CN106544050A - The cyclic utilization system and its method of damaged tire - Google Patents
The cyclic utilization system and its method of damaged tire Download PDFInfo
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- CN106544050A CN106544050A CN201611026824.1A CN201611026824A CN106544050A CN 106544050 A CN106544050 A CN 106544050A CN 201611026824 A CN201611026824 A CN 201611026824A CN 106544050 A CN106544050 A CN 106544050A
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- cracking
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- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/002—Removal of contaminants
- C10K1/003—Removal of contaminants of acid contaminants, e.g. acid gas removal
- C10K1/004—Sulfur containing contaminants, e.g. hydrogen sulfide
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/12—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/30—Alkali metal compounds
- B01D2251/304—Alkali metal compounds of sodium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/604—Hydroxides
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The invention discloses a kind of cyclic utilization system of damaged tire, damaged tire breaker is connected with the feeding end of continuous cracking device, heater is connected with the heat supply end of continuous cracking device, the slag output end of continuous cracking device is connected with carbon black conveying device, and the oil gas outlet side Jing separators of continuous cracking device are connected with two-way oil gas cooling device；The waste gas outlet of continuous cracking device is connected with heater all the way, and another road is connected with smoke eliminator；In two-way oil gas cooling device, at least the end of oil gas cooling device is connected with combustible gas purifying tower by not condenser cooler all the way, and combustible gas purifying tower is connected with heater all the way, and another road is connected with emergent torch；Also disclose a kind of circulation utilization method of damaged tire.The present invention not only can carry out recycling to damaged tire, additionally it is possible to carry out recycling to the available resources in removal process.
Description
Technical field
The invention belongs to damaged tire recovery technology field, and in particular to a kind of cyclic utilization system of damaged tire and its side
Method.
Background technology
The recycling of damaged tire has become development trend, but the recycling of damaged tire is only to damaged tire at present
Itself carry out recycling, and the available resources produced in recovery process it is basic nobody take into account.
The content of the invention
In view of this, present invention is primarily targeted at providing a kind of cyclic utilization system and its method of damaged tire.
To reach above-mentioned purpose, the technical scheme is that what is be achieved in that：
The embodiment of the present invention provides a kind of cyclic utilization system of damaged tire, and the system includes damaged tire breaker, connects
Continuous cracker, separator, oil gas cooling device, smoke eliminator, heater, combustible gas purifying tower, carbon black conveying device；Institute
The feeding end that damaged tire breaker is stated with continuous cracking device is connected, and the heater is connected with the heat supply end of continuous cracking device,
The slag output end of the continuous cracking device is connected with carbon black conveying device, the oil gas outlet side Jing separators of the continuous cracking device with
Two-way oil gas cooling device connects；The waste gas outlet of the continuous cracking device is connected with heater all the way, and another road is net with flue gas
Connection is put in makeup；In the two-way oil gas cooling device at least all the way the end of oil gas cooling device by not condenser cooler with
Combustible gas purifying tower connects, and the combustible gas purifying tower is connected with heater all the way, and another road is connected with emergent torch.
In such scheme, horizontal type cooler that the oil gas cooling device includes being sequentially connected, cooling jacket, accumulator tank；
The accumulator tank is connected with combustible gas purifying tower by fixed gas cooler.
In such scheme, the output end Jing cooler of the combustible gas purifying tower is connected with water sealed tank, air accumulator, institute in turn
State air accumulator to be connected with heater all the way, separately lead up to water sealed tank and be connected with emergent torch.
In such scheme, air-cooled cooler that the smoke eliminator includes being sequentially connected, water-cooling cooler, at least one
Individual alkali adsorption tower, column for smoke purification, the column for smoke purification are connected with chimney by air-introduced machine, and the alkali adsorption tower is connected with spray
Drench pump.
In such scheme, water-cooled discharging machine that the carbon black conveying device includes being sequentially connected, water-cooled elevator, belt are defeated
Send the magnetic separator being provided with above machine, bucket elevator, the belt conveyor for steel wire in carbon black is removed, the bucket type
Elevator is connected with carbon black transition feed bin by the long-range conveyer arranged above which.
