CN205774331U - A kind of cracking scrap rubber device - Google Patents
A kind of cracking scrap rubber device Download PDFInfo
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- CN205774331U CN205774331U CN201620478750.4U CN201620478750U CN205774331U CN 205774331 U CN205774331 U CN 205774331U CN 201620478750 U CN201620478750 U CN 201620478750U CN 205774331 U CN205774331 U CN 205774331U
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- temperature
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- scrap rubber
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- 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
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Abstract
This utility model relates to environmental technology field, specifically discloses a kind of cracking scrap rubber device, and the cracking scrap rubber device that this utility model provides includes: storage bin；The screw feeding pipe being connected with described storage bin；The reaction generator being connected with described screw feeding pipe, wherein, described reaction generator is cascade reaction generator, and described cascade reaction generator has different warm areas；The black collector being connected with described reaction generator and oil gas collection tank；The condenser being connected with described oil gas collection tank；The gs-oil separator being connected with described condenser；The accumulator tank being connected with described oil gas collection tank, described condenser and described gs-oil separator respectively；The absolute oil collection device being connected with described accumulator tank and wastewater treatment equipment.The cracking scrap rubber device that this utility model provides uses the third-order reaction device that temperature gradually rises so that scrap rubber reaction is fully, it is to avoid the problem that moment is caused coking by high temperature.
Description
[technical field]
This utility model relates to environmental technology field, particularly relates to a kind of cracking scrap rubber device.
[background technology]
Manufacturing development makes the yield of scrap rubber also be on the increase, and can cause environment the biggest
Pollution.Along with the gradually enhancing of people's environmental consciousness, people increasingly pay attention to the recovery profit of scrap rubber
With, the recycling of scrap rubber commercially has the biggest prospect, can be by useless rubber by cracking technique
Glue become the white carbon black with economic benefits again with.
During realizing this utility model, utility model people finds that prior art at least exists
Problems with: the cracking technology of existing scrap rubber uses high-temperature heating mode, and scrap rubber moment is by high temperature
Coking can be caused, be unfavorable for the abundant cracking of scrap rubber, crack and insufficient cause resource utilization the highest,
Easily cause the waste of raw material.Therefore, existing scrap rubber cracking technology still needs to improve further.
[utility model content]
The technical problems to be solved in the utility model is that existing Prediction for Solid Waste Treatment Technology is immature, money
The efficiency of source trans-utilization is low.
For solving above-mentioned technical problem, this utility model offer techniques below scheme:
This utility model provides one cracking scrap rubber device, including:
Storage bin；
The screw feeding pipe being connected with described storage bin；
The reaction generator being connected with described screw feeding pipe, wherein, described reaction generator is cascade
Reaction generator, described cascade reaction generator has different warm areas；
The black collector being connected with described reaction generator and oil gas collection tank；
The condenser being connected with described oil gas collection tank；
The gs-oil separator being connected with described condenser；
The accumulator tank being connected with described oil gas collection tank, described condenser and described gs-oil separator respectively；
The absolute oil collection device being connected with described accumulator tank and wastewater treatment equipment.
In certain embodiments, described device also includes being arranged at described storage bin and described screw feeding
Nitrogen purging device between pipe.
First order reaction generator that in certain embodiments, described reaction generator includes being sequentially connected with,
Second level reaction generator and third level reaction generator；Described first order reaction generator includes successively
Connecting the first temperature province and the second temperature province, described second level reaction generator includes being sequentially connected with
3rd temperature province and the 4th temperature province, described third level reaction generator includes being sequentially connected with the 5th
Temperature province and the 6th temperature province.
In certain embodiments, described first temperature province temperature is set as 100～150 DEG C, described second
Temperature province temperature is set as 200～250 DEG C, and described 3rd temperature province temperature is set as 300～350 DEG C,
Described 4th temperature province temperature is set as 400～450 DEG C, and described 5th temperature province temperature is set as
500～550 DEG C, described 6th temperature province temperature is set as 600～650 DEG C.
In certain embodiments, described oil gas collection tank top is provided with oil spray equipment, described oil gas
Arranging Fuel Tanking Unit bottom collecting tank, described Fuel Tanking Unit is outside is wound around electromagnetic heating coil.
Having the beneficial effects that of this utility model specific embodiment: the cracking that this utility model provides is given up rubber
Adhesive dispenser uses the third-order reaction device that temperature gradually rises so that scrap rubber reaction is fully, it is to avoid wink
Between caused the problem of coking by high temperature, simultaneously, moreover it is possible to the high-temperature oil gas produced in course of reaction carried out
Recycling after separation, improves the conversion ratio of resource, meets environmental requirement.
