CN109456787A - A kind of waste tire processing unit and processing method - Google Patents
A kind of waste tire processing unit and processing method Download PDFInfo
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- CN109456787A CN109456787A CN201810896495.9A CN201810896495A CN109456787A CN 109456787 A CN109456787 A CN 109456787A CN 201810896495 A CN201810896495 A CN 201810896495A CN 109456787 A CN109456787 A CN 109456787A
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- oil
- gas
- waste tire
- carbon black
- reaction unit
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Classifications
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- 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
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/44—Carbon
- C09C1/48—Carbon black
- C09C1/482—Preparation from used rubber products, e.g. tyres
-
- 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
- C10G1/008—Controlling or regulating of liquefaction 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The invention discloses a kind of waste tire processing unit and processing methods.The device includes three tire crushing device, reaction unit, carbon black grinding device parts, wherein reaction unit part uses the tubular reactor with auger, realize device long period continuous operation, device consumption and production cost are reduced, while avoiding secondary pollution caused by the frequent shutting down in tire treatment process.The material inlet and products export of reaction unit use the safety seal structure for preventing air from entering, and effectively avoid air and enter reaction unit, realize internal negative pressure operation, eliminate security risk.Oil gas chilling technique, the hidden danger of cancellation element frequent shutdowns due to internal coking are used before oil-gas condenser.Effectively waste tire can be recycled using the method for device processing waste tire.
Description
Technical field
The present invention relates to the process field of waste tire more particularly to a kind of waste tire is handled by thermal cracking mode
Device and processing method.
Background technique
With the high speed development of auto industry, the every annual meeting in China generates a large amount of waste tire.Waste tire has very strong
Heat resistance, anti-degradability, be difficult to handle by natural degradation.If using the original processing method such as conventional incineration, landfill,
Greatly pollution will be generated to environment.How to realize that waste tire recycles, oneself becomes the research hotspot of World Focusing.At present
In the various methods of processing waste tire, the resources such as the available carbon black of mode, cracked oil, steel wire that thermal cracking is handled are real
The recycling of existing waste tire, is accordingly regarded as ideal processing mode.The cracking technique of tire mostly uses interval to grasp at present
Work or successive batches of cracking techniques, but the technology need to carry out heating cooling operation to furnace body repeatedly, cause the same of energy waste
When also improve production cost.The tank reactor relatively mostly used simultaneously is inevitably opened in device operational process
Kettle or operation of uncapping, the pernicious gas that will lead to generation in this way is excessive, causes secondary pollution.On the other hand processed in tire
High-temperature oil gas obtained in journey will appear coking during condensation, cause device can not long period smoothly run, with
Bring some potential safety problems.
Summary of the invention
The present invention is intended to provide the processing unit and processing method of a kind of waste tire, can long-term continuous and steady operation, it is raw
It produces at low cost, secondary pollution will not be generated in production process.
To achieve the goals above, the present invention provides a kind of processing units of waste tire.
The device includes the tire crushing device, reaction unit, carbon black grinding device being sequentially connected, and special character exists
In the structure of the reaction unit includes outer housing, the air-heating furnace being connected with outer housing, and feed(raw material)inlet is arranged on outer housing
Sealing device and carbon black outlet sealing device, the band of the interior connection feed(raw material)inlet sealing device and carbon black outlet sealing device of outer housing
There is the tubular reactor of auger, the oil gas extraction mouth on tubular reactor be set, produces the roots blower that mouth is connected with oil gas,
The oil gas quencher being connected is exported with roots blower, the cold cracking solution oil-in on oil gas quencher is set, is gone out with oil gas quencher
The connected oil-gas condenser of mouth is located at the fixed gas outlet on oil-gas condenser top, and being located at oil-gas condenser lower part has cracked oil
Outlet.
Further, the tubular reactor with auger is one or more groups of series connection, the length of every group of tubular reactor
Degree is 4-8m, diameter 0.4-1.2m.
