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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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Citations
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Journal ArticleDOI

Unraveling the effects of Ce/Zr molar ratio in mesoporous CexZr1-xO2 on the performance of dry reforming of methane over the supported Ni catalysts

TL;DR: In this article , Ni supported on the ordered mesoporous CexZr1−xO2 with various Ce/Zr molar ratios prepared by a programmed evaporation-induced self-assembly method were employed for dry reforming of methane.
Journal ArticleDOI

CO2 capture from H2O and O2 containing flue gas integrating with dry reforming methane using Ni-doping CaO dual functional materials

TL;DR: In this paper , the authors investigated the ICCU-DRM using simulated flue gases (10 % CO2 + 6.7 % O2+ 6.0 % H2O) in the presence of Ni-CaO dual functional materials, aiming to optimise Ni loading and metal support interaction.
Journal ArticleDOI

Intensified performance of methane dry reforming based on non-thermal plasma technology: Recent progress and key challenges

TL;DR: In this article , the activation of CH4 and CO2 under the non-thermal plasma and highlights the effect of process parameters on the conversion and selectivity in detail, and the opportunity and challenges of plasma catalysts are summarized.
Journal ArticleDOI

Deactivation Mechanism and Anti-Deactivation Measures of Metal Catalyst in the Dry Reforming of Methane: A Review

TL;DR: In this article , the problem of catalyst deactivation during the dry reforming of carbon dioxide and methane to syngas was investigated. And the results revealed that changing the type and size of active metal, adjusting the properties of the support, and adding additives can further regulate the dispersion of the active component.
References
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Journal ArticleDOI

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Journal ArticleDOI

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TL;DR: In this article, the Fischer-Tropsch (FT) reaction is used to produce purified syngas and its composition should match the overall usage ratio of the FT reactions, which depends on the product selectivity.
Journal ArticleDOI

A review of dry (CO2) reforming of methane over noble metal catalysts

TL;DR: Dry (CO2) reforming of methane literature for catalysts based on Rh, Ru, Pt, and Pd metals is reviewed, including the effect of these noble metals on the kinetics, mechanism and deactivation of these catalysts.
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