CN206553459U - A kind of domestic garbage pyrolysis processing system - Google Patents
A kind of domestic garbage pyrolysis processing system Download PDFInfo
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- CN206553459U CN206553459U CN201720134547.XU CN201720134547U CN206553459U CN 206553459 U CN206553459 U CN 206553459U CN 201720134547 U CN201720134547 U CN 201720134547U CN 206553459 U CN206553459 U CN 206553459U
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 80
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 79
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 43
- 239000003546 flue gas Substances 0.000 claims abstract description 43
- 239000000428 dust Substances 0.000 claims abstract description 25
- 238000002309 gasification Methods 0.000 claims abstract description 23
- 239000007789 gas Substances 0.000 claims abstract description 20
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 239000003517 fume Substances 0.000 claims abstract description 11
- 239000000779 smoke Substances 0.000 claims description 25
- 230000009977 dual effect Effects 0.000 claims description 23
- 238000010304 firing Methods 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 11
- 239000007921 spray Substances 0.000 claims description 11
- 235000019504 cigarettes Nutrition 0.000 claims description 8
- 239000002699 waste material Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 230000004087 circulation Effects 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 4
- 239000005864 Sulphur Substances 0.000 claims description 4
- 238000005235 decoking Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 239000002351 wastewater Substances 0.000 claims description 4
- 239000006199 nebulizer Substances 0.000 claims description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 239000003344 environmental pollutant Substances 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 abstract description 4
- 231100000719 pollutant Toxicity 0.000 abstract description 4
- 238000009825 accumulation Methods 0.000 abstract description 3
- 238000005979 thermal decomposition reaction Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 5
- 239000000571 coke Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model is related to a kind of domestic garbage pyrolysis processing system；By setting moisture film processing system to be used as one-level fume treatment, realize and the flue gas after pyrolysis is subjected to watering cooling, make tar liquefaction accumulation, while making dust one-level sulfide etc. soluble in water；Simultaneously, using whirlwind processing system as two grades of tar separators, flue gas water removal and further chalk dust removing and tar are realized, and then complete the removal of the impurity in flue gas, flue gas harmless treatment is realized, the problem of solving pollutant removal in pyrolysis gas or flue gas；Simultaneously as the cooling effect of the moisture film processing system, the pyrolysis gasification system can not only realize low temperature pyrogenation, moreover it is possible to compatible high temperature, high-efficiency thermal decomposition operation.
Description
Technical field
The utility model belongs to environment-friendly garbage processing technology field, and in particular to a kind of domestic garbage pyrolysis processing system.
Background technology
Technology of garbage disposal includes pyrolysis and incinerated.Present most of garbage disposals are to use high temperature incinerator, by stove
Temperature is heated to 850 DEG C and incinerated, and energy expenditure is big, and easily produces many harmful substances in incineration course, especially
It is hypertoxic carcinogenic contaminant dioxin.
Pyrolysis（Pyrolysis）Also known as destructive distillation, thermal decomposition or charing, refers to that organic matter adds in the state of anaerobic or anoxic
Heat, is allowed to the process decomposed.I.e. pyrolysis is the thermal instability using organic matter, under conditions of anaerobic or anoxic, utilizes heat
Can be broken the chemical combination key of compound, by the organic matter of macromolecule be converted into the fuel gas of small-molecular-weight, liquid fuel and
The process of coke.
After the completion of house refuse is pyrolyzed in pyrolysis oven, the coke of solid-state is stayed in stove, fuel gas, moisture and liquid
Fuel etc. is discharged in the form of flue gas, also needs further separating treatment, can be only achieved the purpose for not polluting air.Such as existing skill
In art, Patent No. CN105903749A patent of invention proposes a kind of system of domestic rubbish disposal, including material storage container, oil removal
Pond, revolving bed pyrolysis oven, indirect condenser, oily-water seperating equipment, the invention also propose a kind of method, including step：Will life
Combustible in rubbish, which is sent into, carries out anoxybiotic pyrolysis in the revolving bed pyrolysis oven；By the pyrogenous origin pyrolysis gas-liquid mixture of institute
The indirect condenser is sent into, condensed pyrolytic behavior is sent into the oily-water seperating equipment.
