CN108644794A - A kind of improvement VOCs systems - Google Patents
A kind of improvement VOCs systems Download PDFInfo
- Publication number
- CN108644794A CN108644794A CN201810452713.XA CN201810452713A CN108644794A CN 108644794 A CN108644794 A CN 108644794A CN 201810452713 A CN201810452713 A CN 201810452713A CN 108644794 A CN108644794 A CN 108644794A
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- pipeline
- vocs
- air
- preheating device
- unhurried current
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- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 70
- 230000006872 improvement Effects 0.000 title claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 30
- 238000005192 partition Methods 0.000 claims abstract description 9
- 230000001681 protective effect Effects 0.000 claims description 6
- 238000005086 pumping Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 33
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 18
- 230000009467 reduction Effects 0.000 abstract description 12
- 239000003345 natural gas Substances 0.000 abstract description 9
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 16
- 238000004519 manufacturing process Methods 0.000 description 16
- 238000005265 energy consumption Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000012530 fluid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
The present invention relates to a kind of improvement VOCs systems, including shell and partition board, high temperature furnace is separated out unhurried current air flue by partition board, and the high temperature furnace for heating unhurried current air flue is equipped in unhurried current air flue;Its middle casing is respectively equipped with return air heating device and preheating device, at least one baking oven is equipped between return air heating device and preheating device, it is connected by air-heater between baking oven side and return air heating device, it is connected by taking out exhaust gas fan between the baking oven other side and preheating device, jet pipe is equipped in high temperature furnace, jet pipe is connected with new wind turbine, and new wind turbine one end is connected with preheating device.The beneficial effects of the invention are as follows:More stable, more thorough emission reduction:It takes in unhurried current air flue, return air heating device and the preheating device that VOCs airflow circulatings are walked, VOCs air-flows are to air without direct emission, only enter on a small quantity when needing release in return air heating device or preheating device, in the case where sufficient natural gas fires flame and Quantity of heat, this small amount of VOCs is thoroughly handled.
Description
Technical field
The present invention relates to a kind of improvement VOCs systems.
Background technology
The pollution of China VOCs has been subjected to going into politics mansion to the extensive concern of the common people, administers extremely urgent.So far, VOCs
Treatment process can be divided into source reduction technology, process control technology and end treatment technology, and feelings are controlled from domestic existing VOCs
From the point of view of condition, every profession and trade mainly uses end-of-pipe control technology, and control measures are taken to the volatile organic matter generated.Wherein,
In traditional VOCs treatment field comparative maturity, application is relatively extensive for absorption, absorption, condensation, combustion technology;UF membrane,
Biotechnology, plasma technology are then emerging technologies, are also obtaining extensive concern in the recent period.But these technologies reported or used
It mainly considers a problem from point, i.e., is only dedicated to reductions of total VOCs to air discharge capacity(That is emission reduction), can usually bring it
The increase etc. of his new problem, such as secondary pollution, safety in utilization and enterprise's total energy consumption, few technologies are from generation VOCs's
The industry actual production overall situation is set out, and is systematically carried out VOCs improvement, energy saving, emission reduction and safety issue are once solved.
The application number 200810185561.8 of first Chinese patent, a kind of entitled environment friendly energy-saving air-discharging treating device and side
Method;The application number 200920152633.9 of second Chinese patent, a kind of entitled energy conservation and environmental protection organic solvent voc treatment device;
The application number 201610742937.5 of third Chinese patent, a kind of entitled energy-saving organic waste gas treatment system;4th China
The application number 201610833165.6 of patent, a kind of entitled energy-efficient formula spraying drying system;The Shen of 5th Chinese patent
Please numbers 201710787572.2, a kind of entitled combustion-type VOC processing units;With the application number of the 6th Chinese patent
201711329846.X the entitled energy saving hybrid processing system of Industrial Stoves VOC exhaust gas;It has all referred to not only energy saving but also emission reduction
VOCs treatment technologies, common point are directly to carry out burning processing after concentrating VOCs, generated treated qualified air-flow
Discharging directly into atmosphere, generated thermal energy are utilized by heat exchange, are reduced enterprise and are produced total energy consumption.
