SI21606A - Mechanical recycling procedure for composite polymeric material - Google Patents
Mechanical recycling procedure for composite polymeric material Download PDFInfo
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- SI21606A SI21606A SI200300232A SI200300232A SI21606A SI 21606 A SI21606 A SI 21606A SI 200300232 A SI200300232 A SI 200300232A SI 200300232 A SI200300232 A SI 200300232A SI 21606 A SI21606 A SI 21606A
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- Slovenia
- Prior art keywords
- extruder
- polymethylmethacrylate
- parts
- polyester resin
- composite
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- 239000000463 material Substances 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 30
- 239000002131 composite material Substances 0.000 title claims abstract description 20
- 238000004064 recycling Methods 0.000 title claims description 15
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 claims abstract description 15
- 239000002245 particle Substances 0.000 claims abstract description 14
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 claims abstract description 13
- 238000001125 extrusion Methods 0.000 claims abstract description 10
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 16
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 16
- 239000002699 waste material Substances 0.000 claims description 9
- 229920001225 polyester resin Polymers 0.000 claims description 5
- 239000004645 polyester resin Substances 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 2
- 239000003365 glass fiber Substances 0.000 abstract description 8
- 229920006337 unsaturated polyester resin Polymers 0.000 abstract description 8
- 239000000654 additive Substances 0.000 abstract description 3
- 230000007704 transition Effects 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 13
- 229920000642 polymer Polymers 0.000 description 7
- 239000002861 polymer material Substances 0.000 description 5
- 229920001169 thermoplastic Polymers 0.000 description 5
- 239000004416 thermosoftening plastic Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 241000237858 Gastropoda Species 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 229920006037 cross link polymer Polymers 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000010812 mixed waste Substances 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 239000012815 thermoplastic material Substances 0.000 description 2
- 239000004635 Polyester fiberglass Substances 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000010786 composite waste Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B17/0404—Disintegrating plastics, e.g. by milling to powder
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/0026—Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
- B29B17/0042—Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting for shaping parts, e.g. multilayered parts with at least one layer containing regenerated plastic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/06—Recovery or working-up of waste materials of polymers without chemical reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2033/00—Use of polymers of unsaturated acids or derivatives thereof as moulding material
- B29K2033/04—Polymers of esters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2033/00—Use of polymers of unsaturated acids or derivatives thereof as moulding material
- B29K2033/04—Polymers of esters
- B29K2033/12—Polymers of methacrylic acid esters, e.g. PMMA, i.e. polymethylmethacrylate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2055/00—Use of specific polymers obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in a single one of main groups B29K2023/00 - B29K2049/00, e.g. having a vinyl group, as moulding material
- B29K2055/02—ABS polymers, i.e. acrylonitrile-butadiene-styrene polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
- B29K2067/06—Unsaturated polyesters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
- B29K2105/08—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of continuous length, e.g. cords, rovings, mats, fabrics, strands or yarns
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- 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
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Sustainable Development (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
POSTOPEK MEHANSKEGA RECIKLIRANJA KOMPOZITNEGA POLIMERNEGA MATERIALAMECHANICAL RECYCLING PROCEDURE FOR COMPOSITE POLYMER MATERIAL
Predmet izuma je postopek mehanskega recikliranja odpadnega kompozitnega polimernega materiala v izdelke različnih dimenzij. Odpadni kompozitni polimerni material za recikliranje po izumu je sestavljen iz 30 - 40 delov (po masi) nenasičene poliestrske smole ojačene s steklenimi vlakni, 30 - 60 delov delno zamreženega polimetilmetakrilata in 0-70 delov kopolimera akrilonitril-butadien-stiren (ABS). Tovrstni kompozitni material se uporablja za izdelavo nosilnih izdelkov večjih dimenzij, kot so na primer kopalniški elementi, tobogani ali plovila. Recikliranje tovrstnega kompozitnega materiala omejuje težavna ločitev sestavnih komponent in dejstvo, da nenasičena poliestrska smola in delno zamrežen polimetilmetakrilat nista termoplastna materiala, ki bi ju bilo mogoče preoblikovati v obliki taline. Odpadki iz tovrstnih kompozitnih materialov se zato večinoma odlagajo na odlagališčih odpadkov.The subject of the invention is a process of mechanical recycling of waste composite polymer material into products of different dimensions. The waste composite polymer recycling material according to the invention consists of 30-40 parts (by weight) of glass fiber-reinforced polyester resin, 30-60 parts of partially cross-linked polymethylmethacrylate and 0-70 parts of acrylonitrile-butadiene-styrene (ABS) copolymer. This type of composite material is used for the production of large-scale load-bearing products such as bathroom fixtures, slides or vessels. The recycling of this composite material is limited by the difficult separation of constituent components and the fact that unsaturated polyester resin and partially cross-linked polymethylmethacrylate are not thermoplastic materials that can be transformed into melt. Waste from such composite materials is therefore mostly disposed of at landfills.
