CN102796550A - Cracking furnace for tire - Google Patents
Cracking furnace for tire Download PDFInfo
- Publication number
- CN102796550A CN102796550A CN201210206913XA CN201210206913A CN102796550A CN 102796550 A CN102796550 A CN 102796550A CN 201210206913X A CN201210206913X A CN 201210206913XA CN 201210206913 A CN201210206913 A CN 201210206913A CN 102796550 A CN102796550 A CN 102796550A
- Authority
- CN
- China
- Prior art keywords
- spherical tank
- pyrolysis stove
- dividing plate
- tire pyrolysis
- tire
- 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
- 238000005336 cracking Methods 0.000 title abstract description 13
- 238000012546 transfer Methods 0.000 claims abstract description 15
- 238000000197 pyrolysis Methods 0.000 claims description 15
- 239000000470 constituent Substances 0.000 claims description 6
- 239000002737 fuel gas Substances 0.000 claims description 6
- 238000009423 ventilation Methods 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 3
- 125000006850 spacer group Chemical group 0.000 claims description 2
- 238000000354 decomposition reaction Methods 0.000 abstract description 7
- 239000000446 fuel Substances 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract 5
- 239000007789 gas Substances 0.000 description 16
- 230000000694 effects Effects 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000002699 waste material 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
- 208000009714 Severe Dengue Diseases 0.000 description 1
- 208000036142 Viral infection Diseases 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- -1 tire Substances 0.000 description 1
- 239000004636 vulcanized rubber Substances 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- 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
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The invention discloses a cracking furnace for a tire. The cracking furnace for the tire comprises a cracking furnace body, a connection tube, a spherical tank, and a separation tower; the connection tube is connected with the cracking furnace body and the spherical tank; a spiral separation plate is arranged in the spherical tank, and the bottom of the spherical tank is provided with a discharge port which is connected with the cracking furnace body; the separation tower is arranged on the top of the spherical tank; a condenser is arranged on the top in the separation tower; a distributor is arranged underneath the condenser; and the condenser is provided with a separation port which is connected with external transfer tanks. The cracking furnace for the tire has the advantages of high decomposition degree, high product quality, low fuel consumption, low environmental pollution and the like.
Description
Technical field
The present invention relates to a kind of pyrolyzer, relate to a kind of pyrolyzer that can be used for waste and old raw materials such as tire, plastics particularly.
Background technology
Because the prosperity that drives steam turbine turner industry of prosperous economy, whole world Motor vehicles number increases rapidly, have every year 2000000000 to 3,000,000,000 damaged tires to produce approximately, and China also can produce any more several hundred million junked tire every year.Junked tire is mainly synthesized by vulcanized rubber, and its character is highly stable, can in physical environment, continue more than 100 years and unlikely addling.In addition, the elasticity of junked tire is good, toughness is strong, can't therefore occupy a large amount of space, traditional landfill site and cause landfill site shortening working life, so be not suitable for burying with general waste with the mechanical force compacting.As if arbitrarily banking up and meeting rain ponding, then might cause the generation of singapore hemorrhagic fever disease.Except that taking up space; Junked tire contains high heating value, stores accidentally very easily catching fire if pile up, and not only produces virose dioxin gas and causes atmospheric pollution; The molten oil that is produced, slag also can permeate the ground and cause soil and phreatic pollution, have a strong impact on environment and quality of life.Therefore, the junked tire problem will cause the serious environmental pollution problem if can't deal carefully with.
Treatment process to junked tire has at present: one, utilize again: be about to the damaged tire renovation, and tire grinds into fine glue powder etc.Two, rubber for tire is cracked into combustible gas and products such as liquid oil, carbon black.Yet, in the existing pyrolyzer design, exist cracking insufficient usually, the quality product after the cracking is low, and gas entrainment impurity is many in the cracking process, often causes line clogging, causes defectives such as security incident.
Summary of the invention
The object of the present invention is to provide a kind of tire pyrolysis stove, to solve the problems referred to above that exist in the prior art.
Technical scheme provided by the invention is following:
A kind of tire pyrolysis stove is characterized in that, comprising:
One pyrolyzer body;
One pipe connecting, it connects pyrolyzer body and spherical tank;
One spherical tank, its inside are provided with a volution spacer plate, and the bottom is provided with a drain, and this drain is connected with the pyrolyzer body; And
One is located at the knockout tower at spherical tank top; Said knockout tower inner top is provided with a condensing surface; The condensing surface below is provided with one and is used for condensed fluid is turned back to spherical tank or is discharged into outside sparger, and said sparger is provided with a separating opening, and this separating opening connects outside transfer jar.
