Oxygen-containing coal bed gas deoxidation catalyst and preparation thereof as well as applications
A technology for deoxidation catalyst and coalbed methane, applied in metal/metal oxide/metal hydroxide catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problem of high labor intensity of coking, slag removal, and high cost of catalytic deoxidation treatment. , the catalyst is expensive and other problems, to achieve the effect of easy operation, price reduction, easy automatic control
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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 alumin...
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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