But it is this by heat exchange realization heat energy utilization, necessarily there is certain heat loss;The directly method of burning processing
The VOCs for comparing high concentration is needed, is easier that safety problem occurs, for example explode;Discharging directly into atmosphere after VOCs burnings, works as equipment
When fluctuation of service, discharge beyond standards are easy, the stability of regulation effect is poor.
The application number 201710839338.X of 7th Chinese patent, entitled energy saving VOC exhaust treatment systems;Relatively preceding institute
For stating patent, the energy-saving and emission-reduction that not only have its common, it is also contemplated that it is total will to account for VOCs exhaust gas for the self-contained thermal energy of exhaust gas
For drying in the VOCs exhaust gas recirculations to the drying cavity body of amount 20% to 40%.
The application number 201710097254.3 of 8th Chinese patent, it is entitled for handling VOC gas method for pyrolysis, relatively
The advance of 7th Chinese patent is the high usage of waste gas stream thermal energy:VOCs air-flows collected by from production equipment exist
After the processing of 700 to 800 degree, gained cleans thermal current 100% and returns production equipment by pipeline, greatly improves the profit of thermal energy
With rate, reduce the total energy consumption of actual production.Although the technology and taking improvement to arrange the volatile organic matter generated
Apply, but high temperature remove VOCs cleaning thermal current not according to the such direct emission air of other technologies, but by temperature adjustment after
Input needs the production equipment of hot wind directly to replace the ambient wind for needing electric energy or steam that can heat originally, and carries new generate
VOCs enter next cycle, achieved the purpose that it is a kind of not only having handled VOCs and reduce produce total energy consumption;In the technology
It burns without the concentration also flames of anger, is that the VOCs that will be collected into directly is pyrolyzed in high temperature furnace, safety has obtained certain
It improves.But its cleaning gas tream does not lead to air, but forms airflow circulating, persistently have at production equipment a small amount of fresh air into
Enter, pressure can gradually increase, and entire gas channel has the security risk of explosion;And the technology is only referred to VOCs airflow circulatings
There is a certain distance part there is no produce reality is considered comprehensively from system treatment technology.
Invention content
Itd is proposed the invention solves above-mentioned technical problem it is a kind of can solve the problems, such as emission reduction, it is energy saving and safety three aspects
Improvement VOCs systems.
Shell is separated out unhurried current air flue by a kind of improvement VOCs systems according to the present invention, including shell and partition board, partition board,
The high temperature furnace for heating unhurried current air flue is equipped in unhurried current air flue, middle casing is respectively equipped with return air heating device and pre- hot charging
It sets, at least one baking oven is equipped between return air heating device and preheating device, is passed through between baking oven side and return air heating device
Air-heater is connected, and is connected by taking out exhaust gas fan between the baking oven other side and preheating device, and jet pipe, spray are equipped in high temperature furnace
Pipe is connected with new wind turbine, and new wind turbine one end is connected with preheating device.
Specific further the baking oven side is equipped with ink tank, and the entrance for taking out exhaust gas fan extends at ink tank side.
Specific further the shell is equipped with protective device, and protective device is tonifying Qi fan, and the outlet of tonifying Qi fan extends
To unhurried current air flue.
It is specific to be further connected by one way pressure-reducing valve between described new wind turbine one end and preheating device, it is unidirectional to depressurize
It is connected by back pressure pipe between the gas outlet of valve and new wind turbine.
Specific further the return air heating device includes the first pipeline and the second pipeline, and the second pipeline is placed in the first pipe
In road, the first pipeline is connected with unhurried current air flue, and the second pipeline is connected with high temperature furnace.
Specific further, second pipeline is connected with the air inlet of air-heater.
Specific further second pipeline is equipped with exhaust fan, and exhaust fan is equipped with first outlet.
