CN201087185Y - Full-automatic oil refining device by waste plastics and scrap tire capable of continuously feeding and tapping - Google Patents
Full-automatic oil refining device by waste plastics and scrap tire capable of continuously feeding and tapping Download PDFInfo
- Publication number
- CN201087185Y CN201087185Y CNU2007200915241U CN200720091524U CN201087185Y CN 201087185 Y CN201087185 Y CN 201087185Y CN U2007200915241 U CNU2007200915241 U CN U2007200915241U CN 200720091524 U CN200720091524 U CN 200720091524U CN 201087185 Y CN201087185 Y CN 201087185Y
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- feeding
- cracking
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- oil refining
- plastic waste
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The utility model relates to a fully automatic and continuous feeding and slag discharging oil refining device for waste plastic and scrap tyre. The utility model comprises a discharging mechanism, a cracking mechanism and a condensation reorganization mechanism, wherein, the discharging mechanism is mainly composed of two-stage spiral feeding devices (3) and (4), material conveyors (1) and (2); a connecting device (9) and a sealing cover plate (10) are arranged between the two-stage spiral feeding devices (3) and (4), and one end of the spiral feeding device (4) is arranged in a cracking device (13) through a furnace cavity (12); a feeding inlet (5) with a valve (6) and a slag outlet (7) with a valve (8) are arranged on the spiral feeding devices (3); the material conveyor (1) is arranged at the upper part of the feeding inlet (5), and the material conveyor (2) is arranged at the lower part of the slag outlet (7). The utility model has the advantages that the heat energy generated during the cracking process is recycled and utilized; the cracking caldron adopts a rotating type, the heating area is enlarged, the cracking speed is enhanced, and the heat loss is also reduced; the continuous device is adopted for feeding and slag discharging, thereby the labor intensity of workers is reduced.
Description
(1) technical field
The utility model relates to the device that a kind of cracking waste plastics, damaged tire are produced liquid fuel, uninterrupted feed of particularly a kind of continous way and the refining liquid fuel device of slagging tap.
(2) background technology
Along with developing rapidly of global plastics, rubber industryization, though give the people's the life part that brings a lot of convenience, produced simultaneously plastic waste, damaged tire also cause huge pollution to human environment.Great amount of manpower and material resources and financial resources have all been dropped into to the regeneration of plastic waste, damaged tire in countries in the world.Wherein utilize plastic waste, damaged tire to produce the project of fuel, the heat that has obtained most countries is held in both hands.But see its this class production unit device, all have such or such defective, as the cracking process environmental protection can not be up to standard, high energy consumption, easily coking, dangerous, labour intensity is big, facility investment is not easy to greatly promote equipment making complexity etc.
(3) technology contents
The purpose of the utility model is to overcome the defective that prior art exists, provide a kind of automatically can continuous-feeding, the device of the cracking waste plastics of slagging tap, damaged tire.
To achieve these goals, the utility model is according to following technical scheme.Plastic waste, damaged tire oil refining apparatus that full-automatic continuous-feeding is slagged tap, comprise to discharging mechanism, cracking mechanism and condensation reorganization mechanism, the described discharging mechanism that gives mainly is made up of two-part feeding screw, two material conveyors, coupling device and seal cover board are set between the two-part feeding screw, and an end of one of them feeding screw places in the cracker through burner hearth; The opening for feed of band valve and the slag notch of band valve are set on another feeding screw; On opening for feed top material conveyor is set), in the bottom of slag notch material conveyor is set.
Described cracking mechanism mainly comprises body of heater, places the intravital cracking still of stove, between body of heater and cracking still flue is set; Cracking still one end and reheat-type oil gas macromole reformer are provided with strainer and gas sealer according to pipe connection on the pipeline that is connected.On the cracking still inwall, screw blade is set.
Described condensation reorganization mechanism mainly comprises primary dust removing chamber, two-stage dust removal devulcanizer, condenser and the storage tank that has valve, it is indoor that reheat-type oil gas macromole reformer is arranged on primary dust removing, the inlet mouth of reformer is connected with the delivery port of cracking still, the air outlet of reformer is connected with the inlet mouth of condenser, and the air outlet of condenser is connected with storage tank; According to pipe connection, the two-stage dust removal devulcanizer also is connected with blower fan between primary dust removing chamber and the two-stage dust removal devulcanizer.
