Oxygen-containing coal bed gas deoxidation catalyst and preparation thereof as well as applications

A technology of deoxidation catalyst and coal bed gas, which is applied in the direction of metal/metal oxide/metal hydroxide catalyst, molecular sieve catalyst, chemical instruments and methods, etc., which can solve the problems of coking, slagging labor intensity, and high cost of catalytic deoxidation treatment , Catalysts are expensive and other problems, to achieve the effect of easy operation, price reduction, and easy automatic control

Inactive Publication Date: 2008-12-17
HAO HUA CHENGDU TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage is that the catalyst is expensive, and coalbed methane contains sulfide, and sulfur has a poisonous effect on precious metals, which will cause catalyst deactivation. Therefore, desulfurization must be carried out before deoxidation, and then deoxidation reaction, which increases the cost of deoxidation. Resulting in higher cost of catalytic deoxidation treatment of coalbed methane
But the disadvantage is that this method consumes precious coke resources, and the consumption cost of coke is about 50% of the entire operating cost.
In addition, the coke deoxidation method is labor-intensive in adding coke and slag, and the environment is dusty, and there are various forms of sulfide in the coke.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] The strip-shaped oxygen-containing coalbed methane deoxidation catalyst of this embodiment is composed of 1% active component, 50% active auxiliary agent and 49% carrier, and the active component is cobalt nitrate equivalent to 1% cobalt oxide in the catalyst, The active auxiliary agent is composed of manganese nitrate equivalent to 10% of manganese dioxide, zinc chloride with 10% of zinc oxide, and copper sulfate with 30% of copper oxide. The carrier is 49% of alumina, named doc1.

[0047] The preparation method of the oxygen-containing coal bed gas deoxidation catalyst of the present embodiment is:

[0048] (1) Mix 3.9g cobalt nitrate hexahydrate (equivalent to 1g cobalt oxide), 29g manganese nitrate tetrahydrate (equivalent to 10g manganese dioxide), 16.8g anhydrous zinc chloride (equivalent to 10g zinc oxide) and 94g pentahydrate Copper sulfate (equivalent to 30g copper oxide) was dissolved in 100g water to form an aqueous solution;

[0049] (2) immerse 49g of alum...

Embodiment 2

[0052] The oxygen-containing coalbed methane deoxygenation catalyst of this embodiment is composed of 60% active component, 1% active auxiliary agent and 39% carrier. The active component is cobalt acetate which is equivalent to 60% cobalt oxide content in the catalyst. The auxiliary agent is ferrous sulfate with a content of 1% of ferric oxide, and the carrier is composed of 20% titanium oxide and 19% zirconium oxide, named doc2.

[0053] (1) 199g of cobalt acetate tetrahydrate (equivalent to 60g of cobalt oxide), 20g of titanium oxide and 19g of zirconia are fully mixed, extruded, dried at 120°C for 2 hours, and calcined at 400°C for 5 hours to obtain the pre-catalyst body;

[0054] (2) 3.5g of ferrous sulfate heptahydrate (equivalent to 1g of ferric oxide) was dissolved in 50g of water to form an aqueous solution;

[0055] (3) Immerse the catalyst precursor prepared in step (1) into the solution prepared in step (2), immerse at room temperature for 12 hours, dry at 120°C f...

Embodiment 3

[0057] The oxygen-containing coalbed methane deoxidation catalyst of the present embodiment is composed of 30% active component, 30% active auxiliary agent and 40% carrier. The active component is cobalt chloride equivalent to 30% cobalt oxide, and the active auxiliary agent It is composed of 5% manganese chloride equivalent to manganese dioxide and 25% zinc nitrate equivalent to zinc oxide, and the carrier is 10% magnesium oxide, 10% calcium oxide, 10% silicon dioxide and 10% type A molecular sieve Composed of, named doc3.

[0058] (1) 11.4g manganese chloride tetrahydrate (equivalent to 5g manganese dioxide), 91.7g zinc nitrate hexahydrate (equivalent to 25g zinc oxide), 10g magnesium oxide, 10g calcium oxide, 10g silicon dioxide and 10g of A Type molecular sieves were fully mixed, rolled into balls, dried at 120°C for 1.5 hours, and calcined at 450°C for 4.5 hours to obtain a catalyst precursor;

[0059] (2) 95.2g cobalt chloride hexahydrate (equivalent to 30g cobalt oxide...

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PUM

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Abstract

The invention discloses a deoxidizing catalyst for a coal-seam gas containing oxygen and a preparation method as well as an application thereof. The deoxidizing catalyst of the invention consists of an active component, an active auxiliary and a porous carrier. The active component is the compound of Co; the active auxiliary is one or more compounds of Mn, Fe, Zn and Cu; the porous carrier is one or more of aluminum oxide, titanium oxide, zirconium oxide, magnesium oxide, calcium oxide, silicon oxide, a phosphor-aluminium molecular sieve, an A-typed molecular sieve, an X-typed molecular sieve, a Y-typed molecular sieve, a mordenite, a ZSM-5 zeolite, diatomaceous earth, kaolinite, natural clay, aluminum silicate and magnesium silicate; calculated by oxide, the weight percentage of the active component is 1 to 60 percent; the weight percentage of the active auxiliary is 1 to 50 percent; the rest is the carrier. The catalyst of the invention has certain sulfur-resistance performance, is applicable to the deoxidization treatment of coal-seam gas with an oxygen content of 3 to 6 percent (V / V) and is capable of causing the oxygen content in the coal-seam gas to be lower than 0.5 percent by deoxidization.

Description

technical field [0001] The invention relates to a catalyst, in particular to an oxygen-containing coal bed gas deoxidation catalyst and its preparation method and its application in the oxygen-containing coal bed gas deoxidation. Background technique [0002] Coalbed methane exists in large quantities in coal seams, and is an unconventional natural gas; it is one of the main causes of underground accidents in coal mines. In fact, coalbed methane is a new energy with high calorific value and no pollution. It can be used as fuel for power generation, process fuel, chemical raw material and residential fuel. my country emits about 30 billion cubic meters of coal-bed methane into the atmosphere every year, causing huge environmental pressure and waste of resources. Reasonable and comprehensive utilization of coalbed methane can make up for my country's energy shortage. At the same time, the recovery and utilization of coalbed methane can also help to protect the environment. T...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/889B01J23/70B01J29/78B01J29/80C10L3/06
Inventor 廖炯陈耀壮胡善霖姚松柏雷菊梅白燕
Owner HAO HUA CHENGDU TECH
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