CN102220151A - Horizontal waste plastic and tire cracking furnace - Google Patents
Horizontal waste plastic and tire cracking furnace Download PDFInfo
- Publication number
- CN102220151A CN102220151A CN2010101474651A CN201010147465A CN102220151A CN 102220151 A CN102220151 A CN 102220151A CN 2010101474651 A CN2010101474651 A CN 2010101474651A CN 201010147465 A CN201010147465 A CN 201010147465A CN 102220151 A CN102220151 A CN 102220151A
- Authority
- CN
- China
- Prior art keywords
- scraper
- reactor
- horizontal
- used plastics
- conducting strip
- 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.)
- Granted
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/32—Other processes in ovens with mechanical conveying means
- C10B47/34—Other processes in ovens with mechanical conveying means with rotary scraping devices
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention discloses a horizontal waste plastic and tire cracking furnace, which comprises a horizontal furnace body, wherein the side face of the lower part of the furnace body has a furnace door; a chimney is formed on the upper side of the furnace body; a horizontal reaction kettle is arranged in the furnace; a feed inlet is formed at one end of the reaction kettle, and the other end of the reaction kettle has an exhaust hole; a power source for driving a reaction kettle to rotate is arranged in the furnace body; a spiral conducting strip is arranged in the reaction kettle; and more than one scrapper and more than one flow guide stirrer are arranged on the conducting strip. In the invention, as the horizontal rotary shaft-free stirring and the spiral conducting strip as well as a fin type spiral heat-conducting flow guide plate device are adopted in the thermal cracking and catalysis of waste plastics and waste tire, the trouble that winding materials wind on the stirring shaft and cause the halt of the furnace is avoided. Meanwhile, the drawback that the conventional horizontal rotary kettle incapable of stirring and therefore makes the heat conducting effect unobvious and prolongs cracking and catalyzing time is overcome.
Description
Technical field
The present invention discloses a kind of pyrolyzer, particularly a kind of horizontal waste or used plastics, tire pyrolysis stove.
Background technology
Along with the rise of chemistry, chemical industry, the application of chemical products in people's daily life more and more widely, the consequent is exactly the handling problem of some chemical wastes, as plastic waste, damaged tire etc.But therefore plastic waste, damaged tire etc. need manually utilize processing again to it in occurring in nature natural decomposition hardly, therefore, year rise recently and utilize plastic waste, damaged tire oil refining and gas making generating etc.Utilize plastic waste, damaged tire oil refining and gas making generating etc. all to need a device, it is exactly pyrolyzer, the pyrolyzer of plastic waste of the prior art, damaged tire oil refining is divided into two kinds of vertical heater and horizontal chamber ovens, but in the production use, the shortcoming vertical or horizontal chamber oven of finding social now existing plastic waste, damaged tire oil refining is as follows: because waste or used plastics contains imponderable twister (such as iron wire, steel wire), when adopting vertical response still cracking material, its stir shaft is twined by the twister in the material easily, causes reactor to be shut down midway and removes obstacles; When adopting the horizontal reacting still, though can avoid the problem of material twister, it is the sorting operation of having saved cleaved material certainly, because the horizontal reacting still is no whipping appts, also just is far from being and scrapes the wall device function.But the horizontal reacting still is to rely on the kettle rotation, utilize still cornice hydrodynamic body to flow, therefore it is uneven to cause conducting heat, the liquid flow district is little, also may produce the liquid-flow quiescent centre, and the cracking liquid of plastic waste, damaged tire is viscoid, no matter the mixing speed or the horizontal chamber oven kettle rotating speed that are vertical heater are very low usually, fluidic moves and only can extend to very short distance and be not enough to overcome fluidic stickiness power, causes kettle high-temperature coking or low temperature coking phenomenon, makes the hot side coking rapid.When work (time) reach about 60 hours, thickness of coke layer can reach 10-20mm, form thermal resistance, cause the kettle distortion, shortened the safe-use period of reactor, and wasted a large amount of energy, man-hour is produced in waste, especially the workman is in exceedingly odious thick carbon black dust environmental work for a long time in removing the coking process, has a strong impact on operator ' s health.
