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A kind of coal bed gas deoxidation catalyst and its preparation method and application

A technology for deoxidation catalyst and coalbed methane, which is applied in Raney-type catalysts, chemical instruments and methods, and physical/chemical process catalysts, etc. problem, to achieve the effect of less impurities, simple preparation method and high loading capacity

Active Publication Date: 2019-08-20
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The preparation process of the catalyst is complicated, and it needs to be calcined at a high temperature of 700-850°C. The high temperature calcining causes quite a lot of particles to sinter, which makes the utilization rate of the metal lower, and the amorphous Raney metal decreases, resulting in a decrease in activity.

Method used

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  • A kind of coal bed gas deoxidation catalyst and its preparation method and application
  • A kind of coal bed gas deoxidation catalyst and its preparation method and application
  • A kind of coal bed gas deoxidation catalyst and its preparation method and application

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preparation example Construction

[0030] Second aspect, the present invention provides the preparation method of above-mentioned catalyst, and this method comprises the following steps:

[0031] (1) The carrier and the active component are mixed and shaped to obtain a catalyst precursor;

[0032] (2) Calcining the catalyst precursor obtained in step (1) under an inert atmosphere.

[0033] In the preparation method of the present invention, for the composition and content of the carrier and the active component, all can refer to the description of the corresponding content above, and will not be repeated here.

[0034] In the preparation method of the present invention, preferably, in step (1), the preparation method of the active component includes: mixing and contacting the metal alloy with an alkaline solution to obtain an activated Raney alloy.

[0035] Preferably, the contact temperature is 25-95°C, more preferably 40-70°C; the contact time is 5min-72h, more preferably 1-48h; the concentration of the alka...

Embodiment 1

[0052] This example is used to illustrate the coal bed gas deoxidation catalyst and its preparation method of the present invention.

[0053] (1) Weigh 100g nickel-aluminum alloy powder, wherein the Ni content is 48% by weight, the aluminum content is 52% by weight, add 1000g of 20% by weight NaOH solution prepared with deionized water, keep the temperature at 70°C, and after 8 hours The solution was filtered to obtain activated Raney alloy powder, which was rinsed with distilled water for 3 times and then spread flat in an ice-bath container for rapid cooling for 24 hours to obtain passivated Raney alloy.

[0054] (2) the Raney alloy of the passivation that 60g superfine silicon dioxide and 60g step (1) obtains is put into kneader, kneading 40min under rotating speed 50 rev / mins, add 50ml 3% by weight in kneading process Nitric acid solution and 50ml distilled water, after kneading, extrude the catalyst precursor (strip, Φ 3mm) with twin-screw extruder.

[0055] (3) Measure ...

Embodiment 2

[0057] This example is used to illustrate the coal bed gas deoxidation catalyst and its preparation method of the present invention.

[0058] (1) Weigh 100g nickel-aluminum alloy powder, wherein the Ni content is 48% by weight, the aluminum content is 52% by weight, add 1000g of 15% by weight KOH solution prepared with deionized water, keep the temperature at 60°C, and after 12 hours The solution was filtered to obtain activated Raney alloy powder, which was rinsed with distilled water for 3 times and then spread flat in an ice-bath container for rapid cooling for 24 hours to obtain passivated Raney alloy.

[0059] (2) the Raney alloy of passivation that 80g superfine silicon dioxide and 60g step (1) obtains is put into kneader, kneading 40min under rotating speed 50 rev / mins, add 50ml 3% by weight in kneading process Nitric acid solution and 50ml distilled water, after kneading, extrude the catalyst precursor (strip, Φ 3mm) with twin-screw extruder.

[0060] (3) Measure 15ml...

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Abstract

The invention relates to the field of coal mine zone coalbed methane exploitation and use and discloses a coalbed methane deoxidation catalyst and its preparation method and use, and a coalbed methane deoxidation method. The catalyst comprises an active component and a carrier. The active component is a Raney alloy and the carrier is silica. The catalyst is used in a coalbed methane deoxidation reaction and has the advantages of easy molding, low preparation cost, high catalytic activity and large amount of treatment.

Description

technical field [0001] The invention relates to the field of mining and application of coalbed methane in coal mining areas, in particular to a catalyst for deoxidizing coalbed methane, its preparation method and application, and a method for deoxidizing coalbed methane. Background technique [0002] Coalbed methane (commonly known as gas) exists in large quantities in coal seams and contains a large amount of hydrocarbon compound methane. In the mining process of coal mines, due to the explosive properties of coalbed methane, if it is not handled carefully, it is very easy to cause underground accidents in coal mines, so the initial method is to release it into the atmosphere. Since the main component methane is a greenhouse gas, its greenhouse effect is CO 2 More than 20 times of that, a large amount of coal-bed methane is discharged into the atmosphere, aggravating the global greenhouse effect. [0003] With the increasing scarcity of oil resources and the impact on the...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J25/02C10L3/10
Inventor 郝雪松鲁树亮王秀玲刘小波张利军杜志国徐洋吴佳佳及振秋
Owner CHINA PETROLEUM & CHEM CORP