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Preparing method of ozone heterogeneous oxidized solid catalyst

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

Inactive Publication Date: 2017-08-25
SICHUAN NORMAL UNIVERSITY
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  • 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 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, filter, and dry the reaction product at 102°C-106°C to obtain a modified carrier for pore expansion; pore expansion Put the modified carrier into the ultrasonic reactor, add the aqueous solution prepared by C component and deionized water, the weight concentration of C component is 3%~8%, stir and mix evenly, control the ultrasonic power density to 0.3~0.8W / m 3 , frequency 20kHz ~ 30kHz, 40 ℃ ~ 55 ℃, ultrasonic vibration 2h ~ 5h, the ultrasonic surface activation carrier mixture is obtained; the ultrasonic surface activation carrier mixture is transferred to the hydrothermal reaction kettle, and then add D component and deionized water to prepare The aqueous solution, the weight concentration of D component is 40% ~ 55%, by weight, the weight ratio of D component deionized aqueous solution: ultrasonic surface activation carrier mixture = 1: (1.5 ~ 2), control temperature 120 ℃ ~ 180°C, the hydrothermal reaction time is 8h~16h, and then dried to obtain fine particles; the fine particles are burned in a muffle furnace at 600°C~950°C for 3h~8h to obtain a solid catalyst for ozone heterogeneous oxidation

Method used

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Examples

Experimental program
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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 -200 mesh to +400 mesh standard sieve 2.75g γ-oxidized Aluminum, 3.75g barite, 4.75g brucite, 5.75g serpentinite, 6.75g fly ash, 7.75g coal gangue, lithium hypochlorite and bis(acetylacetonate)beryllium weight (3g): porous material The weight (31.5g)=1:10.5, heat up to 36°C, continue to stir and react for 3.2h, filter, dry at 103°C and obtain 31g of pore-enlarging modified carrier; in a 500ml ultrasonic reactor, put pore-enlarging modified Carrier 31g, then add 3.25g dimethyl dioctadecyl ammonium chloride and dissolve in 100ml deionized water aqueous solution, the weight c...

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: bis(acetylacetonate) beryllium weight ratio = 1:1.5; add deionized water to wash to neutral, dry at 103°C to remove moisture, and then sieve -200 mesh to +400 mesh standard sieve 1.45g gamma-oxidized Aluminum, 1.65g barite, 1.85g brucite, 2.05g serpentinite, 2.25g fly ash, 2.45g coal gangue, lithium hypochlorite and bis(acetylacetonate)beryllium weight (0.6g): Porous The weight of the material (11.7g)=1:19.5, heat up to 48°C, continue to stir and react for 5.8h, filter, and dry at 105°C to obtain a pore-expanding modified carrier of 11.5g; put it into a 100ml ultrasonic reactor Modified carrier 11.5g, add the aqueous solution that 2.2g dimethyl dioctadecyl ammonium chloride is dissolved in 26ml deionized water ...

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PUM

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Abstract

The invention relates to a preparing method of an ozone heterogeneous oxidized solid catalyst, and belongs to the technical field of environment-friendly and chemical catalysts. The preparing method comprises the steps of after using gamma-aluminium oxide, barite, brucite, serpentine, fly ash and coal gangue as carriers to expand pore sizes through lithium chlorate and beryllium acetylacetonate, adding a surfactant dimethyl chloride dioctadecyl to conduct activating treatment under the action of ultrasonic waves, then making the carriers conduct a hydrothermal reaction with a composite mineralizer borax and potassium sulfate, a catalytic activity active auxiliary tetrakis(2,2,6,6-tetramethyl-3,5-heptanedionato)cerium(IV), tris[4,4,4-trifluoro-1-(2-thienyl)-1,3-butanedionato-O,O']europium, tris(2,2,6,6-tetramethyl-3,5-heptanedionato)gadolinium and tris[N,N-bis(trimethylsilyl)amide]erbium, catalytic activity center precursor lysine manganese, ammonium zirconium carbonate, gold potassium chloride and dichlorodiamminoplatinum in a hydrothermal reaction kettle under the action of an emulsion oleamide propyl trimethyl methyl sulfate ammonium, and after conducting drying to remove moisture, conducting calcination in a muffle furnace to obtain the ozone heterogeneous oxidized 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): B01J23/68B01J32/00B01J20/20B01J20/30C02F1/28C02F1/78C02F101/30
CPCB01J20/041B01J20/045B01J20/06B01J20/08B01J20/10B01J20/103B01J20/20C02F1/281C02F1/725C02F1/78B01J23/688B01J37/084B01J37/10C02F2101/30C02F2305/02B01J2220/4812B01J2220/42B01J2220/4806B01J35/60
Inventor 朱明范耀月周小澜
Owner SICHUAN NORMAL UNIVERSITY
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