Summary of the invention
At above-mentioned short shortcoming of the pyrolyzer of the prior art life-span of mentioning, the invention provides a kind of long-life pyrolyzer, it has additional scraper in reactor, can prevent the reactor coking, thereby increases the work-ing life of pyrolyzer.
The technical scheme that the present invention solves its technical problem employing is: a kind of horizontal waste or used plastics, tire pyrolysis stove, pyrolyzer comprises the flat body of heater that crouches, the body of heater lower side has fire door, the side is provided with chimney on the body of heater, is provided with horizontally-arranged reactor in the body of heater, and reactor one end has opening for feed, the other end has the air outlet, be provided with in the body of heater and drive the propulsion source that reactor rotates, reactor inside is provided with the volution conducting strip, and more than one scraper and more than one water conservancy diversion agitator are housed on the conducting strip.
The technical scheme that the present invention solves its technical problem employing further comprises:
The horizontal interface of described conducting strip is triangular in shape, the trilateral base is mounted on the reactor inwall, trilateral drift angle place is installed with spiral helicine scraper back up pad, and scraper back up pad and conducting strip be arranged in parallel, and scraper and water conservancy diversion agitator are installed on the scraper back up pad.
Described scraper back up pad both sides have the scraper leading groove of bar shaped, and the scraper leading groove correspondence on the relative face of scraper back up pad is offered, and the scraper two ends are bolster, and scraper is arranged in the scraper leading groove by two bolsters.
Described scraper cross section is anchor shape, and the length of scraper is greater than the vertical length from the bolster of scraper to the reactor inwall.
Described water conservancy diversion agitator is fin shape, and the water conservancy diversion agitator is installed in scraper back up pad top.
The setting angle of described water conservancy diversion agitator is 15 °-30 °.
Described opening for feed and air outlet are arranged on the axis of reactor, and the opening for feed diameter is greater than the air outlet diameter.
Described propulsion source adopts three-phase machine, and three-phase machine rotates by the gear drive reactor that belt drives the reactor outside.
Described chimney adopts Square Factory Chimney, and edge is provided with circular arc chamfering, is provided with the above cascade device of one deck in the chimney.
The invention has the beneficial effects as follows: stir and the spiral conducting strip because the present invention has adopted horizontal rotation not have axle to thermo-cracking, the catalysis of plastic waste, damaged tire; and fin formula spiral heat conduction guide vane means, removed twister and twined stir shaft and need to shut down the puzzlement of removing obstacles.Also solved simultaneously existing horizontal revolving reaction still,, delayed the defective of cracking and catalysis time because of no agitating function causes heat-transfer effect not obvious.Especially the present invention has adopted a nothing axle scraper to scrape wall device, power is used in the utilization rotation and fluid is scraped wall from the living randomness of cutting down output, strengthened heat transfer effect, stoped the generation of reactor wall coking, overall coefficient of heat transfer is not scraped the horizontal revolving reaction still of wall and improved 30% than having now, and it is rapid to have solved existing horizontal revolving reaction still coking, and is burnt thick even reach more than ten millimeter, cause heat transfer coefficient low, be similar to the difficult problem of adiabatic operation.
The present invention will be further described below in conjunction with the drawings and specific embodiments.
Description of drawings
Fig. 1 is integral body of the present invention and internal structure synoptic diagram.
Fig. 2 is a tangent plane structural representation of the present invention.
Fig. 3 is a side of the present invention biopsy cavity marker devices structural representation.
Among the figure, 1-liquid level, 2-scraper, 3-thermal oil, 4-back up pad, 5-inducer, 6-water conservancy diversion fin, 7-leading groove, 8-supporting plate, 9-reactor, 10-back shaft, 11-thermal source.
Embodiment
Present embodiment is the preferred embodiment for the present invention, and other all its principles are identical with present embodiment or proximate with basic structure, all within protection domain of the present invention.
