CN105114955B - The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition - Google Patents
The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition Download PDFInfo
- Publication number
- CN105114955B CN105114955B CN201510504033.4A CN201510504033A CN105114955B CN 105114955 B CN105114955 B CN 105114955B CN 201510504033 A CN201510504033 A CN 201510504033A CN 105114955 B CN105114955 B CN 105114955B
- Authority
- CN
- China
- Prior art keywords
- flue gas
- rotary kiln
- carbonization
- outlet
- kiln
- 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.)
- Active
Links
- 238000003763 carbonization Methods 0.000 title claims abstract description 31
- 238000005979 thermal decomposition reaction Methods 0.000 title claims abstract description 7
- 238000002360 preparation method Methods 0.000 title abstract description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 69
- 239000003546 flue gas Substances 0.000 claims abstract description 69
- 239000000463 material Substances 0.000 claims abstract description 45
- 230000001066 destructive effect Effects 0.000 claims abstract description 32
- 238000002309 gasification Methods 0.000 claims abstract description 25
- 230000009977 dual effect Effects 0.000 claims abstract description 21
- 238000010304 firing Methods 0.000 claims abstract description 21
- 239000007789 gas Substances 0.000 claims abstract description 21
- 239000000428 dust Substances 0.000 claims abstract description 19
- 239000007921 spray Substances 0.000 claims abstract description 17
- 230000003472 neutralizing effect Effects 0.000 claims abstract description 16
- 239000002918 waste heat Substances 0.000 claims abstract description 15
- 238000009434 installation Methods 0.000 claims abstract description 13
- 238000002485 combustion reaction Methods 0.000 claims abstract description 7
- 238000001035 drying Methods 0.000 claims abstract description 5
- 238000010410 dusting Methods 0.000 claims abstract description 4
- 238000011017 operating method Methods 0.000 claims abstract description 4
- 239000000779 smoke Substances 0.000 claims abstract description 4
- 238000000197 pyrolysis Methods 0.000 claims description 40
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 4
- 230000001939 inductive effect Effects 0.000 claims description 4
- 231100000614 poison Toxicity 0.000 claims description 4
- 230000007096 poisonous effect Effects 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 230000001154 acute effect Effects 0.000 claims description 3
- 238000004380 ashing Methods 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 3
- 239000000920 calcium hydroxide Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000005416 organic matter Substances 0.000 claims description 3
- 238000003786 synthesis reaction Methods 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 229910001385 heavy metal Inorganic materials 0.000 claims description 2
- 239000003610 charcoal Substances 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 9
- 239000000446 fuel Substances 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000006386 neutralization reaction Methods 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000003517 fume Substances 0.000 description 3
- 230000036760 body temperature Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
Rotary kiln type continuous carbonization incinerator for thermal decomposition, including feed arrangement, kiln body slewing equipment, carbonization gasification installation, exhaust gas cleaner.Kiln body slewing equipment right-hand member is provided with feed arrangement, and kiln body slewing equipment left end is provided with carbonization gasification installation, and the left end of carbonization gasification installation is provided with exhaust gas cleaner；Kiln body slewing equipment includes rotary kiln, and carbonization gasification installation includes destructive gasifying room, dual firing chamber, and exhaust gas cleaner includes cyclone dust collectors, waste heat boiler, chilling tower, neutralizing tower, sack cleaner, air-introduced machine, spray scrubber；Preparation method includes following operating procedure：Combustion at the beginning of material → combustion at the beginning of material destructive gasifying → flue gas → flue gas rough dusting → flue gas heat exchange → flue gas chilling → flue gas neutralization → smoke secondary dedusting → flue gas deacidification → flue gas qualified discharge.The present invention can be given up or trade waste using high-temperature flue gas drying, carbonization doctor, save fuel, and discharge environmental protection reduces the operating cost of enterprise.
Description
Technical field
The invention belongs to energy-conserving and environment-protective equipment and technical field, more particularly to a kind of rotary kiln type continuous carbonization pyrolytic gasification
The preparation method of incinerator, it is adaptable to which doctor gives up or trade waste（Containing danger wastes）Destructive distillation, pyrolysis, gasification burning.
