Preparation method of ozone heterogeneous oxidation solid catalyst

A heterogeneous oxidation, solid catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low catalyst adsorption, poor toxicity resistance, Easy to lose catalytic activity and other problems

Inactive Publication Date: 2017-08-18
SICHUAN NORMAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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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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 of perlite with -200 mesh to +400 mesh standard sieve , 3.75g albite feldspar, 4.75g bentonite, 5.75g polyhalite, 6.75g sodium saltpetre, 7.75g dolomite, weight of lithium hypochlorite and bis(acetylacetonate) beryllium (3g): weight of porous material (31.5 g)=1:10.5, heat up to 36°C, continue to stir 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, and then Add 3.25g of 2,6-bis(diethylaminomethyl)-4-nonylphenol-benzene quaternary ammonium chloride and dissolve ...

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 of bis(acetylacetonate) beryllium=1:1.5; add deionized water to wash to neutral, dry at 103°C to remove moisture, and then sieve 1.45g perlite of -200 mesh to +400 mesh standard sieve , 1.65g albite feldspar, 1.85g bentonite, 2.05g polyhalite, 2.25g sodium saltpeter, 2.45g dolomite, weight of 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 11.5g of pore-enlarging modified carrier g, then add 2.2g of 2,6-bis(diethylaminomethyl)-4-nonylphenol-benzene quaternary ammonium chloride solutio...

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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 engineering catalysts. The preparation method includes using perlite, albite, bentonite, polyhalite, nitratine and dolomite as carriers; subjecting the carriers to pore expanding through lithium hypochlorite and bis(acetylacetone)beryllium, and adding a surfactant 2, 6-di(diethylamino methyl)-4-nonyl phenol-chlorobenzene quaternary ammonium salt, activating under ultrasonic action; enabling the activated carriers to be in hydrothermal reaction with composite mineralizing agent borax and potassium sulfate, catalytic active auxiliary precursor 1, 1, 1-trifluoroacetylacetone neodymium, holmium oxalate decahydrate, tri[N, N-bis(trimethylsilane)amine]erbium, andtrifluoromethane thulium sulfonate (III) and catalytic activity central precursor cobalt gluconate, nickel citrate, potassium tetrachloroaurate and hexanitroso rhodium trisodium in a hydrothermal reaction kettle under action of an emulsifier diethyl maleate bis(chlorinated dodecyl dimethyl ammonium); drying for removing water; firing in a muffle furnace to obtain the ozone heterogeneous oxidation solid catalyst.

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
CPCB01J23/894B01J20/04B01J20/043B01J20/045B01J20/06B01J20/106B01J20/12B01J20/16B01J20/20B01J35/10B01J35/1023B01J35/1042B01J35/1061B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/281C02F1/725C02F1/78C02F2101/30C02F2305/02
Inventor 朱明何汐然王麒麟
Owner SICHUAN NORMAL UNIVERSITY
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