CN204294204U - Pyrolysis reactor continuous feeding device - Google Patents
Pyrolysis reactor continuous feeding device Download PDFInfo
- Publication number
- CN204294204U CN204294204U CN201420683031.7U CN201420683031U CN204294204U CN 204294204 U CN204294204 U CN 204294204U CN 201420683031 U CN201420683031 U CN 201420683031U CN 204294204 U CN204294204 U CN 204294204U
- Authority
- CN
- China
- Prior art keywords
- raw materials
- hopper
- electric control
- feeding
- pneumatic electric
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 28
- 239000002994 raw material Substances 0.000 claims description 55
- 230000008676 import Effects 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 description 9
- 239000010920 waste tyre Substances 0.000 description 4
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000007792 addition Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
The utility model discloses a kind of pyrolysis reactor continuous feeding device, comprise the first feeding screw and the second feeding screw, described first feeding screw is provided with first material inlet and two the first material outlets, wherein, first material outlet is connected with the first hopper by the first feedstock transportation pipeline, another first material outlet is connected with the second hopper by the second feedstock transportation pipeline, described second feeding screw is provided with two the second material inlets and second material outlet, one of them second material inlet is connected with above-mentioned first hopper by the 3rd feedstock transportation pipeline, another second material inlet is connected with above-mentioned second hopper by the 4th feedstock transportation pipeline, described second material outlet is connected with pyrolysis reactor by material conveying tube road, Wuyuan.The utility model achieves the continuous uniform charging of pyrolysis feed, is conducive to the temperature control of pyrolysis system and the rational utilization of equipment, achieves the maximum production capacity of equipment.
Description
Technical Field
The utility model belongs to the technical field of junked tire pyrolysis, especially, relate to a pyrolysis reactor is feed arrangement in succession.
Background
The large amount of waste tires causes serious environmental pollution and resource waste, and the existing waste tires are treated and disposed by retreading, reclaimed rubber and rubber powder preparation, pyrolysis, incineration and the like. The pyrolysis method can recover resources to the maximum extent, has the characteristics of large treatment capacity of the waste tires, high benefit, small environmental pollution and the like, more accords with the principles of resource utilization, harmlessness and reduction of waste treatment, and is a main flow mode for waste tire treatment. In order to realize the stable control of the pyrolysis reaction temperature and pressure and realize the maximum reasonable utilization of equipment, a pyrolysis reaction system mostly adopts a continuous and uniform reaction mode, but most of the existing pyrolysis reaction feeding devices are complex in structure and cannot realize continuous feeding well.
It will thus be seen that the prior art is susceptible to further improvements and enhancements.
SUMMERY OF THE UTILITY MODEL
The utility model provides a continuous feeding device of a pyrolysis reactor, which avoids the defects of the prior art.
The utility model discloses the technical scheme who adopts does:
continuous feed arrangement of pyrolytic reactor, including first screw feeder and second screw feeder, first screw feeder is provided with a first raw materials import and two first raw materials export, and wherein, a first raw materials export links to each other with first hopper through first raw materials conveying pipeline, and another first raw materials export links to each other with the second hopper through second raw materials conveying pipeline, second screw feeder is provided with two second raw materials import and a second raw materials export, and one of them second raw materials import links to each other with above-mentioned first hopper through third raw materials conveying pipeline, and another second raw materials import links to each other with above-mentioned second hopper through fourth raw materials conveying pipeline, second raw materials export links to each other with pyrolytic reactor through fifth raw materials conveying pipeline.
The pneumatic electric control gate valve of feeding and the pneumatic electric control ball valve of feeding all have set gradually on first, the second feedstock delivery pipe, all set gradually ejection of compact pneumatic electric control gate valve and the pneumatic electric control ball valve of ejection of compact on third, the fourth feedstock delivery pipe, the pneumatic electric control gate valve of the feeding, ejection of compact and the pneumatic electric control ball valve of the feeding, ejection of compact all link to each other with circuit control system.
And the first hopper and the second hopper are both provided with a high limit material level meter and a low limit material level meter.
And stirring motors are arranged on the first hopper and the second hopper.
And a conveying motor is arranged on the second spiral feeder and is a variable frequency motor.
Since the technical scheme is used, the utility model discloses the beneficial effect who gains does:
the utility model discloses a continuous even feeding of pyrolysis raw materials is favorable to the rational utilization of the temperature control of pyrolysis system and equipment, has realized the maximum capacity of equipment.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Wherein,
1. a first screw feeder 101, a first raw material inlet 102, a first raw material outlet 2, a first raw material conveying pipeline 3, a second raw material conveying pipeline 4, a feeding pneumatic electric control gate valve 5, a feeding pneumatic electric control ball valve 6, a first hopper 7, a high limit level indicator 8, a low limit level indicator 9, a stirring motor 10, a second hopper 11, a third raw material conveying pipeline 12, a fourth raw material conveying pipeline 13, a second screw feeder 1301, a second raw material inlet 1302, a second raw material outlet 14, a fifth raw material conveying pipeline 15, a conveying motor 16, a discharging pneumatic electric control gate valve 17, a discharging pneumatic electric control ball valve 13
Detailed Description
The present invention will be described in further detail with reference to the following drawings and specific embodiments, but the present invention is not limited to these embodiments.