The present invention is directed to material contains the prehensile foreign material and improves the high viscosity fluid heat transfer coefficient, slows down glutinous still thing coking speed and be provided with.Please referring to accompanying drawing 1, accompanying drawing 2 and accompanying drawing 3, the body of heater among the present invention is a horizontal circular, and burner hearth adopts the chamber burner, thermal source 11 is located at reactor 9 belows, in the present embodiment, reactor 9 is drum type, and is horizontally-arranged, and can be along contrary two-way rotation, the side is provided with chimney on the body of heater, and in the present embodiment, chimney is the square fillet, establish multilayer cascade device in the chimney, can reduce waste gas, dust that the present invention discharges.In the present embodiment, the rotation of reactor 9 adopts three-phase machine as propulsion source, carries out speed change with the belt driven gear, drive reactor 9 rotations then, in the present embodiment, a working hole is respectively offered in the position, axis at horizontal reacting still 9 two ends, the diameter difference of two work, wherein, the hole that diameter is bigger is a material opening for feed 12, and the less hole of another diameter is air outlet 13, and air outlet 13 can connect the refining equipment of next stage.Among the present invention, be provided with cross section spiral flow deflector triangular in shape 5 in the reactor 9 (in the present embodiment, trilateral spiral flow deflector 5 has heat transfer device concurrently, charging drives device and automatic three functions of deslagging device), in the present embodiment, inducer 5 is hollow, inducer 5 contains thermal oil 3, inducer 5 shape in the shape of a spiral in the present embodiment, and the base of triangular cross section is close to reactor 9 inwalls and is fixedly installed.When reactor 9 when clockwise direction rotates, conducting strip 5 drives device as a kind of charging, quickens the material input; When reactor 9 when being rotated counterclockwise, conducting strip 5 is as a kind of automatic deslagging device, the waste material residue is delivered to slag notch 14 places that are located at spirrillum inducer 5 end points automatically the waste material residue is discharged, be marked with thermal oil 3 in the hollow triangle of conducting strip 5, strengthen heat conductive efficiency as heat-transfer medium.On the triangled tip of spiral conducting strip 5, prolong the hand of spiral scraper resting support 4 is housed, be that scraper bracing frame 4 be arranged in parallel with conducting strip 5, scraper resting support 4 can be used as the auxiliary heat-conducting piece of conducting strip 5 simultaneously, in the present embodiment, offer some leading grooves 7 with the direction that stretches of scraper resting support 4, leading groove 7 corresponding settings the on the relative face of bracing frame 4, leading groove 7 is as the leading instrument of scraper 2.Please referring to accompanying drawing 2, in the present embodiment, scraper 2 cross sections are the design of anchor shape, and promptly the cross section of scraper 2 bottom is leg-of-mutton scraper head, and scraper head is provided with connecting rod, and the cross section global shape is similar to the shape of the anchor of using on the ship.Vertical two ends of scraper 2 are hung by bolster 10 respectively and hang in leading groove 7, the lateral length of scraper 2 is greater than the vertical length from the bolster of scraper 2 to reactor 9 inwalls, can guarantee scraper 2 constantly with reactor 9 in side contacts, scraper 2 longitudinal lengths are identical with the pitch of spirrillum bracing frame 4, can guarantee the interior effect to reactor 9 inwalls of scraper 2 maximum ranges.The wall method of scraping of the present invention is that bolster 10 with scraper 2 is an oscillation centre, scraper 2 slides along leading groove 7 with the rotation of reactor 9, randomness is scraped wall to reactor 9 inwalls, the glutinous still thing of attenuate reactor thermal boundary layer prevents that reactor 9 inwall cokings are blocked up effectively, and the coking speed of reactor 9 inwalls that slow down, simultaneously scraper 2 also acts on the hot-fluid that wall is pressed close in edge of a knife front and sweeps, and with the cold fluid uniform mixing at reactor 9 middle parts, improve heat transfer coefficient, save energy consumption.The present invention is in scraper resting support 4 upper ends, prolong the some horizontal water conservancy diversion fins 6 of scraper resting support 4 hand of spiral devices, in the present embodiment, water conservancy diversion fin 6 setting angles and supporting-point are 15-30 ° (be between resting support 4 tangent lines at water conservancy diversion fin plane, 6 place and its point of suppon place angle be 10-30 °), force the fluid heat transferring motion with this.
The present invention in use, reactor 9 is to clockwise direction rotation, throw from opening for feed 12 and remove waste material, simultaneously, 9 heating of 11 pairs of reactors of thermal source; After the plastic waste in the reactor 9, damaged tire cracking were finished, reactor 9 was discharged residue to counterclockwise rotating from slag notch.