Prior art, the problem of failing to solve pollutant removal of impurities in pyrolysis gas or flue gas, its fume emission to air
In, it still can produce certain environmental pollution.
Existing pyrolysis system, can only clothes made of brocade low temperature or high temperature pyrolysis, in the prior art, without high/low temperature integrate be pyrolyzed
System is provided.
The content of the invention
The utility model aims to provide a kind of domestic garbage pyrolysis processing system, to solve asking for existing pyrolysis gas pollution
Topic.
Concrete scheme is as follows：Domestic garbage pyrolysis processing system, including pipeline is connected successively pyrolysis gasification system, cigarette
Gas processing system and exhaust system, the pyrolysis gasification system are used for domestic garbage pyrolysis to produce flue gas, and the flue gas is successively
By being emitted into air after the smoke processing system and exhaust system；It is characterized in that：The smoke processing system includes phase
The one-level of mutual pipeline connection, two grades of tar separators；The one-level tar separator is moisture film processing system, the moisture film processing system
It is connected with the pyrolysis gasification system pipeline to realize that the pyrolysis gasification system is connected with smoke processing system pipeline, and to the flue gas
Carry out cooling and sulphur removal and chalk dust removing and decoking oil processing；Two grades of tar separators are whirlwind processing system, to the moisture film
The flue gas that processing system is discharged is removed water, chalk dust removing and decoking oil processing；The whirlwind processing system pipeline is conducted to discharge
System is to realize that smoke processing system is connected with exhaust system pipeline.
Further, in addition to burnt water separating system, the burnt water separating system includes a burnt water inlet and a separation water
Outlet；The burnt water inlet is connected with the smoke processing system and exhaust system pipeline respectively, to receive the smoke processing system
And the waste liquid produced by exhaust system；If being provided with dry nebulizer in the moisture film processing system, the separation water out is connected with one
Water pump, and each atomizer is connected to by the pump tube；The burnt water separating system separates water in waste liquid, and to moisture film
Processing system supplies water, and then realizes the water circulation use of the moisture film processing system.
Further, the burnt water separating system includes no less than two burnt water separating barrels of pipeline connection successively；Phase pipeline
In two burnt water separating barrels of connection, waste water filtering produced by one of Jiao's water separating barrel is to another burnt water separating barrel
To carry out separating treatment again, and then realize multistage Jiao Shui separation.
Further, the exhaust system includes whirlwind processor, electric cleaner and the chimney of pipeline connection successively；The rotation
Wind processor is connected with the whirlwind processing system pipeline, is connected with realizing smoke processing system with exhaust system pipeline.
Further, the electric cleaner is to be additionally provided with sack cleaner on high pressure plasma fume cleaning device, the chimney.
Further, the pyrolysis gasification system includes being pyrolyzed main stove and dual firing chamber, and the top of the main stove of the pyrolysis is provided with cigarette
Gas is exported；The dual firing chamber one end is connected with exhanst gas outlet pipeline, and the other end is connected with the moisture film processing system pipeline, to realize
Pyrolysis gasification system is connected with smoke processing system pipeline；The dual firing chamber, which connects, is additionally provided with spray on the pipeline of the moisture film processing system
Mouth is drenched, for the flue gas spray cooling discharged by the dual firing chamber.
Further, the pyrolysis gasification system also includes hydraulic pressure feeder and bucket elevator；The main stove of the pyrolysis it is upper
Portion is provided with a material inlet, and the hydraulic pressure feeder is at the material inlet；The bucket elevator one end is located at ground, the other end
Above the dog-house of the hydraulic pressure feeder, ground house refuse is promoted to the hydraulic pressure feeder, and pass through the hydraulic pressure
Feeder is added in the main stove of the pyrolysis.
The utility model realizes by setting moisture film processing system to be used as one-level fume treatment and enters the flue gas after pyrolysis
Row watering cooling, makes tar liquefaction accumulation, while making dust one-level sulfide etc. soluble in water；Meanwhile, by whirlwind processing system
As two grades of tar separators, flue gas water removal and further chalk dust removing and tar are realized, and then complete in flue gas
Impurity remove, realize flue gas harmless treatment, the problem of solving pollutant removal in pyrolysis gas or flue gas；Meanwhile, by
In the cooling effect of the moisture film processing system, the pyrolysis gasification system can not only realize low temperature pyrogenation, moreover it is possible to compatible high temperature, efficiently
Operation is pyrolyzed, high/low temperature is additionally provided and integrates pyrolysis system.
