, 2002, 210 (02) : 418 - 430
  • [9] Deactivation and regeneration of heterogeneous catalysts in green diesel production by hydrothermal process
    Zhang, Jing
    Ma, Huiling
    Zeng, Defu
    Yao, Xiaoyi
    [J]. Huagong Jinzhan/Chemical Industry and Engineering Progress, 2022, 41 (02): : 682 - 689
  • [10] Deactivation study of the hydrodeoxygenation of p-methylguaiacol over silica supported rhodium and platinum catalysts
    Bouxin, F. P.
    Zhang, X.
    Kings, I. N.
    Lee, A. F.
    Simmons, M. J. H.
    Wilson, K.
    Jackson, S. D.
    [J]. APPLIED CATALYSIS A-GENERAL, 2017, 539 : 29 - 37