Because the present invention has adopted horizontal rotation not have axle to thermo-cracking, the catalysis of plastic waste, damaged tire and stirred and the spiral conducting strip, and fin formula spiral heat conduction guide vane means, removed twister and twined stir shaft and need to shut down the puzzlement of removing obstacles.Also solved simultaneously existing horizontal revolving reaction still,, delayed the defective of cracking and catalysis time because of no agitating function causes heat-transfer effect not obvious.Especially the present invention has adopted a nothing axle scraper to scrape wall device, power is used in the utilization rotation and fluid is scraped wall from the living randomness of cutting down output, strengthened heat transfer effect, stoped the generation of reactor wall coking, overall coefficient of heat transfer is not scraped the horizontal revolving reaction still of wall and improved 30% than having now, and it is rapid to have solved existing horizontal revolving reaction still coking, and is burnt thick even reach more than ten millimeter, cause heat transfer coefficient low, be similar to the difficult problem of adiabatic operation.
Claims (9)
1. a horizontal waste or used plastics, tire pyrolysis stove, it is characterized in that: described pyrolyzer comprises the flat body of heater that crouches, the body of heater lower side has fire door, the side is provided with chimney on the body of heater, is provided with horizontally-arranged reactor in the body of heater, and reactor one end has opening for feed, the other end has the air outlet, be provided with in the body of heater and drive the propulsion source that reactor rotates, reactor inside is provided with the volution conducting strip, and more than one scraper and more than one water conservancy diversion agitator are housed on the conducting strip.
2. horizontal waste or used plastics according to claim 1, tire pyrolysis stove, it is characterized in that: the horizontal interface of described conducting strip is triangular in shape, the trilateral base is mounted on the reactor inwall, trilateral drift angle place is installed with spiral helicine scraper back up pad, scraper back up pad and conducting strip be arranged in parallel, and scraper and water conservancy diversion agitator are installed on the scraper back up pad.
3. horizontal waste or used plastics according to claim 2, tire pyrolysis stove, it is characterized in that: described scraper back up pad both sides have the scraper leading groove of bar shaped, scraper leading groove correspondence on the relative face of scraper back up pad is offered, the scraper two ends are bolster, and scraper is arranged in the scraper leading groove by two bolsters.
4. according to claim 1 or 2 or 3 described horizontal waste or used plastics, tire pyrolysis stove, it is characterized in that: described scraper cross section is anchor shape, and the length of scraper is greater than the vertical length from the bolster of scraper to the reactor inwall.
5. horizontal waste or used plastics according to claim 2, tire pyrolysis stove is characterized in that: described water conservancy diversion agitator is fin shape, and the water conservancy diversion agitator is installed in scraper back up pad top.
6. horizontal waste or used plastics according to claim 5, tire pyrolysis stove is characterized in that: the setting angle of described water conservancy diversion agitator is 15 °-30 °.
7. horizontal waste or used plastics according to claim 1, tire pyrolysis stove is characterized in that: described opening for feed and air outlet are arranged on the axis of reactor, and the opening for feed diameter is greater than the air outlet diameter.
8. horizontal waste or used plastics according to claim 1, tire pyrolysis stove is characterized in that: described propulsion source adopts three-phase machine, and three-phase machine rotates by the gear drive reactor that belt drives the reactor outside.
