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Preparation method for preparing synthesis gas NiO@SiO2 core-shell type catalyst by employing low-concentration coalbed methane

A technology for synthesis gas and coalbed methane, which is applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., which can solve the difficulty in controlling the particle size of precious metal nanoparticles and the complicated operation process. And other issues

Active Publication Date: 2015-07-01
清创人和生态工程技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The operation process of this method is complicated, and the core part is noble metal. Since the acid solution can only corrode the iron oxide and has no effect on the noble metal, it is difficult to control the particle size of the noble metal nanoparticles.

Method used

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  • Preparation method for preparing synthesis gas NiO@SiO2 core-shell type catalyst by employing low-concentration coalbed methane
  • Preparation method for preparing synthesis gas NiO@SiO2 core-shell type catalyst by employing low-concentration coalbed methane
  • Preparation method for preparing synthesis gas NiO@SiO2 core-shell type catalyst by employing low-concentration coalbed methane

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Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0028]Catalyst preparation: Weigh 2.1g of soluble metallic nickel salt and 10.7g of polyvinylpyrrolidone, and dissolve them in 100ml of pentanediol solution. in N 2 Under protection, the above solution was heated to 200° C. and stirred at this temperature for 4 h, then the solution was further heated to 270° C., stirred for 1 h, and cooled to room temperature. 100 ml of acetone solution was added to obtain a precipitate, which was centrifuged and washed with ethanol, and the obtained nanoparticles were dispersed in 100 ml of ethanol. Take 100ml of the ethanol solution in which the nanoparticles were dispersed in the previous step, add 1g of polyvinylpyrrolidone to the solution, and stir at room temperature for 12h. Add 10ml of ammonia solution to the above solution and place it in an ultrasonic oscillator for 30min. Add 0.1ml tetraethyl orthosilicate and 5ml ethanol solution to the above solution, and continue ultrasonic oscillation for 1h. The product was collected by cent...

Embodiment approach 2

[0034] Catalyst preparation:

[0035] Weigh 4.3g soluble metal nickel salt, 16g polyvinylpyrrolidone, and dissolve it in 100ml pentanediol solution. in N 2 Under protection, the above solution was heated to 170° C. and stirred at this temperature for 2.5 h, then the solution was further heated to 200° C., stirred for 1.5 h, and cooled to room temperature. 150ml of acetone solution was added to obtain a precipitate, which was centrifuged and washed with ethanol, and the obtained nanoparticles were dispersed in 200ml of ethanol. Take 100ml of the ethanol solution in which the nanoparticles were dispersed in the previous step, add 1.6g of polyvinylpyrrolidone to the solution, and stir at room temperature for 12h. Add 17ml of ammonia solution to the above solution and place it in an ultrasonic oscillator for 30min. Add 0.5ml tetraethyl orthosilicate and 10ml ethanol solution to the above solution, and continue ultrasonic oscillation for 1h. The product was collected by centrif...

Embodiment approach 3

[0041] Catalyst preparation: reference example 1;

[0042] Catalytic performance evaluation: The catalytic reaction was carried out in a fixed-bed reactor. Before the reaction, the catalyst was first heated at 750°C with H 2 Reduction for 2h; then feed the raw material gas, which forms CH 4 / O 2 / N 2 2 / 1 / 2 (molar ratio), normal pressure, reaction temperature 750°C, constant space velocity of 1×10 5 ml·h -1 g -1 , The product was analyzed by gas chromatography after condensing to remove water. The experimental results of Example 3 are shown in Table 3.

[0043] Table 3 NiOSiO 2 Catalytic Performance of Catalysts at Different Space Velocities

[0044] time (h) Methane conversion rate (%) CO selectivity (%) h 2 selectivity (%) h 2 / CO 0 0.75 0.76 0.61 1.6 1 0.83 0.79 0.64 1.63 2 0.86 0.81 0.67 1.65 3 0.87 0.83 0.67 1.62 4 0.88 0.83 0.67 1.68 5 0.88 0.85 0.7 1.62 6 0.89 0.85 0.7 1.65 18 0.87 ...

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Abstract

The invention discloses a preparation method for preparing a synthesis gas NiO@SiO2 core-shell type catalyst by employing low-concentration coalbed methane, belongs to the technical fields of a natural gas chemical industry and a coal chemical industry, and mainly solves the problems of easy sintering and easy carbon deposit of an existing method for preparing a catalyst in the synthesis gas preparation process by employing the low-concentration coalbed methane. The method disclosed by the invention is characterized by comprising the following steps: firstly, preparing nanoscale NiO particles from a soluble nickel salt by adopting a thermal decomposition method; dispersing the nano particles into ethanol, and adding a soluble silicon source; decomposing and polymerizing the soluble silicon source, so as to form encapsulated microspheres containing NiO nano particles; and etching in an alkaline environment, and finally preparing a multi-channel core-shell type NiO@SiO2 catalyst. The core-shell type NiO@SiO2 catalyst prepared by the preparation method disclosed by the invention displays good sintering resistance and good coke formation resistance in a synthesis gas preparation reaction employing the low-concentration coalbed methane.

Description

technical field [0001] A kind of low concentration coalbed methane of the present invention makes synthetic gas NiOSiO 2 The preparation method of the core-shell catalyst belongs to the technical field of natural gas chemical industry and coal chemical industry. Background technique [0002] Coalbed methane refers to self-generated and self-storage gas stored in coal seams, and its active ingredient is methane. my country is a large coal-producing country, and its coal-bed methane resources are very rich, ranking third in the world in reserves, but its utilization rate is very low. Coalbed methane can be divided into surface extraction and underground extraction of coalbed methane according to the extraction method. 4 The content is more than 85% (volume fraction, the same below), which is the main way of resource utilization of coalbed methane, but its scale is small. Underground extraction of coalbed methane is coalbed methane extracted from underground mines for mining...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J35/00C01B3/40
CPCY02P20/52
Inventor 王俊文丁传敏刘世斌高晓峰原沁波
Owner 清创人和生态工程技术有限公司