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Journal ArticleDOI

Mesoporous H-AlMCM-41 supported NiO-MoO3 catalysts for hydrodenitrogenation of o-toluidine: I. Effect of MoO3 loading

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TLDR
The mesoporous molecular sieve, H-AlMCM-41, was synthesized hydrothermally and used as support for the preparation of series of sequentially impregnated NiO-MoO 3 catalysts as discussed by the authors.
Abstract
The mesoporous molecular sieve, H-AlMCM-41 (Si/Al = 100) was synthesized hydrothermally and used as support for the preparation of series of sequentially impregnated NiO-MoO 3 catalysts. Various amounts of MoO 3 (12, 18, 24 and 30 wt.%) along with of 7 wt.% of NiO were loaded in order to optimize the MoO 3 loading level for obtaining maximum HDN activity. These catalysts were well-characterized by physico-chemical techniques, such as X-ray diffraction (XRD), N 2 adsorption–desorption, SEM, FT-Raman spectroscopy, UV–vis DRS and FT-IR spectra of CO adsorption and tested for hydrodenitrogenation (HDN) of o -toluidine. The change in dispersion with MoO 3 loading was studied by FT-IR spectra of CO adsorbed samples. HDN activities of various NiO-MoO 3 catalysts were evaluated and the activities are accounted in terms of physico-chemical characteristics of the catalytic materials. Catalyst with 7 wt.% NiO-24 wt.% MoO 3 showed maximum HDN activity when compared to other catalysts and its enhanced activity due to the fine dispersion of MoO 3 as well as due to formation of an additional Ni–Mo–O phase from AlMCM-41, as revealed by FT-IR of CO adsorption, FT-Raman and XRD studies.

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Citations
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Journal ArticleDOI

Ni catalysts with Mo promoter for methane steam reforming

TL;DR: In this paper, NiO/Al2O3 precursors were prepared by simultaneous precipitation, in a Ni:Al molar ratio of 3:1, promoted with Mo oxide (0.05, 0.5, 1.0 and 2.0%).
Journal Article

MCM-41-supported CO-MO catalysts for deep hydrodesulfurization of light cycle oil : Sulfur removal from gasoline and distillate streams

TL;DR: In this paper, a mesoporous MCM-41-supported Co-Mo catalyst was used for the desulfurization of light cycle oil (LCO), a byproduct of the fluid catalytic cracking (FCC) process in a petroleum refinery.
Journal ArticleDOI

Structure and Reducibility of NiO-MoO3/γ-Al2O3 Catalysts: Effects of Loading and Molar Ratio

TL;DR: In this article, the effects of loading and molar ratio on the structure and reducibility of NiO-MoO3/γ-Al2O3 catalysts have been investigated.
Journal ArticleDOI

Synthesis of hierarchically porous silicas with mesophase transformations in a four-component microemulsion-type system and the catalytic performance for dibenzothiophene hydrodesulfurization

TL;DR: In this paper, the NiMo/Al-hierarchical porous silica catalyst with pore structures of MCF-disordered-SBA-15-type showed the best hydrodesulfurization performance among all the studied catalysts.
Journal ArticleDOI

Mo–Ni/Al-SBA-15 (Sulfide) Catalysts for Hydrodenitrogenation: Effect of Si/Al Ratio on Catalytic Activity

TL;DR: In this paper, Mo-Ni/Al-SBA-15(10) was used for Methylcyclohexylamine conversion to hydrocarbons and the observed trend of activity is correlated with the aluminum content, and it was concluded that the variation in Si/Al ratio remarkably affects the hydrodenitrogenation ability of Al-Sba-15 supported Mo−Ni catalysts.
References
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Reference BookDOI

Handbook of Heterogeneous Catalysis

TL;DR: This paper presents a meta-modelling system that automates the very labor-intensive and therefore time-heavy and therefore expensive and expensive process of characterization and activation of Solid Catalysts.
Journal ArticleDOI

Structure and Function of the Catalyst and the Promoter in Co—Mo Hydrodesulfurization Catalysts

TL;DR: The authors discuss le role d'un promoteur modifiant un catalyseur, notamment determination du nombre de sites actifs, and discuss the role of un promoteur in modifying a catalyseure.
Journal ArticleDOI

Hydrocracking of Vacuum Gasoil on the Novel Mesoporous MCM-41 Aluminosilicate Catalyst

TL;DR: The MCM-41-based catalyst was seen to give superior HDS, HDN, and HC activities to the latter two catalysts in a one-stage operation using an untreated gasoil.
Journal ArticleDOI

In Situ Raman Spectroscopy of Alumina-Supported Metal Oxide Catalysts

TL;DR: In this paper, the molecular structures of the surface overlayerers of rhenium(VII) oxide, molybdenum(VI) oxide and titanium(IV) oxide on γ-alumina were determined by in situ Raman spectroscopy under dehydrated conditions.
Journal ArticleDOI

Study of nickel-molybdenum-.gamma.-aluminum oxide catalysts by x-ray photoelectron and Raman spectroscopy. Comparison with cobalt-molybdenum-.gamma.-aluminum oxide catalysts

TL;DR: Several series of nickel (or Co) molybdenum oxide catalysts supported on X-ray photoelectron and Raman spectroscopy have been studied by as discussed by the authors, where the combination of these two techniques is a complementary approach to the alumina coverage, the nature of the deposited species, and the interaction between these species.
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