CN206799536U - A kind of full-automatic damaged tire cracker - Google Patents
A kind of full-automatic damaged tire cracker Download PDFInfo
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- CN206799536U CN206799536U CN201720039967.XU CN201720039967U CN206799536U CN 206799536 U CN206799536 U CN 206799536U CN 201720039967 U CN201720039967 U CN 201720039967U CN 206799536 U CN206799536 U CN 206799536U
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- tank
- kettle
- damaged tire
- pump
- water
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Abstract
It the utility model is related to field of Environment Protection, especially a kind of full-automatic damaged tire cracker, including damaged tire input unit, embryotomic device, concentration equipment, steel wire retracting device, belt conveyor, first vavuum pump, desulfurizing dust-collector, dryer, helixseal charger, liquefaction kettle, first gasification kettle filtration tank, second gasification kettle filtration tank, condenser, catch pot, gear oil pump, fuel reservoir, water circulating pump, circulate water input unit, electric heater, thermal medium storage tank, air-introduced machine, gas pump, heat carrier furnace, burner, water sealed tank, dry gas purification tank, dry gas surge tank, steam-water separation tank；By after being cracked to damaged tire can olefiant gas body carry out proposing oil processing, absorption processing is carried out to harmful substance, recycled fuel gas as heat energy, effectively damaged tire is turned waste into wealth, simple in construction, easy to operate, energy consumption is low, securely and reliably, completely innoxious, pollution-free and optimal recycling can be achieved.
Description
Technical field
Field of Environment Protection is the utility model is related to, especially a kind of full-automatic pollution-free low energy consumption damaged tire cracker.
Background technology
Junked tire has very strong heat resistanceheat resistant, heat biology, mechanical resistance, and is difficult degraded, and decades all without disappearing naturally
Lose, long-term air storage, do not only take up a large amount of soils, and easily grow killing propagation disease, be known as " black dirt
Dye ", each enterprise and scientific research institution are being explored always for many years handles damaged tire processing method, solves this and is difficult to determine for many years
The problem of exhausted, it is mostly to use intermittent autoclave refining equipment to solve this problem at present, but this equipment is unable to continuous industry
Production, high energy consumption, security is excessively poor, explosion issues often occurs, and environmental protection is not up to standard, and fails in final solution processing
Poisonous fume, waste water and scrap problems are discharged, so as to produce secondary pollution.
The content of the invention
In order to solve the technical deficiency present in existing apparatus, the utility model provides a kind of full-automatic damaged tire cracking
Device, the apparatus structure is simple, easy to operate, and energy consumption is low, securely and reliably, completely innoxious, pollution-free and optimal money can be achieved
Sourceization utilizes.
The utility model solves its technical problem the technical scheme adopted is that a kind of full-automatic damaged tire cracker,
Including damaged tire input unit, embryotomic device, concentration equipment, steel wire retracting device, belt conveyor, the first vavuum pump, desulfurization
Deduster, dryer, helixseal charger, liquefaction kettle, slag extractor, the first gasification kettle filtration tank, the second gasification kettle filtration tank,
Condenser, catch pot, gear oil pump, fuel reservoir, gasoline output device, water circulating pump, circulate water input unit, circulation
Water output device, electric heater, thermal medium storage tank, air-introduced machine, gas pump, heat carrier furnace, burner, water sealed tank, dry gas purification
Tank, dry gas surge tank, steam-water separation tank, the second vavuum pump, blowdown apparatus；Embryotomic device both ends connect damaged tire input dress respectively
Put and concentration equipment, steel wire retracting device are located at concentration equipment lower end, be connected by delivery pipe with concentration equipment, belt conveyor
Both ends connect concentration equipment and dryer respectively, and dryer lower end is connected with the first vavuum pump, the connection of the first vavuum pump other end
Desulfurizing dust-collector, helixseal charger both ends connect dryer and liquefaction kettle respectively, and slag extractor is connected to liquid by delivery pipe
Change kettle lower end, the first gasification kettle filtration tank both ends connect liquefaction kettle and the second gasification kettle filtration tank, the second gasification kettle filtering respectively
The tower other end connects condenser, condenser other end connection catch pot middle part, and catch pot upper and lower ends connect respectively
Second vavuum pump and gear oil pump, gear oil pump other end connection fuel reservoir, fuel reservoir other end connection gasoline output dress
Put, gas water separation tank both ends connect the second vavuum pump and dry gas surge tank, the connection dry gas purification of the dry gas surge tank other end respectively
Device one end, dry gas purifier other end connection water sealed tank one end, gas water separation tank, dry gas surge tank, dry gas purification tank and water seal
There are blowdown apparatus, water sealed tank other end connection burner in tank lower end, and burner is located in heat carrier furnace, heat carrier furnace top two
Individual exhaust outlet connects dryer and liquefaction kettle respectively, and electric heater connection thermal medium storage tank, air-introduced machine and gas pump are located side by side at
In thermal medium storage tank, thermal medium storage tank lower end connection heat carrier furnace and liquefaction kettle, thermal medium storage tank upper end connection heat carrier furnace, follow
Ring water pump both ends connect circulation water input unit and condenser, recirculated water output device connection condenser one end respectively.