Background technology
Existing rotary kiln device generally existing kiln body temperature drift, chamber temperature is relatively low needs fuel oil or gas-fired combustion-supporting,
Increase enterprise operation cost.
Notification number is CN2295914 Chinese patent, a kind of rotary kiln type waste incinerator is disclosed, it is characterized in that by justifying
Type kiln cylinder, kiln hood cover body, kiln tail cover body, sealing device, burner, air feed mouthful, exhaust opening, charging aperture, ash hole, driving dress
Put, refractory material installs connection composition, and it is applied to burning domestic garbage, industrial refuse and poisonous and harmful substance, be a kind of
Environmental protection machinery device, its is simple in construction, low cost, continuous burning various garbage, and combustion rate is high, easy to use, with promotion price
Value.According to the patent, there is following technological deficiency：Because traditional rotary kiln gives up or trade waste in processing doctor（Containing danger
Dangerous discarded object）Deng material when, kiln body air feed is uneven, causes material to be burned inside kiln body, do not reach destructive distillation, pyrolysis, gasification
Purpose, so as to cause gas fume of combustion chamber amount not enough, temperature is relatively low, does not reach national related environmental requirement, and then need fuel oil
Or gas-fired combustion-supporting, directly increase enterprise operation cost.
The content of the invention
The purpose of the present invention is constantly rotated using itself body of heater in order to solve the above technical problems, providing one kind, makes material
Ceaselessly seethe, roll in stove, thermally equivalent connects tentatively the rotary kiln type of dry materials, destructive distillation, pyrolysis, gasification
The preparation method of continuous Retort Pyrolysis Gasification Incineration stove.
In order to realize above-mentioned purpose, this invention takes following technical solution：Rotary kiln type continuous carbonization heat
Incinerator, including feed arrangement are solved, kiln body slewing equipment, carbonization gasification installation, exhaust gas cleaner, its feature exist
In：
Described kiln body slewing equipment right-hand member is provided with feed arrangement, and kiln body slewing equipment left end is provided with carbonization gas
Makeup is put, and the left end of carbonization gasification installation is provided with exhaust gas cleaner；Kiln body slewing equipment includes rotary kiln, destructive distillation heat
Solve gasification installation include destructive gasifying room, dual firing chamber, exhaust gas cleaner include cyclone dust collectors, waste heat boiler, chilling tower, in
With tower, sack cleaner, air-introduced machine, spray scrubber, chimney, the wherein outlet of feed arrangement is communicated with the entrance of rotary kiln；
The outlet of rotary kiln is communicated with the upper entrance of destructive gasifying room, the outlet of destructive gasifying room and the lower entrances phase of dual firing chamber
Logical, the upper outlet of dual firing chamber is communicated with the entrance of cyclone dust collectors, the top exit of cyclone dust collectors and the top of waste heat boiler
Portion's entrance is communicated, and the lower part outlet of waste heat boiler is communicated with the top entry of chilling tower, the lower part outlet and neutralizing tower of chilling tower
Lower entrances communicate, the upper outlet of neutralizing tower is communicated with the entrance of sack cleaner, and the outlet of sack cleaner is by drawing
Blower fan, air inducing pipeline enter the lower part outlet of spray scrubber, and the upper outlet of spray scrubber is connected with chimney.
Described rotary kiln is horizontal, and the center line of rotary kiln and the angle of horizontal plane are acute angle, the center line of rotary kiln
Less than the center line of feed arrangement.
Described rotary kiln is internally provided with flow deflector so that material is rotationally advancing, continuous discharge.
Material in described destructive gasifying room produces flammable pyrolysis gas in abundant destructive distillation, pyrolysis, gasification,
And dual firing chamber is sent into by air-introduced machine, destructive gasifying room bottom is provided with rotation continuous discharging device, can after the completion of material ashing
Discharged by drawing mechanism.
Described destructive gasifying room bottom is evenly equipped with cloth air port, can be increased according to material destructive distillation situation in destructive gasifying room
Or reduce wind supply quantity.
Described dual firing chamber's import is provided with spray burner, can reach combustion-supporting, combustion chamber air feed and protection burner.
Described feed arrangement is hydraulic means continuous feed.
A kind of preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition, including following operating procedure：
1）, fire at the beginning of material, open that burner is combustion-supporting, when kiln temperature rise is rotated, pusher, which is pushed into material, to be rotated
In kiln, material is constantly rotated in rotation kiln drying, preliminary pyrolysis, burning material, rotary kiln using itself kiln body, material is existed
Advance is ceaselessly seethed in kiln；
2）, material destructive gasifying, preliminary destructive distillation, pyrolysis material from rotary kiln afterbody enter destructive gasifying room in, pass through
The uniform cloth air port in bottom, accurately controls oxygen, and material and the oxygen contact of preliminary carbonization are fully dry in destructive gasifying room
Evaporate, be pyrolyzed, gasify；
3）, fire at the beginning of flue gas, the flue gas produced after pyrolysis fully burns into dual firing chamber, effectively eliminates in discarded object
Organic matter and poisonous and harmful substance；
4）, flue gas rough dusting, the flue gas after burning enters cyclone dust collectors, preliminary to remove the bulky grain contained in flue gas
Dust；
5）, flue gas heat exchange, high-temperature flue gas enter waste heat boiler or other heat exchangers；
6）, flue gas chilling, complete heat exchange after flue gas from heat boiler outlet enter chilling tower, high-temperature flue gas is in chilling tower
Interior temperature is chilled to 180 DEG C in 1 second from 550 DEG C, it is to avoid the synthesis again of bioxin；
7）, flue gas neutralize, flue gas enters neutralizing tower from the outlet of chilling tower, and calcium hydroxide and activated carbon are added in neutralizing tower, is gone
Except the sour gas and heavy metal that contain in flue gas；
8）, smoke secondary dedusting, flue gas enters sack cleaner, further removes the dust that contains in flue gas and its harmful
Material；
9）, flue gas deacidification, flue gas enters spray scrubber under air-introduced machine effect, further removes the acid that contains in flue gas
Property gas；
10）, flue gas qualified discharge, the flue gas after washing is discharged into air through chimney.
The present invention had both solved traditional rotary kiln type incinerator kiln body temperature drift, dual firing chamber's temperature during carbonization
Degree it is relatively low need to extra oil or gas-fired combustion-supporting the problem of, solve again traditional rotary kiln carbonization it is insufficient bring it is secondary
Pollution problem, can be given up or trade waste using high-temperature flue gas drying, carbonization doctor（Containing danger wastes）Material, by even
Continuous pyrolytic gasification, the combustible fumes decomposited export is burnt, and burns stable, has saved fuel, and discharge has reached country
Environmental requirement, the higher problem of fuel consumption needed for solving equipment improves equipment economy, reduces the operation of enterprise
Cost.
Brief description of the drawings
Fig. 1 is the process chart of the present invention.
Fig. 2 is the structural representation of the present invention.
In figure：1. rotary kiln；2. destructive gasifying room；3. dual firing chamber；4. cyclone dust collectors；5. waste heat boiler；6. chilling tower；
7. neutralizing tower；8. sack cleaner；9. air-introduced machine；10. spray scrubber；11. chimney.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings, but not as limitation of the present invention：
Rotary kiln type continuous carbonization incinerator for thermal decomposition, including feed arrangement, kiln body slewing equipment, carbonization gasification
Device, exhaust gas cleaner, described kiln body slewing equipment right-hand member are provided with feed arrangement, and kiln body slewing equipment left end is provided with
Carbonization gasification installation, the left end of carbonization gasification installation is provided with exhaust gas cleaner；Kiln body slewing equipment includes rotation
Rotary kiln 1, carbonization gasification installation includes destructive gasifying room 2, dual firing chamber 3, and exhaust gas cleaner includes cyclone dust collectors 4, remaining
Heat boiler 5, chilling tower 6, neutralizing tower 7, sack cleaner 8, air-introduced machine 9, spray scrubber 10, wherein chimney 11, feed arrangement
Outlet communicated with the entrance of rotary kiln 1；The outlet of rotary kiln 1 is communicated with the upper entrance of destructive gasifying room 2, destructive gasifying room
