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Method of preparation of solid catalyst by ozone heterogeneous oxidation

A heterogeneous oxidation and solid catalyst technology, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc. It can solve the problem of catalyst performance such as adsorption and toxicity resistance impact, catalyst loss of catalytic activity, easy loss of catalytic activity and other issues, to achieve good environmental and economic benefits, enhance anti-toxicity, and inhibit smelting out

Inactive Publication Date: 2017-08-25
SICHUAN NORMAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the wide variety of pollutants and the complex chemical composition of wastewater, it will have adverse effects on the performance of the catalyst, such as adsorption and anti-toxicity, and the catalyst will easily lose its catalytic activity.
At present, the main problems of the preparation method of ozone heterogeneous oxidation solid catalyst are small adsorption capacity, low adsorption selectivity, poor toxicity resistance of the catalyst, and easy loss of catalytic activity; development and use of multi-component porous carriers to increase the adsorption of the catalyst Capacity, enhanced adsorption selectivity, using rare earth metals, transition metals and noble metals to form multi-metal catalytic active centers to improve catalyst anti-toxicity and catalytic activity The preparation method of ozone heterogeneous oxidation solid catalyst has greater environmental benefits and higher Practical value

Method used

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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: the weight ratio=1:1.2 of bis(acetylacetonate) beryllium; add 2.75g activated carbon, 3.75g carnallite, 4.75g potassium feldspar, 5.75 The weight of g boronite, 6.75g aluminum hydroxide, 7.75g lapis lazuli, lithium hypochlorite and bis(acetylacetonate) beryllium (3g): the weight of porous mineral material (31.5g) = 1:9.5, heated to 36 ℃, continue to stir and react for 3.2h, wash and filter, and obtain 31g of pore-enlarging modified carrier after drying to constant weight; in a 500ml ultrasonic reactor, put 31g of pore-enlarging modified carrier, and then add 3.25g of dimethylhexadecyl ethyl ether Ammonium ethyl sulfate is dissolved in 100ml of deionized water in aqueous solution, the weight concentration of the...

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: the weight ratio=1:1.5 of bis(acetylacetonate) beryllium; add 1.45g activated carbon, 1.65g carnallite, 1.85g potassium feldspar, 2.05 The weight (0.6g) of g boronite, 2.25g aluminum hydroxide, 2.45g lapis lazuli, lithium hypochlorite and bis(acetylacetonate) beryllium: the weight of porous mineral material (11.7g)=1:19.5, heating up to 48°C, continue to stir and react for 5.8 hours, wash and filter, dry and constant weight to obtain 11.5g of pore-enlarging modified carrier; put 11.5g of pore-enlarging modified carrier into a 100ml ultrasonic reactor, and then add 2.2g of dimethylhexadecane Ammonium alkyl ethyl ethyl sulfate is dissolved in 26ml of deionized water, the weight concentration of the aqueous solutio...

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PUM

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Abstract

The invention relates to a method of preparation of solid catalyst by ozone heterogeneous oxidation, belongs to the technical field of environmental protection and chemical engineering catalysts. Activated carbon, carnallite, potassium feldspar, magnesium borate ore, aluminum hydroxide and lapis lazuli are adopted as carriers after subjecting to bore-reaming by lithium hypochlorite and di-(acetylacetone) beryllium, activating treatment is conducted by the subjoining of surfactant dimethyl cetyl alkyl ethyl ammonium ethyl sulphate under the action of ultrasonic waves, the carriers are subject to hydrothermal reaction in a hydrothermal reaction kettle with a composite mineralizer borax and potassium sulfate, precursors of catalytic coagent acetyl acetone samarium, tri-(4, 4, 4-trifluoro-1-(2-thiophene)-1, 3-diacetyl) europium, tri-(6, 6, 7, 7, 8, 8, 8-sevoflurane-2, 2-dimethyl-3, 5-octylene diketone) dysprosium (III), tri-(trifluoromethane sulfonyl imine) ytterbium, cobalt gluconate, L-aspartate amino acid molybdenum, catechol ethylenediamine tungsten complex and tetrachloro dihydrate iridium under the action of emulsifying agent octadecyl di-hydroxyethyl methyl ammonium sulfate, after stoving, the moisture content is removed, and a solid catalyst by ozone heterogeneous oxidation is obtained by firing in a muffle furnace.

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
CPCB01J20/04B01J20/045B01J20/046B01J20/06B01J20/08B01J20/16B01J20/20C02F1/281C02F1/725C02F1/78B01J23/8993B01J37/084B01J37/10C02F2101/30C02F2305/02B01J2220/4812B01J2220/4806B01J2220/42B01J35/60B01J35/617B01J35/635B01J35/647
Inventor 熊文萱朱明岳馥莲
Owner SICHUAN NORMAL UNIVERSITY
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