Obstoječe metode predelave odpadkov kompozitnih polimernih materialov temeljijo na tem, da večinski delež mešanice predstavlja termoplastičen material, ki oblije ostale dele zmesi, ki imajo vlogo polnila. Uveljavljeni postopki uporabljajo abrazijsko odporne ekstruderje, delež termoplasta pa po priporočilih izdelovalcev naprav naj ne bi bil manjši od 70 %. Takšna metodo bi bilo mogoče uporabiti tudi za navedeni kompozitni polimerni material, vendar bi se v tem primeru zaradi dodatka termoplasta (da bi predstavljal okoli 70% končne zmesi) celotna količina materiala močno povečala. Tu opisani izum rešuje tehnični problem recikliranja mešanega polimernega odpadka iz zamreženih polimerov, brez ali z minimalnimi dodatki termoplastov.Existing methods of processing waste composite polymeric materials are based on the fact that the majority of the mixture is a thermoplastic material that wraps other parts of the mixture as fillers. The established procedures use abrasion-resistant extruders and the thermoplastic fraction should not be less than 70%, according to the recommendations of the device manufacturers. Such a method could also be applied to said composite polymer material, but in this case, due to the addition of a thermoplastic (to represent about 70% of the final mixture), the total amount of material would be greatly increased. The invention described herein solves the technical problem of recycling mixed polymer waste from cross-linked polymers, without or with minimal thermoplastic additives.
Objavljeni izumi na področju recikliranja polimernih kompozitov iz zamreženih polimerov temeljijo na metodah depolimerizacije in ponovne uporabe produktov (WO 03/051956 Al), uporabi topil pri povišanih temperaturah (WO 01723463 Al, US 2002/0017162 Al) ali na postopku pirolize (WO 02/088277 Al). Naštete metode zahtevajo velik vložek energije in sodijo v t. im. metode kemijske reciklaže pri katerih je polimer večinoma razgrajen oz. kemijsko obdelan. Mehansko recikliranje kompozitnega odpadka s pretežnim delom poliestrske smoleje opisano v izumu (EP 1 273 627 Al), vendar gre v tem primeru za sestavo materiala, ki se bistveno razlikuje od materiala opisanega v tem izumu. Naloga in cilj izuma, ki je postopek za recikliranje kompozitnega polimernega materiala z nizko vsebnostjo termoplastov, ki bo tehnološko enostavno, energijsko nezahtevno in ekonomično.Published inventions in the field of recycling polymer composites from cross-linked polymers are based on depolymerization and reuse methods (WO 03/051956 Al), use of solvents at elevated temperatures (WO 01723463 Al, US 2002/0017162 Al) or pyrolysis process (WO 02 / 088277 Al). The above methods require a large amount of energy and fall into t. im. chemical recycling methods in which the polymer is mainly degraded or chemically treated. Mechanical recycling of composite waste with a predominantly polyester resin described in the invention (EP 1 273 627 Al), but in this case it is a material composition substantially different from the material described in the present invention. The object and object of the invention is a process for recycling a low-thermoplastic composite polymer material that will be technologically simple, energy-efficient and economical.
Po izumu je naloga rešena s postopkom mehanskega recikliranja odpadnega kompozitnega polimernega materiala po neodvisnem patentnem zahtevku.According to the invention, the problem is solved by a process of mechanical recycling of waste composite polymer material according to an independent claim.
