CN105771640A - Treatment equipment for organic waste gases - Google Patents
Treatment equipment for organic waste gases Download PDFInfo
- Publication number
- CN105771640A CN105771640A CN201610317767.6A CN201610317767A CN105771640A CN 105771640 A CN105771640 A CN 105771640A CN 201610317767 A CN201610317767 A CN 201610317767A CN 105771640 A CN105771640 A CN 105771640A
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- chamber
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- locellus
- valve
- waste gas
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8678—Removing components of undefined structure
- B01D53/8687—Organic components
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0258—Other waste gases from painting equipments or paint drying installations
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40086—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by using a purge gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/401—Further details for adsorption processes and devices using a single bed
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/14—Gaseous waste or fumes
Abstract
The invention discloses treatment equipment for organic waste gases and relates to the field of waste gas purification. The treatment equipment comprises an absorption concentrating system and a desorption catalytic combustion system, wherein the absorption concentrating system of the waste gases sequentially comprises a waste gas secondary filter, a waste gas filtering chamber and an adsorption fan which are connected; a first chamber, a second chamber, a third chamber and a fourth chamber are arranged in the waste gas filtering chamber; an adsorption inlet, an adsorption outlet, a concentrating inlet and a concentrating outlet are formed in the waste gas filtering chamber; the desorption catalytic combustion system comprises a regeneration blower, an electric heater, a catalytic combustion chamber, a gas mixing chamber and a primary efficiency air filter; a waste gas outlet is formed outside a motor of the adsorption fan. According to the device, by controlling opening and time of multiple chambers, an adsorbing combustion stage and a desorbing combustion stage can continuously work for operating.
Description
Technical field
The present invention relates to waste gas purification field, be specifically related to a kind of VOCs treatment equipment.
Background technology
Producing toxic and harmful in the processes such as rubber production, coating manufacture, typography, spraying coating process, the workman in workshop not only can be caused very big actual bodily harm by these pollutant, also can air be polluted during discharge.Along with the raising of the enhancing of people's environmental consciousness, country's industry and atmosphere pollutants emission standards, therefore waste gas is carried out purified treatment qualified discharge and had mandatory.At present, the mainstream technology treatment effeciency burning cost relatively low, direct of domestic process large-wind-volume low-concentration organic exhaust gas is higher, and it is big that equipment takes up an area volume.Thus, minimizing up-front investment, reduction floor space, raising treatment effect are particularly important.
Summary of the invention
For the deficiencies in the prior art, it is an object of the invention to provide a kind of poisonous and harmful substances processing the process generations such as rubber production, coating manufacture, typography, spraying coating process, including Adsorption Concentration system and desorption catalyzing combustion system.Controlled by the folding of multiple chambers and time so that absorption and desorption combustion phases can run in continuous operation.The waste gas of low concentration Wind Volume is by concentrating, under the effect of catalyst, non-flaming combustion is carried out after desorption, the temperature that own combustion produces simultaneously can meet ignition temperature, it is not necessary to external heat again, fully generates the VOCs treatment equipment of carbon dioxide and water after burning.
nullPresent invention solves the technical problem that and can realize by the following technical solutions: a kind of VOCs treatment equipment，Including Adsorption Concentration system and desorption catalyzing combustion system，Wherein said waste gas Adsorption Concentration system includes the waste gas secondary filter being connected successively、Waste gas filter chamber and absorption blower fan，The first chamber it is provided with in waste gas filter chamber、Second chamber、3rd chamber and the 4th chamber，Waste gas filter chamber is provided with absorption entrance、Absorption outlet、Concentration entrance and concentration outlet，One end of waste gas secondary filter is provided with exhaust gas entrance，The other end of waste gas secondary filter is connected on absorption entrance，Described desorption catalyzing combustion system includes regeneration blower fan、Electric heater、Catalytic combustor、Gas mixer chamber and just imitate air filter，The two ends just imitating air filter are connected on gas mixer chamber，Gas mixer chamber is connected with catalytic combustor，Catalytic combustor is connected with electric heater，Electric heater is connected with regeneration blower motor，Concentration outlet is connected with regeneration blower motor，Concentration entrance is connected with gas mixer chamber，Absorption outlet is connected with catalytic combustor，The connecting tube of absorption outlet and catalytic combustor is provided with absorption blower motor，Absorption blower motor is externally provided with waste gas outlet.
