JP2020521834A - Manufacturing method and application of enhanced toughening and transparent masterbatch - Google Patents
Manufacturing method and application of enhanced toughening and transparent masterbatch Download PDFInfo
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- 239000004594 Masterbatch (MB) Substances 0.000 title claims abstract description 94
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 claims abstract description 46
- 239000000463 material Substances 0.000 claims abstract description 31
- 239000002362 mulch Substances 0.000 claims abstract description 24
- 239000011347 resin Substances 0.000 claims abstract description 22
- 229920005989 resin Polymers 0.000 claims abstract description 22
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims description 53
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 claims description 42
- 239000004626 polylactic acid Substances 0.000 claims description 33
- 229920000747 poly(lactic acid) Polymers 0.000 claims description 32
- 239000012745 toughening agent Substances 0.000 claims description 24
- 239000002270 dispersing agent Substances 0.000 claims description 19
- 239000002245 particle Substances 0.000 claims description 17
- 230000002209 hydrophobic effect Effects 0.000 claims description 16
- 238000000071 blow moulding Methods 0.000 claims description 15
- 239000000155 melt Substances 0.000 claims description 15
- 239000000314 lubricant Substances 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 12
- 238000005728 strengthening Methods 0.000 claims description 12
- 238000009792 diffusion process Methods 0.000 claims description 11
- 239000003921 oil Substances 0.000 claims description 11
- 235000019198 oils Nutrition 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 10
- 229920001296 polysiloxane Polymers 0.000 claims description 10
- 239000004005 microsphere Substances 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 9
- 235000012424 soybean oil Nutrition 0.000 claims description 9
- 239000003549 soybean oil Substances 0.000 claims description 9
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 8
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 8
- 239000003381 stabilizer Substances 0.000 claims description 8
- OLFNXLXEGXRUOI-UHFFFAOYSA-N 2-(benzotriazol-2-yl)-4,6-bis(2-phenylpropan-2-yl)phenol Chemical compound C=1C(N2N=C3C=CC=CC3=N2)=C(O)C(C(C)(C)C=2C=CC=CC=2)=CC=1C(C)(C)C1=CC=CC=C1 OLFNXLXEGXRUOI-UHFFFAOYSA-N 0.000 claims description 6
- FMRHJJZUHUTGKE-UHFFFAOYSA-N Ethylhexyl salicylate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1O FMRHJJZUHUTGKE-UHFFFAOYSA-N 0.000 claims description 6
- 239000012963 UV stabilizer Substances 0.000 claims description 6
- 239000008476 aike Substances 0.000 claims description 6
- 239000006096 absorbing agent Substances 0.000 claims description 5
- WSQZNZLOZXSBHA-UHFFFAOYSA-N 3,8-dioxabicyclo[8.2.2]tetradeca-1(12),10,13-triene-2,9-dione Chemical compound O=C1OCCCCOC(=O)C2=CC=C1C=C2 WSQZNZLOZXSBHA-UHFFFAOYSA-N 0.000 claims description 4
- 239000006097 ultraviolet radiation absorber Substances 0.000 claims description 4
- 239000008187 granular material Substances 0.000 claims description 3
- 239000012744 reinforcing agent Substances 0.000 claims description 3
- 230000003014 reinforcing effect Effects 0.000 claims description 3
- 150000001412 amines Chemical class 0.000 claims description 2
- QRUDEWIWKLJBPS-UHFFFAOYSA-N benzotriazole Chemical compound C1=CC=C2N[N][N]C2=C1 QRUDEWIWKLJBPS-UHFFFAOYSA-N 0.000 claims description 2
- 239000012964 benzotriazole Substances 0.000 claims description 2
- 239000000326 ultraviolet stabilizing agent Substances 0.000 claims description 2
- 239000002562 thickening agent Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 22
- 238000012545 processing Methods 0.000 abstract description 19
- 239000002994 raw material Substances 0.000 abstract description 8
- 230000002708 enhancing effect Effects 0.000 abstract description 5
- 238000009264 composting Methods 0.000 abstract description 4
- 238000004806 packaging method and process Methods 0.000 abstract description 4
- 230000003287 optical effect Effects 0.000 abstract description 3
- 239000004621 biodegradable polymer Substances 0.000 abstract 1
- 229920002988 biodegradable polymer Polymers 0.000 abstract 1
- 239000003623 enhancer Substances 0.000 abstract 1
- 229920001896 polybutyrate Polymers 0.000 abstract 1
- 239000010408 film Substances 0.000 description 165
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- -1 polyhydroxyester Polymers 0.000 description 8
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- 229920000092 linear low density polyethylene Polymers 0.000 description 3
- 239000004707 linear low-density polyethylene Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- 229920000379 polypropylene carbonate Polymers 0.000 description 3
- 238000002834 transmittance Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 229920000704 biodegradable plastic Polymers 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 239000002075 main ingredient Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000001782 photodegradation Methods 0.000 description 2
- 239000002985 plastic film Substances 0.000 description 2
- 229920006255 plastic film Polymers 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical group O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229920003232 aliphatic polyester Polymers 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 238000003490 calendering Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000008395 clarifying agent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- QBSJMKIUCUGGNG-UHFFFAOYSA-N isoprocarb Chemical group CNC(=O)OC1=CC=CC=C1C(C)C QBSJMKIUCUGGNG-UHFFFAOYSA-N 0.000 description 1
- 230000005226 mechanical processes and functions Effects 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 239000008191 permeabilizing agent Substances 0.000 description 1
- 239000004632 polycaprolactone Substances 0.000 description 1
- 229920001610 polycaprolactone Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920006254 polymer film Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
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- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
- A01G13/00—Protecting plants
- A01G13/02—Protective coverings for plants; Coverings for the ground; Devices for laying-out or removing coverings
-
- 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
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/205—Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase
-
- 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
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/36—Silica
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/16—Solid spheres
- C08K7/18—Solid spheres inorganic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L33/04—Homopolymers or copolymers of esters
- C08L33/06—Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, which oxygen atoms are present only as part of the carboxyl radical
- C08L33/10—Homopolymers or copolymers of methacrylic acid esters
- C08L33/12—Homopolymers or copolymers of methyl methacrylate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L91/00—Compositions of oils, fats or waxes; Compositions of derivatives thereof
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental Sciences (AREA)
- Toxicology (AREA)
- General Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
本発明は生分解高分子材料分野に属し、特に増強増靭増透マスターバッチ(強度、強靭さと透明さが増強できるMasterbatches)に関する。このマスターバッチはポリアジペート/テレフタレートと増強増靭増透剤(強靭さと透明さを増す増強剤)を主原料として製造される。フィムルに加工するだけでなくマルチフィルムにも加工することができる。超薄型完全生分解性フィルム製品の加工を容易にし、力学・光学性能及び使用の安定性を維持できるとともに、フィルムの生産のコストを大幅に下げることもできる。その生産過程は簡単で、把握しやすい。出来上がったマスターバッチは性質が安定し、完全に分解され、分散性がよい。本発明の少量のマスターバッチと分解樹脂(PBAT+PLA等)を加えて使用すれば、6μm以下の超薄型完全生分解性フィルム製品が作成可能である。そして、制作の過程での開口性がよく、加工の安定さが強まり、機械特性が優秀である。これはフィルム包装、買い物袋、農業用マルチフィルム、ゴミ袋及び分別埋立、堆肥作り処理などに広く活用できる。The present invention belongs to the field of biodegradable polymer materials, and particularly relates to an enhanced toughening and transparent masterbatch (Masterbatches capable of enhancing strength, toughness and transparency). This masterbatch is manufactured by using polyadipate/terephthalate and an enhanced toughening/transparent agent (an enhancer that increases toughness and transparency) as main raw materials. It can be processed not only into film but also into multi-film. It can facilitate the processing of ultra-thin, fully biodegradable film products, maintain the mechanical and optical performance and stability of use, and can significantly reduce the cost of film production. Its production process is simple and easy to grasp. The finished masterbatch has stable properties, is completely decomposed, and has good dispersibility. If a small amount of the masterbatch of the present invention and a decomposed resin (PBAT+PLA, etc.) are added and used, an ultrathin completely biodegradable film product having a size of 6 μm or less can be prepared. In addition, it has good openability in the process of production, strengthens the stability of processing, and has excellent mechanical properties. It can be widely used for film packaging, shopping bags, agricultural mulch film, garbage bags and separate landfills, composting processing, etc.
Description
本発明は材料分野に属し、詳しくは完全生分解性プラスチックマスターバッチに関し、特に増強増靭増透マスターバッチとその製造方法及び応用に関する。 TECHNICAL FIELD The present invention belongs to the field of materials, and more particularly to a completely biodegradable plastic masterbatch, and more particularly to an enhanced toughening and transparent masterbatch, a method for producing the same and an application thereof.
プラスチックフィルムやマルチフィルムは日常生活、工業・農業生産において大きな役割を果たしている。しかし、現在使われているプラスチックフィルムとマルチフィルムの大部分は短時間で分解され難いポリオレフィンフィルム、もしくは澱粉と光分解促進剤を添加した不完全分解フィルムである。これらのフィルム材料の使用は、プラスチック汚染問題を起こさせ、人類の持続的な発展に隠れた危険をもたらす。完全生分解性フィルムは、完全生分解性プラスチックをブロー成形、鋳造(cast)あるいはカレンダー加工工程により製造され、微生物により完全に分解されることができ、生分解の最終産物が二酸化炭素と水であり、自然界により完全に分解されることができるため、ポリオレフィン類製品を代替することで、白い公害(White Pollution)を解決する重要な手段である。 Plastic films and mulch films play a major role in daily life, industrial and agricultural production. However, most of the plastic films and mulch films currently used are polyolefin films that are difficult to decompose in a short time, or incompletely decomposed films to which starch and a photodegradation accelerator are added. The use of these film materials causes plastic pollution problems and poses a hidden danger to the sustainable development of mankind. The fully biodegradable film is produced by blow molding, casting or calendering process of completely biodegradable plastic, and can be completely decomposed by microorganisms. The end product of biodegradation is carbon dioxide and water. Since it can be completely decomposed by nature, it is an important means for solving white pollution by substituting polyolefin products.
