On the structure and hydrotreating performance of carbon-supported CoMo- and NiMo-sulfides

被引:55
作者
Dugulan, A. I. [1 ]
van Veen, J. A. R. [2 ,3 ]
Hensen, E. J. M. [2 ]
机构
[1] Delft Univ Technol, Reactor Inst Delft, NL-2629 JB Delft, Netherlands
[2] Eindhoven Univ Technol, Schuit Inst Catalysis, NL-5600 MB Eindhoven, Netherlands
[3] Shell Global Solut Int BV, NL-1030 BN Amsterdam, Netherlands
关键词
Hydrotreating; Carbon support; 'Co-Mo-S'; HDS; HDN; MOSSBAUER EMISSION-SPECTROSCOPY; MO-S PHASE; HYDRODESULFURIZATION CATALYSTS; DEEP HYDRODESULFURIZATION; ACTIVE PHASE; COBALT; SULFIDATION; ALUMINA; EXAFS; TEMPERATURE;
D O I
10.1016/j.apcatb.2013.05.013
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
The sulfiding behaviour and hydrotreating performance of CoMo and NiMo on carbon catalysts were investigated, with a view to establishing the suitability of an active-carbon carrier for industrial hydrotreatment purposes. The sulfidation process (H-2/H2S at 0.1 and 4 MPa) was followed with Co-57 Mossbauer emission spectroscopy, and X-ray absorption spectroscopy (Mo- and Co-edge). It turns out that the structural evolution of the CoMo/C catalyst is in broad terms very similar to that of a CoMo/Al2O3 one, including the type I -> II phase transition at increased sulfiding pressure, albeit that some sintering takes place concomitantly. In the hydrotreating part a NiMo/C catalyst was employed, sulfided at I or 4 MPa, in trickle-flow conditions at 3.5 (HDS) and 6 (HDN) MPa. It transpires that the adsorption properties of NiMo/C are quite different from those of a NiMo/alumina, in that dibenzthiophene, quinoline, and polyaromatics are much stronger adsorbed on the carbon-supported catalyst. This leads to very high dibenzothiophene HDS and quinoline HDN activities, but to a disappointing performance in the hydrotreatment of a heavy gasoil, where the polyaromatics can compete effectively for adsorption on the active HDS/N sites. (c) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:178 / 186
页数:9
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