CN103085193B - Regeneration method of anhydrous waste plastic - Google Patents
Regeneration method of anhydrous waste plastic Download PDFInfo
- Publication number
- CN103085193B CN103085193B CN201310034347.3A CN201310034347A CN103085193B CN 103085193 B CN103085193 B CN 103085193B CN 201310034347 A CN201310034347 A CN 201310034347A CN 103085193 B CN103085193 B CN 103085193B
- Authority
- CN
- China
- Prior art keywords
- comminutor
- granulation
- impurities
- removal
- pelletizing
- 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
Classifications
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The invention discloses a regeneration method of anhydrous waste plastic without washing. The method comprises the steps of crushing, purifying, dust absorbing, separating, pelletizing, sized dicing and packing, and specifically comprises the steps as follows: (1) crushing and purifying: crushing a polyethylene or polypropylene material in a crushing machine, and sequentially performing the steps of purifying by gravity, purifying by magnetic force, purifying by cutting, and falling impurity by inertia; (2) dust absorbing and separating: separating the crushed and purified material in three stages through a dust collector, a cyclone separator and a separator; and (3) pelletizing, sized dicing and packing, wherein the pelletizing comprises three forms: heating by a first pelletizer, reheating and filtering residue by a second pelletizer, and pelletizing by a third pelletizer, and qualified plastic wire produced in the third pelletizer is weighed and packed after being sized dicing. The regeneration method disclosed by the invention has the advantages of no need of washing, less pollution, low labor intensity, short process, simple device, low cost, and high recovery rate.
Description
Technical field
The present invention relates to a kind of plastic reclaimed chemical manufacturing technology field, particularly relate to a kind of anhydrous dry type waste plastic regeneration method.
Background technology
Come out so far from plastic product, be widely applied to social industry-by-industry, facilitated social development and progress, bring great convenience to the production of people, life, social use amount is increasing.But various waste or used plastics also increases the impact of environment and harm, and the regeneration of waste or used plastics has developed into the pith of recycle business thereupon.
Washing method processing waste or used plastics in current prior art with water, the method is backward in technique always, with artificial many, labour intensity is large, production efficiency is low, and energy consumption is high, work under bad environment, useless creeping loses many, particularly water consumption is large, constantly rinses, causes large amount of sewage, mud is mingled with and moulds silk discharge, severe contamination rivers and underground water source, pollute surrounding environment and a large amount of farmland.Our living environment of severe exacerbation, also misfortune and descendants.Such as application number is: the application for a patent for invention of " 201010507426.8 ", it discloses a kind of recycling process method of waste or used plastics, concrete steps comprise, first by waste polyethylene plastic crushing, by washing barrel cleaning, then in pond, secondary rinsing is dried, and then by carrying out plastics processing with various primary material, activator, compatilizer etc., finally cuts into various particular plastics.
Summary of the invention
Object of the present invention is exactly provide a kind of to mould renovation process in order to solve the problems of the technologies described above without the need to the anhydrous useless of washing.
The present invention solves the problems of the technologies described above the technical scheme adopted to be: a kind of anhydrous giving up moulds renovation process, and the method is without the need to washing, and the method comprises the step of fragmentation, removal of impurities, dust suction, separation, granulation, pelletizing, packaging, is specially:
(1) broken, removal of impurities;
Polyethylene or polypropylene material are carried out fragmentation in disintegrating machine, and the material after fragmentation to fall assorted step through gravity removal of impurities, magnetic force removal of impurities, sawing sheet removal of impurities and inertia successively;
(2) dust suction, separation;
Dust and material to be carried out first time by dust catcher and are separated by the material after broken, removal of impurities, and the mass transport for the first time after separation is to feed bin; Carried out second time with partial material through cyclone separator by the dust of dust catcher sucking-off to be separated, the material after second time is separated through separator by satisfactory for size feed separation to collection box, and flow to feed bin in order to granulation;
(3) granulation, pelletizing, packaging;
Described granulation comprises three grades of granulation modes, is respectively at the first granulator heating, to heat and filter residue and production granulation in the 3rd comminutor at the second comminutor again, produces produce qualified and mould silk and to weigh after pelletizing packaging from the 3rd comminutor.
