CN206858484U - A kind of anaerobic pyrolysis gasification domestic garbage treating system - Google Patents
A kind of anaerobic pyrolysis gasification domestic garbage treating system Download PDFInfo
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- CN206858484U CN206858484U CN201720714600.3U CN201720714600U CN206858484U CN 206858484 U CN206858484 U CN 206858484U CN 201720714600 U CN201720714600 U CN 201720714600U CN 206858484 U CN206858484 U CN 206858484U
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- pyrolysis
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- residue
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- pyrolysis chamber
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Abstract
It the utility model is related to a kind of anaerobic pyrolysis gasification domestic garbage treating system, including feed mechanism, vavuum pump, pyrolysis chamber, microwave catalysis cracking room, residue room, in addition to gas condensed device and pressurized storage tank；The pyrolysis chamber connects vavuum pump, and the solid material in the feed mechanism enters the pyrolysis chamber vacuumized, after being pyrolyzed through pyrolysis chamber, produces residue and steam；The residue enters microwave catalysis cracking room through straight-line drainage conduit, and residue room is directly discharged to after cracking；The steam is preserved to pressurized storage tank after the condensation of gas condensed device；The pressurized storage tank divides two-way to export：The burner of the pyrolysis chamber is connected to all the way, and another way is connected to gas turbo-generator set.Not only no pollution discharges the utility model, and using house refuse circulating generation.
Description
Technical field
Debirs processing technology field is the utility model is related to, at specifically a kind of anaerobic pyrolysis gasification house refuse
Reason system.
Background technology
One of the main reason for solid life refuse pollution is puzzlement current social sustainable development.At present, for organic
Solid waste generally use is landfill method or burning method processing.Landfill not only wastes land resource, occupies good farmland, Er Qiehui
Generation contains a large amount of pollutants；And burning facility one-time investment is big, operating cost is high outer, and it usually requires that solid waste has ratio
Higher calorific value.These traditional processing methods can not effectively handle solid waste, it is difficult to reach solid pollutant preventing and treating and " subtract
The target of quantization, innoxious, recycling ", moreover, can not be recycled.
Utility model content
In view of the above-mentioned problems, the utility model provides a kind of no pollution discharge and using house refuse circulating generation
Anaerobic pyrolysis gasification domestic garbage treating system.
Technical scheme is used by the utility model solves above-mentioned technical problem：A kind of anaerobic pyrolysis gasification house refuse
Processing system, including feed mechanism, vavuum pump, pyrolysis chamber, microwave catalysis cracking room, residue room, in addition to gas condensed device and
Pressurized storage tank；The pyrolysis chamber connects vavuum pump, and the solid material in the feed mechanism enters the pyrolysis chamber vacuumized, warp
After pyrolysis chamber's pyrolysis, residue and steam are produced；The residue enters microwave catalysis cracking room through straight-line drainage conduit, straight after cracking
Connect and be emitted into residue room；The steam is preserved to pressurized storage tank after the condensation of gas condensed device；The pressurized storage tank point
Two-way exports：The burner of the pyrolysis chamber is connected to all the way, and another way is connected to gas turbo-generator set.
Preferably, the feed mechanism includes an infundibulate hopper, the hopper top is provided with charging aperture, and bottom is set
There is discharging opening, be provided with agitating shaft and cutter in hopper, the hopper is connected by discharging opening with pyrolysis chamber.
Preferably, the pyrolysis chamber includes pyrolysis preheating chamber and the pyrolysis hot room being connected with the pyrolysis preheating chamber, institute
State hopper discharging opening to connect with pyrolysis preheating chamber, the pyrolysis hot room is communicated to the straight-line drainage conduit.
Preferably, the pyrolysis hot room includes horizontal-type pusher pipe, spiral propeller, pot arch and burner, institute
State and enter to the horizontal-type pusher pipe at pan feeding of the solid material through horizontal-type pusher pipe in pyrolysis preheating chamber, in the spiral shell
Under the promotion for revolving propeller, the solid material at pan feeding is advanced at the discharging of the horizontal-type pusher pipe, then in Action of Gravity Field
Under fall into straight-line drainage conduit, the burner and be connected with pot arch, pot arch is to the solid in the horizontal-type pusher pipe
Material is heated.
Preferably, the straight-line drainage conduit is vertically arranged with horizontal-type pusher pipe.