現在の完全生分解性フィルムは主にポリ乳酸、ポリカプロラクトン、脂肪族ポリエステル、脂肪族ポリカーボネート、ポリヒドロキシエステル、澱粉等からなるが、上述したポリマー自体の特徴と欠点の為、単一ポリマーをフィルム材料として使用することは難しい。現在の研究には、主にブレンド改質、共重合改質、可塑化改質および複合改質によってフィルムの総合性能を改善している。中国特許文献CN103589124Bは完全生分解性PLA/PBAT複合フィルム及びその製造方法を開示しており、中国特許文献CN104744898Aは完全生分解性フィルム及びその製造方法を開示しており、そのうち、該当のフィルムはポリ乳酸(PLA)、ポリプロピレンカーボネート(PPC)、ポリアジペート/ブチレンテレフタレート(PBAT)及び熱安定剤からなるが、上述のフィルム製品厚みは6um〜50umで、普遍的に厚いため、コストが高くなる。しかしながら、厚みが大きすぎると光透過性が悪くなり、小さすぎると強度が弱くなるため、短期間で商業化することができないし、最適な機能バランスに達することができない。分解され難いポリオレフィン類フィルムとは異なり、完全生分解性フィルムは、加工が便利で性能が優れている範囲において、フィルム製品は薄いほど好ましい。しかしながら、試験を通して、6μm未満の超薄型フィルムは、フィルムブロー成型工程で気泡開放が困難であったり、引張強度及び引裂強度が大幅に低下されたり、ヘイズが大きったりする問題が存在する。そしてフィルムとして現場で使用される場合、日射により樹脂分子鎖架橋、フィルムの靭性の低下、及び脆さの増加、並びにフィルムの早期裂けが現れる。したがって、既存の超薄型の完全生分解性フィルム製品の加工及び性能における欠点を克服し、専用の増強増靭増透マスターバッチを提供することが解決すべき課題である。 Currently, the completely biodegradable film is mainly composed of polylactic acid, polycaprolactone, aliphatic polyester, aliphatic polycarbonate, polyhydroxyester, starch, etc. However, due to the above-mentioned characteristics and defects of the polymer itself, a single polymer film is used. It is difficult to use as a material. Current research has mainly improved the overall performance of the film by blend modification, copolymerization modification, plasticization modification and composite modification. Chinese patent document CN103589124B discloses a fully biodegradable PLA/PBAT composite film and a manufacturing method thereof, and Chinese patent document CN1047444898A discloses a fully biodegradable film and a manufacturing method thereof, of which the corresponding film is It is composed of polylactic acid (PLA), polypropylene carbonate (PPC), polyadipate/butylene terephthalate (PBAT) and a heat stabilizer, but the above-mentioned film product thickness is 6 μm to 50 μm, which is generally thick and therefore costly. However, if the thickness is too large, the light transmissivity deteriorates, and if it is too small, the strength becomes weak, so that it cannot be commercialized in a short period of time and the optimum functional balance cannot be reached. Unlike polyolefin films, which are difficult to decompose, a fully biodegradable film is preferable as the film product is thinner, in the range where processing is convenient and performance is excellent. However, through the tests, ultra-thin films of less than 6 μm have problems that it is difficult to open bubbles in the film blow molding process, tensile strength and tear strength are significantly reduced, and haze is large. When used as a film in the field, solar radiation causes crosslinking of resin molecular chains, a decrease in toughness of the film, an increase in brittleness, and premature tearing of the film. Therefore, it is a problem to be solved to overcome the drawbacks in processing and performance of existing ultra-thin fully biodegradable film products and to provide a dedicated enhanced toughening and transparency masterbatch.
本発明は従来技術に存在する多くの問題に対して、増強増靭増透マスターバッチ及びその製造方法と応用を提供する。このマスターバッチはポリアジペート/テレフタレートを主原料として製造され、フィルムに加工されるだけでなくマルチフィルムにも加工されることができ、超薄型完全生分解性フィルム製品の加工の順調さと力学・光学物性及び安定性を維持するとともに、フィルムのコストを大幅に下げることができる。このマスターバッチの生産過程は簡単で、把握しやすいし、得られたマスターバッチは安定した性質を有し、完全に分解され、分散性も良い。本発明のマスターバッチを少量添加し、分解樹脂(PBAT+PLA等)と配合して使用すれば、6μm以下の超薄型完全生分解性フィルム製品を作製することができ、超薄型フィルムブロー成形工程において気泡開放が容易で、加工安定性が高まり、機械的機能が優れており、フィルム類包装、買い物袋、農業用マルチフィルム、ゴミ分別埋立、堆肥作り処理などに幅広く使用できる。 The present invention provides an enhanced toughening and translucent masterbatch and its manufacturing method and application to many problems existing in the prior art. This masterbatch is manufactured using polyadipate/terephthalate as the main raw material, and it can be processed not only into film but also into multi-film. The smoothness and mechanics of processing ultra-thin fully biodegradable film products The cost of the film can be significantly reduced while maintaining the optical properties and stability. The production process of this masterbatch is simple and easy to grasp, and the obtained masterbatch has stable properties, is completely decomposed and has good dispersibility. By adding a small amount of the masterbatch of the present invention and mixing it with a decomposition resin (PBAT+PLA, etc.), an ultrathin completely biodegradable film product having a size of 6 μm or less can be produced. With its easy opening of air bubbles, improved processing stability, and excellent mechanical function, it can be widely used for film packaging, shopping bags, agricultural mulch film, waste landfill, composting, etc.
本発明の具体的な技術解決手段は以下のとおりである。
増強増靭増透マスターバッチであって、重量部で計算すると、主な成分として、ポリアジペート/テレフタレート65〜88重量部、増強増靭増透剤10〜20重量部を含む。
The concrete technical solution means of the present invention is as follows.
An enhanced toughening and transparency masterbatch containing 65 to 88 parts by weight of a polyadipate/terephthalate and 10 to 20 parts by weight of an enhanced toughening and transparency agent as main components, calculated in parts by weight.
そのうち、前記ポリアジペート/テレフタレートは担体樹脂であり、メルトフローレートは2〜5 g/10minであり、酸価は15未満である。本発明において使用されたポリアジペート/テレフタレートは超薄型完全生分解性フィルム用マスターバッチの製造及び使用性能にとって非常に重要であり、全ての材料を溶融させるだけでなく、高温に耐えられ、揮発及び分解を起こさなく、後の工程において本発明が提供したマスターバッチを用いて超薄型完全生分解性フィルムを製造するとき、他の完全生分解性フィルムとのより良い相溶性を有し、かつフィルムの分解を起こさせない必要があるため、発明者は多くの樹脂から当該樹脂をマスターバッチの担体樹脂として選択して、かつ具体的な用量を上記のように限定する。その用量の範囲でマスターバッチのそれぞれの機能の最適なバランスが取れる。 Among them, the polyadipate/terephthalate is a carrier resin, the melt flow rate is 2 to 5 g/10 min, and the acid value is less than 15. The polyadipate/terephthalate used in the present invention is very important for the production and use performance of the masterbatch for ultrathin fully biodegradable film, not only melting all materials, but also capable of withstanding high temperature and volatilizing. And without causing decomposition, when producing an ultrathin fully biodegradable film using the masterbatch provided by the present invention in a later step, has a better compatibility with other fully biodegradable films, And since it is necessary not to cause the film to decompose, the inventor selects the resin from many resins as the masterbatch carrier resin and limits the specific dose as described above. The dose range provides the optimum balance of each function of the masterbatch.
前記増強増靭増透剤は、無機増強増靭増透剤、有機増強増靭増透剤のうちの1種又は複数種であり、前記無機増強増靭増透剤は疎水性ナノシリカから選択され、前記疎水性ナノシリカの粒径は5〜25nmであり、前記有機増強増靭増透剤は、Akerma AX〜8900、ADX〜1200s樹脂相溶化剤又はHangzhou Aike CE〜AZ01相溶化剤のうちの一種又は複数種である。 The enhanced toughening agent is one or more of an inorganic enhanced toughening agent and an organic enhanced toughening agent, and the inorganic enhanced toughening agent is selected from hydrophobic nanosilica. The hydrophobic nanosilica has a particle size of 5 to 25 nm, and the organic enhanced toughening and transparent agent is one of Akerma AX to 8900, ADX to 1200s resin compatibilizer or Hangzhou Aike CE to AZ01 compatibilizer. Or, there are multiple types.
増強増靭増透剤が20重量部を超えないようにする理由は、樹脂と原料を混合する過程における粉体の損失を少なくさせ、分布の均一性及び造粒の利便性を保証し、後のフィルム加工における複数種の樹脂の相溶性を高めるとともに、複数種フィラーの過多的な添加によりフィルムの機械的性能が下げることはないからである。 The reason why the strengthening/toughening/permeabilizing agent does not exceed 20 parts by weight is to reduce the loss of powder in the process of mixing the resin and the raw materials, to ensure the uniformity of distribution and the convenience of granulation. This is because the compatibility of a plurality of kinds of resins in the film processing is increased and the mechanical performance of the film is not deteriorated by the excessive addition of the plurality of kinds of fillers.
上述した増強増靭増透剤を選択すると、担体樹脂との相溶性が良いため、高濃度のマスターバッチを得られ、フィルムの後期加工過程において、造核剤及び相溶化のような作用をし、超薄型フィルムの加工の安定性に有利であるとともに、超薄型完全生分解性フィルムの力学物性を高めることもできる。 When the above-mentioned reinforced toughening agent and transparency agent are selected, the compatibility with the carrier resin is good, so that a high-concentration masterbatch can be obtained, and it acts as a nucleating agent and a compatibilizing agent in the later processing step of the film. In addition to being advantageous in the stability of processing of the ultrathin film, it is possible to enhance the mechanical properties of the ultrathin completely biodegradable film.
また、用途により上記の組み合わせの基に他の添加剤成分を添加しても良い。 Further, other additive components may be added to the above-mentioned combination group depending on the use.
より具体的に、発明者はまた超薄型完全生分解性フィルム用増強増靭増透剤マスターバッチを提供した。重量部で計算すると、主要成分として、
ポリアジペート/テレフタレート65〜88重量部、増強増靭増透剤10〜20重量部、潤滑剤0.5〜30重量部、分散剤1〜5重量部を含む。
More specifically, the inventor has also provided enhanced toughening and transparency masterbatch for ultrathin fully biodegradable films. When calculated in parts by weight, as the main component,
Includes 65 to 88 parts by weight of polyadipate/terephthalate, 10 to 20 parts by weight of reinforcing and toughening agent, 0.5 to 30 parts by weight of lubricant, and 1 to 5 parts by weight of dispersant.
そのうち、前記潤滑剤はポリマーPMMAミクロスフェア、シリカミクロスフェアのうちの1種又は2種である。前記ポリマーPMMAミクロスフェアの粒径は0.5〜5μmであり、前記シリカミクロスフェアの粒径は1〜5μmであり、いずれも市場で直接購入可能なものである。 Among them, the lubricant is one or two of polymer PMMA microspheres and silica microspheres. The particle size of the polymer PMMA microspheres is 0.5 to 5 μm, and the particle size of the silica microspheres is 1 to 5 μm, both of which can be directly purchased on the market.
前記潤滑剤は本発明においてフィルムの開口部を潤滑にする作用をし、超薄型完全生分解性フィルムを加工するときフィルムの開口に有利であるとともに、ミクロスフェアの粒径は5μm未満であるため、後に製造される超薄型完全生分解性フィルムの機械的物性と透光性を保証することができる。 In the present invention, the lubricant acts to lubricate the openings of the film, is advantageous for opening the film when processing an ultrathin fully biodegradable film, and the particle size of the microspheres is less than 5 μm. Therefore, the mechanical properties and translucency of the ultrathin fully biodegradable film produced later can be guaranteed.
本発明に係る前記分散剤は前記エポキシ化大豆油、有機シリコーン拡散オイルから選択される1種又は2種である。前記分散剤を選択使用することでよりよく増強増靭増透剤と配合することができ、担体(carrier)樹脂における増強増靭増透剤の分散に有利である。また、本発明の技術において、分散剤及び有機溶媒の添加の代わりに公知の物理分散方法で分散させることもできるが、効果は分散剤を添加した場合と比べて低いため、上述した分散剤を添加する方法が好ましい。 The dispersant according to the present invention is one or two selected from the epoxidized soybean oil and the organic silicone diffusion oil. By selectively using the dispersant, the dispersant can be better blended with the toughening and transparency enhancing agent, which is advantageous for dispersion of the toughening and transparency enhancing agent in the carrier resin. Further, in the technique of the present invention, it is possible to disperse by a known physical dispersion method instead of the addition of the dispersant and the organic solvent, but the effect is lower than when the dispersant is added. The method of addition is preferred.
本発明に係る全ての添加剤は環境に優しい試剤と材料であり、自然界で完全に分解される。 All additives according to the present invention are environmentally friendly reagents and materials and are completely decomposed in nature.
前記超薄型完全生分解性フィルム用増強増靭増透マスターバッチの製造方法は、
所定量の増強増靭増透剤、分散剤を四塩化炭素に溶融して分散させ、均一に撹拌した後、四塩化炭素を蒸留して混合物を得る工程(1)と、
工程(1)から得られた混合物、ポリアジペート/テレフタレート、潤滑剤を順次に重量部で高速ミキサーに入れ、10〜30分間混錬する工程(2)と、
工程(2)から得られた均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る工程(3)とを含む。
The method for producing an enhanced toughening and transparent masterbatch for the ultrathin completely biodegradable film,
A step (1) of obtaining a mixture by melting a predetermined amount of an enhanced toughening agent and a dispersant in carbon tetrachloride for dispersion, stirring the mixture uniformly, and distilling carbon tetrachloride;
A step (2) in which the mixture obtained from the step (1), the polyadipate/terephthalate, and the lubricant are sequentially put in a high-speed mixer in parts by weight and kneaded for 10 to 30 minutes;
For the ultrathin completely biodegradable film, the homogeneously mixed mixture obtained from step (2) is put into a twin-screw extruder, extruded under the condition of 135 to 160° C., air cooled and granulated. A step (3) of obtaining an enhanced toughening and transparent masterbatch.
上述の製造方法において、発明者はまず四塩化炭素を溶媒として増強増靭剤を溶解して分散させ、そして揮発性溶剤を用いて分散剤を増強増靭剤の表面に被覆させ、担体樹脂における増強増靭剤の分散効果は公知の混合方法より良い。 In the above-mentioned production method, the inventor first dissolves and disperses the enhanced toughening agent in carbon tetrachloride as a solvent, and then coats the dispersant on the surface of the enhanced toughening agent using a volatile solvent, The dispersing effect of the strengthening toughening agent is better than that of known mixing methods.
その他、分散剤と有機溶媒を添加しない製造方法は、
所定量の増強増靭増透剤、ポリアジペート/テレフタレート、潤滑剤を重量部で順次に高速ミキサーに入れ、10〜30分間混錬する工程(1)と、
工程(1)から得られた均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る工程(2)とを含む。
In addition, the manufacturing method without adding a dispersant and an organic solvent is
A step (1) of sequentially adding a predetermined amount of a strengthening/toughening agent, a polyadipate/terephthalate, and a lubricant in a high-speed mixer in parts by weight and kneading for 10 to 30 minutes;
The uniformly mixed mixture obtained from the step (1) is put in a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated, and for ultrathin completely biodegradable film A step (2) of obtaining an enhanced toughening and transparent masterbatch.
前記超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得た後、発明者はさらに前記マスターバッチの具体的な応用を提供し、それを超薄超透明型完全生分解性フィルムブロー成形フィルム級材料に使用した。このフィルムブロー成形フィルム級材料は、重量部で計算すると、主な成分として、
ポリアジペート/テレフタレート80〜90重量部、ポリ乳酸0.5〜20重量部、超薄型完全生分解性フィルム用増強増靭増透マスターバッチ1〜5重量部を含む。
After obtaining the enhanced toughening/transparency masterbatch for the ultrathin fully biodegradable film, the inventor further provides a specific application of the masterbatch, which is an ultrathin ultratransparent fully biodegradable film. Used for blow molded film grade materials. This film blow molding film grade material, when calculated in parts by weight, as the main component,
Includes 80 to 90 parts by weight of polyadipate/terephthalate, 0.5 to 20 parts by weight of polylactic acid, and 1 to 5 parts by weight of enhanced toughening and transparent masterbatch for ultrathin completely biodegradable film.
そのうち、ポリアジペート/テレフタレート及びポリ乳酸を担体樹脂とし、そのメルトフローレートは2〜5 g/10minであり、酸価は15未満であり、マスターバッチ材料の中のポリアジペート/テレフタレートの規格と同じであり、前記ポリ乳酸のメルトフローレートは2〜5 g/10minである。 Among them, polyadipate/terephthalate and polylactic acid are used as carrier resins, the melt flow rate is 2 to 5 g/10 min, the acid value is less than 15, which is the same as the standard of polyadipate/terephthalate in the masterbatch material. And the melt flow rate of the polylactic acid is 2 to 5 g/10 min.
対応するブロー成形フィルム級材料の製法方法は、
ポリアジペート/テレフタレート、ポリ乳酸、超薄超透明型完全生分解性フィルム用増強増靭増透マスターバッチを高速ミキサーに入れ、700〜1000 r/minの速度攪拌速度で5〜8分間撹拌する工程(1)と、
均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して得る工程(2)とを含む。
The manufacturing method of the corresponding blow molded film grade material is
A process of adding polyadipate/terephthalate, polylactic acid, and an ultra-thin ultra-transparent type fully enhanced biodegradable film toughening and increasing transparency masterbatch into a high-speed mixer and stirring at a speed stirring speed of 700 to 1000 r/min for 5 to 8 minutes. (1),
The step (2) of putting the uniformly mixed mixture in a twin-screw extruder, extruding the mixture under conditions of 135 to 160° C., air cooling and granulating is included.
上述した方法で得られたブロー成形フィルム級材料は、直接に厚さ6μm以下の超薄型フィルムに成形することができ、その引張強度及び引裂伸度率は同じ厚みのLLDPEフィルムより優れるため、PE製品を完全に代替することができ、その上優秀な加工性能を有し、特殊な製造設備で加工する必要もない。 The blow-molded film grade material obtained by the method described above can be directly formed into an ultrathin film having a thickness of 6 μm or less, and its tensile strength and tear elongation ratio are superior to those of the LLDPE film having the same thickness. It can completely replace PE products, has excellent processing performance, and does not need to be processed by special manufacturing equipment.
