KR100455803B1 - Products manufacturing process for recycling waste plastics - Google Patents
Products manufacturing process for recycling waste plastics Download PDFInfo
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- KR100455803B1 KR100455803B1 KR10-2001-0058495A KR20010058495A KR100455803B1 KR 100455803 B1 KR100455803 B1 KR 100455803B1 KR 20010058495 A KR20010058495 A KR 20010058495A KR 100455803 B1 KR100455803 B1 KR 100455803B1
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- waste plastic
- waste
- extruder
- waste plastics
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- 239000002699 waste material Substances 0.000 title claims abstract description 70
- 229920003023 plastic Polymers 0.000 title claims abstract description 64
- 239000004033 plastic Substances 0.000 title claims abstract description 64
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 8
- 238000004064 recycling Methods 0.000 title abstract description 5
- 239000004200 microcrystalline wax Substances 0.000 claims abstract description 25
- 239000011230 binding agent Substances 0.000 claims abstract description 24
- 238000002156 mixing Methods 0.000 claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 15
- 238000002844 melting Methods 0.000 claims abstract description 14
- 230000008018 melting Effects 0.000 claims abstract description 14
- 239000011256 inorganic filler Substances 0.000 claims abstract description 11
- 229910003475 inorganic filler Inorganic materials 0.000 claims abstract description 11
- 238000010137 moulding (plastic) Methods 0.000 claims abstract description 10
- 229910002012 Aerosil® Inorganic materials 0.000 claims abstract description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000010445 mica Substances 0.000 claims abstract description 9
- 229910052618 mica group Inorganic materials 0.000 claims abstract description 9
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 8
- -1 galvanized Chemical compound 0.000 claims abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000010439 graphite Substances 0.000 claims abstract description 6
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 6
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 claims abstract description 5
- 239000010459 dolomite Substances 0.000 claims abstract description 5
- 229910000514 dolomite Inorganic materials 0.000 claims abstract description 5
- 229920005989 resin Polymers 0.000 claims abstract description 5
- 239000011347 resin Substances 0.000 claims abstract description 5
- 229920001187 thermosetting polymer Polymers 0.000 claims abstract description 5
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims abstract description 5
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 claims abstract description 4
- 239000010433 feldspar Substances 0.000 claims abstract description 4
- 239000010436 fluorite Substances 0.000 claims abstract description 4
- 125000001905 inorganic group Chemical group 0.000 claims abstract description 4
- 229920005992 thermoplastic resin Polymers 0.000 claims abstract description 4
- 239000010954 inorganic particle Substances 0.000 claims abstract description 3
- 239000012258 stirred mixture Substances 0.000 claims abstract 2
- 238000000465 moulding Methods 0.000 claims description 16
- 239000000945 filler Substances 0.000 claims description 14
- 239000002216 antistatic agent Substances 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 7
- 238000001125 extrusion Methods 0.000 abstract description 9
- 239000004575 stone Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 10
- 239000002245 particle Substances 0.000 description 7
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 3
- 239000000440 bentonite Substances 0.000 description 3
- 229910000278 bentonite Inorganic materials 0.000 description 3
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229920003002 synthetic resin Polymers 0.000 description 3
- 239000000057 synthetic resin Substances 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- 239000001856 Ethyl cellulose Substances 0.000 description 2
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910001570 bauxite Inorganic materials 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003822 epoxy resin Substances 0.000 description 2
- 229920001249 ethyl cellulose Polymers 0.000 description 2
- 235000019325 ethyl cellulose Nutrition 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 239000010450 olivine Substances 0.000 description 2
- 229910052609 olivine Inorganic materials 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 229920000647 polyepoxide Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 229920006324 polyoxymethylene Polymers 0.000 description 2
- 229920002689 polyvinyl acetate Polymers 0.000 description 2