9. horizontal waste or used plastics according to claim 1, tire pyrolysis stove is characterized in that: described chimney adopts Square Factory Chimney, and edge is provided with circular arc chamfering, is provided with the above cascade device of one deck in the chimney.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101474651A CN102220151B (en) | 2010-04-16 | 2010-04-16 | Horizontal waste plastic and tire cracking furnace |
| PCT/CN2010/075547 WO2011127701A1 (en) | 2010-04-16 | 2010-07-29 | Horizontal cracking furnace for waste plastics or tires |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101474651A CN102220151B (en) | 2010-04-16 | 2010-04-16 | Horizontal waste plastic and tire cracking furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102220151A true CN102220151A (en) | 2011-10-19 |
| CN102220151B CN102220151B (en) | 2013-07-24 |
Family
ID=44776865
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010101474651A Expired - Fee Related CN102220151B (en) | 2010-04-16 | 2010-04-16 | Horizontal waste plastic and tire cracking furnace |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN102220151B (en) |
| WO (1) | WO2011127701A1 (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104327877A (en) * | 2013-07-22 | 2015-02-04 | 李艺 | Double-heating efficient energy-saving equipment possessing internal and external double kettles and used for cracking waste tyres, waste plastic and waste engine oil |
| CN104629785A (en) * | 2013-11-13 | 2015-05-20 | 辽宁压克力塑胶有限公司 | Renewable resource cracking furnace |
| CN104789251A (en) * | 2015-05-05 | 2015-07-22 | 湖南奔骥环保能源科技有限责任公司 | External-rotation and internal-turning full-automatic continuous cracking and refining device |
| CN105062517A (en) * | 2015-07-29 | 2015-11-18 | 王庆普 | Oilfield working waste pyrolysis reacting furnace inner wall coke removal apparatus |
| CN107033932A (en) * | 2017-05-25 | 2017-08-11 | 常熟市伟国环保成套设备有限公司 | A kind of multi-functional successively biaxial fluidized bed cracking stove for being used to handle urban waste |
| CN107267181A (en) * | 2017-07-20 | 2017-10-20 | 孙振轩 | Horizontal rotary damaged tire pyrocrack furnace |
| CN111518571A (en) * | 2020-05-28 | 2020-08-11 | 李珊珊 | Coke oven with high production efficiency |
| CN113462411A (en) * | 2021-05-22 | 2021-10-01 | 众智机械(临沂)有限公司 | Horizontal pyrolysis device for solid waste treatment |
| CN115305103A (en) * | 2022-06-30 | 2022-11-08 | 胡进 | Reaction device for enhancing apparent heat transfer coefficient in organic solid waste thermal cracking process |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102746862B (en) * | 2012-06-07 | 2013-09-25 | 河北景明循环产业股份有限公司 | Waste organic matter continuous cracking industrial fluidized bed |
| CN108641736A (en) * | 2018-07-09 | 2018-10-12 | 苏州普洛代尔机电有限公司 | Biomass cracking carbide furnace |
| CN114713170A (en) * | 2022-04-14 | 2022-07-08 | 安徽匠星联创新材料科技有限公司 | Reation kettle is used in epoxy preparation |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2486551Y (en) * | 2001-07-12 | 2002-04-17 | 张赵祥 | Pyrolytic catalytic furnace for waste plastic |
| CN2591041Y (en) * | 2002-12-28 | 2003-12-10 | 王林生 | Improved waste tyre thermal cracking apparatus |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5846385A (en) * | 1997-05-20 | 1998-12-08 | Chien; Szu Jeng | Process and apparatus for energy recovering through waste classification and calcination |
| JPH1161155A (en) * | 1997-08-20 | 1999-03-05 | Motoda Electron Co Ltd | Control of production state of thermal decomposition gas on thermal decomposition treatment of waste plastic or the like and treatment of produced thermal decomposition gas |
| JPH11114531A (en) * | 1997-10-16 | 1999-04-27 | Toshiba Corp | Waste plastic treating device |
| CN2542662Y (en) * | 2002-05-17 | 2003-04-02 | 丁清云 | Pyrolyzer for preparing fuel by pyrolyzing waste rubber |
| CN2564575Y (en) * | 2002-07-16 | 2003-08-06 | 上海绿人生态经济科技有限公司 | Thermal cracking furnace with screw airflow guide plate |
| CN1952045A (en) * | 2006-09-29 | 2007-04-25 | 浙江大学 | Horizontal type slew cylinder structure cracking furnace for waste steel wire blank continuous thermal cracking |
| CN200995997Y (en) * | 2007-01-31 | 2007-12-26 | 宜兴市昌华过滤器材有限公司 | Horizontal impulse pyrolyzer |
| CN201660599U (en) * | 2010-04-16 | 2010-12-01 | 华南再生资源（中山）有限公司 | Horizontal-type waste plastic and tire cracking furnace |
