CN209568062U - The continuous anaerobic carbonization running gear of superheated steam - Google Patents
The continuous anaerobic carbonization running gear of superheated steam Download PDFInfo
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- CN209568062U CN209568062U CN201822254900.5U CN201822254900U CN209568062U CN 209568062 U CN209568062 U CN 209568062U CN 201822254900 U CN201822254900 U CN 201822254900U CN 209568062 U CN209568062 U CN 209568062U
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- 238000003763 carbonization Methods 0.000 title claims abstract description 60
- 239000000463 material Substances 0.000 claims description 20
- 238000001816 cooling Methods 0.000 claims description 18
- 238000007599 discharging Methods 0.000 claims description 17
- 230000007246 mechanism Effects 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 238000003860 storage Methods 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 230000008859 change Effects 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 4
- 239000010815 organic waste Substances 0.000 abstract description 10
- 238000005516 engineering process Methods 0.000 abstract description 6
- 239000005416 organic matter Substances 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- 239000000543 intermediate Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000007664 blowing Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
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- 230000005540 biological transmission Effects 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000005315 distribution function Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- OBOXTJCIIVUZEN-UHFFFAOYSA-N [C].[O] Chemical compound [C].[O] OBOXTJCIIVUZEN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
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- 239000010793 electronic waste Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
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- 238000001704 evaporation Methods 0.000 description 1
- 235000021050 feed intake Nutrition 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
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Abstract
The utility model relates to overheat steam technology fields, more particularly, to a kind of continuous anaerobic carbonization running gear of superheated steam comprising: superheated steam pipeline assembly and the first carbide furnace set gradually from top to bottom, the second carbide furnace, third carbide furnace；The superheated steam general pipeline is connect with first carbide furnace, the second carbide furnace, third carbide furnace respectively by each superheated steam branch pipe, and the exhaust main is connect with first carbide furnace, the second carbide furnace, third carbide furnace respectively by each exhaust branch pipe.The continuous anaerobic carbonization running gear of the superheated steam, which can be realized, carries out the continuous anaerobic carbonization of superheated steam to organic waste, and the continuous anaerobic carbonization running gear of the superheated steam passes through the mutual cooperation between the first carbide furnace, the second carbide furnace, third carbide furnace of setting, and smooth, the smooth execution of the continuous anaerobic carbonization of superheated steam can be thoroughly realized using three-level carbonization.
Description
Technical field
The utility model relates to overheat steam technology fields, run more particularly, to a kind of continuous anaerobic carbonization of superheated steam
Device.
Background technique
It is annual to generate a large amount of dangerous organic waste with the fast development of the industries such as China Chemical Industry, pesticide, medicine,
Although many wastes can destroy pollutant difficult to degrade by simply burning, a large amount of hypertoxic gas two can be generated simultaneously
Dislike the wastes such as English and residue, flying dust.Currently, the problem that with high salt, high-COD waste water administers hardly possible is increasingly prominent.
Traditional method: 1. biochemical method can not be handled because salinity is high；2. multiple-effect evaporation condensing crystallizing only will
Dangerous waste is converted into solid-state form from liquid, and poisonous and hazardous organic matter is not eliminated in salt of endangering；3. embrane method filters, the easily stifled replacement of film
Frequently, operating cost is high, and cannot thoroughly effectively remove organic matter；4. burn, since inorganic matter salt easily melts, burner hearth,
In fire grate, pipeline easy " hardened ", frequent blowing out is caused to clear up, operating cost is high, and disposing capacity is low；5. commonly carbonization technology, no
Pipe is internal heat type or external-heat, and " melting ", " hardened " phenomenon occur in inorganic salts, causes carbonization to be not thorough, the difficulties such as operating cost height
Topic.
The information disclosed in the background technology section is intended only to deepen the reason to the general background technology of the utility model
Solution, and it is known to those skilled in the art existing to be not construed as recognizing or imply that the information is constituted in any form
Technology.