Further, in fragmentation, removal step, gravity removal of impurities is carried out in the blanking processor being arranged on crusher lower, by carrying out magnetic force removal of impurities by magnetic force trash separator after blanking processor, in cutting machine, carry out sawing sheet removal of impurities, finally enter the inertia assorted device that falls through the material of three removal of impurities and realize inertia and fall assorted.
Further, in dust suction, separating step, in order to be greater than, 100 objects are totally broken moulds silk to the satisfactory material of described size.
The present invention compared with prior art, has the following advantages:
(1) without the need to washing, dry process produce can process clean, meet granulation conditions mould a block, and without sewage discharge, meet environmental requirement, and as usual can produce at northern severe winter, realize all-weather and produce;
(2) workshop does not have flying dust pollution, and discharge air multistage filtering separation, discharge, free of air pollution through dust arrester, except artificial toward except conveyer belt feeding, basic prosthetic is worked, and alleviates labour intensity, decreases the amount of labour used, solves on-the-spot pollution;
(3) flow process is short, and equipment is simple, and running is reliable, and cost is low, and system unit-hour output is high, and siccative is broken, siccative granulation power consumption low (compared with former WATER-WASHING METHOD), and production efficiency is high, and unit cost reduces;
(4) rate of recovery of the present invention is high, and Plastic is substantially lossless, also therefore non-pollutant discharge.The grit of discharging respectively when producing with bag of cement and cement flour all can distinguish reuse again or back to nature.
Accompanying drawing explanation
Fig. 1 is the anhydrous useless step schematic diagram moulding renovation process of the present invention.
In figure, each component names is as follows:
1-conveyer, 2-disintegrating machine, 3-blanking processor, 4-magnetic force trash separator; 5-filter, 6-cutting machine, 7-inertia falls assorted device, 8-dust catcher; 9-feeder, 10-cyclone separator, 11-separator, 12-main air blower; 13-collection box, 14-feed bin, 15-Material sucking machine; 16-feeding machine, 17-circulating fan, 18-first comminutor; 19-second comminutor, 20-the 3rd comminutor, 21-pelleter
Detailed description of the invention
Describe the present invention below in conjunction with accompanying drawing.
Anhydrous useless renovation process of moulding is exactly undertaken giving up moulding to regenerate by disposable technique replacement WATER-WASHING METHOD being processed into qualified particle, pp material such as various waste and old plastic woven bag, cement are moulded regeneration such as compiling packaging bag by disposable technique and are processed into plastic grain by this production method, or polyethylene raw material such as various waste and old plastic film regeneration are processed into and mould grain.
Next introduce anhydrous giving up of the present invention by specific embodiment and mould renovation process, it mainly comprises fragmentation, removal of impurities, dust suction, separation, granulation, pelletizing, packaging and other steps, and details are as follows for concrete steps:
One, broken, removal of impurities
Raw material fragmentation is carried out in disintegrating machine, and the raw material after fragmentation falls assorted through gravity removal of impurities, magnetic force removal of impurities, sawing sheet removal of impurities and inertia successively, then carries out the step of dust suction, separation.Concrete steps are as follows:
First waste or used plastics raw material is transported to workshop from storehouse, then feeding is to conveyer 1, by conveyer belt running and enter disintegrating machine 2 after magnetic inspection, after fragmentation, enter the blanking processor 3 being arranged on disintegrating machine 2 bottom carry out gravity removal of impurities, by the speed of regulating shaft to blowing in blanking processor 3, overcome the interference of turning round wind in blanking processor, make lighter useless block of moulding to axial operation, and not sedimentation is blocked, stone simultaneously, cement block, grit, spill from the assorted mouth that falls of the bottom of blanking processor after the heavy foreign material sedimentation such as metal object, the assorted mouthpiece that falls is gradient, thus heavy foreign material can utilize gradient to skid off voluntarily, realize the removal of impurities of first gravity.
Material after fragmentation enters magnetic force trash separator 4 by blanking processor 3, and that does not remove in blanking processor uselessly moulds the much the same metal sundries of block weight, under the effect of magnetic force, falls, adsorbed and carry out clearing up and collecting from the bottom sedimentation of magnetic force trash separator 4.Then, material, through filter 5, by filter screen by clean for the impurity filter being less than 5mm, realizes second removal of impurities.
Material through second removal of impurities enters cutting machine 6, under the quick machinery repeatedly strike of cutting machine and the comprehensive function of wind-force, the useless attachment, sand and dust, earth etc. moulded on block comes off, and skids off voluntarily from the inclined-plane of the dust fall plate of the bottom of cutting machine, realizes third time removal of impurities.Enter inertia through the material of three removal of impurities to fall assorted device 7, remove remaining impurity.
Two, dust suction, separation
Dust and material to be carried out first time by dust catcher and are separated by the material after broken, removal of impurities, and the mass transport for the first time after separation is to feed bin; Carried out second time with partial material through cyclone separator by the dust of dust catcher sucking-off to be separated, the material after second time is separated through separator by satisfactory for size feed separation to collection box, and flow to feed bin in order to granulation.Concrete steps are as follows:
Material after the 4th removal of impurities-inertia falls to mixing enters dust catcher 8, dust and material is carried out first time to be separated, and is separated clean material and is delivered to feed bin 14, in order to granulation by feeder 9.
Enter cyclone separator 10 and carry out second time through the dust of dust catcher 8 sucking-off and the broken silk of moulding of part and be separated, dust and the tiny silk of moulding of trace fall into from cyclone separator and connect dirt bag.And separate from cyclone separator 10 brokenly mould silk and micronic dust enters separator 11, through third time be separated will be greater than 100 objects totally broken silk of moulding all reclaim and enter collection box 13, prepare against granulation by conveying device automatic transport to feed bin.
Through the isolated atomic dirt of separator 11 (superfine dust) after dust arrester filters, automatically enter and connect dirt bag.Filter clean air to meet environmental requirement and then discharged outside workshop by main air blower 12 after test.
Three, granulation, pelletizing, packaging
Granulation comprises three grades of granulation modes, is respectively at the first granulator heating, to heat and filter residue and production granulation in the 3rd comminutor at the second comminutor again, produces produce qualified and mould silk and to weigh after pelletizing packaging from the 3rd comminutor.Specific as follows:
The clean plastic wire block meeting granulation conditions in feed bin 14 sends into feeding machine 16 through Material sucking machine 15; feeding machine 16 is with the speed of coupling and the mode by mechanical pressurization; siccative is moulded uniformly a block and feed the first comminutor 18; feeding machine 16 is provided with feeding machine circulating fan 17, can circulation return air to feed bin 14.A block of moulding after the first comminutor 18 heats is admitted to the second grain-making machine 19; after heating filter residue again, the 3rd comminutor 20 is entered in the second comminutor; produce from the 3rd comminutor 20 silk of moulding produced and enter cooling bath, packaging of weighing after eventually passing pelleter 21 pelletizing.