2 outlet is communicated with the lower entrances of dual firing chamber 3, and the upper outlet of dual firing chamber 3 is communicated with the entrance of cyclone dust collectors 4, whirlwind
The top exit of deduster 4 is communicated with the top entry of waste heat boiler 5, the lower part outlet of waste heat boiler 5 and the top of chilling tower 6
Entrance is communicated, and the lower part outlet of chilling tower 6 is communicated with the lower entrances of neutralizing tower 7, the upper outlet and bag-type dust of neutralizing tower 7
The entrance of device 8 is communicated, and the bottom that the outlet of sack cleaner 8 enters spray scrubber 10 by air-introduced machine 9, air inducing pipeline goes out
Mouthful, the upper outlet of spray scrubber 10 is connected with chimney 11；Described rotary kiln 1 is horizontal, the center line and water of rotary kiln 1
The angle of plane is acute angle, and the center line of rotary kiln 1 is less than the center line of feed arrangement；Described rotary kiln 1 is internally provided with
Flow deflector so that material is rotationally advancing, continuous discharge；Material in described destructive gasifying room 2 is in abundant destructive distillation, pyrolysis, gas
Flammable pyrolysis gas is produced during change, and dual firing chamber 3 is sent into by air-introduced machine, the bottom of destructive gasifying room 2 is provided with rotation
Continuous discharging device, can be discharged after the completion of material ashing by drawing mechanism；The described bottom of destructive gasifying room 2 is evenly equipped with cloth wind
Mouthful, wind supply quantity can be increased or decreased according to material destructive distillation situation in destructive gasifying room 2；The described import of dual firing chamber 3 is provided with spray
Burner, can reach combustion-supporting, combustion chamber air feed and protection burner, extend burner service life；Described feed arrangement is liquid
Pressure device continuous feed.
When it is implemented, a kind of preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition, including following operation
Step：1）, fire at the beginning of material, open that burner is combustion-supporting, when temperature in rotary kiln 1 is raised, material is pushed into rotary kiln 1 by pusher
Interior, material drying, preliminary pyrolysis, burning material in rotary kiln 1, rotary kiln 1 are constantly rotated using itself kiln body, material is existed
Advance is ceaselessly seethed in kiln；2）, material destructive gasifying, preliminary destructive distillation, pyrolysis material enter carbonization gas from the afterbody of rotary kiln 1
Change in room 2, by the uniform cloth air port in bottom, accurately control oxygen, material and the oxygen contact of preliminary carbonization, in destructive gasifying
Abundant destructive distillation, pyrolysis, gasification in room 2；3）, fire at the beginning of flue gas, the flue gas produced after pyrolysis enters dual firing chamber 3 and fully burnt, effectively
The organic matter eliminated in discarded object and poisonous and harmful substance；4）, flue gas rough dusting, the flue gas after burning removes into whirlwind
Dirt device 4, it is preliminary to remove the big dust particle contained in flue gas；5）, flue gas heat exchange, high-temperature flue gas enter waste heat boiler 5 or other
Heat exchanger；6）, flue gas chilling, complete the flue gas after heat exchange and enter chilling tower 6 from the outlet of waste heat boiler 5, high-temperature flue gas is in chilling
Temperature is chilled to 180 DEG C in 1 second from 550 DEG C in tower 6, it is to avoid the synthesis again of bioxin；7）, flue gas neutralize, flue gas is from chilling
The outlet of tower 6, which enters, adds calcium hydroxide and activated carbon in neutralizing tower 7, neutralizing tower 7, remove the sour gas and a huge sum of money contained in flue gas
Category；8）, smoke secondary dedusting, flue gas enters sack cleaner 8, further removes the dust and its nuisance that contain in flue gas
Matter；9）, flue gas deacidification, flue gas enters spray scrubber 10 under the effect of air-introduced machine 9, further removes the acidity that contains in flue gas
Gas；10）, flue gas qualified discharge, the flue gas after washing is discharged into air through chimney 11.
The present invention gives up doctor or trade waste（Containing danger wastes）Decomposited in material destructive distillation, pyrolysis, gasification
Combustible fumes export burnt, reduce fuel consumption, the higher problem of fuel consumption needed for solving equipment improves and set
The economy of received shipment row, reduces the operating cost of enterprise.
