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Catalyst for hydrogen production from methane and preparation method and application thereof

A catalyst and methane technology, which is applied in the field of methane hydrogen production catalyst and its preparation, can solve the problems of large initial investment and achieve the effects of uniform distribution, light relative weight and promotion of dispersion

Active Publication Date: 2020-08-04
SOUTHWEST RES & DESIGN INST OF CHEM IND +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Hydrogen production by reforming natural gas has the advantage of low hydrogen production cost, and can fully rely on the existing natural gas infrastructure experience to develop hydrogen energy infrastructure, but the initial investment in equipment is relatively large, and the hydrogen produced needs to be purified to meet the needs of fuel. battery requirements

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0035] This embodiment also provides a method for preparing a methane hydrogen production catalyst, comprising the following steps:

[0036] (1) Preparation of silicon-aluminum-titanium composite oxide: Add titanium source, aluminum source and silicon source solutions into the reaction vessel, adjust the pH of the mixed solution at a certain temperature to form a precipitate, age for a certain period of time, filter the precipitate, wash, Dry to obtain silicon-aluminum-titanium composite oxide;

[0037] (2) Preparation of powder catalyst: disperse the silicon-aluminum-titanium composite oxide prepared in step (1) in the palladium source impregnation solution, stir at a certain temperature for a certain period of time, evaporate the water to dryness, then continue drying and calcining to obtain a powder catalyst ;

[0038] (3) Mix the powder catalyst prepared in step (2) with the molding aid glass fiber and deionized water, and process the mixture, mud refining, aging and extr...

example 1

[0049] (1) Take 1L mixed solution of titanium nitrate, aluminum nitrate and sodium silicate, the concentration of titanium nitrate is calculated as TiO 2 Calculated as 20g / L, the concentration of aluminum nitrate is Al 2 o 3 Calculated as 100g / L, the concentration of sodium silicate is SiO 2 Calculated as 40g / L. Add the mixed solution into the constant temperature reaction kettle, control the temperature in the constant temperature reaction kettle to be 65°C, and add K 2 CO 3 aqueous solution, the rate of addition is 4mL / min, and the pH value of the mixed solution in the constant temperature reactor is adjusted to 8.0. After continuing to stir at constant temperature for 1.5 h, the mixed solution in the constant temperature reaction kettle was filtered to obtain a solid. The solid matter was washed 4 times, and then dried at 80° C. for 8.0 hours to obtain a silicon-aluminum-titanium composite oxide.

[0050] (2) Take 0.5L palladium nitrate impregnation solution, the conc...

example 2

[0054] (1) Take 1L mixed solution of titanium nitrate, aluminum nitrate and sodium silicate, the concentration of titanium nitrate is calculated as TiO 2 Calculated as 40g / L, the concentration of aluminum nitrate is Al 2 o 3 Calculated as 80g / L, the concentration of sodium silicate is SiO 2 Calculated as 60g / L. Add the mixed solution into the constant temperature reaction kettle, control the temperature in the constant temperature reaction kettle to be 75°C, and add the solute mass fraction of 50% K 2 CO 3 aqueous solution, the rate of addition is 2mL / min, and the pH value of the mixed solution in the constant temperature reactor is adjusted to 10.0. After continuing to stir at constant temperature for 1.5 h, the mixed solution in the constant temperature reaction kettle was filtered to obtain a solid. The solid matter was washed 4 times, and then dried at 100° C. for 8.0 hours to obtain a silicon-aluminum-titanium composite oxide.

[0055] (2) Take 0.5L palladium nitrat...

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Abstract

The invention provides a catalyst for hydrogen production from methane as well as a preparation method and an application of the catalyst. The effective components of the catalyst comprise a silicon-aluminum-titanium composite oxide serving as a carrier and palladium oxide serving as an active component, preferably honeycomb forming, and glass fibers serve as a reinforcing agent. The preparation method of the catalyst comprises the following steps: firstly, preparing a silicon-aluminum-titanium composite oxide by a coprecipitation method, secondly, loading palladium on the silicon-aluminum-titanium composite oxide by an excessive impregnation method, then, carrying out extrusion molding on the honeycomb catalyst, and finally, carrying out molding post-treatment on the honeycomb catalyst. The prepared catalyst for hydrogen production has the advantages of high mechanical strength, good activity and reliable production process, and can meet the requirement of miniaturized methane hydrogen production.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, in particular to a methane hydrogen production catalyst and its preparation method and application. Background technique [0002] Miniaturized CH4-containing gas reforming (reaction of CH4 and H2O) to produce hydrogen, hydrogen energy and hydrogen fuel cell technology is one of the very important innovative technologies in the future energy technology revolution. Hydrogen energy is characterized by green environmental protection and high energy In the future, it will play an important role in my country's energy system. In recent years, hydrogen fuel cell technology has made major breakthroughs. It basically meets the requirements for vehicle use in terms of life, reliability, and practical performance. Fuel cell vehicles have begun to be put on the market on a large scale, and encourage a new generation Innovative development of distributed hydrogen production technology. By 2020, my co...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/44B01J35/04B01J35/10C01B3/40
CPCB01J23/44C01B3/40C01B2203/0233B01J35/394B01J35/56B01J35/61Y02P20/52
Inventor 曾凌云刘玉成郑珩冯雅晨谭青凡美婷胡方王藤汪涛胡瑜飞袁家均
Owner SOUTHWEST RES & DESIGN INST OF CHEM IND