Preparation method of ozone heterogeneous oxidized solid catalyst

A heterogeneous oxidation and solid catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of poor toxicity resistance, low catalyst adsorption, easy loss of catalytic activity, etc. Achieve strong adsorption, inhibit smelting out, improve anti-toxicity and catalytic activity

Inactive Publication Date: 2017-08-08
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

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Effect test

Embodiment 1

[0007] Example 1: 1.35g lithium hypochlorite, 1.65g bis(acetylacetonate) beryllium, 140ml deionized water, were added to a sealable reactor with a volume of 500ml, stirred and mixed, and the weight concentration of the aqueous solution was 2.1%, the time Lithium chlorate: bis(acetylacetonate) beryllium weight ratio = 1:1.2; add deionized water to wash to neutrality, dry at 103 ° C to remove moisture, sieve -200 mesh ~ +400 mesh standard sieve 2.75g wheat rice Stone, 3.75g wollastonite, 4.75g potassium feldspar, 5.75g borosite, 6.75g illite, 7.75g sodium borolite, lithium hypochlorite and bis(acetylacetonate) beryllium weight (3g): Porous The weight of the material (31.5g) = 1:10.5, the temperature was raised to 36°C, the reaction was continued for 3.2h, filtered, and dried at 103°C to obtain 31g of modified pore-enlarging carrier; 31 g of a sexual carrier, and then add an aqueous solution of 3.25 g of octadecyl trimethyl ammonium chloride dissolved in 100 ml of deionized water...

Embodiment 2

[0008] Example 2: 0.24g lithium hypochlorite, 0.36g bis(acetylacetonate) beryllium, 10ml deionized water, were added to a sealable reactor with a volume of 100ml, stirred and mixed uniformly, the weight concentration of this aqueous solution was 5.7%, the time Lithium chlorate: bis(acetylacetonate) beryllium weight ratio = 1:1.5; add deionized water to wash to neutrality, dry at 103 ° C to remove moisture, sieve -200 mesh ~ +400 mesh standard sieve 1.45g wheat rice Stone, 1.65g wollastonite, 1.85g potassium feldspar, 2.05g borosite, 2.25g illite, 2.45g sodium borolite, lithium hypochlorite and bis(acetylacetonate) beryllium weight (0.6g): The weight of the porous material (11.7g) = 1:19.5, the temperature was raised to 48°C, the reaction was continued for 5.8h, filtered, and dried at 105°C to obtain 11.5g of modified carrier for pore expansion; 11.5 g of the pore modified carrier, and then add 2.2 g of an aqueous solution of octadecyl trimethyl ammonium chloride dissolved in 2...

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Abstract

The invention relates to a preparation method of an ozone heterogeneous oxidized solid catalyst, and belongs to the technical field of environmental protection and chemical catalyst. The preparation method comprises the following steps: taking maifanite, wollastonite, potassium feldspar, szaibelyite, illite and raphite as carriers, performing lithium hypochlorite and bis(acetylacetonato) beryllium reaming, adding octadecyl trimethyl ammonium chloride to perform activating treatment under an ultrasonic effect; and then enabling the active carriers to perform hydrothermal reaction with the compound mineralizing agent borax and potassium sulfate, catalytic active promoter precursors scandium isopropoxide (III), thulium trifluoromethane sulfonate (III), tri(trifluoromethane sulfimide)ytterbium, lutetium carbonate hydrate, catalytic active center precursors titanocene ring substituted salicylic complex, L-aspartic acid molybdenum, gold potassium tetrachloride and iridium tetrachloride dihydrate under the effect of the emulsifier N-decyl dimethyl-N -trimethyl-2-hydroxypropyl ammonium dichloride, drying to remove the moisture, firing in a muffle furnace to obtain the ozone heterogeneous oxidized solid catalyst.

Description

technical field [0001] 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. Background technique [0002] Ozone oxidation technology utilizes the characteristics of strong ozone oxidation ability, 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. Low ozone utilization leads to high operating costs for water treatment. At the same time, organic pollutants are removed. The low rate and easy to cause secondary pollution of water body limit its application; the ozone heterogeneous catalytic oxidation technology has the advantages of easy separation, recovery and reus...

Claims

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Application Information

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IPC IPC(8): B01J23/68B01J20/20B01J20/30C02F1/78
CPCB01J23/686B01J20/04B01J20/06B01J20/10B01J20/12B01J20/16B01J20/20B01J35/10B01J37/084B01J37/10B01J2220/42B01J2220/4806B01J2220/4812C02F1/725C02F1/78C02F2305/02
Inventor 朱明夏梦琦石雨晴
Owner SICHUAN NORMAL UNIVERSITY
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