Contrast activities of four alumina and alumina-silica-supported nickel-molybdenum sulfide catalysts for deep desulfurization of gas oils

被引:24
作者
Kunisada, N
Choi, KH
Korai, Y
Mochida, I [1 ]
Nakano, K
机构
[1] Kyushu Univ, Inst Mat Chem & Engn, Kasuga, Fukuoka 8168580, Japan
[2] Catalysts & Chem Ind Co Ltd, Kitakyushu, Fukuoka 8080027, Japan
关键词
hydrodesulfurization; NiMo catalyst; acidity; gas oil;
D O I
10.1016/j.apcata.2004.10.048
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
Four NiMoS catalysts on conventional alumina (NMA-1), acidified alumina (NMA-2), and on two alumina-silica mixtures of different preparation procedures with 70% (NMASA1 -70) and 50% (NMASA2-50) silica supports were prepared. In HDS and HDN of straight run gas oil (SRGO) and its desulfurized oil (HSRGO), their selective activities toward above reactions were compared since the best combination of two catalysts in two-layer bed was expected to achieve deep HDS of SRGO rather easily. NMA-1 removed reactive sulfur species effectively and refractory sulfur species moderately but failed to remove nitrogen species in SRGO. The catalyst was not effective. to remove. refractory sulfur species in HSRGO to achieve the total sulfur level of less than 10 ppm S in the second layer. NiMoS on acidified alumina (NMA-2) and NMASA 1 -70 removed nitrogen species very effectively but sulfur species in SRGO were not so efficiently removed. Both catalysts were very active for HSRGO to attain 10 ppm sulfur level. Rapid HDN in SRGO over the catalysts appears to retard HDS of SRGO, leaving even reactive sulfur species unreacted. Among the catalysts, NiMoASA2-50 was very active for all reactions to achieve less than 10 ppm from SRGO via two stages. The rapid HDN over the particular catalyst allowed the effective HDS after the rapid completion of HDN. Such contrast activities of four catalysts are compared as regards their surface area, acidity and NiMoS location on the support particles. NiMo on alumina or on the border of acidified alumina and silica of right content is most activated for HDN as well as RDS. Acidity appears essential for HDN. Larger surface area of the particular alumina-silica support is certainly favorable for both RDS and HDN. The larger content of silica in NMASA1-70 may not be favorable for high dispersion of NiMoS to show higher activity for RDS while HDN, progresses. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:235 / 239
页数:5
相关论文
共 11 条
  • [1] Preparation and characterization of nano-sized CoMo/Al2O3 catalyst for hydrodesulfurization
    Choi, KH
    Korai, Y
    Mochida, I
    [J]. APPLIED CATALYSIS A-GENERAL, 2004, 260 (02) : 229 - 236
  • [2] Facile ultra-deep desulfurization of gas oil through two-stage or -layer catalyst bed
    Choi, KH
    Kunisada, N
    Korai, Y
    Mochida, I
    Nakano, K
    [J]. CATALYSIS TODAY, 2003, 86 (1-4) : 277 - 286
  • [3] Hydrodesulfurization of 4,6-DMDBT in the high boiling fraction of gas oil
    Choi, KH
    Korai, Y
    Mochida, I
    [J]. CHEMISTRY LETTERS, 2003, 32 (05) : 434 - 435
  • [4] On the sulfur tolerance of supported Ni(Co)Mo sulfide hydrotreating catalysts
    Hensen, EJM
    de Beer, V
    van Veen, JAR
    van Santen, RA
    [J]. JOURNAL OF CATALYSIS, 2003, 215 (02) : 353 - 357
  • [5] SURFACE-STRUCTURES OF SUPPORTED MOLYBDENUM OXIDE CATALYSTS - CHARACTERIZATION BY RAMAN AND MO L(3)-EDGE XANES
    HU, HC
    WACHS, IE
    BARE, SR
    [J]. JOURNAL OF PHYSICAL CHEMISTRY, 1995, 99 (27) : 10897 - 10910
  • [6] Hydrodesulfurization pathway of 4,6-dimethyldibenzothiophene through isomerization over Y-zeolite containing CoMo/Al2O3 catalyst
    Isoda, T
    Nagao, S
    Ma, XL
    Korai, Y
    Mochida, I
    [J]. ENERGY & FUELS, 1996, 10 (05) : 1078 - 1082
  • [7] Novel zeolite based support for NiMo sulfide in deep HDS of gas oil
    Kunisada, N
    Choi, KH
    Korai, Y
    Mochida, I
    Nakano, K
    [J]. APPLIED CATALYSIS A-GENERAL, 2004, 269 (1-2) : 43 - 51
  • [8] Effective supports to moderate H2S inhibition on cobalt and nickel molybdenum sulfide catalysts in deep desulfurization of gas oil
    Kunisada, N
    Choi, KH
    Korai, Y
    Mochida, I
    [J]. APPLIED CATALYSIS A-GENERAL, 2004, 260 (02) : 185 - 190
  • [9] Deep hydrodesulfurization of diesel fuel: Design of reaction process and catalysts
    Mochida, I
    Sakanishi, K
    Ma, XL
    Nagao, S
    Isoda, T
    [J]. CATALYSIS TODAY, 1996, 29 (1-4) : 185 - 189
  • [10] Influences of nitrogen species on the hydrodesulfurization reactivity of a gas oil over sulfide catalysts of variable activity
    Murti, SDS
    Yang, H
    Choi, KH
    Korai, Y
    Mochida, I
    [J]. APPLIED CATALYSIS A-GENERAL, 2003, 252 (02) : 331 - 346