- 239000011118 polyvinyl acetate Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000001993 wax Substances 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- 239000004640 Melamine resin Substances 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 229930182556 Polyacetal Natural products 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 241000907903 Shorea Species 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000009415 formwork Methods 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 239000002023 wood Substances 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
- 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
- B29C48/022—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
-
- 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
- B29K2101/00—Use of unspecified macromolecular compounds as moulding material
- B29K2101/10—Thermosetting resins
-
- 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
- B29K2101/00—Use of unspecified macromolecular compounds as moulding material
- B29K2101/12—Thermoplastic materials
-
- 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
- B29K2509/00—Use of inorganic materials not provided for in groups B29K2503/00 - B29K2507/00, as filler
-
- 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)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
본 발명은 각기 상이한 성질을 가지고 있는 각종 폐플라스틱을 선별없이 혼합하여 표면이 매끄럽고 기계적 경도 및 강도가 우수한 폐플라스틱 성형물을 압출성형할 수 있도록 한 폐플라스틱 재활용을 위한 폐플라스틱 성형물의 제조방법에 관한 것으로, 성질이 다를 각종 폐플라스틱과, 무기질 입자를 혼합하고 이를 압출기에 투입하여 용융시키면서 압출하여 폐플라스틱 성형물을 제조하는 것에 있어서, 열가소성수지 및 열경화성수지로 구성되는 각종 폐플라스틱은 80∼85 중량%이고, 사문석·납석·감란석·불석·마이카(운모)·흑연· 돌로마이트로 구성되는 무기질그룹으로부터 선택된 2종 이상으로 된 무기질 충진제는 5∼10 중량%이며, 여기에 결합제인 마이크로왁스 3∼5 중량% 및 나머지 잔량으로서 에어로실, 아연화, 산화티탄, 벤톤으로 구성되는 기타 결합제를 포함하여 상기 각 조성물들이 100%(중량)이 되게 혼합시킨 상태에서 900∼1000rpm으로 고속회전으로 10여분 동안 교반한 다음, 교반된 혼합물을 압출기에 투입하여 180∼280℃의 온도범위에서 용융시키면서 압출하여 피성형물을 제조하는 것을 특징으로 하는 발명이다.The present invention relates to a method for producing waste plastic molding for recycling waste plastic, which allows extrusion plastic molding of waste plastic molding having a smooth surface and excellent mechanical hardness and strength by mixing various waste plastics having different properties without selection. In the manufacture of waste plastic moldings by mixing various kinds of waste plastics having different properties and inorganic particles, and putting them in an extruder and melting them, the waste plastics composed of thermoplastic resins and thermosetting resins are 80 to 85% by weight. 5-10 wt% of inorganic fillers selected from the inorganic group consisting of serpentine, feldspar, perennial stone, fluorite, mica (mica), graphite, and dolomite, with 3 to 5 weight of binder microwax Consisting of aerosil, galvanized, titanium oxide, benton as% and remaining balance Each composition including the other binder was stirred at a high speed rotation at 900 to 1000 rpm for 10 minutes while mixing the composition to 100% (weight), and then the stirred mixture was introduced into an extruder at a temperature range of 180 to 280 ° C. The invention is characterized by producing an object by extruding while melting.
Description
본 발명은 각기 상이한 성질을 가지고 있는 각종 폐플라스틱을 선별없이 혼합하여 표면이 매끄럽고 기계적 경도 및 강도가 우수한 폐플라스틱 성형물을 압출성형할 수 있도록 한 폐플라스틱 재활용을 위한 폐플라스틱 성형물의 제조방법에 관한 것이다.The present invention relates to a method for producing waste plastic molding for waste plastic recycling, which allows extrusion of a waste plastic molding having a smooth surface and excellent mechanical hardness and strength by mixing various waste plastics having different properties without selection. .
산업기술이 날로 발전함과 더불어 플라스틱이 사용된 제품이 많아지고 있으며, 이에 따라 사용수명이 다한 플라스틱 제품에 의해 발생되고 있는 폐플라스틱을 재활용하기 위한 여러 방안들이 제안되고 있다.As industrial technology develops day by day, many products using plastics are increasing. Accordingly, various methods for recycling waste plastics generated by plastic products having reached the end of their service life have been proposed.
그런데, 플라스틱은 그 성분 및 성질이 같은 것끼리는 융합이 잘이루어지지만 성분이 다르면 융합이 않되는 성질을 가지고 있다.By the way, plastic has the property that the components and properties of the same fusion is well done, but if the components are different, the fusion is not.
또한 폐플라스틱을 재활용하기 위해서는 같은 원료의 성분 및 색상에 따라 종류별로 분리수거하고 또 깨끗하게 세척한 후에 처리해야만 재활용이 가능하였다.In addition, in order to recycle the waste plastics, the waste plastics can be recycled only after they have been collected and sorted according to the type and color of the same raw material.
따라서 각종 폐합성수지를 종류별로 분리하지 않고 재활용할 수 있는 기술로서 국내 등록특허공보에 특허 제 227305 호로 게재되어 있다.Therefore, as a technology that can be recycled without separating the various waste synthetic resins by type, it is published as a patent No. 227305 in the domestic registered patent.
위 특허는 각종 성분 폐합성수지를 종류별로 선별하지 않고 또한 각 성분들의 혼합비에 관계없이 혼합이 이루어질 수 있도록 하는 방법이 제안되고 있지만, 위 특허의 청구범위에 기재된 발명의 내용에서 보듯이 성분이 다른 폐합성수지액들이 100-200 메쉬로 미분쇄된 활석에 의하여 결합시키는 구성임을 알 수 있다.Although the above patent proposes a method of mixing various component waste synthetic resins by type and irrespective of the mixing ratio of the respective components, it is proposed that the wastes having different components as shown in the contents of the invention described in the claims of the above patent. It can be seen that the synthetic resin liquids are bonded by talc pulverized into 100-200 mesh.