It is specific that further the preheating device includes third pipeline and the 4th pipeline, and the 4th pipeline is placed in third pipeline,
Third pipeline with take out exhaust gas fan air outlet be connected, third pipeline with unhurried current air flue entrance be connected, third pipeline and
Second pipeline is connected.
Specific further, the 4th piping connection has main air blower.
The beneficial effects of the invention are as follows:
1. more stable, more thorough emission reduction:Take unhurried current air flue, return air heating device and preheating device that VOCs airflow circulatings are walked
Interior, VOCs air-flows without direct emission, only enter in return air heating device or preheating device air when needing release on a small quantity,
It is very long and under having sufficient natural gas combustion flame and Quantity of heat, this small amount of VOCs is handled substantially;Although high temperature furnace occasionally has work
Make deficiency, the VOCs not being adequately processed enters next cycle with hot wind, will not pollute air, emission reduction effect is more stable.
2. more excellent is energy saving:Treated that hot-fluid can very introduce return air heating device for high temperature furnace, into production
Equipment participates in production, can allow production equipment that need not can maintain to run well using electric energy or steam substantially, greatly reduce
The total energy consumption of production;In addition, the natural gas of open fire burning generates heat by drainage, a part enters preheating device, by institute
The VOCs air-flows of collection are preheated, and a part enters return air heating device, will be cleaned hot-fluid and are maintained at the temperature that baking oven needs;
This allows enterprise while reaching discharge standard using technical finesse VOCs, and energy consumption significantly reduces, and enterprise directly increases income, will locate
It manages VOCs to organically combine with enterprise getting profit, fundamentally solves the problems, such as that prior art operation ratio is low so that life air obtains
To practical improvement.
3. safer system:Buffer runner is provided with and connects open to atmosphere tonifying Qi fan, and the of cooperation return air heating device
One outlet, can make the unobstructed no high pressure of air-flow, greatly reduce whole system and the possibility exploded occur;Pending VOCs low concentrations
It is difficult to directly burn, the binary channel design of inside and outside separation makes it not contact open fire, is not susceptible to fire.
Description of the drawings
The above-mentioned and/or additional aspect and advantage of the present invention will become in the description from combination following accompanying drawings to embodiment
Obviously and it is readily appreciated that.
Fig. 1 is the structural diagram of the present invention.
It is reference sign below:
Shell 1;Partition board 101;High temperature furnace 2;Protective device 3;Jet pipe 4;New wind turbine 401;First outlet 5;Exhaust fan 6;First
Pipeline 7;Second pipeline 8;Air-heater 9;Baking oven 10;Ink tank 1001;Take out exhaust gas fan 11;Third pipeline 12;4th pipeline 13;
One way pressure-reducing valve 14;Main air blower 15;Back pressure pipe 16.
Specific implementation mode
The embodiment of the present invention is described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning to end
Same or similar label indicates same or similar element or element with the same or similar functions.Below with reference to attached
The embodiment of figure description is exemplary, and is only used for explaining the present invention, and is not considered as limiting the invention.
A kind of improvement VOCs systems according to the ... of the embodiment of the present invention, including shell 1 and partition board 101 are described below with reference to Fig. 1,
Shell 1 is separated out unhurried current air flue by partition board 101, and the high temperature furnace 2 for heating unhurried current air flue is equipped in unhurried current air flue;Its middle casing
1 is respectively equipped with return air heating device and preheating device, and at least one baking oven 10 is equipped between return air heating device and preheating device,
It is connected by air-heater 9 between 10 side of baking oven and return air heating device, is passed through between 10 other side of baking oven and preheating device
It takes out exhaust gas fan 11 to be connected, jet pipe 4 is equipped in high temperature furnace 2, jet pipe 4 is connected with new wind turbine 401, the connection of 401 one end of new wind turbine
There is preheating device.The shell 1 is equipped with protective device 3, and protective device 3 is tonifying Qi fan, and the outlet of tonifying Qi fan extends to slow
In gas road, supplement air is carried out to unhurried current air flue and accelerates circulation.
