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Vanadium-based liquid-phase catalyst and preparation method thereof

A liquid-phase catalyst and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of catalyst specific surface area reduction, catalyst clogging, high cost of vanadium-based catalysts, etc.

Active Publication Date: 2015-07-01
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] In view of the deficiencies of the existing technology, in order to solve the problems of the high cost of the existing vanadium-based catalysts, and the reduction of the specific surface area of ​​the catalyst due to catalyst sintering, deposition of ammonium salt and fly ash after long-term reaction, the decrease of catalytic activity, and even the problem of catalyst clogging , the present invention proposes for the first time a kind of vanadium that is insensitive to air, water and acid, has good thermal stability, simple synthesis, circulation and regeneration methods, is easy to industrialize, and shows high contact area and high catalytic activity in flue gas denitrification. Liquid-based catalyst and preparation method thereof, which can be used for desulfurization and denitrification of flue gas

Method used

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  • Vanadium-based liquid-phase catalyst and preparation method thereof
  • Vanadium-based liquid-phase catalyst and preparation method thereof
  • Vanadium-based liquid-phase catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0054] Prepare a 0.2mol / L sodium metavanadate aqueous solution; mix the resulting aqueous solution with the fatty chain primary amine N1923 in a ratio of 1:1, and add 1:1 H 2 SO 4 Aqueous solution, adjust the equilibrium pH after the reaction at 6-8. Take the reacted organic phase and deionized water in a ratio of 1:10 and fully mix and wash the organic phase. After the washed organic phase was dehydrated by a centrifuge at 2000 rpm, it was placed in an environment of 4° C. and aged for 48 hours to prepare a vanadium-based liquid-phase catalyst.

[0055] Take 50ml of the catalyst prepared above, pass argon gas at 100°C for 30 minutes, and then feed the reaction gas, the reaction gas is composed of NH 3 , NO, SO 2 , O 2 and diluent N 2 Composition, where NH 3 , NO is 1000ppm, SO 2 500ppm, O 2 5%. Control airspeed 10000h -1 , the reaction temperature is 200°C, and the residence time in the liquid phase catalyst is 1s. After the reaction, SO 2 The conversion rate reac...

Embodiment 2

[0060] Prepare an aqueous solution to be reacted, which contains 0.1mol / L sodium metavanadate, 0.2mol / L sodium molybdate, and 0.2mol / L sodium tungstate; compare the resulting aqueous solution to be reacted with the quaternary ammonium salt N263 by 2: 1 mix, by supplementing with 1:1 H 2 SO 4 Aqueous solution, adjust the equilibrium pH after the reaction at 6-8. Take the reacted organic phase and deionized water in a ratio of 1:10 and fully mix and wash the organic phase. After the washed organic phase was dehydrated by a centrifuge at 2000 rpm, it was placed in an environment of 100° C. for 48 hours of static aging to prepare a vanadium-based liquid-phase catalyst containing Mo and W.

[0061] Take 50ml of the catalyst prepared above, pass argon gas at 100°C for 30 minutes, and then feed the reaction gas, the reaction gas is composed of NH 3 , NO, SO 2 , O 2 and diluent N 2 Composition, where NH 3 , NO is 1000ppm, SO 2 500ppm, O 2 5%. Control airspeed 10000h -1 , th...

Embodiment 3

[0063] Prepare an aqueous solution to be reacted, which contains 0.1mol / L sodium metavanadate, 0.2mol / L sodium molybdate, and 0.2mol / L sodium tungstate; prepare tertiary amine TOA, primary amine Primene JM-T, and secondary amine 7203 The organic phase mixed at a volume ratio of 1:1:1; the organic phase and the aqueous solution are mixed at a ratio of 1:1, and the H 2 SO 4 Aqueous solution, adjust the equilibrium pH after the reaction at 6-8. Take the reacted organic phase and deionized water in a ratio of 1:10 and fully mix and wash the organic phase. After the washed organic phase is dehydrated by a 2000rpm centrifuge, it is placed in an environment of 100°C and mixed with n-triacane in a volume ratio of 1:1, and then left to mature for 48 hours to prepare a vanadium-based compound containing Mo and W. liquid phase catalyst.

[0064] Take 50ml of the catalyst prepared above, pass argon gas at 100°C for 30 minutes, and then feed the reaction gas, the reaction gas is compose...

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Abstract

The invention relates to a vanadium-based liquid-phase catalyst prepared with an extraction reaction of organic amine to oxysalts of metals such as vanadium. Through the controlling over operation conditions, vanadium-containing catalytically active substances and co-catalysts in a water solution are extracted into an organic phase; a curing treatment is carried out, such that the vanadium liquid-phase catalyst is prepared. The catalyst is not sensitive to air, water, or acid, and has good thermal stability. The synthesizing, circulation, and regeneration methods of the catalyst are simple, such that industrialized production can easily be realized. In flue gas denitration, the catalyst shows high contact area and high catalytic activity.

Description

technical field [0001] The invention relates to a vanadium-based liquid-phase catalyst and a preparation method thereof, in particular to a method for loading a vanadium-based catalyst in an organic liquid phase by an extraction method. Background technique [0002] Vanadium compounds are a class of catalysts with high catalytic activity, which can be used to catalyze the oxidation of sulfur oxides (SO x ), nitrogen oxides (NO x , mainly referring to NO and NO 2 ), so it is used for simultaneous desulfurization and denitrification in the treatment of industrial flue gas such as coal-fired boilers and thermal power plants, and is also widely used in the catalytic oxidation process of sulfuric acid, phthalic anhydride, and maleic anhydride. [0003] Previous studies have shown that SO in gas x , NO x Pollutants are the main pollutants in industrial waste gas such as flue gas. Selective catalytic oxidation is a widely used treatment technology at home and abroad. Vanadium-b...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/36B01D53/86B01D53/60
CPCY02A50/20
Inventor 林晓曹宏斌李杰张懿
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI