CN107243503A - A kind of organic solid waste pyrolysis waste residue recycle device and method - Google Patents
A kind of organic solid waste pyrolysis waste residue recycle device and method Download PDFInfo
- Publication number
- CN107243503A CN107243503A CN201710559901.8A CN201710559901A CN107243503A CN 107243503 A CN107243503 A CN 107243503A CN 201710559901 A CN201710559901 A CN 201710559901A CN 107243503 A CN107243503 A CN 107243503A
- Authority
- CN
- China
- Prior art keywords
- ash
- water cooling
- high temperature
- lime
- shaft conveyor
- 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.)
- Pending
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 23
- 239000002910 solid waste Substances 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims abstract description 13
- 238000000197 pyrolysis Methods 0.000 title claims description 12
- 238000001816 cooling Methods 0.000 claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 14
- 238000002485 combustion reaction Methods 0.000 claims abstract description 14
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000002184 metal Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 4
- 239000003610 charcoal Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000002296 pyrolytic carbon Substances 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims description 3
- 230000008929 regeneration Effects 0.000 claims 1
- 238000011069 regeneration method Methods 0.000 claims 1
- 238000011084 recovery Methods 0.000 abstract description 5
- 239000002689 soil Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 239000000428 dust Substances 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
- 239000003570 air Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000002921 fermentation waste Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000010563 solid-state fermentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/02—Heating arrangements using combustion heating
Abstract
Waste residue recycle device is pyrolyzed the invention discloses a kind of organic solid waste, it is characterised in that：Including the first water cooling non-shaft conveyor, high temperature ash can, the second water cooling non-shaft conveyor, lime-ash processor, ash can, powdered carbon combustion device, the first water cooling non-shaft conveyor is connected with high temperature ash can, the outlet of the high temperature ash can is connected with the second water cooling non-shaft conveyor, the second water cooling non-shaft conveyor is connected to the charging aperture of lime-ash processor, the discharging opening connection of the lime-ash processor and ash can；Conveyer is provided with the ash can and powdered carbon combustion device is connected to；With reference to the device, the invention also discloses a kind of recoverying and utilizing method of waste residue.The technical scheme that the present invention is provided has compared with much progress compared with for prior art, is mainly reflected in：Recovery degree height, not waste of resource.
Description
Technical field
The present invention relates to the recovery profit of a kind of retracting device and recovery method, more particularly to a kind of organic solid waste pyrolysis waste residue
Use device and method.
Background technology
The harmful solid waste of China year yield at 15,000,000 tons or so, harmful solid waste can penetrate into soil in soil after weathering
Earth, destroys the corrosion capacity of decomposition of soil；The solid waste of long-term outdoor placement can be volatilized substantial amounts of waste gas and dust, and air is caused
Severe contamination etc., solid waste pollution problem has caused the attention of society.
The processing to chemical solid waste mainly uses the mode such as landfill, biological treatment after burning at present.Burning process lack
On the one hand point is that cost is high, and flying dust (harmful components containing dioxin), the stench on the other hand produced therewith also brings along secondary dirt
Dye.China is in the stage of urbanization rate fast lifting, and urban land has been scarce resource, and filling needs large area
Secondary pollution problem after soil, landfill is also very serious.
Pyrolytic technique is a kind of dangerous waste treatment technology of novel environment friendly, compared with for conventional art have larger progressive；
But still there is certain destruction to environment in the waste residue produced after Non-oxygen pyrolytic, in addition, in pyrolysis waste residue it is main into
It is divided into powdered carbon, higher calorific value is had according to it, after certain metal ingredient is contained in removing waste residue, can be provided for drying
Metal in thermal source, organic solid waste isolates rear reproducible utilization.
The content of the invention
To solve Solid state fermentation waste of resource in existing pyrolytic technique, not environmentally friendly enough shortcoming, the invention provides
A kind of organic solid waste pyrolysis waste residue recycle device simple in construction, being easy to popularization, in addition, with reference to the recycle device also
There is provided a set of corresponding recoverying and utilizing method.
