CN211420054U - Continuous feeding type pyrolysis device - Google Patents

Continuous feeding type pyrolysis device Download PDF

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Publication number
CN211420054U
CN211420054U CN202020008970.7U CN202020008970U CN211420054U CN 211420054 U CN211420054 U CN 211420054U CN 202020008970 U CN202020008970 U CN 202020008970U CN 211420054 U CN211420054 U CN 211420054U
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China
Prior art keywords
star
wheel
feeding
shaped
discharging
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Expired - Fee Related
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CN202020008970.7U
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Chinese (zh)
Inventor
武金辉
柳毅博
丛伯一
许丝雨
周冠池
刘雷
巩志强
王振波
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China University of Petroleum East China
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China University of Petroleum East China
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Priority to CN202020008970.7U priority Critical patent/CN211420054U/en
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Abstract

The utility model relates to a continuous feed formula pyrolysis device, the device include motor, bearing member one, boiler tube, intake pipe one, hopper, broken vaulting pole, star type feeding wheel one, a feeding section of thick bamboo, star type feeding wheel two, heating furnace, blast pipe, bearing member two, star type discharging wheel one, go out a feed cylinder, star type discharging wheel two, discharge gate, intake pipe two, spiral auger. During operation, through the linkage of two star type feeding wheels, kept apart gaseous when guaranteeing that the material gets into the furnace body, the material is through the pyrolysis back, through the linkage of two star type play material wheels with material eduction gear, the pyrolysis is gaseous to be discharged from the blast pipe. The pyrolysis device realizes simultaneous processing of continuous feeding and continuous discharging, greatly improves the production efficiency, and has the advantages of simple structure and wide application range.

