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
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
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.
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com