CN206935034U - A kind of refuse pyrolysis smoke eliminator - Google Patents
A kind of refuse pyrolysis smoke eliminator Download PDFInfo
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- CN206935034U CN206935034U CN201720481453.XU CN201720481453U CN206935034U CN 206935034 U CN206935034 U CN 206935034U CN 201720481453 U CN201720481453 U CN 201720481453U CN 206935034 U CN206935034 U CN 206935034U
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Abstract
The utility model discloses a kind of refuse pyrolysis smoke eliminator.Including be sequentially connected dust arrester, in desulfurization and device, liquid-gas separation device, high-precision purifier, centrifugal blower；Air inlet pipe is connected with dust arrester, centrifugal blower is connected with blast pipe；Dust arrester includes inner casing, shell, cooling water pipe is provided between inner casing and shell, cooling water pipe is spirally wrapped around inner casing outer surface；In dust arrester first baffle, second baffle are provided with by left-to-right, the inside of dust arrester is divided into first passage, second channel, third channel by first baffle and second baffle, first passage is connected with air inlet pipe, third channel is connected with escape pipe, second channel upper end is connected with first passage upper end, second channel is connected with third channel lower end, second channel and third channel lower end dress water, the second baffle lower end insertion water surface.The utility model can cool down to flue gas, avoid high-temperature flue gas from impacting the service life of equipment.
Description
Technical field
It the utility model is related to smoke eliminator, and in particular to a kind of refuse pyrolysis smoke eliminator.
Background technology
Rubbish produces substantial amounts of flue gas after burning, and substantial amounts of dust, noxious material are contained in its flue gas, it is therefore desirable to
Flue gas is purified, and flue-gas temperature caused by burning is higher, if using water bath dust collector, also water temperature can be made to continue to rise
Height, influence service life.
Utility model content
The purpose of this utility model is to provide a kind of refuse pyrolysis smoke eliminator solve existing for rubbish heat
Solution smoke eliminator fail to cool to flue gas, cause high-temperature flue gas influence device service life the problem of.
To solve above-mentioned technical problem, the utility model uses following technical scheme：A kind of refuse pyrolysis gas cleaning
Device；Including be sequentially connected dust arrester, in desulfurization and device, liquid-gas separation device, high-precision purifier, centrifugation wind
Machine；Air inlet pipe is connected with described dust arrester, described centrifugal blower is connected with blast pipe；Described dust arrester includes
Inner casing, shell, are provided with cooling water pipe between inner casing and shell, cooling water pipe is spirally wrapped around inner casing outer surface；It is described
Dust arrester in by left-to-right be provided with first baffle, second baffle, first baffle and second baffle are by dust arrester
Part is first passage, second channel, third channel, and first passage is connected with air inlet pipe, and third channel is connected with escape pipe, the
One baffle plate upper opening, second baffle lower opening, second channel upper end are connected with first passage upper end, second channel and the 3rd
Passage lower end connects, second channel and third channel lower end dress water, the second baffle lower end insertion water surface.
Flue gas is introduced into dust arrester by air inlet pipe, the solids in flue gas is passed through spray by the way of water bath dust-removing
Water drenching settles down, then by desulfurization and device, carrying out removing reaction of Salmon-Saxl；Pass through liquid-gas separation device again, remove in gas
Vapor and liquid impurity；Pass through high-precision purifier again, high-precision purifier contains circulating condensing, high voltage electric field, born
The processes such as electronics, ozone, charcoal absorption, finally discharged by centrifugal blower from blast pipe, wherein in desulfurization and device, liquid gas
Separator, high-precision purifier are prior art, inventive point not of the present utility model.In dust arrester, cooling
Water pipe cools down to flue gas, and flue gas passes sequentially through first passage, second channel, increase heat flue gas in dust arrester when
Between so that the effect that cooling water pipe cools down to flue gas is more preferable, and flue gas is discharged after water bath dust-removing by third channel through escape pipe.
Preferably, described dust arrester lower end is provided with sewage draining exit.The dirt of dust can will be absorbed every a period of time
Water is discharged.
Preferably, described cooling water pipe from top to bottom be wrapped in inner casing outer surface, be separately provided with water pump, water pump one
The delivery port of end connection cooling water pipe lower end, other end connection dust arrester top.Water in cooling water pipe is pumped into dedusting dress
In putting, as water bath dust-removing water, more economize on water.