Description

Continuous feeding type pyrolysis device
Technical Field
The utility model relates to a pyrolysis device, in particular to continuous feed formula pyrolysis device.
Background
Pyrolysis is a technique for cracking organic components in materials into light components under anaerobic conditions, escaping volatile products and forming solid residues, and has a wide application prospect. The existing pyrolysis device can not realize continuous pyrolysis treatment well, and the pyrolysis efficiency of the treatment device which realizes continuous pyrolysis is still to be improved.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model provides a continuous feed formula pyrolysis device through the linkage of two star type feeding wheels, has kept apart gas when guaranteeing that the material gets into the furnace body to let in inert gas through the intake pipe and guarantee the pyrolysis condition. After the material is pyrolyzed, the material is discharged from the material discharge device through the linkage of the two star-shaped discharge wheels, and the pyrolysis gas is discharged from the exhaust pipe, so that the material pyrolysis efficiency is greatly improved.
In order to achieve the above purpose, the technical scheme of the utility model is as follows: a continuous feeding type pyrolysis device comprises a motor, a bearing component I, a furnace tube, an air inlet tube I, a hopper, an arch breaking rod, a star-shaped feeding wheel I, a feeding cylinder, a star-shaped feeding wheel II, a heating furnace I, a heating furnace II, a heating furnace III, an exhaust pipe, a bearing component II, a star-shaped discharging wheel I, a discharging cylinder, a star-shaped discharging wheel II, a discharging port, an air inlet tube II and a spiral auger. The motor is connected with the spiral flood dragon, the bearing member I and the bearing member II are both connected with the furnace tube, the arch breaking rod is installed inside the hopper, the hopper is installed on the upper portion of the feeding cylinder, and the star-shaped feeding wheel I and the star-shaped feeding wheel II are installed inside the feeding cylinder. The first air inlet pipe is arranged in the middle of the feeding cylinder and is positioned between the first star-shaped feeding wheel and the second star-shaped feeding wheel. The feeding cylinder is connected with the furnace tube. The middle section of the furnace tube is sequentially provided with the first heating furnace, the second heating furnace and the third heating furnace. The star-shaped discharging wheel I and the star-shaped discharging wheel II are arranged in the discharging barrel, and the air inlet pipe II is arranged in the middle of the discharging barrel and is positioned between the star-shaped discharging wheel I and the star-shaped discharging wheel II. The discharging barrel and the furnace tube are installed together.
Furthermore, the arch breaking rod is formed by welding four connecting rods to form a semi-closed ring shape and is arranged at the middle lower part of the hopper.
Further, the first star-shaped feeding wheel and the second star-shaped feeding wheel are identical in structure and are welded with a plurality of blades which are uniformly distributed, and the first star-shaped feeding wheel and the second star-shaped feeding wheel can enable materials to enter blade gaps when rotating, so that the materials are conveyed through rotation.
Further, the upper part of the feeding cylinder is in a round cake shape, the middle part of the feeding cylinder is in a cylindrical shape, the lower part of the feeding cylinder is in a round cake shape, the upper part of the feeding cylinder is provided with a first star-shaped feeding wheel, the middle part of the feeding cylinder is provided with the first air inlet pipe, and the lower part of the feeding cylinder is provided with a second star-shaped feeding.
Furthermore, the spiral auger is welded with a plurality of spiral blades, and the spiral auger can drive materials to move forwards when rotating, so that the continuous conveying of the materials is ensured, and the continuous pyrolysis of the materials is further completed.
Further, the furnace tube is of a cylindrical structure, two ends of the furnace tube are connected with the bearing component, the middle part of the furnace tube is connected with the heating furnace, the furnace tube is connected with the feeding cylinder at the end close to the motor, and the other end of the furnace tube is connected with the discharging cylinder and the exhaust pipe.
The utility model discloses a theory of operation is: a motor of a continuous feeding type pyrolysis device is started to drive a spiral auger to rotate. The material enters the feeding cylinder from the hopper through the arch breaking rod, and enters the furnace tube from the feeding cylinder through the rotation of the star-shaped feeding wheel I and the star-shaped feeding wheel II and contacts with the spiral auger. Under the drive of the spiral auger, the material moves forward along the furnace tube. And protective gas enters the feeding cylinder through the first gas inlet pipe, so that air in the hopper is prevented from entering the pyrolysis furnace, and meanwhile, the protective gas and the materials enter the furnace pipe together. Under the action of the first heating furnace, the materials are heated and subjected to low-temperature pyrolysis, under the action of the second heating furnace, the materials are subjected to high-temperature pyrolysis, under the action of the third heating furnace, the materials begin to cool, and meanwhile, pyrolysis gas is discharged through the exhaust pipe. The material after the pyrolysis is driven by the spiral auger and gets into out the feed cylinder, and under the effect of star type play material wheel one and star type play material wheel two, the material leaves the pyrolysis oven by the discharge gate, and protective gas gets into out the feed cylinder by intake pipe two simultaneously, has prevented that the air from getting into the pyrolysis oven by the discharge gate.
Compared with the prior art, the utility model discloses the beneficial effect who has does:
