CN107575876A - A kind of garbage flue gas processing system and method - Google Patents
A kind of garbage flue gas processing system and method Download PDFInfo
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- CN107575876A CN107575876A CN201710996896.7A CN201710996896A CN107575876A CN 107575876 A CN107575876 A CN 107575876A CN 201710996896 A CN201710996896 A CN 201710996896A CN 107575876 A CN107575876 A CN 107575876A
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- flue gas
- heat exchanger
- combustion furnace
- processing system
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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Abstract
The present invention proposes a kind of garbage flue gas processing system and method, belong to technical field of waste treatment, system includes combustion furnace, the side of combustion furnace is connected to rubbish storeroom by conveying device, the opposite side of combustion furnace is connected to deslagging device, the top of combustion furnace is provided with smoke exhaust pipe, smoke exhaust pipe is sequentially connected to first order heat exchanger and second level heat exchanger, flue gas is less than 200 DEG C after being exchanged heat in first order heat exchanger and second level heat exchanger, the end of smoke exhaust pipe is provided with the bag-type dust collector that can remove flue gas endoparticle, the rear end of bag-type dust collector is connected to the absorbent charcoal adsorber of adsorbable bioxin, the rear end of absorbent charcoal adsorber is connected to deacidifying device, the rear end of deacidifying device is provided with chimney.Flue gas drastically cools to less than 200 DEG C after exchanging heat twice, so that bioxin does not reach the condition of synthesis, greatly reduces the generation of bioxin, the flue gas for making finally to discharge meets discharging standards.
Description
Technical field
The present invention relates to field of garbage disposal, more particularly to a kind of garbage flue gas processing system and method.
Background technology
In recent years, as China's domestic waste pollution situation is on the rise, the harmless treatment of rubbish enjoys people
Concern.At present, domestic garbage burning factory coordinates bag-type dust generally using spray charcoal absorption heavy metal in flue gas He bioxin
Device, the flue dust in tail gas, heavy metal He bioxin are collected in the ash of sack cleaner trapping, although sack cleaner exports
Flue gas at or below current state environmental emissioning standard, but the huge sum of money in sack cleaner trapping grey (abbreviation flying dust)
Belong to, bioxin severe overweights.Its cloth bag of the waste incinerator of domestic production traps grey Zhong content of dioxin and reaches thousands of ng-TEQ/
Kg, flying dust contain a large amount of harmful heavy metals and hypertoxic organic matter bioxin, consumer waste incineration contamination control standard (GB18485-
2001) incineration of refuse flyash category hazardous waste is explicitly pointed out, it is impossible to which arbitrarily landfill is stacked, therefore how to realize waste incineration Er Evil
English zero-emission and reduce heavy metals emission and have important practical significance and application value.
The content of the invention
The problem of existing for prior art, the present invention provide a kind of bioxin that reduces and produced, and control noxious gas emission
Garbage flue gas processing system and method.
To achieve these goals, the present invention adopts the following technical scheme that：
A kind of garbage flue gas processing system, including combustion furnace, it is defeated for passing through for the side of incineration firing, the combustion furnace
Device is sent to be connected to rubbish storeroom, the opposite side of the combustion furnace is connected to deslagging device, and the top of the combustion furnace is provided with
For the smoke exhaust pipe of combustion product gases discharge, the smoke exhaust pipe is sequentially connected to first order heat exchanger and second level heat exchanger, flue gas in
It is less than 200 DEG C after being exchanged heat in the first order heat exchanger and the second level heat exchanger, the end of the smoke exhaust pipe is provided with and can gone
Except the bag-type dust collector of flue gas endoparticle, the rear end of the bag-type dust collector is connected to the activated carbon suction of adsorbable bioxin
Adsorption device, the rear end of the absorbent charcoal adsorber are connected to the deacidifying device of removable flue gas middle acid substance, the depickling
The rear end of device is provided with the chimney for flue gas discharge.
Further, not to be in the mood for spiral conveyor, rubbish is automatically sent to the conveying device by the spiral conveyor of not being in the mood for
The bottom of the combustion furnace.
Further, the deslagging device includes the mucking machine for being connected to side at the top of the combustion furnace, and is connected to institute
State the inder pot that goes out of mucking machine, the burning slag in the combustion furnace is discharged by the mucking machine, and be stored in it is described go out inder pot in return
Receive.