Preferably, described absorption entrance, absorption outlet, concentration entrance, concentration exit are equipped with cylinder locellus valve, wherein absorption porch is provided with the first cylinder locellus valve, the second cylinder locellus valve, the 3rd cylinder locellus valve and the 4th cylinder locellus valve, first cylinder locellus valve communicates with described first chamber, second cylinder locellus valve communicates with described second chamber, 3rd cylinder locellus valve communicates with described 3rd chamber, and the 4th cylinder locellus valve communicates with described 4th chamber；Absorption exit is provided with the 5th cylinder locellus valve, the 6th cylinder locellus, the 7th cylinder locellus and the 8th cylinder locellus valve, 5th cylinder locellus valve communicates with described first chamber, 6th cylinder locellus communicates with described second chamber, 7th cylinder locellus communicates with described 3rd chamber, and the 8th cylinder locellus valve communicates with described 4th chamber；Concentration porch is provided with the 9th cylinder locellus valve, the tenth cylinder locellus valve, the 11st cylinder locellus valve and the 12nd cylinder locellus valve, 9th cylinder locellus valve communicates with described first chamber, tenth cylinder locellus communicates with described second chamber, 11st cylinder locellus communicates with described 3rd chamber, and the 12nd cylinder locellus valve communicates with described 4th chamber；The concentration outlet place of being provided with is provided with the 13rd cylinder locellus valve, the 14th cylinder locellus valve, the 15th cylinder locellus valve and the 16th cylinder locellus valve, 13rd cylinder locellus valve communicates with described first chamber, 14th cylinder locellus communicates with described second chamber, 15th cylinder locellus communicates with described 3rd chamber, and the 16th cylinder locellus valve communicates with described 4th chamber.
Preferably, described cylinder locellus valve be provided with magnetic switch be connected.
Preferably, the connecting tube of described just effect air filter one end and described gas mixer chamber is provided with the first manual modulation valve, just the effect air filter other end is provided with the second manual modulation valve and pneumatic operated valve with the connecting tube of described gas mixer chamber, and pneumatic operated valve is provided with pneumatic operated valve letter in reply device；Connecting tube between gas mixer chamber and described catalytic combustor is provided with the 3rd manual modulation valve, is provided with the 4th manual modulation valve between catalytic combustor and described waste gas filter chamber.
Preferably, on described electric heater, outer wall is provided with the first temperature detector, on electric heater, inwall is provided with the second temperature detector, the 3rd temperature detector it is provided with between electric heater and described catalytic combustor, described catalytic combustor is provided with the 4th temperature detector and is connected, and is provided with the 5th temperature detector between described waste gas filter chamber and described gas mixer chamber.
Preferably, the bottom of described waste gas filter chamber is provided with ash-valve.
Provide the benefit that: this device is by controlling the opening and closing of different chamber, it is possible to achieve Adsorption Concentration system and desorption catalyzing combustion system are run continuously, it is not necessary to increase equipment in parallel and carry out off-line desorption；In running, air current flow is open, so being absent from the danger of blast；Adding catalyst in combustion, reduce the activation energy that reaction is required, thus reducing the temperature required of organic substance burning, decreasing energy expenditure；Catalytic combustor catalysis burning can make waste gas carry out non-flaming combustion at a lower temperature, reduces ignition temperature, thus avoiding thermal losses well while not affecting efficiency of combustion；The high-temperature gas produced that simultaneously burns takes a part and carries out hybrid cooling with air, obtains resolving desired gas, it is to avoid heat losses；This equipment is specific to what VOCs processed, it is possible to be used in combination with other mineral waste Flash Gas Compression Skid Systems.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of VOCs treatment equipment of the present invention；
Wherein 1, exhaust gas entrance；2, waste gas secondary filter；3, waste gas filter chamber；4, adsorb entrance；5, absorption outlet；6, concentrate entrance；7, concentration outlet；8, adsorb blower motor；9, gas mixer chamber；10, catalytic combustor；11, just imitate air filter；12, electric heater；13, regenerate blower motor；14, cylinder locellus valve；15, magnetic switch；16, ash-valve；17, pneumatic operated valve；18, pneumatic operated valve letter in reply device；19, the first manual modulation valve；20, the second manual modulation valve；21, the 3rd manual modulation valve；22, the 4th manual modulation valve；23, the first temperature detector；24, the second temperature detector；25, the 3rd temperature detector；26, the 4th temperature detector；27, the 5th temperature detector；28, waste gas outlet.