Postopek po izumu temelji na iztiskanju (ekstrudiranje) mletega mešanega odpadka. Zaradi narave materiala mora ekstruder imeti vijak (polž), ki dovoljuje nemoten pretok nestaljenih, omehčanih delcev zdrobljenega materiala. Velikost delcev in s tem oblika polža je odvisna od predpriprave materiala v postopku mletja in/ali sejanja. Ekstruder mora imeti urejeno zunanje gretje, ki dovoljuje doseganje temperatur, pri katerih pride do znižanja viskoznosti (delnega taljenja) poliestra, polimetilmetakrilata in/ali ABS. Uporabljamo lahko estruder z enojnim ali dvojnim polžem, z ali brez možnosti odplinjevanja segrete mase. Pri izvedbi smo uporabljali ekstruder s polžem premera vsaj 25 mm in temperature med 180 in 230 °C.The process according to the invention is based on extrusion of ground mixed waste. Due to the nature of the material, the extruder must have a screw (snail) that permits a smooth flow of non-molten, softened particles of crushed material. The particle size and thus the shape of the snail depend on the pre-preparation of the material during the grinding and / or sieving process. The extruder must have a regulated external heating system that allows temperatures to be reached at which the viscosity (partial melting) of polyester, polymethylmethacrylate and / or ABS is reached. Single or double auger estruder can be used, with or without the possibility of degassing the heated mass. An extruder with a screw diameter of at least 25 mm and temperatures between 180 and 230 ° C was used.
Pred predelavo je material potrebno zmleti do velikosti delcev, ki omogočajo nemoteno uvajanje materiala v ekstruder, kar je odvisno predvsem od načina dovajanja materiala, dovodnih odprtin in premera polža. Za doseganje homogenosti in relativno gladke površine izdelka je material pred predelavo potrebno posušiti do konstantne mase, da ne vsebuje vlage. Delež ABS kopolimera lahko poljubno spreminjamo vendar to vpliva na predelovalne lastnosti materiala. Brez ABS ali z majhnim deležem ABS je omogočeno polnjenje kalupov in ekstrudiranje nezahtevnih oblik, z večanjem deleža ABS pa je možno ekstrudirati bolj zahtevne oblike.Prior to processing, the material must be ground to a particle size that allows the material to be introduced into the extruder without interruption, depending mainly on the method of material feed, inlet openings and the screw diameter. In order to achieve homogeneity and a relatively smooth surface of the product, the material must be dried to a constant mass before being processed so as not to contain moisture. The proportion of ABS copolymer can be varied arbitrarily, but this affects the processing properties of the material. Without ABS or with a small amount of ABS, it is possible to fill the molds and extrude non-demanding shapes, and by increasing the proportion of ABS it is possible to extrude more complex shapes.
Mešani odpadek se pri prehodu skozi ekstruder premeša in pod vplivom toplote zmehča. Omehčani poliester, polimetilmetakrilat in ABS povežejo nestaljene polimerne delce in steklena vlakna, tako da iz naprave prihaja homogena gmota, oblikovana v kontinuimi profil. Oblika profila je odvisna od izbire izhodne šobe, oz. namembnosti izdelka. Izdelek je mogoče oblikovati tudi z uvajanjem omehčane mase v kovinske kalupe različnih dimenzij in oblik. Ohlajeni izdelki imajo trdnosti, ki so primerljive s trdnostmi ivemih plošč. Površinsko in po prerezu so opazni večji delci polimetilmetakrilata, poliestrske smole in vlaken, ki pa so med seboj trdno povezani. Izdelek ne vpija vode in ne nabreka v prisotnosti vlage. Na površino izdelka lahko v postopku kontinuimega izstiskanja z uporabo koekstruzije nanesemo plast polimetilmetakrilata, ki da izdelku brezhibno zunanjo podobo.The mixed waste is mixed in the passage through the extruder and softened under the influence of heat. Softened polyester, polymethylmethacrylate and ABS connect non-molten polymer particles and glass fibers to produce a homogeneous mass formed in a continuous profile from the device. The shape of the profile depends on the choice of the outlet nozzle, respectively. destination of the product. The product can also be shaped by introducing a softened mass into metal molds of various dimensions and shapes. Chilled products have strengths that are comparable to the strengths of ive boards. On the surface and after the cross section, larger particles of polymethylmethacrylate, polyester resin and fibers are observed, but they are strongly interconnected. The product does not absorb water or swell in the presence of moisture. During the continuous extrusion process, a layer of polymethylmethacrylate can be applied to the surface of the product by continuous extrusion, which gives the product a flawless appearance.
Tu opisani izum izboljšuje postopek mehanskega recikliranja polimernega kompozita na osnovi polimetilmetakrilata, ABS, nenasičene poliestrske smole in steklenih vlaken. Glavna prednost opisanega postopka je, da omogoča cenovno sprejemljivo mehansko recikliranje velikih količin mešanega polimernega odpadka, brez ali z minimalno vsebnostjo termoplastov, veziv ali drugih dodatkov, ki bi predelavo podražili in povečali količino predelanega materiala.The invention described herein improves the process of mechanical recycling of a polymer composite based on polymethylmethacrylate, ABS, unsaturated polyester resin and glass fibers. The main advantage of the process described is that it allows for affordable mechanical recycling of large quantities of mixed polymer waste, without or with minimal content of thermoplastics, binders or other additives, which would increase the cost of processing and increase the amount of material recovered.