前記フィルム用マスターバッチの他に、発明者はさらに超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを提供した。は重量部で計算すすると、主な成分として、
ポリアジペート/テレフタレート65〜85重量部、ポリ乳酸1〜20重量部、増強増靭増透剤10〜20重量部、潤滑剤5〜30重量部、分散剤1〜5重量部、安定剤1〜5重量部を含む。
In addition to the above film masterbatch, the inventor further provided an ultra-thin fully biodegradable multi-film enhanced toughening and transparency masterbatch. When calculated in parts by weight, as the main component,
65 to 85 parts by weight of polyadipate/terephthalate, 1 to 20 parts by weight of polylactic acid, 10 to 20 parts by weight of reinforcing and toughening agent, 5 to 30 parts by weight of lubricant, 1 to 5 parts by weight of dispersant, and 1 to stabilizer. Including 5 parts by weight.
そのうち、ポリ乳酸及びポリアジペート/テレフタレートを担体樹脂とし、そのメルトフローレートは2〜5 g/10minであり、酸価は15未満であり、ポリアジペート/テレフタレートと同じ規格である。 Among them, polylactic acid and polyadipate/terephthalate are used as a carrier resin, the melt flow rate thereof is 2 to 5 g/10 min, the acid value is less than 15, which is the same standard as polyadipate/terephthalate.
上記で使用される潤滑剤及び分散剤はフィルムマスターバッチの候補物質と同じであるため、発明者はここで繰り述べないこととする。そして前記安定剤は紫外線吸収剤及び紫外線安定剤のうちの1種又は2種であり、前記紫外線吸収剤は低揮発性ベンゾトリアゾール紫外線吸収剤Tinuvin 234である。前記紫外線安定剤は立体障害アミン安定剤Uvinul(登録商標) 5050Hであり、超薄型完全生分解性フィルム加工過程及び現場で使用する時における光分解問題を防ぐことができ、使用寿命を延ばすことができる。 The lubricants and dispersants used above are the same as the candidate substances for the film masterbatch, so the inventor will not repeat them here. The stabilizer is one or two of an ultraviolet absorber and an ultraviolet stabilizer, and the ultraviolet absorber is a low-volatile benzotriazole ultraviolet absorber Tinuvin 234. The UV stabilizer is a sterically hindered amine stabilizer Uvinul (registered trademark) 5050H, which can prevent the photodegradation problem during the process of processing an ultra-thin completely biodegradable film and in the field, and extend the service life. You can
発明者は上記マルチフィルム用増強増靭増透マスターバッチの製造方法も提供した。その製造方法は、
所定量の増強増靭増透剤、分散剤を四塩化炭素に溶解し分散させ、均一に撹拌した後、四塩化炭素を蒸留して混合物を得る工程(1)と、
工程(1)からで得られた混合物、ポリアジペート/テレフタレート、ポリ乳酸、安定剤、潤滑剤を重量部で順次に高速ミキサーに入れ、700〜1000r/minの速度で10〜30分間撹拌して混錬する工程(2)と、
工程(2)から得られた均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押し出し、空冷にして造粒して、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る工程(3)とを含む。
The inventor has also provided a method for producing the masterbatch for enhanced toughness and transparency for mulch film. The manufacturing method is
A step (1) of dissolving a predetermined amount of a strengthening/toughening agent and a dispersant in carbon tetrachloride to disperse and uniformly stirring, and then distilling carbon tetrachloride to obtain a mixture;
The mixture obtained from the step (1), polyadipate/terephthalate, polylactic acid, stabilizer and lubricant were sequentially added to a high speed mixer in parts by weight and stirred at a speed of 700 to 1000 r/min for 10 to 30 minutes. Kneading step (2),
For the ultrathin completely biodegradable film, put the uniformly mixed mixture obtained from step (2) in a twin-screw extruder, extrude under the condition of 135-160° C., air cool and granulate. A step (3) of obtaining an enhanced toughening and transparent masterbatch.
同じように、上記マスターバッチは分散剤の代わりに公知の物理分散方法で分散させても良い。具体的な方法は上述した超薄型完全生分解性フィルム用増強増靭増透マスターバッチの製造方法を参考して良い。 Similarly, the masterbatch may be dispersed by a known physical dispersion method instead of the dispersant. For the specific method, the manufacturing method of the above-mentioned masterbatch for enhancing toughness and transparency for ultrathin biodegradable film may be referred to.
上述した通り、本発明が提供したマスターバッチはポリアジペート/テレフタレート及び増強増靭増透剤を主原料として製造され、フィルムに加工されるだけでなくマルチフィルムにも加工されることができ、超薄型完全生分解性フィルム製品の加工の順調さと力学・光学物性及び使用安定性を維持するとともに、原材料のコストを大幅に下げることができる。このマスターバッチの生産過程は簡単で、把握しやすいし、得られたマスターバッチは安定した性質を有し、水分が一切なく、完全に分解され、分散性が良い。本発明のマスターバッチを少量添加することで、6μm以下の超薄型完全生分解性フィルム製品を成形することができ、超薄型完全フィルム成形過程において気泡開放が容易で、加工安定性が高まり、機械物性もており、フィルム類包装、買い物袋、農業用マルチフィルム、ゴミ袋及び分別埋立、堆肥作り処理など幅広く応用できる。 As described above, the masterbatch provided by the present invention is manufactured by using polyadipate/terephthalate and an enhanced toughening/clarifying agent as main materials, and can be processed into not only a film but also a multi-film. It is possible to maintain the smooth processing of thin, completely biodegradable film products, maintain mechanical and optical properties, and use stability, and significantly reduce the cost of raw materials. The production process of this masterbatch is simple and easy to grasp, and the obtained masterbatch has stable properties, has no water content, is completely decomposed, and has good dispersibility. By adding a small amount of the masterbatch of the present invention, an ultra-thin completely biodegradable film product having a size of 6 μm or less can be formed, and it is easy to open the bubbles in the ultra-thin complete film forming process and the processing stability is enhanced. It also has mechanical properties and can be widely applied to film packaging, shopping bags, agricultural mulch film, garbage bags and separate landfills, and composting processing.
(実施例1)
超薄型完全生分解性フィルム用増強増靭増透マスターバッチの成分は、重量部で計算すると、以下の通りである。
ポリアジペート/テレフタレート 75重量部
疎水性ナノシリカ(粒径5〜10nm) 20重量部
ポリマーPMMAミクロスフェア(粒径2〜3μm) 30重量部
エポキシ化大豆油 1重量部
(Example 1)
The components of the enhanced toughening and transparent masterbatch for ultrathin completely biodegradable film are as follows, calculated in parts by weight.
Polyadipate/terephthalate 75 parts by weight Hydrophobic nanosilica (particle size 5-10 nm) 20 parts by weight Polymer PMMA microspheres (particle size 2-3 μm) 30 parts by weight Epoxidized soybean oil 1 part by weight
以下の工程により製造して得られる。
疎水性ナノシリカ及びエポキシ化大豆油を四塩化炭素に溶解した分散させ、均一に撹拌し、四塩化炭素を蒸留して混合物1を得て、混合物1、ポリアジペート/テレフタレート及びポリマーPMMAミクロスフェアを高速ミキサーに順次に入れ、700〜1000r/minの速度で10〜30分間混錬して混合物2を得て、混合物2を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る。
It is produced by the following steps.
Hydrophobic nanosilica and epoxidized soybean oil are dissolved and dispersed in carbon tetrachloride, stirred uniformly, carbon tetrachloride is distilled to obtain mixture 1, and mixture 1, polyadipate/terephthalate and polymer PMMA microspheres are spun at high speed. Put in a mixer one by one, knead at a speed of 700 to 1000 r/min for 10 to 30 minutes to obtain a mixture 2, put the mixture 2 in a twin-screw extruder, extrude under the condition of 135 to 160° C., and air cool. And granulated to obtain a masterbatch with enhanced toughness and transparency for ultrathin completely biodegradable film.
当該マスターバッチを用いて超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を製造する。重量部で計算すると、主な成分として、
ポリアジペート/テレフタレート87重量部、ポリ乳酸10重量部、超薄超透明型明完全生分解性フィルム用増強増靭増透マスターバッチ3重量部を含む。
The masterbatch is used to produce an ultrathin ultratransparent fully biodegradable film blow molded film grade material. When calculated in parts by weight, as the main ingredients,
Includes 87 parts by weight of polyadipate/terephthalate, 10 parts by weight of polylactic acid, and 3 parts by weight of masterbatch for strengthening/toughening/permeation for ultra-thin ultra-transparent bright fully biodegradable film.
そのうち前記ポリアジペート/テレフタレートを担体樹脂とし、そのメルトフローレートは5 g/10minであり、酸価は15未満である。前記ポリ乳酸のメルトフローレートは2.5 g/10minである。 Among them, the polyadipate/terephthalate is used as a carrier resin, the melt flow rate is 5 g/10 min, and the acid value is less than 15. The melt flow rate of the polylactic acid is 2.5 g/10 min.
