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Synthesis method of catalyst for preparing hydrogen through propane steam reforming

A technology of steam reforming and synthesis methods, which is applied in the fields of chemical instruments and methods, hydrogen/synthesis gas production, metal/metal oxide/metal hydroxide catalysts, etc. Carbon deactivation and other issues, to achieve the effect of good synthesis repeatability, simple synthesis steps, and no three-waste emissions

Pending Publication Date: 2022-05-27
SOUTHEAST UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

my country's natural gas steam reforming technology has matured, including (1) desulfurization pretreatment of raw materials; (2) steam conversion; (3) shift reaction; (4) purification, the device is reliable in operation, economical and suitable for large-scale However, since the main component of natural gas is methane, this technology has complex process flow, high reaction temperature (~800°C), low raw material utilization rate, low conversion rate of CO in the shift reaction (less than 45%), and the traditional Ni catalyst is easy to accumulate Carbon deactivation and other issues
[0005] Existing studies have shown that nickel catalysts have low selectivity to hydrogen due to their high surface activity on carbon elements and unbalanced surface chemical properties in the application of propane steam reforming to hydrogen production, and the by-products carbon monoxide, carbon dioxide and methane High content, easy carbon deposition and deactivation, short catalyst life, etc.

Method used

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  • Synthesis method of catalyst for preparing hydrogen through propane steam reforming
  • Synthesis method of catalyst for preparing hydrogen through propane steam reforming
  • Synthesis method of catalyst for preparing hydrogen through propane steam reforming

Examples

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Embodiment 1

[0026] A catalyst for preparing hydrogen by steam reforming of propane, which contains the following components in the following mass fractions: 5% active component and 95% silica carrier; the Ni / In molar ratio of the active component is 2 nickel indium metal intermediate compound.

[0027] The preparation method of the novel supported catalyst described in this embodiment is a deposition-precipitation method, which specifically includes the following steps:

[0028] (1) 950 mg of silica was weighed and calcined at 400° C. for 6 h by passing air into the pre-treatment device. 123 mg of nickel nitrate hexahydrate and 87 mg of hydrated indium nitrate were weighed and dissolved in a small amount of deionized water. The mixture was heated to 80°C, and the treated silica carrier was added simultaneously, and then 2M sodium hydroxide was added to adjust the pH to 6 to 8, washed with deionized water and filtered three times to prepare a silica carrier deposited on the silica carrier...

Embodiment 2

[0031] A novel supported catalyst contains the following mass fractions of active components: 10% and titanium dioxide carrier: 90%; the nickel-indium intermetallic compound whose active component Ni / In molar ratio is 2.

[0032] The preparation method of the novel supported catalyst described in this embodiment is a deposition-precipitation method, which specifically includes the following steps:

[0033] (1) 900 mg of titanium dioxide was weighed and calcined at 200° C. for 6 h by passing air into the pre-treatment device. Weigh 247 mg of nickel nitrate hexahydrate and 174 mg and dissolve in a small amount of deionized water. The mixture was heated to 80°C while adding the treated titanium dioxide carrier, then 2M sodium hydroxide was added to adjust the pH to 9, deionized water was washed and filtered three times to prepare nickel indium hydroxide deposited on the titanium dioxide carrier. The obtained nickel indium hydroxide was dried in a vacuum oven for 12 h, and then r...

Embodiment 3

[0036] A new type of supported catalyst, which contains the following components in the following mass fractions: 15% active component and 85% silica carrier; the nickel-indium intermetallic compound whose active component Ni / In molar ratio is 2.

[0037] The preparation method of the novel supported catalyst described in this embodiment is a deposition-precipitation method, which specifically includes the following steps:

[0038](1) 850 mg of silica was weighed and calcined at 400° C. for 6 h by passing air into the pre-treatment device. 168 mg of nickel dichloride and 171 mg of indium trichloride were weighed and dissolved in a small amount of deionized water. The mixture was heated to 80°C, and the treated silica carrier was added at the same time, and then 2M sodium hydroxide was added to adjust the pH to 6 to 8, washed with deionized water and filtered three times to prepare a silica carrier deposited on the silica carrier. Nickel indium hydroxide. The obtained nickel ...

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Abstract

The invention belongs to the technical field of hydrogen preparation, and discloses a method for preparing a hydrogen catalyst through propane steam reforming. The catalyst comprises the following components in percentage by mass: 5-20% of an active component and 95-80% of an oxide carrier, the active component comprises Ni < x > In < y > with different Ni / In proportions; the carrier is an oxide. The non-toxic nickel-indium intermetallic compound shows excellent selectivity and stability in the aspect of propane steam reforming hydrogen production due to a unique electronic structure. Wherein the selectivity of hydrogen in Ni2In / SiO2 is as high as 72%, the potential of replacing an industrial nickel-based catalyst is shown, and the catalyst has a wide application prospect.

Description

technical field [0001] The invention relates to the field of hydrogen preparation, in particular to a preparation method of a novel supported nickel indium catalyst and the application of the supported catalyst in propane steam reforming reaction. Background technique [0002] In order to solve the problem of global energy and environmental pollution, all countries in the world are striving to seek green new energy. Compared with traditional energy, hydrogen has the advantages of high combustion value, high thermal comprehensive efficiency and zero carbon emission, and is the most potential new energy in the future. At the same time, the super battery life and extremely short charging time of hydrogen fuel cells make hydrogen energy vehicles gradually occupy the market of fuel vehicles. However, the problem that currently restricts the development of the hydrogen energy industry is the high cost of hydrogen production. [0003] At present, my country mainly uses six types ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/825B01J23/83C01B3/40
CPCB01J23/825B01J23/83C01B3/40C01B2203/0233C01B2203/1235C01B2203/1058C01B2203/1082Y02P20/52
Inventor 宋元军张彤
Owner SOUTHEAST UNIV