As shown in fig. 1, the pyrolysis reactor continuous feeding device comprises a first screw feeder 1 and a second screw feeder 13, wherein the first screw feeder 1 is provided with a first raw material inlet 101 and two first raw material outlets 102, one first raw material outlet 101 is connected with a first hopper 6 through a first raw material conveying pipeline 2, the other first raw material outlet 102 is connected with a second hopper 10 through a second raw material conveying pipeline 3, the first hopper 6 and the second hopper 10 are both provided with a high limit level gauge 7 and a low limit level gauge 8, the first hopper 6 and the second hopper 10 are both provided with a stirring motor 9 for facilitating the raw material to sink down, the second screw feeder 13 is provided with two second raw material inlets 1301 and a second raw material outlet 1302, one second raw material inlet 1301 is connected with the first hopper 6 through a third raw material conveying pipeline 11, another second raw materials import 1301 links to each other with above-mentioned second hopper 10 through fourth raw materials conveying line 12, is provided with conveying motor 15 on the second spiral feeder 13, and conveying motor 15 is inverter motor, second raw materials export 1302 passes through fifth raw materials conveying line 14 and links to each other with pyrolysis reactor, all set gradually feeding pneumatic electric control gate valve 4 and feeding pneumatic electric control ball valve 5 on first, the second raw materials conveying line, all set gradually ejection of compact pneumatic electric control gate valve 16 and ejection of compact pneumatic electric control ball valve 17 on third, the fourth raw materials conveying line, it all links to each other with circuit control system to advance, ejection of compact pneumatic electric control gate valve and advance, ejection of compact pneumatic electric control ball valve.
When the material level of the first and second material hoppers is at the low material limit level, the feeding pneumatic electric control gate valve 4 and the feeding pneumatic electric control ball valve 5 on the first and second material conveying pipelines are opened, the discharging pneumatic electric control gate valve 16 and the discharging pneumatic electric control ball valve 17 on the third and fourth material conveying pipelines are closed, the balance of the feeding and discharging speed is achieved by setting the feeding speed, namely, when the first material hopper 6 is at the low limit level, the second material hopper 10 is required to be at the high material limit level, at this time, the feeding pneumatic electric control gate valve 4 and the feeding pneumatic electric control ball valve 5 on the first material conveying pipeline 2 are opened, the discharging pneumatic electric control gate valve 16 and the discharging pneumatic electric control ball valve 17 on the third material conveying pipeline 11 are closed, the feeding pneumatic electric control gate valve 4 and the feeding pneumatic electric control ball valve 5 on the second material conveying pipeline 3 are closed, the discharging pneumatic electric control gate valve 16 and the discharging pneumatic electric control ball valve 17 on the fourth material conveying pipeline 12 are opened, control input speed, first hopper 6 just feeds into to high limit material level when making 10 ejection of compact of second hopper to low limit material level, and first, second hopper so circulation is used repeatedly, has realized even continuous feeding to guarantee that pyrolysis reactor can not fluctuate because of the inhomogeneous big pyrolysis temperature that appears of feeding, influence the pyrolysis process.
The parts not mentioned in the utility model can be realized by adopting or using the prior art for reference.
Furthermore, the terms "first," "second," "third," "fourth," and "fifth" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
The specific embodiments described herein are merely illustrative of the spirit of the invention. Various modifications, additions and substitutions for the specific embodiments described herein may be made by those skilled in the art without departing from the spirit of the invention or exceeding the scope of the invention as defined in the accompanying claims.
Claims (5)
1. Pyrolysis reactor continuous feed device, its characterized in that: including first screw feeder and second screw feeder, first screw feeder is provided with a first raw materials import and two first raw materials exports, and wherein, a first raw materials export links to each other with first hopper through first raw materials conveying pipeline, and another first raw materials export links to each other with the second hopper through second raw materials conveying pipeline, second screw feeder is provided with two second raw materials import and a second raw materials export, and one of them second raw materials import links to each other with above-mentioned first hopper through third raw materials conveying pipeline, and another second raw materials import links to each other with above-mentioned second hopper through fourth raw materials conveying pipeline, second raw materials export links to each other with pyrolytic reaction ware through fifth raw materials conveying pipeline.
2. The pyrolysis reactor continuous feed apparatus of claim 1, wherein: the pneumatic electric control gate valve of feeding and the pneumatic electric control ball valve of feeding all have set gradually on first, the second feedstock delivery pipe, all set gradually ejection of compact pneumatic electric control gate valve and the pneumatic electric control ball valve of ejection of compact on third, the fourth feedstock delivery pipe, the pneumatic electric control gate valve of the feeding, ejection of compact and the pneumatic electric control ball valve of the feeding, ejection of compact all link to each other with circuit control system.