The present invention without the need to washing, dry process produce can process clean, meet granulation conditions mould a block, and without sewage discharge, meet environmental requirement.Production system of the present invention is negative-pressure sealed operation.Workshop does not have flying dust and pollutes, and discharges air multistage filtering separation, discharges, free of air pollution through dust arrester.The present invention because of without the need to washing, northern severe winter can be produced as usual, realize all-weather produce.The each operation of the whole production process of the present invention is automation closed operation, except artificial toward except conveyer belt feeding, basic prosthetic work, alleviate labour intensity, decrease the amount of labour used, solve on-the-spot pollution, improve useless working environment and the industry image moulding regeneration industry of tradition, improve industry self-confidence and self-esteem.Flow process of the present invention is short, and equipment is simple, and running is reliable, and cost is low, and system unit-hour output is high, and siccative is broken, siccative granulation power consumption low (compared with former WATER-WASHING METHOD), and production efficiency is high, and unit cost reduces.The rate of recovery of the present invention is high, and Plastic is substantially lossless, also therefore non-pollutant discharge.The grit of discharging respectively when producing with bag of cement and cement flour all can distinguish reuse again or back to nature.
The present invention be instead of by the mode that physics is broken apart and pollutes water-washing method that is heavy, complex process, and existing plant equipment can be utilized to carry out processing, and equipment investment fund is lower, extensively can be adopted by medium-sized and small enterprises.
Present invention process is mature on the whole, after repetition test, test, test manufacture, again improving, the high-volume actual production of model machine production system, product quality reaches purpose of design (exceeding washing material), production capacity can reach 800kg in one hour, and production capacity meets or exceeds theoretical yield.
By reference to the accompanying drawings the specific embodiment of the present invention is described although above-mentioned; but not limiting the scope of the invention; one of ordinary skill in the art should be understood that; on the basis of technical scheme of the present invention, those skilled in the art do not need to pay various amendment or distortion that creative work can make still within protection scope of the present invention.
Claims (1)
1. anhydrous giving up moulds a renovation process, and the method is without the need to washing, and it is characterized in that, the method comprises the step of fragmentation, removal of impurities, dust suction, separation, granulation, pelletizing, packaging, is specially:
(1) broken, removal of impurities;
Polyethylene or polypropylene material are carried out fragmentation in disintegrating machine, and the material after fragmentation is entered the blanking processor being arranged on crusher lower and carries out gravity removal of impurities, enters magnetic force trash separator and carry out magnetic force removal of impurities, enter cutting machine and to be hit by machinery and wind-force effect is carried out sawing sheet removal of impurities and carries out inertia to fall assorted step through the inertia assorted device that falls;
(2) dust suction, separation;
Dust and material to be carried out first time by dust catcher and are separated by the material after broken, removal of impurities, and the mass transport for the first time after separation is to feed bin; Carried out second time with partial material through cyclone separator by the dust of dust catcher sucking-off to be separated, the material after second time is separated through separator by satisfactory for size feed separation to collection box, and flow to feed bin in order to granulation; In order to be greater than, 100 objects are totally broken moulds silk to the satisfactory material of described size;
(3) granulation, pelletizing, packaging;