Preferably, described dust arrester inner upper end is provided with spray equipment, water pump one end is connected under cooling water pipe
The delivery port other end at end is connected with spray equipment.Water in cooling water pipe is pumped into spray equipment, then carries out spraying and dedusting, is made
Obtain dust removing effects more preferably, while more using water wisely.
Preferably, gas compression pump is set between described air inlet pipe and dust arrester.Gas compression pump can be to flue gas
It is pressurized, increases the effect of water bath dust-removing.
Preferably, it is additionally provided with cooling device between described water pump and spray equipment.Cooling water pipe is to dust arrester
After cooling, the water temperature rise in it, cooling device is set, is pumped into dust arrester, overall cooling effect after water temperature is reduced again again
Fruit is more preferable.
Compared with prior art, the utility model can at least produce a kind of following beneficial effect：The utility model is using cold
But water pipe cools down to flue gas, while increases time of the flue gas of heat in dust arrester so that cooling water pipe is cold to flue gas
But effect is more preferable, avoids high-temperature flue gas from impacting the service life of equipment；The utility model will can be inhaled every a period of time
The sewage discharge of dust is received；Water in cooling water pipe is pumped into dust arrester by the utility model, as water bath dust-removing water,
More economize on water；The utility model increases spraying and dedusting so that dust removing effects are more preferably；The utility model is pressurized to flue gas, is increased
Add the effect of water bath dust-removing；After the utility model is cooled down using cooling water pipe to dust arrester, cool through apparatus for supercooling, it is overall
Cooling effect is more preferable.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of dust arrester of the present utility model.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining
The utility model, it is not used to limit the utility model.
Fig. 1, Fig. 2 show the structure of such a refuse pyrolysis smoke eliminator, and several implementations are enumerated with reference to legend
Example.
Embodiment 1：
A kind of refuse pyrolysis smoke eliminator；Including be sequentially connected dust arrester 1, in desulfurization and device 2, liquid qi leel
From device 3, high-precision purifier 4, centrifugal blower 5；Air inlet pipe 6, described centrifugation wind are connected with described dust arrester 1
Machine 5 is connected with blast pipe 7；Described dust arrester 1 includes inner casing 8, shell 9, and cooling water is provided between inner casing 8 and shell 9
Pipe 12, cooling water pipe 12 are spirally wrapped around the outer surface of inner casing 8；In described dust arrester 1 first is provided with by left-to-right
The inside of dust arrester 1 is divided into first passage 17, second by baffle plate 10, second baffle 11, first baffle 10 and second baffle 11
Passage 18, third channel 19, first passage 17 are connected with air inlet pipe 6, and third channel 19 is connected with escape pipe 14, first baffle 10
Upper opening, the lower opening of second baffle 11, the upper end of second channel 18 are connected with the upper end of first passage 17, second channel 18 and
The lower end of triple channel 19 connects, second channel 18 and the lower end of third channel 19 dress water, the lower end of the second baffle 11 insertion water surface.
Flue gas is introduced into dust arrester 1 by air inlet pipe 6, passes through the solids in flue gas by the way of water bath dust-removing
Shower water settles down, then by, with device 2, carrying out removing reaction of Salmon-Saxl in desulfurization；Pass through liquid-gas separation device 3 again, remove gas
In vapor and liquid impurity；Pass through high-precision purifier 4 again, high-precision purifier 4 contains circulating condensing, high-tension electricity
The processes such as field, negatron, ozone, charcoal absorption, finally discharge from blast pipe 7 by centrifugal blower 5, wherein in desulfurization and fill
Put 2, liquid-gas separation device 3, high-precision purifier 4 is prior art, inventive point not of the present utility model.Filled in dedusting
In putting 1, cooling water pipe 12 cools down to flue gas, and flue gas passes sequentially through first passage 17, second channel 18, increases the flue gas of heat
Time in dust arrester 1 so that the effect that cooling water pipe 12 cools down to flue gas is more preferable, and flue gas is after water bath dust-removing by
Triple channel 19 is discharged through escape pipe 14.
