CN206207422U - Heat scission reaction stove - Google Patents
Heat scission reaction stove Download PDFInfo
- Publication number
- CN206207422U CN206207422U CN201621117686.3U CN201621117686U CN206207422U CN 206207422 U CN206207422 U CN 206207422U CN 201621117686 U CN201621117686 U CN 201621117686U CN 206207422 U CN206207422 U CN 206207422U
- Authority
- CN
- China
- Prior art keywords
- transfer canal
- transfer
- main body
- lower floor
- scission reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 30
- 238000010504 bond cleavage reaction Methods 0.000 title claims abstract description 28
- 230000007017 scission Effects 0.000 title claims abstract description 28
- 238000000197 pyrolysis Methods 0.000 claims abstract description 29
- 230000007246 mechanism Effects 0.000 claims abstract description 25
- 238000007599 discharging Methods 0.000 claims abstract description 8
- 239000000779 smoke Substances 0.000 claims abstract description 6
- 238000011068 loading method Methods 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 10
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 230000010006 flight Effects 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims 1
- 238000004227 thermal cracking Methods 0.000 abstract description 5
- 230000008929 regeneration Effects 0.000 abstract description 4
- 238000011069 regeneration method Methods 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 11
- 239000010813 municipal solid waste Substances 0.000 description 9
- 230000006872 improvement Effects 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000002361 compost Substances 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model provides a kind of heat scission reaction stove, including furnace chamber main body, first transfer canal, second transfer canal, the actuating unit that transfer mechanism and the first transfer canal of driving are rotated, furnace chamber main body includes upper strata hothouse and pyrolysis chamber of lower floor, connected by some smoke ventilators between upper strata hothouse and pyrolysis chamber of lower floor, exhaust opening is provided with the top of the hothouse of upper strata, some gas nozzles are set in pyrolysis chamber of lower floor, first transfer canal crosses upper strata hothouse, one end of first transfer canal sets loading hopper, the other end of the first transfer canal connects one end of the second transfer canal by transfer mechanism, second transfer canal crosses pyrolysis chamber of lower floor, second transfer canal is rotated with the side wall of pyrolysis chamber of lower floor and is connected, the other end connection discharging mechanism of the second transfer canal.The utility model provides a kind of heat scission reaction stove, and it can carry out thermal cracking reformation to house refuse, to realize energy regeneration and be comprehensively utilized without useless.
Description
Technical field
The utility model is related to technical field of domestic garbage treatment, more particularly to a kind of heat scission reaction stove.
Background technology
The harmless treatment of domestic waste and energy shortage problem are one of important topics of current era, current world's model
Interior widely used technology of garbage disposal scheme is enclosed, particularly for organic matter, however it remains the problem for being difficult to overcome, can
It is described below:1st, burning method, the heat on the one hand producing is used to generate electricity and heat, and on the other hand maximum drawback is to burn away the refuse
When produce the pernicious gas such as dioxin, environment is polluted again.The early investment of burning disposal is larger simultaneously, burns relevant device easy
In damage, the replacement cycle is short, and energy conversion efficiency is very low, if to solve environmental issue, corresponding cost is very high, and causing cannot
The situation of profit running.2nd, landfill method, a large amount of garbage leachates are permeated the ground by earth's surface in landfill method, to urban environment and underground water
Severe contamination is caused in source, and takes a large amount of land resources, and also can produce toxic gas, therefore this trash processing way
Limited or cancelled by policy gradually.3rd, composting process, because consumer garbage compost amount is big in composting process, nutrient content is low, for a long time
Polluted using soil and groundwater matter is easily caused, selectivity is strong, many component of refuse cannot be biodegradable, so, the rule of compost
Mould is difficult that too greatly, integrated treatment can not be carried out to rubbish.4th, biological treatment, biological fermentation process once once turned at rubbish
One important exploration of reason, its basic advantage is exactly can be in part with discarded object, the valuable ethanol of output.But fermentation
Some reluctant acid waste liquids can be inherently produced, and production technology efficiency is very low (cycle is long, produces benefit than small), and
There is very strong selectivity to rubbish, this just significantly limit the application of this technique, it is more difficult to largely process day refuse.Generation
Various countries of boundary, especially European countries on several pilot plants, the running in past 10 years, do not have one be profit, be all within
Carried out under the subsidy of government, and be the more simple discarded object of directional process, such as wooden slag, vinasse, sugar residue, the dregs of fat etc..
Utility model content
The purpose of this utility model there are provided a kind of heat scission reaction stove, and it can carry out thermal cracking weight to house refuse
It is whole, to realize energy regeneration and be comprehensively utilized without useless.
