CN203517822U - Catalytic combustion photo-catalyst waste gas treatment device - Google Patents
Catalytic combustion photo-catalyst waste gas treatment device Download PDFInfo
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- CN203517822U CN203517822U CN201320450457.3U CN201320450457U CN203517822U CN 203517822 U CN203517822 U CN 203517822U CN 201320450457 U CN201320450457 U CN 201320450457U CN 203517822 U CN203517822 U CN 203517822U
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Abstract
The utility model discloses a catalytic combustion photo-catalyst waste gas treatment device which comprises a catalytic combustion purification tower and a photo-catalyst purification tower. The catalytic combustion purification tower is composed of an adsorption system and a catalyst chamber, wherein the adsorption system is formed by a plurality of activated carbon adsorption beds. A heater and a combustion bed provided with metal catalysts are arranged in the catalyst chamber. Organic waste gas of a waste gas source enters the catalyst combustion purification tower is treated by the adsorption system and then enters the photo-catalyst purification tower to be treated, and therefore clean gas is obtained and is exhausted through a fan. When a certain activated carbon adsorption bed of the adsorption system reaches adsorption saturation to perform desorption, adsorption stops, a corresponding desorption valve is opened, the heater in the catalyst chamber is started, hot air generated in the catalyst chamber is sent to the adsorption beds, activated carbon desorbs high-concentration organic gas after being heated, the organic gas is led into the catalyst combustion bed through a desorption fan, and under the action of the metal catalysts, flameless catalyst combustion is performed.
Description
technical field:
The utility model belongs to environmental technology field, is specifically related to a kind of device that utilizes catalytic combustion+photocatalyst to carry out exhaust-gas treatment.
background technology:
At present,, there is the features such as complicated component, concentration are high, inflammable, explosive in the high-concentration organic waste gas that petrochemical plant, pharmaceutical factory etc. produce, conventional waste gas purification technique as: active carbon adsorption, combustion method, low-temperature plasma etc. are difficult to applicable.As: the problems such as active carbon adsorption is applicable to Wind Volume, low concentration gas is processed, and exists resistance coefficient large, and Energy in use is large, and the difficult support of saturation point of absorption is controlled, and adsorption capacity is little, operating cost height.By the technology of catalytic combustion, still there is peculiar smell merely in a lot of local reflections of catalytic combustion.Need consideration group technology to process it.My company studies catalytic combustion and the processing of photocatalyst technology to industrial organic exhaust gas for many years, the Patents obtaining has: ZL201120573467.7, ZL201120573467.7, ZL201120573479.X etc., on this basis, purified treatment for organic exhaust gas high concentration, Wind Volume is for further study, designs new process route.
summary of the invention:
The technical problems to be solved in the utility model is to provide a kind of purifying processing device that can process various high concentrations, Wind Volume organic exhaust gas, has that waste gas purification is effective, equipment operation energy consumption is low, the feature of convenient management.
Solve the technical scheme that its technical problem adopts as follows:
A kind of catalytic combustion photocatalyst emission-control equipment, comprise a catalytic combustion purifying column and a photocatalyst purifying column, the adsorption system that described catalytic combustion purifying column is comprised of a plurality of activated carbon adsorption beds and a catalyst chamber form, and be provided with heater and form with the burning bed that is provided with metallic catalyst in catalyst chamber;
Adsorption system is under adsorbed state, and exhaust gas source organic exhaust gas enters catalytic combustion purifying column, after adsorption system is processed, then enters photocatalyst purifying column and processes, and obtains clean gas and discharges through blower fan;
Certain activated carbon adsorption bed in adsorption system reaches and adsorbs full closing while carrying out desorb, stop absorption, open corresponding desorption valve, open the heater in catalyst chamber, the hot-air producing in catalyst chamber is sent into adsorbent bed, active carbon is subject to thermal desorption to go out the organic gas of high concentration, through desorption blower fan, introduces catalytic combustion bed, under the effect of metallic catalyst, under 200~300 degree, carries out flameless catalytic combustion.
Described catalytic combustion purifying column is provided with temperature-control adjustment device.