Utility model content
The purpose of this utility model is to provide a kind of continuous anaerobic carbonization running gear of superheated steam and methods, with solution
Organic waste carbonization certainly existing in the prior art is not thorough, cannot achieve the skill of the continuous anaerobic carbonization organic matter of superheated steam
Art problem.
To achieve the goals above, the utility model uses following technical scheme:
The utility model provides a kind of continuous anaerobic carbonization running gear of superheated steam comprising: superheated steam pipeline is total
At with the first carbide furnace, the second carbide furnace, third carbide furnace that set gradually from top to bottom；The first end of first carbide furnace
Upper entrance for inputting material to be processed, the lower part outlet of the second end of first carbide furnace and second carbonization
The upper entrance of the second end of furnace connects, and the of the lower part outlet of the first end of second carbide furnace and the third carbide furnace
The upper entrance of one end connects, and the lower part outlet of the second end of the third carbide furnace is used to export the material after carbonization；It is described
Superheated steam pipeline assembly includes: superheated steam general pipeline, superheated steam branch pipe, exhaust main and exhaust branch pipe；The overheat is steamed
Vapour general pipeline is connect with first carbide furnace, the second carbide furnace, third carbide furnace respectively by each superheated steam branch pipe, described
Exhaust main is connect with first carbide furnace, the second carbide furnace, third carbide furnace respectively by each exhaust branch pipe.
As a kind of further technical solution, the exhaust branch pipe include first exhaust branch pipe, second exhaust branch pipe and
Third exhaust branch pipe, the first exhaust branch pipe are connected to the middle part of first carbide furnace, the second exhaust branch pipe connection
In the middle part of second carbide furnace, the third exhaust branch pipe is connected to the middle part of third carbide furnace；The superheated steam branch
Pipe includes: the first superheated steam branch pipe, the second superheated steam branch pipe and third superheated steam branch pipe, the first superheated steam branch
Pipe is connected to the middle part of first carbide furnace, and the second superheated steam branch pipe is connected to the middle part of second carbide furnace,
The third superheated steam branch pipe is connected to the middle part of third carbide furnace.
As a kind of further technical solution, the exhaust branch pipe is also designed to following scheme: being connected to every
The front end or end of one layer of carbide furnace.The superheated steam branch pipe is also designed to following scheme: being connected to each layer of carbon
Change the front end or end of furnace.
As a kind of further technical solution, first carbide furnace, the second carbide furnace, third carbide furnace pass through respectively
The realization of frequency conversion speed-down machine controls its feeding main shaft.
As a kind of further technical solution, further includes: rack；The first load carrier, are provided in the rack
Two load carriers and third load carrier are provided with first carbide furnace, second carrying on first load carrier
It is provided with second carbide furnace in mechanism, the third carbide furnace is provided on the third load carrier.
As a kind of further technical solution, further includes: ladder, the ladder have three layers of ladder structure, adjacent ladder
There is a half space, the ladder is set to the side of the rack between minor structure.
As a kind of further technical solution, the angle of every layer of ladder structure and horizontal plane is 30 DEG C to 45 DEG C.
As a kind of further technical solution, the upper entrance and feed mechanism of the first end of first carbide furnace connect
It connects, the lower part outlet of the second end of the third carbide furnace is connect with discharging mechanism.
As a kind of further technical solution, the feed mechanism includes: storage bin, bucket elevator and feeding passage, institute
The bottom that storage bin is set to the bucket elevator is stated, the bucket elevator is used to for the treating material in storage bin being promoted to described
The import of feeding passage, the feeding passage include: upper ramp way, lower ramp way and augers；The spiral pushes away
The entrance of device is sent to connect with the upper ramp way, the outlet of the augers and the lower ramp way；The updip
Access ramp is connect with the top of the bucket elevator, and the lower ramp way is connect with the entrance of first carbide furnace.
