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 poor toxicity resistance, easy loss of catalytic activity, Solve the problems of low catalyst adsorption, achieve strong adsorption, improve anti-toxicity and catalytic activity, and inhibit melting and precipitation

Inactive Publication Date: 2017-09-15
SICHUAN NORMAL UNIVERSITY
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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 organometallic compounds as catalyst precursors, common transition metal organic compounds and noble metal compounds as catalyst active center precursors, and multi-component porous supports are prepared by hydrothermal reaction and high-temperature calcination to prepare multi-metal-containing ozone heterogeneous oxidation 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 for 3h-6h,

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  • Preparation method of ozone heterogeneous oxidation solid catalyst
  • Preparation method of ozone heterogeneous oxidation solid catalyst

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[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; 2.75g wheat rice with deionized water, washed to neutrality, dried at 103℃ to remove water, and then sieved through -200 mesh to +400 mesh standard sieve Stone, 3.75g wollastonite, 4.75g activated carbon, 5.75g carnallite, 6.75g illite, 7.75g sodium borite, lithium hypochlorite and bis(acetylacetone) beryllium weight (3g): of porous material Weight (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 the expanded modified carrier into a 500ml ultrasonic reactor 31g, then add 3.25g of tetradecyltributylammonium chloride in 100ml of deionized water solution, the weight concentration of the aq...

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; 1.45g wheat rice which is washed with deionized water until it is neutral, dried at 103℃ to remove water, and then sieved through -200 mesh to +400 mesh standard sieve Stone, 1.65g wollastonite, 1.85g activated carbon, 2.05g carnallite, 2.25g illite, 2.45g sodium borite, lithium hypochlorite and bis(acetylacetone) beryllium weight (0.6g): porous material The weight (11.7g)=1:19.5, the temperature is raised to 48℃, the reaction is continued for 5.8h, filtered, and dried at 105℃ to obtain 11.5g of the expanded modified carrier; in a 100ml ultrasonic reactor, put into the expanded modified carrier 11.5g of the carrier, and then add 2.2g of tetradecyltributylammonium chloride in ...

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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. Medical stone, wollastonite, activated carbon, carnallite, illite and sodium borite are used as carriers, and after the carrier is modified by lithium hypochlorite and bis(acetylacetonate) beryllium, the surfactant tetradecane is added Tributyl ammonium chloride is subjected to surface activation treatment under the action of ultrasonic waves, and then the activated carrier is mixed with the composite mineralizer borax and potassium sulfate in a hydrothermal reaction kettle, and the precursor of the catalytic activity auxiliary agent scandium (III) isopropoxide, three (4,4,4‑trifluoro‑1‑(2‑thiophene)‑1,3‑butanedione)europium, tris(2,2,6,6‑tetramethyl‑3,5‑heptanedionate ) gadolinium, holmium oxalate decahydrate, catalytic active center component precursor titanocene ring substituted salicylic acid complex, copper glutamate, osmium hexachloride dipotassium, dichlorodiammine platinum, in emulsifier double dodecyl Under the action of alkyl dimethyl ammonium bromide, carry out hydrothermal reaction, dry to remove moisture, and ignite in a muffle furnace 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): B01J23/89B01J35/10B01J37/08B01J37/10B01J37/34B01J20/20B01J20/28B01J20/30
CPCB01J23/8946B01J20/06B01J20/20B01J20/28054B01J35/10B01J37/084B01J37/10B01J37/343
Inventor 朱明江燕妮岳馥莲
Owner SICHUAN NORMAL UNIVERSITY
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