Embryotomic device is anaerobic cracking reaction kettle.
There are heating jacket and heating coil axle in helixseal charger front end.
There is gas phase catalyst in dry gas surge tank and dry gas purification tank.
Air-introduced machine includes falling film absorbing device.
Condenser is heat exchanger.
There is liquid-phase catalyst in liquefaction kettle.
All operations are by PC control operation.
All devices are equipped with temperature indicator, pressure indicator, safety valve.
Workflow, damaged tire is delivered to this damaged tire cracker by damaged tire input unit, damaged tire passes through
Oil gas is largely converted into after the anaerobic cracking of embryotomic device, also there is Certain residues, mainly steel wire and powdered carbon black, steel wire
It is recovered in concentration equipment by magnetic separation into steel wire retracting device, remaining oil gas and powdered carbon black pass through belt conveyor
It is delivered to dryer and carries out drying and processing, now the first vavuum pump is by the hydrogen sulfide in oil gas and absorbing hydrogen chloride gas to desulfurization
Removed in deduster, so as to reduce the harm to environment, then Remaining Oil And Gas and powdered carbon black are fed via helixseal
Enter helixseal charger after the heating jacket and the further drying and processing of heating coil axle of machine front end, fed in helixseal
Further compression deoxidation treatment is carried out in machine, the oil gas and powdered carbon black after then handling enter liquefaction kettle, lead in liquefaction kettle
Liquid-phase catalyst effect is crossed by the too black dispatch of powdery to slag extractor, then oil gas is via the first gasification kettle filtration tank and the second gas
Enter condenser after changing the preliminary treatment of kettle filtration tank, condenser is a heat exchanger, and recirculated water is inputted and filled by water circulating pump
Water in putting is inputted to condenser, is then discharged by recirculated water output device, and oil gas enters oil after handling within the condenser
Gas knockout drum, it can be carried out after catch pot processing by gear oil pump being absorbed into fuel reservoir into the gas of oil product,
Enter gasoline output device after being handled in fuel reservoir, become the gasoline obtained by us；Can not after catch pot processing
It can pass through the second vavuum pump into oil product gas into the gas of oil product, such as methane, propane and carbon monoxide, and with impurity
Gas water separation tank is absorbed into, preliminary hydro-extraction processing is carried out in gas water separation tank, toxic gas and moisture enter blowdown apparatus
Handled, remaining gas sequentially enters dry gas surge tank and dry gas purification tank by gas phase catalyst therein to being left gas
Further purified, then carry out being completely dried processing into water sealed tank, formation is combustible can not be into oil substances and heavy oil
Into heat carrier furnace, it can not be heated into oil substances by the burner in heat carrier furnace, form the secondary use of resource, formed
Heat energy enters dryer and carries out drying and processing, and then heavy oil enters liquefaction kettle and carried out further into oily circular treatment, electric heater
Thermal medium storage tank is heated, gas pump provides power support for heating, and air-introduced machine, which contains falling film absorbing device, effectively to be inhaled
Pernicious gas caused by burning is received, electric heater and thermal medium storage tank provide initial thermal energy, while heat carrier for whole device
Part incendivity in stove can not olefiant gas body also can enter thermal medium storage tank as thermal medium, recycled as heating source.