| CN101824332B (en) * | 2010-06-02 | 2013-10-09 | 华南再生资源（中山）有限公司 | Production equipment for comprehensively utilizing renewable energy resources of waste and old plastics, tires and waste engine oil |
-
2010
- 2010-04-16 CN CN2010101474651A patent/CN102220151B/en not_active Expired - Fee Related
- 2010-07-29 WO PCT/CN2010/075547 patent/WO2011127701A1/en active Application Filing
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2486551Y (en) * | 2001-07-12 | 2002-04-17 | 张赵祥 | Pyrolytic catalytic furnace for waste plastic |
| CN2591041Y (en) * | 2002-12-28 | 2003-12-10 | 王林生 | Improved waste tyre thermal cracking apparatus |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104327877A (en) * | 2013-07-22 | 2015-02-04 | 李艺 | Double-heating efficient energy-saving equipment possessing internal and external double kettles and used for cracking waste tyres, waste plastic and waste engine oil |
| CN104629785A (en) * | 2013-11-13 | 2015-05-20 | 辽宁压克力塑胶有限公司 | Renewable resource cracking furnace |
| CN104629785B (en) * | 2013-11-13 | 2016-08-24 | 辽宁压克力塑胶有限公司 | Regenerated resources pyrolysis furnace |
| CN104789251A (en) * | 2015-05-05 | 2015-07-22 | 湖南奔骥环保能源科技有限责任公司 | External-rotation and internal-turning full-automatic continuous cracking and refining device |
| CN105062517A (en) * | 2015-07-29 | 2015-11-18 | 王庆普 | Oilfield working waste pyrolysis reacting furnace inner wall coke removal apparatus |
| CN107033932A (en) * | 2017-05-25 | 2017-08-11 | 常熟市伟国环保成套设备有限公司 | A kind of multi-functional successively biaxial fluidized bed cracking stove for being used to handle urban waste |
| CN107267181A (en) * | 2017-07-20 | 2017-10-20 | 孙振轩 | Horizontal rotary damaged tire pyrocrack furnace |
| CN111518571A (en) * | 2020-05-28 | 2020-08-11 | 李珊珊 | Coke oven with high production efficiency |
| CN113462411A (en) * | 2021-05-22 | 2021-10-01 | 众智机械(临沂)有限公司 | Horizontal pyrolysis device for solid waste treatment |
| CN115305103A (en) * | 2022-06-30 | 2022-11-08 | 胡进 | Reaction device for enhancing apparent heat transfer coefficient in organic solid waste thermal cracking process |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102220151B (en) | 2013-07-24 |
| WO2011127701A1 (en) | 2011-10-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102220151B (en) | Horizontal waste plastic and tire cracking furnace | |
| CN102220152B (en) | Reactor wall scraper | |
| CN201660599U (en) | Horizontal-type waste plastic and tire cracking furnace | |
| CN107446599B (en) | Vertical pyrolysis device of solid organic waste | |
| CN201538567U (en) | Asphaltic mixture insulation spiral conveyor | |
| CN111012667A (en) | Medicine machine is fried to even drum-type of being heated | |
| CN212357146U (en) | Petroleum is refined with petroleum distillation plant | |
| CN211754259U (en) | Crude oil dehydration device | |
| CN208860183U (en) | Waste-heat recovery device is used in a kind of processing of industrial waste gas | |
| CN215975949U (en) | Novel furnace bottom roller nodulation duster | |
| CN204529754U (en) | A kind of pitch oxidation reactor | |
| CN212560141U (en) | Novel efficient rotary type heat-conducting oil frying pan | |
| TWI441910B (en) | Reactor tank scraper | |
| CN211546414U (en) | Pyrolysis device for solid organic waste | |
| CN2799560Y (en) | Rotary carbonizing tower for carbonizing organic viscous solid residues | |
| CN112646591A (en) | Rotary furnace hearth thermal cracker | |
| TWI436004B (en) | Horizontal cracking furnace for waste plastics and tyres | |
| CN112221450A (en) | Starch glue processing is with constant temperature heating cauldron that has temperature monitoring mechanism | |
| CN215276785U (en) | Stirring subassembly, agitating unit and microwave pyrolysis equipment | |
| CN217635684U (en) | Inside burnt processing mechanism that hangs of boiler furnace | |
| CN215113231U (en) | Hot-blast furnace with protective structure for ceramic manufacture | |
| CN221036734U (en) | Secondary aluminum smelting device | |
| CN218553154U (en) | Anti-coking rapid distillation device | |
| CN216667984U (en) | Heating furnace water seal tank capable of improving slag scraping capacity | |
| CN220506756U (en) | Waste heat recovery device for heat power supply |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130724 Termination date: 20160416 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |