CN204922999U - Rubbish is walked crosswise screening whirlwind and is thoughtlessly fired pyrolysis device - Google Patents
Rubbish is walked crosswise screening whirlwind and is thoughtlessly fired pyrolysis device Download PDFInfo
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- CN204922999U CN204922999U CN201520636114.5U CN201520636114U CN204922999U CN 204922999 U CN204922999 U CN 204922999U CN 201520636114 U CN201520636114 U CN 201520636114U CN 204922999 U CN204922999 U CN 204922999U
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Abstract
The utility model discloses a rubbish is walked crosswise screening whirlwind and is thoughtlessly fired pyrolysis device. Block easily in order to overcome current garbage pyrolytic processing apparatus, the gaseous phase pyrolysis is insufficient, the power consumption is many, is unfavorable for preventing dioxin formation etc. Inadequately, rubbish enters the mouth and sets up the shelves wall at the cavity the side below of rubbish entry is equipped with sieves the mechanism the below of screening mechanism is equipped with the solid phase pyrolysis chamber the top of screening mechanism is equipped with the gaseous phase pyrolysis chamber, and be equipped with in the lower part of this gaseous phase pyrolysis chamber and thoughtlessly revolve lumen, all chambeies of calming the anger, thoughtlessly revolve calm the anger passageway and the calm the anger all chamber intercommunication of lumen through its perisporium, calm the anger all chambeies and be connected with hot air transportation mechanism. The utility model is used for refuse treatment, it can sieve rubbish in the process of burning simultaneously automatically, carries out the progressive pyrolysis of categorised locellus, prevents blocking of pyrolytic process, and the pyrolysis of gaseous phase secondary is more energy -conserving, more abundant, can prevent the formation of dioxin better, and operation expense is low, and the effect is profitable.
Description
Technical field
The utility model relates to a kind of waste incineration pyrolysis treatment device, is specially a kind of rubbish and walks crosswise screening whirlwind mixed combustion pyrolysis installation.
Background technology
Refuse pyrolysis is the garbage disposal means that developed country extensively adopts, and in the country that the arable lands such as Japan are in great shortage, waste incineration pyrolysis processing ratio reaches 65-80%.But conventional garbage burns pyrolysis treatment device and has the following disadvantages:
One is, conventional garbage burns pyrolysis installation and can not realize sieving rubbish burning process is simultaneously automatic, can not carry out the progressive pyrolysis of classification locellus, the further pyrolysis of gaseous substance except cinder insufficient, easy generation pyrolysis blocks, and affects the environment-friendly garbage pyrolysis preventing bioxin from generating.In conventional garbage mixture, containing the Multiple components such as life organic matter and plastics, glass, ceramics, metal, cement block, before burning, classification intractability is large, and cost is high, adopts garbage mixture directly to enter stove more burn so.But garbage mixture does not sieve and directly enters stove to burn the problem brought be that incineration temperature is difficult to simultaneous adaptation and easily produces the organic waste of bioxin and easily cause the inorganic refuse blocking, affect burning state and deslagging.The retardance of blocking up of burning process, not only increase maintenance cost, and burning state is changed, the control that leading portion suppresses bioxin to generate is burned in impact, increase difficulty and the expense of follow-up bioxin process, add follow-up gas cleaning and remove the possibility that dioxins materials causes secondary pollution.
Two are, existing incinerator technological process mechanism unit is lateral extension, the gaseous substance of easy upwards ascension such as moisture, flue gas etc. that refuse pyrolysis process produces, need the air-introduced machine of relatively high power just can make it transverse shifting and enter next step process, especially easily producing that the organic matter of bioxin is tentatively pyrogenous origin can hot gas, Secondary Air burns further again, and process power consumption is high, and process is difficult to fully, and effect is undesirable; And mechanism unit lateral extension, floor space is large, and one-time investment is large.Build mark 142-2009 regulation, " newly-built grate furnace incineration plant main equipment and the investment estimate of system based on import can by higher than 500,000 yuan/(t/d) controls; The investment estimate that grate furnace incineration plant main equipment all domesticizes can by not higher than 400,000 yuan/(t/d) control; The indices for investment estimate of newly-built fluid bed furnace incineration plant can by not higher than 350,000 yuan/(t/d) control ".To this, advanced economy basis and the powerful investment capacity is not had to be difficult to build up.
