Preparation method of ozone heterogeneous oxidation solid catalyst

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 attapulgite, diopside, montmorillonite, potassium halite, fly ash and coal gangue porous materials as carriers, and the carrier is modified by lithium hypochlorite and bis(acetylacetonate) beryllium. , adding the surfactant dioctadecylmethyl-2-hydroxyethylammonium chloride to carry out surface activation treatment under the action of ultrasonic waves, and then the ultrasonic surface activation carrier is mixed with composite mineralizer borax and potassium sulfate in a hydrothermal reaction kettle , catalyst precursors tris(3‑trifluoroacetyl‑D‑camphor) praseodymium (III), 1,1,1‑trifluoroacetylacetonate neodymium, tris (6,6,7,7,8,8 ,8‑heptafluoro‑2,2‑dimethyl‑3,5‑octenedione) dysprosium(III), tris[N,N‑bis(trimethylsilyl)amine]erbium rare earth organometallic compound, catalytic Active center component precursor common transition metal organic compound ferrous fumarate, nickel citrate, copper glutamate and noble metal compound terpyridyl ruthenium chloride hexahydrate, in emulsifier dimethylaminoethanol laurate chloroacetic acid The hydrothermal reaction is carried out under the action of ammonium, and the reaction product is dried to remove moisture, and burned at a certain temperature in a muffle 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, belonging to the technical field of environmental protection and chemical catalysts. Background technique [0002] Ozone oxidation technology takes advantage of the strong ability of ozone to oxidize and decompose many organic pollutants, and is widely used in wastewater treatment. Ozone catalytic oxidation technology is divided into homogeneous catalytic oxidation of ozone and heterogeneous catalytic oxidation of ozone. In homogeneous catalytic oxidation of ozone, the catalyst is difficult to separate and recycle and reuse, and the low utilization rate of ozone leads to higher water treatment operating costs and removal of organic pollutants. The low rate and easy to cause secondary pollution of water make its application limited; the ozone heterogeneous catalytic oxidation technology has catalysts that are easy to separate and recover and can be reused, hi...

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 for 3h-6h, filter, and dry the reaction product at 102°C-106°C to obtain a modified carrier for pore expansion; pore expansion Put the modified carrier into the ultrasonic reactor, add the aqueous solution prepared by C component and deionized water, the weight concentration of C component is 3%~8%, stir and mix evenly, control the ultrasonic power density to 0.3~0.8W / m 3 , frequency 20kHz ~ 30kHz, 40 ℃ ~ 55 ℃, ultrasonic vibration 2h ~ 5h, the ultrasonic surface activation carrier mixture is obtained; the ultrasonic surface activation carrier mixture is transferred to the hydrothermal reaction kettle, and then add D component and deionized water to prepare The aqueous solution, the weight concentration of D component is 40% ~ 55%, by weight, the weight ratio of D component deionized aqueous solution: ultrasonic surface activation carrier mixture = 1: (1.5 ~ 2), control temperature 120 ℃ ~ 180°C, the hydrothermal reaction time is 8h~16h, and then dried to obtain fine particles; the fine particles are burned in a muffle furnace at 600°C~950°C for 3h~8h to obtain a solid catalyst for ozone heterogeneous oxidation