CN107033941A - Tire micelle cracking apparatus and cracking technology - Google Patents
Tire micelle cracking apparatus and cracking technology Download PDFInfo
- Publication number
- CN107033941A CN107033941A CN201710356170.7A CN201710356170A CN107033941A CN 107033941 A CN107033941 A CN 107033941A CN 201710356170 A CN201710356170 A CN 201710356170A CN 107033941 A CN107033941 A CN 107033941A
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- Prior art keywords
- micelle
- cracking
- cracking reactor
- delivery line
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- 238000005336 cracking Methods 0.000 title claims abstract description 99
- 239000000693 micelle Substances 0.000 title claims abstract description 72
- 238000005516 engineering process Methods 0.000 title claims abstract description 15
- 238000007789 sealing Methods 0.000 claims abstract description 25
- 238000007599 discharging Methods 0.000 claims abstract description 16
- 230000005611 electricity Effects 0.000 claims abstract description 16
- 239000006229 carbon black Substances 0.000 claims abstract description 14
- 239000007789 gas Substances 0.000 claims description 65
- 229930195733 hydrocarbon Natural products 0.000 claims description 15
- 150000002430 hydrocarbons Chemical class 0.000 claims description 15
- 239000000571 coke Substances 0.000 claims description 13
- 238000006243 chemical reaction Methods 0.000 claims description 12
- 239000004215 Carbon black (E152) Substances 0.000 claims description 9
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 230000005484 gravity Effects 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 5
- 239000000084 colloidal system Substances 0.000 claims description 5
- 239000006148 magnetic separator Substances 0.000 claims description 5
- 239000010959 steel Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000000567 combustion gas Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 238000005194 fractionation Methods 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000003738 black carbon Substances 0.000 description 1
- 238000012962 cracking technique Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000004636 vulcanized rubber Substances 0.000 description 1
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
- C10B19/00—Heating of coke ovens by electrical means
-
- 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
- C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
-
- 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
- C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
-
- 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
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- 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)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The present invention relates to a kind of tire micelle cracking apparatus and cracking technology, including cracking reactor, the top of the cracking reactor is provided with micelle feed bin, and the discharging opening of micelle feed bin is connected by middle part hopper with the charging aperture of cracking reactor；The middle part hopper upper and lower ends are respectively equipped with the first push-pull valve and the second push-pull valve；The bottom of the cracking reactor is provided with sealing bolt conveyer, and the discharging opening of cracking reactor connects the charging aperture of sealing bolt conveyer, the discharging opening connection carbon black repository of sealing bolt conveyer by expansion joint；The bottom of the cracking reactor is provided with oil gas delivery line, and oil gas delivery line connection fractionating column, the bottom connection cracking oil tank of fractionating column, the top of fractionating column connects flammable gas delivery line, and flammable gas delivery line connects gas electricity generator.Using the cracking technology of the equipment, tire micelle can be transformed into reproducible carbon black, cracked oil and combustible gas in the environment of elevated-temperature seal, it is safe, it is pollution-free.
Description
Technical field
The present invention relates to a kind of cracking apparatus and cracking technology, especially a kind of tire micelle cracking apparatus and cracking work
Skill.
Background technology
The recycling of junked tire is the huge problem that today's society faces.How scientific and effective, environmental protection
And regeneration treatment junked tire is the problem in China or even the world with can producing distinct economic.China's junked tire is led at present
Processing mode is wanted to have been friends in the past tyre rebuilding, vulcanized rubber powder, reclaimed rubber, local method oil refining and some non-batch processing cracking technologies etc.,
Though a certain amount of junked tire of digestion can be handled and certain economic benefit can be produced to environment and occupational health
Negative effect is also fairly obvious, and being badly in need of one kind at present can handle junked tire while again to scientific and effective and environmental protection
The junked tire New Process for Treatment of good economic benefit can be brought for enterprise.
The content of the invention
The purpose of the present invention is to overcome the deficiencies in the prior art there is provided a kind of tire micelle cracking apparatus and cracking
Technique, can transform into reproducible carbon black, cracked oil and combustible gas, security by tire micelle in the environment of elevated-temperature seal
Height, it is pollution-free.