Further, the flue-gas temperature of the smoke exhaust pipe porch is 850 DEG C~1000 DEG C, is changed through the first order heat exchanger
Flue-gas temperature after heat is less than 600 DEG C, and the flue-gas temperature after second level heat exchanger heat exchange is less than 200 DEG C.
Further, the side of the first order heat exchanger or the second level heat exchanger is provided with cooling tower, the cooling tower
Water tank the first order heat exchanger and the second level heat exchanger are connected to by water pipe, the water pipe side is provided with water pump,
Cooling water is pumped into the first order heat exchanger and the second level heat exchanger by the water pump.
Further, water temperature detection point is provided with the water tank, monitors the temperature of cooling water in the water tank in real time.
Further, in addition to air-introduced machine, the air-introduced machine are arranged at the absorbent charcoal adsorber and the deacidifying device
Between, or be arranged between the smoke evacuation pipe end and the bag-type dust collector, it is the burning by the air-introduced machine
Negative pressure is provided in stove.
Further, acidity is provided between the deacidifying device and the air-introduced machine or the absorbent charcoal adsorber to monitor
Point, in real time monitoring enter the concentration of flue gas middle acid substance before the deacidifying device, and by feedback of the information to the deacidifying device,
The deacidifying device automatically adjusts the amount of sprinkling depickling solution according to concentration value.
Further, the side of the combustion furnace, which is provided with, is used to spray quadruple effect denitration liquid to remove the nitrogen and sulfide in flue gas
Spray equipment, the spray equipment is connected to out of stock control station, and automatically controlling the spray by the denitration control station fills
The spray flux put.
A kind of method based on above-mentioned garbage flue gas processing system processing rubbish, including the conveying device start, rubbish
The combustion furnace is delivered to by the conveying device by the rubbish storeroom, burnt in the combustion furnace, the combustion furnace
Interior penetrating quadruple effect denitration liquid is to remove the sulphur-containing substance in combustion product gases, and burning slag is discharged by the deslagging device, combustion product gases
Into the smoke exhaust pipe, and exchanged heat successively with first order heat exchanger and second level heat exchanger, flue-gas temperature is less than after exchanging heat twice
200 DEG C, flue gas after heat exchange removes particle by the bag-type dust collector, subsequently into being gone in the absorbent charcoal adsorber
Chu bioxin, finally enter and acidic materials are removed in the deacidifying device, handle the flue gas of completion by the smoke stack emission to room
Outside.
Beneficial effects of the present invention：
Incineration firing processing is carried out by combustion furnace, the flue gas after burning passes through first order heat exchanger and second level heat exchanger
Less than 200 DEG C are drastically cooled to after exchanging heat twice, so that bioxin does not reach the condition of synthesis, greatly reduces bioxin
Generation, flue gas is then passed through bag-type dust collector and removes deleterious particle, absorbent charcoal adsorber is entered back into, is inhaled by activated carbon
Adsorption device will can not avoid generating the absorption interception of bioxin in fume treatment so that the dioxin in flue gas index finally discharged
Meet national standard discharge standard.The present invention provides a whole set of garbage flue gas processing system, and the flue gas for ensureing to be discharged into air meets
National standard, effect on environment is small, and system processing integrity degree is high, multiple functional, and the efficiency high of garbage disposal, while whole system
The plant area of system is small, and system is concentrated, and is advantageous to garbage disposal.
Brief description of the drawings
Fig. 1 is the structural representation of first embodiment of the invention garbage flue gas processing system；
Fig. 2 is the structural representation of second embodiment of the invention garbage flue gas processing system；
In figure, 1-rubbish storeroom, 2-not being in the mood for spiral conveyor, 3-combustion furnace, 4-mucking machine, 5-go out inder pot,
6-smoke exhaust pipe, 7-first order heat exchanger, 8-second level heat exchanger, 9-cooling tower, 10-water tank, 11-air-introduced machine, 12-
Bag-type dust collector, 13-absorbent charcoal adsorber, 14-acidity monitoring point, 15-deacidifying device, 16-chimney, 17-it is out of stock
Control station, 18-slag releasing channel, 19-process chamber, 20-water pipe, 21-water pump.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only the part of the embodiment of the present invention, rather than whole embodiments.Base
Embodiment in the present invention, those of ordinary skill in the art obtained under the premise of creative work is not made it is all its
His embodiment, belongs to the scope of protection of the invention.
