Preparation method for solid catalyst for ozone heterogeneous oxidization

A heterogeneous oxidation and solid catalyst technology, applied in the direction of heterogeneous catalyst chemical elements, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of poor toxicity resistance and catalyst adsorption Low, easy to lose catalytic activity and other issues, to achieve strong adsorption, inhibit smelting out, improve anti-toxicity and catalytic activity

Inactive Publication Date: 2017-08-04
SICHUAN NORMAL UNIVERSITY
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  • Abstract
  • Description
  • Claims
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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

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  • Preparation method for solid catalyst for ozone heterogeneous oxidization
  • Preparation method for solid catalyst for ozone heterogeneous oxidization

Examples

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Example Embodiment

[0007] Embodiment 1:1.4g lithium hypochlorite, 1.7g two (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 2.2%, times Lithium chlorate: the weight ratio of bis(acetylacetonate) beryllium=1:1.2; add deionized water to wash to neutral, dry at 103°C to remove moisture, and then sieve 2.8g erionite of -200 mesh to +400 mesh standard sieve , 3.8g garnet, 4.7g medical stone, 5.8g wollastonite, 6.7g potassium feldspar, 7.8g boronite, lithium hypochlorite and bis(acetylacetonate) beryllium weight (3.1g): Porous material The weight (31.6g)=1:10.2, heat up to 36°C, continue to stir and react for 3.2h, filter, dry at 103°C and obtain 30g of pore-expanding modified carrier; in a 500ml ultrasonic reactor, put pore-enlarging modified Carrier 30g, add the aqueous solution that 3.3g dodecyltrimethylammonium chloride is dissolved in 100ml deionized water again, ...

Example Embodiment

[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 erionite of -200 mesh to +400 mesh standard sieve , 1.65g garnet, 1.85g medical stone, 2.05g wollastonite, 2.25g potassium feldspar, 2.45g boronite, 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 Carrier 11.5g, add the aqueous solution that 2.2g dodecyltrimethylammonium chloride is dissolved in 26ml deionized...

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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 erionite, garnet, medical stone, wollastonite, potassium feldspar and boromagnesite porous material as the carrier, and after the carrier is modified by lithium hypochlorite and bis(acetylacetonate) beryllium to expand the pores, add The surface active agent dodecyltrimethylammonium chloride is subjected to surface activation treatment under the action of ultrasonic waves, and then the ultrasonic surface activation carrier is mixed with the composite mineralizer borax and potassium sulfate and the precursor of the catalytic activity auxiliary agent in a hydrothermal reaction kettle. Scandium (III) propoxide, tris(hexafluoroacetylacetonate) yttrium (III) dihydrate, lanthanum stearate, lutetium carbonate hydrate Rare earth metal organic compound, catalytic active center component precursor common transition metal organic compound Dioxocene Titanium ring substituted salicylic acid complex, vanadium pyruvate isonicotinoyl hydrazone, ferrous fumarate and noble metal compound hexachloroosmium dipotassium, under the action of emulsifier dodecyldimethylhydroxyethylammonium chloride 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): B01J23/89B01J32/00C02F1/28C02F1/78C02F101/30
CPCB01J23/002B01J23/898B01J35/023B01J35/026B01J35/1023B01J35/1042B01J35/1061B01J2523/00C02F1/281C02F1/725C02F1/78C02F2101/30
Inventor 朱明宋佳柠廖乾邑
Owner SICHUAN NORMAL UNIVERSITY
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