Described granulation comprises three grades of granulation modes, is respectively at the first granulator heating, to heat and filter residue and production granulation in the 3rd comminutor at the second comminutor again, produces produce qualified and mould silk and to weigh after pelletizing packaging from the 3rd comminutor, be specially: the clean plastic wire block meeting granulation conditions in feed bin sends into feeding machine through Material sucking machine, feeding machine is with the speed of coupling and the mode by mechanical pressurization, clean plastic wire block is fed the first comminutor uniformly, feeding machine is provided with feeding machine circulating fan, can circulation return air to feed bin, a block of moulding after the first granulator heating is admitted to the second comminutor, after heating filter residue again, the 3rd comminutor is entered in the second comminutor, produce from the 3rd comminutor the silk of moulding produced and enter cooling bath, to weigh after eventually passing pelleter pelletizing packaging.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310034347.3A CN103085193B (en) | 2013-01-29 | 2013-01-29 | Regeneration method of anhydrous waste plastic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310034347.3A CN103085193B (en) | 2013-01-29 | 2013-01-29 | Regeneration method of anhydrous waste plastic |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103085193A CN103085193A (en) | 2013-05-08 |
CN103085193B true CN103085193B (en) | 2015-07-15 |
Family
ID=48198563
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310034347.3A Expired - Fee Related CN103085193B (en) | 2013-01-29 | 2013-01-29 | Regeneration method of anhydrous waste plastic |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103085193B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014179907A1 (en) * | 2013-05-07 | 2014-11-13 | Sun Lizhi | Apparatus for recycling waste plastic by dry method and recycling method |
CN104959361B (en) * | 2015-06-18 | 2018-01-19 | 孙文星 | A kind of waste and old clothes innocuity disposal system and its processing method |
CN104960109B (en) * | 2015-06-18 | 2017-06-16 | 孙立志 | A kind of polyethylene waste or used plastics innocuity disposal system and its processing method |
CN107379321B (en) * | 2017-07-06 | 2019-05-03 | 砀山国晴塑料制品有限公司 | A kind of method of the anhydrous clean and reuse of waste plastic |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102303381A (en) * | 2011-06-19 | 2012-01-04 | 阳文皇 | Washing-free reclaiming method for garbage plastic and special equipment |
CN102785299A (en) * | 2012-08-21 | 2012-11-21 | 六安市洁美再生物资回收有限公司 | Polystyrene foam recovery granulating process |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4284616A (en) * | 1978-02-15 | 1981-08-18 | Intenco, Inc. | Process for recovering carbon black and hydrocarbons from used tires |
JP2964399B2 (en) * | 1998-02-23 | 1999-10-18 | 姜 昌美 | Recycled paper pellets, recycled paper pellet granulation method, and recycled paper pellet pelletizer |
-
2013
- 2013-01-29 CN CN201310034347.3A patent/CN103085193B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102303381A (en) * | 2011-06-19 | 2012-01-04 | 阳文皇 | Washing-free reclaiming method for garbage plastic and special equipment |
CN102785299A (en) * | 2012-08-21 | 2012-11-21 | 六安市洁美再生物资回收有限公司 | Polystyrene foam recovery granulating process |
Also Published As
Publication number | Publication date |
---|---|
CN103085193A (en) | 2013-05-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203381061U (en) | Dry-process waste plastic reclaimation device | |
CN205925938U (en) | Waste glass smashes recovery system | |
CN103537470B (en) | Solid waste Recovery Purifying reutilization system | |
CN101274322A (en) | Method for sorting consumer waste | |
CN103085193B (en) | Regeneration method of anhydrous waste plastic | |
CN202779142U (en) | Fixed type building rubbish treatment system | |
CN113369143B (en) | Decoration and construction waste recycling classification equipment and manufacturing method thereof | |
CN101954306B (en) | Biomass waste crushing system | |
JPH044083A (en) | System and device for screening waste construction material by utilizing hydraulic power | |
CN201848941U (en) | Large tire recovery production line | |
KR100358687B1 (en) | The constructive recycling methods and instruments of Reclaimed waste. | |
CN105062605A (en) | Biomass particle forming method | |
CN204220604U (en) | Cities and towns composting dry type Automated fine screening installation | |
CN108080402A (en) | Decoration garbage recycling recycles disposal system and method | |
CN201702000U (en) | Crushing system of biomass wastes | |
WO2014179907A1 (en) | Apparatus for recycling waste plastic by dry method and recycling method | |
CN101862810B (en) | Cast used sand and slag recycling equipment | |
CN103343027A (en) | Manufacturing equipment and method of fuel bar | |
CN209191063U (en) | Plastic cleaning equipment | |
CN208373249U (en) | A kind of recycled aggregate trimmer | |
CN212040902U (en) | Dust removal stores up whitewashed environmental protection shape system sand integration system | |
CN201848940U (en) | Minitype tyre recycling production line | |
CN110899308B (en) | Household garbage-oriented recycling system and method | |
CN210474264U (en) | Building engineering waste recovery device | |
CN203140686U (en) | Foundry used sand recycling treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
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: 20150715 Termination date: 20210129 |