The above embodiment of the present invention, it is only for clearly demonstrate examples of the invention, but be not limited to
Protection scope of the present invention, all equivalent technical schemes fall within scope of the invention, and scope of patent protection of the invention should
Limited by every claim.
Claims (1)
1. the operating method of rotary kiln type continuous carbonization incinerator for thermal decomposition, including feed arrangement, kiln body slewing equipment, destructive distillation
Pyrolysis gasifying device, exhaust gas cleaner, it is characterised in that：Described kiln body slewing equipment right-hand member is provided with feed arrangement, kiln
Body slewing equipment left end is provided with carbonization gasification installation, and the left end of carbonization gasification installation is provided with tail gas clean-up dress
Put；Kiln body slewing equipment includes rotary kiln（1）, carbonization gasification installation include destructive gasifying room（2）, dual firing chamber（3）, tail gas
Purifier includes cyclone dust collectors（4）, waste heat boiler（5）, chilling tower（6）, neutralizing tower（7）, sack cleaner（8）, air inducing
Machine（9）, spray scrubber（10）, chimney（11）, the wherein outlet of feed arrangement and rotary kiln（1）Entrance communicate；Rotary kiln
（1）Outlet and destructive gasifying room（2）Upper entrance communicate, destructive gasifying room（2）Outlet and dual firing chamber（3）Bottom enter
Mouth is communicated, dual firing chamber（3）Upper outlet and cyclone dust collectors（4）Entrance communicate, cyclone dust collectors（4）Top exit with
Waste heat boiler（5）Top entry communicate, waste heat boiler（5）Lower part outlet and chilling tower（6）Top entry communicate, chilling
Tower（6）Lower part outlet and neutralizing tower（7）Lower entrances communicate, neutralizing tower（7）Upper outlet and sack cleaner（8）'s
Entrance is communicated, sack cleaner（8）Outlet pass through air-introduced machine（9）, air inducing pipeline connection spray scrubber（10）Bottom enter
Mouthful, spray scrubber（10）Upper outlet and chimney（11）Connection；Described rotary kiln（1）For horizontal, rotary kiln（1）Axle
It is acute angle, rotary kiln to the angle of center line and horizontal plane（1）Longitudinal center line be less than feed arrangement longitudinal center line；Institute
The rotary kiln stated（1）It is internally provided with flow deflector so that material is rotationally advancing, continuous discharge；Described destructive gasifying room（2）It is interior
Material flammable pyrolysis gas is produced in abundant destructive distillation, pyrolysis, gasification, and dual firing chamber is sent into by air-introduced machine（3）,
Destructive gasifying room（2）Bottom is provided with rotation continuous discharging device, can be discharged after the completion of material ashing by drawing mechanism；It is described
Destructive gasifying room（2）Bottom is evenly equipped with cloth air port, can be according to destructive gasifying room（2）Interior material destructive distillation situation, is increased or decreased
Wind supply quantity；Described dual firing chamber（3）Import is provided with spray burner, can reach combustion-supporting, combustion chamber air feed and protect the work of burner
With；Described feed arrangement is hydraulic continuous feed arrangement；
Including following operating procedure：
1）, fire at the beginning of material, it is combustion-supporting to open burner, treats rotary kiln（1）During interior temperature rise, material is pushed into rotary kiln by pusher
（1）Interior, material is in rotary kiln（1）Interior drying, preliminary pyrolysis, burning, rotary kiln（1）Constantly rotated using itself kiln body, make thing
Material ceaselessly seethes advance in kiln；
2）, material destructive gasifying, preliminary destructive distillation, the material of pyrolysis are from rotary kiln（1）Afterbody enters destructive gasifying room（2）In, lead to
The uniform cloth air port in bottom is crossed, oxygen, material and the oxygen contact of preliminary carbonization, in destructive gasifying room is accurately controlled（2）Inside fill
