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Preparation method of catalyst for methane steam reforming to produce hydrogen

A methane steam reforming technology for hydrogen production, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc. Deep oxidation of products, increase in catalyst cost and other issues, to achieve the effect of improving conversion rate and product selectivity, avoiding further oxidation, and accelerating adsorption and desorption speed

Active Publication Date: 2016-06-08
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
[0005] Although in the prior art, the method for preparing the nickel-based catalyst for 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

[0025] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, dried at 110°C for 8h, and the obtained catalyst was calcined at 450°C for 4h to obtain catalyst precursor A, in which Mo accounted for 9.3wt% of the weight of catalyst precursor A in terms of elements, and Co in terms of elements Accounting for 1.8wt% of catalyst precursor A weight, Ni accounts for 2.9wt% of catalyst precursor A weight in terms of elements, V accounts for 1.7wt% of catalyst precursor A weight in terms of elements; 20g of catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrog...

Embodiment 2

[0027] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, dried at 110°C for 8h, and the obtained catalyst was calcined at 450°C for 4h to obtain catalyst precursor A, in which Mo accounted for 9.3wt% of the weight of catalyst precursor A in terms of elements, and Co in terms of elements Accounting for 1.8wt% of catalyst precursor A weight, Ni accounts for 2.9wt% of catalyst precursor A weight in terms of elements, V accounts for 1.7wt% of catalyst precursor A weight in terms of elements; 20g of catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrog...

Embodiment 3

[0029] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the surface of the catalyst was removed by extraction, dried at 110°C for 8h, and the obtained catalyst was calcined at 450°C for 4h to obtain catalyst precursor A, in which Mo accounted for 9.3wt% of the weight of catalyst precursor A in terms of elements, and Co in terms of elements Accounting for 1.8wt% of catalyst precursor A weight, Ni accounts for 2.9wt% of catalyst precursor A weight in terms of elements, V accounts for 1.7wt% of catalyst precursor A weight in terms of elements; 20g of catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrog...

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PUM

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Abstract

The invention relates to a preparation method of a catalyst for methane steam reforming to produce hydrogen. The catalyst comprises an active component, an auxiliary agent, and a carrier. The preparation method comprises the following steps: processing the catalyst for waste residual oil hydrogenation to produce a catalyst precursor (A); then reducing the catalyst precursor (A) in a reducing atmosphere; adding the reduced catalyst precursor (A) and a polyol solution into a high pressure reactor to carry out hydrogenation reactions, collecting the effluents of the reactions, filtering, drying to obtain a catalyst precursor (B); dissolving an active component precursor and an auxiliary agent precursor into water to prepare a solution (C), adding the catalyst precursor (B), drying, and burning to obtain the catalyst. The catalyst for waste residual oil hydrogenation is fully utilized to produce the provided catalyst, the cost is reduced, moreover, more active components are dispersed on the surface of carriers, the utilization rate of active metal is improved, and the conversation rate of methane and product selectivity are both improved.

Description

technical field [0001] The invention relates to a method for preparing a catalyst for steam reforming of methane to produce hydrogen, in particular to a method for preparing a supported nickel-based catalyst for steam reforming of methane to produce hydrogen. 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 of s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/883C01B3/40
CPCY02P20/52
Inventor 孙晓丹张舒冬张信伟刘继华
Owner CHINA PETROLEUM & CHEM CORP
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