Further, the feed(raw material)inlet sealing device is internal descending tapered pipeline, and variable diameter ratio is 1.05:
1-2:1。
Further, the carbon black outlet sealing device is rotary seal valve.
Further, gap is transversely provided with 1-8 baffling between tubular reactor in the reaction unit outer housing
Plate forms the S-shaped flow channel of hot-air in outer enclosure interior.
Further, thermocouple is equipped with baffle plate relative position in the reaction unit outer housing.
To achieve the goals above, the present invention provides the processing of the waste tire using above-mentioned waste tire processing unit
The step of method, this method includes:
(1) waste tire is delivered to the tire crushing device, length and width is obtained after crushing and is no more than 12mm's
Blob of viscose, while removing the steel wire in tire；
(2) air enters reaction unit from the hot air inlet of reaction unit lower part after the heating of air-heating furnace,
Hot-air is S-shaped to flow up after baffle plate baffling, is finally discharged from the hot air outlet on reaction unit top, in device
The heating fuel of start-up air-heating furnace is the device in Gas introduced outside device, and it is oil that fuel is heated after device runs smoothly
The fixed gas that gas condenser obtains；
(3) obtained blob of viscose is delivered to the reaction unit, blob of viscose seals under the drive of auger through feed(raw material)inlet
Device enters in tubular reactor, and under the heating of air-heating furnace, blob of viscose is reacted in inside reactor, is filled according to reaction
Interior temperature adjustment auger revolving speed is set, finally obtained solid product is carbon black, and carbon black is exported under the drive of auger by carbon black close
Seal apparatus enters carbon black grinding device, and obtained gaseous products are produced by roots blower from oil and gas gathering mouth, send to oil gas chilling
Device carries out chilling, and hot oil gas is mixed with cold cracked oil in oil gas quencher carries out chilling, in device start-up oil gas chilling
Cold cracked oil in device introduces outside device, and cold cracked oil is the cracked oil that oil-gas condenser obtains after device runs smoothly,
Material after over-quenching enters oil-gas condenser and is condensed, and the gaseous products obtained after condensation are fixed gas, through returning
The heating fuel of air-heating furnace is used for after receipts, obtained liquid-phase product to be cracked oil, and a part is sent to oil gas quencher and used
In high-temperature oil gas chilling, remainder is product cracked oil；
(4) the solid product carbon black that reaction unit obtains is delivered in the carbon black grinding device, by crushing, packing
Process obtains finished product carbon black.
Further, the treating capacity of step (3) described reactor is 1-10t/h, and auger revolving speed is 0.5-3rpm, reaction temperature
Degree is 300-440 DEG C, reaction pressure 0.10-0.08MPa.
Further, the mix and convert mass ratio of the hot oil gas in step (3) the oil gas quencher and cold cracked oil is 5:1-
1:1, temperature of charge is 200-300 DEG C after chilling.
Further, the condensation temperature of step (3) described oil-gas condenser is 40-60 DEG C.
It applies the technical scheme of the present invention, the sealing dress of tubular reactor and feed(raw material)inlet and carbon black outlet with auger
It sets, realizes the continuous operation of reactive moieties, avoid intermittently operated and batch continuous operation heats up and drops to furnace body repeatedly
Energy waste problem brought by temperature, saved the energy reduces production cost again.It avoids occurring uncapping in operation, open simultaneously
Kettle operation, reduces leaking for pernicious gas, prevents secondary pollution.The feed(raw material)inlet of another aspect reactor and carbon black outlet are set
The sealing structure set can lead to the accidents such as the reactor occurred in reaction process explosion to avoid because air enters, it is ensured that dress
Set the operation of safety and steady.Reaction temperature is controlled at 350-440 DEG C, can achieve the purpose converted completely, realizes waste tire
Recycling and utilization to the greatest extent.
In order to solve the coking problem that high-temperature oil gas occurs in condensation process, the present invention is used in high-temperature oil gas chilling skill
Art adds the mode of cold cracked oil into high-temperature oil gas to solve this problem.After cold cracked oil is added, height is quickly reduced
The temperature of warm oil gas, while the residence time for also reducing easily coking substance in condensation raw material reduces coking possibility.It is cold simultaneously
Cracked oil can also have certain solute effect to coking substance.The technical solution successfully solves high-temperature oil gas in condensation process
In coking problem, it is ensured that equipment safety, steady, macrocyclic operation.