the utility model provides a continuous feed formula pyrolysis device through the linkage of two star type feeding wheels, has kept apart gas when guaranteeing that the material gets into the furnace body to let in protective gas through the intake pipe and guarantee the pyrolysis. After the material is pyrolyzed, the material is discharged from the material discharge device through the linkage of the two star-shaped discharge wheels, and the pyrolysis gas is discharged from the exhaust pipe, so that the material pyrolysis efficiency is greatly improved.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the examples or the prior art descriptions will be briefly described below.
Fig. 1 is a schematic view of the overall structure of a continuous feeding type pyrolysis device of the present invention.
1. Motor 2 bearing component 3 furnace tube
4. Air inlet pipe I5, hopper 6, arch breaking rod
7. Star-shaped feeding wheel I8, feeding cylinder 9, star-shaped feeding wheel II
10. Heating furnace I11, heating furnace II 12 and heating furnace III
13. Exhaust pipe 14, bearing member two 15, star type discharging wheel one
16. Discharging barrel 17, star-shaped discharging wheel II 18 and discharging port
19. Air inlet pipe II 20. spiral auger 20
Detailed Description
The technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiment of the present invention. As shown in fig. 1, a continuous feeding type pyrolysis device comprises a motor 1, a bearing member I2, a furnace tube 3, an air inlet tube I4, a hopper 5, an arch breaking rod 6, a star-shaped feeding wheel I7, a feeding cylinder 8, a star-shaped feeding wheel II 9, a heating furnace I10, a heating furnace II 11, a heating furnace III 12, an exhaust pipe 13, a bearing member II 14, a star-shaped discharging wheel I15, a discharging cylinder 16, a star-shaped discharging wheel II 17, a discharging port 18, an air inlet tube II 19 and a spiral auger 20. Motor 1 is connected with spiral flood dragon 20, and bearing member one 2 and bearing member two 14 all are connected with boiler tube 3, broken hunch pole 6 and install in the inside of hopper 5, and hopper 5 installs on the upper portion of feed cylinder 8, and star type feed wheel one 7 and star type feed wheel two 9 are equipped with to the inside of feed cylinder 8. The air inlet pipe I4 is arranged in the middle of the feeding cylinder 8 and is positioned between the star-shaped feeding wheel I7 and the star-shaped feeding wheel II 9. The feeding cylinder 8 is connected with the furnace tube 3. The middle section of the furnace tube 3 is sequentially provided with a first heating furnace 10, a second heating furnace 11 and a third heating furnace 12. The inside of the discharging barrel 16 is provided with a first star-shaped discharging wheel 15 and a second star-shaped discharging wheel 17, and the air inlet pipe 19 is arranged in the middle of the discharging barrel 16 and is positioned between the first star-shaped discharging wheel 15 and the second star-shaped discharging wheel 17. The discharging barrel 16 is installed together with the furnace tube 3.
The arch breaking rod 6 is formed by welding four connecting rods to form a semi-closed ring shape and is arranged at the middle lower part of the hopper 5.
The first star-shaped feeding wheel 7 and the second star-shaped feeding wheel 9 are identical in structure, a plurality of blades which are uniformly distributed are welded, the first star-shaped feeding wheel 7 and the second star-shaped feeding wheel 9 can enable materials to enter blade gaps when rotating, and the materials are conveyed through rotation.
The upper part of the feeding cylinder 8 is in a round cake shape, the middle part of the feeding cylinder is in a cylindrical shape, the lower part of the feeding cylinder is in a round cake shape, the upper part of the feeding cylinder is provided with a star-shaped feeding wheel I7, the middle part of the feeding cylinder is provided with an air inlet pipe I4, and the lower part of the feeding cylinder is provided with a star-.
The spiral auger 20 is welded with a plurality of spiral blades, and the spiral auger 20 can drive materials to move forward when rotating, so that the continuous conveying of the materials is ensured, and the continuous pyrolysis of the materials is further completed.
The furnace tube 3 is a cylindrical structure, two ends of the furnace tube are both connected with bearing components, the middle part of the furnace tube is connected with the heating furnace, the end close to the motor 1 is connected with the feeding cylinder 8, and the other end of the furnace tube is connected with the discharging cylinder 16 and the exhaust pipe 13.
The utility model discloses a theory of operation is: a motor 1 of a continuous feeding type pyrolysis device is started to drive a spiral auger 20 to rotate. The material enters the feeding cylinder 8 from the hopper 5 through the arch breaking rod 6, and enters the furnace tube 3 from the feeding cylinder 8 through the rotation of the star-shaped feeding wheel I7 and the star-shaped feeding wheel II 9 and contacts with the spiral auger 20. The material moves forward along the furnace tube 3 under the drive of the spiral auger 20. And protective gas enters the feeding cylinder 8 through the first air inlet pipe 4, so that air in the hopper 5 is prevented from entering the pyrolysis furnace, and meanwhile, the protective gas and the materials enter the furnace tube 3 together. Under the action of the first heating furnace 10, the materials are heated and subjected to low-temperature pyrolysis, under the action of the second heating furnace 11, the materials are subjected to high-temperature pyrolysis, under the action of the third heating furnace 12, the materials begin to cool, and meanwhile, pyrolysis gas is discharged through the exhaust pipe 13. The material after pyrolysis is driven by spiral auger 20, gets into out feed cylinder 16, under the effect of star type material wheel one 15 and star type material wheel two 17, the material leaves the pyrolysis oven by discharge gate 18, and protective gas gets into out feed cylinder 16 by intake pipe two 19 simultaneously, has prevented that the air from getting into the pyrolysis oven by discharge gate 18.
The utility model provides a continuous feed formula pyrolysis device through the linkage of two star type feeding wheels, has kept apart gas when guaranteeing that the material gets into the furnace body to let in protective gas through the intake pipe and guarantee the pyrolysis condition. After the material is pyrolyzed, the material is discharged from the material discharge device through the linkage of the two star-shaped discharge wheels, and the pyrolysis gas is discharged from the exhaust pipe, so that the material pyrolysis efficiency is greatly improved. The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.