Embodiment 2：
A kind of refuse pyrolysis smoke eliminator；Including be sequentially connected dust arrester 1, in desulfurization and device 2, liquid qi leel
From device 3, high-precision purifier 4, centrifugal blower 5；Air inlet pipe 6, described centrifugation wind are connected with described dust arrester 1
Machine 5 is connected with blast pipe 7；Described dust arrester 1 includes inner casing 8, shell 9, and cooling water is provided between inner casing 8 and shell 9
Pipe 12, cooling water pipe 12 are spirally wrapped around the outer surface of inner casing 8；In described dust arrester 1 first is provided with by left-to-right
The inside of dust arrester 1 is divided into first passage 17, second by baffle plate 10, second baffle 11, first baffle 10 and second baffle 11
Passage 18, third channel 19, first passage 17 are connected with air inlet pipe 6, and third channel 19 is connected with escape pipe 14, first baffle 10
Upper opening, the lower opening of second baffle 11, the upper end of second channel 18 are connected with the upper end of first passage 17, second channel 18 and
The lower end of triple channel 19 connects, second channel 18 and the lower end of third channel 19 dress water, the lower end of the second baffle 11 insertion water surface.Described
The lower end of dust arrester 1 is provided with sewage draining exit 16.The sewage for absorbing dust can be discharged every a period of time.
Flue gas is introduced into dust arrester 1 by air inlet pipe 6, passes through the solids in flue gas by the way of water bath dust-removing
Shower water settles down, then by, with device 2, carrying out removing reaction of Salmon-Saxl in desulfurization；Pass through liquid-gas separation device 3 again, remove gas
In vapor and liquid impurity；Pass through high-precision purifier 4 again, high-precision purifier 4 contains circulating condensing, high-tension electricity
The processes such as field, negatron, ozone, charcoal absorption, finally discharge from blast pipe 7 by centrifugal blower 5, wherein in desulfurization and fill
Put 2, liquid-gas separation device 3, high-precision purifier 4 is prior art, inventive point not of the present utility model.Filled in dedusting
In putting 1, cooling water pipe 12 cools down to flue gas, and flue gas passes sequentially through first passage 17, second channel 18, increases the flue gas of heat
Time in dust arrester 1 so that the effect that cooling water pipe 12 cools down to flue gas is more preferable, and flue gas is after water bath dust-removing by
Triple channel 19 is discharged through escape pipe 14.
Embodiment 3：
A kind of refuse pyrolysis smoke eliminator；Including be sequentially connected dust arrester 1, in desulfurization and device 2, liquid qi leel
From device 3, high-precision purifier 4, centrifugal blower 5；Air inlet pipe 6, described centrifugation wind are connected with described dust arrester 1
Machine 5 is connected with blast pipe 7；Described dust arrester 1 includes inner casing 8, shell 9, and cooling water is provided between inner casing 8 and shell 9
Pipe 12, cooling water pipe 12 are spirally wrapped around the outer surface of inner casing 8；It is another to be provided with water pump 13, the one end of water pump 13 connection cooling water
The delivery port of the lower end of pipe 12, other end connection dust arrester 1 top.Water in cooling water pipe 12 is pumped into dust arrester 1, made
For water bath dust-removing water, more economize on water.First baffle 10, second baffle 11 are provided with by left-to-right in described dust arrester 1,
The inside of dust arrester 1 is divided into first passage 17, second channel 18, third channel 19 by first baffle 10 and second baffle 11,
First passage 17 is connected with air inlet pipe 6, and third channel 19 is connected with escape pipe 14, the upper opening of first baffle 10, second baffle
11 lower openings, the upper end of second channel 18 are connected with the upper end of first passage 17, and second channel 18 is connected with the lower end of third channel 19,
Second channel 18 and the lower end of third channel 19 dress water, the lower end of the second baffle 11 insertion water surface.The described lower end of dust arrester 1 is set
There is sewage draining exit 16.The sewage for absorbing dust can be discharged every a period of time.
Flue gas is introduced into dust arrester 1 by air inlet pipe 6, passes through the solids in flue gas by the way of water bath dust-removing
Shower water settles down, then by, with device 2, carrying out removing reaction of Salmon-Saxl in desulfurization；Pass through liquid-gas separation device 3 again, remove gas
In vapor and liquid impurity；Pass through high-precision purifier 4 again, high-precision purifier 4 contains circulating condensing, high-tension electricity
The processes such as field, negatron, ozone, charcoal absorption, finally discharge from blast pipe 7 by centrifugal blower 5, wherein in desulfurization and fill
Put 2, liquid-gas separation device 3, high-precision purifier 4 is prior art, inventive point not of the present utility model.Filled in dedusting
In putting 1, cooling water pipe 12 cools down to flue gas, and flue gas passes sequentially through first passage 17, second channel 18, increases the flue gas of heat
Time in dust arrester 1 so that the effect that cooling water pipe 12 cools down to flue gas is more preferable, and flue gas is after water bath dust-removing by
Triple channel 19 is discharged through escape pipe 14.
