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Cu-based catalyst for hydrogen production through methanol reforming, and preparation method and application thereof

A reforming hydrogen production and catalyst technology, which is applied in the field of hydrogen energy, can solve the problem of poor catalytic effect of CuO, and achieve good catalytic activity, high activity, and simple preparation method

Active Publication Date: 2022-03-11
RES CENT FOR ECO ENVIRONMENTAL SCI THE CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] At present, CuO-based catalysts are usually used for methanol reforming to produce hydrogen, but the catalytic effect of CuO is not as good as that of simple Cu.

Method used

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  • Cu-based catalyst for hydrogen production through methanol reforming, and preparation method and application thereof
  • Cu-based catalyst for hydrogen production through methanol reforming, and preparation method and application thereof
  • Cu-based catalyst for hydrogen production through methanol reforming, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0048] This embodiment provides a preparation method and application of a Cu-based catalyst. The preparation method and application include the following steps:

[0049] (1) 30g of cerium nitrate, 10g of lanthanum nitrate and 4g of copper nitrate were dissolved in 400mL of water, 90g of urea was added thereto, heat treated at 90°C for 24h, filtered, washed and dried to obtain a precipitate;

[0050] (2) calcining the precipitate obtained in step (1) at 450° C. for 4 hours to obtain a precursor;

[0051] (3) Pulverize the precursor obtained in step (2), pass it through a 50-mesh sieve, weigh 500mg of the precursor and put it into a quartz tube fixed-bed reactor, feed it at 0.06mL / s and vaporize at 175°C Methanol and water, the molar ratio of methanol and water is 1:3, and then the reaction temperature is raised to 350° C. at a rate of 5° C. / min to carry out the catalyst performance test.

Embodiment 2

[0053] This embodiment provides a preparation method and application of a Cu-based catalyst. The preparation method and application include the following steps:

[0054] (1) 10 g of cerium nitrate, 20 g of lanthanum nitrate and 0.15 g of copper nitrate were dissolved in 400 mL of water, 90 g of urea was added thereto, heat treated at 85° C. for 36 h, filtered, washed, and dried to obtain a precipitate;

[0055] (2) calcining the precipitate obtained in step (1) at 400° C. for 5 hours to obtain a precursor;

[0056] (3) Pulverize the precursor obtained in step (2), pass it through a 50-mesh sieve, weigh 500 mg of the precursor and put it into a quartz tube fixed-bed reactor, feed it at 0.06 mL / s and vaporize at 150 °C Methanol and water, the molar ratio of methanol and water is 1:4, and then the reaction temperature is raised to 300° C. at a rate of 5° C. / min to carry out the catalyst performance test.

Embodiment 3

[0058] This embodiment provides a preparation method and application of a Cu-based catalyst. The preparation method and application include the following steps:

[0059] (1) 20g of cerium nitrate, 15g of lanthanum nitrate and 1.75g ​​of copper nitrate were dissolved in 400mL of water, 90g of urea was added thereto, heat treated at 95°C for 9h, filtered, washed and dried to obtain a precipitate;

[0060] (2) calcining the precipitate obtained in step (1) at 500° C. for 3 hours to obtain a precursor;

[0061] (3) Pulverize the precursor obtained in step (2), pass it through a 50-mesh sieve, weigh 500 mg of the precursor and put it into a quartz tube fixed-bed reactor, feed it at 0.06 mL / s and vaporize at 200 °C Methanol and water, the molar ratio of methanol and water is 1:1, and then the reaction temperature is raised to 400°C at a rate of 5°C / min to carry out the catalyst performance test.

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Abstract

The invention relates to a Cu-based catalyst for hydrogen production by methanol reforming and a preparation method and application thereof, the Cu-based catalyst comprises a composite solid solution, and the composite solid solution is loaded with an active component Cu; the composite solid solution comprises a Ce-La solid solution. The Cu-based catalyst is self-activated in a methanol reforming hydrogen production reaction, reduced Cu particles are smaller in size and higher in activity, and the Cu-based catalyst can enable the methanol conversion rate to reach 99% or above and is suitable for large-scale industrial use.

Description

technical field [0001] The invention belongs to the field of hydrogen energy, and in particular relates to a Cu-based catalyst for methanol reforming to produce hydrogen, a preparation method and application thereof. Background technique [0002] "Hydrogen" is an ideal energy carrier that can efficiently convert renewable and clean energy such as wind energy, water energy, solar energy, and biomass energy into electrical energy through fuel cells without emitting CO. 2 and other greenhouse gases. However, due to the lack of safe, environmentally friendly and economical H 2 source, the development of hydrogen energy and fuel cell industries has been severely restricted. [0003] CO 2 and H 2 Methanol prepared as a raw material has the reputation of "liquid sunshine", so that the source of methanol is no longer limited to fossil energy. The methanol reforming hydrogen production reaction conditions are mild, and the H in the product 2 The content is high, and the cost of...

Claims

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Application Information

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IPC IPC(8): B01J23/83C01B3/32
CPCB01J23/83C01B3/32
Inventor 贺泓徐光艳韩雪余运波张梦媛刘帝儒
Owner RES CENT FOR ECO ENVIRONMENTAL SCI THE CHINESE ACAD OF SCI