In described photocatalyst purifying column, be provided with photoion body device and photocatalyst purification plant.
The activated carbon adsorption bed of described adsorption system is many charcoals layer structure.
The utility model catalytic combustion photocatalyst emission-control equipment, adopts catalytic combustion to remove large molecule waste gas peculiar smell most, high concentration, the waste gas of high concentration is converted into the gas of low concentration, and macromolecular gas key mapping is interrupted and becomes micromolecular gas.Remaining low concentration, little molecule gas with foreign flavor are removed through photocatalyst purification plant.Can substantially reach the object of factory's circle free from extraneous odour.
The present invention is applicable to the high concentrations in place such as petrochemical plant, pharmaceutical factory, the organic exhaust gas of Wind Volume.
Accompanying drawing explanation
Fig. 1 is the utility model structured flowchart.
the specific embodiment:
A kind of catalytic combustion photocatalyst emission-control equipment, comprise a catalytic combustion purifying column and a photocatalyst purifying column, the adsorption system that described catalytic combustion purifying column is comprised of a plurality of activated carbon adsorption beds and a catalyst chamber form, and be provided with heater and form with the burning bed that is provided with metallic catalyst in catalyst chamber; Exhaust gas source organic exhaust gas enters catalytic combustion purifying column, after adsorption system is processed, then enters photocatalyst purifying column and processes, and obtains clean gas and discharges through blower fan.
A plurality of activated carbon adsorption beds in adsorption system share a desorption system, certain activated carbon adsorption bed in adsorption system reaches and adsorbs full closing while carrying out desorb, stop absorption, open corresponding desorption valve, open the heater in catalyst chamber, catalyst to catalytic combustion bed inside carries out preheating, produce a certain amount of hot-air simultaneously, when bed temperature reaches setting value, hot-air is sent into adsorbent bed, active carbon is subject to thermal desorption to go out the organic gas of high concentration, through desorption blower fan, introduce catalytic combustion bed, under the effect of metallic catalyst, 200~300 degree carry out flameless catalytic combustion, organic principle is converted into nontoxic, harmless CO
2and H
2o discharges a large amount of heats simultaneously, can maintain the required initiation temperature of catalytic combustion, and make waste gas burning process substantially not need additional energy consumption (electric energy), and part heat is back to the desorption and regeneration of active carbon in adsorbent bed, thus the energy consumption of greatly reducing.When burnt gas concentration is higher, reaction temperature is when higher, attemperating unit is opened automatically, supplement fresh cold air reducing temperature, guarantee catalytic combustion bed safety, efficiently operation.
The heater of catalytic combustion purifying column adopts the finned electric heating tube of far infrared, safety, efficient; Desorption-catalytic combustion system delicate structure in catalytic combustion purifying column, the compound circulation hold over system of hot blast, the thermal efficiency is high, and energy loss is few, has realized the thermal balance of desorption heat absorption with burning heat release, and combustion process does not consume additional electric energy, and energy consumption is low especially.
Catalyst chamber initiation temperature is low, thorough, the safe flameless combustion of burning, and product is nontoxic, harmless; Catalyst long service life, discarded object recoverable.
The activated carbon adsorption bed of adsorption system is many charcoals layer structure, and charcoal layer is evenly distributed, stablizes, air-flow pressure drop is little, the excellent properties that absorption property is good.
In photocatalyst purifying column, be provided with photoion body device and photocatalyst purification plant, photoion body device produces high-energy electron, directly decomposes as pernicious gases such as benzene,toluene,xylene, ketone, aldehydes, NMHCs, makes its degraded generation CO rapidly
2, H
2o, all kinds of pernicious gases that photocatalyst purification plant can be degraded and is not yet degraded, thus reach the comparatively satisfied comprehensive degradation effect of waste exhaust gases, good to the removal effect of organic exhaust gas Wind Volume, low concentration and peculiar smell.
The utility model processing air quantity is large, and treatment effect is good, and the cost of investment, the floor space that greatly reduce facility are little, and facility operation is stable, failure rate is low, and maintaining is easy, and operating cost is low, has avoided the wasting of resources, secondary pollution and safety hazard.
