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Journal ArticleDOI

Uncoupling the size and support effects of Ni catalysts for dry reforming of methane

TLDR
In this paper, a unique Ni-based catalyst in which the Ni nanoparticle size and support can be varied independently was devised for dry reforming of methane (DRM) at 800°C without a significant change in the Ni size, and overlayers of various metal oxides, including SiO 2, Al 2 O 3, MgO, ZrO 2, TiO 2.
Abstract
The dry reforming of methane (DRM; CH 4  + CO 2 ↔  2H 2  + 2CO) can be a good way to utilize greenhouse gases for the production of valuable syn-gas. Ni-based catalysts have been used for this reaction; however, the Ni size effect and support effect were highly coupled and therefore could not be observed separately. Here, a unique catalyst in which the Ni nanoparticle size and support can be varied independently was devised. Highly uniform Ni nanoparticles with sizes of 2.6, 5.2, 9.0, and 17.3 nm were tested for DRM at 800 °C without a significant change in the Ni size, and overlayers of various metal oxides, including SiO 2 , Al 2 O 3 , MgO, ZrO 2 , TiO 2 , were tested with the 5.2 nm of Ni nanoparticles. The dependence of the CH 4 or CO 2 turnover frequency on the Ni size and support was evaluated separately. The 2.6 nm Ni nanoparticles showed 4.1 times higher methane turnover frequency than those with a size of 17.3 nm. When various metal oxide overlayers were tested with the same 5.2 nm Ni, Al 2 O 3 exhibited 4.3 times higher methane turnover frequency than SiO 2 . The independent observation of the effects of the Ni nanoparticle size and support will provide valuable guidelines for designing effective methane dry reforming catalysts.

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Journal ArticleDOI

Core–shell structured catalysts for thermocatalytic, photocatalytic, and electrocatalytic conversion of CO2

TL;DR: This review provides an in-depth assessment of core-shell structured catalysts for the thermocatalysis, photocatalytic, and electrocatalytic conversion of CO2 into synthesis gas and valuable hydrocarbons.
Journal ArticleDOI

A review on catalyst development for dry reforming of methane to syngas: Recent advances

TL;DR: In this paper, a review provides a contemporary assessment of progresses recorded on synergistic interplay among catalyst components (active metals, support, promoters and binders) during dry reforming using state-of-the-art experimental and theoretical techniques.
Journal ArticleDOI

Silica–Ceria sandwiched Ni core–shell catalyst for low temperature dry reforming of biogas: Coke resistance and mechanistic insights

TL;DR: In this paper, a sandwiched core-shell structured Ni-SiO2@CeO2 catalyst, with nickel nanoparticles encapsulated between silica and ceria, was developed and applied for dry reforming of biogas under low temperature conditions to test its coke inhibition properties.
Journal ArticleDOI

Coke formation and deactivation during catalytic reforming of biomass and waste pyrolysis products: A review

TL;DR: In this article, a review deals with the currently existing alternatives at the catalyst and reactor level to cope with catalyst deactivation and increase process stability, and then delves with the fundamental phenomena occurring during this catalysts deactivation.
References
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Journal ArticleDOI

Design, synthesis, and use of cobalt-based Fischer-Tropsch synthesis catalysts

TL;DR: In this article, Fischer-Tropsch synthesis (FTS) catalysts with high cobalt concentration and site density are used for the synthesis of hydrocarbons from CO/H2 mixtures.
Journal ArticleDOI

CO2 Reforming of CH4

TL;DR: Although technological practice should minimize environmental impact, this is not always economically feasible as mentioned in this paper, and during the past decade, there has been increasing global concern over the environmental impact of technology.
Journal ArticleDOI

The statistics of surface atoms and surface sites on metal crystals

R. Van Hardeveld, +1 more
- 01 Jun 1969 - 
TL;DR: In this paper, the number of surface atoms at the surface of a metal crystal can be differentiated according to the number (j) and arrangement of their nearest neighbours in the crystal.
Journal ArticleDOI

Isotopic and kinetic assessment of the mechanism of reactions of CH4 with CO2 or H2O to form synthesis gas and carbon on nickel catalysts

TL;DR: Turnover rates for forward reactions of CH 4/CO 2 and CH 4 /H 2 O mixtures were proportional to CH 4 pressure (5-450 kPa) and independent of the partial pressure of the CO 2 or H 2 O coreactants (5 −450 kPA), indicating that these reactions are mechanistically equivalent as discussed by the authors.
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