In preferred embodiment of the present invention, said pyrolyzer body is built-in spiral plate type.
In preferred embodiment of the present invention, this pipe connecting comprises a vertical section and a tilting section, wherein, vertically alternately is intervally distributed with a plurality of spoilers on the section at this.Its quantity is provided with as required.As 5-8.
In preferred embodiment of the present invention, said transfer jar comprises a heavy constituent transfer jar and a light constituent transfer jar.
In preferred embodiment of the present invention, the vertical air outlet of said knockout tower is connected to one group of cupping jar, and then is connected to the fuel gas inlet of pyrolyzer body bottom.This group cupping jar is used for storing and the transfer inflammable gas.
In preferred embodiment of the present invention, the lower end internal interval of this knockout tower alternately is provided with plural piece baffle plate.
In preferred embodiment of the present invention, said sparger comprises the following intercepting basin that traverses in the knockout tower inner chamber, and this intercepting basin is provided with at least one bar shaped air channel, and a dividing plate is all established on each air channel both sides, and the epimere of dividing plate is provided with ventilating pit; The inboard of each dividing plate is provided with at least one conduit, and each conduit and the dividing plate outside are provided with at least one pod apertures; Intercepting basin is established at the dividing plate top of each air channel, and last intercepting basin is connected with two dividing plate tops of air channel, and guarantees to have enough ventilation spaces; A distance above apart from base plate is provided with a separating opening, and said separating opening position is lower than pod apertures.
The xsect of said conduit is semicircle or square or trilateral.
The xsect of last intercepting basin is a V-arrangement.
Advantage of the present invention is following:
1, junked tire decomposes produces cracked gas and undecomposed particle completely, and moves upward along pipe connecting.Under the baffle effect that alternate intervals is provided with, most macrobeads are kept off down by baffle plate, and come back to decomposition again in the burner hearth.All the other continue to get in the spherical tank.Because the volume ratio pipeline of spherical tank is a lot of greatly, gas slows down suddenly in this speed, relends the barrier effect that helps the volution separator; Air-flow slowly rises twist; In this process, most fine particles and coarse particles are all precipitated, and deposit in the bottom of spherical tank.Get back to the pyrolyzer main body from the bottom again.Therefore, the present invention decomposes fully, and it is blocked to avoid pipeline of the prior art to be prone to, and decomposes incomplete drawback.
2, be provided with sparger, can let phlegma come back in the spherical tank, and then return cracking once more in the burner hearth, or be discharged on the transfer jar, make that phlegma can be according to the needs cracking of cracking degree.Cracked gas can become heavy constituent and light constituent is collected.
3, the inflammable gas after the decomposition can return the base burning of pyrolyzer main body through the outlet entering group cupping jar at knockout tower top.After treating trouble-free burning, the present invention even need not to add in addition fuel, the gas that only needs tire to decompose can be kept normal operation.Therefore, reduced pollution to environment.
Thereby, advantage such as it is little that the present invention has degree of decomposition height, good product quality and fuel consumption, and environmental pollution is little.
Description of drawings
Fig. 1 is the structural representation of tire pyrolysis stove of the present invention;
Fig. 2 is the structural representation of the knockout tower part of tire pyrolysis stove of the present invention;
Fig. 3 is the local structure synoptic diagram of sparger.
1 pyrolyzer main body
11 fuel gas inlets, 12 fuel gas inlets, 13 built-in screw type scraper plates
2 pipe connectings
21 vertical section 22 tilting sections 23 baffle plates
3 spherical tanks
31 inlets, 32 drains 33 detect mouthful 34 volution spherical separators
4 knockout towers
41 baffle plates, 42 fillers
Intercepting basin 43-2 dividing plate 43-3 separating opening 43-4 goes up intercepting basin 43-5 pod apertures under the 43 sparger 43-1
43-6 conduit 43-7 internal space 43-8 dividing plate epimere
44 condensing surfaces, 45 pneumatic outlets, 46 evacuation ports
5 transfer jars
6 transfer jars
Embodiment
Specific embodiment of the present invention, with reference to Fig. 1, a kind of tire pyrolysis stove mainly is made up of pyrolyzer main body 1, pipe connecting 2, spherical tank 3 and knockout tower 4 etc.