3. The pyrolysis reactor continuous feed apparatus of claim 1, wherein: and the first hopper and the second hopper are both provided with a high limit material level meter and a low limit material level meter.
4. The pyrolysis reactor continuous feed apparatus of claim 1, wherein: and stirring motors are arranged on the first hopper and the second hopper.
5. The pyrolysis reactor continuous feed apparatus of claim 1, wherein: and a conveying motor is arranged on the second spiral feeder and is a variable frequency motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420683031.7U CN204294204U (en) | 2014-11-14 | 2014-11-14 | Pyrolysis reactor continuous feeding device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420683031.7U CN204294204U (en) | 2014-11-14 | 2014-11-14 | Pyrolysis reactor continuous feeding device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204294204U true CN204294204U (en) | 2015-04-29 |
Family
ID=53099788
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420683031.7U Expired - Fee Related CN204294204U (en) | 2014-11-14 | 2014-11-14 | Pyrolysis reactor continuous feeding device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204294204U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105505417A (en) * | 2016-01-30 | 2016-04-20 | 农业部规划设计研究院 | Continuous type pyrolysis carbonization full-sealing technological method |
| CN107149870A (en) * | 2017-06-30 | 2017-09-12 | 大唐环境产业集团股份有限公司 | One kind combination lime stone handling system |
| CN107287457A (en) * | 2017-07-17 | 2017-10-24 | 中国恩菲工程技术有限公司 | Rare earth ore concentrate continuous decomposition equipment |
| CN109609162A (en) * | 2019-01-02 | 2019-04-12 | 青岛伊克斯达智能装备有限公司 | Serialization bidirectional feed device and feed process for solid material thermal cracking |
| CN111018039A (en) * | 2020-01-17 | 2020-04-17 | 上海盛弘环境科技有限公司 | Harmless and recycling treatment method for high-concentration organic matter waste liquid |
-
2014
- 2014-11-14 CN CN201420683031.7U patent/CN204294204U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105505417A (en) * | 2016-01-30 | 2016-04-20 | 农业部规划设计研究院 | Continuous type pyrolysis carbonization full-sealing technological method |
| CN107149870A (en) * | 2017-06-30 | 2017-09-12 | 大唐环境产业集团股份有限公司 | One kind combination lime stone handling system |
| CN107287457A (en) * | 2017-07-17 | 2017-10-24 | 中国恩菲工程技术有限公司 | Rare earth ore concentrate continuous decomposition equipment |
| CN107287457B (en) * | 2017-07-17 | 2023-01-13 | 中国恩菲工程技术有限公司 | Continuous decomposition equipment for rare earth concentrate |
| CN109609162A (en) * | 2019-01-02 | 2019-04-12 | 青岛伊克斯达智能装备有限公司 | Serialization bidirectional feed device and feed process for solid material thermal cracking |
| CN111018039A (en) * | 2020-01-17 | 2020-04-17 | 上海盛弘环境科技有限公司 | Harmless and recycling treatment method for high-concentration organic matter waste liquid |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204294204U (en) | Pyrolysis reactor continuous feeding device | |
| CN203212028U (en) | Pneumatic quantitative feeding device | |
| CN202773689U (en) | Feed feeding machine | |
| CN205007647U (en) | Lotion thickener underflow circulation homogenization device | |
| CN109535477A (en) | A kind of scrap rubber low-temp recovery equipment | |
| CN104971524A (en) | Paste thickener bottom flow circulation homogenizing device | |
| CN203782077U (en) | Waste rubber plasticizing device | |
| CN203943002U (en) | The automatic recovery type biscuit roller printing machine | |
| CN208449173U (en) | A kind of full-automatic novel feeding station | |
| CN203639616U (en) | Chemical fiber feeding system | |
| CN202912417U (en) | Solid particle transport distributor | |
| CN204933951U (en) | A kind of automation charging device of wiring board printing-ink production line | |
| CN204675141U (en) | A kind of Double-port moulding mixture storehouse | |
| CN203540497U (en) | Quantitative feeding system of liquid material | |
| CN201040408Y (en) | Desulfurization device for rubber | |
| CN203610090U (en) | Rapid material preparing equipment | |
| CN203360976U (en) | Asphalt mixture stirring equipment | |
| CN203805169U (en) | Double-stage conveying device of rubber material granulation equipment | |
| CN203484129U (en) | Deslagging screw rod device | |
| CN204820407U (en) | Vertical biomass fuel briquetting machine | |
| CN204245115U (en) | A kind of expanding apparatus | |
| CN205091039U (en) | Weightless weigher platform device of buildding of grain powder mixed type | |
| CN202860488U (en) | Solid material charging device | |
| CN103468295B (en) | Reactor reaction unit | |
| CN203805167U (en) | Double-screw conveying device of rubber material granulation equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150429 Termination date: 20161114 |