2015
DOI: 10.1007/s13203-015-0124-z
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Preparation and hydrodesulfurization properties of cobalt–molybdenum–phosphorous catalysts for removal of dibenzothiophene

Abstract: In this study, a series of cobalt-molybdenumphosphorous acid (Co-Mo-P) impregnating solutions with various Co/Mo molar ratios (0.2, 0.25, 0.3, 0.35) were synthesized, and desulfurization catalysts were prepared by mixing the solutions with c-Al 2 O 3 through an incipientwetness impregnation method. The Co-Mo-P supported cAl 2 O 3 catalysts were tested in the hydrodesulfurization of dibenzothiophene (DBT). The catalysts were characterized by N 2 adsorption-desorption isotherms, XRD, py-FT-IR, and HRTEM. Nitroge… Show more

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Cited by 11 publications
(6 citation statements)
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“…17,18 In order to obtain superior hydrodesulfurization performance, modied catalyst should be utilized, which could be achieved by the employment of novel preparation methods or incorporation of suitable promotors. Positive effects of various promotors such as zirconia, 18 titania, 19 uorine, 20 boron 21 and phosphorus 22 have been reported by numerous studies. It is also well established that the addition of chelating ligands in the catalyst preparation is a benecial way to improve catalytic performance in the HDS process.…”
Section: Introductionmentioning
confidence: 96%
“…17,18 In order to obtain superior hydrodesulfurization performance, modied catalyst should be utilized, which could be achieved by the employment of novel preparation methods or incorporation of suitable promotors. Positive effects of various promotors such as zirconia, 18 titania, 19 uorine, 20 boron 21 and phosphorus 22 have been reported by numerous studies. It is also well established that the addition of chelating ligands in the catalyst preparation is a benecial way to improve catalytic performance in the HDS process.…”
Section: Introductionmentioning
confidence: 96%
“…However, DFs obtained from gas condensates often do not meet modern standards not only in terms of the cetane number (CN), but also in terms of the content of sulfur compounds (SC). Traditionally, the reduction of the SC content in DFs in industry is carried out using hydrotreating processes [1][2][3][4][5][6][7][8][9][10][11][12][13].…”
Section: Introductionmentioning
confidence: 99%
“…The demand for low-sulfur fuels is increasing due to the implementation of stricter environmental regulations in the last decade worldwide. Nonetheless, the processing of heavier crude oil with higher sulfur, nitrogen and metal contents is growing, necessitating the increased use of hydrodesulfurization catalysts in petroleum refineries ( Marafi and Stanislaus, 2007 ; Akcil et al, 2015 ; Li et al, 2015 ). Hydrodesulfurization catalysts generally consist of the MoS 2 active phase with Co or Ni promoters supported on γ-Al 2 O 3 ( Ihan, 2020 ).…”
Section: Introductionmentioning
confidence: 99%