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Methane Reforming Catalyst - Crossref

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Last Updated: 16 November 2021

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Hydrogen production via methane dry reforming process over CoAl and CoMgAl-Hydrotalcite derived catalysts

Abstract Carbon Monoxide 0. 67 Al 0. 31 and Co 0. 14 Mg 0. 54 Al 0. 31 hydrotalcite based drivers were prepared by a co-precipitation approach at a dealt with pH=11, displaying an appropriate hydrotalcite structure to be utilized as a catalyst in the reaction of the dry reforming of methane. The outcomes of the TPR evaluation proved that CoAl-HT has much better catalytic performances than CoMgAl-HT. The solid CoMgAl-HTc-R calls for high reduction temperature contrasted to CoAl-HTc-R because of the solid CoO-MgO interactions.

Source link: https://doi.org/10.1088/1755-1315/880/1/012035


The effect of interfacial engineering on the deactivation resistance of nickel-based catalysts for dry reforming of methane

Abstract Methane completely dry reforming response can convert carbon monoxide 2 and CH 4, 2 kinds of greenhouse gases with extremely secure chemical properties, to produce syngas, which can be made use of to synthesize useful commercial products. Compared to solitary steel nickel, the discerning doping of multi steels and sustains programs higher catalytic task and anti poisoning resistance due to changing the chemical and structural properties of the catalyst by enhancing the alloy effect and the pressure in between metal and assistance.

Source link: https://doi.org/10.1088/1742-6596/2076/1/012041


Transport Mechanism of Steam Methane Reforming on Fixed Bed Catalyst Heated by High Temperature Helium for Hydrogen Production: A Computational Fluid Dynamics Investigation

Abstract In this study, we numerically assessed the efficiency of a steam methane reforming reactor heated up utilizing high-temperature helium for hydrogen production. The outcome showed that with a rise in the reactant gas inlet rate, the temperature level at the same reactor size setting reduced. The maximum gas temperature distinction at the gas collection chamber got to around 55 ° C. When the helium inlet temperature enhanced by 200 ° C, the greatest temperature of the reactant gas raised by 132 ° C.

Source link: https://doi.org/10.1115/1.4040377

* Please keep in mind that all text is summarized by machine, we do not bear any responsibility, and you should always check original source before taking any actions

* Please keep in mind that all text is summarized by machine, we do not bear any responsibility, and you should always check original source before taking any actions