그러나 위 특허는 무기질의 활석입자에 용융된 수지액이 사방에서 달라붙게 하여 작용으로 성질이 다른 수지용액을 결합시키는 매개체 역활만을 하고 있기 때문에 압출성형된 성형물의 표면이 거칠고 강도면에서도 미흡하다는 것이 단점으로 지적되고 있다.However, the above patent only plays the role of a medium that binds the melted resin solution to inorganic talc particles from all directions and binds the resin solution with different properties, so that the surface of the extruded molding is rough and has insufficient strength. It is pointed out.
본 발명은 상기와 같은 종래 기술에서 나타나는 제반 사항을 감안하여 제안한 것으로, 용융점 및 성질이 각기 다른 여러 종류의 열가소성 및 열경화성 폐플라스틱들을 선별공정이나 세척공정없이 혼합 및 용융시켜서 압출성형하는 공정으로 표면이 매끄럽고 강도가 우수한 폐플라스틱 재활용 성형물을 제조할 수 있도록 하는데 목적을 두고 발명한 것이다.The present invention has been proposed in view of the above-mentioned general matters. The surface of the thermoplastic resin and thermosetting waste plastics having different melting points and properties is extruded by mixing and melting without sorting or washing. The invention was invented for the purpose of producing a smooth, high strength waste plastic recycled molding.
이를 위한 본 발명의 기술적 수단은,Technical means of the present invention for this purpose,
성질이 다른 각종 폐플라스틱과, 무기질 입자를 혼합하고 이를 압출기에 투입하여 용융시키면서 압출하여 폐플라스틱 성형물을 제조하는 것에 있어서,In the manufacture of waste plastic moldings by mixing various waste plastics having different properties and inorganic particles and injecting them into an extruder and melting them,
열가소성수지 및 열경화성수지로 구성되는 각종 폐플라스틱은 80∼85 중량%이고, 사문석(serpentine)·납석(pyrophylite)·감란석(olivines)·불석(alumino)·마이카(mica: 운모)·흑연(graphite)·복사이트(bauxite)·돌로마이트(dolomite)·몬모릴로나이트(montmorllonite)로 구성되는 무기질그룹으로부터 선택된 2종 이상으로 된 무기질 충진제는 5∼10 중량%이며, 여기에 결합제인 마이크로왁스(microwax)를 3∼5 중량% 포함하여 혼합시킨 상태에서 900∼1000rpm으로 고속회전으로 10여분 동안 교반한 다음, 교반된 혼합물을 압출기에 투입하여 180∼280℃의 온도범위에서 용융시키면서 압출하여 피성형물을 제조하는 것을 특징으로 하는 것이다.The waste plastics composed of thermoplastic resins and thermosetting resins are 80 to 85% by weight, and serpentine, pyrophylite, olivines, aluminium, mica and mica are graphite. 5-10% by weight of an inorganic filler selected from the inorganic group consisting of bauxite, dolomite and montmorllonite, and the binder microwax is 3%. After stirring for about 10 minutes at a high speed rotation at 900 ~ 1000rpm in a mixed state containing ~ 5% by weight, the mixture is put into an extruder and extruded while melting at a temperature range of 180 ~ 280 ℃ to prepare a molding It is characterized by.
그리고, 상기 결합제는 마이크로왁스(microwax) 3∼5 중량%에다 에어로실(aerosil), 아연화(zno), 산화티탄(TiO2), 벤톤(bentonite) 각 성분들을 총 10 중량%의 범위내에서 혼합하는 것을 특징으로 하는 것이며,In addition, the binder is 3 to 5% by weight of the microwax (microwax) and aerosil (azero), zinc (zno), titanium oxide (TiO 2 ), Benton (bentonite) each of the components in a range of 10% by weight in total It is characterized by
또한 상기 폐플라스틱, 결합제 및 충진제를 혼합시킨 상태로 압출기에 투입할 때 상기 혼합물의 전체 중량에 대하여 대전방지제를 0.2∼0.3 중량% 추가하여 압출기에 투입하여 피성형물을 제조하는 것을 특징으로 하는 것이다.In addition, when added to the extruder in a state in which the waste plastic, binder and filler are mixed, an antistatic agent is added 0.2 to 0.3% by weight based on the total weight of the mixture, characterized in that the injection molding machine to produce a to-be-molded product.
본 발명의 바람직한 실시예를 이하에서 설명하기로 한다.Preferred embodiments of the present invention will be described below.
본 발명은 폐기처리되는 폐플라스틱을 주원료로 하며, 무기질로 구성되는 충진제를 보조원료로 하고, 여기에 겹합제인 마이크로왁스(microwax)를 소량 첨가하여 혼합하는 것을 특징으로 하고 있으며, 또한 상기 결합제로서는 마이크로왁스 3∼5 중량%에다 에어로실(aerosil), 아연화(ZnO), 산화티탄(TiO2), 및 벤톤(bentonite) 등의 성분들을 총 10 중량% 범위에서 혼합하거나 또는 극소량의대전방지제를 추가하여 혼합하여 폐플라스틱 재활용 성형물을 압출성형하는 것을 특징으로 한다.The present invention is characterized in that the waste plastic to be disposed of is used as a main raw material, and a filler made of inorganic matter is used as an auxiliary raw material, and a small amount of microwax, which is a superposition agent, is added thereto and mixed. 3 to 5% by weight of microwax plus 10% by weight of components such as aerosil, zinc (ZnO), titanium oxide (TiO 2 ) and bentonite, or a very small amount of antistatic agent By mixing to extrude the waste plastic recycled molding.