Further between water seal strainer that increases and the storage tank according to pipe connection, the pipeline of drawing from the water seal strainer communicates with burner hearth flue in the cracking mechanism by vacuum breaker again.
Between primary dust removing chamber and the described cracking mechanism burner hearth inner flue according to pipe connection.
By above-mentioned description as can be known, the utility model has following superiority.
1, makes full use of the heat energy that is produced in the parallel off process and carry out recycling; What produce in the cracking process does not coagulate inflammable gas, by water seal filtration and plate check valve twice security device, makes full combustion of gas, thereby reaches the purpose of energy-conserving and environment-protective, production safety.
2, cracking still has adopted revolvingly, has increased heating surface area, has improved rate of cleavage, has also reduced thermal losses; Rotary cracking still has solved the problem of easy coking in the still under the situation of utilizing oil gas sealer assurance oil gas not reveal.
3, feed and slag tap and adopted the continuous uninterrupted device has reduced working strength of workers.
4, entire equipment is simple, not only can reduce cost but also making and operation easily.
(4) description of drawings
Fig. 1 is the utility model structural representation.
(5) embodiment
Concrete structure of the present utility model sees also accompanying drawing 1.When use equipment carries out plastic waste or damaged tire cracking, at first seal cover board 10 is taken off, after by coupling device 9 feeding screw 3 and 4 being connected and fixed then, start drive-motor feeding screw and cracking still 13 are rotated.Restart transfer roller 1, Open valve 6 is sent into plastic waste or damaged tire in the opening for feed 5, and by feeding screw it is sent in the cracking still 13, treat to stop all motors after material is filled still, feeding screw 4 is separated with 3, cover seal cover board 10, just can enter ordinary production.
The gas-oil mixture of producing in cracking process enters into reheat-type oil gas macromole reformer 17 through filter 15, air seal device 16.Owing to be filled with molecular sieve in the reformer, make and contain macromolecular oil gas and reassemble into small molecules oil gas therein, be condensed into by condenser 21 again and enter oil storage behind the liquid fuel and irritate 22.Because the inflammable gas that has a condensation also irritates 22 with entering into oil storage, this gas can burn in water seal strainer 23, vacuum breaker 24 enter the flue 11 of burner hearth.Meanwhile under the graviational interaction of blower fan 20, hot blast and dust in the burner hearth 12 enter into primary dust removing chamber 18 through flue 11, and reheat-type oil gas macromole reformer 17 is heated.In heating, can remove the part dust, further remove dust and carry out desulfurization through two-stage dust removal devulcanizer 19 again.Regularly opening the valve 25 that is arranged on bottom, primary dust removing chamber discharges dust.
Because screw blade 14 is set on the inwall of cracking still 13, material is entered in the still, slag charge is discharged in still when cracking still reverses.Take off seal cover board 10 when slagging tap, feeding screw 4 is fixedlyed connected with 3, and starter motor also makes cracking still 13 counter-rotatings, opens valve 8 and transfer roller 2 simultaneously, residue in the still drops on the transfer roller 2 by slag notch 7 and to send in the residue pool under the acting in opposition of still inner screwy fin.After residue goes out only in the still, valve-off 8, transfer roller 2, equipment enters into the state of charging.
Claims (7)
1. plastic waste, damaged tire oil refining apparatus that full-automatic continuous-feeding is slagged tap, comprise to discharging mechanism, cracking mechanism and condensation reorganization mechanism, it is characterized in that the described discharging mechanism that gives mainly is made up of two-part feeding screw (3) and (4), material conveyor (1) and (2), coupling device (9) and seal cover board (10) are set between two-part feeding screw (3) and (4), and wherein an end of feeding screw (4) places in the cracker (13) through burner hearth (12); The opening for feed (5) of band valve (6) and the slag notch (7) of band valve (8) are set on another feeding screw (3); On opening for feed (5) top material conveyor (1) is set, material conveyor (2) is set in the bottom of slag notch (7).
2. the plastic waste that full-automatic continuous-feeding as claimed in claim 1 is slagged tap, damaged tire oil refining apparatus, it is characterized in that described cracking mechanism mainly comprises body of heater (12), places the intravital cracking still of stove (13), is provided with flue (11) between body of heater (12) and cracking still (13); Cracking still one end and reheat-type oil gas macromole reformer (17) are through pipe connection.
