2018
DOI: 10.1021/acs.iecr.8b03383
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Layered Double Hydroxide Method for Preparing Ni–Mo/γ-Al2O3 Ultradeep Hydrodesulfurization Catalysts

Abstract: This article reports a novel strategy for preparing NiMo/γ-Al2O3 ultradeep hydrodesulfurization (HDS) catalysts via thermal decomposition of layered double hydroxides (LDHs). Ni–Al–[C6H4(COO)2]2–-LDHs/γ-Al2O3 (terephthalate-pillared Ni–Al-LDHs/γ-Al2O3) composites were first obtained by in situ crystallization of Ni–Al–[C6H4(COO)2]2–-LDHs on the surface of γ-Al2O3. Then Ni–Al–Mo7O24 6–-LDHs/γ-Al2O3 composites were synthesized from the above composites by the anion exchange of [C6H4(COO)2]2– with Mo7O24 6–. Fina… Show more

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Cited by 6 publications
(3 citation statements)
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“…In addition, flake-flower architectures formed under a high content amount of nickel (49-52 wt.%) when the MoO 3 content was below 7 wt.%, and the Mo-Ni/ASA catalyst displayed a two times higher yield than a commercial NiMoP/Al 2 O 3 due to the higher Ni dispersion [16]. Lv et al demonstrated that the Ni-Mo/γ-Al 2 O 3 catalyst prepared by the thermal decomposition of the layered double hydroxides Ni-Al-[C 6 H 4 (COO) 2 ] 2− -LDHs/γ-Al 2 O 3 showed a better dispersion of the NiO and MoO 3 on the alumina surface, and the yield of the catalyst increased by 20% more than the catalyst prepared by an impregnation method, while the preparation process was complicated and required a long time [17]. Past research has demonstrated that the dispersion of the active species can be improved by optimizing the catalyst preparation method.…”
Section: Introductionmentioning
confidence: 99%
“…In addition, flake-flower architectures formed under a high content amount of nickel (49-52 wt.%) when the MoO 3 content was below 7 wt.%, and the Mo-Ni/ASA catalyst displayed a two times higher yield than a commercial NiMoP/Al 2 O 3 due to the higher Ni dispersion [16]. Lv et al demonstrated that the Ni-Mo/γ-Al 2 O 3 catalyst prepared by the thermal decomposition of the layered double hydroxides Ni-Al-[C 6 H 4 (COO) 2 ] 2− -LDHs/γ-Al 2 O 3 showed a better dispersion of the NiO and MoO 3 on the alumina surface, and the yield of the catalyst increased by 20% more than the catalyst prepared by an impregnation method, while the preparation process was complicated and required a long time [17]. Past research has demonstrated that the dispersion of the active species can be improved by optimizing the catalyst preparation method.…”
Section: Introductionmentioning
confidence: 99%
“…Many studies have aimed at exploring highly dispersed metal catalysts. Several methods, such as deposition–precipitation, equilibrium deposition filtration, and chemical vapor deposition, and sonochemical, , have been developed. However, the well dispersed metal catalyst has a major drawback.…”
Section: Introductionmentioning
confidence: 99%
“…[8][9][10] However, the conventional alumina interact strongly with metal oxide precursors to form species that are hard to be reduced or sulded. [11][12][13] Towards this, various new support materials are introduced for HDS catalysts. Those carbon-based materials, such as active carbon or graphene with hierarchical structures and high surface area, seem to be promising support materials in hydrotreating reactions of heavy crude oil.…”
Section: Introductionmentioning
confidence: 99%