The embodiment of the present invention also provides a kind of circulation utilization method of damaged tire, and the method is realized by following steps：
Step 1：Damaged tire crushing stage, for steel bead wire is removed by damaged tire of the diameter less than 90mm, is broken for 45-
The block rubber of 55mm, separates the ferrous metal in block rubber, and the block rubber after sorting is blended in one with low temperature sulfur transfer catalyst
Cracking is waited for after rising；
Step 2：Cleavage stages, outside first pass, fuel oil improves reaction temperature to 200-300 DEG C, starts cracking
Reaction, rubber cracking of the heavy constituent in block rubber by thermal cracking for gaseous material, i.e. macromolecular divide into the low hydrocarbon of small-molecular-weight
Son, crack the oil gas for producing it is cool it is solidifying after, collect cracked oil and cracking gas respectively；When reaction produce cracking gas by purify after energy
During enough persistently guarantee reaction temperatures, stop outside and then supply, using the cracking gas heat supply after purification, cracking reaction is continuously entered
OK；Solid phase after cracking is carbon black and steel scrap silk；
Step 3：Waste gas purification stage, the waste gas part in cracking reaction reaction are discharged after purification, one in addition
Divide for providing heat for reaction temperature.
In such scheme, the method also includes removing steel bead wire for the damaged tire with diameter greater than 90mm, is broken for
The block rubber of 45-55mm or so, the block rubber are broken into the micelle of 2～4mm again, remove the irony in micelle through magnetic separation
Metal, then by sorting by rubber grain and fiber separation, obtain can direct marketing micelle.
In such scheme, the method also includes being ground purity higher micelle again, and micelle is ground to 25 mesh
Hereinafter, then by screening is centrifuged, rubber powder is obtained, residue on sieve comes back for milling grinding.
Compared with prior art, beneficial effects of the present invention：
The present invention not only can carry out recycling to damaged tire, additionally it is possible to the available resources in removal process
Carry out recycling.
Description of the drawings
Fig. 1 provides a kind of structured flowchart of the cyclic utilization system of damaged tire for the embodiment of the present invention；
Fig. 2 provides a kind of structural representation of the oil gas cooling device of the cyclic utilization system of damaged tire for the embodiment of the present invention
Figure；
Fig. 3 provides a kind of structural representation of the smoke eliminator of the cyclic utilization system of damaged tire for the embodiment of the present invention
Figure；
Fig. 4 provides a kind of structural representation of the carbon black conveying device of the cyclic utilization system of damaged tire for the embodiment of the present invention
Figure.
Specific embodiment
In order that the objects, technical solutions and advantages of the present invention become more apparent, it is below in conjunction with drawings and Examples, right
The present invention is further elaborated.It should be appreciated that specific embodiment described herein is only to explain the present invention, and
It is not used in the restriction present invention.
The embodiment of the present invention provides a kind of cyclic utilization system of damaged tire, as shown in figure 1, the system includes that damaged tire breaks
Crushing device 1, continuous cracking device 2, separator 3, oil gas cooling device 4, smoke eliminator 5, heater 6, combustible gas purifying tower
7th, carbon black conveying device 8；The damaged tire breaker 1 is connected with the feeding end of continuous cracking device 2, the heater 6 with even
The heat supply end connection of continuous cracker 2, the slag output end of the continuous cracking device 2 are connected with carbon black conveying device 8, the continuous cracking
The oil gas outlet side Jing separator 3 of device 2 is connected with two-way oil gas cooling device 4；The waste gas outlet of the continuous cracking device 2 is all the way
It is connected with heater 6, another road is connected with smoke eliminator 5；In the two-way oil gas cooling device 4, at least oil gas is cold all the way
But the end of device 4 is connected with combustible gas purifying tower 7 by not condenser cooler, 7 one tunnel of combustible gas purifying tower with heat
Device 6 connects, and another road is connected with emergent torch 9.
The damaged tire breaker 1 is by batcher, high inclination angle conveyer, transition feed bin, batcher, belt conveyer scale, catalysis
Agent feeder and feed screw composition, for damaged tire block is delivered to transition feed bin, then percutaneous belt scale weighing are delivered to
In feed screw, additive is added in feed screw by catalyst feeder, broken by the feed screw
Block rubber be supplied to continuous cracking device 2.
