Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Catalyst for catalytic combustion of ketone and benzene-containing tail gas and preparation method thereof

A combustion catalyst and catalytic combustion technology, applied in the direction of catalyst activation/preparation, combustion method, physical/chemical process catalyst, etc., to achieve high-efficiency treatment, improved activity, and favorable effects of high dispersion

Active Publication Date: 2019-05-21
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
View PDF17 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Organic gases such as butanone-toluene are contained in the process tail gas, in order to meet the emission standards of air pollutants

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Catalyst for catalytic combustion of ketone and benzene-containing tail gas and preparation method thereof
  • Catalyst for catalytic combustion of ketone and benzene-containing tail gas and preparation method thereof
  • Catalyst for catalytic combustion of ketone and benzene-containing tail gas and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Weigh CeO prepared by homogeneous method 2 1g, to be thin 10g, aluminum nitrate nonahydrate 6.5g, γ-Al 2 o 3 1.3g, aluminum hydroxide Al(OH) 3 6.5g, 30g of water, put into a ball mill and mill for 4 hours to prepare slurry A; soak 1ml of 400-mesh honeycomb ceramic carrier in the slurry for 5min, take it out, blow out the excess slurry in the pores with compressed air, and then microwave dry , baked at 600°C for 2 hours to obtain a carrier B coated with a mixed oxide coating; dip the carrier B coated with a mixed oxide coating into a palladium nitrate solution, blow out the excess solution in the pores of the honeycomb carrier with compressed air; After drying for 5 minutes, it was calcined at 550° C. for 4 hours to obtain monolithic catalyst C. The prepared catalyst was prepared in 10vol.%H 2 -90vol.%N 2 Under atmosphere, 450 DEG C reduced for 2 hours, obtained the monolithic structure catalyst S-1 (0.1wt%Pd / 20wt.%(0.94Al 2 o 3 -0.06CeO 2 ) / cordierite honey...

Embodiment 2

[0030] Weigh 8.0g of ammonium cerium nitrate, 10g of pseudothin, 6.5g of aluminum nitrate, γ-Al 2 o 3 1.3g, aluminum hydroxide Al(OH) 3 6.5g, 30g of water, put into a ball mill jar and mill for 2 hours to prepare slurry A; soak 1ml of 400 mesh honeycomb ceramic carrier in the slurry for 5min and take it out, blow out the excess slurry in the pores with compressed air, and then microwave dry , baked at 600°C for 2 hours to obtain a carrier B coated with a mixed oxide coating; dip the carrier B coated with a mixed oxide coating into a platinum nitrate solution, blow out the excess solution in the pores of the honeycomb carrier with compressed air; After drying for 5 minutes, it was calcined at 550° C. for 4 hours to obtain monolithic catalyst C. The prepared catalyst was heated at 10vol.%H 2 -90vol.%N 2 Under the atmosphere, 450 ℃ reduced for 2 hours, and the monolithic catalyst S-2 (0.2wt%Pt / 30wt.%(0.86Al 2 o 3 -0.14CeO 2 ) / cordierite honeycomb). Catalyst S-2 continuou...

Embodiment 3

[0032] Weigh 2.5g of manganese nitrate, 5g of pseudothin, 4g of aluminum nitrate, γ-Al 2 o 3 8.2g, aluminum hydroxide Al(OH) 3 3g, 30g of dilute nitric acid, added into a ball mill and milled for 4 hours to prepare slurry A; soak 1ml of 400 mesh honeycomb ceramic carrier in the slurry for 5min and take it out, blow out the excess slurry in the pores with compressed air, and then microwave dry , baked at 600°C for 2 hours to obtain a carrier B coated with a mixed oxide coating; dip the carrier B coated with a mixed oxide coating into a palladium nitrate solution, and blow out the excess solution in the pores of the honeycomb carrier with compressed air; microwave After drying for 5 minutes, it was calcined at 550° C. for 4 hours to obtain monolithic catalyst C. The prepared catalyst was heated at 10vol.%H 2 -90vol.%N 2 Under atmosphere, 450 ℃ of reductions 2 hours, make the whole structure catalyst S-3 (0.1wt%Pd / 23wt.%(0.94Al 2 o 3 -0.06MnO 2 ) / cordierite honeycomb).

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses an integral catalyst for catalytic oxidation of ketone and benzene-containing tail gas and a preparation method thereof. The active component of the catalyst is Pd or Pt or Pd-Pt in a certain proportion. A carrier coating is a (1-a)Al2O3-aMxOy compound oxide. The active component of the catalyst is loaded by means of an equivalent-volume impregnation / excessive impregnationmethod. A transitional metal compound oxide is prepared by means of methods such as coprecipitation, sol-gel and mechanical ball-milling. The catalyst has relatively high ketone and benzene-containingtail gas combustion activity and stability and can be also used for a catalytic removal process of other VOCs gas such as ketone and benzene-containing tail gas.

Description

technical field [0001] The invention relates to a catalyst for catalytic combustion of ketone-containing benzene tail gas and a preparation method thereof, in particular to a catalyst for catalytic combustion of ketone-containing benzene tail gas and a preparation method thereof. Background technique [0002] At present, the VOCs treatment technology at home and abroad is mainly based on catalytic combustion and adsorption. In particular, catalytic combustion has the advantages of low VOCs concentration requirements and no secondary pollution. It is the most effective VOCs purification technology. At present, the combustion catalysts used in my country need to be imported, and the main suppliers are Johnson Matthey in the UK, BASF in Germany, Süd-Chemie in Germany (acquired by Clariant), Topsoe in Denmark, etc. From the perspective of active components, there are mainly two types of noble metal catalysts and composite oxide catalysts. Among them, the active components of nob...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/44B01J23/63B01J23/656B01J23/89B01J37/02B01J37/18B01D53/86B01D53/72F23G7/07
Inventor 王胜王树东林乐汪明哲
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products

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