The beneficial effects of the utility model are a kind of full-automatic pollution-free low energy consumption damaged tire crackers, by useless
After tire pyrolysis can olefiant gas body carry out proposing oil processing, absorption processing is carried out to harmful substance, using fuel gas as heat energy
Recycle, effectively damaged tire turned waste into wealth, simple in construction, easy to operate, energy consumption is low, securely and reliably, can be achieved entirely without
Evilization, pollution-free and optimal recycling.
Brief description of the drawings
The utility model is further illustrated with reference to the accompanying drawings and examples.
Fig. 1 is structural representation of the present utility model.
1. damaged tire input unit in figure, 2. embryotomic devices, 3. concentration equipments, 4. steel wire retracting devices, 5. Belt Conveyings
Machine, 6. first vavuum pumps, 7. desulfurizing dust-collectors, 8. dryers, 9. helixseal chargers, 10. liquefaction kettles, 11. slag extractors,
12. the first gasification kettle filtration tank, 13. second gasification kettle filtration tanks, 14. condensers, 15. catch pots, 16. gear oil pumps,
17. fuel reservoir, 18. gasoline output devices, 19. water circulating pumps, 20. circulation water input units, 21. recirculated water output devices,
22. electric heater, 23. thermal medium storage tanks, 24. air-introduced machines, 25. gas pumps, 26. heat carrier furnaces, 27. burners, 28. water seals
Tank, 29. dry gas purification tanks, 30. dry gas surge tanks, 31. steam-water separation tanks, 32. second vavuum pumps, 33. blowdown apparatus.
Embodiment
Referring to the drawings, a kind of full-automatic damaged tire cracker, including damaged tire input unit 1, embryotomic device 2, magnetic separation
Device 3, steel wire retracting device 4, belt conveyor 5, the first vavuum pump 6, desulfurizing dust-collector 7, dryer 8, helixseal charging
Machine 9, liquefaction kettle 10, slag extractor 11, the first gasification kettle filtration tank 12, the second gasification kettle filtration tank 13, condenser 14, Oil-gas Separation
Tank 15, gear oil pump 16, fuel reservoir 17, gasoline output device 18, water circulating pump 19, circulate water input unit 20, recirculated water
Output device 21, electric heater 22, thermal medium storage tank 23, air-introduced machine 24, gas pump 25, heat carrier furnace 26, burner 27, water seal
Tank 28, dry gas purification tank 29, dry gas surge tank 30, steam-water separation tank 31, the second vavuum pump 32, blowdown apparatus 33；Embryotomic device 2
Both ends connect damaged tire input unit 1 and concentration equipment 3 respectively, and steel wire retracting device 4 is located at the lower end of concentration equipment 3, by defeated
Pipe is sent to be connected with concentration equipment 3, the both ends of belt conveyor 5 connect concentration equipment 3 and dryer 8, the connection of the lower end of dryer 8 respectively
There is the first vavuum pump 6, the other end of the first vavuum pump 6 connection desulfurizing dust-collector 7, the both ends of helixseal charger 9 connect baking respectively
Dry machine 8 and liquefaction kettle 10, slag extractor 11 are connected to the lower end of liquefaction kettle 10, the both ends point of the first gasification kettle filtration tank 12 by delivery pipe
Not Lian Jie liquefaction kettle 10 and second gasify kettle filtration tank 13, the other end connection condenser 14 of the second gasification kettle filtration tank 13, condensation
The middle part of the other end of device 14 connection catch pot 15, the upper and lower ends of catch pot 15 connect the second vavuum pump 32 and gear respectively
Oil pump 16, the other end of gear oil pump 16 connection fuel reservoir 17, the other end of fuel reservoir 17 connection gasoline output device 18, air water
The both ends of knockout drum 31 connect the second vavuum pump 32 and dry gas surge tank 30, the connection dry gas purification of the other end of dry gas surge tank 30 respectively
The one end of device 29, the other end of dry gas purifier 29 connection water sealed tank 28 one end, gas water separation tank 31, dry gas surge tank 30, dry gas are net
Changing tank 29 and the lower end of water sealed tank 28 has blowdown apparatus 33, and the other end of water sealed tank 28 connection burner 27, burner 27 is positioned at warm
In bearer boiler 26, two, 26 top of heat carrier furnace exhaust outlet connects dryer 8 and liquefaction kettle 10 respectively, and electric heater 22 connects heat
Medium storage tank 23, air-introduced machine 24 and gas pump 25 are located side by side in thermal medium storage tank 23, and the lower end of thermal medium storage tank 23 connection heat carries
Body stove 26 and liquefaction kettle 10, the upper end of thermal medium storage tank 23 connection heat carrier furnace 26, the both ends of water circulating pump 19 connect recirculated water respectively
Input unit 20 and condenser 14, recirculated water output device 21 connect the one end of condenser 14.