Three are, conventional garbage burn pyrolysis installation need supplementary energy many, and waste incineration itself generation heat utilize usefulness not high enough, cause waste incineration cost high.Further, conventional garbage incinerator has higher requirement to refuse thermal value and moisture.CJ/T118-2000 specifies, " enter the average annual moisture of stove house refuse and should not be greater than 50%, average annual content of ashes should not be greater than 30%, and average annual low heat valve should not be less than 4.18MJ/kg ".For ensureing smooth combustion, " domestic refuse treatment project technical regulation " specifies, " incinerator answers collocation point ignition combustor and auxiliary burner ", needs the auxiliary fuel of at substantial.
Conventional garbage burns the deficiency of pyrolysis installation, significantly limit waste incineration pyrolysis applying in China, especially in the application of small and medium-sized cities.
Although some domestic entity and individual are devoted to the research of waste incineration pyrolysis installation always, try hard to overcome existing deficiency.Such as document CN201410085904.9, discloses on the basis of conventional garbage electricity generation system, has added pretreatment system, flue gas treating system, and percolation liquid treating system, in the generation reducing bioxin presoma, done good try; Document CN201320090207.3, disclose and use oxygen-enriched combusting equipment and secondary air system, to ensure incinerator waste gas burning temperature to greatest extent, make the flow-disturbing being conducive to secondary combustion chamber, extend in the secondary combustion chamber time of staying, in decomposition bioxin, achieve certain effect.But these technology all can not carry out automatic sieving to rubbish in pyrolysis, the progressive pyrolysis of locellus of can not classifying, generate with bioxin to prevent from blocking, practicality is not strong, and pyrolysis benefit is not high.
Utility model content
The purpose of this utility model is exactly for above-mentioned deficiency, a kind of rubbish is provided to walk crosswise screening whirlwind mixed combustion pyrolysis installation, it can realize sieving rubbish burning process is simultaneously automatic, carry out the progressive pyrolysis of classification locellus, prevent blocking of pyrolytic process, especially secondary burning pyrolysis is energy-conservation, abundant, can realize better preventing bioxin from generating environmental protection pyrolysis, and space availability ratio is high, take up an area few, can construction investment be reduced, reduce pyrolysis energy consumption, operation expense is low, and the effect efficiency of garbage disposal is better.
For achieving the above object, the technical solution of the utility model is, screening whirlwind mixed combustion pyrolysis installation walked crosswise by this rubbish, comprise the cavity with garbage inlet, described garbage inlet is arranged on sidewall or the shelves wall of cavity, the screening mechanism making rubbish walk crosswise screening pyrolysis is provided with at the side-lower of described garbage inlet, solid phase pyrolysis chamber is provided with in the below of described screening mechanism, vapour-phase pyrolysis room is provided with above described screening mechanism, the bottom of this vapour-phase pyrolysis room has DL lumen, to calm the anger all chambeies, the upper and lower side of described DL lumen has opening, described DL lumen is communicated with all chambeies of calming the anger by the passage of calming the anger of its perisporium, described all chambeies of calming the anger are connected with hot-air conveying mechanism.
Described screening mechanism can have some lateral separations and arrange homodromous sieve roller, has sieve apart from (interval), can arrange hot-air conveying mechanism at described screening mechanism between each sieve roller,
Described passage of calming the anger axially is opened in the perisporium of DL lumen along DL lumen.
Narrow wide under described passage of calming the anger.
Described passage of calming the anger is cut sth. askew to be communicated with by DL lumen wall and to be calmed the anger all chambeies and DL lumen.
The sidewall of garbage inlet is being set or is being provided with moisture passages between shelves wall and vapour-phase pyrolysis room, mixed gas passage is provided with above described vapour-phase pyrolysis room, described moisture passages, vapour-phase pyrolysis room respectively with mixed gas channel connection, described mixed gas passage is communicated with Hun Qi pyrolysis chamber.Further, described Hun Qi pyrolysis chamber can be connected with heat exchange mechanism, purification mechanism.
Be provided with below between described moisture passages and vapour-phase pyrolysis room guide every.
At least Liang Ge solid phase pyrolysis chamber is provided with in the below of described screening mechanism, described each solid phase pyrolysis chamber has interconnective skew wall, described solid phase pyrolysis chamber has burning chamber, wind chamber, lime-ash passage, described wind chamber is communicated with burning chamber by the air channel of interbed, and described lime-ash channel connection burning chamber is through interbed, wind chamber.
Lug is provided with at the lime-ash passage perisporium by wind chamber.