As a kind of further technical solution, the bucket elevator includes: scrapper conveyor or pipe chain machine.
As a kind of further technical solution, the discharging device includes: water cooling stirring cage or lag cooler；The water cooling is stirred
The quantity of cage is one or more；The quantity of the lag cooler is one or more.
By adopting the above technical scheme, the utility model has the following beneficial effects:
The utility model provide a kind of continuous anaerobic carbonization running gear of superheated steam, it can be achieved that organic waste into
Row superheated steam anaerobic carbonization, and the continuous anaerobic carbonization running gear of the superheated steam passes through the first carbide furnace of setting, the
Mutual cooperation between two carbide furnaces, third carbide furnace can thoroughly realize the continuous non-oxygen carbon of superheated steam by three-level carbonization
Smooth, the smooth execution changed.
Detailed description of the invention
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the side view of the continuous anaerobic carbonization running gear of superheated steam provided by the embodiment of the utility model；
Fig. 2 is the front view of the continuous anaerobic carbonization running gear of superheated steam provided by the embodiment of the utility model；
Fig. 3 is the top view of the continuous anaerobic carbonization running gear of superheated steam provided by the embodiment of the utility model.
Icon: 1- storage bin；2- bucket elevator；3- feeding passage；4- augers；The first carbide furnace of 5-；The second carbon of 6-
Change furnace；7- third carbide furnace；8- rack；10- diagonal brace；11- ladder；12- fence；13- superheated steam general pipeline；14- exhaust main；
71- Blowing stopper；91- discharging stirring cage；92- water(-cooling) jacket；131- the first superheated steam branch pipe；132- the second superheated steam branch pipe；
133- third superheated steam branch pipe；141- first exhaust branch pipe；142- second exhaust branch pipe；143- third exhaust branch pipe.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
Field those of ordinary skill every other embodiment obtained without making creative work belongs to practical
Novel protected range.
Specific embodiment of the present utility model is described in detail below in conjunction with attached drawing.It should be understood that herein
Described specific embodiment is only used for describing and explaining the present invention, and is not intended to limit the utility model.
Embodiment one
In conjunction with shown in Fig. 1 to Fig. 3, the present embodiment provides a kind of continuous anaerobic carbonization running gears of superheated steam, comprising: carbon
Change furnace operating unit, the carbide furnace operating unit include: superheated steam pipeline assembly and set gradually from top to bottom first
Carbide furnace 5, the second carbide furnace 6, third carbide furnace 7；The upper entrance and feeding passage 3 of the first end of first carbide furnace 5
Outlet connection, the lower part outlet of the second end of first carbide furnace 5 and the top of the second end of second carbide furnace 6 enter
The upper entrance of the first end of mouth connection, the lower part outlet of the first end of second carbide furnace 6 and the third carbide furnace 7 connects
It connects, the lower part outlet of the second end of the third carbide furnace 7 is connect with discharging mechanism.The continuous anaerobic carbonization operation of the superheated steam
Device is, it can be achieved that carry out superheated steam anaerobic carbonization, and the continuous anaerobic carbonization operation dress of the superheated steam to organic waste
The mutual cooperation between the first carbide furnace, the second carbide furnace, third carbide furnace by setting is set, it can be thorough by three-level carbonization
Smooth, the smooth execution of the bottom realization continuous anaerobic carbonization of superheated steam.
It is worth noting that the continuous anaerobic carbonization running gear of the present embodiment superheated steam is not limited to medicine intermediate, agriculture
With high salt, the high-COD waste water generated in the intermediates production processes such as medicine intermediate, printing and dyeing intermediate, food processing, handles generation
Organic carbon processing in (derivative) high COD slag salt, also includes the electronic wastes, dirt such as mobile phone, electric wire, cable, wiring board
The carbonization treatment of the intermediate organic matter such as mud, greasy filth.