Embodiment 4：
A kind of refuse pyrolysis smoke eliminator；Including be sequentially connected dust arrester 1, in desulfurization and device 2, liquid qi leel
From device 3, high-precision purifier 4, centrifugal blower 5；Air inlet pipe 6, described centrifugation wind are connected with described dust arrester 1
Machine 5 is connected with blast pipe 7；Described dust arrester 1 includes inner casing 8, shell 9, and cooling water is provided between inner casing 8 and shell 9
Pipe 12, cooling water pipe 12 are spirally wrapped around the outer surface of inner casing 8；Another to be provided with water pump 13, the inner upper end of dust arrester 1 is set
There is spray equipment 15, the delivery port other end of the one end of water pump 13 connection cooling water pipe 12 lower end is connected with spray equipment 15.Will be cold
But the water in water pipe 12 is pumped into spray equipment 15, then carries out spraying and dedusting so that dust removing effects more preferably, while are more economized on
Water.Last dust removal by spraying water is re-used as water bath dust-removing water, more economizes on water.By left-to-right setting in described dust arrester 1
There are first baffle 10, second baffle 11, the inside of dust arrester 1 is divided into first passage by first baffle 10 and second baffle 11
17th, second channel 18, third channel 19, first passage 17 are connected with air inlet pipe 6, and third channel 19 is connected with escape pipe 14, the
The upper opening of one baffle plate 10, the lower opening of second baffle 11, the upper end of second channel 18 are connected with the upper end of first passage 17, and second is logical
Road 18 is connected with the lower end of third channel 19, second channel 18 and the lower end of third channel 19 dress water, the lower end of second baffle 11 insertion water
Face.The described lower end of dust arrester 1 is provided with sewage draining exit 16.The sewage for absorbing dust can be discharged every a period of time.
Flue gas is introduced into dust arrester 1 by air inlet pipe 6, passes through the solids in flue gas by the way of water bath dust-removing
Shower water settles down, then by, with device 2, carrying out removing reaction of Salmon-Saxl in desulfurization；Pass through liquid-gas separation device 3 again, remove gas
In vapor and liquid impurity；Pass through high-precision purifier 4 again, high-precision purifier 4 contains circulating condensing, high-tension electricity
The processes such as field, negatron, ozone, charcoal absorption, finally discharge from blast pipe 7 by centrifugal blower 5, wherein in desulfurization and fill
Put 2, liquid-gas separation device 3, high-precision purifier 4 is prior art, inventive point not of the present utility model.Filled in dedusting
In putting 1, cooling water pipe 12 cools down to flue gas, and flue gas passes sequentially through first passage 17, second channel 18, increases the flue gas of heat
Time in dust arrester 1 so that the effect that cooling water pipe 12 cools down to flue gas is more preferable, and flue gas is by water bath dust-removing, spray
Discharged after dedusting by third channel 19 through escape pipe 14.
Embodiment 5：
A kind of refuse pyrolysis smoke eliminator；Including be sequentially connected dust arrester 1, in desulfurization and device 2, liquid qi leel
From device 3, high-precision purifier 4, centrifugal blower 5；Air inlet pipe 6, described centrifugation wind are connected with described dust arrester 1
Machine 5 is connected with blast pipe 7；Gas compression pump 21 is set between described air inlet pipe 6 and dust arrester 1.Gas compression pump 21 can
Flue gas is pressurized, increases the effect of water bath dust-removing.Described dust arrester 1 includes inner casing 8, shell 9, inner casing 8 and shell 9
Between be provided with cooling water pipe 12, cooling water pipe 12 is spirally wrapped around the outer surface of inner casing 8；Separately it is provided with water pump 13, dedusting
The inner upper end of device 1 is provided with spray equipment 15, the delivery port other end of the one end of water pump 13 connection cooling water pipe 12 lower end and spray
Shower device 15 connects.Water in cooling water pipe 12 is pumped into spray equipment 15, then carries out spraying and dedusting so that dust removing effects are more
It is good, while more using water wisely.Last dust removal by spraying water is re-used as water bath dust-removing water, more economizes on water.Described dedusting dress
Put in 1 and be provided with first baffle 10, second baffle 11 by left-to-right, first baffle 10 and second baffle 11 are by dust arrester 1
Inside is divided into first passage 17, second channel 18, third channel 19, and first passage 17 is connected with air inlet pipe 6, third channel 19 with
Escape pipe 14 connects, the upper opening of first baffle 10, the lower opening of second baffle 11, the upper end of second channel 18 and first passage 17
Upper end is connected, and second channel 18 is connected with the lower end of third channel 19, second channel 18 and the lower end of third channel 19 dress water, second gear
The water surface is inserted in the lower end of plate 11.The described lower end of dust arrester 1 is provided with sewage draining exit 16.Dust can will be absorbed every a period of time
Sewage is discharged.