前記超薄超透明型明完全生分解性フィルムブロー成形フィルム級材料の製造方法は以下の通りである: The method for producing the ultra-thin ultra-transparent bright fully biodegradable film blow molded film grade material is as follows:
ポリアジペート/テレフタレート、ポリ乳酸、超薄超透明型完全生分解性フィルム用増強増靭増透マスターバッチを高速ミキサーに入れ、700〜1000r/minの速度で5〜8分間撹拌して、上述した均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を得る。 The polyadipate/terephthalate, polylactic acid, and the ultra-thin ultra-transparent enhanced bioreinforcing film-reinforced masterbatch were placed in a high-speed mixer and stirred at a speed of 700 to 1000 r/min for 5 to 8 minutes, and then the above-mentioned process was performed. The uniformly mixed mixture is put into a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated to obtain an ultrathin ultra-transparent completely biodegradable film blow-molded film grade material.
本実施例によって提供される超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を用いて、5±1μmのフィルム製品を成形することができ、常温で直射日光を避けて12ヶ月間保存した場合、機械物性において大きな変化はない。引張強度は30MPaであり、縦方向及び横方向の延伸倍率は合計900%を超えている。 Using the ultra-thin ultra-transparent type fully biodegradable film blow-molded film grade material provided by this example, a film product of 5±1 μm can be molded and stored at room temperature for 12 months while avoiding direct sunlight. When it does, there is no significant change in mechanical properties. The tensile strength is 30 MPa, and the stretching ratio in the machine direction and the transverse direction exceeds 900% in total.
(実施例2)
超薄型完全生分解性フィルム用増強増靭増透マスターバッチの成分は、重量部で計算すると、以下の通りである。
ポリアジペート/テレフタレート 69重量部
疎水性ナノシリカ(粒径5〜10nm) 10重量部
Aike CE〜AZ01 10重量部
シリカミクロスフェア(粒径2〜3μm) 10重量部
エポキシ化大豆油 0.5重量部
有機シリコーン拡散油 0.5重量部
(Example 2)
The components of the enhanced toughening and transparent masterbatch for ultrathin completely biodegradable film are as follows, calculated in parts by weight.
Polyadipate/terephthalate 69 parts by weight Hydrophobic nanosilica (particle size 5-10 nm) 10 parts by weight Aike CE-AZ01 10 parts by weight Silica microspheres (particle size 2-3 μm) 10 parts by weight Epoxidized soybean oil 0.5 parts by weight Organic Silicone diffusion oil 0.5 parts by weight
以下の工程により製造して得られる。
疎水性ナノシリカ、エポキシ化大豆油及び有機シリコーン拡散油を四塩化炭素に溶解して分散させ、均一に撹拌し、四塩化炭素を蒸留して混合物1を得て、混合物1、ポリアジペート/テレフタレート及びポAike CE〜AZ01、シリカミクロスフェアを高速ミキサーに順次に入れ、700〜1000r/minの速度で10〜30分間混錬して混合物2を得て、混合物2を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る。
It is produced by the following steps.
Hydrophobic nanosilica, epoxidized soybean oil and organic silicone diffusion oil are dissolved and dispersed in carbon tetrachloride, stirred uniformly, carbon tetrachloride is distilled to obtain mixture 1, and mixture 1, polyadipate/terephthalate and PO Aike CE to AZ01 and silica microspheres were sequentially put into a high speed mixer and kneaded at a speed of 700 to 1000 r/min for 10 to 30 minutes to obtain a mixture 2, and the mixture 2 was put in a twin-screw extruder and put in a tube. It is extruded under the condition of ~160°C, air-cooled and granulated to obtain an ultra-thin fully biodegradable film enhanced toughening and transparent masterbatch.
当該マスターバッチを応用して超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を製造する。重量部で計算すると、主な成分として、
ポリアジペート/テレフタレート85重量部、ポリ乳酸10重量部、超薄超透明型完全生分解性フィルム用増強増靭増透マスターバッチ5重量部を含む。
The masterbatch is applied to produce an ultrathin ultratransparent fully biodegradable film blow-molded film grade material. When calculated in parts by weight, as the main ingredients,
Includes 85 parts by weight of polyadipate/terephthalate, 10 parts by weight of polylactic acid, and 5 parts by weight of masterbatch for strengthening/toughening/transparency for ultra-thin ultra-transparent completely biodegradable film.
そのうち、前記ポリアジペート/テレフタレートを担体樹脂とし、そのメルトフローレートは5 g/10minであり、酸価は15未満である。前記ポリ乳酸のメルトフローレートは2.5 g/10minである。 Among them, the polyadipate/terephthalate is used as a carrier resin, the melt flow rate is 5 g/10 min, and the acid value is less than 15. The melt flow rate of the polylactic acid is 2.5 g/10 min.
前記超薄超透明型完全生分解性フィルムブロー成形フィルム級材料の製造方法は以下の通りである。
ポリアジペート/テレフタレート、ポリ乳酸、超薄超透明型明完全生分解性フィルム用増強増靭増透マスターバッチを高速ミキサーに入れ、700〜1000r/minの速度で5〜8分間攪拌して、上述した均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を得る。
The method for producing the ultra-thin ultra-transparent completely biodegradable film blow-molded film grade material is as follows.
The polyadipate/terephthalate, polylactic acid, and the ultra-thin ultra-transparent, bright and completely biodegradable film enhanced and toughening/transparent masterbatch were put into a high-speed mixer, and the mixture was stirred at a speed of 700 to 1000 r/min for 5 to 8 minutes, and The uniformly mixed mixture was put in a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated to obtain an ultrathin ultra-transparent completely biodegradable film blow-molded film grade material. ..
本実施例によって提供される超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を用いて、5±1μmのフィルム製品を成形することができる。常温で直射日光を避けて12ヶ月間保存した場合、機械物性において変化はない。引張強度は35MPaであり、縦、横方向の延伸倍率は合計800%を超えている。 The ultra-thin ultra-transparent fully biodegradable film blow molded film grade material provided by this example can be used to mold film products of 5±1 μm. There is no change in mechanical properties when stored at room temperature for 12 months while avoiding direct sunlight. The tensile strength is 35 MPa, and the stretching ratio in the longitudinal and transverse directions exceeds 800% in total.
(実施例3)
超薄型完全生分解性フィルム用増強増靭増透マスターバッチの成分は、重量部で計算すると、以下の通りである。
ポリアジペート/テレフタレート 68重量部
疎水性ナノシリカ(粒径10〜20nm) 15重量部
Arkema AX〜8900 5重量部
シリカミクロスフェア(粒径1μm) 5重量部
有機シリコーン拡散油 2重量部
(Example 3)
The components of the enhanced toughening and transparent masterbatch for ultrathin completely biodegradable film are as follows, calculated in parts by weight.
Polyadipate/terephthalate 68 parts by weight Hydrophobic nanosilica (particle size 10 to 20 nm) 15 parts by weight Arkema AX-8900 5 parts by weight Silica microspheres (particle size 1 μm) 5 parts by weight Organic silicone diffusion oil 2 parts by weight
以下の工程により製造して得られる。
疎水性ナノシリカ及び有機シリコーン拡散油を四塩化炭素に溶解して分散させ、均一に撹拌し、四塩化炭素を蒸留して混合物1を得て、混合物1、ポリアジペート/テレフタレート及びポArkema AX〜8900、シリカミクロスフェアを高速ミキサーに順次に入れ、700〜1000r/minの速度で10〜30分間混錬して混合物2を得て、混合物2を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る。
It is produced by the following steps.
Hydrophobic nanosilica and organosilicone diffusion oil are dissolved and dispersed in carbon tetrachloride, stirred uniformly, carbon tetrachloride is distilled to obtain mixture 1, mixture 1, polyadipate/terephthalate and poly Arkema AX-8900. , Silica microspheres were sequentially put into a high-speed mixer, and kneaded at a speed of 700 to 1000 r/min for 10 to 30 minutes to obtain a mixture 2, and the mixture 2 was put into a twin-screw extruder and heated at a temperature of 135 to 160°C. Under high pressure, air-cooled and granulated to obtain an enhanced thinness toughening and transparency masterbatch for ultrathin fully biodegradable film.
当該マスターバッチを用いて超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を製造する。重量部で計算すると、主要成分として、
ポリアジペート/テレフタレート90重量部、ポリ乳酸5重量部、超薄超透明型完全生分解性フィルム用増強増靭増透マスターバッチ5重量部を含む。
The masterbatch is used to produce an ultrathin ultratransparent fully biodegradable film blow molded film grade material. When calculated in parts by weight, as the main component,
Includes 90 parts by weight of polyadipate/terephthalate, 5 parts by weight of polylactic acid, and 5 parts by weight of masterbatch for strengthening/toughening/permeation for ultra-thin ultra-transparent completely biodegradable film.
そのうち、前記ポリアジペート/テレフタレートを担体樹脂とし、そのメルトフローレートは5 g/10minである。前記ポリ乳酸のメルトフローレートは2.5 g/10minである。 Among them, the polyadipate/terephthalate is used as a carrier resin, and its melt flow rate is 5 g/10 min. The melt flow rate of the polylactic acid is 2.5 g/10 min.
前記超薄超透明型完全生分解性フィルムブロー成形フィルム級材料の製造方法は以下の通りである。
ポリアジペート/テレフタレート、ポリ乳酸、超薄超透明型完全生分解性フィルム用増強増靭増透マスターバッチを高速ミキサーに入れ、700〜1000r/minの速度で5〜8分間撹拌して、上述した均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を得る。
The method for producing the ultra-thin ultra-transparent completely biodegradable film blow-molded film grade material is as follows.