The continuous cracking device 2 is made up of intelligent metering charger, continuous cracking device, for by block rubber and catalyst one
Rise and cracker is continuously introduced into by intelligent metering charger, carry out cracking cracking reaction, the coarse carbon black and steel of acquisition at ambient pressure
Silk Jing carbon blacks conveying device 8 is exported, and the oil gas of acquisition is exported into separator 3.The heater 6 produce high-temperature flue gas with follow
After the flue gas mixing that ring is utilized, the heat for needed for the cracking of damaged tire is provided reduces fuel consumption, reduces the row of flue gas
High-volume.The fuel of the heater 6 mainly cracks the not solidifying combustible gas for producing using damaged tire, need to be using outer when production line starts
Purchase fuel, diesel oil or fuel gas.
As shown in Fig. 2 the oil gas cooling device 4 includes the horizontal type cooler 401 being sequentially connected, cooling jacket 402, collects
Oil tank 403；The accumulator tank 403 is connected with combustible gas purifying tower 7 by fixed gas cooler；It is oil gas Jing separators 3, horizontal cold
But, after device 401 and cooling jacket 402 are cooled down, separated, fluid oil enters accumulator tank 403, is delivered to tank field by oil pump, does not coagulate
Combustible gas is entered.
As shown in figure 3, the smoke eliminator 5 include being sequentially connected air-cooled cooler 501, water-cooling cooler 502,
At least one alkali adsorption tower 503, column for smoke purification 504, the column for smoke purification 504 are connected with chimney 506 by air-introduced machine 505
Connect, the alkali adsorption tower 503 is connected with spray pump 507；From continuous cracking device discharge recycle after a small amount of flue gas Jing wind
After cold cooler 501 and water-cooling cooler 502 are cooled down, into alkali adsorption tower 503 and column for smoke purification 504, Jing after multistage purification
Qualified discharge；503 inner absorbent of the alkali adsorption tower adopts sodium hydroxide solution, the main SOx absorbed in flue gas, NOx and
The harmful components such as grain thing, filling active carbon filler in the column for smoke purification 504, by physical absorption fine processing flue gas
The harmful components such as SOx, NOx and particulate matter.
The output end Jing cooler of the combustible gas purifying tower 7 is connected with water sealed tank, air accumulator, the air accumulator one in turn
Road is connected with heater 6, is separately led up to water sealed tank and is connected with emergent torch 9；Do not coagulate combustible gas to enter by fixed gas cooler
After the cooling of one step, Jing after combustible gas purifying tower 7 is purified, in the presence of total head blower fan, Jing water sealed tanks send into vacuum tank, Jing voltage stabilizings
Burn into combustor after tank voltage stabilizing；, for NaOH solution, main absorption do not coagulate in combustible gas for the absorbent that combustible gas purifying is adopted
The harmful components such as sulfide；The combustible gas that do not coagulate after purification all sends into combustor as fuel, and the heat for producing that burns is used
Crack in damaged tire.
As shown in figure 4, the carbon black conveying device 8 include being sequentially connected water-cooled discharging machine 801, water-cooled elevator 802,
Be provided with above belt conveyor 803, bucket elevator 804, the belt conveyor 803 for by carbon black steel wire remove
Magnetic separator 805, the bucket elevator 804 are connected with carbon black transition feed bin 807 by the long-range conveyer 806 arranged above which
Connect.
The embodiment of the present invention also provides a kind of circulation utilization method of damaged tire, and the method is realized by following steps：
Step 1：Damaged tire crushing stage, for steel bead wire is removed by damaged tire of the diameter less than 90mm, is broken for 45-
The block rubber of 55mm, separates the ferrous metal in block rubber, and the block rubber after sorting is blended in one with low temperature sulfur transfer catalyst
Cracking is waited for after rising；
Step 2：Cleavage stages, outside first pass, fuel oil improves reaction temperature to 200-300 DEG C, starts cracking
Reaction, rubber cracking of the heavy constituent in block rubber by thermal cracking for gaseous material, i.e. macromolecular divide into the low hydrocarbon of small-molecular-weight
Son, crack the oil gas for producing it is cool it is solidifying after, collect cracked oil and cracking gas respectively；When reaction produce cracking gas by purify after energy
During enough persistently guarantee reaction temperatures, stop outside and then supply, using the cracking gas heat supply after purification, cracking reaction is continuously entered
OK；Solid phase after cracking is carbon black and steel scrap silk；
Step 3：Waste gas purification stage, the waste gas part in cracking reaction reaction are discharged after purification, one in addition
Divide for providing heat for reaction temperature.