The technical scheme provided according to the present invention, the tire micelle cracking apparatus, including cracking reactor, its feature
It is：The top of the cracking reactor is provided with micelle feed bin, and the discharging opening of micelle feed bin passes through middle part hopper and cracking reactor
Charging aperture be connected；The middle part hopper upper and lower ends are respectively equipped with the first push-pull valve and the second push-pull valve；The cracking is anti-
The bottom of device is answered to be provided with sealing bolt conveyer, the discharging opening of cracking reactor connects sealing bolt conveyer by expansion joint
Charging aperture, the discharging opening connection carbon black repository of sealing bolt conveyer；The bottom of the cracking reactor is exported provided with oil gas
Pipe, oil gas delivery line connection fractionating column, the bottom connection cracking oil tank of fractionating column, the top connection combustible gas export of fractionating column
Pipe, flammable gas delivery line connects gas electricity generator.
Further, the cracking reactor is that electrical heating is provided with Double-layer sleeve-type, chuck, and inner tube is reaction compartment.
Further, the 3rd push-pull valve is provided between the discharging opening and expansion joint of the cracking reactor.
Further, the flammable gas delivery line is provided with blower fan.
The tire micelle cracking technology, it is characterized in that, comprise the following steps：
（a）Micelle is fitted into micelle feed bin；
（b）The first push-pull valve is first opened, micelle enters middle part hopper, is then shut off the first push-pull valve, opens the second push-pull valve, glue
Grain enters cracking reactor, closes the second push-pull valve；
（c）Micelle internally falls under gravity after entering cracking reactor, and the heating-up temperature of cracking reactor is 450-
Between 500 DEG C, micelle begins to cracking in this temperature range；In course of reaction, micelle is converted to hydrocarbon gas and coke,
Hydrocarbon gas is transported under fractionation column base, coke by oil gas delivery line and falls on cracking reactor bottom, defeated by sealing screw
Machine is sent to be cooled down after discharging into carbon black storage silo；
（d）Hydrocarbon gas is fractionated into combustible gas and cracked oil after entering fractionating column；Combustible gas is delivered to by flammable gas delivery line
Gas electricity generator generates electricity；The storage of cracked oil tank is fallen under after cracked oil condensation.
Further, the micelle is that junked tire is formed through broken, and unnecessary steel wire, colloid diameter are removed by magnetic separator
For 1-15mm.
Further, the outlet pressure of the oil gas delivery line is -400-0pa.
Tire micelle cracking apparatus and cracking technology of the present invention, can turn tire micelle in the environment of elevated-temperature seal
It is melted into as reproducible carbon black, cracked oil and combustible gas, it is safe, it is pollution-free.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Embodiment
With reference to specific accompanying drawing, the invention will be further described.
As shown in Figure 1：The tire micelle cracking apparatus includes micelle feed bin 1, the first push-pull valve 2, middle part hopper 3, the
Two push-pull valves 4, cracking reactor 5, expansion joint 6, the 3rd push-pull valve 7, sealing bolt conveyer 8, carbon black repository 9, combustion gas hair
Motor 10, flammable gas delivery line 11, blower fan 12, fractionating column 13, oil gas delivery line 14, cracking oil tank 15 etc..
As shown in figure 1, the present invention includes cracking reactor 5, cracking reactor 5 is provided with electricity in Double-layer sleeve-type, chuck
Heating, inner tube is reaction compartment, and the top of cracking reactor 5 is provided with micelle feed bin 1, and the discharging opening of micelle feed bin 1 passes through middle part
Hopper 3 is connected with the charging aperture of cracking reactor 5；The upper and lower ends of middle part hopper 3 are respectively equipped with the first push-pull valve 2 and
Two push-pull valves 4；The bottom of the cracking reactor 5 is provided with sealing bolt conveyer 8, and the discharging opening of cracking reactor 5 passes through swollen
Swollen section 6 connects the charging aperture of sealing bolt conveyer 8, and the 3rd plate is provided between the discharging opening and expansion joint 6 of cracking reactor 5
Valve 7, the discharging opening connection carbon black repository 9 of sealing bolt conveyer 8；The bottom of cracking reactor 5 is provided with oil gas delivery line 14,
Oil gas delivery line 14 connects fractionating column 13, and the bottom connection of fractionating column 13 cracks oil tank 15, and the top connection of fractionating column 13 is flammable
Gas delivery line 11, flammable gas delivery line 11 is provided with blower fan 12, and flammable gas delivery line 11 connects gas electricity generator 10.