The present invention concrete technical scheme be：
A kind of organic solid waste is pyrolyzed waste residue recycle device, it is characterised in that：Including the first water cooling non-shaft conveyor, height
Warm ash can, the second water cooling non-shaft conveyor, lime-ash processor, ash can, powdered carbon combustion device, the first water cooling non-shaft conveyor with
High temperature ash can is connected, and the outlet of the high temperature ash can is connected with the second water cooling non-shaft conveyor, the shaftless conveying of the second water cooling
Machine is connected to the charging aperture of lime-ash processor, the discharging opening connection of the lime-ash processor and ash can；Provided with defeated in the ash can
Send device and be connected to powdered carbon combustion device.
A kind of organic solid waste is pyrolyzed waste residue recoverying and utilizing method, it is characterised in that：Organic solid waste pyrolysis system is periodically discharged
High temperature charcoal ash, to ensure the treating capacity of production, pyrolysis system ash discharge is shorter to the time of high temperature ash can, shaftless by the first water cooling
Conveyer carries out entering high temperature ash can after just cooling down, and using the time in ash discharge cycle, high temperature ash can is shaftless defeated by the second water cooling
Machine is sent to cool down laggard ash charge Slag treatment device, the metal after the processing of lime-ash processor in discharge pyrolytic carbon ash, ash content enters ash can, so
After be transported to powdered carbon combustion device burning after, be drying system heat supply, metal export trade.
The technical scheme that the present invention is provided has compared with much progress compared with for prior art, is mainly reflected in：Recovery degree height,
Do not waste, it is possible to achieve final zero " waste residue " discharge.
Brief description of the drawings
Fig. 1 is the structural representation that a kind of organic solid waste that the present invention is provided is pyrolyzed waste residue recycle device
Identified in figure：
1. the first water cooling non-shaft conveyor；2. high temperature ash can；3. the second water cooling non-shaft conveyor；4. lime-ash processor；5.
Ash can；6. powdered carbon combustion device.
Embodiment
Waste residue recycle device is pyrolyzed to a kind of disclosed organic solid waste below in conjunction with drawings and Examples
And method is further explained.
A kind of organic solid waste pyrolysis waste residue recycle device as shown in Figure 1, including the first water cooling non-shaft conveyor 1,
High temperature ash can 2, the second water cooling non-shaft conveyor 3, lime-ash processor 4, ash can 5, powdered carbon combustion device 6, first water cooling are shaftless
Conveyer 1 is connected with high temperature ash can 2, and the outlet of the high temperature ash can 2 is connected with the second water cooling non-shaft conveyor 3, described second
Water cooling non-shaft conveyor 3 is connected to the charging aperture of lime-ash processor 4, discharging opening connection and the ash can 5 of the lime-ash processor 4；
Conveyer is provided with the ash can 5 and powdered carbon combustion device 6 is connected to.
Waste residue recycle device is pyrolyzed with reference to above-mentioned organic solid waste, the waste residue recoverying and utilizing method that the present invention is provided includes
Following steps：
Organic solid waste pyrolysis system periodically discharges high temperature charcoal ash, and to ensure the treating capacity of production, pyrolysis system ash discharge is paramount
The time of warm ash can is shorter, enters high temperature ash can 2 after the first water cooling non-shaft conveyor 1 just cool down, and utilizes ash discharge week
The time of phase, high temperature ash can 2 is cooled down at laggard ash charge Slag treatment device 4, lime-ash processor 4 by the second water cooling non-shaft conveyor 3
The metal in pyrolytic carbon ash is discharged after reason, ash content enters ash can 5, be then delivered to after the burning of powdered carbon combustion device 6, be drying system
Heat supply, regenerated metal.
First and last, this recycle device is simple in construction, be easy to popularization, more environmental protection, and powdered carbon combustion device will remove gold
The waste residue of category carries out combustion heat supplying, saves the energy；The metal export trade of recovery, economizes on resources.
Above example is the explanation of the embodiment to the present invention, rather than limitation of the present invention, relevant technology
The technical staff in field without departing from the spirit and scope of the present invention, can also make various conversion and change and obtain
To corresponding equivalent technical scheme, therefore all equivalent technical schemes should be included into the patent protection model of the present invention
Enclose.