Brief description of the drawings
Fig. 1 shows the utility model domestic garbage pyrolysis processing system side view；
Fig. 2 shows Fig. 1 top views.
Embodiment
To further illustrate each embodiment, the utility model is provided with accompanying drawing.These accompanying drawings are in the utility model is disclosed
A part for appearance, it is mainly to illustrate embodiment, and running of the associated description of specification to explain embodiment can be coordinated former
Reason.Coordinate and refer to these contents, those of ordinary skill in the art will be understood that other possible embodiments and this practicality are new
The advantage of type.Component in figure is not necessarily to scale, and similar element numbers are conventionally used to indicate similar component.
The utility model is further illustrated in conjunction with the drawings and specific embodiments.
With reference to shown in Fig. 1 and Fig. 2, the domestic garbage pyrolysis processing system of the embodiment, including：Pyrolysis gasification system 1, cigarette
Gas processing system 2, exhaust system 3 and burnt water separating system 4, the pyrolysis gasification system 1, smoke processing system 2, exhaust system
3 and burnt water separating system 4 be sequentially connected by pipeline and connect conducting, to form a fume treatment half-duplex channel, the pyrolytic gasification
System 1 is used to contain house refuse and by domestic garbage pyrolysis to produce flue gas and coke, and coke is solid-state, is stayed in the pyrolysis
In gasification system 1, the flue gas passes sequentially through the smoke processing system 2 and exhaust system 3, to be emitted into air after processing.
The pyrolysis gasification system 1 includes：Bucket elevator 13, hydraulic pressure feeder 12, the main stove 10 of pyrolysis and dual firing chamber
11；The side wall wall on the top of the main stove 10 of the pyrolysis is provided with a material inlet（Not shown in figure）, the hydraulic pressure feeder 12 pacifies
Loaded on a base station to be arranged at the material inlet of the main stove 10 of the pyrolysis；The bucket elevator 13 is tilted obliquely by ground
Set, its one end is on ground, and the other end is located at the top of the dog-house 120 of the hydraulic pressure feeder 12, by hopper by ground
Face is promoted to the top of dog-house 120 and overturn, ground house refuse（Not shown in figure）It is promoted in the hydraulic pressure feeder 12,
And added by the hydraulic pressure feeder 12 in the main stove 10 of the pyrolysis.
Exhanst gas outlet and venting are offered successively on the main top wall of stove 10 of the pyrolysis, and the venting is let out provided with one
Explosion-protection equipment is pressed, the exhanst gas outlet is conducted to cigarette by the air inlet end of pipeline connection to dual firing chamber 11 by the dual firing chamber 11
Gas processing system 2.
The one end of dual firing chamber 11 is connected with being pyrolyzed the exhanst gas outlet pipeline of main stove 10, and the other end is managed with smoke processing system 2
Road is connected, and then is realized pyrolysis gasification system 1 and be connected with the pipeline of smoke processing system 2；And the dual firing chamber 11 connects the cigarette
Spray nozzle 43 is additionally provided with the pipeline of gas processing system 2, the spray nozzle 43 is used for spraying cold water, with by the dual firing chamber 11 row
The flue gas gone out is cooled.
The smoke processing system 2 includes the one-level tar separator and two grades of tar separators that mutual pipeline is connected；
In the embodiment, the one-level tar separator is moisture film processing system, specifically, the moisture film processing system is two water film dedustings
Two atomizers 210 are equipped with device 21, each water dust scrubber 21, and each water dust scrubber 21 is respectively provided with one and enters cigarette
Mouth and an outlet flue, the smoke inlet of each water dust scrubber 21 are connected with the flue gas outlet side pipeline of the dual firing chamber 11,
And then cooling processing is carried out to the flue gas that the dual firing chamber 11 discharges, meanwhile, the sulfide in flue gas is dissolved in water, tar cooling liquid
Change and dust precipitation, so that the dust from gas discharged from flue is extremely limited.