The heating device of reactor in the present invention is air-heating furnace, and heat medium is hot-air.Hot-air is entering
After the outer housing of reaction unit, tubular reactor is heated.Lower part high-temperature hot air forms reaction zone, top Cryogenic air
Forming raw material preheating area realizes the Multi-class propagation of thermal energy.Outer housing is internally provided with thermocouple, can be according to the variation of temperature
Adjust auger revolving speed, the carbon black products gone bail for be up to state standards require while, realize the maximum yield of cracked oil.
For this heating method compared with other traditional heating modes, structure is simple, and low energy consumption, while flexible operation, securely and reliably.
Detailed description of the invention
The accompanying drawings constituting a part of this application is used to provide further understanding of the present invention, composition pair
Improper restriction of the invention.
Fig. 1 is process flow chart of the invention；
Fig. 2 is reaction unit structural schematic diagram in the present invention；
Fig. 3 is reaction unit baffle plate and thermocouple distribution schematic diagram in the present invention.
In figure: 1, feed(raw material)inlet sealing device, 2, oil gas extraction mouth, 3, carbon black outlet sealing device, 4, hot air outlet,
5, outer housing, 6, the tubular reactor with auger, 7, insulating layer, 8, baffle plate, 9, furnace fuel, 10, air intake,
11, air-heating furnace, 12, hot air inlet.
Specific embodiment
In order to deepen the understanding of the present invention, below in conjunction with embodiment and attached drawing, the invention will be further described.
Fig. 1 shows process flow chart of the invention, as shown in Figure 1, waste tire is delivered to the broken dress of tire first
It sets, obtains the blob of viscose that length and width is no more than 12mm after crushing, while removing the steel wire in tire.Obtained blob of viscose is conveyed
Reaction unit, blob of viscose enters in tubular reactor under the drive of auger through feed(raw material)inlet sealing device, in air-heating furnace
Under heating, blob of viscose is reacted in inside reactor, adjusts auger revolving speed, finally obtained solid-state according to temperature in reaction unit
Product is coarse carbon black, and coarse carbon black enters carbon black grinding device by carbon black outlet sealing device under the drive of auger, obtained heat
Oil gas is produced by roots blower from oil and gas gathering mouth, is sent to oil gas quencher and is mixed progress chilling with cold cracked oil, through over-quenching
Material afterwards enters oil-gas condenser and is condensed, and the gaseous products obtained after condensation are fixed gas, is used for after recovered
The heating fuel of air-heating furnace, obtained liquid-phase product are finished product cracked oil, and a part is sent to oil gas quencher for height
Warm oil gas chilling, remainder are sent to cracking oil tank.The solid product coarse carbon black that reaction unit obtains is delivered to the charcoal
In black grinding device, thin carbon black is obtained by crushing, thin carbon black obtains finished product carbon black by packaging process, send to product zone.
Following embodiment is all made of process flow shown in FIG. 1.
Embodiment 1
It include: feed(raw material)inlet sealing device 1 in figure Fig. 2 shows the structural schematic diagram of reaction unit in embodiment 1；Oil
Gas produces mouth 2；Carbon black outlet sealing device 3；Hot air outlet 4；Outer housing 5；Tubular reactor 6 with auger；Insulating layer
7；Baffle plate 8；Furnace fuel 9；Air intake 10；Air-heating furnace 11；Hot-air 12；Oil gas quencher 13；Oil gas condensation
Device 14.
