Preparation method of ozone heterogeneous oxidation solid catalyst

A heterogeneous oxidation and solid catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of easy loss of catalytic activity, poor toxicity resistance, The problem of low catalyst adsorption, to achieve the effect of improving anti-toxicity and catalytic activity, strong adsorption, and inhibiting melting and precipitation

Inactive Publication Date: 2017-08-04
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 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 of ozone heterogeneous oxidation solid catalyst
  • Preparation method of ozone heterogeneous oxidation solid catalyst

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Embodiment 1

[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 pure diatom, 5.8g kyanite, 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, the wei...

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 erionite of -200 mesh to +400 mesh standard sieve , 1.65g garnet, 1.85g pure diatom, 2.05g kyanite, 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 water ...

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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 environmental-friendly and chemical engineering catalysts. The preparation method comprises the following steps: by taking erionite, garnet, diatom pure, kyanite, potassium feldspar and szaibelyite as a carrier, after chambering and modifying the carrier through lithium hypochlorite and di(acetylacetone) beryllium, adding a surfactant dodecyl trimethyl ammonium chloride for surface activating treatment under the action of ultrasonic waves; then performing a reaction on the ultrasonic surface activated carrier in a hydrothermal reaction kettle and a compound mineralizer borax and potassium sulfate and catalytic active auxiliary agent precursors isoproscandium oxide (III), a tri(hexafluoroacetyl acetone) yttrium (III) dihydrate, tri(3-trifluoro acetyl-D-camphor) praseodymium (III) and tri(trifluoromethane sulfimide) ytterbium; and performing a hydrothermal reaction with catalytic active central compound precursors a titanocene ring substituted salicylic acid complex, vanadium isonicotinoyl hydrazone pyruvate, cupric glutamate and dipotassium hexachloroosmate under the action of an emulsifier N-dodecyl dimethyl-N'-dodecyl-2-hydroxypropyl ammonium dichloride, drying a reaction product to remove water, and firing the reaction product 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
CPCB01J23/898B01J20/04B01J20/06B01J20/103B01J20/14B01J20/16B01J20/165B01J20/20B01J35/10B01J35/1023B01J35/1042B01J35/1061B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/281C02F1/725C02F1/78C02F2101/30C02F2305/02
Inventor 朱明丁瑶江燕妮
Owner SICHUAN NORMAL UNIVERSITY
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