[accompanying drawing explanation]
A kind of structural representation cracking scrap rubber device that Fig. 1 provides for this utility model embodiment 1.
[detailed description of the invention]
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with
Drawings and Examples, are further elaborated to this utility model.Should be appreciated that this place is retouched
The specific embodiment stated, only in order to explain this utility model, is not used to limit this utility model.
Embodiment 1
As it is shown in figure 1, this utility model provides one cracking scrap rubber device, including:
Storage bin 1, the described storage bin 1 scrap rubber after storing break process, it is desirable to break process
After scrap rubber size reach below 40mm, damaged tire blob of viscose after break process etc. can be as
Scrap rubber is stored in storage bin 1.
The screw feeding pipe 2 being connected with described storage bin 1, described screw feeding pipe 2 is varying pitch structure,
Scrap rubber can be entered reducing extruding, the gas that volume compression is carried secretly in discharging scrap rubber simultaneously therein
, in follow-up entrance reactor, preferably there is cracking reaction in body, it is ensured that the purity of scrap rubber.
The reaction generator 3 being connected with described screw feeding pipe 2, described reaction generator 3 is anti-for cascade
Generator, described cascade reaction generator is answered to have different warm areas；Described reaction generator 3 includes
The first order reaction generator 31, second level reaction generator 32 and the third level reaction that are sequentially connected with occur
Device 33；Described first order reaction generator 31 includes being sequentially connected with the first temperature province 311 and the second temperature
Degree region 312, described second level reaction generator 32 includes being sequentially connected with the 3rd temperature province 321 He
4th temperature province 322, described third level reaction generator 33 includes being sequentially connected with the 5th temperature province
331 and the 6th temperature province 332, described first territory, humidity province 311 temperature is set as 100～150 DEG C,
Described second temperature province 312 temperature is set as 200～250 DEG C, described 3rd temperature province 321 temperature
Being set as 300～350 DEG C, described 4th temperature province 322 temperature is set as 400～450 DEG C, described
Five temperature province 331 temperature are set as 500～550 DEG C, and described 6th temperature province 332 temperature is set as
600～650 DEG C；Pressure within described reaction generator 3 is tiny structure, scope-100Pa～0Pa it
Between, its pressure control by being arranged at the gas air-blower control of described reaction generator 3 rear end, useless rubber
Glue is easily caused coking suddenly encountering high temperature, the therefore reaction generator 3 of this utility model embodiment
Use the form of three-stage cascade, different warm areas is set inside every one-level, it is possible to ensure that scrap rubber is splitting
Gradually heat up during solution so that scrap rubber reaction is more uniformly fully；This reaction simultaneously occurs
Device 3 external diameter is not more than 530mm, and wall thickness is not more than 20mm, and reaction generator overall length is not more than
6000mm, has volume little, lightweight, the advantage of low cost.
The black collector 4 being connected with described reaction generator 3 and oil gas collection tank 5, scrap rubber is instead
After reacting in answering generator 3, will produce white carbon black and high-temperature oil gas, white carbon black is through reaction generator 3
Terminal carries out recycling in will be fed into black collector 4, the high-temperature oil gas produced in course of reaction
Process further in the discharge of the gas outlet of reaction generator 3 will be fed into oil gas collection tank 5, oil gas
Collecting tank 5 top is provided with oil spray equipment 51, arranges Fuel Tanking Unit bottom described oil gas collection tank 5
52, described Fuel Tanking Unit 52 is outside is wound around electromagnetic heating coil, and high-temperature oil gas enters oil gas collection tank 5
After, the oily spray equipment 51 on oil gas collection tank 5 top can be to the high-temperature oil gas in oil gas collection tank 5
Wash, effectively reduce the ash in oil gas and carbon black pellet impurity, make subsequent condensation get off
Oil product is purified, quality uprises, and the mist of oil that oil spray equipment 51 sprays into is carried secretly in oil gas collecting tank 5
High-temperature oil gas in dust and particulate matter drop in the Fuel Tanking Unit 52 of bottom air collector 5, storage
Oil device 52 is outside is wound around electromagnetic heating coil, is added by the oil gas within heating Fuel Tanking Unit 52
Sending into condenser 6 after heat, described oil gas collection tank 5 Fuel Tanking Unit 52 top is provided with oil product overfall,
Overfall accesses a Residual Oil Tank, and Residual Oil Tank can not evaporate into the residual oil of condenser 6 after collecting heating
Impurity.