The structure of the reaction unit as shown in Figure 2 includes outer housing 5, the air-heating furnace 11 being connected with outer housing 5, shell
Feed(raw material)inlet sealing device 1 and carbon black outlet sealing device 3, connection feed(raw material)inlet sealing device and charcoal in outer housing are set on body
The oil gas extraction mouth 2 on tubular reactor 6 is arranged in, with oil gas in the tubular reactor 6 with auger of black outlet sealing device
The connected roots blower of mouth 2 is produced, the oil gas quencher 13 being connected is exported with roots blower, is arranged on oil gas quencher 13
Cold cracking solution oil-in exports the oil-gas condenser 14 being connected with oil gas quencher, is located at the fixed gas on 14 top of oil-gas condenser
Outlet, being located at oil-gas condenser lower part has cracking oil export.
The tubular reactor with auger is 6 groups of series connection in the present embodiment, and the length of every group of tubular reactor is 6m, directly
Diameter is 0.8m.Feed(raw material)inlet sealing device is internal descending tapered pipeline, and variable diameter ratio is 1.5:1.Carbon black outlet is close
Encapsulation is set to rotary seal valve.Gap is equipped with 5 baffle plates, outer housing between tubular reactor in reaction unit outer housing
Outside is equipped with insulating layer.
The treating capacity of reactor is 2.5t/h in the present embodiment, and auger revolving speed is 2rpm, and reaction temperature is 400 DEG C, reaction
Pressure is that the mixed proportion of the hot oil gas and cold cracked oil in 99.7kPa quencher is 2:1, and temperature is 280 DEG C after chilling.Oil gas
The final condensation temperature of condenser is 50 DEG C.
Waste tire after treatment cracked oil the rate of recovery be 45.26%, sootlecovery rate be 35.17%, fixed gas
The rate of recovery is 12.03%, and long-term operation may be implemented in device, and the cycle of operation reaches 1 year or more.
Embodiment 2
Tubular reactor in the present embodiment with auger is 4 groups of series connection, and the length of every group of tubular reactor is 6m, diameter
For 0.8m.Feed(raw material)inlet sealing device is internal descending tapered pipeline, and variable diameter ratio is 1.05:1.Carbon black exit seal
Device is rotary seal valve.Gap is equipped with 3 baffle plates tubular reactor between in reaction unit outer housing, outside outer housing
Portion is equipped with insulating layer.
The treating capacity of reactor is 1.5t/h in the present embodiment, and auger revolving speed is 3rpm, and reaction temperature is 420 DEG C, reaction
Pressure is 99.6kPa.The mixed proportion of hot oil gas in oil gas quencher and cold cracked oil is 1:1, oil-gas condenser it is final
Condensation temperature is 40 DEG C.
Waste tire after treatment cracked oil the rate of recovery be 44.65%, sootlecovery rate be 34.83%, fixed gas
The rate of recovery is 12.93%, and long-term operation may be implemented in device, and the cycle of operation reaches 1 year or more.
Embodiment 3
The tubular reactor with auger is 6 groups of series connection in the present embodiment, and the length of every group of tubular reactor is 4m, directly
Diameter is 1m.Feed(raw material)inlet sealing device is internal descending tapered pipeline, and variable diameter ratio is 2:1.Carbon black exit seal dress
It is set to rotary seal valve.Gap is equipped with 5 baffle plates tubular reactor between in reaction unit outer housing, outside outer housing
Equipped with insulating layer.
The treating capacity of reactor is 4.5t/h in the present embodiment, and auger revolving speed is 2rpm, and reaction temperature is 370 DEG C, reaction
Pressure is 99.7kPa.The mixed proportion of hot oil gas in oil gas quencher and cold cracked oil is 2:1, oil-gas condenser it is final
Condensation temperature is 60 DEG C.
Waste tire after treatment cracked oil the rate of recovery be 43.65%, sootlecovery rate be 35.79%, fixed gas
The rate of recovery is 11.76%, and long-term operation may be implemented in device, and the cycle of operation reaches 1 year or more.
Embodiment 4
The tubular reactor with auger is 6 groups of series connection in the present embodiment, and the length of every group of tubular reactor is 6m, directly
Diameter is 0.8m.Feed(raw material)inlet sealing device is internal descending tapered pipeline, and variable diameter ratio is 1.5:1.Carbon black outlet is close
Encapsulation is set to rotary seal valve.Gap is equipped with 5 baffle plates, outer housing between tubular reactor in reaction unit outer housing
Outside is equipped with insulating layer.