Two grades of tar separators are whirlwind processing system, specifically, in this embodiment, the whirlwind processing system is Jiao
Oily cyclone separator 22, the air inlet end pipeline of the tar cyclone separator 22 is conducted to the outlet flue of water dust scrubber 21, makes this
The flue gas that water dust scrubber 21 is discharged enters the tar cyclone separator 22, it is removed water, chalk dust removing and tar separation are gone
Except processing；The pipeline of tar cyclone separator 22 is conducted to exhaust system 3 to realize that smoke processing system 2 is managed with exhaust system 3
Road is connected.
The exhaust system 3 includes a whirlwind processor 31, two electric cleaners 32 and chimney 33；The whirlwind processor 31
Air inlet end pipeline be connected to the outlet side of tar cyclone separator 22, and the outlet side of the whirlwind processor 31 passes through two electricity
Deduster 32 is conducted to the chimney 33, is connected with realizing smoke processing system 2 with the pipeline of exhaust system 3.In this embodiment,
The electric cleaner 32 is high pressure plasma fume cleaning device, and the chimney top openend is also arranged with a sack cleaner 330.For
Thorough removal harmful metal elements and dust, the exhaust system 3 can also set an absorbent charcoal adsorber again, it is sufficient to full
The relevant regulation of the most stringent of dust emissions of foot.The absorbent charcoal adsorber can be in chimney 33.
The burnt water separating system 4 includes four burnt water separating barrels 40 of pipeline connection successively；Two Jiao of phase pipeline connection
In water separating barrel 40, waste water filtering produced by the discharge outlet of one of Jiao's water separating barrel 40 is to another burnt water separating barrel
40 entrance, to carry out separating treatment again, and then realizes multistage Jiao Shui separation；From Figure 2 it can be seen that the burnt water collection pipe A
One end is communicated to the entrance of the first order burnt water separating barrel 40, and then makes the entrance of the first order burnt water separating barrel 40 as Jiao
The burnt water inlet of water separating system 4, meanwhile, the burnt water collection pipe A passes through branch pipe pipeline connection to whirlwind processor 31, Jiao respectively
The waste liquid outlet of oily cyclone separator 22 and water dust scrubber 21, to realize the collection to waste liquid；The afterbody, i.e.,
The discharge outlet of level Four Jiao water separating barrel 40 as the burnt water separating system 4 separation water out；The burnt water inlet respectively with the cigarette
Gas processing system 2 and the connection of the pipeline of exhaust system 3, to receive the smoke processing system 2 and useless produced by exhaust system 3
Liquid, wherein, based on the waste liquid produced with water dust scrubber 21；The separation water out is connected with a water pump 42, and passes through the water pump
42 pipelines are connected to each atomizer 210 and spray nozzle 43；The burnt water separating system 4 separates water in waste liquid, and to moisture film
Processing system supplies water, and then realizes the water circulation use of the moisture film processing system.
The utility model realizes by setting moisture film processing system to be used as one-level fume treatment and enters the flue gas after pyrolysis
Row watering cooling, makes tar liquefaction accumulation, while making dust one-level sulfide etc. soluble in water；Meanwhile, by whirlwind processing system
As two grades of tar separators, flue gas water removal and further chalk dust removing and tar are realized, and then complete in flue gas
Impurity remove, realize flue gas harmless treatment, the problem of solving pollutant removal in pyrolysis gas or flue gas；Meanwhile, by
In the cooling effect of the moisture film processing system, the pyrolysis gasification system can not only realize low temperature pyrogenation, moreover it is possible to compatible high temperature, efficiently
Operation is pyrolyzed, high/low temperature is additionally provided and integrates pyrolysis system.