Compared with prior art, the utility model has the advantages that：
1st, the invention is fast to the processing speed of house refuse, efficiency high, and can accomplish that no pollution discharges, and can thoroughly eliminate
Foul smell,；
2nd, the invention can produce high-quality natural gas power, cannot be only used for providing power to the burner of pyrolysis chamber,
The power of whole system is circulated, without powering by exterior power, and can be used for being supplied with group of motors to each
Electricity；
3rd, the setting of the vavuum pump can vacuumize pyrolysis chamber, so that pyrolysis chamber's anaerobic pyrolysis, is advantageous to improve
Efficiency is pyrolyzed, meanwhile, avoid producing waste gas；
4th, the agitating shaft and cutter set in the hopper is advantageous to that the solid material in hopper is stirred and cut
Cut, make the larger solid material of volume is convenient to fall into pyrolysis chamber from discharging opening, to be fully pyrolyzed；
5th, the residue that the setting of the straight-line drainage conduit facilitates pyrolysis chamber to discharge more efficiently is fallen into microwave catalysis point
Room is solved, solves easily to block pipeline using the residue caused by horizontally-arranged drainage conduit in the prior art, and need power to arrange
The problem of going out.
Brief description of the drawings
Fig. 1 is a kind of structural representation of preferred embodiment of the utility model.
Embodiment
The utility model is described in detail below in conjunction with Fig. 1, herein illustrative examples and explanation of the present utility model
For explaining the utility model, but it is not intended as to restriction of the present utility model.
A kind of anaerobic pyrolysis gasifies domestic garbage treating system, including feed mechanism 1, vavuum pump 2, pyrolysis chamber, microwave are urged
Change cracking room 6, residue room 7, in addition to gas condensed device 8 and pressurized storage tank 9；The pyrolysis chamber connects vavuum pump 2, it is described on
Expect that in-house solid material enters the pyrolysis chamber vacuumized, after being pyrolyzed through pyrolysis chamber, produce residue and steam；The residue warp
Straight-line drainage conduit 5 enters microwave catalysis cracking room 6, and residue room 7 is directly discharged to after cracking；The steam is through gas condensed device
Preserved after 8 condensations to pressurized storage tank 9；The pressurized storage tank divides two-way to export：The combustion of the pyrolysis chamber is connected to all the way
Burner 44, another way are connected to gas turbo-generator set 10.The feed mechanism includes an infundibulate hopper, the hopper
Top is provided with charging aperture, and bottom is provided with discharging opening, and agitating shaft and cutter are provided with hopper, and the hopper passes through discharging opening and heat
Solve room connection.When the larger solid material of right volume in hopper, the agitating shaft and cutter are cut to the solid material
Cut and stir, pyrolysis chamber is fallen into from discharging opening so that solid material is convenient, so as to fully be pyrolyzed.
The pyrolysis chamber includes pyrolysis preheating chamber 3 and the pyrolysis hot room being connected with the pyrolysis preheating chamber, and the hopper goes out
Material mouth connects with pyrolysis preheating chamber 3, and the pyrolysis hot room is communicated to the straight-line drainage conduit 5.In the pyrolysis preheating chamber
Temperature be generally 45-200 DEG C, pyrolysis hot room temperature up to 400-750 DEG C.
The pyrolysis hot room includes horizontal-type pusher pipe 41, spiral propeller 42, pot arch 43 and burner 44, described
The horizontal-type pusher pipe is entered at pan feeding of the solid material through horizontal-type pusher pipe in pyrolysis preheating chamber, in the spiral
Under the promotion of propeller, the solid material at pan feeding is advanced at the discharging of the horizontal-type pusher pipe, then under gravity
Fall into straight-line drainage conduit 5, the burner and be connected with pot arch, pot arch is to the solids in the horizontal-type pusher pipe
Material is heated.
The straight-line drainage conduit 5 is vertically arranged with horizontal-type pusher pipe 41.
In implementation process, start vavuum pump 2, pyrolysis chamber is then delivered to solid material in hopper into vacuum state,
Solid material in hopper is fallen into pyrolysis preheating chamber 3, after preheated to 100 DEG C, is entered back into pyrolysis hot room, through pyrolysis plus
After greenhouse pyrolysis, residue and steam are produced.In pyrolysis chamber's pyrolytic process, burner 44 is persistently to the pot arch of pyrolysis hot room
43 are heated, meanwhile, the solid material in horizontal-type pusher pipe 41 is pushed at discharging by spiral propeller 42 at pan feeding, so
Residue is fallen under gravity into straight-line drainage conduit 5 afterwards, is then directly discharged to again after the cracking of microwave catalysis cracking room 6
Residue room 7, brickmaking etc. can be can be used for residue, reusable edible, avoids waste of resource.After the steam purification, a part
Flowed out from tabacco barn 11, another part is condensed through gas condensed device 8, and condensed gas can enter through vacuum extraction valve 12 and add
Air accumulator 9 is pressed, meanwhile, a part of concentrate can be produced after condensation and can be used for gas supply or shunting.The pressurized storage tank 9 divides
Two-way exports：The burner 44 of the pyrolysis chamber is connected to all the way, for providing generation driving force to burner, makes whole system
Power can circulate, and without being powered by exterior power, another way is connected to gas turbo-generator set 10, for combustion
Gas turbine generator group provides power.