Izvedbeni primer 1Example 1
Kompozit s sestavo: 50 % polimetilmetakrilat, 30 % nenasičena poliestrska smola in 20 % steklena vlakna, smo zmleli do maksimalne velikosti delcev 11 mm. Dobljeno zmes smo vodili v enovijačni ekstruder s polžem premera 25 mm. Izstiskanje je potekalo pri temperaturi 220 °C. Dobljeni polni profil je bil po ohlajanju kompakten, homogen in trden. Notranjost profila je bila homogena in brez zračnih mehurčkov. Med predelavo ni prišlo do termičnega pregrevanja oziroma nekontroliranega termičnega razpada katerekoli komponente mešanega materiala.Composite Composition: 50% polymethylmethacrylate, 30% unsaturated polyester resin and 20% glass fibers were ground to a maximum particle size of 11 mm. The resulting mixture was run into a single screw extruder with a screw diameter of 25 mm. The extrusion was carried out at 220 ° C. The resulting full profile was compact, homogeneous and solid after cooling. The inside of the profile was homogeneous and free of air bubbles. No thermal overheating or uncontrolled thermal decay of any mixed material component occurred during processing.
Izvedbeni primer 2Example 2
Kompozit s sestavo: 50 % polimetilmetakrilat,, 35 % nenasičena poliestrska smola in 15 % steklena vlakna, smo zmleli do maksimalne velikosti delcev 15 mm. Dobljeno zmes smo vodili v enovijačni ekstruder s polžem premera 60 mm. Izstiskanje je potekalo pri temperaturi 190 °C. Staljeno zmes smo uvajali direktno v kovinski kalup, dokler ta ni bil poln. Uvajanje smo potem prekinili, model zaprli in pustili, da se je ohladil do temeprature približno 50 °C. Model smo potem odprli iz njega odstranili izdelek. Prerez izdelka je pokazal, daje notranjost izdelka homogena.Composite Composition: 50% polymethylmethacrylate, 35% unsaturated polyester resin and 15% glass fibers were ground to a maximum particle size of 15 mm. The resulting mixture was run into a single screw extruder with a 60 mm diameter screw. The extrusion was carried out at 190 ° C. The molten mixture was introduced directly into the metal mold until it was full. The induction was then interrupted, the model closed and allowed to cool to a temperature of about 50 ° C. The model was then opened to remove the product from it. The cross-section of the product showed that the interior of the product was homogeneous.
Izvedbeni primer 3Example 3
Kompozit s sestavo; 50 % polimetilmetakrilat, 10 % akrilonitril-butadien-stiren kopolimer, 25 % nenasičena poliestrska smola in 15 % steklena vlakna, smo zmleli do maksimalne velikosti delcev 15 mm. Dobljeno zmes smo vodili v eno vijačni ekstruder s polžem premera 60 mm. Izstiskanje je potekalo pri temperaturi 190 °C. Dobljena cev s stenami debeline med 5 in 7 mm je bila po ohlajanju kompaktna, homogena in trdna ter brez zračnih mehurčkov.Composite composition; 50% polymethylmethacrylate, 10% acrylonitrile butadiene styrene copolymer, 25% unsaturated polyester resin and 15% glass fibers were ground to a maximum particle size of 15 mm. The resulting mixture was run into a single screw extruder with a 60 mm diameter screw. The extrusion was carried out at 190 ° C. The resulting tube, with walls between 5 and 7 mm thick, was compact, homogeneous and solid after cooling, with no air bubbles.
Izvedbeni primer 4Example 4
Kompozit s sestavo: 33 % polimetilmetakrilat, 40 % akrilonitril-butadien-stiren kopolimer, 17 % nenasičena poliestrska smola in 10 % steklena vlakna, smo zmleli do maksimalne velikosti delcev 15 mm. Dobljeno zmes smo vodili v enovijačni ekstruder s polžem premera 60 mm. Izstiskanje je potekalo pri temperaturi 190 °C. Profil je bil kalibriran. Dobljena palica premera 35 mm je bila po ohlajanju kompaktna, homogena in trdna ter brez zračnih mehurčkov.Composite Composition: 33% polymethylmethacrylate, 40% acrylonitrile butadiene styrene copolymer, 17% unsaturated polyester resin and 10% glass fibers were ground to a maximum particle size of 15 mm. The resulting mixture was run into a single screw extruder with a 60 mm diameter screw. The extrusion was carried out at 190 ° C. Profile was calibrated. The resulting 35 mm diameter rod was compact, homogeneous and solid after cooling, with no air bubbles.
