Preparation method for solid catalyst for ozone heterogeneous oxidization

A heterogeneous oxidation and solid catalyst technology, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc. It can solve the problem of catalyst performance such as adsorption and toxicity resistance impact, catalyst loss of catalytic activity, easy loss of catalytic activity and other issues, to achieve good environmental and economic benefits, enhance anti-toxicity, and inhibit smelting out

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

AI Technical Summary

Problems solved by technology

Due to the wide variety of pollutants and the complex chemical composition of wastewater, it will have adverse effects on the performance of the catalyst, such as adsorption and anti-toxicity, and the catalyst will easily lose its catalytic activity.
At present, the main problems of the preparation method of ozone heterogeneous oxidation solid catalyst are small adsorption capacity, low adsorption selectivity, poor toxicity resistance of the catalyst, and easy

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[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: the weight ratio=1:1.2 of bis(acetylacetonate) beryllium; add 2.75g activated carbon, 3.75g carnallite, 4.75g potassium feldspar, 5.75 The weight of g boronite, 6.75g magnesium spinel, 7.75g serpentinite, lithium hypochlorite and bis(acetylacetonate) beryllium (3g): the weight of porous mineral material (31.5g) = 1:9.5, heating To 36°C, continue to stir and react for 3.2h, wash and filter, dry and constant weight to obtain 31g of pore-enlarging modified carrier; in a 500ml ultrasonic reactor, put 31g of pore-enlarging modified carrier, and then add 3.25g of dimethylhexadecane Ammonium ethyl ethyl sulfate is dissolved in 100ml of deionized water, the weight concentration of the aqueous solution is 3.1%, stir and...

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=1:1.5 of bis(acetylacetonate) beryllium; add 1.45g activated carbon, 1.65g carnallite, 1.85g potassium feldspar, 2.05 The weight of magnesite, 2.25g magnesium spinel, 2.45g serpentinite, lithium hypochlorite and bis(acetylacetonate) beryllium (0.6g): the weight of porous mineral material (11.7g)=1:19.5, Raise the temperature to 48°C, continue to stir and react for 5.8 hours, wash and filter, and obtain 11.5 g of pore-enlarging modified carrier after drying to constant weight; in a 100ml ultrasonic reactor, put 11.5 g of pore-enlarging modified carrier, and then add 2.2 g of dimethyl Cetyl ethyl ammonium ethyl sulfate is dissolved in 26ml of deionized water in an aqueous solution, the weight conc...

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PUM

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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 activated carbon, carnallite, potassium feldspar, boronite, magnesium spinel and peridotite porous mineral material as a carrier, and after the carrier is modified by lithium hypochlorite and bis(acetylacetonate) beryllium to expand pores, The surface active agent dimethyl hexadecylethyl ammonium ethyl sulfate is added to carry out surface activation treatment under the action of ultrasonic waves, and then the composite mineralizer composed of borax and potassium sulfate formed by the ultrasonic surface activation carrier in a hydrothermal reaction kettle, acetyl Samarium acetone, tris(4,4,4‑trifluoro‑1‑(2‑thiophene)‑1,3‑butanedione) europium, tris(6,6,7,7,8,8,8‑heptafluoro ‑2,2‑Dimethyl‑3,5‑Octenedione) Dysprosium(III), Thulium(III) Trifluoromethanesulfonate Rare Earth Metal Compounds Catalytic Active Auxiliary, Cobalt Gluconate, Molybdenum L‑Aspartic Acid , catechol ethylenediamine tungsten complex, hexachloroosmium dipotassium transition metal catalytic active center component, under the action of emulsifier octadecyl dimethyl hydroxyethyl ammonium perchlorate for hydrothermal reaction, the reaction After the 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): B01J23/89B01J32/00B01J20/20B01J20/30C02F1/28C02F1/78C02F101/30
CPCB01J23/8993B01J20/04B01J20/046B01J20/06B01J20/08B01J20/10B01J20/16B01J20/20B01J35/10B01J35/1023B01J35/1042B01J35/1061B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/281C02F1/725C02F1/78C02F2101/30C02F2305/02
Inventor 朱明江燕妮苏智
Owner SICHUAN NORMAL UNIVERSITY
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