The polyadipate/terephthalate, polylactic acid, and the ultra-thin ultra-transparent enhanced bioreinforcing film-reinforced masterbatch were placed in a high-speed mixer and stirred at a speed of 700 to 1000 r/min for 5 to 8 minutes, and then the above-mentioned process was performed. The uniformly mixed mixture is put into a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated to obtain an ultrathin ultra-transparent completely biodegradable film blow-molded film grade material.
本実施例によって提供される超薄超透明型完全生分解性フィルムブロー成形フィルム級材料を用いて、5±1μmのフィルム製品を成形することができる。常温で直射日光を避けて12ヶ月間保存した場合、機械物性において変化はない;引張強度は28MPAであり;縦、横方向の延伸倍率は合計750%を超えている。 The ultra-thin ultra-transparent fully biodegradable film blow molded film grade material provided by this example can be used to mold film products of 5±1 μm. There is no change in the mechanical properties when stored at room temperature for 12 months while avoiding direct sunlight; the tensile strength is 28MPA; the stretching ratio in the longitudinal and transverse directions exceeds 750% in total.
(実施例4)
上述した実施例1で得られた超薄型完全生分解性フィルム用増強増靭増透マスターバッチを超薄型フィルムのブロー成形に応用する場合、二種類の添加方法がある。その一つは、マスターバッチを超薄型フィルム成分の1〜20重量%でブロー成形材料と直接に混合し、ブロー成形機に入れ押出して成形する。もう一つは、マスターバッチを超薄型フィルム成分の1〜20重量%で他の成分と一緒に混合して造粒して、ブロー成形機に入れて押出してブロー成形する方法である。
(Example 4)
In the case of applying the enhanced toughening and transparent masterbatch for the ultrathin completely biodegradable film obtained in Example 1 described above to the blow molding of the ultrathin film, there are two types of addition methods. In one, the masterbatch is directly mixed with a blow molding material in an amount of 1 to 20% by weight of an ultrathin film component, put into a blow molding machine and extruded and molded. The other is a method in which the masterbatch is mixed with 1 to 20% by weight of the ultrathin film component together with other components, granulated, put into a blow molding machine, and extruded to be blow molded.
(応用実施例1)
成分及び添加量(重量部)
PBAT 90重量部
PLA 5重量部
実施例1で製造された超薄型完全生分解性フィルム用増強増靭増透マスターバッチ
5重量部
(Application Example 1)
Ingredients and amount added (parts by weight)
PBAT 90 parts by weight PLA 5 parts by weight Enhanced super-tough and translucent masterbatch for ultra-thin fully biodegradable film produced in Example 1
5 parts by weight
製造工程は、上述の調合方法で各原材料の重量を計り、高速ミキサーに入れ5分間撹拌することである。均一に混合した後、二軸押出機で押出して造粒する。混合物をブロー成形機のホッパーに入れ、均一な円筒形フィルム(厚みが4〜6μmであればいい)にブロー成形し、切断、巻取りして超薄型完全生分解性フィルムを製造する。 The manufacturing process is to weigh each raw material by the above-mentioned blending method, put it in a high speed mixer, and stir for 5 minutes. After uniformly mixing, the mixture is extruded by a twin-screw extruder and granulated. The mixture is put in a hopper of a blow molding machine, blow-molded into a uniform cylindrical film (having a thickness of 4 to 6 μm), cut and wound to produce an ultrathin completely biodegradable film.
(応用実施例2)
成分及び添加量(重量部)
PBAT 92重量部
PPC 5重量部
実施例1で製造された超薄型完全生分解性フィルム用増強増靭増透マスターバッチ
3重量部
(Application Example 2)
Ingredients and amount added (parts by weight)
PBAT 92 parts by weight PPC 5 parts by weight Enhanced thinning and strengthening transparency masterbatch for the ultrathin fully biodegradable film produced in Example 1
3 parts by weight
製造工程は、上述の調合方法で各原材料の重量を計り、高速ミキサーに入れ5分間撹拌することである。均一に混合した後、混合物をブロー成形機のホッパーに入れ、均一な円筒形フイルム(厚みが4〜6μmであればいい)にブロー成形させ、切断、巻取りして超薄型完全生分解性フィルムを製造する。 The manufacturing process is to weigh each raw material by the above-mentioned blending method, put it in a high speed mixer, and stir for 5 minutes. After mixing evenly, put the mixture in the hopper of blow molding machine, blow mold into a uniform cylindrical film (if the thickness is 4 to 6 μm), cut and wind to obtain ultrathin complete biodegradability. Produce a film.
GB/T1040.3プラスチック引張特性の測定の第3部分:フィルム及びシートの試験の条件は、引張速度を200mm/minとし、得られたフィルムの各特性は下記の表に示す通りである。比較例は同等樹脂を採用し、超薄型完全生分解性フィルム用増強増靭増透マスターバッチを添加せずに製造したフィルムである。 GB/T1040.3 Third Part of Plastic Tensile Property Measurements: The conditions for testing films and sheets were a pulling speed of 200 mm/min, and the properties of the resulting films are as shown in the table below. The comparative example is a film produced by adopting an equivalent resin and adding no strengthening/toughening/transparency masterbatch for an ultrathin completely biodegradable film.
以上から確認できるように、本発明によって製造された超薄型完全生分解性フィルム用増強増靭増透マスターバッチを用いて製造した超薄型完全生分解性フィルムは、透光率、引張強度及び引裂延伸率が厚みの大きい完全生分解性フィルムより優秀で、良好な加工性も有している。 As can be confirmed from the above, the ultrathin fully biodegradable film produced by using the enhanced thinning/toughening/transparency masterbatch for the ultrathin fully biodegradable film produced by the present invention has a light transmittance and a tensile strength. In addition, the tear stretch ratio is superior to that of a fully biodegradable film having a large thickness, and also has good processability.
(実施例5)
GB/T1040.3プラスチック引張特性の測定の第3部分である。フィルム及びシートの試験の条件は、引張速度を200mm/minとし、実施例1〜3においてそれぞれのブロー成形フィルム級材料を用いて得られたフィルムの各特性は下記の表に示す通りである。
比較例は同じ厚みのLLDPEフィルムである。
(Example 5)
GB/T 1040.3 This is the third part of the measurement of plastic tensile properties. The conditions of the film and sheet test are as follows: the pulling speed is 200 mm/min, and the properties of the films obtained by using the blow-molded film grade materials in Examples 1 to 3 are as shown in the table below.
The comparative example is an LLDPE film having the same thickness.
以上から確認できるように、本発明によって製造されたブロー成形フィルム級材料を用いて成形した超薄型完全生分解性フィルムは、透光率がよく、引張強度及び引裂延伸率が同じ厚みのLLDPEフィルムより良く、PEフィルムを完全に代替できる。そして良好な加工性能も有しており、かつ特殊な加工設備で製造する必要もない。本発明の樹脂を用いて製造されるフィルム製品は常温において安定性がよく、直射日光を避けて12ヶ月も保存でき、機械特性が優れており、フィルム包装、買い物袋、ゴミ分別埋立、堆肥作り処理など広く活用できる。 As can be confirmed from the above, the ultrathin completely biodegradable film formed by using the blow-molded film grade material produced according to the present invention has good light transmittance, and has the same tensile strength and tear stretch ratio as LLDPE. Better than film, it can completely replace PE film. It also has good processing performance and does not need to be manufactured with special processing equipment. The film products manufactured using the resin of the present invention have good stability at room temperature, can be stored for 12 months without direct sunlight, and have excellent mechanical properties. They are film packaging, shopping bags, waste landfills, and composting. Can be widely used for processing.
(実施例7)
超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチの成分は、重量部で計算すると、以下の通りである。
ポリアジペート/テレフタレート 67重量部
ポリ乳酸 1重量部
疎水性ナノシリカ(粒径5〜10nm) 20重量部
ポリマーPMMAミクロスフェア(粒径2〜3μm) 10重量部
エポキシ化大豆油 2重量部
紫外線吸収剤Tinuvin 234 1重量部
(Example 7)
The components of the enhanced toughening and transparent masterbatch for ultrathin fully biodegradable mulch film are as follows, calculated in parts by weight.
Polyadipate/terephthalate 67 parts by weight Polylactic acid 1 part by weight Hydrophobic nanosilica (particle size 5-10 nm) 20 parts by weight Polymer PMMA microspheres (particle size 2-3 μm) 10 parts by weight Epoxidized soybean oil 2 parts by weight UV absorber Tinuvin 234 1 part by weight
以下の工程により製造して得られる。
疎水性ナノシリカ及びエポキシ化大豆油を四塩化炭素に溶解して分散させ、均一に撹拌し、四塩化炭素を蒸留して混合物1を得て、混合物1、ポリアジペート/テレフタレート、ポリ乳酸、紫外線吸収剤Tinuvin 234及びポリマーPMMAミクロスフェアを高速ミキサーに順次に入れ、700〜1000r/minの速度で10〜30分間混錬して混合物2を得て、混合物2を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを得る。
It is produced by the following steps.
Hydrophobic nanosilica and epoxidized soybean oil are dissolved and dispersed in carbon tetrachloride, stirred uniformly, carbon tetrachloride is distilled to obtain mixture 1, and mixture 1, polyadipate/terephthalate, polylactic acid, UV absorption The agent Tinuvin 234 and the polymer PMMA microspheres were sequentially charged into a high-speed mixer and kneaded at a speed of 700 to 1000 r/min for 10 to 30 minutes to obtain a mixture 2, and the mixture 2 was put into a twin-screw extruder and heated to 135-135. It is extruded under the condition of 160° C., air-cooled and granulated to obtain an ultra-thin fully biodegradable reinforced multi-film enhanced toughening and transparent masterbatch.
