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Process for step-by-step improvement of methane conversion through methane cracking and carbon elimination

A technology for methane and carbon elimination, applied in the field of catalytic conversion of methane to syngas, can solve the problems of high price of Pt, limit industrial application, reduce catalyst stability, etc., and achieve the effect of being beneficial to utilization

Active Publication Date: 2016-11-09
NORTHWEST UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Chinese patent [CN101637726] discloses a method for improving the carbon deposition resistance of methane carbon dioxide reforming catalysts. The patent uses γ-Al 2 o 3 or NiAl 2 o 4 As the carrier, Ni is used as the active component, and a small amount of Pt is used as the auxiliary agent to prepare a nickel-based catalyst. It has good anti-coking performance for carbon dioxide reforming of methane, but the addition of auxiliary agents is limited due to the high price of Pt and limited resources. To realize the industrial application of anti-carbon deposition
Catalysts usually obtained by reduction of perovskite have good activity, stability and anti-coking properties, but their specific surface area is small, which limits industrial applications.
In addition, this method also has the problem that the reduction temperature is too high
[0007] The above methods only improve the anti-coking or anti-sintering performance of the catalyst through the improvement of the catalyst. However, carbon deposition and sintering often occur at the same time, and they will affect each other, greatly reducing the stability of the catalyst.

Method used

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  • Process for step-by-step improvement of methane conversion through methane cracking and carbon elimination
  • Process for step-by-step improvement of methane conversion through methane cracking and carbon elimination
  • Process for step-by-step improvement of methane conversion through methane cracking and carbon elimination

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Experimental program
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Effect test

Embodiment 1

[0043] Into the fixed bed packed with catalyst, pass CH 4 When the mixed gas with Ar is used for the methane carbon dioxide reforming reaction, the methane cracking reaction is carried out at a temperature of 450°C and a pressure of 0.1 MPa. The methane cracking reaction is carried out for 10 minutes, and the gas is detected online by gas chromatography at the 5th minute. Element. After 10 minutes of methane cracking reaction, switch to 30mL / min Ar gas purge for 5 minutes, and then pass CO 2 Mixed gas with Ar, carry out carbon removal reaction at a temperature of 450°C and a pressure of 0.1MP. The reaction is carried out for 15 minutes. After the reaction is completed, it is purged with 30mL / min Ar gas for 5 minutes to complete a methane conversion reaction, and then crack the methane And the carbon removal reaction cycle continues, and 12 methane conversion reactions are completed. Among them, when reacting, the space velocity is 3.6x10 4 mL / (h·gcat), CH 4 The flow rate o...

Embodiment 2

[0045] The difference from Example 1 is that the catalyst is Ni / MgO treated with cold plasma.

Embodiment 3

[0047] Unlike Example 1, the catalyst is cold plasma treated Ni / SiO 2 .

[0048] Such as figure 1 , figure 2 , image 3 Shown, use the method for stepwise reaction among the embodiment 1-3, respectively with the Ni / MgAlO that cold plasma is processed 4 ,, Ni / MgO, Ni / SiO 2 When the methane carbon dioxide reforming reaction is carried out as a catalyst, the initial conversion rate of methane is between 64.67%-62.25%, and the conversion rate of methane is between 63.39%-61.88 after undergoing 12 methane conversion reactions, and there is no obvious decline, indicating that Using the method for reaction, the catalyst has better stability and can maintain the methane carbon dioxide reforming reaction for a long time.

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Abstract

The invention provides a process for step-by-step improvement of methane conversion through methane cracking and carbon elimination. The process comprises the following steps: introducing mixed gas of CH4 and Ar into a fixed bed filled with a catalyst and carrying out a methane cracking reaction at a pressure of 0.1 to 3 MPa and a temperature of 300 to 900 DEG C for 10 to 60 min; carrying out purging with Ar; introducing carbon elimination gas and carrying out a carbon elimination reaction at a pressure of 0.1 to 3 MPa and a temperature of 400 to 900 DEG C for 15 to 60 min; carrying out purging with Ar again to finish a methane conversion reaction once; and repeating the cracking reaction and the carbon elimination reaction to complete the methane conversion reaction a plurality of times. According to the invention, the methane cracking reaction is carried out first and then the carbon elimination reaction is carried out so as to eliminate accumulated carbon the surface of a catalyst; since the separate two-step reactions need low temperature, energy consumption is reduced and sintering of the catalyst at high temperature is avoided at the same time; and the method allows the catalyst to maintain catalytic activity for a long time.

Description

technical field [0001] The invention relates to a method for preparing synthesis gas by catalytic conversion of methane, in particular to a process for improving methane conversion step by step through methane cracking and carbon elimination. Background technique [0002] The methods of catalytic conversion of methane to synthesis gas mainly include carbon dioxide reforming of methane, steam reforming of methane and partial oxidation of methane. These reactions convert the greenhouse gas methane into synthesis gas capable of synthesizing various chemicals, and have bright application prospects. Nickel-based catalysts have been widely used in the above reactions due to their abundant resources, low price, high activity, and high selectivity. However, nickel-based catalysts have problems of carbon deposition and sintering, which hinder the industrial application of methane to synthesis gas. Most of the research work in the prior art is devoted to overcoming a shortcoming of ni...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/26
CPCC01B3/26C01B2203/0277C01B2203/1058C01B2203/1241
Inventor 赵彬然陈占溥陈云静刘亚俊郭怀正马晓迅
Owner NORTHWEST UNIV
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