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Monolithic catalyst for catalyzing ozone to degrade VOCs as well as preparation and application of monolithic catalyst

A monolithic catalyst and ozone degradation technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems such as difficult balance between stability and mass transfer efficiency

Active Publication Date: 2021-05-25
NANJING UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the technical problem that the stability and mass transfer efficiency of the active components of the existing catalytic ozone oxidation VOCs catalysts are difficult to balance, a monolithic catalyst for catalytic ozone degradation VOCs is provided. The active component catalyzes the mass transfer efficiency and the mechanical stability of the coating at the same time;

Method used

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  • Monolithic catalyst for catalyzing ozone to degrade VOCs as well as preparation and application of monolithic catalyst
  • Monolithic catalyst for catalyzing ozone to degrade VOCs as well as preparation and application of monolithic catalyst

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preparation example Construction

[0034] A kind of preparation method of catalytic ozone degrading VOCs monolithic catalyst of the present invention, preparation step is

[0035] (1) Substrate pretreatment

[0036] Inorganic ceramics are used as the substrate, and the substrate is pretreated by alkali washing and / or acid etching and / or heat treatment; specifically, this step is to heat the Y-type molecular sieve to 200-300°C in the air atmosphere, and pass in water vapor And raise the temperature to 650-850°C, keep it for 4-6 hours, then lower the temperature to 200-400°C and stop the introduction of water vapor, lower the temperature to below 100°C in the air atmosphere and take out the sample; then prepare 0.5-2mol / L of nitric acid solution, put the above-mentioned Y-type molecular sieve and nitric acid solution treated with water vapor into a three-necked flask at a solid-to-liquid ratio of 1: (8-12), and stir and react in a reflux device at 60-100°C 4 to 6 hours, after the reaction, the sample was washed...

Embodiment 1

[0042] Carrier pretreatment: choose a honeycomb cordierite ceramic carrier with a pore density of 600cpsi and a wall thickness of 3mil, and activate it in an air atmosphere at 350°C for 4 hours to remove impurities after washing. After roasting, soak in 20% sodium hydroxide solution for 2 minutes, blow off the residual liquid and wash with deionized water until neutral, then soak in 10% nitric acid solution, control the temperature of the oil bath to make the acid solution boil, every 1 hour Change the acid, etch for 3 hours, wash with deionized water until neutral.

[0043] Powder catalyst preparation: heat commercial Y-type molecular sieves to 200°C in air atmosphere; blow high-purity nitrogen into water and heat to 100°C, introduce into the quartz tube after the air flow is stable, and raise the temperature to 850°C for 4 hours, then Lower the temperature to 400°C and stop water injection, lower the temperature to below 100°C in the air atmosphere and take out the sample; p...

Embodiment 2

[0047] Carrier pretreatment: select a honeycomb cordierite ceramic carrier with a pore density of 400cpsi and a wall thickness of 4mil, and activate it in an air atmosphere at 350°C for 4 hours to remove impurities after washing. After roasting, soak in 20% sodium hydroxide solution for 2 minutes, blow off the residual liquid and wash with deionized water until neutral, then soak in 26% nitric acid solution, control the temperature of the oil bath to make the acid solution boil, every 1 hour Change the acid, etch for 2 hours, wash with deionized water until neutral.

[0048] Powder catalyst preparation: heat commercial Y-type molecular sieves to 300°C in air atmosphere; blow high-purity nitrogen into water and heat to 100°C, introduce into the quartz tube after the air flow is stable, and raise the temperature to 750°C for 5 hours, then Lower the temperature to 400°C and stop water injection, lower the temperature to below 100°C in the air atmosphere and take out the sample; p...

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Abstract

The invention relates to a monolithic catalyst for catalyzing ozone to degrade VOCs, and belongs to the technical field of catalyzing ozone to oxidize VOCs. The monolithic catalyst comprises inorganic ceramic and a molecular sieve, the molecular sieve is loaded on the inorganic ceramic, and the specific surface area of the inorganic ceramic is 30-250 m<2> / g; the surface of the inorganic ceramic comprises micropores, and the aperture of the micropores is 5-10 microns; the specific surface area of the molecular sieve is 300-600 m<2> / g, and the silica-alumina ratio of the molecular sieve is not less than 5; the molecular sieve is loaded with a non-noble metal oxide, and the mass of the non-noble metal oxide accounts for 0.5-10% of the mass of the molecular sieve; the surface of the inorganic ceramic is coated with silica sol, and an organic pore-forming agent is used in the preparation process of the catalyst; through the treatment that the surface of the inorganic ceramic is coated with the silica sol and the organic pore-forming agent, the mass transfer efficiency and the mechanical stability of the coating are improved while the catalytic action of the active components is fully exerted.

Description

technical field [0001] The invention belongs to the technical field of catalytic ozone oxidation of VOCs, and more specifically relates to a monolithic catalyst for catalytic ozone degradation of VOCs and its preparation and application. Background technique [0002] Catalyst, as the core of the catalytic process, is one of the key concerns in the field of catalysis research. Although noble metal catalysts represented by Pt, Pb, Au, and Ag have the advantages of low light-off temperature, high catalytic activity, and less likely to produce secondary pollutants, their cost is too high, their thermal stability is poor, and they are easy to be lost during use. Catalyst poisoning, which greatly limits the industrial application of noble metal catalysts. At present, oxides of non-noble metals are often used instead of noble metals to reduce catalyst preparation costs and improve application stability. Non-noble metal oxide catalysts mainly include transition metal oxides, perov...

Claims

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Application Information

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IPC IPC(8): B01J29/08B01J29/16B01J35/10B01D53/76B01D53/86B01D53/44
CPCB01J29/084B01J29/166B01D53/8687B01D53/76B01D2251/104B01J35/60
Inventor 龙超许博文邵琦董浩张健
Owner NANJING UNIV
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