(実施例8)
超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチの成分は、重量部で計算すると、以下の通りである。
ポリアジペート/テレフタレート 69重量部
ポリ乳酸 10重量部
疎水性ナノシリカ(粒径15〜25nm) 10重量部
Aike CE〜AZ01 10重量部
シリカミクロスフェア(粒径2〜3μm) 5重量部
有機シリコーン拡散油 1重量部
紫外線吸収剤Tinuvin 234 2.5重量部
紫外線安定剤Uvinul(登録商標) 5050H 2.5重量部
(Example 8)
The components of the enhanced toughening and transparent masterbatch for ultrathin fully biodegradable mulch film are as follows, calculated in parts by weight.
Polyadipate/terephthalate 69 parts by weight Polylactic acid 10 parts by weight Hydrophobic nanosilica (particle size 15 to 25 nm) 10 parts by weight Aike CE-AZ01 10 parts by weight Silica microspheres (particle size 2 to 3 μm) 5 parts by weight Organic silicone diffusion oil 1 Parts by weight UV absorber Tinuvin 234 2.5 parts by weight UV stabilizer Uvinul® 5050H 2.5 parts by weight
以下の工程により製造して得られる。
疎水性ナノシリカ及び有機シリコーン拡散油を四塩化炭素に溶解して分散させ、均一に撹拌し、四塩化炭素を蒸留して混合物1を得て、混合物1、ポリアジペート/テレフタレート、ポリ乳酸、Aike CE〜AZ01、紫外線吸収剤Tinuvin 234、紫外線安定剤Uvinul(登録商標) 5050H及びシリカミクロスフェアを高速ミキサーに順次に入れ、700〜1000r/minの速度で10〜30分間撹拌して混錬して混合物2を得て、混合物2を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを得る。
It is produced by the following steps.
Hydrophobic nanosilica and organic silicone diffusion oil are dissolved and dispersed in carbon tetrachloride, uniformly stirred, carbon tetrachloride is distilled to obtain mixture 1, and mixture 1, polyadipate/terephthalate, polylactic acid, Aike CE ~AZ01, UV absorber Tinuvin 234, UV stabilizer Uvinul (registered trademark) 5050H, and silica microspheres are sequentially put into a high-speed mixer, and stirred and kneaded at a speed of 700 to 1000 r/min for 10 to 30 minutes to obtain a mixture. 2, the mixture 2 was put into a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated, and an ultrathin fully biodegradable multi-film enhanced toughening and transparency master. Get a batch.
(実施例9)
超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチの成分は、重量部で計算すると、以下の通りである。
ポリアジペート/テレフタレート 85重量部
ポリ乳酸 20重量部
疎水性ナノシリカ(粒径10〜20nm) 10重量部
Arkema AX〜8900 10重量部
シリカミクロスフェア(粒径1μm) 1重量部
紫外線安定剤Uvinul(登録商標) 5050H 2.5重量部
有機シリコーン拡散油 1.5重量部
(Example 9)
The components of the enhanced toughening and transparent masterbatch for ultrathin fully biodegradable mulch film are as follows, calculated in parts by weight.
Polyadipate/terephthalate 85 parts by weight Polylactic acid 20 parts by weight Hydrophobic nanosilica (particle size 10 to 20 nm) 10 parts by weight Arkema AX-8900 10 parts by weight Silica microspheres (particle size 1 μm) 1 part by weight UV stabilizer Uvinul (registered trademark) ) 5050H 2.5 parts by weight Organic silicone diffusion oil 1.5 parts by weight
以下のように製造して得られる。
疎水性ナノシリカ及び有機シリコーン拡散油を四塩化炭素に溶解して分散させ、均一に撹拌し、四塩化炭素を蒸留して混合物1を得て、混合物1、ポリアジペート/テレフタレート、紫外線安定剤Uvinul(登録商標) 5050H 、Arkema AX〜8900及びシリカミクロスフェアを高速ミキサーに順次に入れ、700〜1000r/minの速度で10〜30分間撹拌して混錬して混合物2を得て、混合物2を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して、超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを得る。
It is obtained by manufacturing as follows.
Hydrophobic nanosilica and organic silicone diffusion oil are dissolved and dispersed in carbon tetrachloride, uniformly stirred, carbon tetrachloride is distilled to obtain mixture 1, and mixture 1, polyadipate/terephthalate, UV stabilizer Uvinul( (Registered trademark) 5050H, Arkema AX-8900 and silica microspheres are sequentially put in a high-speed mixer, stirred at a speed of 700-1000 r/min for 10-30 minutes to knead to obtain a mixture 2, and a mixture 2 is mixed. It is put into a shaft extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated to obtain an ultrathin fully biodegradable reinforced multi-film enhanced toughening and transparent masterbatch.
(実施例10)
本発明の超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを超薄型マルチフィルムのブロー成形に使用されるのには、主に二種類の添加方法がある。その一つはマスターバッチを超薄型マルチフィルム成分の1〜5重量%でブロー成形フィルム級材料と直接混合し、ブロー成形機に入れ押出して成形する。もう一つはマスターバッチを超薄型マルチフィルム成分の1〜5重量%で他の成分とともに混合して造粒された後、ブロー成形機に入れて押出して成形する。
(Example 10)
There are mainly two types of addition methods for using the ultrathin fully biodegradable multi-film enhanced and toughening/permeable masterbatch of the present invention for blow molding of ultra-thin multi-film. One is to directly mix the masterbatch with blow-molded film grade material at 1 to 5% by weight of the ultrathin mulch film component, put it in a blow molding machine and extrude it. The other is to mix the masterbatch with other components in an amount of 1 to 5% by weight of the ultrathin mulch film component and granulate it, and then put it into a blow molding machine and extrude it.
(応用実施例3)
成分及び量(重量部)
PBAT 90重量部
PLA 5重量部
実施例7で製造された超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチ 5重量部
(Application Example 3)
Ingredients and amounts (parts by weight)
90 parts by weight of PBAT 5 parts by weight of PLA 5 parts by weight of masterbatch with enhanced toughness and transparency for ultra-thin fully biodegradable mulch film manufactured in Example 7
製造工程は、上述の調合方法で各原材料の重量を計り、高速ミキサーに入れて5分間撹拌することである。均一に混合した後、二軸押出機で押出して造粒する。混合物をブロー成形機のホッパーに入れ、均一な円筒形マルチフィルム(厚みが4〜5μmであればいい)にブロー成形し、切断、巻取りして超薄型完全生分解性マルチフィルムを製造して得る。 The manufacturing process is to weigh each raw material by the above-mentioned blending method, put it in a high speed mixer, and stir for 5 minutes. After uniformly mixing, the mixture is extruded by a twin-screw extruder and granulated. The mixture is placed in the hopper of a blow molding machine, blow molded into a uniform cylindrical mulch film (if the thickness is 4-5 μm), cut and wound to produce an ultrathin fully biodegradable mulch film. Get it.
(応用実施例4)
成分及び添加量(重量部)
PBAT 92重量部
PPC 5重量部
実施例7で製造された超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチ 3重量部
(Application Example 4)
Ingredients and amount added (parts by weight)
92 parts by weight of PBAT 5 parts by weight of PPC 3 parts by weight of masterbatch with enhanced toughness and transparency for ultra-thin fully biodegradable mulch film manufactured in Example 7
製造工程は、上述の調合方法で各原材料の重量を計り、高速ミキサーに入れて5分間撹拌することである。均一に混合した後、混合物をブロー成形機のホッパーに入れ、均一な円筒形マルチフィルム(厚みが4〜5μmであればいい、幅90〜200cmであればいい)にブロー成形し、切断、巻取りして超薄型完全生分解性マルチフィルムを製造して得る。 The manufacturing process is to weigh each raw material by the above-mentioned blending method, put it in a high speed mixer, and stir for 5 minutes. After uniformly mixing, the mixture is put into a hopper of a blow molding machine, blow-molded into a uniform cylindrical multi-film (having a thickness of 4 to 5 μm, a width of 90 to 200 cm), cutting and winding. Obtained by taking ultra thin thin biodegradable mulch film.
GB/T1040.3プラスチッチク引張特性の測定の第3部分:フィルム及びシートの試験の条件は、引張速度を200mm/minとし、得られたフィルムの各特性は下記の表に示す通りである。比較例は同等樹脂を採用し、超薄型完全生分解性フマルチィルム用増強増靭増透マスターバッチを添加せず製造されたマルチフィルムである。 GB/T1040.3 PLASTICHIK THICK PATTERN 3rd Part of Measurement of Tensile Properties: The conditions of the film and sheet tests were a tensile speed of 200 mm/min, and the respective properties of the obtained film are as shown in the table below. The comparative example is a mulch film produced by using an equivalent resin and adding no masterbatch for enhancing toughness and transparency for ultrathin completely biodegradable films.
以上から確認できるように、本発明によって製造された超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを用いて製造した超薄型完全生分解性マルチフィルムは、透光率、引張強度及び引裂延伸率が厚みの高い完全生分解性マルチフィルムより優秀であるとともに、良好な加工性も有している。 As can be confirmed from the above, the ultrathin fully biodegradable mulch film produced by using the ultra-thin fully biodegradable mulch film enhanced strengthening/transparency masterbatch produced by the present invention has a light transmittance, It has superior tensile strength and tear draw ratio to the fully biodegradable mulch film with high thickness, and also has good processability.