The operation principle and the course of work of the present invention：As shown in figure 1, the micelle being stored in micelle feed bin 1 is by first
The alternating folding running of the push-pull valve 4 of push-pull valve 2 and second, micelle is sent into cracking reactor 5, sky is avoided while feeding
Gas enters in cracking reactor 5, it is to avoid it is dangerous that a large amount of oxygen in air mix generation with fuel gas；Cracking reactor 5 is
Electrical heating in Double-layer sleeve-type, chuck is heated to the micelle in inner tube, and thermal source can be controlled accurately, controls the temperature of cracking
Spend for 450-500 DEG C, temperature is uniform so that cracking process will not produce pernicious gas；Whole cracking reactor 5 is vertical peace
Put, micelle relies on gravity fall, without Powered Propulsion；Threeth push-pull valve 7 of the cracking black carbon by bottom is generated after micelle reaction
And the running of sealing spiral conveyer 8 is transported to carbon black repository 9 and cools down and send into downstream treatment systems；Generation oil gas passes through oil
Gas delivery line 14 is exported, and into fractionating column 13, fractionation turns into cracked oil and fuel gas；Fuel gas supplies gas electricity generator 10, hair
Electricity provides the heat energy of cracking reactor；Cracked oil condensation is sunk, and is stored in cracking oil tank 15 and is further processed.
Embodiment one：A kind of tire micelle cracking technology, comprises the following steps：
（a）By junked tire through broken micelle, unnecessary steel wire is removed by magnetic separator, colloid diameter is 1mm, load glue
In pellet storehouse 1；
（b）The first push-pull valve 2 is first opened, micelle enters middle part hopper 3, is then shut off the first push-pull valve 2, opens the second push-pull valve
4, micelle enters cracking reactor 5, closes the second push-pull valve 4；This process can continuously repeat progress, it is ensured that continuous feed with it is close
Envelope；
（c）Micelle internally falls under gravity after entering cracking reactor, and the heating-up temperature of cracking reactor is 450
DEG C, micelle begins to cracking, electrically heated good control, it is ensured that micelle thermally equivalent, it is to avoid local mistake in this temperature range
Hot or insufficient reaction；In course of reaction, rubber is converted to hydro carbons and coke, in such circumstances, and hydro carbons is all gaseous state, by
Closed oil gas delivery line 14 is transported to the bottom of fractionating column 13, and cracking reactor oil gas vent pressure limit is -400-0pa；It is raw
Into coke under fall on the bottom of cracking reactor 5, coke enters after being discharged by sealing spiral conveyer 8 into carbon black storage silo 9
Row cooling；Used when 3rd push-pull valve 7 is maintenance, be normally opened under normal condition；Sealing spiral conveyer 8 is the mode of materials envelope
Realize the combination of sealing and conveying, it is ensured that completely cut off the entrance of air in operation；
（d）The hydrocarbon gas being cracked to form is fractionated into combustible gas and cracked oil after entering fractionating column 13；Combustible gas is by blower fan 12
Take away, delivering to gas electricity generator 10 by flammable gas delivery line 11 generates electricity；Blower fan 12 controls for PLC module, it is ensured that system is micro-
Negative pressure；Cracked oil tank 15 is fallen under after cracked oil condensation to store, and can carry out the processing of next stage.
Embodiment two：A kind of tire micelle cracking technology, comprises the following steps：
（a）By junked tire through broken micelle, unnecessary steel wire is removed by magnetic separator, colloid diameter is 15mm, loaded
In micelle feed bin 1；
（b）The first push-pull valve 2 is first opened, micelle enters middle part hopper 3, is then shut off the first push-pull valve 2, opens the second push-pull valve
4, micelle enters cracking reactor 5, closes the second push-pull valve 4；This process can continuously repeat progress, it is ensured that continuous feed with it is close
Envelope；
（c）Micelle internally falls under gravity after entering cracking reactor, and the heating-up temperature of cracking reactor is 500
DEG C, micelle begins to cracking, electrically heated good control, it is ensured that micelle thermally equivalent, it is to avoid local mistake in this temperature range
Hot or insufficient reaction；In course of reaction, rubber is converted to hydro carbons and coke, in such circumstances, and hydro carbons is all gaseous state, by
Closed oil gas delivery line 14 is transported to the bottom of fractionating column 13, and cracking reactor oil gas vent pressure limit is -400-0pa；It is raw
Into coke under fall on the bottom of cracking reactor 5, coke enters after being discharged by sealing spiral conveyer 8 into carbon black storage silo 9
Row cooling；Used when 3rd push-pull valve 7 is maintenance, be normally opened under normal condition；Sealing spiral conveyer 8 is the mode of materials envelope
Realize the combination of sealing and conveying, it is ensured that completely cut off the entrance of air in operation；
（d）The hydrocarbon gas being cracked to form is fractionated into combustible gas and cracked oil after entering fractionating column 13；Combustible gas is by blower fan 12
Take away, delivering to gas electricity generator 10 by flammable gas delivery line 11 generates electricity；Blower fan 12 controls for PLC module, it is ensured that system is micro-
Negative pressure；Cracked oil tank 15 is fallen under after cracked oil condensation to store, and can carry out the processing of next stage.