Flue gas is introduced into dust arrester 1 by air inlet pipe 6, passes through the solids in flue gas by the way of water bath dust-removing
Shower water settles down, then by, with device 2, carrying out removing reaction of Salmon-Saxl in desulfurization；Pass through liquid-gas separation device 3 again, remove gas
In vapor and liquid impurity；Pass through high-precision purifier 4 again, high-precision purifier 4 contains circulating condensing, high-tension electricity
The processes such as field, negatron, ozone, charcoal absorption, finally discharge from blast pipe 7 by centrifugal blower 5, wherein in desulfurization and fill
Put 2, liquid-gas separation device 3, high-precision purifier 4 is prior art, inventive point not of the present utility model.Filled in dedusting
In putting 1, cooling water pipe 12 cools down to flue gas, and flue gas passes sequentially through first passage 17, second channel 18, increases the flue gas of heat
Time in dust arrester 1 so that the effect that cooling water pipe 12 cools down to flue gas is more preferable, and flue gas is by water bath dust-removing, spray
Discharged after dedusting by third channel 19 through escape pipe 14.
Optimum embodiment：
A kind of refuse pyrolysis smoke eliminator；Including be sequentially connected dust arrester 1, in desulfurization and device 2, liquid qi leel
From device 3, high-precision purifier 4, centrifugal blower 5；Air inlet pipe 6, described centrifugation wind are connected with described dust arrester 1
Machine 5 is connected with blast pipe 7；Gas compression pump 21 is set between described air inlet pipe 6 and dust arrester 1.Gas compression pump 21 can
Flue gas is pressurized, increases the effect of water bath dust-removing.Described dust arrester 1 includes inner casing 8, shell 9, inner casing 8 and shell 9
Between be provided with cooling water pipe 12, cooling water pipe 12 is spirally wrapped around the outer surface of inner casing 8；Separately it is provided with water pump 13, dedusting
The inner upper end of device 1 is provided with spray equipment 15, the delivery port other end of the one end of water pump 13 connection cooling water pipe 12 lower end and spray
Shower device 15 connects.Water in cooling water pipe 12 is pumped into spray equipment 15, then carries out spraying and dedusting so that dust removing effects are more
It is good, while more using water wisely.Last dust removal by spraying water is re-used as water bath dust-removing water, more economizes on water.Described water pump 13
Cooling device 20 is additionally provided between spray equipment 15.After cooling water pipe 12 cools down to dust arrester 1, the water temperature liter in it
Height, cooling device 20 is set, is pumped into dust arrester 1 after water temperature is reduced again again, overall cooling effect is more preferable.Described dedusting
First baffle 10, second baffle 11 are provided with by left-to-right in device 1, and first baffle 10 and second baffle 11 are by dust arrester 1
Inside be divided into first passage 17, second channel 18, third channel 19, first passage 17 is connected with air inlet pipe 6, third channel 19
It is connected with escape pipe 14, the upper opening of first baffle 10, the lower opening of second baffle 11, the upper end of second channel 18 and first passage
17 upper ends are connected, and second channel 18 is connected with the lower end of third channel 19, second channel 18 and the lower end of third channel 19 dress water, and second
The water surface is inserted in the lower end of baffle plate 11.The described lower end of dust arrester 1 is provided with sewage draining exit 16.Dust can will be absorbed every a period of time
Sewage discharge.