본 발명에서 사용되는 폐플라스틱은 폴리염화비닐(PVC), 폴리스틸렌(PS), ABS수지, 폴리아세탈(POM), 폴리에틸렌(PE), 폴리아미드(PA), 나일론(NAL), 나일론섬유, 폴리프로필렌(PP), 아크릴, 폴리카아보네이트(PC), 폴리에텔렌테레프탈레이트(PETP), 초산셀롤로오스(CA), 에틸셀롤로오스(EC), 폴리초산비닐(PVAC) 등 열가소성 폐플라스틱과; 멜라민수지(MF), 페놀수지(PF), 우레아수지(PUR), 에폭시수지(EP), 폴리디아릴프탈레이트(PVAE) 등 열경화성 폐플라스틱이 사용되며, 이들 각 폐플라스틱은 수명이 다하여 폐기처리되는 순수 플라스틱 제품은 물론이고 금속, 지류, 목재 등 플라스틱이 아닌 재료와 함께 혼용되어 제조된 모든 제품으로부터 얻어지는 폐플라스틱을 전부 포함한다.Waste plastics used in the present invention are polyvinyl chloride (PVC), polystyrene (PS), ABS resin, polyacetal (POM), polyethylene (PE), polyamide (PA), nylon (NAL), nylon fibers, polypropylene Thermoplastic waste plastics such as (PP), acrylic, polycarbonate (PC), polyethylene terephthalate (PETP), cellulose acetate (CA), ethyl cellulose (EC), and polyvinyl acetate (PVAC); ; Thermosetting waste plastics such as melamine resin (MF), phenol resin (PF), urea resin (PUR), epoxy resin (EP), polydiaryl phthalate (PVAE), etc. are used. Pure plastic products, as well as all waste plastics obtained from all products manufactured by mixing with non-plastic materials such as metals, feeders, wood, etc.
또한 상기 폐플라스틱은 각 제품의 폐기처리시 얻어지는 상태 그대로를 취하여 일정 크기 즉, 크기는 5∼15mm, 두께는 1∼3mm 정도로 작게 분쇄하여 사용한다.In addition, the waste plastics are taken as they are obtained during the disposal of each product, and used to be crushed to a predetermined size, that is, 5 to 15 mm in size and 1 to 3 mm in thickness.
상기 폐플라스틱의 사용량은 피성형물의 전체 중량에 대하여 80∼85 중량% 범위로 혼합하는 것이며, 폐플라스틱이 85 중량% 이상일 경우에는 피성형물에 뒤틀림 현상 등의 변형이 생기게 되어 안정성에 문제가 발생될 수 있으며, 폐플라스틱이 80 중량% 이하일 경우에는 피성형물의 경도 및 강도와 같은 기계적인 성질이 저하되는 문제점이 발생될 수 있다.The used amount of the waste plastic is mixed in the range of 80 to 85% by weight with respect to the total weight of the molding, and when the waste plastic is more than 85% by weight, deformation of the molded product may occur, such as distortion, which may cause stability problems. When the waste plastic is 80 wt% or less, a problem may occur such that mechanical properties such as hardness and strength of the molding are lowered.
또한 폐플라스틱과 함께 마이크로왁스와 흑연(graphite)을 첨가하여 피성형물의 표면광택을 유지하고 내산성, 내식성 및 기계적 강도를 보완했다.In addition, microwax and graphite were added together with the waste plastic to maintain the surface gloss of the molding and complement the acid resistance, corrosion resistance and mechanical strength.
본 발명에서 사용되는 충진제는 사문석·납석·감람석·불석·마이카(운모)·흑연·복사이트(bauxite)·돌로마이트(dolomite)·몬모릴로나이트(montmorllonite)로 구성되는 무기질그룹으로부터 선택된 2종 이상을 혼합하는 것이며, 무기질 충진제는 서로 다른 성질을 가진 여러 종류의 폐플라스틱이 용융 및 혼합되는 과정에서 균일하게 분포된 상태하에서 피성형물이 압출성형되게 하므로서 피성형물의 기계적인 성질 즉, 경도 및 강도 등이 우수한 성질을 갖게 하는 역활을 담당하는 것으로, 상기 무기질 충진제의 사용량은 피성형물의 전체 중량에 대하여 5∼10% 이내의 범위이며, 또한 상기 무기질 충진제는 300∼350 메쉬로 미분쇄된 것을 사용하는 것이 바람직한데, 이는 무기질 충진제가 미분쇄된 것일수록 폐플라스틱 용융액에 고르게 분산된 상태로 혼합될 수 있기 때문이다.The filler used in the present invention is a mixture of two or more selected from an inorganic group consisting of serpentine, feldspar, olivine, fluorite, mica, mica, graphite, bauxite, dolomite, and montmorllonite. Inorganic fillers are excellent in mechanical properties, that is, hardness and strength, etc., as the moldings are extruded in a uniformly distributed state in the process of melting and mixing various kinds of waste plastics having different properties. In this role, the amount of the inorganic filler is in the range of 5 to 10% based on the total weight of the molding, and the inorganic filler is preferably pulverized to 300 to 350 mesh. This means that the more finely ground the inorganic filler is, the more uniformly it can be mixed in the waste plastic melt. Because.