It is to be appreciated that the directional instruction (such as up, down, left, right, before and after ...) of institute is only used in the embodiment of the present invention
In explaining the relative position relation under a certain particular pose (as shown in drawings) between each part, motion conditions etc., if should
When particular pose changes, then directionality instruction also correspondingly changes therewith.In addition, be related in the present invention " first ",
The description of " second " etc. is only used for describing purpose, and it is not intended that instruction or implying its relative importance or implicit indicating institute
The quantity of the technical characteristic of instruction.Thus, " first " is defined, the feature of " second " can be expressed or implicitly include at least
One this feature.
Such as Fig. 1 and Fig. 2, the present invention provides a kind of garbage flue gas processing system, including combustion furnace 3, for for incineration firing,
The side of combustion furnace 3 is connected to rubbish storeroom 1 by conveying device, and rubbish storeroom 1 is used as temporary transient feed bin, stores pending
Rubbish, conveying device is arranged between rubbish storeroom 1 and combustion furnace 3, and in the present embodiment, conveying device is is not in the mood for spiral
Conveyer belt 2, rubbish are automatically sent to the bottom of combustion furnace 3 by not being in the mood for spiral conveyor 2, by the start and stop of conveying device, for burning
Stove 3 provides pending rubbish.The opposite side of combustion furnace 3 is connected to deslagging device, rubbish high-temperature gasification in combustion furnace 3, produces
The burning slag such as ashes discharged by deslagging device, deslagging device includes the mucking machine 4 for being connected to the top side of combustion furnace 3, and
Be connected to mucking machine 4 goes out inder pot 5, and the burning slag such as ashes in combustion furnace 3 is discharged by mucking machine 4, and is stored in out in inder pot 5
Reclaim post-processing.The side of combustion furnace 3 is provided with spray equipment, for spraying quadruple effect denitration liquid to remove the nitrogen and sulphur in flue gas
Compound, spray equipment is connected to out of stock control station 17, and monitoring instrument is provided with denitration control station 17, monitors the dense of flue gas in real time
Degree, so as to automatically control the amount for the quadruple effect denitration liquid that spray equipment sprays into combustion furnace, four can be reduced by monitoring in real time
The waste of denitration liquid is imitated, and can makes final flue gas reach discharging standards.
The top of combustion furnace 3 is provided with smoke exhaust pipe 6, and caused flue gas is discharged by smoke exhaust pipe 6 after the high-temp combustion of combustion furnace 3.Row
The flue-gas temperature of the porch of smoke pipe 6 is 850 DEG C~1000 DEG C, and smoke exhaust pipe 6 is sequentially connected to first order heat exchanger 7 and the second level is changed
Hot device 8, is exchanged heat with the cooling water in first order heat exchanger 7 and second level heat exchanger 8, after the heat exchange of first order heat exchanger 7
Flue-gas temperature drastically cool to less than 600 DEG C, the flue-gas temperature after the heat exchange of second level heat exchanger 8 is drastically cooled to and is less than
200 DEG C, so that bioxin does not reach the condition of synthesis, greatly reduce the generation of bioxin.First order heat exchanger 7 or the second
The side of level heat exchanger 8 is provided with cooling tower 9, and the water tank 10 of cooling tower 9 is connected to first order heat exchanger 7 and second by water pipe 20
Level heat exchanger 8, the side of water pipe 20 is provided with water pump 21, is pumped into by water pump 21 into first order heat exchanger 7 and second level heat exchanger 8
Cooling water.One or more water temperature detection points are provided with water tank 10, in real time in detection water tank 10 cooling water temperature, ensure to the
First-class heat exchanger 7 and second level heat exchanger 8 provide the cooling water of suitable temperature, so as to quick cooled flue gas.