The treating capacity of reactor is 3.0t/h in the present embodiment, and auger revolving speed is 1rpm, and reaction temperature is 400 DEG C, reaction
Pressure is 300Pa.The mixed proportion of hot oil gas in oil gas quencher and cold cracked oil is 4:1, oil-gas condenser it is final cold
Solidifying temperature is 40 DEG C.
Waste tire after treatment cracked oil the rate of recovery be 44.72%, sootlecovery rate be 35.03%, fixed gas
The rate of recovery is 12.22%, and long-term operation may be implemented in device, and the cycle of operation reaches 1 year or more.
Above embodiments are merely a preferred embodiment of the present invention, and are not intended to restrict the invention, for this field
For technical staff, the invention may be variously modified and varied.All within the spirits and principles of the present invention, made any
Modification, equivalent replacement, improvement etc., should all be included in the protection scope of the present invention.
Claims (10)
1. a kind of processing unit of waste tire, tire crushing device, reaction unit, carbon black including being sequentially connected crush dress
It sets, which is characterized in that the structure of the reaction unit includes outer housing, the air-heating furnace being connected with outer housing, on outer housing
Feed(raw material)inlet sealing device and carbon black outlet sealing device are set, connection feed(raw material)inlet sealing device and carbon black outlet in outer housing
The tubular reactor with auger of sealing device is arranged in the oil gas extraction mouth on tubular reactor, produces mouth phase with oil gas
Roots blower even exports the oil gas quenching apparatus being connected with roots blower, and the cold cracked oil being arranged on oil gas quenching apparatus enters
Mouthful, the oil-gas condenser being connected is exported with oil gas quenching apparatus, the fixed gas outlet on oil-gas condenser top is located at, is located at oil gas
The cracking oil export of condenser.
2. the processing unit of waste tire according to claim 1, which is characterized in that the tubular reactor with auger
For one or more groups of series connection, the length of every group of tubular reactor is 4-8m, diameter 0.4-1.2m.
3. the processing unit of waste tire according to claim 1, which is characterized in that the feed(raw material)inlet sealing device is interior
The descending tapered pipeline in portion, variable diameter ratio are 1.05:1-2:1.
4. the processing unit of waste tire according to claim 1, which is characterized in that the carbon black outlet sealing device is rotation
Turn sealing valve.
5. the processing unit of waste tire according to claim 1, which is characterized in that in the reaction unit outer housing and manage
Gap is transversely provided with 1-8 baffle plate between formula reactor, forms the S-shaped flow channel of hot-air in outer enclosure interior.
6. the processing unit of waste tire according to claim 5, which is characterized in that in the reaction unit outer housing and roll over
Flowing plate relative position is equipped with thermocouple.
7. a kind of processing method of the waste tire of the processing unit using waste tire as described in claim 1, feature exist
In step includes:
(1) waste tire is delivered to the tire crushing device, obtains the glue that length and width is no more than 12mm after crushing
Block, while removing the steel wire in tire；
(2) air enters reaction unit from the hot air inlet of reaction unit lower part, heat is empty after the heating of air-heating furnace
Gas is S-shaped to flow up after baffle plate baffling, is finally discharged from the hot air outlet on reaction unit top, drives in device
The heating fuel of stage air heating furnace is the device in Gas introduced outside device, and it is that oil gas is cold that fuel is heated after device runs smoothly
The fixed gas that condenser obtains；
(3) obtained blob of viscose is delivered to the reaction unit, blob of viscose is under the drive of auger through feed(raw material)inlet sealing device
Into in tubular reactor, under the heating of air-heating furnace, blob of viscose is reacted in inside reactor, according in reaction unit
Temperature adjusts auger revolving speed, and finally obtained solid product is carbon black, and carbon black is filled under the drive of auger by carbon black exit seal
Set enter carbon black grinding device, obtained gaseous products by roots blower from oil and gas gathering mouth produce, send to oil gas quencher into
Row chilling, hot oil gas is mixed with cold cracked oil in oil gas quencher carries out chilling, in device start-up oil gas quencher
Cold cracked oil introduced outside device, cold cracked oil is the obtained cracked oil of oil-gas condenser after device runs smoothly, and is passed through
Material after chilling enters oil-gas condenser and is condensed, and the gaseous products obtained after condensation are fixed gas, after recovered
For the heating fuel of air-heating furnace, obtained liquid-phase product is cracked oil, and a part is sent to oil gas quencher for height
Warm oil gas chilling, remainder are product cracked oil；
(4) the solid product carbon black that reaction unit obtains is delivered in the carbon black grinding device, by crushing, packaging process
Obtain finished product carbon black.
8. the processing method of waste tire according to claim 6, which is characterized in that the place of step (3) described reactor
Reason amount is 1-10t/h, and auger revolving speed is 0.5-3rpm, and reaction temperature is 300-440 DEG C, reaction pressure 0.10-0.08MPa.
9. the processing method of waste tire according to claim 6, which is characterized in that step (3) the oil gas quencher
In hot oil gas and the mix and convert mass ratio of cold cracked oil be 5:1-1:1, temperature of charge is 200-300 DEG C after chilling.
10. the processing method of waste tire according to claim 6, which is characterized in that step (3) described oil-gas condenser
Condensation temperature be 40-60 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810896495.9A CN109456787B (en) | 2018-08-08 | 2018-08-08 | Waste tire treatment device and treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810896495.9A CN109456787B (en) | 2018-08-08 | 2018-08-08 | Waste tire treatment device and treatment method |
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| Publication Number | Publication Date |
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| CN109456787A true CN109456787A (en) | 2019-03-12 |
| CN109456787B CN109456787B (en) | 2021-02-09 |
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ID=65606344
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| Application Number | Title | Priority Date | Filing Date |
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| CN201810896495.9A Active CN109456787B (en) | 2018-08-08 | 2018-08-08 | Waste tire treatment device and treatment method |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1338341A (en) * | 2001-04-06 | 2002-03-06 | 陈黄传 | Method and equipment for reclaiming organic waste without pollution |
| CN101481619A (en) * | 2008-01-11 | 2009-07-15 | 山东科技大学 | Self-mixing downflow fluidized bed rapid pyrolysis process for solid organics |
| CN101555413A (en) * | 2008-04-10 | 2009-10-14 | 环拓科技股份有限公司 | Continuous type steam cracking equipment and cracking furnace used for same |
| CN104059684A (en) * | 2014-06-09 | 2014-09-24 | 青岛东方循环能源有限公司 | Waste tire cracking furnace |
| CN205473594U (en) * | 2016-03-31 | 2016-08-17 | 华云新能源科技（深圳）有限公司 | Pyrolysis treatment device of feeder and rubber waste and/or waste plastics |
-
2018
- 2018-08-08 CN CN201810896495.9A patent/CN109456787B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1338341A (en) * | 2001-04-06 | 2002-03-06 | 陈黄传 | Method and equipment for reclaiming organic waste without pollution |
| CN101481619A (en) * | 2008-01-11 | 2009-07-15 | 山东科技大学 | Self-mixing downflow fluidized bed rapid pyrolysis process for solid organics |
| CN101555413A (en) * | 2008-04-10 | 2009-10-14 | 环拓科技股份有限公司 | Continuous type steam cracking equipment and cracking furnace used for same |
| CN104059684A (en) * | 2014-06-09 | 2014-09-24 | 青岛东方循环能源有限公司 | Waste tire cracking furnace |
| CN205473594U (en) * | 2016-03-31 | 2016-08-17 | 华云新能源科技（深圳）有限公司 | Pyrolysis treatment device of feeder and rubber waste and/or waste plastics |
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| Publication number | Publication date |
|---|---|
| CN109456787B (en) | 2021-02-09 |
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