Preparation method of ozone heterogeneous oxidation solid catalyst

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

Inactive Publication Date: 2017-08-11
SICHUAN NORMAL UNIVERSITY
View PDF0 Cites 0 Cited by
  • 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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

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 attapulgite of -200 mesh to +400 mesh standard sieve Weight of soil, 3.75g diopside, 4.75g talc, 5.75g sodaite, 6.75g fly ash, 7.75g coal gangue, lithium hypochlorite and bis(acetylacetonate)beryllium (3g): weight of porous material (31.5g)=1:10.5, heat up to 36°C, continue to stir for 3.2h, filter, dry at 103°C and obtain 31g of pore-enlarging modified carrier; put 31g of pore-enlarging modified carrier into a 500ml ultrasonic reactor , then add 3.25g of trioctylmethylammonium chloride and dissolve in 100ml of deionized water. The weight concentration of the aqueous ...

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 1.45g attapulgite of -200 mesh to +400 mesh standard sieve Weight of soil, 1.65g diopside, 1.85g talc, 2.05g sodastone, 2.25g fly ash, 2.45g coal gangue, lithium hypochlorite and bis(acetylacetonate) beryllium (0.6g): Porous material Weight (11.7g) = 1:19.5, heat up to 48°C, continue to stir for 5.8h, filter, dry at 105°C and obtain 11.5g of pore-enlarging modified carrier; in a 100ml ultrasonic reactor, put pore-enlarging modified Carrier 11.5g, then add 2.2g of trioctylmethylammonium chloride dissolved in 26ml of deionized water aqueous solution, the weight concentration o...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a preparation method of an ozone heterogeneous oxidation solid catalyst, belonging to the technical field of environmental protection and chemical catalysts. In the preparation method, attapulgite, diopside, talc, soda ash, fly ash and coal gangue porous materials are used as carriers; The surface active agent trioctyl methyl ammonium chloride is subjected to surface activation treatment under the action of ultrasonic waves, and then the ultrasonic surface activation carrier is combined with the composite mineralizer borax and potassium sulfate in the hydrothermal reactor, and the catalytic active promoter precursor three (3 ‑Trifluoroacetyl‑D‑camphor) praseodymium (III), tricyclopentadienyl promethium, hydrated terbium triacetate, tris(trifluoromethanesulfonimide) ytterbium rare earth metal organic compound, catalytic active center component precursor Ordinary transition metal organic compounds ferrous fumarate, nickel citrate and noble metal compounds silver(I) dithiocyanate, potassium hexachloroosmium, under the action of emulsifier trimethylaminoethanol laurate ammonium chloride The hydrothermal reaction is carried out, and after the reaction product is dried to remove moisture, it is fired in a muffle furnace at a certain temperature to obtain an 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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): B01J23/89B01J32/00B01J20/20B01J20/30C02F1/28C02F1/78C02F101/30
CPCB01J23/894B01J20/041B01J20/043B01J20/06B01J20/08B01J20/10B01J20/103B01J20/12B01J20/20B01J35/10B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/281C02F1/725C02F1/78C02F2101/30C02F2305/02
Inventor 朱明刘阳宋佳柠
Owner SICHUAN NORMAL UNIVERSITY
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products