Such as Fig. 1, in the first embodiment, smoke exhaust pipe 6 is inverted U shape inflection, and its bottom end is connected with bag-type dust collector
12, dust and deleterious particle in flue gas are can remove, bag-type dust collector 12 is generally industrial cloth bag gas wash tower.Bag-type dust fills
The rear end for putting 12 is connected to absorbent charcoal adsorber 13, generally activated carbon adsorber, by absorbent charcoal adsorber 13 by cigarette
It can not avoid generating the absorption interception of bioxin in gas disposal so that the dioxin in flue gas index finally discharged meets national standard row
Put standard.The rear end of absorbent charcoal adsorber 13 is connected to air-introduced machine 11, is that negative pressure is provided in combustion furnace 3 by air-introduced machine 11,
Air-introduced machine 11 is placed on to the rear of bag-type dust collector 12 and absorbent charcoal adsorber 13, is to protect air-introduced machine 11 to avoid accumulating
Tired dust etc. causes efficiency to reduce.The rear end of air-introduced machine 11 is connected with deacidifying device 15, can remove the acidic materials in flue gas
Remove, usually spray denitrfying agent and carry out depickling.One or more acidity monitoring points are provided between deacidifying device 15 and air-introduced machine 11,
It can monitor the concentration into the flue gas middle acid substance before deacidifying device 15 in real time, and by feedback of the information to deacidifying device 15, take off
Sour device 15 is according to the concentration value automatic decision of monitoring and adjusts the amount of sprinkling depickling solution (denitrfying agent), by monitoring in real time both
The waste of depickling solution can be reduced, and can makes final flue gas reach discharging standards.The rear end of deacidifying device 15 is provided with and supplies cigarette
The chimney 16 of gas discharge, handle the flue gas of completion directly can be emitted into outdoor by chimney 16.
Such as Fig. 2, in a second embodiment, smoke exhaust pipe 6 is inverted U shape inflection, and its bottom end is directly connected in air-introduced machine 11,
In the present embodiment, air-introduced machine 11 is high pressure centrifugal blower fan, is that combustion furnace 3 provides negative pressure by high pressure centrifugal blower fan.Draw
The rear end of blower fan 11 is connected to bag-type dust collector 12, can remove dust and deleterious particle in flue gas.After bag-type dust collector 12
End is connected to absorbent charcoal adsorber 13, will can not avoid generating bioxin in fume treatment by absorbent charcoal adsorber 13
Absorption intercepts so that the dioxin in flue gas index finally discharged meets national standard discharge standard.After absorbent charcoal adsorber 13
End is connected to deacidifying device 15, and deacidifying device 15 can remove the acidic materials in flue gas, usually spray denitrfying agent and carry out
Depickling.One or more acidity monitoring points 14 are provided between deacidifying device 15 and absorbent charcoal adsorber 13, can monitor in real time into
Enter the concentration of the flue gas middle acid substance before deacidifying device 15, and by feedback of the information to deacidifying device 15, the basis of deacidifying device 15
The concentration value automatic decision of monitoring simultaneously adjusts the amount of sprinkling depickling solution (denitrfying agent), and by monitoring in real time, can to reduce depickling molten
The waste of liquid, and can make final flue gas reach discharging standards.The rear end of deacidifying device 15 is provided with the chimney for flue gas discharge
16, handle the flue gas of completion directly can be emitted into outdoor by chimney 16.
The present invention by combustion furnace 3, mucking machine 4, go out inder pot 5, air-introduced machine 11, bag-type dust collector 12, charcoal absorption fill
Put 13, deacidifying device 15 and out of stock control station 17 may be contained within process chamber 19, in the present embodiment, process chamber 19 is to close
Room, rubbish storeroom 1 is arranged at outside process chamber 19, is not in the mood for spiral conveyor 2 and is entered in process chamber 19 and be connected to burning
Stove 3.Smoke exhaust pipe 6 stretches out from the roof of process chamber 19, is inverted U shape inflection, is entered back into after exchanging heat twice in process chamber 19.Cigarette
Chimney 16 is connected to deacidifying device 15, and is stretched out by the side wall of process chamber 19, and the side wall of process chamber 19 is additionally provided with slag releasing channel 18, supplies
The inder pot 5 that goes out filled transports.Said apparatus or equipment are integrated in process chamber 19 by the present invention, take up an area small, system concentration, and
Integrity degree is high, multiple functional, is advantageous to garbage disposal.Foul smell decomposes after the high-temp combustion of combustion furnace 3, and air-introduced machine 11 can also be right
Negative pressure is caused inside process chamber 19, ensures that stink will not be excessive, so as to effectively control foul smell.