Postopek mehanskega recikliranja odpadnega kompozitnega polimernega materiala iz delno zamreženega polimetilmetakrilata, akrilonitril-butadien-stiren kopolimera, nenasičene poliestrske smole in steklenih vlaken v izdelke različnih dimenzij je torej značilen po tem, da je material pred predelavo zmlet do velikosti delcev, ki je primerna za doziranje v ekstruder, da postopek poteka v napravi za izstiskanje - ekstruderju, ki je ogret na delovno temperaturo med 180 in 230 °C. Material sestavljen iz 30 - 40 delov (po masi) nenasičene poliestrske smole ojačene s steklenimi vlakni, 30-60 delov delno zamreženega polimetilmetakrilata in 0 - 70 delov kopolimera akrilonitril-butadien-stiren (ABS). Ekstruder dovoljuje prehod nestaljenih delcev materiala. Material pred predelavo ne vsebuje vlage oziroma je sušen do konstantne mase. Maso, ki izhaja iz ekstruderja oblikuje v kontinuirni profil različnih oblik, v odvisnosti od izhodne šobe in namembnosti izdelkov. Kontinuime profile se lahko prevleče s plastjo polimetilmetakrilata z uporabo koekstruzije. Maso, ki izhaja iz ekstruderja se lahko oblikuje tudi z uvajanem v kalupe različnih dimenzij in oblik.The process of mechanical recycling of waste composite polymeric material from partially cross-linked polymethylmethacrylate, acrylonitrile-butadiene-styrene copolymer, unsaturated polyester resin and fiberglass into products of different dimensions is characterized in that the material is suitable for grinding to a particle size prior to processing in an extruder, that the process takes place in a extruder - an extruder heated to an operating temperature between 180 and 230 ° C. Material consisting of 30 - 40 parts by weight of unsaturated glass fiber reinforced polyester resin, 30-60 parts of partially crosslinked polymethylmethacrylate and 0 - 70 parts of copolymer of acrylonitrile butadiene styrene (ABS). The extruder permits the passage of loose particles of material. The material does not contain moisture or is dry to constant weight before processing. The mass resulting from the extruder is formed into a continuous profile of different shapes, depending on the outlet nozzle and the intended use of the products. Continuous profiles can be coated with a layer of polymethylmethacrylate using co-extrusion. The mass resulting from the extruder can also be formed by being introduced into molds of various dimensions and shapes.
Postopek po izumu je energijsko in materialno varčen, saj ne zahteva velikega vložka energije ali dodanih materialov. Zaradi tega je izum specifičen in ekonomsko učinkovit.The process according to the invention is energy and material saving since it does not require a large input of energy or added materials. This makes the invention specific and economically efficient.
Zgoraj navedeni izvedbeni primeri izuma ne omejujejo, temveč ga le pojasnjujejo.The foregoing embodiments of the invention do not limit, but merely explain.
Claims (6)
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SI200300232A SI21606A (en) | 2003-09-12 | 2003-09-12 | Mechanical recycling procedure for composite polymeric material |
PCT/SI2004/000026 WO2005026244A1 (en) | 2003-09-12 | 2004-08-18 | Process for mechanical recycling of composite polymeric material |
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FR2964588B1 (en) * | 2010-09-10 | 2012-10-12 | Fi Process | METHOD FOR RECYCLING MIXED PLASTIC WASTE AND PRODUCT OBTAINED THEREBY |
EP4019576A1 (en) | 2020-12-28 | 2022-06-29 | Trinseo Europe GmbH | Recycling method for elastomer toughened thermoplastic polymers |
BR102021025568B1 (en) * | 2021-12-17 | 2023-01-17 | Senai/Cetiqt - Serviço Nacional De Aprendizagem Industrial-Centro De Tecnologia Da Indústria Química E Têxtil | PROCESS OF REUSE OF SYNTHETIC TEXTILE WASTE TO OBTAIN CONTINUOUS YARN |
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US5876644A (en) * | 1996-08-27 | 1999-03-02 | Wellman, Inc. | Food quality polyester recycling |
CA2256614A1 (en) * | 1998-03-16 | 1999-09-16 | Collins & Aikman Products Co. | An improved process of recycling waste polymeric material and an article utilizing the same |
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