What the utility model was realized in:
A kind of heat scission reaction stove, including furnace chamber main body, the first transfer canal, the second transfer canal, transfer mechanism and
The actuating unit for driving first transfer canal to rotate, the furnace chamber main body includes upper strata hothouse and pyrolysis chamber of lower floor, institute
State and connected by some smoke ventilators between upper strata hothouse and the pyrolysis chamber of lower floor, be provided with the top of the upper strata hothouse
Exhaust opening, sets some gas nozzles in the pyrolysis chamber of lower floor, first transfer canal crosses the upper strata hothouse, described
One end of first transfer canal sets loading hopper, and the other end of first transfer canal connects described by the transfer mechanism
One end of second transfer canal, second transfer canal crosses the pyrolysis chamber of lower floor, second transfer canal with it is described
The side wall of pyrolysis chamber of lower floor rotates connection, the other end connection discharging mechanism of second transfer canal.
Used as the improvement of above-mentioned heat scission reaction stove, first transfer canal includes the first pipe main body and drives life
The screw conveyer structure that rubbish living is transmitted in first pipe main body.
Used as the improvement of above-mentioned heat scission reaction stove, second transfer canal includes second pipe main body and is built in
Spiral chip architecture in the second pipe main body, the spiral chip architecture is included due to prolonging one end of the second pipe main body
Some flights of the other end of the second pipe main body are extended, the surface of each flight is provided with some stock guides.
As the improvement of above-mentioned heat scission reaction stove, the also air including being be arranged in parallel with second transfer canal respectively
Pipeline and gas pipeline, one end of the air duct are connected with combustion fan, the air duct and the gas pipeline it
Between be communicated with some connecting tubes, some gas nozzles are distributed in some connecting tubes.
As the improvement of above-mentioned heat scission reaction stove, a blast pipe, the blast pipe are provided with the top of the discharging mechanism
Connect one end of the gas pipeline.
Used as the improvement of above-mentioned heat scission reaction stove, the transfer mechanism includes that the material feeding box being disposed vertically and level are put
The feed sleeve put, the material feeding box connects the other end of first transfer canal, the feed sleeve include first end with
And the second end of connection second transfer canal, the material feeding box is communicated with above the first end with the feeding sleeve
Charging aperture inside cylinder, and the first end is built-in with the movable push driven by hydraulic stem.
Used as the improvement of above-mentioned heat scission reaction stove, the lateral wall of the furnace chamber main body is provided with heat-insulation layer.
The beneficial effects of the utility model are:The heat scission reaction stove that the utility model is provided, it includes furnace chamber main body, the
The actuating unit that one transfer canal, the second transfer canal, transfer mechanism and the first transfer canal of driving are rotated, furnace chamber main body bag
Upper strata hothouse and pyrolysis chamber of lower floor are included, some gas nozzles, some gas nozzle flame burnings, a side are set in pyrolysis chamber of lower floor
Face can heat the temperature in directly pyrolysis chamber of lifting lower floor, on the other hand be able to must be acted in lifting indirectly by some smoke ventilators
Temperature in layer hothouse.During work, house refuse passes through the first transfer canal first, and in the presence of the hothouse of upper strata,
Preliminarily dried treatment is carried out, after finishing, the transfer through transfer mechanism enters the second transfer canal, because the second transfer canal is under
In layer pyrolysis chamber, it has been integrally formed high temperature anaerobic sealed environment, thus, the house refuse after preliminarily dried treatment is the
In two transfer canal transmit process, can progressively produce heat scission reaction, with after the mixture for forming oil, gas and carbide through going out
The discharge of material mechanism.It can be seen that, this heat scission reaction stove, it can carry out thermal cracking reformation to house refuse, with realize energy regeneration and
Without useless comprehensive utilization.
Brief description of the drawings
In order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, before creative labor is not paid
Put, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is a kind of overall structure diagram of preferred embodiment of the utility model heat scission reaction stove.
Specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of the utility model protection.
As shown in figure 1, the present embodiment provides a kind of heat scission reaction stove 1, including furnace chamber main body 11, the first transfer canal
12nd, the actuating unit (not shown) that the second transfer canal 13, transfer mechanism 14 and driving the first transfer canal 14 are rotated, furnace chamber
Main body 11 includes upper strata hothouse 111 and pyrolysis chamber of lower floor 112, leads between the upper strata hothouse 111 and pyrolysis chamber of lower floor 112
Cross some smoke ventilators 113 to connect, the top of upper strata hothouse 111 is provided with exhaust opening 114, pyrolysis chamber of lower floor 112 and sets some
Gas nozzle 151, the first transfer canal 12 crosses upper strata hothouse 111, and one end of the first transfer canal 12 sets loading hopper 16,
The other end of the first transfer canal 12 connects one end of the second transfer canal 13 by transfer mechanism 14, and the second transfer canal 13 is horizontal
Layer pyrolysis chamber 112 is worn, the second transfer canal 13 is rotated with the side wall of pyrolysis chamber of lower floor 112 and is connected, the second transfer canal 112
The other end connects discharging mechanism 17.
In the present embodiment, as shown in figure 1, the first transfer canal 12 includes the first pipe main body and drives house refuse
The screw conveyer structure (not shown) transmitted in the first pipe main body.Second transfer canal 13 includes second pipe main body 131
And the spiral chip architecture 132 in second pipe main body 131 is built in, spiral chip architecture 132 is included due to second pipe main body
131 one end extends to some flights of the other end of second pipe main body 131, and the surface of each flight is provided with some leading
Flitch, actuating unit can be rotary drive motor, to drive the second transfer canal 13 overall in the transfer of pyrolysis chamber of lower floor 112
Dynamic, now, the synchronous axial system of spiral chip architecture 132 in second pipe main body 131 is causing to enter into second pipe main body 131
While interior house refuse is sent to the other end by its one end, house refuse can be synchronized and blend treatment, accelerate pyrolysis
Efficiency, and some stock guides that the surface of flight is set, can play certain guiding and acceleration stirring action.To ensure second
Sealing in pipe main body 131, the joint of second pipe main body 131 and transfer mechanism 14, second pipe main body 131 and goes out
The joint and second pipe main body 131 for expecting mechanism 17 pass through bearing arrangement with the side wall joint of pyrolysis chamber of lower floor 112
Docked with the cooperation of sealing ring.
As shown in figure 1, heat scission reaction stove 1 also includes the air duct being be arranged in parallel with the second transfer canal 13 respectively
152 are connected with combustion fan 154, air duct 152 and gas pipeline 153 with gas pipeline 153, one end of air duct 153
Between be communicated with some connecting tubes 155, some gas nozzles 151 are distributed in some connecting tubes 154.The top of discharging mechanism 17
Be provided with a blast pipe 171, blast pipe 171 connects one end of gas pipeline 153, due to house refuse can be produced after thermal cracking can
Combustion gas body, is comprehensively utilized during these fuel gas are guided into gas pipeline 153 by blast pipe 171, more energy efficient environmental protection.
As shown in figure 1, transfer mechanism 14 includes the feed sleeve 142 of the material feeding box 141 and horizontal positioned being disposed vertically,
Material feeding box 131 connects the other end of the first transfer canal 12, and feed sleeve 142 includes that first end 1421 and connection second are transmitted
Second end 1422 of pipeline 13, the top of first end 1421 is communicated with the charging inside material feeding box 141 and feed sleeve 142
Mouthful, and first end 1421 is built-in with the movable push 144 driven by hydraulic stem 143, during work, is driven by hydraulic stem 143 and lived
Dynamic push pedal 144 is caused in the second transfer canal of house refuse iterative method 13 come in by material feeding box 141.Outside furnace chamber main body 11
Side wall is provided with heat-insulation layer (not shown), to ensure that upper strata hothouse 111 too fast will not flow with the heat in pyrolysis chamber of lower floor 112
Lose.
The present embodiment provide heat scission reaction stove, it include furnace chamber main body, the first transfer canal, the second transfer canal,
The actuating unit that transfer mechanism and the first transfer canal of driving are rotated, furnace chamber main body includes that upper strata hothouse and lower floor are pyrolyzed
Room, sets some gas nozzles in pyrolysis chamber of lower floor, on the one hand some gas nozzle flame burnings can heat directly lifting lower floor heat
Indoor temperature is solved, the temperature in lifting upper strata hothouse indirectly on the other hand can must be acted on by some smoke ventilators.Work
When, house refuse in the presence of the hothouse of upper strata, carries out preliminarily dried treatment first by the first transfer canal, finishes
Afterwards, the second transfer canal is entered through the transfer of transfer mechanism, because the second transfer canal is in pyrolysis chamber of lower floor, it is internal overall
Form high temperature anaerobic sealed environment, thus, preliminarily dried treatment after house refuse in the second transfer canal transmit process,
Heat scission reaction can be progressively produced, to be discharged through discharging mechanism after forming oil, gas and the mixture of carbide.It can be seen that, this heat
Cracking reaction stove, it can carry out thermal cracking reformation to house refuse, to realize energy regeneration and be comprehensively utilized without useless.
Preferred embodiment of the present utility model is the foregoing is only, is not used to limit the utility model, it is all at this
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc. should be included in the utility model
Protection domain within.
Claims (7)
1. a kind of heat scission reaction stove, it is characterised in that including furnace chamber main body, the first transfer canal, the second transfer canal, transfer
The actuating unit that mechanism and driving first transfer canal are rotated, the furnace chamber main body includes upper strata hothouse and lower floor's heat
Solution room, is connected between the upper strata hothouse and the pyrolysis chamber of lower floor by some smoke ventilators, the upper strata hothouse
Top is provided with exhaust opening, and some gas nozzles are set in the pyrolysis chamber of lower floor, and first transfer canal crosses the upper strata and does
Dry room, one end of first transfer canal sets loading hopper, and the other end of first transfer canal is by the transfer machine
Structure connects one end of second transfer canal, and second transfer canal crosses the pyrolysis chamber of lower floor, second transmission
Pipeline is rotated with the side wall of the pyrolysis chamber of lower floor and is connected, the other end connection discharging mechanism of second transfer canal.
2. heat scission reaction stove as claimed in claim 1, it is characterised in that first transfer canal includes the first pipeline master
The screw conveyer structure that body and driving house refuse are transmitted in first pipe main body.
3. heat scission reaction stove as claimed in claim 1, it is characterised in that second transfer canal includes second pipe master
Body and the spiral chip architecture being built in the second pipe main body, the spiral chip architecture are included due to the second pipe
One end of main body extends to some flights of the other end of the second pipe main body, and the surface of each flight is provided with
Some stock guides.
4. heat scission reaction stove as claimed in claim 1, it is characterised in that also including flat with second transfer canal respectively
Air duct and gas pipeline that row is set, one end of the air duct is connected with combustion fan, the air duct and institute
State and be communicated with some connecting tubes between gas pipeline, some gas nozzles are distributed in some connecting tubes.
5. heat scission reaction stove as claimed in claim 4 a, it is characterised in that exhaust is provided with the top of the discharging mechanism
Pipe, the blast pipe connects one end of the gas pipeline.
6. heat scission reaction stove as claimed in claim 1, it is characterised in that the transfer mechanism includes the charging being disposed vertically
The feed sleeve of case and horizontal positioned, the material feeding box connects the other end of first transfer canal, the feed sleeve
The second end including first end and connection second transfer canal, is communicated with the material feeding box above the first end
It is built-in with by the movable push of hydraulic stem driving with the charging aperture inside the feed sleeve, and the first end.
7. heat scission reaction stove as claimed in claim 1, it is characterised in that the lateral wall of the furnace chamber main body is provided with insulation
Layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621117686.3U CN206207422U (en) | 2016-10-12 | 2016-10-12 | Heat scission reaction stove |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621117686.3U CN206207422U (en) | 2016-10-12 | 2016-10-12 | Heat scission reaction stove |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206207422U true CN206207422U (en) | 2017-05-31 |
Family
ID=58761015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201621117686.3U Expired - Fee Related CN206207422U (en) | 2016-10-12 | 2016-10-12 | Heat scission reaction stove |
Country Status (1)
Country | Link |
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CN (1) | CN206207422U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107987563A (en) * | 2018-01-29 | 2018-05-04 | 刁英健 | A kind of device and its production technology using tar slag production carbon black |
CN108329938A (en) * | 2018-02-11 | 2018-07-27 | 湖南尚威新能源环保有限公司 | A kind of horizontal double-tube destructive distillation refuse disposal installation |
CN108709187A (en) * | 2018-06-05 | 2018-10-26 | 江苏天楹环保能源成套设备有限公司 | A kind of domestic waste incineration feed hopper arch breaking apparatus |
CN110566974A (en) * | 2019-09-16 | 2019-12-13 | 谢樱 | Novel pyrolysis device |
-
2016
- 2016-10-12 CN CN201621117686.3U patent/CN206207422U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107987563A (en) * | 2018-01-29 | 2018-05-04 | 刁英健 | A kind of device and its production technology using tar slag production carbon black |
CN108329938A (en) * | 2018-02-11 | 2018-07-27 | 湖南尚威新能源环保有限公司 | A kind of horizontal double-tube destructive distillation refuse disposal installation |
CN108709187A (en) * | 2018-06-05 | 2018-10-26 | 江苏天楹环保能源成套设备有限公司 | A kind of domestic waste incineration feed hopper arch breaking apparatus |
CN110566974A (en) * | 2019-09-16 | 2019-12-13 | 谢樱 | Novel pyrolysis device |
CN110566974B (en) * | 2019-09-16 | 2024-05-31 | 谢樱 | Novel pyrolysis device |
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Legal Events
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170531 |