Method for removing cyanogens-containing waste gas

A waste gas and removal technology, which is applied in the field of removing cyanide-containing waste gas and catalytic combustion method to remove cyanide-containing waste gas, can solve the problem of low specific surface area of ​​alumina carrier, higher requirements for removal conditions, poor dispersion of active components, etc. problems, to achieve low-temperature activity, no by-products, and improve the effect of dispersion

Inactive Publication Date: 2012-10-17
BEIJING UNIV OF CHEM TECH
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] The key technology of the catalytic combustion method is to develop high-efficiency catalysts for different processes. At present, the catalysts used to remove cyanide-containing waste gas are mainly noble metal catalysts. For example, patents CN1404900A, CN1404904A and CN1404905A disclose methods for removing hydrogen cyanide waste gas. The catalyst used is mainly single or multiple proportioning metals of platinum, palladium and rhodium, but the price of precious metals is expensive, the number of active centers is small, and the utilization rate of precious metals is low; what patent CN1416950A uses is a platinum metal catalyst loaded with alumina as a carrier , although the utilization rate of the metal is improved and the number of active centers is increased, the high price also limits the application in this field due to the lack of precious metal resources.
In order to solve the above problems, the patent CN1462652A proposes to use alumina as a carrier to support copper metal catalyst, and hydrogen cyanide, ammonia, tar, air and nitrogen as reaction raw materials, at a space velocity of 1000-50000h -1 , the hydrogen cyanide waste gas is removed at a temperature of 100-300°C. This method reduces the cost of the catalyst, but due to the low specific surface area of ​​the alumina carrier, the dispersion of the active components is poor, and the catalytic activity is affected to a certain extent. The lowest conversion rates of hydrogen, ammonia and tar are about 84%, 68% and 92% respectively, and the intr

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  • Method for removing cyanogens-containing waste gas
  • Method for removing cyanogens-containing waste gas
  • Method for removing cyanogens-containing waste gas

Examples

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Embodiment 1

[0026] Embodiment 1: take by weighing 0.0756gCu (NO 3 ) 2 ·3H 2 O (chemically pure reagent), and dissolve it in water to form an impregnating solution, then weigh 1g of SBA-15 mesoporous molecular sieve and add it to the impregnating solution, stir in a water bath at 40°C for 24 hours, and then use a rotary evaporator to remove the impregnating solution. Finally, the above-mentioned supported catalyst was placed in an air atmosphere at a rate of 2 °C / min to 550 °C and calcined for 10 hours to obtain a Cu / SBA-15 catalyst with a mass fraction of 5% copper supported. The prepared catalyst was placed in a miniature fixed-bed quartz reactor, and then the reactor was heated to 450°C, and a CH 3 CN(1vol%), O 2 (5vol%) and N 2 (As a balance gas) mixed gas, the air velocity of the mixed gas is 20000h -1, using an American Nicolet Nexus 470 infrared spectrometer with a 2.4m optical path gas analysis cell for online gas quantitative analysis, so as to obtain the conversion rate of a...

Embodiment 2

[0027] Embodiment 2: take by weighing 0.1538gCr (NO 3 ) 3 9H 2 O, and dissolve it in water to make an impregnating liquid, then weigh 1g of SBA-16 mesoporous molecular sieve and add it to the impregnating liquid, stir in a water bath at 40°C for 24 hours, then use a rotary evaporator to remove the water in the impregnating liquid, and finally The above-mentioned supported catalyst was placed in an air atmosphere at a rate of 2 °C / min to 550 °C and calcined for 10 hours to obtain a Cr / SBA-15 catalyst with a mass fraction of 2% chromium supported. Put the prepared catalyst in a miniature fixed-bed quartz reactor, then raise the temperature of the reactor to 500°C, and pass through the reactor containing CH 3 CN(1vol%), O 2 (5vol%) and N 2 (As a balance gas) mixed gas, the air velocity of the mixed gas is 20000h -1 , using an American Nicolet Nexus 470 infrared spectrometer with a 2.4m optical path gas analysis cell for online gas quantitative analysis, so as to obtain the c...

Embodiment 3

[0028] Embodiment 3: take by weighing 0.0986gCo(NO 3 ) 2 ·6H 2 O, and dissolve it in water to form an impregnating liquid, then weigh 1g of KIT-5 mesoporous molecular sieve and add it to the impregnating liquid, stir in a water bath at 40°C for 24 hours, then use a rotary evaporator to remove the water in the impregnating liquid, and finally The above-mentioned supported catalyst was placed in an air atmosphere at a rate of 2 °C / min to 550 °C and calcined for 10 hours to obtain a Co / KIT-5 catalyst with a mass fraction of 2% cobalt. Put the prepared catalyst in a miniature fixed-bed quartz reactor, then raise the temperature of the reactor to 400°C, and pass through the reactor containing CH 3 CN(1vol%), O 2 (5vol%) and N 2 (As a balance gas) mixed gas, the air velocity of the mixed gas is 20000h -1 , using an American NicoletNexus 470 infrared spectrometer with a 2.4m optical path gas analysis cell for online gas quantitative analysis, so as to obtain the conversion rate ...

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Abstract

The invention relates to a method for removing cyanogen-containing waste gas. A catalytic removal reaction is carried out on cyanogen-containing waste gas by using a transition metal supported mesoporous molecular sieve catalyst, wherein a mesoporous molecular sieve carrier is MCM-41, MCM-48, SBA-15, SBA-16, KIT-5 or KIT-6; a transition metal active component is one or more of Cu, Co, Cr, Mn, Ag or V; and the mass ratio of the carrier to the transition metal component is 1;(0.02-0.07). The method comprises the following steps: placing the molecular sieve catalyst in a fixed bed quartz reactor; introducing a mixed gas of the cyanogens-containing waste gas, oxygen and nitrogen into a reaction furnace at the space speed of 17000-24000h<-1> at normal pressure under the condition that the temperature of the reaction furnace is raised to 350-650 DEG; and removing the waste gas through catalytic combustion. The prepared catalyst is used for inspecting the selective catalytic combustion of the cyanogens-containing waste gas, has the characteristics of low combustion starting temperature and high N2 selectivity, and is suitable for efficient purification of the cyanogen-containing waste gas.

Description

technical field [0001] The invention belongs to a method for removing cyanide-containing waste gas, and specifically relates to a method for removing cyanide-containing waste gas by using a transition metal-loaded mesoporous molecular sieve as a catalyst through a catalytic combustion method, which can be used for removing hydrogen cyanide , acrylonitrile and CH 3 CN (acetonitrile) and other cyanide-containing waste gas. Background technique [0002] At present, there are three main methods for removing cyanide-containing waste gas: absorption method, adsorption method and combustion method. The catalytic combustion method in the combustion method is to react the cyanide-containing waste gas with oxygen under the action of a catalyst to convert it into nitrogen, nitrogen dioxide and water. Because the catalytic combustion method has the advantages of low ignition temperature, no secondary pollution, reusable waste heat, convenient operation and management, and low operatin...

Claims

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Application Information

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IPC IPC(8): F23G7/07B01J29/78B01J29/74B01J29/03
Inventor 陈标华曹宇张润铎
Owner BEIJING UNIV OF CHEM TECH
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