The method also includes removing steel bead wire for the damaged tire with diameter greater than 90mm, is broken for 45-55mm or so
Block rubber, the block rubber is broken into the micelle of 2～4mm again, removes the ferrous metal in micelle through magnetic separation, then passes through
Sorting by rubber grain and fiber separation, obtain can direct marketing micelle.
The method also includes being ground purity higher micelle again, micelle is ground to below 25 mesh, then is passed through
Centrifugation screening, obtains rubber powder, and residue on sieve comes back for milling grinding.
The above, only presently preferred embodiments of the present invention is not intended to limit protection scope of the present invention.
Claims (8)
1. a kind of cyclic utilization system of damaged tire, it is characterised in that the system includes damaged tire breaker, continuous cracking
Device, separator, oil gas cooling device, smoke eliminator, heater, combustible gas purifying tower, carbon black conveying device；The useless wheel
Tire breaker is connected with the feeding end of continuous cracking device, and the heater is connected with the heat supply end of continuous cracking device, the company
The slag output end of continuous cracker is connected with carbon black conveying device, the oil gas outlet side Jing separators of the continuous cracking device and two road binders
Air cooling device connects；The waste gas outlet of the continuous cracking device is connected with heater all the way, another road and smoke eliminator
Connection；In the two-way oil gas cooling device, at least the end of oil gas cooling device passes through not condenser cooler and combustible gas all the way
Purifying column connects, and the combustible gas purifying tower is connected with heater all the way, and another road is connected with emergent torch.
2. the cyclic utilization system of damaged tire according to claim 1, it is characterised in that：The oil gas cooling device includes
The horizontal type cooler that is sequentially connected, cooling jacket, accumulator tank；The accumulator tank is by fixed gas cooler and combustible gas purifying tower
Connection.
3. the cyclic utilization system of damaged tire according to claim 1 and 2, it is characterised in that：The combustible gas purifying tower
Output end Jing cooler be connected with water sealed tank, air accumulator in turn, the air accumulator is connected with heater all the way, is separately led up to
Water sealed tank is connected with emergent torch.
4. the cyclic utilization system of damaged tire according to claim 3, it is characterised in that：The smoke eliminator includes
The air-cooled cooler that is sequentially connected, water-cooling cooler, at least one alkali adsorption tower, column for smoke purification, the column for smoke purification lead to
Cross air-introduced machine to be connected with chimney, the alkali adsorption tower is connected with spray pump.
5. the cyclic utilization system of damaged tire according to claim 4, it is characterised in that：The carbon black conveying device includes
Arrange above the water-cooled discharging machine that is sequentially connected, water-cooled elevator, belt conveyor, bucket elevator, the belt conveyor
There is the magnetic separator for steel wire in carbon black is removed, the bucket elevator passes through long-range conveyer and the carbon black arranged above which
Transition feed bin connects.
6. a kind of circulation utilization method of damaged tire, it is characterised in that：The method is realized by following steps：
Step 1：Damaged tire crushing stage, for steel bead wire is removed by damaged tire of the diameter less than 90mm, is broken for 45-55mm
Block rubber, separate the ferrous metal in block rubber, after the block rubber after sorting and low temperature sulfur transfer catalyst are mixed
Wait for cracking；
Step 2：Cleavage stages, outside first pass, fuel oil improves reaction temperature to 200-300 DEG C, starts to occur cracking instead
Should, the heavy constituent in block rubber by thermal cracking for gaseous material, i.e. macromolecular rubber cracking into small-molecular-weight low hydrocarbon molecule,
Oil gas that cracking is produced it is cool it is solidifying after, collect cracked oil and cracking gas respectively；When the cracking gas that reaction is produced can after purification
When persistently ensureing reaction temperature, stop outside and then supply, using the cracking gas heat supply after purification, cracking reaction is carried out continuously；
Solid phase after cracking is carbon black and steel scrap silk；
Step 3：Waste gas purification stage, the waste gas part in cracking reaction reaction are discharged after purification, and another part is used
In providing heat for reaction temperature.