The domestic garbage pyrolysis processing system of the embodiment, Low Temperature Pyrolysis Process is as follows：
S1：House refuse is added and is pyrolyzed main stove, enters by natural magnezization air and is pyrolyzed in main stove to the house refuse
It is pyrolyzed；Main in-furnace temperature is pyrolyzed in the range of 300 DEG C to 350 DEG C：
During refuse pyrolysis low temperature, close heat and support blower fan, enter by natural magnezization air and be pyrolyzed in pyrolysis oven, stove
Interior temperature 300-350 degree；
S2:The flue gas produced by being pyrolyzed main stove is heated by dual firing chamber；In the step, spray nozzle, which is in, to close
Closed state, burning combustible gas, powder ash, Jiao are handled through dual firing chamber's electrical heating；
S3：Flue gas is passed sequentially through one-level tar separator, two grades of tar separators and exhaust system, discharged after processing
To air：
Flue gas spraying cooling, sulphur removal, chalk dust removing, decoking oil processing are carried out into one-level tar separator, Jiao is subsequently entered
In oily cyclone separator, turned back by the flue gas in three roads, separation dust, tar processing carry out oil subsequently into whirlwind processor
Water is separated, and can be most expelled directly out after high pressure plasma fume cleaning afterwards.The embodiment can be by so waste water, tar be received together
Collect in the burnt water separating barrels of four circulations, row filtration cycle is used, the, which resupplies one-level tar separator, is sprayed, it is long-term oneself
Dynamic circulation.
The domestic garbage pyrolysis processing system of the embodiment, high temperature pyrolysis process is as follows：
S1：House refuse is added and is pyrolyzed main stove, hot wind supply enters to be pyrolyzed in main stove to be pyrolyzed to the house refuse, should
Main in-furnace temperature is pyrolyzed in step in the range of 700 DEG C to 900 DEG C：
During refuse pyrolysis high temperature, blower fan can be supported to open heat, provide rubbish in stove hot blast pyrolysis, blower variable frequency can
Regulating air volume, makes the temperature in furnace reach 700-900 degree；
S2:Flue gas of the dual firing chamber produced by being pyrolyzed main stove is electrically heated processing, and dual firing chamber's temperature is located at 900 DEG C extremely
In the range of 1000 DEG C；Meanwhile, open spray nozzle and cold water is sprayed to flue gas, the flue gas cool-down that dual firing chamber is discharged is to not higher than
300℃：
Held through dual firing chamber after burning and hot oxygen supply, dual firing chamber's temperature can control in 900-1000 degree and heat burning
Fuel gas, powder ash, tar, spray cold true processing by spray nozzle, flue-gas temperature are dropped into less than 300 degree；
S3：Flue gas is passed sequentially through one-level tar separator, two grades of tar separators and exhaust system, be then emitted into
Air：
Atomization is carried out by one-level tar separator and drops to less than 50 degree, to reach cooling, sulphur removal, chalk dust removing, tar removing
Effect；Subsequently enter in the second tar cyclone separator, turned back by the flue gas in three roads, separation dust, tar processing；Into
Whirlwind processor carries out water-oil separating, is handled through high pressure plasma fume cleaning, eventually passes sack cleaner discharge up to standard.
Although specifically showing and describing the utility model with reference to preferred embodiment, those skilled in the art should
This is understood, is not departing from the spirit and scope of the present utility model that appended claims are limited, in form and details
On the utility model can be made a variety of changes, be protection domain of the present utility model.
Claims (7)
1. domestic garbage pyrolysis processing system, including pipeline is connected successively pyrolysis gasification system, smoke processing system and
Exhaust system, the pyrolysis gasification system is used for domestic garbage pyrolysis to produce flue gas, and the flue gas passes sequentially through the fume treatment
To be emitted into air after system and exhaust system；It is characterized in that：The smoke processing system includes one that mutual pipeline is connected
Level, two grades of tar separators；
The one-level tar separator is moisture film processing system, and the moisture film processing system is connected with reality with the pyrolysis gasification system pipeline
Now the pyrolysis gasification system is connected with smoke processing system pipeline, and the flue gas is cooled and sulphur removal and chalk dust removing and removed
Tar processing；
Two grades of tar separators are whirlwind processing system, the flue gas that the moisture film processing system is discharged are removed water, gumming
Dirt and decoking oil processing；
The whirlwind processing system pipeline is conducted to exhaust system to realize that smoke processing system is connected with exhaust system pipeline.