Detailed description of the invention
The preferred embodiment of the present invention is described in detail below in conjunction with accompanying drawing.
nullFig. 1 shows the detailed description of the invention of the present invention a kind of VOCs treatment equipment: a kind of VOCs treatment equipment，Including Adsorption Concentration system and desorption catalyzing combustion system，It is characterized in that: described waste gas Adsorption Concentration system includes the waste gas secondary filter 2 being connected successively、Waste gas filter chamber 3 and absorption blower fan，The first chamber it is provided with in waste gas filter chamber 3、Second chamber、3rd chamber and the 4th chamber，Waste gas filter chamber 3 is provided with absorption entrance 4、Absorption outlet 5、Concentration entrance 6 and concentration outlet 7，One end of waste gas secondary filter 2 is provided with exhaust gas entrance 1，The other end of waste gas secondary filter 2 is connected on absorption entrance 4，Described desorption catalyzing combustion system includes regeneration blower fan、Electric heater 12、Catalytic combustor 10、Gas mixer chamber 9 and just effect air filter 11，The two ends just imitating air filter 11 are connected on gas mixer chamber 9，Gas mixer chamber 9 is connected with catalytic combustor 10，Catalytic combustor 10 is connected with electric heater 12，Electric heater 12 is connected with regeneration blower motor 13，Concentration outlet 7 is connected with regeneration blower motor 13，Concentration entrance 6 is connected with gas mixer chamber 9，Absorption outlet 5 is connected with catalytic combustor 10，The connecting tube of absorption outlet 5 and catalytic combustor 10 is provided with absorption blower motor 8，Absorption blower motor 8 is externally provided with waste gas outlet 28.The bottom of described waste gas filter chamber 3 is provided with ash-valve 16.
Described absorption entrance 4, absorption outlet 5, concentration entrance 6, concentration outlet 7 places are equipped with cylinder locellus valve 14, wherein absorption entrance 4 place is provided with the first cylinder locellus valve the 14, second cylinder locellus valve the 14, the 3rd cylinder locellus valve 14 and the 4th cylinder locellus valve 14, first cylinder locellus valve 14 communicates with described first chamber, second cylinder locellus valve 14 communicates with described second chamber, 3rd cylinder locellus valve 14 communicates with described 3rd chamber, and the 4th cylinder locellus valve 14 communicates with described 4th chamber；Absorption outlet 5 places are provided with the 5th cylinder locellus valve the 14, the 6th cylinder locellus, the 7th cylinder locellus and the 8th cylinder locellus valve 14,5th cylinder locellus valve 14 communicates with described first chamber, 6th cylinder locellus communicates with described second chamber, 7th cylinder locellus communicates with described 3rd chamber, and the 8th cylinder locellus valve 14 communicates with described 4th chamber；Concentration entrance 6 place is provided with the 9th cylinder locellus valve the 14, the tenth cylinder locellus valve the 14, the 11st cylinder locellus valve the 14 and the 12nd cylinder locellus valve 14,9th cylinder locellus valve 14 communicates with described first chamber, tenth cylinder locellus communicates with described second chamber, 11st cylinder locellus communicates with described 3rd chamber, and the 12nd cylinder locellus valve 14 communicates with described 4th chamber；Concentration outlet 7 places of being provided with are provided with the 13rd cylinder locellus valve the 14, the 14th cylinder locellus valve the 14, the 15th cylinder locellus valve the 14 and the 16th cylinder locellus valve 14,13rd cylinder locellus valve 14 communicates with described first chamber, 14th cylinder locellus communicates with described second chamber, 15th cylinder locellus communicates with described 3rd chamber, and the 16th cylinder locellus valve 14 communicates with described 4th chamber.Described cylinder locellus valve 14 is provided with magnetic switch 15 and is connected.