Embodiment three：A kind of tire micelle cracking technology, comprises the following steps：
（a）By junked tire through broken micelle, unnecessary steel wire is removed by magnetic separator, colloid diameter is 10mm, loaded
In micelle feed bin 1；
（b）The first push-pull valve 2 is first opened, micelle enters middle part hopper 3, is then shut off the first push-pull valve 2, opens the second push-pull valve
4, micelle enters cracking reactor 5, closes the second push-pull valve 4；This process can continuously repeat progress, it is ensured that continuous feed with it is close
Envelope；
（c）Micelle internally falls under gravity after entering cracking reactor, and the heating-up temperature of cracking reactor is 460
DEG C, micelle begins to cracking, electrically heated good control, it is ensured that micelle thermally equivalent, it is to avoid local mistake in this temperature range
Hot or insufficient reaction；In course of reaction, rubber is converted to hydro carbons and coke, in such circumstances, and hydro carbons is all gaseous state, by
Closed oil gas delivery line 14 is transported to the bottom of fractionating column 13, and cracking reactor oil gas vent pressure limit is -400-0pa；It is raw
Into coke under fall on the bottom of cracking reactor 5, coke enters after being discharged by sealing spiral conveyer 8 into carbon black storage silo 9
Row cooling；Used when 3rd push-pull valve 7 is maintenance, be normally opened under normal condition；Sealing spiral conveyer 8 is the mode of materials envelope
Realize the combination of sealing and conveying, it is ensured that completely cut off the entrance of air in operation；
（d）The hydrocarbon gas being cracked to form is fractionated into combustible gas and cracked oil after entering fractionating column 13；Combustible gas is by blower fan 12
Take away, delivering to gas electricity generator 10 by flammable gas delivery line 11 generates electricity；Blower fan 12 controls for PLC module, it is ensured that system is micro-
Negative pressure；Cracked oil tank 15 is fallen under after cracked oil condensation to store, and can carry out the processing of next stage.
Claims (7)
1. a kind of tire micelle cracking apparatus, including cracking reactor（5）, it is characterized in that：The cracking reactor（5）Top
Provided with micelle feed bin（1）, micelle feed bin（1）Discharging opening pass through middle part hopper（3）With cracking reactor（5）Charging aperture be connected
It is logical；The middle part hopper（3）Upper and lower ends are respectively equipped with the first push-pull valve（2）With the second push-pull valve（4）；The cracking reactor
（5）Bottom be provided with sealing bolt conveyer（8）, cracking reactor（5）Discharging opening pass through expansion joint（6）Connect sealing bolt
Conveyer（8）Charging aperture, sealing bolt conveyer（8）Discharging opening connection carbon black repository（9）；The cracking reactor
（5）Bottom be provided with oil gas delivery line（14）, oil gas delivery line（14）Connect fractionating column（13）, fractionating column（13）Bottom connection
Crack oil tank（15）, fractionating column（13）Top connect flammable gas delivery line（11）, flammable gas delivery line（11）Connect combustion gas hair
Motor（10）.
2. tire micelle cracking apparatus as claimed in claim 1, it is characterized in that：The cracking reactor（5）For bilayer sleeve
Electrical heating is provided with formula, chuck, inner tube is reaction compartment.
3. tire micelle cracking apparatus as claimed in claim 1, it is characterized in that：The cracking reactor（5）Discharging opening with
Expansion joint（6）Between be provided with the 3rd push-pull valve（7）.
4. tire micelle cracking apparatus as claimed in claim 1, it is characterized in that：The flammable gas delivery line（11）It is provided with wind
Machine（12）.