This pyrolyzer main body 1 is built-in helical flight formula (is prior art, also can adopts other pyrolyzer of the prior art), and it comprises a fixed urceolus and a rotatable built-in screw type scraper plate 13.Its bottom is provided with a fuel inlet 11 and a fuel gas inlet 12.This pyrolyzer is a prior art, and this part non-emphasis of the present invention, so do not give unnecessary details.
The top of this pyrolyzer main body 1 connects a pipe connecting 2, and this pipe connecting comprises vertical section 21 and one tilting section 22, wherein, vertically alternately is intervally distributed with some baffle plates 23 on the section 21 at this.The quantity of this baffle plate can be provided with as required, for example the 5-8 piece.The inlet 31 of the other end of this tilting section 22 and spherical tank 3 is connected.
The bottom of this spherical tank 3 is provided with a drain 32, and this drain 32 is connected with pyrolyzer main body 1 through a pipeline.The inside of this spherical tank is provided with a volution spherical separator 34, and the right side is provided with one and detects mouth 33, and a knockout tower 4 is established at the top.
Referring to Fig. 2, the lower end internal interval of this knockout tower 4 alternately is provided with some baffle plates 41, and the quantity of this baffle plate can be provided with as required, for example the 3-5 piece.The baffle plate top is provided with filler 42, and top interior is provided with condensing surface 44, between the top of condensing surface 44 belows, filler 42, is provided with a sparger 43.The top of knockout tower 4 is provided with pneumatic outlet 45, and it is connected to the fuel gas inlet 12 of pyrolyzer main body 1 through group cupping jar 7 through pipeline.
The concrete structure of this sparger 43 is following: it comprises the following intercepting basin 43-1 that traverses in the knockout tower inner chamber; Be interval with some bar shaped air channels on this intercepting basin 43-1; Each air channel both sides of the edge along its length are respectively equipped with a bar shaped dividing plate 43-2; The top of two dividing plate upper end 43-2 of each air channel is connected to become and is last intercepting basin 43-4, and in the present invention, xsect of intercepting basin is a V-arrangement on this.Dividing plate epimere 43-8 is provided with a plurality of ventilating pit (not shown)
The dividing plate medial surface is provided with the thrust-augmenting nozzle 43-6 that plurality of vertical is arranged in parallel, the spacing 2-10 of thrust-augmenting nozzle centimetre; Thrust-augmenting nozzle 43-6 and the dividing plate outside upper and lower each make a call to a pod apertures 43-5 (also can beat several), 1-5 centimetre at pod apertures interval more.Last intercepting basin 43-4 links to each other with the dividing plate top on each air channel both sides, and enough ventilation space 43-7 are arranged between the dividing plate, and separating opening 43-3 is through on pipe connection to the two transfer jar 5 and 6.The position of this separating opening is higher than the upper end 3-10 centimeters lateral opening of intercepting basin down, and the position is lower than pod apertures 43-5.
Use of the present invention is following: junked tire is put into pyrolyzer main body 1, heating, and the tire decomposes produces cracked gas and undecomposed particle completely, and moves upward along pipe connecting 2.Under baffle plate 23 effects that alternate intervals is provided with, most macrobeads are kept off down by baffle plate 23, and come back to decomposition again in the burner hearth.All the other continue to get in the spherical tank 2.
Because the volume ratio pipeline of spherical tank 2 is a lot of greatly, gas slows down suddenly in this speed, relends the barrier effect that helps the volution separator; Air-flow slowly rises twist; In this process, most fine particles and coarse particles are all precipitated, and deposit in the bottom of spherical tank 2.
Gas continues to rise, and gets into knockout tower 4, and the baffle plate 41 in the knockout tower 4 further precipitates unsegregated fine particle and gets back in the spherical tank 2.Liquid under air-flow gets into packing area 42 and refluxes carries out sufficient heat exchange and carries out rectifying; The clean gas of removing impurity through filler 42 continues to rise, and from the ventilation space 43-7 of sparger 43, passes, and flows out from the ventilating pit of dividing plate epimere 43-8; Continue to rise; Running into condensing surface 44 back condensations becomes liquid, drops onto on the catch tray 43-4, is slipped to then on the catch tray 43-1 of lower end.The fluid accumulation of base plate 43-1 is behind certain altitude, and the pod apertures 43-5 from dividing plate gets into the thrust-augmenting nozzle 43-6 automatically, is distributed to packing section more uniformly, carries out heat exchange with following splitting gas and gets back in the pyrolyzer 1.
