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Catalyst for VOCs catalytic combustion and its preparation method

A technology of catalytic combustion, catalyst

Inactive Publication Date: 2018-06-12
SHANGHAI SHENGJIAN ENVIRONMENTAL SYST TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The loaded active components are dispersed on the surface of the carrier, mostly precious metals such as Pt, Pd, Ru, etc., and the treatment effect is ideal, but there are disadvantages such as easy poisoning and poor high temperature stability. Therefore, the repeated use activity is poor and the price is expensive
When the active component is a transition metal oxide, there are disadvantages such as low catalytic activity and poor catalytic effect of the catalyst.

Method used

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  • Catalyst for VOCs catalytic combustion and its preparation method
  • Catalyst for VOCs catalytic combustion and its preparation method
  • Catalyst for VOCs catalytic combustion and its preparation method

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preparation example Construction

[0039] The present invention also provides a method for preparing a catalyst for catalytic combustion of VOCs, comprising:

[0040] A) Mixing the aqueous solution of lanthanum-containing compound with CeO 2 Mixed, La-CeO was obtained by the first roasting 2 catalyst;

[0041] B) the La-CeO 2 The catalyst is mixed with an aqueous solution of a cobalt-containing compound, and after a second calcination, Co / La-CeO 2 catalyst;

[0042] C) the Co / La-CeO 2 The catalyst is mixed with water, polyvinyl alcohol and colloidal alumina to obtain a slurry;

[0043] D) mixing the honeycomb ceramic substrate with the slurry for coating, and then firing the coated honeycomb ceramic substrate for the third time to obtain a catalyst for catalytic combustion of VOCs.

[0044] The present invention has no special limitation on the preparation method of the aqueous solution of the lanthanum-containing compound, and the preparation method of the aqueous solution well known to those skilled in ...

Embodiment 1

[0074] (1) 0.1655g La(NO 3 ) 3 ·6H 2 O was dissolved in 100ml of distilled water and stirred until completely dissolved to form an aqueous solution of the lanthanum-containing compound.

[0075] (2) Take 1g CeO 2 The powder is mixed with the aqueous solution obtained in (1), stirred by a magnetic stirrer at room temperature for 1 h, impregnated for 8 h, evaporated at 50 °C, dried at 100 °C for 2 h, calcined at 350 °C for 4 h, and ground to obtain La-CeO 2 powder. The La-CeO 2 In the catalyst, the mass fraction of La is 5%.

[0076] (3) 0.5493g Co(CH 3 COO) 2 4H 2 O was dissolved in 100ml of distilled water and stirred until completely dissolved to form an aqueous solution containing cobalt compounds.

[0077] (4) Take 1gLa-CeO 2 The powder is mixed with the aqueous solution obtained in (3), stirred by a magnetic stirrer at room temperature for 1 h, impregnated for 8 h, evaporated at 50 °C, dried at 100 °C for 2 h, calcined at 350 °C for 3 h, and ground to obtain Co / L...

Embodiment 2

[0083] (1) 0.1483g La(CH 3 COO) 3 4H 2 O was dissolved in 100ml of distilled water and stirred until completely dissolved to form an aqueous solution of the lanthanum-containing compound.

[0084] (2) Take 1g CeO 2 The powder is mixed with the aqueous solution obtained in (1), stirred by a magnetic stirrer at room temperature for 2 hours, impregnated for 10 hours, evaporated at 60°C, dried at 110°C for 4 hours, calcined at 450°C for 5 hours, and ground to obtain La-CeO 2 powder. The La-CeO 2 In the catalyst, the mass fraction of La is 5%.

[0085] (3) 0.8944g Co(CH 3 COO) 2 4H 2 O was dissolved in 100ml of distilled water and stirred until completely dissolved to form an aqueous solution containing cobalt compounds.

[0086] (4) Take 1gLa-CeO 2 The powder is mixed with the aqueous solution obtained in (3), stirred by a magnetic stirrer at room temperature for 2 hours, impregnated for 10 hours, evaporated at 60°C, dried at 110°C for 4 hours, calcined at 450°C for 4 ho...

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Abstract

The catalyst provided by the invention is an integrated catalyst; the catalyst takes a honeycomb ceramic matrix as a framework, an aluminum oxide as a coating, and Co, La and Ce as active components;the components are matched with specific content, the catalyst has big specific area and many activity sites while good structure and coating stability. The catalyst is applied to the catalytic combustion reaction of methylbenzene and ethyl acetate, and has high catalytic activity. Meanwhile, the catalyst has stable repeat using activity, and overcomes the shortcomings of poor high-temperature stability and bad repeat using activity of the traditional noble metal catalyst. The experiment indicates that through sonic oscillation, the drop rate of coating is 2% below. When the catalytic combustion temperature is 350 DEG C, the methylbenzene conversion rate is 93.67-95.97%, the ethyl acetate conversion rate is 92.65-95.64%. Through evaluation for continuous 1000 hours, the reaction conversionrate keeps stable.

Description

technical field [0001] The invention relates to the technical field of chemical catalysts and their preparation, in particular to a catalyst for catalytic combustion of VOCs and a preparation method thereof. Background technique [0002] Most of VOCs are toxic and can cause acute and chronic poisoning, even carcinogenesis and mutation. At the same time, VOCs as PM 2.5 precursors, will cause direct or indirect harm to human health. Therefore, the emission of VOCs poses a great threat to human health and the ecological environment. When the VOCs of halogenated hydrocarbons diffuse into the ozone layer, they will chemically react with ozone, resulting in a decrease in ozone concentration, forming an ozone hole, and causing a series of ecological disasters such as the greenhouse effect. Some VOCs of aldehydes and ketones react photochemically with nitrogen oxides in the air under light conditions to form photochemical smog, causing more serious secondary pollution. [0003] A...

Claims

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Application Information

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IPC IPC(8): B01J23/83
CPCB01J23/83B01J37/088
Inventor 张伟明柳晓清袁静汪哲
Owner SHANGHAI SHENGJIAN ENVIRONMENTAL SYST TECH
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