A kind of preparation method of hydrogen production catalyst by steam reforming of methane

A methane water vapor reforming technology for hydrogen production, applied in the direction of molecular sieve catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low metal utilization in carrier channels and accelerate deep oxidation of products , increase catalyst cost and other issues, achieve the effect of improving conversion rate and product selectivity, avoiding further oxidation, and accelerating adsorption and desorption speed

Active Publication Date: 2018-01-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Studies have shown that when noble metals Ru, Rh, Pd, etc. are loaded on a suitable carrier, they all have high reactivity and anti-carbon deposition performance, but the disadvantage of noble metals is that they are expensive; among non-noble metals, nickel catalysts have relatively high High reactivity, Ni / Al is generally used 2 o 3 Catalyst, the reaction conditions are 1.5~3MPa, 850~900℃, the generated H 2 / CO ratio is about 3
[0008] Although in the prior art, the method for preparing the nickel-based catalyst for the steam reforming of methane can obtain a catalyst with better activity, but because the reaction is a fast reaction (this fast reaction is generally under the condition of mass transfer control) The reaction is completed when the reactant reaches the outer surface of the catalyst, so the inner surface of the catalyst does not contribute much to the target reaction, which results in a lower metal utilization rate in the carrier channel and increases the cost of the catalyst. At the same time, it will also accelerate the deep oxidation of the product

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Weigh 2.97g of nickel nitrate and dissolve it in an appropriate amount of deionized water to obtain solution A; use the equal volume impregnation method to load on 20g of alumina (the pore volume is 0.72ml / g, the specific surface area is 242m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 4h, dried at 80°C for 12h, and calcined at 700°C for 4h to obtain catalyst precursor B, wherein Ni accounted for 3% of the weight of the carrier in terms of elements; catalyst precursor B Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 80%, the reduction conditions are 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the mass concentration of the reduced and activated catalyst precursor B and 300mL is Add 10% sorbitol solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adjust the hydrogen pressure to 3MPa, and react at 220°C for 4 hours; place the re...

Embodiment 2

[0032] Weigh 2.97g of nickel nitrate and dissolve it in an appropriate amount of deionized water to obtain solution A; use equal volume impregnation method to load 20g of silicon oxide (pore volume is 1.06ml / g, specific surface area is 387m 2 / g, spherical, equivalent diameter 0.5mm) carrier, aged at room temperature for 6h, dried at 110°C for 10h, and calcined at 600°C for 4h to obtain catalyst precursor B, in which Ni accounted for 3% of the weight of the carrier in terms of elements; catalyst precursor B was in Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 90%, the reduction conditions are 400 ° C, 0.2 MPa (absolute pressure), and the reduction time is 8 hours; % of sorbitol solution was added to the autoclave, sealed and replaced with hydrogen for 4 times, then adjusted the hydrogen pressure to 2MPa, and reacted at 300°C for 2h; the reacted mixture in the above autoclave was placed for 1h, filtered, and the obtained s...

Embodiment 3

[0034] Weigh 2.97g of nickel nitrate and dissolve it in an appropriate amount of deionized water to obtain solution A; load it on 20g of SBA-15 (the pore volume is 1.23ml / g and the specific surface area is 701m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 8h, dried at 120°C for 6h, and calcined at 600°C for 4h to obtain catalyst precursor B, wherein Ni accounted for 3% of the weight of the carrier in terms of elements; catalyst precursor B Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 10%, the reduction conditions are 500°C, 0.2MPa (absolute pressure), and the reduction time is 6h; the mass concentration of catalyst precursor B after reduction and activation is 300mL Add 10% sorbitol solution into the autoclave, seal it and replace it with hydrogen twice, then adjust the hydrogen pressure to 3MPa, and react at 220°C for 4h; place the reacted mixture in the autoclave for 3h, filter, a...

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Abstract

The invention relates to a method for preparing a catalyst for steam reforming of methane to produce hydrogen. The catalyst includes an active component, an auxiliary agent and a carrier. The preparation method firstly dissolves the precursor of the active component in water to obtain a solution A; then Adding carrier, after aging, drying, and roasting, the catalyst precursor B is obtained; the catalyst precursor B is reduced by using a reducing atmosphere; the reduced catalyst precursor B and the polyol solution are added to the reactor for hydrogenation reaction , place the reaction effluent, then filter and dry to obtain catalyst precursor C; dissolve the active component precursor and auxiliary agent precursor in water to obtain solution D, then add catalyst precursor C, after drying and roasting, obtain catalyst. The method of the invention promotes the dispersion of more active components on the carrier surface, not only improves the utilization rate of active metals, but also improves the conversion rate of methane and the selectivity of products.

Description

technical field [0001] The invention relates to a preparation method of a hydrogen production catalyst by steam reforming of methane, in particular to a preparation method of a supported nickel-based catalyst for hydrogen production by steam reforming of methane. Background technique [0002] Methane is rich in resources and has a high hydrogen-to-carbon ratio, making it a good raw material for hydrogen production. Hydrogen, as an efficient and clean secondary energy source, will become one of the main energy sources in the future society. In recent years, hydrogen, as the raw material of fuel cells, has incomparable advantages compared with other fuels, such as high calorific value of hydrogen, no air pollution, etc. The application of hydrogen energy solves the problem of energy shortage on the one hand, and on the other It does not cause environmental pollution. [0003] At present, there are two main ways to produce hydrogen from methane: one is through the production ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J29/035B01J23/78B01J23/83C01B3/40
CPCY02P20/52
Inventor 孙晓丹张舒冬张信伟刘继华
Owner CHINA PETROLEUM & CHEM CORP
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