본 발명의 특징은 폐플라스틱 80∼85 중량%와 충진제 5∼10 중량%에다 결합제인 마이크로왁스를 3∼5 중량%를 포함하여 혼합한 것에 있으며, 또한 상기 폐플라스틱과 충진제 및 결합제인 마이크로왁스를 900∼1000rpm으로 고속회전시켜 교반한 다음 180∼280℃의 온도로 가열하여 용융시키면서 피성형물을 압출성형하는 것에 있다.The present invention is characterized by mixing 80 to 85% by weight of waste plastics and 5 to 10% by weight of a filler, including 3 to 5% by weight of a microwax as a binder, and further comprising the waste wax and microwax as a filler and a binder. After rotating at high speed at 900 to 1000 rpm and stirring, heating and heating to a temperature of 180 to 280 ° C. to melt the object to be extruded.
상기 폐플라스틱은 앞에서 설명한 바와 같이 입자의 크기가 5∼15mm 정도로 작고 두께는 1∼3mm 정도로 얇게 분쇄된 상태로 혼합되는 것이며, 무기질 충진제는 앞에서 설명한 바와 같이 325 메쉬로 미분쇄된 것이고, 결합제인 마이크로왁스는 분말화된 것이 사용된다.The waste plastic is mixed in a state where the particle size is as small as 5 to 15 mm and thin as 1 to 3 mm as described above, and the inorganic filler is finely ground to 325 mesh as described above, and the binder is micro The wax is used powdered.
상기 결합제인 마이크로왁스는 액상으로 용융되었을시 접착성이 매우 강하여어떠한 물질에 일단 접착되면 탈락되지 아니하는 성질을 가지고 있으므로 각종 폐플라스틱과 함께 열을 가하여 액상으로 용융시키게 되면 성질이 다른 2종 이상의 폐플라스틱 용액과 용액을 결합시키는 가교제의 역활을 담당하는 것이다.The binder microwax is very strong adhesive when melted in the liquid phase has a property that once adhered to any material does not fall off, so when melted in the liquid phase by applying heat with various waste plastics two or more wastes of different properties It is responsible for the role of the crosslinking agent to bond the plastic solution and the solution.
또한 상기 마이크로왁스는 폐플라스틱 용액과 미분쇄된 충진제 입자와의 결합력을 높여주는 역활도 담당하게 된다.In addition, the microwax also plays a role of enhancing the binding force between the waste plastic solution and the finely divided filler particles.
그리고 폐플라스틱과 충진제 및 마이크로왁스의 혼합은 믹서기(반버리믹서)가 사용되며, 그 혼합은 900∼1000rpm의 고속회전으로 교반혼합시키는데, 이와 같이 믹서기를 고속회전시키게 되면 크기가 비교적 큰 폐플라스틱 입자들은 더 작게 절단 또는 분쇄되면서 미분상의 충진제 및 분말상으로 된 마이크로왁스와의 혼합이 잘이루어지게 된다.And the mixing of waste plastic, filler and microwax is used a blender (Banbury mixer), the mixing is agitated mixing at a high speed of 900 ~ 1000rpm. As they are cut or pulverized smaller, they become well mixed with finely divided fillers and powdered microwaxes.
상기에서 폐플라스틱 입자와 미분상의 충진제 및 결합제인 마이크로왁스를 900∼1000rpm의 고속회전으로 혼합시키는데 필요한 시간은 대략 10여분 정도가 소요된다.In the above, the time required for mixing the waste plastic particles with the fine powder filler and the microwax of the binder at a high speed of 900 to 1000 rpm is about 10 minutes.
상기와 같이 믹서기에 의해 혼합된 혼합물은 일축 또는 이축 압출기에 투입하여 180∼280℃의 고온의 조건으로 용융시키면서 압출금형을 통해 피성형물을 압출성형하는 것인데, 용융온도를 180℃ 이하로 하게 되면 그 보다 융점이 높은 폐플라스틱은 알갱이 상태로 남아있게 되어 피성형물의 물성에 나쁜 영향을 미치게 되며, 280℃ 이상으로 용융시킬 경우에는 전기에너지가 불필요하게 소모되어 경제성이 떨어진다.The mixture mixed by the mixer as described above is injected into a single screw or twin screw extruder and melted under high temperature conditions of 180 to 280 ° C. while extruding the molding through an extrusion mold. When the melting temperature is 180 ° C. or lower, Waste plastics having a higher melting point remain in the granular state, which adversely affects the physical properties of the moldings, and when melted at 280 ° C. or higher, electrical energy is unnecessarily consumed and economic efficiency is low.
