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Precious metal methanol-to-hydrogen catalyst as well as preparation method and application thereof

A technology for producing hydrogen from methanol and precious metals, which is applied in the direction of catalyst activation/preparation, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, and can solve the problems of low dispersion, high and low CO concentration in hydrogen-rich products CO selectivity and other issues, to achieve high temperature stability, inhibit the formation of carbon deposits, reduce the effect of CO concentration

Pending Publication Date: 2022-05-27
SOUTH UNIVERSITY OF SCIENCE AND TECHNOLOGY OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Patent CN106799228A discloses a catalyst for reforming methanol to produce hydrogen, which uses CeO 2 One or a mixture of oxides of Fe, La, Zr, Mg and Al as a carrier, loaded with 8% of Pt and 15% of In 2 o 3 As a catalyst, the catalyst has a higher conversion rate and lower CO selectivity in the high-temperature methanol hydrogen production reaction, but the catalyst preparation process will produce pungent odor, the Pt loading is high, and the catalyst stability needs to be improved
[0005] In "Hydrogen production over highly active Pt based catalyst coatings by steam reforming of methanol: Effect of support and co-support" International Journal of Hydrogen Energy 2020, 1658-1670, using 15% Pt / 15% In 2 o 3 / CeO 2 Catalyst, high stability, but high Pt loading, low dispersion
[0006] Based on the above, it can be seen that the problems of noble metal methanol hydrogen production catalysts in the prior art are high noble metal loading, low dispersion, lack of water dissociation sites, resulting in higher reaction temperature, and high CO concentration in the hydrogen-rich product gas.

Method used

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  • Precious metal methanol-to-hydrogen catalyst as well as preparation method and application thereof
  • Precious metal methanol-to-hydrogen catalyst as well as preparation method and application thereof
  • Precious metal methanol-to-hydrogen catalyst as well as preparation method and application thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0045] First, weigh 2.6gNa 2 CO 3 Dissolve in 50mL deionized water to prepare 0.5M Na 2 CO 3 solution; take the ratio of Zn to Ga as Zn:Ga=3:1 (mol:mol), weigh 11.2g of Zn(NO 3 ) 2 ·6H 2 O and 3.2 g of Ga nitrate were dissolved in 50 mL of deionized water to prepare 0.75 M of Zn 2+ solution and 0.25M Ga 3+ solution, gradually added dropwise to the aforementioned Na 2 CO 3 In the solution; 6.4g of NaOH was weighed and dissolved in 40mL of deionized water to prepare a 4M NaOH solution, and the pH value was kept at 10 by adding NaOH solution dropwise to the aforementioned metal mixed solution, and the hydrotalcite nanoparticles gradually precipitated; the crystallization process , stirred at room temperature for 17 h, filtered the suspension and washed the particles with deionized water until the pH was close to neutral, and then further washed with 400 mL of ethanol for 2 h, and then put the isolated solid matter in a vacuum drying box and dried for 8 h to obtain ZnGa-LD...

Embodiment example 2

[0049] Comparing implementation case 2 with implementation case 1, the difference is that the ratio of zinc to gallium is 2:1.

[0050] First, weigh 2.6gNa 2 CO 3 Dissolve in 50mL deionized water to prepare 0.5M Na 2 CO 3 solution; take the ratio of Zn to Ga as Zn:Ga=2:1 (mol:mol), weigh 10.4g of Zn(NO 3 )2·6H 2 O and 3.8 g of Ga nitrate were dissolved in 50 mL of deionized water to prepare 0.7 M of Zn 2+ solution and 0.3M Ga 3+ solution, gradually added dropwise to the aforementioned Na 2 CO 3 In the solution; 6.4g of NaOH was weighed and dissolved in 40mL of deionized water to prepare a 4M NaOH solution, and the pH value was maintained at 10 by adding dropwise NaOH solution to the aforementioned metal mixed solution, and the hydrotalcite nanoparticles gradually precipitated; After 17 h stirring at room temperature, the suspension was filtered and the particles were washed with deionized water until the pH was close to neutral, followed by further washing with 400 mL ...

Embodiment example 3

[0053] The implementation case 3 is compared with the implementation cases 1 and 2, the difference is that the ratio of zinc and gallium is 1:1.

[0054] First, weigh 2.6gNa 2 CO 3 Dissolve in 50mL deionized water to prepare 0.5M Na 2 CO 3 solution; take the ratio of Zn to Ga as Zn:Ga=1:1 (mol:mol), weigh 7.4g of hydrated zinc nitrate and 6.4g of hydrated gallium nitrate and dissolve it in 50mL of deionized water to prepare 0.5M of Zn 2+ solution and 0.5M Ga 3+ solution; Weigh 6.4g of NaOH and dissolve it in 40mL of deionized water to prepare a 4M NaOH solution. By adding NaOH solution dropwise to the aforementioned metal mixed solution, the pH value is kept at 10, and the hydrotalcite nanoparticles are gradually precipitated; then crystallized Procedure, stirring at room temperature for 17 h, the suspension was filtered and the particles were washed with deionized water to near neutral pH, followed by further washing with 400 mL of ethanol for 2 h. Put the separated soli...

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Abstract

The invention discloses a noble metal methanol-to-hydrogen catalyst as well as a preparation method and application thereof. The noble metal methanol-to-hydrogen catalyst comprises a carrier, an active component and an auxiliary agent, the carrier is hydrotalcite LDH or roasted hydrotalcite LDO after roasting, the active component is noble metal, and the loading amount of the noble metal is 0.05%-2% based on the mass percentage; the loading capacity of the auxiliary agent is 0.5%-10%; and the particle size of the carrier is 5-500 nm. According to the invention, the ultrathin lamellar hydrotalcite is used as the carrier to support the noble metal to realize atomic-scale high dispersion, the interaction of electron transfer and the like between the active metal and the carrier is regulated and controlled by adding the assistant, the dissociation sites of water are increased, the atomic-scale dispersion immobilization of the active component noble metal is realized, the high-temperature methanol hydrogen production performance is good, and the CO selectivity is low.

Description

technical field [0001] The invention belongs to the technical field of catalysts, in particular to the technical field of methanol hydrogen production catalysts, and more particularly relates to a precious metal methanol hydrogen production catalyst and a preparation method and application thereof. Background technique [0002] Methanol, as an organic liquid-phase hydrogen carrier, can realize on-line in-situ hydrogen production. The reaction temperature of methanol steam reforming (MSR) is mild and the hydrogen yield is high, which is the preferred route for hydrogen production. Catalysts are the key to hydrogen production from methanol reforming. Precious metals such as Pt, Pd, Ru, etc., can be used as active metals to crack methanol, and have excellent catalytic performance, which has been the focus of research. At present, the commonly used supports are metal oxides, such as Al 2 O 3 , CeO 2 , ZnO and SiO 2 It has a large specific surface area and stability, can for...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/62B01J37/03B01J37/08B01J37/02B01J37/18C01B3/22
CPCB01J23/62B01J37/031B01J37/08B01J37/0203B01J23/007B01J37/18C01B3/22C01B2203/0277C01B2203/107C01B2203/1082Y02P20/52
Inventor 索红日刘雪刘科曹道帆赵杭吴昌宁
Owner SOUTH UNIVERSITY OF SCIENCE AND TECHNOLOGY OF CHINA
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