The connecting tube of described just effect air filter 11 one end and described gas mixer chamber 9 is provided with the first manual modulation valve 19, just effect air filter 11 other end is provided with the second manual modulation valve 20 and pneumatic operated valve 17 with the connecting tube of described gas mixer chamber 9, and pneumatic operated valve 17 is provided with pneumatic operated valve letter in reply device 18；Connecting tube between gas mixer chamber 9 and described catalytic combustor 10 is provided with the 3rd manual modulation valve 21, is provided with the 4th manual modulation valve 22 between catalytic combustor 10 and described waste gas filter chamber 3.
On described electric heater 12, outer wall is provided with the first temperature detector 23, on electric heater 12, inwall is provided with the second temperature detector 24, the 3rd temperature detector 25 it is provided with between electric heater 12 and described catalytic combustor 10, described catalytic combustor 10 is provided with the 4th temperature detector 26 and is connected, and is provided with the 5th temperature detector 27 between described waste gas filter chamber 3 and described gas mixer chamber 9.
After waste gas first passes around firsts and seconds dedusting, open waste gas filter chamber 3 and adsorb the cylinder locellus valve 14 of four sub-chamber and the waste gas absorption outlet 5 cylinder locellus valves 14 of entrance 4.Concentration entrance 6 cylinder locellus valve 14 and concentration outlet 7 cylinder locellus valves 14 are closed, and soot cleaning valve is in normally off.Absorption blower motor 8 is started working, and after adsorbing work about 40 hours, adsorbing material absorption is saturated, and equipment enters concentration catalytic stages.
When the adsorbing material in the first chamber reaches absorption saturated capacity, waste gas is adsorbed entrance 4 first cylinder locellus valve 14 and waste gas absorption outlet 5 the 5th cylinder locellus valves 14 cut out, waste gas concentration entrance 6 the 9th cylinder locellus valve 14 and waste gas concentration outlet 7 the 13rd cylinder locellus valves 14 are opened, catalytic combustor 10 the 4th manual modulation valve 22 and the first manual modulation valve 19, second manual modulation valve 20, 3rd manual modulation valve 21 is opened, regeneration blower motor 13 opens work, electric heater 12 is started working simultaneously, regeneration gas enters through concentrating entrance 6 from waste gas, after adsorbing material is resolved, the high-concentration waste gas produced is discharged from waste gas concentration outlet 7, enter catalytic combustor 10 after heated burn and discharge.First temperature detector the 23, second temperature detection, the 3rd temperature detection and the 4th temperature detector 26 carry out temperature and monitor in real time, during beyond temperature range, electric heater 12 is carried out switching manipulation by control system, each several part temperature is made to maintain work in normal temperature range, 5th temperature detector 27 detects the temperature of regeneration gas, when temperature is beyond the temperature range set, control system controls pneumatic operated valve 17 switch and is adjusted.First chamber resolved desorption after 1 hour, waste gas absorption entrance 4 second cylinder locellus valve 14 and waste gas absorption outlet 5 the 6th cylinder locellus valves 14 of the second chamber are closed, waste gas concentration entrance 6 the tenth cylinder locellus valve 14 and waste gas concentration outlet 7 the 14th cylinder locellus valves 14 are opened, simultaneously the waste gas absorption entrance 4 first cylinder locellus valve 14 of the first chamber and waste gas absorption outlet 5 the 5th cylinder locellus valves 14 are opened, waste gas concentration entrance 6 the 9th cylinder locellus valve 14 and waste gas concentration outlet 7 the 13rd cylinder locellus valves 14 are closed, and the first chamber carries out waste gas absorption phase again.Be the second chamber, the 3rd chamber afterwards successively, the 4th chamber is same as above carries out desorption work.When the 4th chamber desorption completes, electric heater 12 cuts out, regeneration blower motor 13 works on 10 minutes and lowers the temperature, it is then shut off, finally, waste gas absorption entrance 4 the 4th cylinder locellus valve 14 and waste gas absorption outlet 5 the 8th cylinder locellus valves 14 of the 4th chamber are opened, and waste gas concentration entrance 6 the 12nd cylinder locellus valve 14 and waste gas concentration outlet 7 the 16th cylinder locellus valves 14 are closed.So far, concentration catalysis combustion phases completes, and all-in-one is again introduced into waste gas absorption phase, periodic duty.
