Preparation method for solid catalyst for ozone heterogeneous oxidization

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 poor toxicity resistance, easy loss of catalytic activity, Problems such as low catalyst adsorption

Inactive Publication Date: 2017-08-04
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 stir

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, 4.75g montmorillonite, 5.75g sylvite, 6.75g amazonite, 7.75g lithium limestone, lithium hypochlorite and bis(acetylacetonate) beryllium weight (3g): porous material Weight (31.5g) = 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; in a 500ml ultrasonic reactor, put the pore-enlarging modified carrier 31g, then add 3.25g nonylphenol base diquaternary ammonium salt and be dissolved in the aqueous solution of 100ml deionized wate...

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, 1.85g montmorillonite, 2.05g sylvite, 2.25g amazonite, 2.45g lithium limestone, lithium hypochlorite and bis(acetylacetonate) beryllium weight (0.6g): Porous material The weight (11.7g)=1:19.5, heat up to 48°C, continue to stir and react 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 Sexual carrier 11.5g, add the aqueous solution that 2.2g nonylphenol base biquaternary ammonium salt is dissolved in 2...

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Abstract

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. The preparation method is to use perlite, albite, montmorillonite, sylvite, amazonite and lithium limestone porous materials as carriers, and after the carrier is modified by lithium hypochlorite and bis(acetylacetonate) beryllium, adding Surfactant nonylphenol-based diquaternary ammonium salt is subjected to surface activation treatment under the action of ultrasonic waves, and then the ultrasonic surface activation carrier is combined with the composite mineralizer borax and potassium sulfate in a hydrothermal reaction kettle, and the catalytic activity auxiliary agent precursor 1,1 , Neodymium 1‑trifluoroacetylacetonate, terbium triacetate hydrate, ytterbium tris(trifluoromethanesulfonimide) ytterbium, lutetium carbonate hydrate rare earth metal organic compound, catalytic active center component precursor common transition metal organic compound cobalt gluconate , nickel citrate, catechol ethylenediamine tungsten complex and noble metal compound hexachloroosmium dipotassium, under the action of emulsifier N-oleoyl-N', N'-diethylethylenediamine hydrochloride Hydrothermal reaction, after the reaction product is dried to remove moisture, it is burned in a muffle furnace at a certain temperature to obtain a solid catalyst for ozone heterogeneous oxidation.

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): B01J23/89B01J20/20B01J20/30C02F1/78
CPCB01J23/8993B01J20/041B01J20/046B01J20/06B01J20/106B01J20/12B01J20/16B01J20/20B01J35/10B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/725C02F1/78C02F2305/02
Inventor 朱明何汐然王麒麟
Owner SICHUAN NORMAL UNIVERSITY
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