Preferably, the present embodiment further include: feed mechanism.The feed mechanism includes: storage bin 1, bucket elevator 2 and feeding
Channel 3, the storage bin 1 are set to the bottom of the bucket elevator 2, and the bucket elevator 2 is used for the organic waste in storage bin 1
Object is promoted to the import of the feeding passage 3.According to the material of mentioned different characteristics, the bucket elevator 2 can also use scrapper conveyor
Or pipe chain machine substitution.
Preferably, the present embodiment further include: discharging mechanism.The discharging mechanism includes: cooling device and discharging device, institute
State the periphery that cooling device is set to the discharging device.
The present embodiment is to guarantee the continuous anaerobic carbonization organic matter of superheated steam, is specifically designed this feeding in continuous material carbide furnace and connects
The structure type of continuous work, continuous coo1ing discharging.It is steamed moreover, organic waste can be made to realize by three-level carbonization with overheat
Vapour comes into full contact with, the operation of the continuous anaerobic carbonization of the superheated steam that follows through.As it can be seen that the present embodiment is from 1 feeding of storage bin to carbon
All transmissions that discharge after change are frequency control feeding, to ensure that the continuous operation of material really, to follow through
Smooth, the smooth execution of the continuous anaerobic carbonization of hot steam.
In the present embodiment, it is preferable that the superheated steam pipeline assembly includes: superheated steam general pipeline 13, superheated steam branch
Pipe, exhaust main 14 and exhaust branch pipe；The superheated steam general pipeline 13 is by each superheated steam branch pipe respectively with described first
Carbide furnace 5, the second carbide furnace 6, third carbide furnace 7 connect, the exhaust main 14 by each exhaust branch pipe respectively with it is described
First carbide furnace 5, the second carbide furnace 6, third carbide furnace 7 connect.
Preferably, the exhaust branch pipe includes first exhaust branch pipe 141, second exhaust branch pipe 142 and third exhaust branch pipe
143, the first exhaust branch pipe 141 is connected to the middle part of first carbide furnace 5, and the second exhaust branch pipe 142 is connected to
The middle part of second carbide furnace 6, the third exhaust branch pipe 143 are connected to the middle part of third carbide furnace 7；The superheated steam
Branch pipe includes: the first superheated steam branch pipe 131, the second superheated steam branch pipe 132 and third superheated steam branch pipe 133, and described
One superheated steam branch pipe 131 is connected to the middle part of first carbide furnace 5, and the second superheated steam branch pipe 132 is connected to institute
The middle part of the second carbide furnace 6 is stated, the third superheated steam branch pipe 133 is connected to the middle part of third carbide furnace 7.
Preferably, the exhaust branch pipe is also designed to following scheme: be connected to each layer of carbide furnace front end or
End.The superheated steam branch pipe is also designed to following scheme: being connected to the front end or end of each layer of carbide furnace.
Preferably, certainly, exhaust branch pipe and superheated steam branch pipe can be independently arranged, can also gathers together and sets
Set, such as: exhaust branch pipe and superheated steam branch pipe can be set in one (such as: superheated steam branch pipe is located at center, and exhaust is propped up
Pipe coaxial package is in the periphery of superheated steam branch pipe).The organic matter in high organic matter or other materials in slag salt passes through first
Carbide furnace 5, the second carbide furnace 6, third carbide furnace 7, come into full contact with superheated steam, the organic exhaust gas warp after anaerobic carbonization cracking
It crosses exhaust branch pipe and imports exhaust main 14, be extracted at rear end deodorization stove high-temperature oxydation and cleaning using the centrifugal blower of exhaust emissions
Reason.
