Ozone heterogeneous oxidation solid catalyst preparation method

A heterogeneous oxidation, solid catalyst technology, applied in heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of easy loss of catalytic activity, catalyst adsorption It can improve the anti-toxicity and catalytic activity, inhibit the melting and precipitation, and have the effect of strong adsorption.

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

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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 stir

Method used

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Examples

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Example Embodiment

[0007] Example 1: 1.35g lithium hypochlorite, 1.65g bis(acetylacetone) beryllium, 140ml deionized water were added to a 500ml sealable reactor and stirred and mixed uniformly. The weight concentration of the aqueous solution was 2.1%. The weight ratio of lithium chlorate: bis(acetylacetone) beryllium=1:1.2; add deionized water to wash to neutrality, dry at 103°C to remove water, sieving 2.75g γ-oxidized by -200 mesh to +400 mesh standard sieve Aluminum, 3.75g barite, 4.75g talc, 5.75g spar, 6.75g aluminum hydroxide, 7.75g celestite, lithium hypochlorite and bis(acetylacetone) beryllium weight (3g): weight of porous material (31.5g)=1:10.5, heat up to 36°C, continue to stir and react for 3.2h, filter, dry at 103°C to obtain 31g of expanded modified carrier; put 31g of expanded modified carrier in a 500ml ultrasonic reactor , Then add 3.25g of dimethyl octadecyl ammonium chloride in 100ml of deionized water solution, the weight concentration of the aqueous solution is 3.1%, stir ...

Example Embodiment

[0008] Example 2: 0.24g lithium hypochlorite, 0.36g bis(acetylacetone) beryllium, 10ml deionized water were added to a 100ml sealable reactor and stirred and mixed uniformly. The weight concentration of the aqueous solution was 5.7%. The weight ratio of lithium chlorate: bis(acetylacetone) beryllium=1:1.5; add deionized water to wash to neutrality, dry at 103°C to remove water, sieving 1.45g γ-oxidized by -200 mesh to +400 mesh standard sieve Aluminum, 1.65g barite, 1.85g talc, 2.05g spar, 2.25g aluminum hydroxide, 2.45g celestite, lithium hypochlorite and bis(acetylacetone) beryllium weight (0.6g): porous material Weight (11.7g)=1:19.5, heat up to 48°C, continue to stir and react for 5.8h, filter, dry at 105°C to obtain 11.5g of expanded modified carrier; put into the expanded modified carrier in a 100ml ultrasonic reactor Carrier 11.5g, then add 2.2g dimethyl dioctadecyl ammonium chloride in 26ml deionized water solution, the weight concentration of the aqueous solution is 7....

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Abstract

The invention belongs to the technical field of environment protection and chemical catalysts and relates to an ozone heterogeneous oxidation solid catalyst preparation method. The preparation method includes: taking porous mineral materials including gamma-aluminum oxide, barite, talc, trona, aluminum hydroxide and celestite as carriers; subjecting the carriers to lithium hypochlorite and bis(acetylacetone)beryllium broaching modification; adding surfactant dioctadecyldimethyl ammonium chloride for surface activation under the action of ultrasonic waves; subjecting the carriers to hydrothermal reaction, with a complex mineralizer composed of borax and potassium sulfate, catalytic activity auxiliary agent precursors including tetra(2,2,6,6-tetramethyl-3,5-hydrochelidonic acid)cerium (IV), samarium acetylacetonate, tri(2,2,6,6-tetradimethyl-3,5-hydrochelidonic acid)gadolinium (III) and holmium oxalate decahydrate and catalytic activity central precursors including lysine manganese, L-aspartic acid molybdenum, trisodium rhodium hexanitrite and dipotassium hexachloroosmium, in a hydrothermal reactor under the action of m-nitrobenzyl dimethyl ammonium bromide serving as an emulsifying agent; drying to remove moisture, and firing in a muffle furnace at a certain temperature to obtain an 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): B01J23/656B01J32/00C02F1/28C02F1/78C02F101/30
CPCB01J23/002B01J23/6562B01J35/023B01J35/026B01J2523/00C02F1/281C02F1/725C02F1/78C02F2101/30
Inventor 朱明刘阳宋佳柠
Owner SICHUAN NORMAL UNIVERSITY
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