Claims (2)
1. a kind of organic solid waste is pyrolyzed waste residue recycle device, it is characterised in that：Including the first water cooling non-shaft conveyor, high temperature
Ash can, the second water cooling non-shaft conveyor, lime-ash processor, ash can, powdered carbon combustion device, the first water cooling non-shaft conveyor and height
Warm ash can is connected, and the outlet of the high temperature ash can is connected with the second water cooling non-shaft conveyor, the second water cooling non-shaft conveyor
It is connected to the charging aperture of lime-ash processor, the discharging opening connection of the lime-ash processor and ash can；Provided with conveying in the ash can
Device is simultaneously connected to powdered carbon combustion device.
2. a kind of organic solid waste is pyrolyzed waste residue recoverying and utilizing method, it is characterised in that：Organic solid waste pyrolysis system periodically discharges height
Warm charcoal ash, to ensure the treating capacity of production, pyrolysis system ash discharge is shorter to the time of high temperature ash can, shaftless defeated by the first water cooling
Machine is sent to carry out entering high temperature ash can after just cooling down, using the time in ash discharge cycle, high temperature ash can passes through the shaftless conveying of the second water cooling
Machine cools down laggard ash charge Slag treatment device, and the metal after the processing of lime-ash processor in discharge pyrolytic carbon ash, ash content enters ash can, then
It is transported to after the burning of powdered carbon combustion device, is drying system heat supply, old metal regeneration.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710559901.8A CN107243503A (en) | 2017-07-11 | 2017-07-11 | A kind of organic solid waste pyrolysis waste residue recycle device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710559901.8A CN107243503A (en) | 2017-07-11 | 2017-07-11 | A kind of organic solid waste pyrolysis waste residue recycle device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107243503A true CN107243503A (en) | 2017-10-13 |
Family
ID=60015165
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710559901.8A Pending CN107243503A (en) | 2017-07-11 | 2017-07-11 | A kind of organic solid waste pyrolysis waste residue recycle device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107243503A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5728196A (en) * | 1994-07-13 | 1998-03-17 | Institut Francais Du Petrole | Process for waste thermolysis |
| CN1234106A (en) * | 1996-10-22 | 1999-11-03 | 特雷德克公司 | Plant for thermolysis and energetic upgrading of waste products |
| CN104976622A (en) * | 2015-08-05 | 2015-10-14 | 中国东方电气集团有限公司 | Household garbage classified gasification system with rotary kiln gasification and plasma fusion capability |
| CN106595321A (en) * | 2016-12-30 | 2017-04-26 | 浙江天禄环境科技有限公司 | Gas locking and carbon discharging separating and cooling device for biological carbon prepared via reduction and gasification |
| CN106623338A (en) * | 2015-10-28 | 2017-05-10 | 格林美股份有限公司 | Waste circuit board harmless treatment method and waste circuit board harmless treatment apparatus |
| CN207308549U (en) * | 2017-07-11 | 2018-05-04 | 盐城绿城环保科技有限公司 | A kind of organic solid waste is pyrolyzed waste residue recycle device |
-
2017
- 2017-07-11 CN CN201710559901.8A patent/CN107243503A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5728196A (en) * | 1994-07-13 | 1998-03-17 | Institut Francais Du Petrole | Process for waste thermolysis |
| CN1234106A (en) * | 1996-10-22 | 1999-11-03 | 特雷德克公司 | Plant for thermolysis and energetic upgrading of waste products |
| CN104976622A (en) * | 2015-08-05 | 2015-10-14 | 中国东方电气集团有限公司 | Household garbage classified gasification system with rotary kiln gasification and plasma fusion capability |
| CN106623338A (en) * | 2015-10-28 | 2017-05-10 | 格林美股份有限公司 | Waste circuit board harmless treatment method and waste circuit board harmless treatment apparatus |
| CN106595321A (en) * | 2016-12-30 | 2017-04-26 | 浙江天禄环境科技有限公司 | Gas locking and carbon discharging separating and cooling device for biological carbon prepared via reduction and gasification |
| CN207308549U (en) * | 2017-07-11 | 2018-05-04 | 盐城绿城环保科技有限公司 | A kind of organic solid waste is pyrolyzed waste residue recycle device |
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|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171013 |