The utility model compares with prior-art devices, garbage inlet described in the utility model is arranged on sidewall or the shelves wall of cavity, the screening mechanism making rubbish walk crosswise screening pyrolysis is provided with at the side-lower of described garbage inlet, solid phase pyrolysis chamber is provided with in the below of described screening mechanism, vapour-phase pyrolysis room is provided with above described screening mechanism, described screening mechanism can arrange homodromous sieve roller and realizes rubbish and walk crosswise motion screening in some lateral separations, can import the hot-air of different temperatures in screening mechanism, vapour-phase pyrolysis room, solid phase pyrolysis chamber as required respectively.When rubbish enters screening mechanism one end or sieve roller on one side from garbage inlet, will the directed other end towards screening mechanism or another side advance, various compositions in rubbish realize the progressive dry capacity reducing (reduced volume) of different section different temperatures in screening mechanism is advanced, screening, pyrolysis, solid phase pyrolysis chamber under Cucumber in rubbish will fall into screening mechanism by the sieve between sieve roller apart from (interval) in advancing, carry out the pyrolysis of different temperatures further, rubbish is at screening mechanism, the meeting upwards ascensions such as the water smoke flue gas that the pyrolysis of solid phase pyrolysis chamber produces, enter the further pyrolysis in vapour-phase pyrolysis room above screening mechanism.Screening classification pyrolysis respectively in advancing like this, not only prevent pyrolysis to block, and owing to entering the preliminary pyrolysis capacity reducing stage of screening mechanism at rubbish, the hot-air of less than 300 DEG C can be supplied as required, first the rubbish entering pyrolysis cavity is carried out preheating, dry, capacity reducing, preliminary pyrolysis, the organic matter of generation bioxin is made not give birth to into the pyrolytic gasification of bioxin at these temperatures---(test shows to give birth to into the combustible organic of non-bioxin, the organic matter of easy Sheng Cheng bioxin in rubbish, below 300 DEG C temperature can pyrolytic gasification be the combustible organic of non-bioxin), this combustible organic and then the vapour-phase pyrolysis room etc. upwards imported to by taking advantage of a situation above screening mechanism, with 300---the hot-air mixing second-time burning pyrolysis of 600 DEG C, just can pyrolitic oxidation and not Sheng Cheng bioxin completely, do not produce the secondary pollution of pyrolysis, the generation of dioxins materials is so just prevented from source, instead of resemble existing dependence to incineration flue gas Shi dioxins materials qualified discharge.
The utility model is provided with DL lumen in the bottom of this vapour-phase pyrolysis room, the periphery of DL lumen has all chambeies of calming the anger, the upper and lower side of described DL lumen has opening, described DL lumen is communicated with all chambeies of calming the anger by the passage of calming the anger of its perisporium, described all chambeies of calming the anger are connected with hot-air conveying mechanism, described passage of calming the anger axially is opened in the perisporium of DL lumen along DL lumen, narrow wide under described passage of calming the anger, described in passage of calming the anger cut sth. askew to be communicated with by DL lumen wall and to calm the anger all chambeies and DL lumen.When the under shed of flue gas from DL lumen enters, after mixing with the hot-air of the higher temperature entered from all chambeies of calming the anger, the mixed combustion of whirlwind will be formed, rotate rising combustion, further pyrolysis, under the effect of air-introduced machine, can be formed better and squeeze spray rotation ascension burning, make combustion and pyrolysis more abundant, without dead angle, energy consumption is low, effective.
The sidewall of garbage inlet is being set or is being provided with moisture passages between shelves wall and vapour-phase pyrolysis room, mixed gas passage is provided with above described vapour-phase pyrolysis room, described moisture passages, vapour-phase pyrolysis room respectively with mixed gas channel connection, described mixed gas passage is communicated with Hun Qi pyrolysis chamber, be provided with below between described moisture passages and vapour-phase pyrolysis room guide every.Gaseous substance can be made like this to classify better the progressive pyrolysis of locellus, and fully pyrolysis, prevents the generation of bioxin better.
At least Liang Ge solid phase pyrolysis chamber is provided with in the below of described screening mechanism, described each solid phase pyrolysis chamber has interconnective skew wall, described solid phase pyrolysis chamber has burning chamber, wind chamber, lime-ash passage, described wind chamber is communicated with burning chamber by the air channel of interbed, described lime-ash channel connection burning chamber, through interbed, wind chamber, is provided with lug at the lime-ash passage perisporium by wind chamber.The pyrolysis under fluidized state of solid matter classification locellus can be realized so better, and the heat energy of pyrolysis can add hot air cavity fully by lime-ash passage, the requirement of the wind that air channel is sprayed satisfied temperature, pressure better, makes fluidized state better, makes pyrolysis more energy-conservation.