Claims (6)

1. A continuous feeding type pyrolysis device comprises a motor, a bearing component I, a furnace tube, an air inlet tube I, a hopper, an arch breaking rod, a star-shaped feeding wheel I, a feeding cylinder, a star-shaped feeding wheel II, a heating furnace I, a heating furnace II, a heating furnace III, an exhaust pipe, a bearing component II, a star-shaped discharging wheel I, a discharging cylinder, a star-shaped discharging wheel II, a discharging port, an air inlet tube II and a spiral auger, wherein the motor is connected with the spiral auger, two ends of the spiral auger are respectively installed with the bearing component I and the bearing component II, the bearing component I and the bearing component II are installed with the furnace tube together, the arch breaking rod is installed with the hopper, the hopper is installed with the feeding cylinder together, the star-shaped feeding wheel I and the star-shaped feeding wheel II are installed in the feeding cylinder, the air inlet tube I is installed in the middle of the feeding cylinder, the feeding cylinder is connected with the furnace tube, the first heating furnace, the second heating furnace and the third heating furnace are sequentially arranged on the furnace tube, the furnace tube is installed with the exhaust pipe, the first star-shaped discharging wheel and the second star-shaped discharging wheel are installed inside the discharging cylinder, the second air inlet pipe is installed in the middle of the discharging cylinder and is located between the first star-shaped discharging wheel and the second star-shaped discharging wheel, and the discharging cylinder is connected with the furnace tube.
2. A continuous feed pyrolysis apparatus as claimed in claim 1 wherein: the arch breaking rod is formed by welding four connecting rods to form a semi-closed ring shape and is arranged at the middle lower part of the hopper.
3. A continuous feed pyrolysis apparatus as claimed in claim 1 wherein: the first star-shaped feeding wheel, the second star-shaped feeding wheel, the first star-shaped discharging wheel and the second star-shaped discharging wheel are identical in structure and are welded with a plurality of uniformly distributed blades.
4. A continuous feed pyrolysis apparatus as claimed in claim 1 wherein: the feeding cylinder and the discharging cylinder have the same structure, the upper part is in a round cake shape, the middle part is in a cylindrical shape, and the lower part is in a round cake shape.
5. A continuous feed pyrolysis apparatus as claimed in claim 1 wherein: the spiral auger is welded with a plurality of uniformly distributed spiral blades, so that the spiral auger can drive materials to advance when rotating.
6. A continuous feed pyrolysis apparatus as claimed in claim 1 wherein: the furnace tube is of a cylindrical structure, two ends of the furnace tube are connected with the bearing component, the middle part of the furnace tube is connected with the heating furnace, the furnace tube is connected with the feeding cylinder at the end close to the motor, and the other end of the furnace tube is connected with the discharging cylinder and the exhaust pipe.
CN202020008970.7U 2020-01-03 2020-01-03 Continuous feeding type pyrolysis device Expired - Fee Related CN211420054U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020008970.7U CN211420054U (en) 2020-01-03 2020-01-03 Continuous feeding type pyrolysis device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020008970.7U CN211420054U (en) 2020-01-03 2020-01-03 Continuous feeding type pyrolysis device

Publications (1)

Publication Number Publication Date
CN211420054U true CN211420054U (en) 2020-09-04

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Application Number Title Priority Date Filing Date
CN202020008970.7U Expired - Fee Related CN211420054U (en) 2020-01-03 2020-01-03 Continuous feeding type pyrolysis device

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114540051A (en) * 2022-01-07 2022-05-27 上海市机电设计研究院有限公司 Sealed feeding device under plastic garbage pyrolysis condition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114540051A (en) * 2022-01-07 2022-05-27 上海市机电设计研究院有限公司 Sealed feeding device under plastic garbage pyrolysis condition
CN114540051B (en) * 2022-01-07 2024-05-17 上海市机电设计研究院有限公司 Sealing feeding device under plastic garbage pyrolysis condition

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200904

Termination date: 20210103

CF01 Termination of patent right due to non-payment of annual fee