5. a kind of tire micelle cracking technology, it is characterized in that, comprise the following steps：
（a）Micelle is loaded into micelle feed bin（1）In；
（b）First open the first push-pull valve（2）, micelle enter middle part hopper（3）, it is then shut off the first push-pull valve（2）, open second
Push-pull valve（4）, micelle enters cracking reactor（5）, close the second push-pull valve（4）；
（c）Micelle internally falls under gravity after entering cracking reactor, and the heating-up temperature of cracking reactor is 450-
Between 500 DEG C, micelle begins to cracking in this temperature range；In course of reaction, micelle is converted to hydrocarbon gas and coke,
Hydrocarbon gas is by oil gas delivery line（14）It is transported to fractionating column（13）Cracking reactor is fallen under bottom, coke（5）Bottom, passes through
Sealing spiral conveyer（8）Enter carbon black storage silo after discharge（9）Cooled down；
（d）Hydrocarbon gas enters fractionating column（13）After be fractionated into combustible gas and cracked oil；Combustible gas passes through flammable gas delivery line
（11）Deliver to gas electricity generator（10）Generate electricity；Cracked oil tank is fallen under after cracked oil condensation（15）Storage.
6. tire micelle cracking technology as claimed in claim 5, it is characterized in that：The micelle is junked tire through broken
Into by the unnecessary steel wire of magnetic separator removal, colloid diameter is 1-15mm.
7. tire micelle cracking technology as claimed in claim 5, it is characterized in that：The oil gas delivery line（14）Outlet pressure
For -400-0pa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710356170.7A CN107033941A (en) | 2017-05-19 | 2017-05-19 | Tire micelle cracking apparatus and cracking technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710356170.7A CN107033941A (en) | 2017-05-19 | 2017-05-19 | Tire micelle cracking apparatus and cracking technology |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107033941A true CN107033941A (en) | 2017-08-11 |
Family
ID=59540618
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710356170.7A Pending CN107033941A (en) | 2017-05-19 | 2017-05-19 | Tire micelle cracking apparatus and cracking technology |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108722320A (en) * | 2018-06-08 | 2018-11-02 | 国宏中晶（北京）科技发展有限公司 | A kind of multiple batches of catalyst adding set and method of waste tire |
| CN109207185A (en) * | 2018-10-23 | 2019-01-15 | 荆门优尔迪资源循环利用有限公司 | A kind of method of waste tire resource reutilization |
| CN109628119A (en) * | 2018-11-05 | 2019-04-16 | 武汉科技大学 | A kind of scrap tire cracking furnace |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| US12031097B2 (en) | 2021-10-14 | 2024-07-09 | Ecolab Usa Inc. | Antifouling agents for plastic-derived synthetic feedstocks |
| US12304888B2 (en) | 2021-03-10 | 2025-05-20 | Ecolab Usa Inc. | Stabilizer additives for plastic-derived synthetic feedstock |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4250158A (en) * | 1978-02-15 | 1981-02-10 | Intenco, Inc. | Process for recovering carbon black and hydrocarbons from used tires |
| 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 |
| CN206902073U (en) * | 2017-05-19 | 2018-01-19 | 无锡市泰新环保科技有限公司 | Tire micelle cracking apparatus |
-
2017
- 2017-05-19 CN CN201710356170.7A patent/CN107033941A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4250158A (en) * | 1978-02-15 | 1981-02-10 | Intenco, Inc. | Process for recovering carbon black and hydrocarbons from used tires |
| 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 |
| CN206902073U (en) * | 2017-05-19 | 2018-01-19 | 无锡市泰新环保科技有限公司 | Tire micelle cracking apparatus |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108722320A (en) * | 2018-06-08 | 2018-11-02 | 国宏中晶（北京）科技发展有限公司 | A kind of multiple batches of catalyst adding set and method of waste tire |
| CN109207185A (en) * | 2018-10-23 | 2019-01-15 | 荆门优尔迪资源循环利用有限公司 | A kind of method of waste tire resource reutilization |
| CN109628119A (en) * | 2018-11-05 | 2019-04-16 | 武汉科技大学 | A kind of scrap tire cracking furnace |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
| US12304888B2 (en) | 2021-03-10 | 2025-05-20 | Ecolab Usa Inc. | Stabilizer additives for plastic-derived synthetic feedstock |
| US12031097B2 (en) | 2021-10-14 | 2024-07-09 | Ecolab Usa Inc. | Antifouling agents for plastic-derived synthetic feedstocks |
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