Based on above-mentioned, this device was controlled by folding and the time of multiple chambers so that absorption and desorption combustion phases can run in continuous operation.The waste gas of low concentration Wind Volume, by concentrating, carries out non-flaming combustion under the effect of catalyst after desorption, the temperature that own combustion produces simultaneously can meet ignition temperature, it is not necessary to external heat again, fully generates carbon dioxide and water after burning.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every equivalent structure utilizing description of the present invention and accompanying drawing content to make or equivalence flow process conversion; or directly or indirectly it is used in other relevant technical fields, all in like manner include in the scope of patent protection of the present invention.
Claims (6)
- null1. a VOCs treatment equipment，Including Adsorption Concentration system and desorption catalyzing combustion system，It is characterized in that: described waste gas Adsorption Concentration system includes the waste gas secondary filter being connected successively、Waste gas filter chamber and absorption blower fan，The first chamber it is provided with in waste gas filter chamber、Second chamber、3rd chamber and the 4th chamber，Waste gas filter chamber is provided with absorption entrance、Absorption outlet、Concentration entrance and concentration outlet，One end of waste gas secondary filter is provided with exhaust gas entrance，The other end of waste gas secondary filter is connected on absorption entrance，Described desorption catalyzing combustion system includes regeneration blower fan、Electric heater、Catalytic combustor、Gas mixer chamber and just imitate air filter，The two ends just imitating air filter are connected on gas mixer chamber，Gas mixer chamber is connected with catalytic combustor，Catalytic combustor is connected with electric heater，Electric heater is connected with regeneration blower motor，Concentration outlet is connected with regeneration blower motor，Concentration entrance is connected with gas mixer chamber，Absorption outlet is connected with catalytic combustor，The connecting tube of absorption outlet and catalytic combustor is provided with absorption blower motor，Absorption blower motor is externally provided with waste gas outlet.
- 2. a kind of VOCs treatment is equipped according to claim 1, it is characterized in that: described absorption entrance, absorption outlet, concentration entrance, concentration exit are equipped with cylinder locellus valve, wherein absorption porch is provided with the first cylinder locellus valve, the second cylinder locellus valve, the 3rd cylinder locellus valve and the 4th cylinder locellus valve, first cylinder locellus valve communicates with described first chamber, second cylinder locellus valve communicates with described second chamber, 3rd cylinder locellus valve communicates with described 3rd chamber, and the 4th cylinder locellus valve communicates with described 4th chamber；Absorption exit is provided with the 5th cylinder locellus valve, the 6th cylinder locellus, the 7th cylinder locellus and the 8th cylinder locellus valve, 5th cylinder locellus valve communicates with described first chamber, 6th cylinder locellus communicates with described second chamber, 7th cylinder locellus communicates with described 3rd chamber, and the 8th cylinder locellus valve communicates with described 4th chamber；Concentration porch is provided with the 9th cylinder locellus valve, the tenth cylinder locellus valve, the 11st cylinder locellus valve and the 12nd cylinder locellus valve, 9th cylinder locellus valve communicates with described first chamber, tenth cylinder locellus communicates with described second chamber, 11st cylinder locellus communicates with described 3rd chamber, and the 12nd cylinder locellus valve communicates with described 4th chamber；The concentration outlet place of being provided with is provided with the 13rd cylinder locellus valve, the 14th cylinder locellus valve, the 15th cylinder locellus valve and the 16th cylinder locellus valve, 13rd cylinder locellus valve communicates with described first chamber, 14th cylinder locellus communicates with described second chamber, 15th cylinder locellus communicates with described 3rd chamber, and the 16th cylinder locellus valve communicates with described 4th chamber.
- 3. a kind of VOCs treatment is equipped according to claim 2, it is characterised in that: described cylinder locellus valve is provided with magnetic switch and is connected.