Embryotomic device 2 is anaerobic cracking reaction kettle.
There are heating jacket and heating coil axle in the front end of helixseal charger 9.
There is gas phase catalyst in dry gas surge tank 30 and dry gas purification tank 23.
Air-introduced machine 24 includes falling film absorbing device.
Condenser 14 is heat exchanger.
There is liquid-phase catalyst in liquefaction kettle 10.
All operations are by PC control operation.
All devices are equipped with temperature indicator, pressure indicator, safety valve.
Workflow, damaged tire is delivered to this damaged tire cracker by damaged tire input unit 1, damaged tire passes through
Oil gas is largely converted into after the anaerobic cracking of embryotomic device 2, also there is Certain residues, mainly steel wire and powdered carbon black, steel
Silk is recovered in concentration equipment 3 by magnetic separation into steel wire retracting device 4, and remaining oil gas and powdered carbon black are defeated by belt
Send machine 5 to be delivered to dryer 8 and carry out drying and processing, now the first vavuum pump 6 inhales the hydrogen sulfide in oil gas and hydrogen chloride gas
Receipts are removed into desulfurizing dust-collector 7, and so as to reduce the harm to environment, then Remaining Oil And Gas and powdered carbon black are via spiral
Enter helixseal charger 9 after the heating jacket and the further drying and processing of heating coil axle of sealing charger 9 front end, in spiral shell
Further compression deoxidation treatment is carried out in rotation sealing charger 9, the oil gas and powdered carbon black after then handling enter liquefaction kettle 10,
By liquid-phase catalyst effect by the too black dispatch of powdery to slag extractor 11 in liquefaction kettle 10, then oil gas is via the first gasification
Enter condenser 14 after the preliminary treatment of the gasification kettle of kettle filtration tank 12 and second filtration tank 13, condenser 14 is a heat exchange
Device, water circulating pump 19 input the water circulated in water input unit 20 to condenser 14, then pass through recirculated water output device
21 discharges, oil gas enter catch pot 15 after being handled in condenser 14, can be into oil product after the processing of catch pot 15
Gas carries out being absorbed into fuel reservoir 17 by gear oil pump 16, enters gasoline output device after being handled in fuel reservoir 17
18, become the gasoline obtained by us；After the processing of catch pot 15 can not into the gas of oil product, such as methane, propane and
Carbon monoxide, and gas water separation tank 31 can be absorbed into by the second vavuum pump 32 into oil product gas with impurity, in gas
Preliminary hydro-extraction processing is carried out in water separation tank 31, toxic gas and moisture handled into blowdown apparatus 33, remaining gas according to
Secondary dry gas surge tank 30 and the dry gas purification tank 29 of entering further is purified by gas phase catalyst therein to remaining gas,
Then carry out being completely dried processing into water sealed tank 28, formation is combustible to enter heat carrier furnace into oil substances and heavy oil
26, it can not be heated into oil substances by the burner 27 in heat carrier furnace 26, form the secondary use of resource, form heat energy and enter
Enter dryer 8 and carry out drying and processing, then heavy oil is carried out further right into oily circular treatment, electric heater 22 into liquefaction kettle 10
Thermal medium storage tank 23 is heated, and gas pump 25 provides power support for heating, and air-introduced machine 24 can have containing falling film absorbing device
Effect absorbs pernicious gas caused by burning, and electric heater 22 and thermal medium storage tank 23 provide initial thermal energy for whole device, together
When heat carrier furnace 26 in part incendivity can not olefiant gas body also can enter thermal medium storage tank 23 as thermal medium, as heating
Source recycles.
