Method for preparing ozone heterogeneous oxidation solid catalysts

A heterogeneous oxidation, solid catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of easy loss of catalytic activity and low catalyst adsorption. , poor anti-toxicity and other problems, to achieve the effect of improving anti-toxicity and catalytic activity, inhibiting precipitation, and strong adsorption

A heterogeneous oxidation, solid catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of easy loss of catalytic activity and low catalyst adsorption. , poor anti-toxicity and other problems, to achieve the effect of improving anti-toxicity and catalytic activity, inhibiting precipitation, and strong adsorption

CN107051445AInactive Publication Date: 2017-08-18SICHUAN NORMAL UNIVERSITY

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0007] Embodiment 1:1.35g lithium hypochlorite, 1.65g bis(acetylacetonate) beryllium, 140ml deionized water, join volume and be that in the sealable reactor of 500ml, stir and mix evenly, the weight concentration of this aqueous solution is 2.1%, times Lithium chlorate: bis(acetylacetonate) beryllium weight ratio=1:1.2; add deionized water to wash to neutral, dry at 103°C to remove moisture, and then sieve 2.75g attapulgite of -200 mesh to +400 mesh standard sieve Weight of soil, 3.75g diopside, 4.75g sepiolite, 5.75g barite, 6.75g perlite, 7.75g albite, lithium hypochlorite and bis(acetylacetonate)beryllium (3g): porous material The weight (31.5g)=1:10.5, heat up to 36°C, continue to stir and react for 3.2h, filter, dry at 103°C and obtain 31g of pore-enlarging modified carrier; in a 500ml ultrasonic reactor, put pore-enlarging modified Carrier 31g, then add 3.25g of dieicosyldimethylammonium chloride dissolved in 100ml deionized water aqueous solution, the weight concentrati...

Embodiment 2

[0008] Embodiment 2: 0.24g lithium hypochlorite, 0.36g bis(acetylacetonate) beryllium, 10ml deionized water, join volume and be that in the sealable reactor of 100ml, stir and mix evenly, the weight concentration of this aqueous solution is 5.7%, times Lithium chlorate: bis(acetylacetonate) beryllium weight ratio=1:1.5; add deionized water to wash to neutral, dry at 103°C to remove moisture, and then sieve 1.45g attapulgite of -200 mesh to +400 mesh standard sieve Weight of soil, 1.65g diopside, 1.85g sepiolite, 2.05g barite, 2.25g perlite, 2.45g albite, lithium hypochlorite and bis(acetylacetonate)beryllium (0.6g): Porous The weight of the material (11.7g)=1:19.5, heat up to 48°C, continue to stir and react for 5.8h, filter, and dry at 105°C to obtain a pore-expanding modified carrier of 11.5g; put it into a 100ml ultrasonic reactor Modified carrier 11.5g, add the aqueous solution of 2.2g dieicosyl dimethyl ammonium chloride dissolved in 26ml deionized water, the weight conce...

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PUM

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Abstract

The invention relates to a method for preparing ozone heterogeneous oxidation solid catalysts, and belongs to the technical field of environmental protection and chemical catalysts. The method includes carrying out pore expansion and modification on carriers which are attapulgite, diopside, sepiolite, baryta feldspar, perlite and albite porous materials by the aid of lithium hypochlorite and bis (acetylacetone) beryllium; adding chlorinated bis-eicosyl dimethyl ammonium into the carriers and carrying surface activation treatment on the carriers under the effects of ultrasonic waves; carrying out hydrothermal reaction on the carriers which are subjected to ultrasonic surface activation, borax, potassium sulfate, tetra-(2, 2, 6, 6-tetramethyl-3, 5-heptadione acid) cerium (IV), tri-[4, 4, 4-trifluoro-1-(2-thiophene)-1, 3-butanedione] europium, tri-(6, 6, 7, 7, 8, 8, 8-heptafluoro-2, 2-dimethyl-3, 5-octene diketone) dysprosium (III), tri-[N, N-bis (trimethylsilane) amine] erbium rare earth metal organic compounds, manganese lysine, ammonium zirconium carbonate, dichlorotetraaminopalladium and tetrachloro iridium dihydrate in hydrothermal reaction kettles under the effect of nitrophenol benzyldimethyl ammonium bromide which is an emulsifier; drying reaction products to remove moisture; burning the reaction products in muffle furnaces at the certain temperatures to obtain the ozone heterogeneous oxidation solid catalysts. The chlorinated bis-eicosyl dimethyl ammonium is used as a catalyst. The borax and the potassium sulfate are used as composite mineralizers, the tetra-(2, 2, 6, 6-tetramethyl-3, 5-heptadione acid) cerium (IV), the tri-[4, 4, 4-trifluoro-1-(2-thiophene)-1, 3-butanedione] europium, the tri-(6, 6, 7, 7, 8, 8, 8-heptafluoro-2, 2-dimethyl-3, 5-octene diketone) dysprosium (III) and the tri-[N, N-bis (trimethylsilane) amine] erbium rare earth metal organic compounds are used as catalytic active auxiliary precursors, the manganese lysine, the ammonium zirconium carbonate, the dichlorotetraaminopalladium and the tetrachloro iridium dihydrate are used as catalytic active central components, the manganese lysine is a common transition metal organic compound, and the dichlorotetraaminopalladium and tetrachloro iridium dihydrate are precious metal compounds.

Description

technical field [0001] The invention relates to a preparation method of a solid catalyst for ozone heterogeneous oxidation, which belongs to the technical fields of environmental protection and chemical catalysts. Background technique [0002] Ozone oxidation technology utilizes the strong oxidation ability of ozone, which can oxidize and decompose many organic pollutants, and is widely used in wastewater treatment. Ozone catalytic oxidation technology is divided into ozone homogeneous catalytic oxidation and ozone heterogeneous catalytic oxidation. Ozone homogeneous catalytic oxidation has catalysts that are difficult to separate, recycle and reuse, and the low utilization rate of ozone leads to high water treatment operation costs. Ozone heterogeneous catalytic oxidation technology has the advantages of easy separation and recovery of catalysts and reusable use, high ozone utilization rate, and high removal rate of organic pollutants, which reduces water treatment. The ad...

Claims

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Application Information

Patent Timeline
18 Aug 2017
Publication
CN107051445A
IPC
B01J23/656; B01J20/20; B01J20/28; B01J20/30; C02F1/28; C02F1/78; B01J32/00; C02F101/30
CPC
B01J20/06; B01J20/12; B01J20/20; C02F1/281; C02F1/725; C02F1/78; B01J20/28016; B01J23/6562
Inventors
朱明; 范耀月