7. the circulation utilization method of a kind of damaged tire according to claim 7, it is characterised in that：The method also include for
Steel bead wire is removed by the damaged tire with diameter greater than 90mm, is broken for the block rubber of 45-55mm or so, and the block rubber is broken again
The micelle of 2～4mm is broken into, and the ferrous metal in micelle is removed through magnetic separation, then by sorting by rubber grain and fiber separation,
Obtain can direct marketing micelle.
8. the circulation utilization method of a kind of damaged tire according to claim 8, it is characterised in that：The method also includes will be pure
The higher micelle of degree is ground again, and micelle is ground to below 25 mesh, then by screening is centrifuged, obtains rubber powder, residue on sieve
Come back for milling grinding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611026824.1A CN106544050A (en) | 2016-11-16 | 2016-11-16 | The cyclic utilization system and its method of damaged tire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611026824.1A CN106544050A (en) | 2016-11-16 | 2016-11-16 | The cyclic utilization system and its method of damaged tire |
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| Publication Number | Publication Date |
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| CN106544050A true CN106544050A (en) | 2017-03-29 |
Family
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| CN201611026824.1A Pending CN106544050A (en) | 2016-11-16 | 2016-11-16 | The cyclic utilization system and its method of damaged tire |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107057745A (en) * | 2017-06-21 | 2017-08-18 | 重庆市聚洪环保科技有限公司 | A kind of low temperature continuous cracking system for rubber |
| CN107177368A (en) * | 2017-07-19 | 2017-09-19 | 山西鑫邦国际橡塑科技开发有限公司 | The continuous thermal splitting system of junked tire normal pressure |
| CN107384458A (en) * | 2017-09-05 | 2017-11-24 | 柳州淦源环保科技有限公司 | The black system and method for a kind of high temperature pyrolysis reaction device and junked tire pyrolysis oil preparation, charcoal processing |
| CN107459996A (en) * | 2017-08-10 | 2017-12-12 | 无锡龙盈环保科技有限公司 | A kind of processing equipment of junked tire |
| CN112358746A (en) * | 2020-11-09 | 2021-02-12 | 江西省永固新能源炭黑有限公司 | Scrap tire schizolysis carbon black carbonization system |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| US12031097B2 (en) | 2022-10-12 | 2024-07-09 | Ecolab Usa Inc. | Antifouling agents for plastic-derived synthetic feedstocks |
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| CN106085490A (en) * | 2016-08-05 | 2016-11-09 | 南京绿帝环保能源科技有限公司 | Damaged tire moving-bed type cracker |
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| CN106085490A (en) * | 2016-08-05 | 2016-11-09 | 南京绿帝环保能源科技有限公司 | Damaged tire moving-bed type cracker |
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| 丁忠浩等: "《固体和气体废弃物再生与利用》", 31 March 2006, 国防工业出版社 * |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107057745A (en) * | 2017-06-21 | 2017-08-18 | 重庆市聚洪环保科技有限公司 | A kind of low temperature continuous cracking system for rubber |
| CN107177368A (en) * | 2017-07-19 | 2017-09-19 | 山西鑫邦国际橡塑科技开发有限公司 | The continuous thermal splitting system of junked tire normal pressure |
| CN107177368B (en) * | 2017-07-19 | 2022-10-18 | 威海启成科技发展有限公司 | Normal-pressure continuous thermal cracking system for waste tires |
| CN107459996A (en) * | 2017-08-10 | 2017-12-12 | 无锡龙盈环保科技有限公司 | A kind of processing equipment of junked tire |
| CN107384458A (en) * | 2017-09-05 | 2017-11-24 | 柳州淦源环保科技有限公司 | The black system and method for a kind of high temperature pyrolysis reaction device and junked tire pyrolysis oil preparation, charcoal processing |
| CN107384458B (en) * | 2017-09-05 | 2023-09-29 | 柳州淦源环保科技有限公司 | System and method for preparing oil and carbon black by pyrolysis of waste tires through high-temperature pyrolysis reactor |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| CN112358746A (en) * | 2020-11-09 | 2021-02-12 | 江西省永固新能源炭黑有限公司 | Scrap tire schizolysis carbon black carbonization system |
| US12031097B2 (en) | 2022-10-12 | 2024-07-09 | Ecolab Usa Inc. | Antifouling agents for plastic-derived synthetic feedstocks |
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Application publication date: 20170329 |