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Preparation method of ozone heterogeneous oxidation solid catalyst

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 performance of catalysts such as adsorption, poor anti-toxicity Influence, the catalyst loses catalytic activity, the catalyst has poor anti-toxicity and other problems, and achieves good environmental and economic benefits, enhanced anti-toxicity, and high adsorption capacity.

Inactive Publication Date: 2017-08-22
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 sodium saltpeter, 7.75g dolomite, lithium hypochlorite and bis(acetylacetonate) beryllium (3g): the weight of porous mineral material (31.5g) = 1:9.5, heated to 36°C , 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 dimethyl hexadecyl ethyl Ammonium ethyl sulfate is dissolved in 100ml of deionized water in an aqueous solution, the weight concentration of the aqueou...

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 of g boronite, 2.25g sodium saltpetre, 2.45g dolomite, lithium hypochlorite and bis(acetylacetonate) beryllium (0.6g): the weight of porous mineral material (11.7g)=1:19.5, heated to 48 ℃, continue to stir and react for 5.8 hours, wash and filter, and dry to constant weight to obtain 11.5g of pore-enlarging modified carrier; in a 100ml ultrasonic reactor, put 11.5g of pore-enlarging modified carrier, and then add 2.2g of dimethylhexadecane Ammonium ethyl ethyl sulfate is dissolved in 26ml of deionized water in an aqueous solution, the weight concentration of the aqueou...

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PUM

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Abstract

The invention relates to a preparation method of an ozone heterogeneous oxidation solid catalyst and belongs to the technical field of environment protection and chemical catalysts. Activated carbon, carnallite, potassium feldspar, camsellite, nitratine and dolomite are utilized as carriers; after the carriers are chambered by lithium hypochlorite and bis(acetylacetone), a surface active agent of dimethyl cetyl ethyl sulfate ammonium is added to perform activating treatment under ultrasonic wave action; the carriers generate hydrothermal reaction with complex mineralizers of borax and potassium sulphate, catalytic activity additive precursors of samarium 2,4-pentanedionate hydrate, tris(4,4,4-trifluoro-1-1(2-thiophene)-1,3-butanedione) europium, tri(6,6,7,7,8,8,8-hepta fluorin-2,2-dimethyl-3,5-octylene diketone) drysprosium (III) and lutetium carbonate hydrate and catalytic activity central precursors of cobalt gluconate, L-molybdenum aspartate, catechol ethylene diamine tungsten coordination compound and dichlorodiammine platinum in a hydrothermal reaction kettle under action of an emulsifier of dodecyl dihydroxypropyl aimethyl sulfate ammonium; the zone heterogeneous oxidation solid catalyst can be obtained through sintering in a muffle furnace after drying and dewatering.

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
CPCB01J20/04B01J20/043B01J20/046B01J20/06B01J20/16B01J20/20C02F1/281C02F1/725C02F1/78B01J23/8993B01J37/084B01J37/10C02F2101/30C02F2305/02B01J2220/4812B01J2220/4806B01J2220/42B01J35/617B01J35/60B01J35/635B01J35/647
Inventor 夏梦琦朱明官悦
Owner SICHUAN NORMAL UNIVERSITY
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