Claims (7)
1. a kind of full-automatic damaged tire cracker, including damaged tire input unit, embryotomic device, concentration equipment, steel wire recovery
Device, belt conveyor, the first vavuum pump, desulfurizing dust-collector, dryer, helixseal charger, liquefaction kettle, slag extractor, the
One gasification kettle filtration tank, the second gasification kettle filtration tank, condenser, catch pot, gear oil pump, fuel reservoir, gasoline output
Device, water circulating pump, circulate water input unit, recirculated water output device, electric heater, thermal medium storage tank, air-introduced machine, combustion gas
Pump, heat carrier furnace, burner, water sealed tank, dry gas purification tank, dry gas surge tank, steam-water separation tank, the second vavuum pump, blowdown dress
Put；Characterized in that, embryotomic device both ends connect damaged tire input unit and concentration equipment respectively, steel wire retracting device is located at magnetic
Screening device lower end, it is connected by delivery pipe with concentration equipment, belt conveyor both ends connect concentration equipment and dryer respectively, dry
Dry machine lower end is connected with the first vavuum pump, first vavuum pump other end connection desulfurizing dust-collector, helixseal charger both ends point
Not Lian Jie dryer and liquefaction kettle, slag extractor is connected to liquefaction kettle lower end by delivery pipe, the first gasification kettle filtration tank both ends point
Not Lian Jie liquefaction kettle and the second gasification kettle filtration tank, the second gasification kettle filtration tank other end connection condenser, the condenser other end
Connect in the middle part of catch pot, catch pot upper and lower ends connect the second vavuum pump and gear oil pump respectively, and gear oil pump is another
One end connects fuel reservoir, and fuel reservoir other end connection gasoline output device, it is true that gas water separation tank both ends connect second respectively
Empty pump and dry gas surge tank, dry gas surge tank other end connection dry gas purifier one end, the connection water seal of the dry gas purifier other end
There are blowdown apparatus, the water sealed tank other end in tank one end, gas water separation tank, dry gas surge tank, dry gas purification tank and water sealed tank lower end
Burner is connected, burner is located in heat carrier furnace, and two, heat carrier furnace top exhaust outlet connects dryer and liquefaction kettle respectively,
Electric heater connects thermal medium storage tank, and air-introduced machine and gas pump are located side by side in thermal medium storage tank, the connection of thermal medium storage tank lower end
Heat carrier furnace and liquefaction kettle, thermal medium storage tank upper end connection heat carrier furnace, water circulating pump both ends connect recirculated water input dress respectively
Put and condenser, recirculated water output device connect condenser one end.
2. a kind of full-automatic damaged tire cracker according to claim 1, it is characterised in that the embryotomic device is nothing
Oxygen cracking reaction kettle.
A kind of 3. full-automatic damaged tire cracker according to claim 1, it is characterised in that the helixseal charging
There are heating jacket and heating coil axle in machine front end.
A kind of 4. full-automatic damaged tire cracker according to claim 1, it is characterised in that the dry gas surge tank and
There is gas phase catalyst in dry gas purification tank.
5. a kind of full-automatic damaged tire cracker according to claim 1, it is characterised in that the air-introduced machine includes
Falling film absorbing device.
6. a kind of full-automatic damaged tire cracker according to claim 1, it is characterised in that the condenser is handed over for heat
Parallel operation.
7. a kind of full-automatic damaged tire cracker according to claim 1, it is characterised in that have liquid in the liquefaction kettle
Phase catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720039967.XU CN206799536U (en) | 2017-01-13 | 2017-01-13 | A kind of full-automatic damaged tire cracker |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720039967.XU CN206799536U (en) | 2017-01-13 | 2017-01-13 | A kind of full-automatic damaged tire cracker |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206799536U true CN206799536U (en) | 2017-12-26 |
Family
ID=60729338
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720039967.XU Expired - Fee Related CN206799536U (en) | 2017-01-13 | 2017-01-13 | A kind of full-automatic damaged tire cracker |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206799536U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115125027A (en) * | 2021-03-26 | 2022-09-30 | 慕尔(大连)科技有限公司 | Pyrolysis gas cyclic utilization device of cracking furnace |
-
2017
- 2017-01-13 CN CN201720039967.XU patent/CN206799536U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115125027A (en) * | 2021-03-26 | 2022-09-30 | 慕尔(大连)科技有限公司 | Pyrolysis gas cyclic utilization device of cracking furnace |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171226 Termination date: 20220113 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |