1999Physical Chemistry Chemical PhysicsRequires access

Hydrodesulfurization and hydrogenation on alumina-supported tungsten and nickel-promoted tungsten catalysts

Toshiaki Kabe, Weihua Qian, Asumi Funato, Yuzo Okoshi, Atsushi Ishihara

Open publisher page 39 citations

Abstract

Hydrodesulfurization (HDS) of radioactive 35S-labeled dibenzothiophene was carried out over a series of alumina-supported W-based catalysts containing ca. 10–35 wt.% WO3 and 0–9 wt.% NiO at temperatures in the range 220–400°C and under a reaction pressure of 50 kg cm-2. The catalytic activities of the catalysts changed depending on the W loadings and sulfidation temperature for W–Al2O3 catalysts. Moreover, the HDS and hydrogenation (HYD) activity of W–Al2O3 catalysts were remarkably enhanced with the addition of nickel. Further, the amount of labile sulfur (S0) on the W–Al2O3 catalyst was much less than that on the corresponding Mo catalyst although the strength of the W–S bond is weaker than that of Mo–S. This is attributed to the fact that the sulfidation of the W–Al2O3 catalyst and the formation of the W–S bond are more difficult. On the other hand, S0 and the rate constant of H2S release (kRE) increased significantly on addition of nickel, as in the case of the Co–Mo catalyst. Moreover, the Ni-promoted W–Al2O3 catalyst with higher Ni/W ratio (0.6) also showed S0 and kRE comparable to those of the corresponding Co–Mo catalyst. These results suggested, therefore, that the promoting effect of nickel enhanced the relative ease of sulfidation of W catalysts and resulting in formation of more active sites simultaneously.

About this research paper

What this paper is about

Hydrodesulfurization (HDS) of radioactive 35S-labeled dibenzothiophene was carried out over a series of alumina-supported W-based catalysts containing ca. 10–35 wt.% WO3 and 0–9 wt.% NiO at temperatures in the range 220–400°C and under a reaction pressure of 50 kg cm-2. The catalytic activities of the catalysts changed depending on the W loadings and sulfidation temperature for W–Al2O3 catalysts. Moreover, the HDS and hydrogenation (HYD) activity of W–Al2O3 catalysts were remarkably enhanced with the addition of nickel. Further, the amount of labile sulfur (S0) on the W–Al2O3 catalyst was much less than that on the corresponding Mo catalyst although the strength of the W–S bond is weaker than that of Mo–S. This is attributed to the fact that the sulfidation of the W–Al2O3 catalyst and the formation of the W–S bond are more difficult. On the other hand, S0 and the rate constant of H2S release (kRE) increased significantly on addition of nickel, as in the case of the Co–Mo catalyst. Moreover, the Ni-promoted W–Al2O3 catalyst with higher Ni/W ratio (0.6) also showed S0 and kRE comparable to those of the corresponding Co–Mo catalyst. These results suggested, therefore, that the promoting effect of nickel enhanced the relative ease of sulfidation of W catalysts and resulting in formation of more active sites simultaneously.

Why it matters

OpenAlex reports 39 citations for this work. Citation counts describe recorded attention and do not establish research quality.

Key contribution

A contribution statement is not available in the OpenAlex record.

Method / approach

Method details are not available in the OpenAlex metadata.

Main findings

Findings are not separately available in the OpenAlex metadata.

Limitations

Limitations are not available in the OpenAlex metadata.

Applications

Application details are not available in the OpenAlex metadata.

Available abstract

Hydrodesulfurization (HDS) of radioactive 35S-labeled dibenzothiophene was carried out over a series of alumina-supported W-based catalysts containing ca. 10–35 wt.% WO3 and 0–9 wt.% NiO at temperatures in the range 220–400°C and under a reaction pressure of 50 kg cm-2. The catalytic activities of the catalysts changed depending on the W loadings and sulfidation temperature for W–Al2O3 catalysts. Moreover, the HDS and hydrogenation (HYD) activity of W–Al2O3 catalysts were remarkably enhanced with the addition of nickel. Further, the amount of labile sulfur (S0) on the W–Al2O3 catalyst was much less than that on the corresponding Mo catalyst although the strength of the W–S bond is weaker than that of Mo–S. This is attributed to the fact that the sulfidation of the W–Al2O3 catalyst and the formation of the W–S bond are more difficult. On the other hand, S0 and the rate constant of H2S release (kRE) increased significantly on addition of nickel, as in the case of the Co–Mo catalyst. Moreover, the Ni-promoted W–Al2O3 catalyst with higher Ni/W ratio (0.6) also showed S0 and kRE comparable to those of the corresponding Co–Mo catalyst. These results suggested, therefore, that the promoting effect of nickel enhanced the relative ease of sulfidation of W catalysts and resulting in formation of more active sites simultaneously.

Key concepts: Sulfidation, Hydrodesulfurization, Catalysis, Dibenzothiophene, Nickel, Tungsten, Chemistry, Inorganic chemistry

Related papers

Back to paper searchBrowse research topicsOriginal source
Hydrodesulfurization and hydrogenation on alumina-supported tungsten and nickel-promoted tungsten catalysts — Research Paper | ScholarLens