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 catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of poor toxicity resistance, low catalyst adsorption, It is easy to lose catalytic activity and other problems, and achieve the effect of strong adsorption, inhibition of melting and precipitation, and improvement of anti-toxicity and catalytic activity

Inactive Publication Date: 2017-09-15
SICHUAN NORMAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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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 wheat rice of -200 mesh to +400 mesh standard sieve Weight (3g) of lithium hypochlorite and bis(acetylacetonate)beryllium (3g) of limestone, 3.75g wollastonite, 4.75g bentonite, 5.75g polyhalite, 6.75g magnesium spinel, 7.75g peridotite: Weight (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; in a 500ml ultrasonic reactor, put the pore-enlarging modified carrier 31g, then add 3.25g octadecyltrimethylammonium chloride and be dissolved in the aqueous solution of 100ml deionized water, ...

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 wheat rice of -200 mesh to +400 mesh standard sieve Weight (0.6 g) of Lithium Hypochlorite and Bis(acetylacetonate)Beryllium, Porous Material The weight (11.7g)=1:19.5, heat up to 48°C, continue to stir and react for 5.8h, filter, dry at 105°C and obtain 11.5g of pore-enlarging modified carrier; in a 100ml ultrasonic reactor, put the pore-enlarging modified Carrier 11.5g, add the aqueous solution that 2.2g octadecyltrimethylammonium chloride is dissolved in 26ml deionized water again, the weight concentration of this aqueous solution is 7.8%, stir and mix evenly, oct...

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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. Medical stone, wollastonite, bentonite, polyhalite, magnesium spinel and peridotite are used as carriers, and after the carrier is expanded by lithium hypochlorite and bis(acetylacetonate) beryllium, the surfactant octadecyl chloride is added Trimethylammonium is activated under the action of ultrasonic waves, and then the activated carrier is mixed with the composite mineralizer borax and potassium sulfate in a hydrothermal reaction kettle, the precursor of the catalytic activity auxiliary agent scandium (III) isopropoxide, holmium oxalate decahydrate, Thulium(III) trifluoromethanesulfonate, lutetium carbonate hydrate, catalytic active center component precursor titanocene ring-substituted salicylic acid complex, L-aspartic acid molybdenum, dithiocyanatosilver(I) acid Potassium, diammine platinum dichloride, carry out hydrothermal reaction under the action of emulsifier N-hexadecyldimethyl-N'-trimethyl-propyl ammonium dichloride, dry to remove moisture, in muffle Ignition in a furnace 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): B01J23/68B01J35/10B01J37/08B01J37/10B01J37/34B01J20/20B01J20/28B01J20/30
CPCB01J23/686B01J20/06B01J20/20B01J20/28054B01J35/10B01J37/084B01J37/10B01J37/343
Inventor 朱明夏梦琦石雨晴
Owner SICHUAN NORMAL UNIVERSITY
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