Have after implementing through the invention as follows:One, is more stable, more thorough emission reduction:Take what VOCs airflow circulatings were walked
Flow slowly air flue, return air heating device and preheating device, and to air without direct emission, only a small amount of VOCs air-flows are needing VOCs air-flows
It wants when release to enter in return air heating device or preheating device, very long and there is sufficient natural gas combustion flame and heat to obtain designated value
Under, this small amount of VOCs is handled substantially(It is catalyzed and is pyrolyzed);Although high temperature furnace occasionally has work insufficient, is not adequately processed
VOCs enters next cycle with hot wind, will not pollute air, emission reduction effect is more stable.
More excellent energy saving of two,:Treated that hot-fluid can very introduce return air heating device for high temperature furnace, into production
Equipment participates in production, can allow production equipment that need not can maintain to run well using electric energy or steam substantially, greatly reduce
The total energy consumption of production;In addition, the natural gas production heat of open fire burning is by drainage, a part enters preheating device, by institute
The VOCs air-flows of collection are tentatively preheated, and another part enters return air heating device, and cleaning hot-fluid, which is maintained at baking oven 10, to be needed
The temperature wanted;This allows enterprise while reaching discharge standard using technical finesse VOCs, and energy consumption significantly reduces, and enterprise is direct
It increases income, processing VOCs and enterprise getting profit is organically combined, fundamentally solve the problems, such as that prior art operation ratio is low so that is raw
Air living obtains practical improvement.
System safer three,:Buffer runner is provided with and connects open to atmosphere tonifying Qi fan, and the of cooperation return air heating device
One outlet 5, can make the unobstructed no high pressure of air-flow, greatly reduce whole system and the possibility exploded occur;Pending VOCs is low dense
Degree is difficult to directly burn, and the binary channel design of inside and outside separation makes it not contact open fire, is not susceptible to fire.
10 side of baking oven of the present invention is equipped with ink tank 1001, and the entrance for taking out exhaust gas fan 11 extends to 1001 side of ink tank
Place can enter the VOCs gases effect that ink tank 1001 generates of collecting;Pass through between described 401 one end of new wind turbine and preheating device
One way pressure-reducing valve 14 is connected, and is connected by back pressure pipe 16 between the gas outlet of one way pressure-reducing valve 14 and new wind turbine 401.It is described
Return air heating device includes the first pipeline 7 and the second pipeline 8, and the second pipeline 8 is placed in the first pipeline 7, the first pipeline 7 and unhurried current
Air flue is connected, and the second pipeline 8 is connected with high temperature furnace 2, and second pipeline 8 is connected with the air inlet of air-heater 9, the
The surplus VOCs gases in the first pipeline of high-temperature gas pair 7 in two pipelines 8 are pyrolyzed and are catalyzed into harmless high-temperature gas.Institute
State the second pipeline 8 be equipped with exhaust fan 6, exhaust fan 6 be equipped with first outlet 5, wherein high-temperature gas by the second pipeline 8 into
Become cryogenic gas after row heat exchange to discharge by first outlet 5.The preheating device includes third pipeline 12 and the 4th
Pipeline 13, the 4th pipeline 13 are placed in third pipeline 12, and third pipeline 12 is connected with the air outlet for taking out exhaust gas fan 11, third
Pipeline 12 is connected with the entrance of unhurried current air flue, and third pipeline 12 is connected with the second pipeline 8.4th pipeline 13 is connected with
Main air blower 15 plays the gas circulation for accelerating the 4th pipeline 13.The path wherein walked as heat source:Heat source is open fire in high temperature
The natural gas to burn in stove 2, the high temperature gas flow of generation is by heat, and main air blower 15 is in running order, and air passes through the 4th pipeline
During 13 enter, air flows through 2 surface of high temperature furnace, and the heat for taking away 2 surface of high temperature furnace obtains pre-heat effect, and cooperation is high
The high temperature heat of warm stove 2 is directly entered in the second pipeline 8, and the second pipeline 8 carries out heat exchange to the first pipeline 7, and implements heat
