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Method for removing CO

A removal and substrate technology, applied in the field of CO removal, can solve the problems of reduced utilization of active metals, low catalyst reactivity, and low treatment efficiency

Active Publication Date: 2022-05-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Traditional methanation catalysts require high-temperature calcination during the preparation process. High-temperature calcination causes considerable sintering of metal particles, which reduces the utilization rate of active metals, and ultimately leads to low reactivity of the catalyst, resulting in excessively high reaction temperatures or difficulty in processing crude hydrogen at high space velocities. CO in the process, the treatment efficiency is low

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Examples

Experimental program
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Embodiment approach

[0016] According to the present invention, in the polymer containing imidazole side groups, the molecular chain of the polymer includes repeating structural units, and each repeating unit may include an imidazole group to form a side chain of the entire molecule. In the present invention, the polymer containing imidazole side groups is not particularly limited, as long as the carbon support can be formed by carbonization. Preferably, the polymer containing imidazole side groups is selected from polyvinylimidazole or a copolymer of vinylimidazole and divinylbenzene. According to one embodiment, the polymer containing imidazole side groups is polyvinylimidazole. The polyvinylimidazole can be prepared by methods well known in the art, and can also be obtained commercially. Generally, the degree of polymerization (Xn) of the polyvinylimidazole can be 1000-10000, for example, with AIBN as the initiator and toluene as the solvent, react in a hydrothermal kettle at 60°C to obtain a ...

preparation example 1

[0038] Take 20 mL of methanol solution with polyvinylimidazole (Xn=2000) concentration of 0.05 g / mL, and 10 mL of methanol solution with nickel nitrate concentration of 0.05 g / mL; into the methanol solution of polyvinylimidazole, and then kept stirring for 4 hours to form a precipitate; the stirred product was filtered, and the obtained solid was washed with methanol for 3 times, and then vacuum-dried at 80°C for 4 hours to obtain a solid powder; Calcined at 400°C for 4h in a nitrogen atmosphere to obtain a N-Ni / C-1 matrix with a nickel loading of 54wt%.

[0039] Take 50g of the N-Ni / C-1 substrate, and treat it with hydrogen at 450°C for 8 hours, and place the reduced substrate in 500mL Ru 3+ Aqueous solution (Ru 3+ 1×10 -4 g / mL ruthenium nitrate aqueous solution) for 24 hours, through adsorption and displacement reaction, Ru is loaded on the substrate, filtered, and washed with deionized water until nearly neutral, to obtain a loaded catalyst containing 0.1wt% Ru. Stored i...

preparation example 2

[0041] Take 20 mL of methanol solution with polyvinylimidazole (Xn=2000) concentration of 0.05 g / mL, and 10 mL of methanol solution with nickel nitrate concentration of 0.05 g / mL; into the methanol solution of polyvinylimidazole, and kept stirring for 3 hours to form a precipitate; the stirred product was filtered, and the obtained solid was washed with methanol for 3 times, then vacuum-dried at 80°C for 4 hours to obtain a solid powder; Calcined at 600°C for 3 hours in a nitrogen atmosphere to obtain a N-Ni / C-2 matrix with a nickel loading of 58 wt%.

[0042] Take 50g of N-Ni / C-2 substrate, reduce it with hydrogen at 500°C for 4 hours, place it in 500mL Ru 3+ Aqueous solution (Ru 3+ 3×10 -4 g / mL of ruthenium nitrate aqueous solution) for 30 hours, through adsorption and displacement reaction, Ru is loaded on the substrate, filtered, and washed with deionized water until nearly neutral, to obtain a loaded catalyst containing 0.3wt% Ru. Stored in deionized water, the catalys...

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Abstract

The invention relates to the field of gas purification, and provides a method for removing CO, which comprises the following steps: in a fixed bed reactor, contacting hydrogen-rich gas containing nitrogen oxides with a supported catalyst, and carrying out methanation reaction under the conditions that the reaction temperature is 160-350 DEG C, the pressure is 0.1-7.0 MPa, the gas space velocity is 10000-20000h <-1 > and the inlet CO concentration is 0.5-2.0 vol%, wherein the supported catalyst comprises a substrate and ruthenium supported on the substrate, the substrate comprises nitrogen-doped carrier carbon and nickel, and coordinate bonds are formed between lone pair electrons on at least part of nickel and nitrogen. According to the method disclosed by the invention, methanation reaction at high space velocity can be realized, and CO in the hydrogen-rich gas can be removed to be less than 1ppm.

Description

technical field [0001] The invention relates to the field of gas purification, and more specifically, to a method for removing CO. Background technique [0002] The most common noble metal catalysts in the industry include supported Pd and Pt catalysts, and supported Ru noble metal catalysts are also used in industry, such as low-temperature methanation reactions. Compared with other noble metal catalysts, the supported Ru catalyst has a good prospect of industrial application due to its relatively cheap price. [0003] At present, the research on supported Ru catalysts mainly focuses on the preparation and application of catalysts, using different supports, different Ru precursors, and different preparation methods to obtain catalysts suitable for hydrogenation or dehydrogenation reactions. For example, an alumina-supported Ru catalyst is obtained by impregnating an alumina carrier; a coconut shell carbon-supported Ru catalyst is obtained by impregnating a coconut shell ca...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/58B01J27/24B01J37/08B01J37/18B01J37/02
CPCC01B3/586B01J27/24B01J37/084B01J37/086B01J37/18B01J37/0207C01B2203/047
Inventor 张齐鲁树亮
Owner CHINA PETROLEUM & CHEM CORP