Preparation method for solid catalyst for ozone heterogeneous oxidization

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, poor resistance to toxicity, The problem of low adsorption of catalysts can achieve the effects of improving anti-toxicity and catalytic activity, strong adsorption, and inhibiting precipitation.

Inactive Publication Date: 2017-08-04
SICHUAN NORMAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
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Problems solved by technology

[0004] In view of the problems of low catalyst adsorption, poor anti-toxicity and easy loss of catalytic activity in the current preparation method of ozone heterogeneous oxidation solid catalyst, a multi-component porous carrier was developed to enhance the adsorption of the catalyst through pore expansion and surface activation. Rare earth metal organic compounds as precursors of catalytic active additives, common transition metal organic compounds and noble metal compounds as precursors of catalytic active centers and multi-component porous carriers through hydrothermal reaction and high temperature calcination to prepare ozone heterogeneous oxidation containing multiple metals The preparation method of solid catalyst to improve the anti-toxicity and catalytic activity of the catalyst is characterized in that component A and deionized water are added into a sealable reactor and stirred to prepare an aqueous solution, and the weight concentration of component A is controlled to be 2% to 6%. After the preparation is completed, add component B under stirring, raise the temperature to 35°C-50°C, continue to st...

Method used

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  • Preparation method for solid catalyst for ozone heterogeneous oxidization

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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 -200 mesh to +400 mesh standard sieve 2.75g γ-oxidized Weight of aluminum, 3.75 g barite, 4.75 g activated carbon, 5.75 g carnallite, 6.75 g bentonite, 7.75 g polyhalite, lithium hypochlorite and bis(acetylacetonate)beryllium (3 g): weight of porous material ( 31.5g) = 1:10.5, heat up to 36°C, continue stirring for 3.2h, filter, dry at 103°C and obtain 31g of pore-enlarging modified carrier; put 31g of pore-enlarging modified carrier into a 500ml ultrasonic reactor, Then add 3.25g ditetradecyl dimethyl ammonium chloride and be dissolved in the aqueous solution of 100ml dei...

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 -200 mesh to +400 mesh standard sieve 1.45g gamma-oxidized Weight of aluminum, 1.65g barite, 1.85g activated carbon, 2.05g carnallite, 2.25g bentonite, 2.45g polyhalite, lithium hypochlorite and bis(acetylacetonate)beryllium (0.6g): weight of porous material (11.7g)=1:19.5, heat up to 48°C, continue to stir for 5.8h, filter, dry at 105°C and obtain 11.5g of pore-enlarging modified carrier; in a 100ml ultrasonic reactor, put the pore-enlarging modified carrier 11.5g, then add 2.2g ditetradecyl dimethyl ammonium chloride dissolved in 26ml deionized water aqueous solution, the...

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Abstract

The invention relates to a preparation method for a solid catalyst for ozone heterogeneous oxidization and belongs to the technical field of an environment-friendly and chemical catalyst. The preparation method comprises the following steps: taking gamma-aluminum oxide, barite, activated carbon, carnallite, bentonite and polyhalite as a carrier; modifying the carrier by broaching with lithium hypochlorite and bis(acetylacetone) beryllium, and then adding surfactant bidecalkyl dimethyl ammonium chloride and performing surface activating treatment under the effect of ultrasonic wave; performing hydrothermal reaction on the carrier, a compound mineralizer including borax and potassium sulphate, catalytic activated assistant precursors, including 4(2, 2, 6, 6, 6-tetramethyl-3, 5-heptanedione) cerium (IV), 1,1,1-trifluoroacetylacetone neodymium, tricyclopentadiene promethium and tri(4,4,4-trifluoro-1-(2-thiophene)-1,3-butanedione) europium and catalytic active core component precursors, including manganese lysine, cupric glutamate and potassium dicyanoargentate and dichlorodiamminoplatinum in a hydrothermal reaction kettle under the effect of chlorinated methyl acryloyl ethyltrimethylammonium chloride used as an emulsifier; drying and dewatering the reaction product; burning in a muffle furnace under a certain temperature, thereby acquiring the solid catalyst for ozone heterogeneous oxidization.

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

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IPC IPC(8): B01J23/89B01J32/00B01J20/20B01J20/30C02F1/28C02F1/78C02F101/30
CPCB01J23/8986B01J20/045B01J20/046B01J20/06B01J20/08B01J20/12B01J20/20B01J35/10B01J35/1023B01J35/1042B01J35/1061B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/281C02F1/725C02F1/78C02F2101/30C02F2305/02
Inventor 朱明周小澜刘阳
Owner SICHUAN NORMAL UNIVERSITY
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