따라서 혼합물은 180∼280℃의 온도범위로 가열하여 용해시키는 것이 바람직하다. 그 이유는 플라스틱은 성분에 따라 융점이 제각기 다르기 때문인데, 통상 융점이 낮은 폐플라스틱은 180℃에서부터 용해되고 융점이 높은 폐플라스틱은 280℃의 온도에서 완전 용해되므로 각종 폐플라스틱의 성분을 고려하여 180∼280℃의 온도범위에서 모든 폐플라스틱을 완전 용해시킬 수 있는 온도로 가열하여 용해시키는 것이며, 또한 일축 및 이축 압출기는 용해되는 혼합물을 혼합시키면서 압출하게 되므로 이 과정에서 용해된 혼합물은 더욱 고르게 교반 및 혼합되면서 압출금형을 통해 피성형물로 압출성형되는 것이다.Therefore, the mixture is preferably dissolved by heating to a temperature range of 180 ~ 280 ℃. The reason for this is that plastics have different melting points depending on their components. Generally, waste plastics with low melting point are melted at 180 ° C and waste plastics with high melting point are completely dissolved at a temperature of 280 ° C. In the temperature range of 280 ° C, all waste plastics are melted by heating to a temperature at which they can be completely dissolved. In addition, the single- and twin-screw extruders are extruded while mixing the dissolving mixture. As it is mixed, it is extruded into an object through an extrusion mold.
한편, 상기 결합제인 마이크로왁스는 그 혼합비가 피성형물의 전체 중량에 비하여 3∼5 중량%로 소량이지만 각종 폐플라스틱 용액 및 무기질인 충진제의 미분입자와 고르게 분산 혼합되어 성질이 다른 폐플라스틱 용액과 용액 그리고 충진제의 미분입자들을 강력하게 결합시키는 가교제 역활을 담당하게 되므로서 압출성형된 피성형물은 기계적인 경도 및 강도가 우수한 상태가 되며, 또한 마이크로왁스의 가교성에 의해 피성형물의 표면이 매끄러운 상태가 된다.On the other hand, the microwax of the binder is a small amount of 3 to 5% by weight compared to the total weight of the molding, but evenly dispersed and mixed with finely divided particles of various waste plastic solutions and inorganic fillers, the waste plastic solution and solution of different properties In addition, the extruded molded article is in a state of excellent mechanical hardness and strength as it plays a role of a crosslinking agent that strongly binds fine particles of the filler, and the surface of the molded article is smoothed by the crosslinkability of microwax. .
상기에서 무기질인 충진제가 5 중량% 미만으로 혼합될 경우에는 성질이 다른 폐플라스틱들 각각의 수축계수를 제어하지 못하게 되어 피성형물의 압출성형시 뒤틀림 등의 변형이 발생될 수 있으며, 10 중량% 이상으로 혼합된 경우에는 피성형물의 압출성형 후 기계적 성질인 경도 및 강도를 저하시키게 될 우려가 있다. 따라서 상기 무기질 충진제는 5∼10 중량%의 범위에서 혼합하는 것이 바람직하다.When the inorganic filler is mixed at less than 5% by weight, it is impossible to control the shrinkage coefficient of each of the waste plastics having different properties, so that deformation, such as distortion, may occur during extrusion of the molded product. In the case of mixing, the hardness and strength, which are mechanical properties, may be lowered after extrusion of the molding. Therefore, the inorganic filler is preferably mixed in the range of 5 to 10% by weight.
다음, 결합제로서 마이크로왁스(microwax) 이외의 결합제인 결합제인 에어로실(aerosil), 아연화(Zno), 산화티탄(TiO2), 벤톤(bentonite) 등 성분은 마이크로왁스와 함께 혼합물의 전체 중량에 대하여 총 10 중량%의 범위내에서 혼합되는 것이며, 각 성분의 결합제들은 마이크로왁스와 함께 피성형물의 결합력을 증대시키는 작용을 한다.Next, as a binder, components such as aerosil, zinc oxide (Zno), titanium oxide (TiO 2 ), bentonite, etc., which are binders other than microwax, are used together with the microwax to the total weight of the mixture. It is mixed in the range of 10% by weight in total, and the binders of each component serve to increase the binding strength of the molding together with the microwax.
상기 결합제 성분 중에서 에어로실은 1미크론 정도로 미분화된 분말이 사용되며, 이와 같이 에어로실 입자는 아주 미세하기 때문에 비표면적이 매우 크다. 또한 에어로실 입자는 규소(Si)와 산소(O) 원자가 결합된 구조로 되어 있고 굴절율은 1.45∼1.55 범위로서 폐플라스틱와 마이크로왁스가 용해되었을 때 그들의 분산효과를 촉진시키는 작용을 하게 되어 폐플라스틱 용액과 마이크로왁스 용액의 분산작용을 촉진시켜 고르게 혼합시키는 역활을 담당한다. 따라서 결합제인 마이크로왁스의 가교결합력이 증대된다.Among the binder components, aerosil is used as a micronized powder on the order of 1 micron. As the aerosil particles are very fine, the specific surface area is very large. In addition, the aerosil particles have a structure in which silicon (Si) and oxygen (O) atoms are combined and have a refractive index in the range of 1.45 to 1.55, which promotes their dispersing effect when the waste plastic and microwax are dissolved. It is responsible for promoting uniform dispersion by dispersing the microwax solution. Therefore, the crosslinking force of the binder microwax is increased.
상기 결합제 성분 중에서 아연화, 산화티탄, 벤톤 각각은 점결성을 가지고 있으므로 마이크로왁스와 함께 폐플라스틱 용액과의 가교결합력을 증대시키는 작용을 한다. 또한 상기한 결합제 성분들 중에서 아연화 및 산화티탄은 자외선을 차단하는 효과를 가지고 있다.Among the binder components, zinc, titanium oxide, and benton each have a caking property, and thus act to increase the crosslinking force with the waste plastic solution together with the microwax. In addition, zinc oxide and titanium oxide among the above binder components have the effect of blocking ultraviolet rays.
한편, 상기 충진제 성분으로서 극소량의 대전방지제를 추가하여 피성형물을 압출성형할 수 있으며, 이때 대전방지제의 투입시기는 믹서기에서 혼합된 혼합물을 압출기에 투입할 때 함께 투입되는 것이며, 또한 대전방지제의 투입량은 압출기로 투입되는 혼합물의 전체 중량(100%)에 대하여 0.2∼0.3 중량%를 추가적으로 투입하는 것이다.On the other hand, by adding a very small amount of the antistatic agent as the filler component, the molding can be extruded, wherein the timing of the antistatic agent is added together when the mixture is mixed in the mixer into the extruder, and the amount of antistatic agent Is added to 0.2 to 0.3% by weight based on the total weight (100%) of the mixture introduced into the extruder.
상기와 같이 압출기에 투입되는 혼합물에 추가적으로 투입되는 대전방지제는 압출기 내에서 혼합물과 함께 이송 및 용융되는 과정에서 혼합되는 것이며, 이와 같이 혼합물과 함께 압출기에 투입된 대전방지제는 폐플라스틱이 압출기 내에서 용융될 때 발생되는 폭발성가스를 소멸시키는 작용을 담당하여 가스에 의해 피성형물의 표면에 기포가 생기는 것을 방지하므로서 압출성형된 피성형물의 표면을 매끄럽게 하는 효과와 함께 피성형물에서 정전기가 발생되지 않게 하는 효과를 나타낸다.As described above, the antistatic agent added to the mixture introduced into the extruder is mixed in the process of being transported and melted together with the mixture in the extruder. Thus, the antistatic agent introduced into the extruder together with the mixture may cause the waste plastic to melt in the extruder. It has the effect of dissipating explosive gas generated at the time, and prevents bubbles from forming on the surface of the object by the gas, thereby smoothing the surface of the extruded object and preventing static electricity from being produced. Indicates.
이상과 같은 본 발명으로 폐플라스틱 평판(plate)를 제조하는 실시예는 다음과 같다.Embodiments for producing a waste plastic plate (plate) in the present invention as described above are as follows.
실시예 1 내지 6은 하기 [표 1]에 기재된 총 19종의 폐플라스틱 중에서 선택적으로 혼합되는 것을 실시예로 하고 있으며, 이때의 폐플라스틱 혼합비는 80∼85 중량%의 범위내이고 Kg단위로 하여 혼합하여 실시한 것이며, 또 결합제로서 마이크로왁스는 3∼5 중량% 범위내이며, 그외의 결합제인 에어로실, 아연화, 산화티탄, 벤톤 각각은 마이크로왁스와 함께 10 중량% 범위내에서 Kg단위로 혼합한 것이며, 또 충진제로서 사문석, 납석, 불석, 감람석, 마이카(운모), 흑연, 복사이트, 돌로마이트, 몬ㅁㅎ랄로나이트 등 성분은 적어도 2종 이상의 성분이 5∼10 중량% 범위내에서 Kg단위로 혼합되는 것이고, 대전방지제는 한국의 유진테크사(상호)에서 제조된 YT-AS 2000(상품명)을 0.2∼0.3 중량% 범위내에서 Kg단위로 추가하여 압출기에 투입한 것을 실시예로 하고 있으며, 각 실시예에 따른 압출성형온도는 180∼280℃의 범위내에서 실시한 것이다.Examples 1 to 6 are examples of selectively mixing among a total of 19 waste plastics listed in Table 1 below, wherein the waste plastic mixing ratio is in the range of 80 to 85% by weight and is in Kg units. As a binder, microwax is in the range of 3 to 5% by weight, and other binders, aerosil, zincated, titanium oxide, and benton, are each mixed with microwax in the range of 10% by weight in Kg units. In addition, as a filler, components such as serpentine, feldspar, fluorite, olivine, mica, graphite, voxite, dolomite, and mondhalonite are contained in Kg units within 5 to 10% by weight of at least two components. The antistatic agent is added to the extruder by adding YT-AS 2000 (trade name) manufactured by Eugene Tech Co., Ltd. (trade name) in the range of 0.2 to 0.3% by weight in Kg units, bracket Extrusion molding temperature according to the embodiment is carried out in the range of 180 ~ 280 ℃.
상기 [표 1]과 같이 여러 종류의 폐플라스틱과 결합제 및 충진제를 혼합시킨 상태에서 압출기로서 폭 10cm, 두께 15mm 의 평판(plate)을 압출성형하면서 약 15℃의 냉각수로 냉각하였을 때 피성형물의 표면이 균일하고 매끄럽게 압출성형된 것을 육안으로 확인할 수 있었으며, 이와 같이 압출성형된 피성형물을 기계적인 성질인 경도 및 각종 강도시험을 통해 측정한 물성치 결과를 하기 [표 2]에 나타내었다.As shown in [Table 1], when the various types of waste plastics, the binder and the filler are mixed, the surface of the molded object is cooled by cooling water of about 15 ° C. while extruded a plate having a width of 10 cm and a thickness of 15 mm as an extruder. This homogeneous and smooth extrusion was visually confirmed that the physical properties of the extruded molded product measured by the hardness and various strength tests of the mechanical properties are shown in Table 2 below.
상기 [표 2]에서 보듯이 본 발명으로 제조된 폐플라스틱 성형물은 기계적 성질인 경도와 강도면에서 우수하고, 내열성, 내후성, 내구성, 내산성, 내식성도 우수하며, 또한 기존의 플라스틱과 같이 압출성형방법으로 제조할 수 있는 것이면 모두 가능하지만 원재료가 폐플라스틱이란 점을 고려하여 위생에는 관련이 없으며 강도가 요구되는 제품으로서, 건물의 바닥재, 벽면마감재, 칸막이, 거푸집, 토류판, 중압관 등의 건축용 자재와 하우스, 축사, 농업용 지지대 또는 하수관이나 공업용수를 수송하는 수송관 등 각종 파이프제품을 압출성형할 수 있다.As shown in the above [Table 2], the waste plastic molded product produced by the present invention has excellent mechanical properties in terms of hardness and strength, and also has excellent heat resistance, weather resistance, durability, acid resistance, corrosion resistance, and extrusion molding method like conventional plastics. It can be used if it can be manufactured, but considering the fact that the raw material is waste plastic, it is not related to hygiene and requires strength, and it is a product that requires construction materials such as building floor materials, wall finishing materials, partitions, formwork, earth plate, and pressure pipe. Various pipe products, such as houses, houses, agricultural supports, sewage pipes, and transport pipes for transporting industrial water, can be extruded.
상기와 같은 본 발명에 의하면 산업폐기물로 폐기처리되는 각종 폐플라스틱을 수거하여 선별작업 및 세척작업을 수행하지 않고 작게 분쇄하여 원료로 사용하므로서 각종 폐플라스틱의 재활용에 이바지할 수 있으며, 또한 기계적인 경도 및 강도가 우수한 제품을 제조할 수 있게 하는 방법을 제공하는 유용한 발명이다.According to the present invention as described above it is possible to contribute to the recycling of various waste plastics by collecting the various waste plastics to be disposed of as industrial waste, and by using a small pulverization as a raw material without performing sorting and washing operations, and also mechanical hardness And useful inventions that provide methods for making products of high strength.
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH05301223A (en) * | 1992-04-24 | 1993-11-16 | Takehiro:Kk | Production of regenerated resin product using resin wastes |
JPH05345842A (en) * | 1992-06-16 | 1993-12-27 | Calp Corp | Compound resin composition for bent sheet |
US5746961A (en) * | 1995-12-04 | 1998-05-05 | Michael J. Stevenson | Method for enhancement of the surfaces of molded plastic products |
EP0899072A1 (en) * | 1997-08-28 | 1999-03-03 | Jae Ho Lee | Method for producing plastic forms from waste synthetic resin |
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---|---|---|---|---|
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JPH05301223A (en) * | 1992-04-24 | 1993-11-16 | Takehiro:Kk | Production of regenerated resin product using resin wastes |
JPH05345842A (en) * | 1992-06-16 | 1993-12-27 | Calp Corp | Compound resin composition for bent sheet |
US5746961A (en) * | 1995-12-04 | 1998-05-05 | Michael J. Stevenson | Method for enhancement of the surfaces of molded plastic products |
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