Preparation method of ozone heterogeneous oxidation solid catalyst

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 easy loss of catalytic activity and catalyst adsorption Low resistance, poor toxicity resistance and other issues

Inactive Publication Date: 2017-08-18
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 magnesium spinel, 7.75g peridotite, 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 nonylphenol base diquaternary ammonium salt and be dissolved in the aqueous solution of 100ml deioni...

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 potash salt, 2.25g magnesium spinel, 2.45g peridotite, weight of lithium hypochlorite and bis(acetylacetonate) beryllium (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 nonylphenol base biquaternary ammonium salt is dissolved in 26ml...

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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 environment protection and chemical engineering catalysts. The preparation method includes using perlite, albite, montmorillonite, sylvinite, magnesium spinel and olivinite as carriers; subjecting the carriers to pore expanding through lithium hypochlorite and bis(acetylacetone)beryllium, and adding a surfactant nonyl phenol diquaternary ammonium salt, activating under ultrasonic action; enabling the activated carriers to be in hydrothermal reaction with composite mineralizing agent borax and potassium sulfate, catalytic active auxiliary precursor 1, 1, 1-trifluoroacetylacetone neodymium, terbium triacetate hydrate, tri[N, N-bis(trimethyl silane)amine]erbium and lutenium carbonate hydrate and catalytic activity central precursor cobalt gluconate, nickel citrate, catechol ethanediamine tungsten complex and terpyridyl ruthenium chloride hexahydrate in a hydrothermal reaction kettle under action of an emulsifier oleamide propyl trimethyl ammonium methyl sulfate; drying for removing water; firing 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): B01J23/89B01J32/00C02F1/28C02F1/78C02F101/30
CPCB01J23/002B01J23/8993B01J35/023B01J35/026B01J35/1023B01J35/1038B01J35/1042B01J35/1061B01J2523/00C02F1/281C02F1/725C02F1/78C02F2101/30
Inventor 朱明何汐然王麒麟
Owner SICHUAN NORMAL UNIVERSITY
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