The utility model is used for garbage disposal, it can realize sieving rubbish burning process is simultaneously automatic, carries out the progressive pyrolysis of classification locellus, prevents blocking of pyrolytic process, especially secondary burning pyrolysis is energy-conservation, abundant, can prevent the generation of bioxin better, and space availability ratio is high, takes up an area few, construction investment can be reduced, reduce pyrolysis energy consumption, operation expense is low, and the effect efficiency of garbage disposal is good.
Accompanying drawing explanation
Fig. 1 is the utility model sectional view.
Fig. 2 is that the vapour-phase pyrolysis room 3 of Fig. 1 is along A-A place profile.
In figure, 1. cavity, 2. Hun Qi pyrolysis chamber, 3. vapour-phase pyrolysis room, 4. mixed gas passage, 5. moisture passages, 6. DL lumen, all chambeies of 7. calming the anger, 8., 9. garbage inlet, 10. screening mechanism, 11. burning chamber, 12. interbeds, 13. wind chambeies, 14. lime-ash passages, 15. solid phase pyrolysis chambers, 16. lugs, 17. calm the anger passage.
Detailed description of the invention
As Fig. 1, shown in Fig. 2, screening whirlwind mixed combustion pyrolysis installation walked crosswise by the utility model rubbish, comprise the cavity 1 with garbage inlet 9, garbage inlet 9 is arranged on the shelves wall of cavity 1, the screening mechanism 10 making rubbish walk crosswise screening pyrolysis is provided with at the side-lower of garbage inlet 9, screening mechanism 10 has six transversely arranged homodromous sieve rollers, there is sieve apart from (interval) between each sieve roller, sieve roller is driven by actuating unit and moves in the same way, screening mechanism has the hot air outlet be connected with hot-air conveying mechanism, rubbish is mobile on sieve roller realizes drying simultaneously, screening, pyrolysis.
Vapour-phase pyrolysis room 3 is provided with above screening mechanism 10, the bottom of vapour-phase pyrolysis room 3 has DL lumen 6, to calm the anger all chambeies 7, the upper and lower side of DL lumen 6 has opening, upper shed is communicated with vapour-phase pyrolysis room 3, under shed is towards the top of screening mechanism 10, enter flue gas, DL lumen 6 is communicated with all chambeies 7 of calming the anger by the passage 17 of calming the anger of its perisporium, all chambeies 7 of calming the anger are connected with hot-air conveying mechanism, passage 17 of calming the anger axially is opened in the perisporium of DL lumen 6 along DL lumen 6, passage 17 of calming the anger is cut sth. askew and is communicated with by DL lumen wall calm the anger all chamber 7 and DL lumen 6, can produce and squeeze spray, DL effect, make the pyrolysis of DL rising combustion evenly fully energy-conservation.
Be provided with moisture passages 5 arranging between the shelves wall of garbage inlet 9 and vapour-phase pyrolysis room 3, mixed gas passage 4 is provided with above vapour-phase pyrolysis room 3, moisture passages 5, vapour-phase pyrolysis room 3 are communicated with mixed gas passage 4 respectively, mixed gas passage 4 is communicated with Hun Qi pyrolysis chamber 2, further, Hun Qi pyrolysis chamber 2 is connected with heat exchange mechanism, purification mechanism.
Be provided with below between moisture passages 5 and vapour-phase pyrolysis room 3 and guide every 8, guide and be tilted to lower protrusion every 8.
Three solid phase pyrolysis chambers 15 are provided with in the below of screening mechanism 10, each solid phase pyrolysis chamber 15 has interconnective skew wall, solid phase pyrolysis chamber 15 has burning chamber 11, wind chamber 13, lime-ash passage 14, wind chamber 13 is communicated with burning chamber 11 by the air channel of interbed 12, lime-ash passage 14 is communicated with burning chamber 11 through interbed 12, wind chamber 13, some lugs 16 are provided with, to increase radiating surface at the lime-ash passage perisporium by wind chamber 13.
The in the end side of (Graph-Oriented 1 rightmost) solid phase pyrolysis chamber, can arrange without the need to or can not the grit chamber of pyrolysis.
Further, passage 17 of calming the anger can be narrow wide below, can be formed and squeeze spray DL ascension combustion and pyrolysis, better effects if.
Further, the sieve roller of the utility model screening mechanism 10 is connected with actuating unit, this actuating unit can be connected with control device, the speed that can realize automatically regulating sieve roller to rotate as required and dynamics, can improve like this under less than 300 DEG C temperature conditions and Cheng the effect of preliminary pyrolysis of bioxin and efficiency to entering chamber garbage pre-heating, drying and not Sheng.