- 4. a kind of VOCs treatment is equipped according to claim 1, it is characterized in that: the connecting tube of described just effect air filter one end and described gas mixer chamber is provided with the first manual modulation valve, just the effect air filter other end is provided with the second manual modulation valve and pneumatic operated valve with the connecting tube of described gas mixer chamber, and pneumatic operated valve is provided with pneumatic operated valve letter in reply device；Connecting tube between gas mixer chamber and described catalytic combustor is provided with the 3rd manual modulation valve, is provided with the 4th manual modulation valve between catalytic combustor and described waste gas filter chamber.
- 5. a kind of VOCs treatment is equipped according to claim 1, it is characterized in that: on described electric heater, outer wall is provided with the first temperature detector, on electric heater, inwall is provided with the second temperature detector, the 3rd temperature detector it is provided with between electric heater and described catalytic combustor, described catalytic combustor is provided with the 4th temperature detector and is connected, and is provided with the 5th temperature detector between described waste gas filter chamber and described gas mixer chamber.
- 6. a kind of VOCs treatment is equipped according to claim 1, it is characterised in that: the bottom of described waste gas filter chamber is provided with ash-valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610317767.6A CN105771640A (en) | 2016-05-14 | 2016-05-14 | Treatment equipment for organic waste gases |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610317767.6A CN105771640A (en) | 2016-05-14 | 2016-05-14 | Treatment equipment for organic waste gases |
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| CN105771640A true CN105771640A (en) | 2016-07-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610317767.6A Pending CN105771640A (en) | 2016-05-14 | 2016-05-14 | Treatment equipment for organic waste gases |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106582194A (en) * | 2016-12-16 | 2017-04-26 | 芜湖万向新元环保科技有限公司 | High-temperature gas mixing chamber |
| CN106838943A (en) * | 2016-12-20 | 2017-06-13 | 芜湖万向新元环保科技有限公司 | A kind of VOCs treatment system |
| CN107970739A (en) * | 2016-10-21 | 2018-05-01 | 无锡云瑞环保设备有限公司 | Zeolite molecular sieve catalysis pyrolysis oven |
| CN114322168A (en) * | 2020-09-29 | 2022-04-12 | 依必安派特穆尔芬根有限两合公司 | Device for disinfecting air by means of combustion |
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| CN101293167A (en) * | 2008-06-27 | 2008-10-29 | 北京工业大学 | Large-air capacity integral continuous operation adsorbing device |
| CN202700317U (en) * | 2012-06-26 | 2013-01-30 | 蔡宇峰 | Chamber-separated off-line desorption molecular sieve filter cartridge adsorption equipment |
| CN202909606U (en) * | 2012-11-12 | 2013-05-01 | 天津市联合环保工程设计有限公司 | Multifunctional integrated treatment device of organic waste gas |
| CN205760440U (en) * | 2016-05-14 | 2016-12-07 | 芜湖万向新元环保科技有限公司 | A kind of VOCs treatment equipment |
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2016
- 2016-05-14 CN CN201610317767.6A patent/CN105771640A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101293167A (en) * | 2008-06-27 | 2008-10-29 | 北京工业大学 | Large-air capacity integral continuous operation adsorbing device |
| CN202700317U (en) * | 2012-06-26 | 2013-01-30 | 蔡宇峰 | Chamber-separated off-line desorption molecular sieve filter cartridge adsorption equipment |
| CN202909606U (en) * | 2012-11-12 | 2013-05-01 | 天津市联合环保工程设计有限公司 | Multifunctional integrated treatment device of organic waste gas |
| CN205760440U (en) * | 2016-05-14 | 2016-12-07 | 芜湖万向新元环保科技有限公司 | A kind of VOCs treatment equipment |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107970739A (en) * | 2016-10-21 | 2018-05-01 | 无锡云瑞环保设备有限公司 | Zeolite molecular sieve catalysis pyrolysis oven |
| CN106582194A (en) * | 2016-12-16 | 2017-04-26 | 芜湖万向新元环保科技有限公司 | High-temperature gas mixing chamber |
| CN106838943A (en) * | 2016-12-20 | 2017-06-13 | 芜湖万向新元环保科技有限公司 | A kind of VOCs treatment system |
| CN114322168A (en) * | 2020-09-29 | 2022-04-12 | 依必安派特穆尔芬根有限两合公司 | Device for disinfecting air by means of combustion |
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Application publication date: 20160720 |
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