Surplus VOCs air-flows in the second pipeline 8 of solution and catalysis finally act on lower discharge cryogenic gas from exhaust fan 6.In addition, taking
The outer access that VOCs air-flows are walked:The Wind Volume air-flow for taking VOCs is received from baking oven 10 and ink tank 1001 using exhaust gas fan 11 is taken out
After collection, by the Wind Volume air flow direction buffer runner of the VOCs of third pipeline 12, during flow direction, due to the 4th pipeline 13
One section of surface for flowing to high temperature furnace 2, makes the air in the 4th pipeline 13 be preheated, to the big of the VOCs of third pipeline 12
Air quantity air-flow is tentatively preheated, when the Wind Volume air-flow of VOCs flowed through in buffer runner 2 surface of high temperature furnace carry out in advance solution and
Catalysis, then in the first pipeline 7, secondary pyrolysis and catalysis are carried out by high-temperature gas in the second pipeline 8, finally weighed by air-heater 9
Enter and return to high-temperature hot-air form in baking oven 10, is formed to being recycled in VOCs production areas of the air without discharge;The third pipeline
There is environment wind inlet at 12, and close to high temperature furnace 2.Third pipeline 12 is provided with one way pressure-reducing valve 14, and in one way pressure-reducing valve
14 are connected with back pressure pipe 16, and the VOCs gases of surplus is made to be transported to natural gas wind turbine 401, and height is sent by natural gas wind turbine 401
It burns in warm stove 2, helps combustion of natural gas, VOCs gases therein are also removed by combustion process, are played energy saving
Effect and reduction VOCs gases discharge.
Although an embodiment of the present invention has been shown and described, it will be understood by those skilled in the art that:Not
In the case of being detached from the principle of the present invention and objective a variety of change, modification, replacement and modification can be carried out to these embodiments, this
The range of invention is limited by claim and its equivalent.
Claims (9)
1. shell (1) is separated out unhurried current gas by a kind of improvement VOCs systems, including shell (1) and partition board (101), partition board (101)
Road, the interior high temperature furnace (2) being equipped with for heating unhurried current air flue of unhurried current air flue, it is characterised in that:Shell (1) is respectively equipped with return air and adds
Thermal and preheating device are equipped at least one baking oven (10), baking oven (10) side between return air heating device and preheating device
It is connected by air-heater (9) between return air heating device, baking oven (10) is between the other side and preheating device by taking out exhaust gas
Wind turbine (11) is connected, and jet pipe (4) is equipped in high temperature furnace (2), and jet pipe (4) is connected with new wind turbine (401), new wind turbine (401) one
End is connected with preheating device.
2. administering VOCs systems according to claim 1, it is characterised in that:Baking oven (10) side is equipped with ink tank
(1001), the entrance for taking out exhaust gas fan (11) extends at ink tank (1001) side.
3. administering VOCs systems according to claim 1, it is characterised in that:The shell (1) is equipped with protective device (3), protects
Protection unit (3) is tonifying Qi fan, and the outlet of tonifying Qi fan extends in unhurried current air flue.
4. administering VOCs systems according to claim 1, it is characterised in that:Described new wind turbine (401) one end and preheating device
Between be connected by one way pressure-reducing valve (14), pass through back pressure between the gas outlet and new wind turbine (401) of one way pressure-reducing valve (14)
Pipe (16) is connected.
5. administering VOCs systems according to claim 1, it is characterised in that:The return air heating device includes the first pipeline
(7) it being placed in the first pipeline (7) with the second pipeline (8), the second pipeline (8), the first pipeline (7) is connected with unhurried current air flue, the
Two pipelines (8) are connected with high temperature furnace (2).
6. administering VOCs systems according to claim 5, it is characterised in that:Second pipeline (8) and air-heater (9) into
Gas port is connected.
7. administering VOCs systems according to claim 5, it is characterised in that:Second pipeline (8) is equipped with exhaust fan
(6), exhaust fan (6) is equipped with first outlet (5).