Divide destructive distillation, pyrolysis, gasification；
3）, fire at the beginning of flue gas, the flue gas produced after pyrolysis enters dual firing chamber（3）Fully burning, is effectively eliminated in discarded object
Organic matter and poisonous and harmful substance；
4）, flue gas rough dusting, the flue gas after burning enters cyclone dust collectors（4）, it is preliminary to remove the bulky grain contained in flue gas
Dust；
5）, flue gas heat exchange, high-temperature flue gas enters waste heat boiler（5）Or other heat exchangers；
6）, flue gas chilling, complete the flue gas after heat exchange from waste heat boiler（5）Outlet enters chilling tower（6）, high-temperature flue gas is in chilling
Tower（6）Interior temperature is chilled to 180 DEG C in 1 second from 550 DEG C, it is to avoid the synthesis again of bioxin；
7）, flue gas neutralize, flue gas is from chilling tower（6）Outlet enters neutralizing tower（7）, neutralizing tower（7）Interior addition calcium hydroxide and activity
Charcoal, removes the sour gas and heavy metal contained in flue gas；
8）, smoke secondary dedusting, flue gas enters sack cleaner（8）, further remove the dust contained in flue gas and its be harmful to
Material；
9）, flue gas deacidification, flue gas is in air-introduced machine（9）Enter spray scrubber under effect（10）, further remove and contain in flue gas
Sour gas；
10）, flue gas qualified discharge, the flue gas after washing is through chimney（11）It is discharged into air.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510504033.4A CN105114955B (en) | 2015-08-18 | 2015-08-18 | The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510504033.4A CN105114955B (en) | 2015-08-18 | 2015-08-18 | The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105114955A CN105114955A (en) | 2015-12-02 |
| CN105114955B true CN105114955B (en) | 2017-10-03 |
Family
ID=54663003
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510504033.4A Active CN105114955B (en) | 2015-08-18 | 2015-08-18 | The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105114955B (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105953253B (en) * | 2016-06-24 | 2018-04-20 | 深圳市三丰环保科技有限公司 | A kind of waste gas treatment equipment |
| CN106753474A (en) * | 2017-02-15 | 2017-05-31 | 吴晓龙 | A kind of domestic garbage pyrolysis processing system and low temperature, high temperature pyrolysis processing method |
| CN107120657A (en) * | 2017-06-11 | 2017-09-01 | 无锡绿麦环保科技有限公司 | Solid waste incineration system and its technique |
| CN107243505A (en) * | 2017-07-25 | 2017-10-13 | 云南大地绿坤环保科技有限公司 | A kind of incineration treatment method of the waste residue containing nitrile |
| CN107641529A (en) * | 2017-10-25 | 2018-01-30 | 广州洲际蓝色环保科技有限公司 | A kind of urban community's organic solid waste thing processing unit |
| CN108726614A (en) * | 2018-05-31 | 2018-11-02 | 平原中德泰兴环保科技装备有限公司 | A kind of industrial waste treatment process and its device |
| CN108955282A (en) * | 2018-06-27 | 2018-12-07 | 四川省玻纤集团有限公司 | A kind of basalt fibre prepares solvent recovery technology from vent gas |
| CN109469903B (en) * | 2018-09-20 | 2020-09-22 | 武汉市嘉恒化工有限公司 | Incineration treatment method for industrial solid waste |
| CN109631052A (en) * | 2019-01-18 | 2019-04-16 | 南昌市医疗废物处置中心有限公司 | A kind of steady and continuous pyrolytic incineration method of clinical waste |
| CN110963661A (en) * | 2019-08-15 | 2020-04-07 | 广州沼能环保科技有限责任公司 | Sludge pyrolysis system |
| CN111072254A (en) * | 2019-12-30 | 2020-04-28 | 苏州同和环保工程有限公司 | High-temperature treatment process for oily sludge |
| CN111112320B (en) * | 2019-12-31 | 2024-02-27 | 江苏盖亚环境科技股份有限公司 | Vehicle-mounted ectopic direct thermal desorption system and application method thereof |
| CN111408608A (en) * | 2020-04-20 | 2020-07-14 | 聊城市鲁西化工工程设计有限责任公司 | Process and system for automatic ash removal and heat energy recovery of waste paint iron drum organic matter pyrolysis and application |
| CN111853793A (en) * | 2020-07-27 | 2020-10-30 | 姚敦卫 | Treatment process of household garbage |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3921765B2 (en) * | 1997-11-20 | 2007-05-30 | 石川島播磨重工業株式会社 | Waste pyrolysis gasification melting equipment |