Preferably, first carbide furnace 5, the second carbide furnace 6, third carbide furnace 7 pass through the realization pair of frequency conversion speed-down machine
Its feeding main shaft is controlled.Preferably, the discharging device includes: water cooling stirring cage or lag cooler；The number of the water cooling stirring cage
Amount is one or more；The quantity of the lag cooler is one or more.Preferably, the water cooling stirring cage includes: water cooling
But set 92 and discharging stirring cage 91, the water(-cooling) jacket 92 are set in the discharging stirring cage 91, the first end of the water(-cooling) jacket 92
Bottom be provided with water inlet pipe, the top of the second end of the water(-cooling) jacket 92 is provided with outlet pipe.Preferably, the water is cooling
The quantity of set 92 is one or more, and multiple water(-cooling) jackets 92 are arranged at intervals at the discharging stirring cage 91.
Preferably, the bucket elevator 2 includes: scrapper conveyor or pipe chain machine.Preferably, the feeding passage 3 includes: updip
Access ramp, lower ramp way and augers 4；The entrance of the augers 4 is connect with the upper ramp way, described
The outlet of augers 4 and the lower ramp way；The upper ramp way is connect with the top of the bucket elevator 2, described
Lower ramp way is connect with the entrance of first carbide furnace 5.
Preferably, the carbide furnace operating unit further include: rack 8；Be provided in the rack 8 first load carrier,
Second load carrier and third load carrier are provided with first carbide furnace 5 on first load carrier, and described second holds
It is provided with second carbide furnace 6 on mounted mechanism, the third carbide furnace 7 is provided on the third load carrier.Preferably,
Diagonal brace 10 is provided in the rack 8.
Preferably, the continuous anaerobic carbonization running gear of the superheated steam further include: ladder 11, the ladder 11 have three layers
Ladder structure, has a half space between adjacent ladder structure, and the ladder 11 is set to the side of the rack 8.
Preferably, the angle of every layer of ladder structure and horizontal plane is 30 DEG C to 45 DEG C.
Preferably, the continuous anaerobic carbonization running gear of the superheated steam further include: be set to 11 side of ladder fence and
The fence 12 of each layer of carbide furnace mounting platform surrounding；The fence 12 includes: railing and jack base, and the railing is set to institute
It states on jack base.
Preferably, the shell of each carbide furnace includes furnace body shell and furnace body inner casing, the furnace body shell and the furnace body
The inside air flue for being connected with superheated steam branch pipe is formed between inner casing.
Preferably, the internal air flue is provided with several stomatas along its length.
Preferably, each carbonization furnace body can not also designed enclosures, add insulating layer outside inner casing, guarantee enclosure interior work
It is minimized as temperature losses.Superheated steam air intake branch is directly installed in the inner casing of every layer of carbide furnace.
Preferably, each carbide furnace can also use double-screw type with single screw.
Such as: carbide furnace includes: furnace body shell, furnace body inner casing, the first output shaft, the second output shaft, gear-box, shaft coupling
The mechanical, electrical machine of device, frequency conversion speed-down；It is formed between the furnace body shell and the furnace body inner casing for being connected with superheated steam branch pipe
Internal air flue, the internal air flue are provided with several stomatas along its length.The motor passes through frequency conversion speed-down machine, shaft coupling
Device is connect with gear-box, and the gear-box exports axis connection, first output shaft and second with the first output shaft, second respectively
Output axis connection is located in the furnace body inner casing, and the two rotates synchronously.It is set on first output shaft, the second output shaft
It is equipped with helical blade structure.
In order to more thoroughly realize that organic waste comes into full contact with superheated steam.
Such as: it is provided between furnace body shell, furnace body inner casing in annular space (channel), which may act as logical in air inlet
Road, the corresponding superheated steam branch pipe connection of the inlet channel.The side (close to the side of discharge port) of the furnace body inner casing is set
It is equipped with gas outlet, which connect with exhaust branch pipe.Certainly, the inner surface of inlet channel is provided with several air inlets.