Flue gas is introduced into dust arrester 1 by air inlet pipe 6, passes through the solids in flue gas by the way of water bath dust-removing
Shower water settles down, then by, with device 2, carrying out removing reaction of Salmon-Saxl in desulfurization；Pass through liquid-gas separation device 3 again, remove gas
In vapor and liquid impurity；Pass through high-precision purifier 4 again, high-precision purifier 4 contains circulating condensing, high-tension electricity
The processes such as field, negatron, ozone, charcoal absorption, finally discharge from blast pipe 7 by centrifugal blower 5, wherein in desulfurization and fill
Put 2, liquid-gas separation device 3, high-precision purifier 4 is prior art, inventive point not of the present utility model.Filled in dedusting
In putting 1, cooling water pipe 12 cools down to flue gas, and flue gas passes sequentially through first passage 17, second channel 18, increases the flue gas of heat
Time in dust arrester 1 so that the effect that cooling water pipe 12 cools down to flue gas is more preferable, and flue gas is by water bath dust-removing, spray
Discharged after dedusting by third channel 19 through escape pipe 14.
Multiple explanatory embodiments spoken of in this manual, refer to combining the concrete structure bag of embodiment description
Include at least one embodiment of the application generality description.It is not certain that statement of the same race, which occur, in multiple places in the description
Refer to same embodiment.Furthermore, it is understood that when describing a structure with reference to any one embodiment, what is advocated is to combine
Other embodiment realizes that this structure falls in the scope of the utility model.
Claims (6)
- A kind of 1. refuse pyrolysis smoke eliminator；Including the dust arrester being sequentially connected（1）, in desulfurization and device（2）, liquid gas Separator（3）, high-precision purifier（4）, centrifugal blower（5）；Described dust arrester（1）On be connected with air inlet pipe（6）, Described centrifugal blower（5）It is connected with blast pipe（7）；It is characterized in that：Described dust arrester（1）Include inner casing（8）, shell （9）, inner casing（8）And shell（9）Between be provided with cooling water pipe（12）, cooling water pipe（12）It is spirally wrapped around inner casing（8） Outer surface；Described dust arrester（1）It is interior to be provided with first baffle by left-to-right（10）, second baffle（11）, first baffle （10）And second baffle（11）By dust arrester（1）Inside be divided into first passage（17）, second channel（18）, third channel （19）, first passage（17）With air inlet pipe（6）Connection, third channel（19）With escape pipe（14）Connection, first baffle（10）On Side's opening, second baffle（11）Lower opening, second channel（18）Upper end and first passage（17）Upper end connects, second channel （18）With third channel（19）Lower end connects, second channel（18）With third channel（19）Lower end fills water, second baffle（11）Under The end insertion water surface.
- A kind of 2. refuse pyrolysis smoke eliminator according to claim 1, it is characterised in that：Described dust arrester （1）Lower end is provided with sewage draining exit（16）.
- A kind of 3. refuse pyrolysis smoke eliminator according to claim 2, it is characterised in that：Described cooling water pipe （12）From top to bottom be wrapped in inner casing（8）Outer surface, separately it is provided with water pump（13）, water pump（13）One end connects cooling water pipe （12）The delivery port of lower end, other end connection dust arrester（1）Top.
- A kind of 4. refuse pyrolysis smoke eliminator according to claim 3, it is characterised in that：Described dust arrester （1）Inner upper end is provided with spray equipment（15）, water pump（13）One end connects cooling water pipe（12）The delivery port other end of lower end With spray equipment（15）Connection.
- A kind of 5. refuse pyrolysis smoke eliminator according to claim 1, it is characterised in that：Described air inlet pipe（6） With dust arrester（1）Between gas compression pump is set（21）.
- A kind of 6. refuse pyrolysis smoke eliminator according to claim 3, it is characterised in that：Described water pump（13）With Spray equipment（15）Between be additionally provided with cooling device（20）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720481453.XU CN206935034U (en) | 2017-05-03 | 2017-05-03 | A kind of refuse pyrolysis smoke eliminator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720481453.XU CN206935034U (en) | 2017-05-03 | 2017-05-03 | A kind of refuse pyrolysis smoke eliminator |
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| Publication Number | Publication Date |
|---|---|
| CN206935034U true CN206935034U (en) | 2018-01-30 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111076178A (en) * | 2018-10-18 | 2020-04-28 | 郑生权 | Self-combustion type domestic garbage cracking furnace |
-
2017
- 2017-05-03 CN CN201720481453.XU patent/CN206935034U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111076178A (en) * | 2018-10-18 | 2020-04-28 | 郑生权 | Self-combustion type domestic garbage cracking furnace |
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