| CN202598539U (en) * | 2012-05-11 | 2012-12-12 | 冯国宇 | Incinerator of waste rotary kiln |
| CN103953930A (en) * | 2014-04-17 | 2014-07-30 | 浙江大学 | Efficient mobile bed gasifier device with pre-dechlorinating function and dechlorinating method of efficient mobile bed gasifier device |
| CN204943506U (en) * | 2015-08-18 | 2016-01-06 | 江苏鼎新环保科技有限公司 | A kind of rotary kiln type continuous carbonization incinerator for thermal decomposition |
-
2015
- 2015-08-18 CN CN201510504033.4A patent/CN105114955B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105114955A (en) | 2015-12-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105114955B (en) | The preparation method of rotary kiln type continuous carbonization incinerator for thermal decomposition | |
| CN103363531B (en) | A kind of dangerous waste incinerator complexes | |
| CN203628674U (en) | Whole-set hazardous waste incinerator device | |
| CN104990084B (en) | A kind of biomass class solid waste and dangerous waste treatment process | |
| CN206094112U (en) | Sludge incineration system | |
| CN102261661B (en) | House refuse incineration gasifier | |
| CN102168853B (en) | Three-dimensional hierarchical air supply combined waste incinerator | |
| CN109899805A (en) | Multipurpose assembles combustion-type rotary furnace | |
| CN207999834U (en) | A kind of medical waste pyrolysis gasification furnace incinerator | |
| CN207122902U (en) | A kind of refuse burning system | |
| CN109468139A (en) | A kind of biomass graded pyrolysis and combustion device | |
| CN106224974A (en) | Waste incineration processing system | |
| CN111256147A (en) | Household garbage pyrolysis gasification incineration grate furnace and treatment system thereof | |
| CN2503361Y (en) | Rotary furnace bed garbage gasification incineration device | |
| CN111928263A (en) | System for utilize rotary kiln to burn burning furnace and handle hazardous waste | |
| CN205061973U (en) | System for indirect heating formula pyrolysis and carbonization living beings | |
| CN107606623B (en) | Small garbage gas-carbon complementary carbonization combustion furnace | |
| CN205383607U (en) | Rubbish is ashless to burn burning furnace | |
| CN207815342U (en) | A kind of garbage burning boiler | |
| CN204943506U (en) | A kind of rotary kiln type continuous carbonization incinerator for thermal decomposition | |
| CN208074962U (en) | A kind of modified form hazardous waste burn system | |
| CN207646043U (en) | Municipal sludge desiccation pyrolytic gasification is controlled oneself incineration system | |
| CN208487625U (en) | A kind of novel combination type solid-liquid incineration furnace | |
| CN206347578U (en) | A kind of waste incineration air and gas system | |
| CN206915970U (en) | A kind of oily sludge is from heat supply Non-oxygen pyrolytic equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210305 Address after: No. 96, Feiyue Road, Xinqiao Town, Jingjiang City, Taizhou City, Jiangsu Province Patentee after: JIANGSU LIANXING COMPLETE SETS OF EQUIPMENT MANUFACTURE Co.,Ltd. Address before: 214500 No.95, Feiyue Road, Xinqiao Town, Jingjiang City, Taizhou City, Jiangsu Province Patentee before: JIANGSU DINGXUN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220513 Address after: 214537 No. 95 Feiyue South Road, Xinqiao Town, Jingjiang City, Taizhou City, Jiangsu Province Patentee after: JIANGSU DINGXUN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: No. 96, Feiyue Road, Xinqiao Town, Jingjiang City, Taizhou City, Jiangsu Province Patentee before: JIANGSU LIANXING COMPLETE SETS OF EQUIPMENT MANUFACTURE Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Preparation method of rotary kiln type continuous retort pyrolysis gasification incinerator Effective date of registration: 20220712 Granted publication date: 20171003 Pledgee: Jingjiang Branch of Bank of China Ltd. Pledgor: JIANGSU DINGXUN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2022980010286 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230607 Granted publication date: 20171003 Pledgee: Jingjiang Branch of Bank of China Ltd. Pledgor: JIANGSU DINGXUN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2022980010286 |