Claims (4)
1. a catalytic combustion photocatalyst emission-control equipment, it is characterized in that: comprise a catalytic combustion purifying column and a photocatalyst purifying column, the adsorption system that described catalytic combustion purifying column is comprised of a plurality of activated carbon adsorption beds and a catalyst chamber form, and be provided with heater and form with the burning bed that is provided with metallic catalyst in catalyst chamber;
Adsorption system is under adsorbed state, and exhaust gas source organic exhaust gas enters catalytic combustion purifying column, after adsorption system is processed, then enters photocatalyst purifying column and processes, and obtains clean gas and discharges through blower fan;
Certain activated carbon adsorption bed in adsorption system reaches and adsorbs full closing while carrying out desorb, stop absorption, open corresponding desorption valve, open the heater in catalyst chamber, the hot-air producing in catalyst chamber is sent into adsorbent bed, active carbon is subject to thermal desorption to go out the organic gas of high concentration, through desorption blower fan, introduces catalytic combustion bed, under the effect of metallic catalyst, under 200~300 degree, carries out flameless catalytic combustion.
2. a kind of catalytic combustion photocatalyst emission-control equipment according to claim 1, is characterized in that: described catalytic combustion purifying column is provided with temperature-control adjustment device.
3. a kind of catalytic combustion photocatalyst emission-control equipment according to claim 1, is characterized in that: in described photocatalyst purifying column, be provided with photoion body device and photocatalyst purification plant.
4. a kind of catalytic combustion photocatalyst emission-control equipment according to claim 1, is characterized in that: the activated carbon adsorption bed of described adsorption system is many charcoals layer structure.
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CN201320450457.3U CN203517822U (en) | 2013-07-26 | 2013-07-26 | Catalytic combustion photo-catalyst waste gas treatment device |
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CN201320450457.3U CN203517822U (en) | 2013-07-26 | 2013-07-26 | Catalytic combustion photo-catalyst waste gas treatment device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103920362A (en) * | 2014-04-22 | 2014-07-16 | 常州友达环保科技有限公司 | Exhaust gas treatment device and method by virtue of online desorption and degradation |
CN105605593A (en) * | 2015-12-05 | 2016-05-25 | 重庆科蓝环保实业有限公司 | Adsorption concentration-preheating type catalytic combustion system for purifying automobiles and coating exhaust gas in related fields and purifying method thereof |
CN106178935A (en) * | 2016-07-12 | 2016-12-07 | 广州同胜环保科技有限公司 | Waste gas cleaning system |
CN106731773A (en) * | 2016-12-30 | 2017-05-31 | 安徽德玉环境工程装备有限公司 | A kind of paint spray booth waste gas treatment equipment |
-
2013
- 2013-07-26 CN CN201320450457.3U patent/CN203517822U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103920362A (en) * | 2014-04-22 | 2014-07-16 | 常州友达环保科技有限公司 | Exhaust gas treatment device and method by virtue of online desorption and degradation |
CN105605593A (en) * | 2015-12-05 | 2016-05-25 | 重庆科蓝环保实业有限公司 | Adsorption concentration-preheating type catalytic combustion system for purifying automobiles and coating exhaust gas in related fields and purifying method thereof |
CN105605593B (en) * | 2015-12-05 | 2019-03-05 | 重庆科蓝环保实业有限公司 | A kind of pre-heated catalytic combustion system of Adsorption Concentration-and its purification method purifying automobile and related fields coating waste gas |
CN106178935A (en) * | 2016-07-12 | 2016-12-07 | 广州同胜环保科技有限公司 | Waste gas cleaning system |
CN106178935B (en) * | 2016-07-12 | 2019-01-25 | 广州同胜环保科技有限公司 | Waste gas cleaning system |
CN106731773A (en) * | 2016-12-30 | 2017-05-31 | 安徽德玉环境工程装备有限公司 | A kind of paint spray booth waste gas treatment equipment |
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CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140402 Termination date: 20190726 |