As qualified through testing product, can open the valve of separating opening 43-3, because the separating opening position is lower than the pod apertures position, the liquid of following catch tray promptly flows out from separating opening 43-3, is placed in transfer jar 5 or 6.
In decomposition course, the macrobead part is at first stopped that by baffle plate 23 deposition, small-particle precipitate in the particle in spherical tank 2, and can get back to through the drain 32 of bottom and continue in the pyrolyzer main body 1 to decompose.
Inflammable gas after the decomposition can be got back to the base burning of pyrolyzer main body 1 through the outlet 45 at knockout tower 4 tops.After treating trouble-free burning, the present invention even need not other fuel, the gas that only needs tire to decompose can run well.
Above-mentionedly be merely a specific embodiment of the present invention, but design concept of the present invention is not limited thereto, allly utilizes this design that the present invention is carried out the change of unsubstantiality, all should belong to the behavior of invading protection domain of the present invention.
Claims (9)
1. a tire pyrolysis stove is characterized in that, comprising:
One pyrolyzer body;
One pipe connecting, it connects pyrolyzer body and spherical tank;
One spherical tank, its inside are provided with a volution spacer plate, and the bottom is provided with a drain, and this drain is connected with the pyrolyzer body; And
One is located at the knockout tower at spherical tank top, and said knockout tower inner top is provided with a condensing surface, and the condensing surface below is provided with one and is used for condensed fluid is turned back to spherical tank or is discharged into outside sparger; Said sparger is provided with a separating opening, and this separating opening connects outside transfer jar.
2. a kind of tire pyrolysis stove as claimed in claim 1 is characterized in that: said pyrolyzer is built-in spiral plate type.
3. a kind of tire pyrolysis stove as claimed in claim 1 is characterized in that: said pipe connecting comprises a vertical section and a tilting section, wherein, vertically alternately is intervally distributed with a plurality of spoilers on the section at this.
4. a kind of tire pyrolysis stove as claimed in claim 1 is characterized in that: said transfer jar comprises a heavy constituent transfer jar and a light constituent transfer jar.
5. a kind of tire pyrolysis stove as claimed in claim 1 is characterized in that: the vertical air outlet of said knockout tower is connected to one group of cupping jar, and then is connected to the fuel gas inlet of pyrolyzer body bottom.
6. a kind of tire pyrolysis stove as claimed in claim 1 is characterized in that: the lower end internal interval of this knockout tower alternately is provided with plural piece spoiler.
7. a kind of tire pyrolysis stove as claimed in claim 1; It is characterized in that: said sparger comprises the following intercepting basin that traverses in the knockout tower inner chamber; This intercepting basin is provided with at least one bar shaped air channel, and a dividing plate is all established on each air channel both sides, and the epimere of dividing plate is provided with ventilating pit; The inboard of each dividing plate is provided with at least one conduit, and each conduit and the dividing plate outside are provided with at least one pod apertures; Intercepting basin is established at the dividing plate top of each air channel, and last intercepting basin is connected with two dividing plate tops of air channel, and guarantees to have enough ventilation spaces; A distance above apart from base plate is provided with a separating opening, and said separating opening position is lower than pod apertures.
8. a kind of tire pyrolysis stove as claimed in claim 7 is characterized in that: the xsect of said conduit is semicircle or square or trilateral.