Certainly, the set-up mode of air inlet can there are many.Such as: the distribution of air inlet from its feed end to discharge end by
It is decrescence few.Another example is: the distribution of air inlet is in the small Normal Distribution Model of the sum of big, the both sides sectional area of the sum of intermediate cross-section product,
Its sectional area distribution function is as follows:
Wherein, f (x) is unit breathing area distribution function；If central point in inlet channel axial direction is origin, x be from
The coordinate value extended in the middle part of inlet channel to its both ends；Wherein, π is pi；Wherein, σ is related with the partial size D of material.The σ is
0.15D-0.55D.Superheated steam can in this way realized maximum at the middle part of middle part furnace chamber, be come into full contact with.
Embodiment two
Second aspect, the utility model also provide a kind of according to the continuous anaerobic carbonization operation dress of superheated steam recited above
The method set comprising:
Superheated steam is respectively enterd into the first carbide furnace 5, the second carbide furnace 6, third carbon using superheated steam pipeline assembly
Change furnace 7 to start to feed intake when temperature rises to 300 to 500 DEG C to preheat each carbide furnace.
The organic waste in storage bin 1 is promoted using bucket elevator 2, bucket elevator 2 is using in variable frequency regulating speed control
Expect speed, bucket elevator 2 promotes material and puts by charging line to feeding screw, and feeding screw will using variable frequency regulating speed control
Organic waste puts into the first carbide furnace 5, and the carbonization material of the first carbide furnace 5 is promoted by frequency conversion speed-down machine, and with overheat
Steam comes into full contact with, is carbonized, and is delivered to the second carbide furnace 6, the carbide of the second carbide furnace 6 by the material that first-stage preliminary is carbonized
Material is promoted by frequency conversion speed-down machine, and is come into full contact with, is carbonized with superheated steam, is delivered to the by the material that second level is sufficiently carbonized
The carbonization material of three carbide furnaces 7, third carbide furnace 7 is promoted by frequency conversion speed-down machine, and is come into full contact with, is carbonized with superheated steam,
The material being thoroughly carbonized by three-level discharges by the frequency control of Blowing stopper 71, and the material after carbonization is sent to discharging mechanism；
All transmissions that discharge after feed bin feeding to carbonization are frequency control feeding, thus ensure that the continuous operation of material really,
To smooth, the smooth execution for the continuous anaerobic carbonization of superheated steam that follows through.
Using discharging mechanism by the high-temperature material water-cooled cooling after carbonization to 80 DEG C hereinafter, cooling after material bagging or throwing
Enter to hopper or collector.
Finally, it should be noted that the above various embodiments is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should
Understand: it is still possible to modify the technical solutions described in the foregoing embodiments, or to some or all of
Technical characteristic is equivalently replaced；And these are modified or replaceed, it does not separate the essence of the corresponding technical solution, and this is practical new
The range of each embodiment technical solution of type.
Claims (10)
1. a kind of continuous anaerobic carbonization running gear of superheated steam characterized by comprising superheated steam pipeline assembly and from upper
The first carbide furnace, the second carbide furnace, the third carbide furnace set gradually under and；The top of the first end of first carbide furnace enters
Mouth is for inputting material to be processed, the lower part outlet of the second end of first carbide furnace and the second of second carbide furnace
The upper entrance at end connects, and the lower part outlet of the first end of second carbide furnace is upper with the first end of the third carbide furnace
The connection of portion's entrance, the lower part outlet of the second end of the third carbide furnace are used to export the material after carbonization；The superheated steam
Pipeline assembly includes: superheated steam general pipeline, superheated steam branch pipe, exhaust main and exhaust branch pipe；The superheated steam general pipeline is logical
It crosses each superheated steam branch pipe to connect with first carbide furnace, the second carbide furnace, third carbide furnace respectively, the exhaust main
It is connect respectively with first carbide furnace, the second carbide furnace, third carbide furnace by each exhaust branch pipe.