Method or process of the present invention based on above-mentioned garbage flue gas processing system processing rubbish are：Conveying device opens first
It is dynamic, it is not in the mood for spiral conveyor 2 and the pending rubbish in rubbish storeroom 1 is delivered in combustion furnace 3, rubbish is in combustion furnace 3
High-temp combustion, during burning in combustion furnace in a combustion room by quadruple effect denitration liquid is sprayed into remove the sulphur-containing substance in combustion product gases, lead to
Denitration control station 17 is crossed to monitor automatically and control the straying quatity of quadruple effect denitration liquid.Caused burning slag is by the row of mucking machine 4 after burning
Go out, and storage supplies subsequent treatment to recovery in inder pot 5 is gone out, caused combustion product gases enter smoke exhaust pipe 6, and are changed successively with the first order
Hot device 7 and second level heat exchanger 8 exchange heat, and flue-gas temperature falls abruptly to less than 200 DEG C after exchanging heat twice so that bioxin does not reach
The condition of synthesis, so as to greatly reduce the generation of bioxin.Flue gas after heat exchange, which enters to remove in bag-type dust collector 12, to be had
Evil particle, it can not avoid generating bioxin in fume treatment subsequently into removing in absorbent charcoal adsorber 13 so that final
The dioxin in flue gas index of discharge meets national standard discharge standard, finally enters and acidic materials are removed in deacidifying device 15, processing
The flue gas of completion is emitted into outdoor by chimney 16.During flue gas is discharged, flue gas is extracted by air-introduced machine 11, makes its outside
Discharge, while make to form subnormal ambient in combustion furnace 3
The above embodiments are merely illustrative of the technical solutions of the present invention and it is unrestricted, although with reference to preferred embodiment to this hair
It is bright to be described in detail, it will be appreciated by those skilled in the art that technical scheme can be modified or waited
With replacing, without departing from the objective and scope of the technical program, it all should cover in scope of the presently claimed invention.
Claims (10)
- A kind of 1. garbage flue gas processing system, it is characterised in that including：Combustion furnace, for for incineration firing, the combustion furnace Side is connected to rubbish storeroom by conveying device, and the opposite side of the combustion furnace is connected to deslagging device, the combustion furnace Top be provided with for combustion product gases discharge smoke exhaust pipe, the smoke exhaust pipe be sequentially connected to first order heat exchanger and the second level heat exchange Device, flue gas are less than 200 DEG C after being exchanged heat in the first order heat exchanger and the second level heat exchanger, the end of the smoke exhaust pipe Bag-type dust collector provided with removable flue gas endoparticle, the rear end of the bag-type dust collector are connected to adsorbable bioxin Absorbent charcoal adsorber, the rear end of the absorbent charcoal adsorber are connected to the deacidifying device of removable flue gas middle acid substance, The rear end of the deacidifying device is provided with the chimney for flue gas discharge.
- 2. garbage flue gas processing system according to claim 1, it is characterised in that：The conveying device is not to be in the mood for spiral transferring Band is sent, rubbish is by the bottom be not in the mood for spiral conveyor and be automatically sent to the combustion furnace.
- 3. garbage flue gas processing system according to claim 1, it is characterised in that：The deslagging device includes being connected to institute State the mucking machine of side at the top of combustion furnace, and be connected to the inder pot that goes out of the mucking machine, the burning slag in the combustion furnace by Mucking machine discharge, and be stored in it is described go out inder pot in reclaim.
- 4. garbage flue gas processing system according to claim 1, it is characterised in that：The flue gas temperature of the smoke exhaust pipe porch Spend for 850 DEG C~1000 DEG C, the flue-gas temperature after first order heat exchanger heat exchange is less than 600 DEG C, is changed through the second level Flue-gas temperature after hot device heat exchange is less than 200 DEG C.
- 5. garbage flue gas processing system according to claim 1, it is characterised in that：The first order heat exchanger or described The side of secondary heat exchanger is provided with cooling tower, and the water tank of the cooling tower is connected to the first order heat exchanger and institute by water pipe Second level heat exchanger is stated, the water pipe side is provided with water pump, by the water pump to the first order heat exchanger and described second Cooling water is pumped into level heat exchanger.
- 6. garbage flue gas processing system according to claim 5, it is characterised in that：Water temperature detection is provided with the water tank Point, the temperature of cooling water in the water tank is monitored in real time.
- 7. garbage flue gas processing system according to claim 1, it is characterised in that：Also include air-introduced machine, the air-introduced machine It is arranged between the absorbent charcoal adsorber and the deacidifying device, or is arranged at the smoke evacuation pipe end and the cloth bag It is to provide negative pressure in the combustion furnace by the air-introduced machine between dust arrester.
