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Journal ArticleDOI

Carbon dioxide reforming of methane to synthesis gas over supported Ni catalysts

Z.L. Zhang, +1 more
- 02 Dec 1994 - 
- Vol. 21, pp 589-595
TLDR
In this article, the authors investigated carbon dioxide reforming of methane to synthesis gas using Ni catalysts in the temperature range of 500-850°C and showed that the overall reaction can be described by a Langmuir-Hinshelwood mechanistic scheme, assuming that methane dissociation is the rate determining step.
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This article is published in Catalysis Today.The article was published on 1994-12-02. It has received 397 citations till now. The article focuses on the topics: Carbon dioxide reforming & Catalysis.

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Citations
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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

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.
Journal ArticleDOI

Carbon Dioxide Reforming of Methane To Produce Synthesis Gas over Metal-Supported Catalysts: State of the Art

TL;DR: In this article, a comprehensive review on the thermodynamics, catalyst selection and activity, reaction mechanism, and kinetics of the CO2 reforming of CH4 is presented, where Ni-based catalysts impregnated on certain supports show carbon free operation and thus attract much attention.
Journal ArticleDOI

Dry reforming of methane over nickel catalysts supported on magnesium aluminate spinels

TL;DR: In this article, a co-precipitation method was used to support Ni-based catalysts for dry reforming of methane to synthesis gas, and the results showed that Ni/MgOγ-Al2O3 and Ni/Al 2O4 catalysts exhibit higher activity and better stability using a stoichiometric feed ratio (1:1).
Journal ArticleDOI

Dry reforming of methane: Influence of process parameters—A review

TL;DR: In this article, the authors explored the influences of the active metal, support, promoter, preparation methods, calcination temperature, reducing environment, particle size and reactor choice on catalytic activity and carbon deposition for the dry reforming of methane.
References
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Journal ArticleDOI

CO2-Reforming of Methane over Transition Metals

TL;DR: In this paper, the authors compared catalysts based on Ni, Ru, Rh, Pd, Ir, and Pt for CO 2 -reforming of methane by studying the equilibrium for methane decomposition, the activity for reforming, and carbon formation.
Journal ArticleDOI

Partial oxidation of methane to synthesis gas using carbon dioxide

TL;DR: In this article, an alternative catalytic strategy for CO2 reform-ing was proposed, which gives excellent yields (90%) from a stoichiometric (1:1) feed of CO2 and CH4.
Journal ArticleDOI

Carbon dioxide reforming of methane with supported rhodium

TL;DR: In this article, a model was constructed for conversion in a pellet by incorporating both the reverse reaction and the effect of external and internal diffusion, and the model was expanded to a large-scale packed bed with appropriate heat transfer parameters.
Journal ArticleDOI

The role of catalyst support on the activity of nickel for reforming methane with CO2

TL;DR: In this paper, the operating conditions needed to inhibit carbon deposition and nickel carbide formation as well as study the possible solid-state reactions within the catalysts in reforming methane with CO2.
Journal ArticleDOI

Activation of CH4 and Its Reaction with CO2 over Supported Rh Catalysts

TL;DR: In this article, the authors investigated the dissociation of CH4 and CO2, as well as the reaction between CH 4 and CO 2, over supported Rh in a fixed-bed continuous-flow reactor.
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