Claims (8)
1. screening whirlwind mixed combustion pyrolysis installation walked crosswise by a rubbish, comprise the cavity (1) with garbage inlet (9), it is characterized in that, described garbage inlet (9) is arranged on sidewall or the shelves wall of cavity (1), the screening mechanism (10) making rubbish walk crosswise screening pyrolysis is provided with at the side-lower of described garbage inlet (9), solid phase pyrolysis chamber (15) is provided with in the below of described screening mechanism (10), vapour-phase pyrolysis room (3) is provided with in the top of described screening mechanism (10), the bottom of this vapour-phase pyrolysis room (3) has DL lumen (6), to calm the anger all chambeies (7), the upper and lower side of described DL lumen (6) has opening, described DL lumen (6) is communicated with all chambeies (7) of calming the anger by the passage of calming the anger (17) of its perisporium, described all chambeies (7) of calming the anger are connected with hot-air conveying mechanism.
2. screening whirlwind mixed combustion pyrolysis installation walked crosswise by rubbish according to claim 1, it is characterized in that, described in passage (17) of calming the anger axially be opened in the perisporium of DL lumen (6) along DL lumen (6).
3. screening whirlwind mixed combustion pyrolysis installation walked crosswise by rubbish according to claim 1, it is characterized in that, described in calm the anger narrow wide under passage (17).
4. screening whirlwind mixed combustion pyrolysis installation walked crosswise by rubbish according to claim 1, it is characterized in that, described in passage (17) of calming the anger cut sth. askew and be communicated with by DL lumen wall calm the anger all chambeies (7) and DL lumen (6).
5. according to claim 1---screening whirlwind mixed combustion pyrolysis installation walked crosswise by the rubbish described in 4 any one, it is characterized in that, the sidewall of garbage inlet (9) is being set or is being provided with moisture passages (5) between shelves wall and vapour-phase pyrolysis room (3), mixed gas passage (4) is provided with in the top of described vapour-phase pyrolysis room (3), described moisture passages (5), vapour-phase pyrolysis room (3) are communicated with mixed gas passage (4) respectively, and described mixed gas passage (4) is communicated with Hun Qi pyrolysis chamber (2).
6. screening whirlwind mixed combustion pyrolysis installation walked crosswise by rubbish according to claim 5, it is characterized in that, is provided with and guides every (8) below between described moisture passages (5) and vapour-phase pyrolysis room (3).
7. according to claim 1---screening whirlwind mixed combustion pyrolysis installation walked crosswise by the rubbish described in 4 any one, it is characterized in that, be provided with in the below of described screening mechanism (10) at least Liang Ge solid phase pyrolysis chamber (15), described each solid phase pyrolysis chamber (15) has interconnective skew wall, described solid phase pyrolysis chamber (15) has burning chamber (11), wind chamber (13), lime-ash passage (14), described wind chamber (13) is communicated with burning chamber (11) by the air channel of interbed (12), described lime-ash passage (14) is communicated with burning chamber (11) through interbed (12), wind chamber (13).
8. screening whirlwind mixed combustion pyrolysis installation walked crosswise by rubbish according to claim 7, it is characterized in that, is provided with lug (16) at the lime-ash passage perisporium by wind chamber (13).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520636114.5U CN204922999U (en) | 2015-08-22 | 2015-08-22 | Rubbish is walked crosswise screening whirlwind and is thoughtlessly fired pyrolysis device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520636114.5U CN204922999U (en) | 2015-08-22 | 2015-08-22 | Rubbish is walked crosswise screening whirlwind and is thoughtlessly fired pyrolysis device |
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| CN204922999U true CN204922999U (en) | 2015-12-30 |
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| CN201520636114.5U Expired - Fee Related CN204922999U (en) | 2015-08-22 | 2015-08-22 | Rubbish is walked crosswise screening whirlwind and is thoughtlessly fired pyrolysis device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106468434A (en) * | 2015-08-22 | 2017-03-01 | 湖南金卫环保设备科技有限公司 | Rubbish row screening whirlwind mixes combustion pyrolysis installation |
| CN110410795A (en) * | 2019-07-23 | 2019-11-05 | 湖北理工学院 | Sludge efficient incineration rotary kiln |
-
2015
- 2015-08-22 CN CN201520636114.5U patent/CN204922999U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106468434A (en) * | 2015-08-22 | 2017-03-01 | 湖南金卫环保设备科技有限公司 | Rubbish row screening whirlwind mixes combustion pyrolysis installation |
| CN110410795A (en) * | 2019-07-23 | 2019-11-05 | 湖北理工学院 | Sludge efficient incineration rotary kiln |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151230 Termination date: 20190822 |
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| CF01 | Termination of patent right due to non-payment of annual fee |