2. the continuous anaerobic carbonization running gear of superheated steam according to claim 1, which is characterized in that the exhaust branch pipe
Including first exhaust branch pipe, second exhaust branch pipe and third exhaust branch pipe, the first exhaust branch pipe is connected to first carbon
Change the middle part of furnace, the second exhaust branch pipe is connected to the middle part of second carbide furnace, and the third exhaust branch pipe is connected to
The middle part of third carbide furnace；The superheated steam branch pipe includes: the first superheated steam branch pipe, the second superheated steam branch pipe and third
Superheated steam branch pipe, the first superheated steam branch pipe are connected to the middle part of first carbide furnace, second superheated steam
Branch pipe is connected to the middle part of second carbide furnace, and the third superheated steam branch pipe is connected to the middle part of third carbide furnace.
3. the continuous anaerobic carbonization running gear of superheated steam according to claim 2, which is characterized in that first carbonization
Furnace, the second carbide furnace, third carbide furnace pass through the realization of frequency conversion speed-down machine respectively and control its feeding main shaft.
4. the continuous anaerobic carbonization running gear of superheated steam according to claim 1, which is characterized in that further include: rack；
It is provided with the first load carrier, the second load carrier and third load carrier in the rack, is set on first load carrier
It is equipped with first carbide furnace, is provided with second carbide furnace on second load carrier, on the third load carrier
It is provided with the third carbide furnace.
5. the continuous anaerobic carbonization running gear of superheated steam according to claim 4, which is characterized in that further include: ladder,
The ladder has three layers of ladder structure, has a half space between adjacent ladder structure, the ladder is set to the machine
The side of frame.
6. the continuous anaerobic carbonization running gear of superheated steam according to claim 5, which is characterized in that every layer of ladder structure
Angle with horizontal plane is 30 DEG C to 45 DEG C.
7. the continuous anaerobic carbonization running gear of superheated steam according to claim 5, which is characterized in that first carbonization
The upper entrance of the first end of furnace is connect with feed mechanism, the lower part outlet and discharging mechanism of the second end of the third carbide furnace
Connection.
8. the continuous anaerobic carbonization running gear of superheated steam according to claim 7, which is characterized in that the feed mechanism
It include: storage bin, bucket elevator and feeding passage, the storage bin is set to the bottom of the bucket elevator, and the bucket elevator is used for
Treating material in storage bin is promoted to the import of the feeding passage, the feeding passage include: upper ramp way, under
Ramp way and augers；The entrance of the augers is connect with the upper ramp way, the augers
Outlet and the lower ramp way；The upper ramp way is connect with the top of the bucket elevator, the lower ramp way with
The entrance of first carbide furnace connects.
9. the continuous anaerobic carbonization running gear of superheated steam according to claim 8, which is characterized in that the bucket elevator packet
It includes: scrapper conveyor or pipe chain machine.
10. the continuous anaerobic carbonization running gear of superheated steam according to claim 7, which is characterized in that the discharging machine
Structure includes: water cooling stirring cage or lag cooler；The quantity of the water cooling stirring cage is one or more；The quantity of the lag cooler is one
It is a or multiple.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201822254900.5U CN209568062U (en) | 2018-12-29 | 2018-12-29 | The continuous anaerobic carbonization running gear of superheated steam |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201822254900.5U CN209568062U (en) | 2018-12-29 | 2018-12-29 | The continuous anaerobic carbonization running gear of superheated steam |
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| CN201822254900.5U Active CN209568062U (en) | 2018-12-29 | 2018-12-29 | The continuous anaerobic carbonization running gear of superheated steam |
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Effective date of registration: 20231201 Address after: 225400 Hanzhuang Road, Huangqiao Industrial Park, Taizhou City, Jiangsu Province Patentee after: Jiangsu Blue Green Environmental Protection Technology Co.,Ltd. Address before: Hanzhuang Road, Huangqiao Economic Development Zone, Taixing City, Taizhou City, Jiangsu Province, 225411 Patentee before: JIANGSU YIER PLASMA SCIENCE & TECHNOLOGY Co.,Ltd. |
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