- 8. garbage flue gas processing system according to claim 7, it is characterised in that：The deacidifying device and the air-introduced machine Or acidity monitoring point is provided between the absorbent charcoal adsorber, acid in monitoring in real time into flue gas before the deacidifying device The concentration of matter, and by feedback of the information to the deacidifying device, it is molten that the deacidifying device according to concentration value automatically adjusts sprinkling depickling The amount of liquid.
- 9. garbage flue gas processing system according to claim 1, it is characterised in that：The side of the combustion furnace, which is provided with, to be used for Quadruple effect denitration liquid is sprayed to remove the spray equipment of nitrogen and sulfide in flue gas, the spray equipment is connected to out of stock control Stand, the quadruple effect denitration liquid that the spray equipment sprays into the combustion furnace is monitored and control automatically by the denitration control station Amount.
- A kind of 10. method of the garbage flue gas processing system processing rubbish based on described in claim 1, it is characterised in that including： The conveying device starts, and rubbish is delivered to the combustion furnace by the rubbish storeroom by the conveying device, in the combustion Burn in stove and burn, quadruple effect denitration liquid is sprayed into the combustion furnace to remove the sulphur-containing substance in combustion product gases, burning slag is by described Deslagging device is discharged, and combustion product gases enter the smoke exhaust pipe, and are exchanged heat successively with first order heat exchanger and second level heat exchanger, and two Flue-gas temperature is less than 200 DEG C after secondary heat exchange, and the flue gas after heat exchange removes particle by the bag-type dust collector, subsequently into institute State and bioxin is removed in absorbent charcoal adsorber, finally enter and acidic materials are removed in the deacidifying device, handle the cigarette of completion Gas is by the smoke stack emission to outdoor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710996896.7A CN107575876A (en) | 2017-10-20 | 2017-10-20 | A kind of garbage flue gas processing system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710996896.7A CN107575876A (en) | 2017-10-20 | 2017-10-20 | A kind of garbage flue gas processing system and method |
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| CN107575876A true CN107575876A (en) | 2018-01-12 |
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| CN101153712A (en) * | 2006-09-29 | 2008-04-02 | 刘立竹 | Medical destructor system |
| CN103657343A (en) * | 2012-09-03 | 2014-03-26 | 中国中化股份有限公司 | Method and device for inhibiting generation of dioxin from incineration flue gas |
| CN104595909A (en) * | 2015-01-29 | 2015-05-06 | 威海鲁源科技环保设备有限公司 | Medical waste incineration and purification device |
| CN107191941A (en) * | 2017-05-27 | 2017-09-22 | 航天凯天环保科技股份有限公司 | It is a kind of to reduce the technique for burning domestic garbage and system of incineration flue gas pollutant |
| CN207569882U (en) * | 2017-10-20 | 2018-07-03 | 珠海市云筒环保科技有限公司 | A kind of garbage flue gas processing system |
-
2017
- 2017-10-20 CN CN201710996896.7A patent/CN107575876A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101153712A (en) * | 2006-09-29 | 2008-04-02 | 刘立竹 | Medical destructor system |
| CN103657343A (en) * | 2012-09-03 | 2014-03-26 | 中国中化股份有限公司 | Method and device for inhibiting generation of dioxin from incineration flue gas |
| CN104595909A (en) * | 2015-01-29 | 2015-05-06 | 威海鲁源科技环保设备有限公司 | Medical waste incineration and purification device |
| CN107191941A (en) * | 2017-05-27 | 2017-09-22 | 航天凯天环保科技股份有限公司 | It is a kind of to reduce the technique for burning domestic garbage and system of incineration flue gas pollutant |
| CN207569882U (en) * | 2017-10-20 | 2018-07-03 | 珠海市云筒环保科技有限公司 | A kind of garbage flue gas processing system |
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Effective date of registration: 20190130 Address after: 519000 202D, No. 51 First Ring Road, Guishan Town, Zhuhai City, Guangdong Province Applicant after: Zhuhai Ebins Technology Co., Ltd. Address before: 519000 First Floor of Building No. 16 Henghui Road, Sanzao Town, Jinwan District, Zhuhai City, Guangdong Province Applicant before: ZHUHAI YUNTONG ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. |