2. domestic garbage pyrolysis processing system according to claim 1, it is characterised in that：Also include burnt water separating system,
The burnt water separating system includes a burnt water inlet and a separation water out；
The burnt water inlet is connected with the smoke processing system and exhaust system pipeline respectively, with receive the smoke processing system with
And the waste liquid produced by exhaust system；
If being provided with dry nebulizer in the moisture film processing system, the separation water out is connected with a water pump, and passes through the pump tube
It is connected to each atomizer；
The burnt water separating system separates water in waste liquid, and moisture film processing system is supplied water, and then realizes the moisture film processing system
The water circulation use of system.
3. domestic garbage pyrolysis processing system according to claim 2, it is characterised in that：The burnt water separating system include according to
No less than two burnt water separating barrels of secondary pipeline connection；In two burnt water separating barrels of phase pipeline connection, one of Jiao's moisture
From the waste water filtering produced by bucket to another burnt water separating barrel to carry out separating treatment again, and then realize multistage burnt moisture
From.
4. domestic garbage pyrolysis processing system according to claim 1, it is characterised in that：The exhaust system includes managing successively
Whirlwind processor, electric cleaner and the chimney of road connection；The whirlwind processor is connected with the whirlwind processing system pipeline, with reality
Show smoke processing system to be connected with exhaust system pipeline.
5. domestic garbage pyrolysis processing system according to claim 4, it is characterised in that：The electric cleaner be high pressure etc. from
Sack cleaner is additionally provided with sub- fume cleaning device, the chimney.
6. according to any described domestic garbage pyrolysis processing systems of claim 1-5, it is characterised in that：The pyrolysis gasification system
Including being pyrolyzed main stove and dual firing chamber, the top of the main stove of the pyrolysis is provided with exhanst gas outlet；
The dual firing chamber one end is connected with exhanst gas outlet pipeline, and the other end is connected with the moisture film processing system pipeline, to realize heat
Solution gasification system is connected with smoke processing system pipeline；
The dual firing chamber connects and is additionally provided with spray nozzle on the pipeline of the moisture film processing system, for the cigarette discharged by the dual firing chamber
Gas spray cooling.
7. domestic garbage pyrolysis processing system according to claim 6, it is characterised in that：The pyrolysis gasification system also includes
Hydraulic pressure feeder and bucket elevator；
The top of the main stove of the pyrolysis is provided with a material inlet, and the hydraulic pressure feeder is at the material inlet；The bucket elevator
One end is located at ground, and ground house refuse is promoted to the hydraulic pressure by the other end above the dog-house of the hydraulic pressure feeder
Feeder, and added by the hydraulic pressure feeder in the main stove of the pyrolysis.
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| CN201720134547.XU CN206553459U (en) | 2017-02-15 | 2017-02-15 | A kind of domestic garbage pyrolysis processing system |
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| CN201720134547.XU CN206553459U (en) | 2017-02-15 | 2017-02-15 | A kind of domestic garbage pyrolysis processing system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106753474A (en) * | 2017-02-15 | 2017-05-31 | 吴晓龙 | A kind of domestic garbage pyrolysis processing system and low temperature, high temperature pyrolysis processing method |
| CN109297024A (en) * | 2018-09-30 | 2019-02-01 | 云南天朗环境科技有限公司 | A kind of volume reduction, innoxious residents in rural community pyrolytic incineration purification system and technique |
-
2017
- 2017-02-15 CN CN201720134547.XU patent/CN206553459U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106753474A (en) * | 2017-02-15 | 2017-05-31 | 吴晓龙 | A kind of domestic garbage pyrolysis processing system and low temperature, high temperature pyrolysis processing method |
| CN109297024A (en) * | 2018-09-30 | 2019-02-01 | 云南天朗环境科技有限公司 | A kind of volume reduction, innoxious residents in rural community pyrolytic incineration purification system and technique |
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Effective date of registration: 20180810 Address after: 362000 No. 222, Gao Li lane, Changcun street, Changtai street, Licheng District, Quanzhou, Fujian Patentee after: Fujian Huixin Environmental Protection Technology Co. Ltd. Address before: 362000 Quanzhou 3003, room 5, 5 yuan, 2 Yuan Yuan Road, Feng Ze District, Fujian. Patentee before: Wu Xiaolong |