8. administering VOCs systems according to claim 1, it is characterised in that:The preheating device include third pipeline (12) and
4th pipeline (13), the 4th pipeline (13) are placed in third pipeline (12), and third pipeline (12) goes out with pumping exhaust gas fan (11)
Air port is connected, and third pipeline (12) is connected with the entrance of unhurried current air flue, and third pipeline (12) is connected with the second pipeline (8)
It is logical.
9. administering VOCs systems according to claim 8, it is characterised in that:4th pipeline (13) is connected with main air blower
(15)。
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810452713.XA CN108644794A (en) | 2018-05-13 | 2018-05-13 | A kind of improvement VOCs systems |
CN201910392667.3A CN110094744B (en) | 2018-05-13 | 2019-05-13 | Energy-saving and emission-reducing system for double-channel treatment of gravure organic waste gas |
CN201920680305.XU CN210398946U (en) | 2018-05-13 | 2019-05-13 | Energy-saving emission-reducing system for treating gravure organic waste gas through double channels |
CN201920678709.5U CN210398945U (en) | 2018-05-13 | 2019-05-13 | Emission reduction system for gravure organic waste gas |
CN201910392691.7A CN110094745B (en) | 2018-05-13 | 2019-05-13 | Energy-saving and emission-reducing method for treating gravure organic waste gas through double channels |
Applications Claiming Priority (1)
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CN201810452713.XA CN108644794A (en) | 2018-05-13 | 2018-05-13 | A kind of improvement VOCs systems |
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CN108644794A true CN108644794A (en) | 2018-10-12 |
Family
ID=63754971
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CN201810452713.XA Pending CN108644794A (en) | 2018-05-13 | 2018-05-13 | A kind of improvement VOCs systems |
CN201910392667.3A Active CN110094744B (en) | 2018-05-13 | 2019-05-13 | Energy-saving and emission-reducing system for double-channel treatment of gravure organic waste gas |
CN201920678709.5U Active CN210398945U (en) | 2018-05-13 | 2019-05-13 | Emission reduction system for gravure organic waste gas |
CN201910392691.7A Active CN110094745B (en) | 2018-05-13 | 2019-05-13 | Energy-saving and emission-reducing method for treating gravure organic waste gas through double channels |
CN201920680305.XU Active CN210398946U (en) | 2018-05-13 | 2019-05-13 | Energy-saving emission-reducing system for treating gravure organic waste gas through double channels |
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CN201910392667.3A Active CN110094744B (en) | 2018-05-13 | 2019-05-13 | Energy-saving and emission-reducing system for double-channel treatment of gravure organic waste gas |
CN201920678709.5U Active CN210398945U (en) | 2018-05-13 | 2019-05-13 | Emission reduction system for gravure organic waste gas |
CN201910392691.7A Active CN110094745B (en) | 2018-05-13 | 2019-05-13 | Energy-saving and emission-reducing method for treating gravure organic waste gas through double channels |
CN201920680305.XU Active CN210398946U (en) | 2018-05-13 | 2019-05-13 | Energy-saving emission-reducing system for treating gravure organic waste gas through double channels |
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Cited By (1)
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CN112590264A (en) * | 2020-10-30 | 2021-04-02 | 佛吉亚(柳州)汽车座椅有限公司 | Method for reducing VOC (volatile organic compounds) of sponge of automobile seat |
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CN108644794A (en) * | 2018-05-13 | 2018-10-12 | 佛山市佳威节能环保设备有限公司 | A kind of improvement VOCs systems |
CN110500599A (en) * | 2019-08-07 | 2019-11-26 | 佛山市佳威节能环保设备有限公司 | A kind of energy-saving and emission-reduction system of gravure organic exhaust gas |
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CN110094744B (en) | 2024-06-25 |
CN210398945U (en) | 2020-04-24 |
CN110094745B (en) | 2020-10-27 |
CN110094745A (en) | 2019-08-06 |
CN110094744A (en) | 2019-08-06 |
CN210398946U (en) | 2020-04-24 |
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