9. a kind of tire pyrolysis stove as claimed in claim 7 is characterized in that: the xsect of going up intercepting basin is a V-arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210206913.XA CN102796550B (en) | 2012-06-20 | 2012-06-20 | Cracking furnace for tire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210206913.XA CN102796550B (en) | 2012-06-20 | 2012-06-20 | Cracking furnace for tire |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102796550A true CN102796550A (en) | 2012-11-28 |
| CN102796550B CN102796550B (en) | 2014-06-04 |
Family
ID=47195861
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210206913.XA Expired - Fee Related CN102796550B (en) | 2012-06-20 | 2012-06-20 | Cracking furnace for tire |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102796550B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104789254A (en) * | 2015-03-25 | 2015-07-22 | 洛阳瑞泽石化工程有限公司 | Waste tire colloidal particle cracking equipment and cracking process thereof |
| CN110793377A (en) * | 2019-12-04 | 2020-02-14 | 何泽梁 | Anti-blocking condenser for bioreactor |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1074447C (en) * | 1999-06-08 | 2001-11-07 | 周鼎力 | Process and equipment for producing gasoline and diesel oil with waste plastics and/or heavy oil |
| CN101307151A (en) * | 2008-03-21 | 2008-11-19 | 北京清大鲁银科技发展有限公司 | Apparatus for treating waste and old tyres |
| CN201161996Y (en) * | 2008-02-20 | 2008-12-10 | 韩丽 | Environment friendly slag withdrawal equipment on horizontal rotating plastic, rubber oil refining apparatus |
| CN101343549A (en) * | 2007-07-11 | 2009-01-14 | 山东西迪艾万达新能源有限公司 | Continuous oiling cracking technique and equipment for scrap tire |
| CN101560000B (en) * | 2009-06-03 | 2011-05-04 | 中国科学院兰州化学物理研究所 | Anti-destabilization flocculent precipitation reversed separating jar |
| JP2012012459A (en) * | 2010-06-30 | 2012-01-19 | Nk Corporation:Kk | Treatment apparatus for waste and method for treating waste |
| CN202610186U (en) * | 2012-06-20 | 2012-12-19 | 种传学 | Cracking furnace of tyre |
-
2012
- 2012-06-20 CN CN201210206913.XA patent/CN102796550B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1074447C (en) * | 1999-06-08 | 2001-11-07 | 周鼎力 | Process and equipment for producing gasoline and diesel oil with waste plastics and/or heavy oil |
| CN101343549A (en) * | 2007-07-11 | 2009-01-14 | 山东西迪艾万达新能源有限公司 | Continuous oiling cracking technique and equipment for scrap tire |
| CN201161996Y (en) * | 2008-02-20 | 2008-12-10 | 韩丽 | Environment friendly slag withdrawal equipment on horizontal rotating plastic, rubber oil refining apparatus |
| CN101307151A (en) * | 2008-03-21 | 2008-11-19 | 北京清大鲁银科技发展有限公司 | Apparatus for treating waste and old tyres |
| CN101560000B (en) * | 2009-06-03 | 2011-05-04 | 中国科学院兰州化学物理研究所 | Anti-destabilization flocculent precipitation reversed separating jar |
| JP2012012459A (en) * | 2010-06-30 | 2012-01-19 | Nk Corporation:Kk | Treatment apparatus for waste and method for treating waste |
| CN202610186U (en) * | 2012-06-20 | 2012-12-19 | 种传学 | Cracking furnace of tyre |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104789254A (en) * | 2015-03-25 | 2015-07-22 | 洛阳瑞泽石化工程有限公司 | Waste tire colloidal particle cracking equipment and cracking process thereof |
| CN110793377A (en) * | 2019-12-04 | 2020-02-14 | 何泽梁 | Anti-blocking condenser for bioreactor |
| CN110793377B (en) * | 2019-12-04 | 2021-10-08 | 山东华凯特化工技术装备有限公司 | Anti-blocking condenser for bioreactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102796550B (en) | 2014-06-04 |
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Address after: 450000 Henan Province, Zhengzhou City Traffic Road 27 Hengye District No. 41 hospital Patentee after: Seed propagation Patentee after: HENAN ASIA-PACIFIC ENERGY TECHNOLOGY Corp. Address before: 450000 Henan Province, Zhengzhou City Traffic Road 27 Hengye District No. 41 hospital Patentee before: Seed propagation Patentee before: HENAN ASIA-PACIFIC ENERGY TECHNOLOGY CO.,LTD. |
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Effective date of registration: 20141028 Address after: 476000 Henan Province, Shangqiu City Development Zone's Permanent Road South (Shangbo high-speed entrance 100 meters West) Patentee after: HENAN ASIA-PACIFIC ENERGY TECHNOLOGY Corp. Address before: 450000 Henan Province, Zhengzhou City Traffic Road 27 Hengye District No. 41 hospital Patentee before: Seed propagation Patentee before: HENAN ASIA-PACIFIC ENERGY TECHNOLOGY Corp. |
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Granted publication date: 20140604 Termination date: 20170620 |