The condenser 6 being connected with described oil gas collection tank 5, the oil gas after heating is entered by described condenser 6
Row condensation process, obtains gaseous steam and oil water mixture after condensation, gaseous steam sends into Oil-gas Separation
Device 7, accumulator tank 8 sent into by oil water mixture.
The gs-oil separator 7 being connected with described condenser 6, described gs-oil separator 7 will obtain after condensation
Gaseous steam carry out Oil-gas Separation and obtain liquid oil and combustible gas, liquid oil will be fed into accumulator tank 8, can
Combustion gas is delivered to gas-purification electricity generation system by blower fan.
The collection being connected with described oil gas collection tank 5, described condenser 6 and described gs-oil separator 7 respectively
Oil tank 8, the oil water mixture and described produced from the condensation of described condenser 6 collected by described accumulator tank 8
The liquid oil that gs-oil separator 7 produces, the oil water mixture collected is carried out oil by described accumulator tank 8
Water separates and obtains liquid oil and waste water, and clean liquid oil will be fed into absolute oil collection device 9 and collects storage,
Waste water will be fed into wastewater treatment equipment 10 and processes rear discharge up to standard, what deserves to be explained is, described accumulator tank
Oil in 8 is delivered to described oil gas collection tank 5 for oil spray equipment 51 to oil gas collection by oil pump
High-temperature oil gas in tank 5 is washed.
Preferably, described device also include being arranged at described storage bin 1 and described screw feeding pipe 2 it
Between nitrogen purging device 11, will broken in storage bin 1 after scrap rubber pour screw feeding pipe 2 into
During, use nitrogen purging device 11 by being full of nitrogen in screw feeding pipe 2 while pouring into, prevent
Only when scrap rubber adds screw feeding pipe 2, air enters, it is ensured that the nothing of compression in screw feeding pipe 2
Oxygen environment, provides double shield to follow-up cracking reaction.
Below in conjunction with specific embodiment, a kind of cracking scrap rubber device provided by the utility model is split
The technological process solving scrap rubber is further detailed: the scrap rubber after first crushing is stored in storage
In feed bin 1, when needing to crack scrap rubber, pour the scrap rubber in storage bin 1 into screw feeding pipe 2,
Employing nitrogen purging device 11 is by being full of nitrogen in screw feeding pipe 2 simultaneously, by screw feeding pipe 2
Scrap rubber after compression volume carries out the cracking reaction of cascade raising temperature and obtains charcoal in sending into reaction generator 3
Black, course of reaction will produce high-temperature oil gas, white carbon black recycles in sending into black collector 4, high
Temperature oil gas carries out washing in will be fed into oil gas collection tank 5, heat after obtain oil gas, oil gas is at condenser 6
Interior gaseous steam and the oil water mixture of obtaining after condensation process, gaseous steam feeding gs-oil separator
7, accumulator tank 8 sent into by oil water mixture, after gaseous steam carries out Oil-gas Separation in gs-oil separator 7
Obtaining liquid oil and combustible gas, combustible gas is delivered to gas-purification electricity generation system, liquid oil by blower fan
Sending into accumulator tank 8, oil water mixture obtains liquid oil and waste water after carrying out oil-water separation in accumulator tank 8,
Clean liquid oil sends into absolute oil collection device 9, waste water send into wastewater treatment equipment 10 process up to standard after
Discharge.
The cracking scrap rubber device that the present embodiment provides uses the third-order reaction device that temperature gradually rises,
Make scrap rubber reaction fully, it is to avoid moment is caused the problem of coking by high temperature, simultaneously, moreover it is possible to will be anti-
Recycling after the high-temperature oil gas of generation separates during Ying, improves the conversion ratio of resource,
Meet environmental requirement.
The foregoing is only preferred embodiment of the present utility model, not new in order to limit this practicality
Type, all any amendment, equivalent and improvement made within spirit of the present utility model and principle
Deng, within should be included in protection domain of the present utility model.
Claims (5)
1. a cracking scrap rubber device, it is characterised in that including:
Storage bin；
The screw feeding pipe being connected with described storage bin；
The reaction generator being connected with described screw feeding pipe, wherein, described reaction generator is cascade
Reaction generator, described cascade reaction generator has different warm areas；
The black collector being connected with described reaction generator and oil gas collection tank；
The condenser being connected with described oil gas collection tank；
The gs-oil separator being connected with described condenser；
The accumulator tank being connected with described oil gas collection tank, described condenser and described gs-oil separator respectively；
The absolute oil collection device being connected with described accumulator tank and wastewater treatment equipment.