3. the plastic waste that full-automatic continuous-feeding as claimed in claim 2 is slagged tap, damaged tire oil refining apparatus is characterized in that on described cracking still (13) inwall screw blade (14) being set.
4. the plastic waste that full-automatic continuous-feeding as claimed in claim 2 is slagged tap, damaged tire oil refining apparatus is characterized in that on cracking still one end and pipeline that reheat-type oil gas macromole reformer (17) is connected strainer (15) and gas sealer (16) being set.
5. the plastic waste that full-automatic continuous-feeding as claimed in claim 1 is slagged tap, the damaged tire oil refining apparatus, it is characterized in that described condensation reorganization mechanism mainly comprises the primary dust removing chamber (18) that has valve (25), two-stage dust removal devulcanizer (19), condenser (21) and storage tank (22), in primary dust removing chamber (18), be provided with reheat-type oil gas macromole reformer (17), the inlet mouth of reformer is connected with the delivery port of cracking still (13), the air outlet of reformer is connected with the inlet mouth of condenser (21), and the air outlet of condenser (21) is connected with storage tank (22); According to pipe connection, two-stage dust removal devulcanizer (19) also is connected with blower fan (20) between primary dust removing chamber (18) and the two-stage dust removal devulcanizer (19).
6. the plastic waste that full-automatic continuous-feeding as claimed in claim 5 is slagged tap, damaged tire oil refining apparatus, it is characterized in that between the water seal strainer (23) that further increases and the storage tank (22) that according to pipe connection the pipeline of drawing communicates with burner hearth flue (11) in the cracking mechanism by vacuum breaker (24) again from water seal strainer (23).
7. the plastic waste that full-automatic continuous-feeding as claimed in claim 5 is slagged tap, damaged tire oil refining apparatus.It is characterized in that between primary dust removing chamber (18) and the described cracking mechanism's burner hearth inner flue (11) according to pipe connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200915241U CN201087185Y (en) | 2007-08-17 | 2007-08-17 | Full-automatic oil refining device by waste plastics and scrap tire capable of continuously feeding and tapping |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200915241U CN201087185Y (en) | 2007-08-17 | 2007-08-17 | Full-automatic oil refining device by waste plastics and scrap tire capable of continuously feeding and tapping |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201087185Y true CN201087185Y (en) | 2008-07-16 |
Family
ID=39634779
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200915241U Expired - Lifetime CN201087185Y (en) | 2007-08-17 | 2007-08-17 | Full-automatic oil refining device by waste plastics and scrap tire capable of continuously feeding and tapping |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201087185Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102504857A (en) * | 2011-11-07 | 2012-06-20 | 李昊民 | Intermittent type waste rubber cracking device |
| CN103937526A (en) * | 2014-04-30 | 2014-07-23 | 辽阳县鼎理商贸有限公司 | Equipment for extracting oil by means of continuously thermally cracking waste tires at normal pressure |
| CN104650944A (en) * | 2014-06-09 | 2015-05-27 | 广西腾博再生能源有限公司 | Waste rubber cracking kettle |
| CN107541233A (en) * | 2017-09-28 | 2018-01-05 | 临汾市尧都区阿宅废旧物资回收有限公司 | A kind of waste plastics tire oil refining furnace |
-
2007
- 2007-08-17 CN CNU2007200915241U patent/CN201087185Y/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102504857A (en) * | 2011-11-07 | 2012-06-20 | 李昊民 | Intermittent type waste rubber cracking device |
| CN102504857B (en) * | 2011-11-07 | 2013-11-06 | 李昊民 | Intermittent type waste rubber cracking device |
| CN103937526A (en) * | 2014-04-30 | 2014-07-23 | 辽阳县鼎理商贸有限公司 | Equipment for extracting oil by means of continuously thermally cracking waste tires at normal pressure |
| CN104650944A (en) * | 2014-06-09 | 2015-05-27 | 广西腾博再生能源有限公司 | Waste rubber cracking kettle |
| CN104650944B (en) * | 2014-06-09 | 2017-02-01 | 广西腾博再生能源有限公司 | Waste rubber cracking kettle |
| CN107541233A (en) * | 2017-09-28 | 2018-01-05 | 临汾市尧都区阿宅废旧物资回收有限公司 | A kind of waste plastics tire oil refining furnace |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080716 |
|
| CX01 | Expiry of patent term |