The technical scheme provided above the utility model embodiment is described in detail, used herein specifically
Individual example is set forth to the principle and embodiment of the utility model embodiment, and the explanation of above example is only applicable to help
Assistant solves the principle of the utility model embodiment；Meanwhile for those of ordinary skill in the art, implement according to the utility model
Example, the there will be changes in embodiment and application, in summary, this specification content should not be construed as
To limitation of the present utility model.
Claims (5)
- The domestic garbage treating system 1. a kind of anaerobic pyrolysis gasifies, it is characterised in that：Including feed mechanism（1）, vavuum pump（2）、 Pyrolysis chamber, microwave catalysis cracking room（6）, residue room（7）, in addition to gas condensed device（8）And pressurized storage tank（9）；The heat Solve room connection vavuum pump（2）, the solid material in the feed mechanism enters the pyrolysis chamber vacuumized, after being pyrolyzed through pyrolysis chamber, Produce residue and steam；The residue is through straight-line drainage conduit（5）Into microwave catalysis cracking room（6）, directly discharged after cracking To residue room（7）；The steam is through gas condensed device（8）Preserved after condensation to pressurized storage tank（9）It is interior；The pressurized storage tank Divide two-way output：The burner of the pyrolysis chamber is connected to all the way（44）, another way is connected to gas turbo-generator set（10）.
- 2. anaerobic pyrolysis gasification domestic garbage treating system according to claim 1, it is characterised in that：The feed mechanism bag An infundibulate hopper is included, the hopper top is provided with charging aperture, and bottom is provided with discharging opening, agitating shaft and cutting are provided with hopper Device, the hopper are connected by discharging opening with pyrolysis chamber.
- 3. anaerobic pyrolysis gasification domestic garbage treating system according to claim 2, it is characterised in that：The pyrolysis chamber includes It is pyrolyzed preheating chamber（3）The pyrolysis hot room being connected with the pyrolysis preheating chamber, the hopper discharging opening and pyrolysis preheating chamber（3）Even Logical, the pyrolysis hot room is communicated to the straight-line drainage conduit（5）.
- 4. anaerobic pyrolysis gasification domestic garbage treating system according to claim 3, it is characterised in that：The pyrolysis hot room Including horizontal-type pusher pipe（41）, spiral propeller（42）, pot arch（43）And burner（44）, it is described to be pyrolyzed in preheating chamber Solid material enters to the horizontal-type pusher pipe at the pan feeding through horizontal-type pusher pipe, in the promotion of the spiral propeller Under, the solid material at pan feeding is advanced at the discharging of the horizontal-type pusher pipe, is then fallen under gravity into straight-line Drainage conduit（5）, the burner is connected with pot arch, and pot arch adds to the solid material in the horizontal-type pusher pipe Heat.
- 5. anaerobic pyrolysis gasification domestic garbage treating system according to claim 4, it is characterised in that：The straight-line discharge Pipe（5）With horizontal-type pusher pipe（41）It is vertically arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720714600.3U CN206858484U (en) | 2017-06-20 | 2017-06-20 | A kind of anaerobic pyrolysis gasification domestic garbage treating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720714600.3U CN206858484U (en) | 2017-06-20 | 2017-06-20 | A kind of anaerobic pyrolysis gasification domestic garbage treating system |
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| Publication Number | Publication Date |
|---|---|
| CN206858484U true CN206858484U (en) | 2018-01-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720714600.3U Expired - Fee Related CN206858484U (en) | 2017-06-20 | 2017-06-20 | A kind of anaerobic pyrolysis gasification domestic garbage treating system |
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| CN (1) | CN206858484U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CZ307774B6 (en) * | 2017-11-17 | 2019-04-24 | RCM Consult s.r.o. | Microwave reactor |
-
2017
- 2017-06-20 CN CN201720714600.3U patent/CN206858484U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CZ307774B6 (en) * | 2017-11-17 | 2019-04-24 | RCM Consult s.r.o. | Microwave reactor |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200509 Address after: Room 2309, Rongcheng International Plaza, No. 9, Xiangfu Middle Road, Yuhua District, Changsha City, Hunan Province Patentee after: Hunan chuanneng environmental protection Co., Ltd Address before: Tongzi high tech Zone of Hunan province Changsha slope road 410005 No. 185 Hunan Province Public Security Bureau household service center building A room 105 Patentee before: CHANGSHA JIAZHONG ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180109 Termination date: 20200620 |
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| CF01 | Termination of patent right due to non-payment of annual fee |