2. cracking scrap rubber device as claimed in claim 1, it is characterised in that described device also wraps
Include the nitrogen purging device being arranged between described storage bin and described screw feeding pipe.
3. cracking scrap rubber device as claimed in claim 2, it is characterised in that described reaction occurs
Device includes that the first order reaction generator being sequentially connected with, second level reaction generator and third level reaction are sent out
Raw device；Described first order reaction generator includes being sequentially connected with the first temperature province and the second temperature province,
Described second level reaction generator includes being sequentially connected with the 3rd temperature province and the 4th temperature province, described
Third level reaction generator includes being sequentially connected with the 5th temperature province and the 6th temperature province.
4. cracking scrap rubber device as claimed in claim 3, it is characterised in that described first temperature
Regional temperature is set as 100～150 DEG C, and described second temperature province temperature is set as 200～250 DEG C, institute
Stating the 3rd temperature province temperature and be set as 300～350 DEG C, described 4th temperature province temperature is set as
400～450 DEG C, described 5th temperature province temperature is set as 500～550 DEG C, described 6th temperature province
Temperature is set as 600～650 DEG C.
5. cracking scrap rubber device as claimed in claim 1, it is characterised in that described oil gas collection
Tank top is provided with oil spray equipment, and described oil gas collection pot bottom arranges Fuel Tanking Unit, described oil storage
Device is outside is wound around electromagnetic heating coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620478750.4U CN205774331U (en) | 2016-05-24 | 2016-05-24 | A kind of cracking scrap rubber device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620478750.4U CN205774331U (en) | 2016-05-24 | 2016-05-24 | A kind of cracking scrap rubber device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205774331U true CN205774331U (en) | 2016-12-07 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620478750.4U Active CN205774331U (en) | 2016-05-24 | 2016-05-24 | A kind of cracking scrap rubber device |
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| CN (1) | CN205774331U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107418603A (en) * | 2016-05-24 | 2017-12-01 | 华云新能源科技（深圳）有限公司 | One kind cracking scrap rubber device and method |
| CN107586556A (en) * | 2017-09-30 | 2018-01-16 | 济南恒誉环保科技股份有限公司 | A kind of technique and system for preventing excessive fragmentation |
| CN107596831A (en) * | 2017-09-30 | 2018-01-19 | 济南恒誉环保科技股份有限公司 | A kind of anti-poly- purification technique and system for cracking oil gas |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
-
2016
- 2016-05-24 CN CN201620478750.4U patent/CN205774331U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107418603A (en) * | 2016-05-24 | 2017-12-01 | 华云新能源科技（深圳）有限公司 | One kind cracking scrap rubber device and method |
| CN107586556A (en) * | 2017-09-30 | 2018-01-16 | 济南恒誉环保科技股份有限公司 | A kind of technique and system for preventing excessive fragmentation |
| CN107596831A (en) * | 2017-09-30 | 2018-01-19 | 济南恒誉环保科技股份有限公司 | A kind of anti-poly- purification technique and system for cracking oil gas |
| CN107596831B (en) * | 2017-09-30 | 2023-05-30 | 济南恒誉环保科技股份有限公司 | Anti-aggregation purification process and system for pyrolysis oil gas |
| US11999920B2 (en) | 2020-09-14 | 2024-06-04 | Ecolab Usa Inc. | Cold flow additives for plastic-derived synthetic feedstock |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190301 Address after: 518022 Main Building, Xinxing Square, Shennan East Road, Guiyuan Street, Guiyuan Street, Luohu District, Shenzhen City, Guangdong Province, 5608 stories Patentee after: Shenzhen Huayun Intelligent Equipment Technology Co., Ltd. Address before: 518022 Diwang Business Center, Xinxing Square, No. 5002 Shennan East Road, Luohu District, Shenzhen City, Guangdong Province, 5308 Patentee before: China Energy Technology (Shenzhen) Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190822 Address after: 518000 Guangdong city of Shenzhen province Qianhai Shenzhen Hong Kong cooperation zone before Bay Road No. 1 building 201 room A (located in Shenzhen Qianhai business secretary Co. Ltd.) Patentee after: Shenzhen Weichuang Rio Tinto Industrial Development Co., Ltd. Address before: 518022 Main Building, Xinxing Plaza, Shennan East Road, Guiyuan Street, Guiyuan Street, Luohu District, Shenzhen City, Guangdong Province, 5608 stories Patentee before: Shenzhen Huayun Intelligent Equipment Technology Co., Ltd. |