A kind of molecular sieve supported type mno2-zno ozone catalyst and preparation method thereof

A molecular sieve, supported technology, applied in the field of environmental purification, can solve the problems of high economic cost, the large-scale promotion and application of ozone catalytic oxidation technology, and difficult problems, so as to improve removal efficiency, save material costs and operating costs. , the effect of increasing the mass transfer rate

Active Publication Date: 2019-01-18
SHANGHAI NAT ENG RES CENT FORNANOTECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Pd, Ru, Pt and other precious metal complexes are used as the catalytic active component of ozone. Although the catalytic activity is good, there are disadvantages such as high economic cost.
Now ozone catalytic oxidation, as an efficient, fast, and non-secondary pollution water treatment technology, has been applied in engineering applications in drinking water, printing and dyeing wastewater, tannery wastewater and other related fields, and has also received more and more attention in the research field. , but the ozone catalytic oxidation technology has not yet been widely promoted and applied in the advanced treatment of industrial wastewater. The main reason is that the preparation of an efficient ozone catalyst is the core and difficult problem of the ozone catalytic oxidation technology.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] The supported ZnO was prepared by in-situ method, and 13X was immersed in Zn(NO 3 ) 2 ·6H 2 O, slowly add hexamethylenetetramine solution dropwise, mix evenly, transfer to a polytetrafluoroethylene reactor, react at 150°C for 12 hours, then wash, filter and dry the product to obtain molecular sieve-supported ZnO nanorods ;

[0024] With molecular sieves loaded with ZnO nanorods as the carrier, KMnO 4 As a source of manganese, it is prepared by in-situ hydrothermal synthesis, that is, according to MnO 2 Mix it with the carrier at a mass ratio of 0.05:1, react at 140°C for 12 hours, wash and dry, and then place it in a muffle furnace at 350°C for 2 hours to obtain molecular sieve-loaded MnO 2 -ZnO ozone catalyst particles, the prepared supported ozone catalyst has a degradation rate of 70.6% for COD of RhB solution.

Embodiment 2

[0026] The supported ZnO was prepared by in-situ method, and alumina was immersed in Zn(NO at a mass ratio of 0.5:1. 3 ) 2 ·6H 2 O, slowly add hexamethylenetetramine solution dropwise, mix evenly, transfer to a polytetrafluoroethylene reactor, react at 150°C for 12 hours, then wash, filter and dry the product to obtain molecular sieve-supported ZnO nanorods ;

[0027] With molecular sieves loaded with ZnO nanorods as the carrier, KMnO 4 As a source of manganese, it is prepared by in-situ hydrothermal synthesis, that is, according to MnO 2 Mix it with the carrier at a mass ratio of 0.1:1, react at 140°C for 12 hours, wash and dry, and then place it in a muffle furnace at 500°C for 2 hours to obtain molecular sieve-loaded MnO 2 -ZnO ozone catalyst particles, the prepared supported ozone catalyst has a COD degradation rate of 81.2% for RhB solution.

Embodiment 3

[0029] The supported ZnO was prepared by in-situ method, and alumina was immersed in Zn(NO at a mass ratio of 2:1. 3 ) 2 ·6H 2 O, slowly add hexamethylenetetramine solution dropwise, mix evenly, transfer to a polytetrafluoroethylene reactor, react at 150°C for 12 hours, then wash, filter and dry the product to obtain molecular sieve-supported ZnO nanorods ;

[0030] With molecular sieves loaded with ZnO nanorods as the carrier, KMnO 4 As a source of manganese, it is prepared by in-situ hydrothermal synthesis, that is, according to MnO 2 Mix it with the carrier at a mass ratio of 0.05:1, react at 140°C for 12 hours, wash and dry, and then calcinate in a muffle furnace at 500°C for 2 hours to obtain molecular sieve-loaded MnO 2 -ZnO ozone catalyst particles, the prepared supported ozone catalyst has a degradation rate of 65.5% for COD of RhB solution.

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Abstract

The invention relates to a molecular sieve loaded MnO2-ZnO ozone catalyst and a preparation method thereof. The preparation method comprises the following steps: preparing loaded MnO2 by virtue of an in-situ method, soaking a molecular sieve into Zn(NO3)2.6H2O in a certain mass ratio, slowly and dropwise adding a hexamine solution, uniformly mixing to obtain a solution, then transferring the solution into a polytetrafluoroethylene reaction kettle, reacting at 150 DEG C for 12 hours to obtain a product, and washing, filtering and drying the product, so as to obtain a molecular sieve loaded MnO2 nanorod; and carrying out in-situ hydro-thermal synthesis by taking the MnO2 nanorod loaded molecular sieve as a carrier and KMnO4 as a manganese source, namely mixing the carrier with KMnO4 in a certain proportion to obtain a mixture, reacting at 140 DEG C for 12 hours, washing, drying, and burning the mixture in a muffle furnace for 2 hours, so as to obtain molecular sieve loaded MnO2-ZnO ozone catalyst particles. According to the molecular sieve loaded MnO2-ZnO ozone catalyst, the utilization ratio of ozone is effectively increased, and the removal efficiency of COD is effectively improved.

Description

technical field [0001] The invention relates to a water pollution control material in the field of environmental purification and a preparation method thereof, in particular to a molecular sieve-loaded MnO 2 - ZnO ozone catalyst and preparation method thereof. Background technique [0002] The increasingly serious water pollution not only reduces the use function of water bodies, further exacerbates the contradiction of water shortage, but also seriously threatens the drinking water safety and health of urban residents. The advanced treatment methods commonly used at home and abroad include: flocculation precipitation method, ozone oxidation, reverse osmosis method, activated carbon method, demulsification, membrane separation method, biological denitrification, dephosphorization method, etc. These technologies have played a certain role in the removal of refractory organic matter, but there are also certain deficiencies, such as the difficulty in the treatment of reverse o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/34B01J29/03B01J29/16C02F1/78
CPCB01J23/34B01J29/0341B01J29/163C02F1/725C02F1/78
Inventor 何丹农童琴严良高小迪代卫国金彩虹
Owner SHANGHAI NAT ENG RES CENT FORNANOTECH
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