Claims (10)
重量部で計算すると、主な成分として、ポリアジペート/テレフタレート65〜88重量部、増強増靭増透剤10〜20重量部を含む、
ことを特徴とする増強増靭増透マスターバッチ。 An enhanced toughening and transparent masterbatch,
When calculated in terms of parts by weight, the main components include polyadipate/terephthalate 65 to 88 parts by weight and an enhanced toughening/thickening agent 10 to 20 parts by weight.
An enhanced toughening and transparent masterbatch characterized by the following.
ことを特徴とする請求項1に記載の増強増靭増透マスターバッチ。 The melt flow rate of the polyadipate/terephthalate is 2 to 5 g/10 min, the acid value is less than 15, and the enhanced toughening agent is an inorganic enhanced toughening agent or an organic enhanced toughening agent. One or more of
The enhanced toughening and transparent masterbatch according to claim 1, wherein
ことを特徴とする請求項1に記載の増強増靭増透マスターバッチ。 The inorganic enhanced toughening agent is selected from hydrophobic nanosilica, the particle size of the hydrophobic nanosilica is 5 to 25 nmx, and the organic enhanced toughening agent is Arkema AX-8900, ADX to 1200s resin compatibilization. Agent or one or more of Hangzhou Aike CE to AZ01 compatibilizer,
The enhanced toughening and transparent masterbatch according to claim 1, wherein
主な成分として、ポリアジペート/テレフタレート65〜88重量部、増強増靭増透剤10〜20重量部、潤滑剤0.5〜30重量部、分散剤1〜5重量部を含み、
前記ポリアジペート/テレフタレートのメルトフローレートは2〜5 g/10minであり、酸価は15未満であり、前記潤滑剤はポリマーPMMAミクロスフェア又はシリカミクロスフェアのうちの1種又は2種であり、前記分散剤はエポキシ化大豆油又は有機シリコーン類拡散オイルから選択される1種又は2種である、
ことを特徴とする超薄型完全生分解性フィルム用増強増靭増透マスターバッチ。 A masterbatch with enhanced toughness and transparency for ultra-thin fully biodegradable film,
Main components include 65 to 88 parts by weight of polyadipate/terephthalate, 10 to 20 parts by weight of reinforcing and toughening agent, 0.5 to 30 parts by weight of lubricant, and 1 to 5 parts by weight of dispersant,
The melt flow rate of the polyadipate/terephthalate is 2-5 g/10 min, the acid value is less than 15, and the lubricant is one or two of polymer PMMA microspheres or silica microspheres, The dispersant is one or two selected from epoxidized soybean oil or organic silicone diffusion oil,
A masterbatch with enhanced toughness and transparency for ultra-thin completely biodegradable films.
所定量の増強増靭増透剤と分散剤を四塩化炭素に溶解して分散させ、均一に攪拌した後、四塩化炭素を蒸留して混合物を得る工程(1)と、
工程(1)から得られた混合物、ポリアジペート/ブチレンテレフタレート、潤滑剤を重量部で順次に高速ミキサーに入れ、10〜30分間混練する工程(2)と、
工程(2)から得られた均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して超薄型完全生分解性フィルム用増強増靭増透マスターバッチを得る工程(3)と、を含む、
ことを特徴とする超薄型完全生分解性フィルム用増強増靭増透マスターバッチの製造方法。 A method for producing an enhanced toughening and transparent masterbatch for an ultra-thin completely biodegradable film,
A step (1) of dissolving a predetermined amount of a strengthening/toughening agent and a dispersant in carbon tetrachloride to disperse and uniformly stirring, and distilling carbon tetrachloride to obtain a mixture;
A step (2) in which the mixture obtained from the step (1), polyadipate/butylene terephthalate, and a lubricant are sequentially put in a high-speed mixer in parts by weight and kneaded for 10 to 30 minutes;
The homogeneously mixed mixture obtained from the step (2) is put into a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated to enhance the ultrathin completely biodegradable film. A step (3) of obtaining a toughening and transparent masterbatch,
A method for producing an enhanced toughening and transparent masterbatch for an ultra-thin completely biodegradable film, which is characterized by the above.
重量部で計算すると、主な成分としてポリアジペート/テレフタレート65〜85重量部、ポリ乳酸1〜20重量部、増強増靭増透剤10〜20重量部、潤滑剤0.5〜30重量部、分散剤1〜5重量部、安定剤1〜5重量部を含み、
前記ポリアジペート/テレフタレートのメルトフローレートは2〜5 g/10minであり、酸価は15未満であり、前記ポリ乳酸のメルトフローレートは2〜5 g/10minであり、酸価は15未満であり、前記潤滑剤はポリマーPMMAミクロスフェア又はシリカミクロスフェアの1種又は2種であり、前記分散剤はエポキシ化大豆油又は有機シリコーン類拡散オイルから選択される1種又は2種であり、前記安定剤は紫外線吸収剤又は紫外線安定剤のうちの1種又は2種である、
ことを特徴とする超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチ。 An ultra-thin fully biodegradable multi-film enhanced toughening and transparent masterbatch,
When calculated in terms of parts by weight, the main components are polyadipate/terephthalate 65 to 85 parts by weight, polylactic acid 1 to 20 parts by weight, an enhanced toughening and transparent agent 10 to 20 parts by weight, a lubricant 0.5 to 30 parts by weight, 1 to 5 parts by weight of a dispersant and 1 to 5 parts by weight of a stabilizer,
The polyadipate/terephthalate has a melt flow rate of 2 to 5 g/10 min and an acid value of less than 15, and the polylactic acid has a melt flow rate of 2 to 5 g/10 min and an acid value of less than 15. And the lubricant is one or two of polymer PMMA microspheres or silica microspheres, and the dispersant is one or two selected from epoxidized soybean oil or organic silicone diffusion oil, and The stabilizer is one or two of an ultraviolet absorber or an ultraviolet stabilizer,
An ultra-thin fully biodegradable multi-film enhanced and toughened and transparent masterbatch.
ことを特徴とする請求項6に記載の超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチ。 The UV absorber is a low-volatile benzotriazole-based UV absorber Tinuvin 234, and the UV stabilizer is a sterically hindered amine stabilizer Uvinul® 5050H,
The enhanced thinning/toughening/transparency masterbatch for an ultrathin completely biodegradable mulch film according to claim 6.
所定量の増強増靭増透剤と分散剤を四塩化炭素に溶解し分散させ、均一に攪拌した後、四塩化炭素を蒸留して混合物を得る工程(1)と
工程(1)から得られた混合物、ポリアジペート/ブチレンテレフタレート、ポリ乳酸、安定剤、潤滑剤を順次に重量部で高速ミキサーに加え、700〜1000r/minの速度で10〜30分間撹拌して混練する工程(2)と、
工程(2)から得られた均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチを得る工程(3)と、を含む、
ことを特徴とする超薄型完全生分解性マルチフィルム用増強増靭増透マスターバッチの製造方法。 A method for producing an enhanced toughening and transparent masterbatch for ultrathin completely biodegradable mulch film,
Obtained from step (1) and step (1) in which a predetermined amount of the strengthening/toughening agent and dispersant are dissolved and dispersed in carbon tetrachloride, and after uniformly stirring, carbon tetrachloride is distilled to obtain a mixture. And the step (2) in which the mixture, polyadipate/butylene terephthalate, polylactic acid, stabilizer and lubricant are sequentially added to a high-speed mixer in parts by weight and stirred at a speed of 700 to 1000 r/min for 10 to 30 minutes. ,
For the ultrathin fully biodegradable mulch film, put the uniformly mixed mixture obtained from step (2) into a twin-screw extruder, extrude under conditions of 135-160°C, air cool and granulate. And (3) obtaining an enhanced toughening and transparent masterbatch.
A method for producing a masterbatch having enhanced toughness and transparency for an ultra-thin completely biodegradable mulch film, which is characterized by the above.
重量部で計算すると、主な成分としてポリアジペート/テレフタレート80〜90重量部、ポリ乳酸0.5〜20重量部、超薄型完全生分解性フィルム用増強増靭増透マスターバッチ1〜5重量部を含み、
前記ポリアジペート/テレフタレートを担体樹脂とし、そのメルトフローレートは2〜5 g/10minであり、酸価は15未満であり、前記ポリ乳酸のメルトフローレートは2〜5 g/10minである、
ことを特徴とする超薄型完全生分解性フィルム用増強増靭増透マスターバッチを応用して製造される超薄超透明型完全生分解性フィルムブロー成形フィルム級材料超薄型。 An ultra-thin ultra-transparent fully biodegradable film blow molding film grade material manufactured by applying an enhanced toughening and transparency masterbatch for ultra-thin fully biodegradable film,
Calculated in parts by weight, the main components are polyadipate/terephthalate 80 to 90 parts by weight, polylactic acid 0.5 to 20 parts by weight, ultra-thin fully biodegradable film enhanced toughening and transparency masterbatch 1 to 5 parts by weight. Including parts,
The carrier resin is polyadipate/terephthalate, the melt flow rate is 2 to 5 g/10 min, the acid value is less than 15, and the melt flow rate of the polylactic acid is 2 to 5 g/10 min.
Ultra-thin ultra-transparent fully biodegradable film blow-molded film grade material manufactured by applying an enhanced toughening/transparency masterbatch for ultra-thin fully biodegradable film.
ポリアジペート/ブチレンテレフタレート、ポリ乳酸、超薄超透明型完全生分解性フィルム用増強増靭増透マスターバッチを高速ミキサーに入れ、700〜1000r/minの速度で5〜8分間撹拌する工程(1)と、
上述した均一に混合された混合物を二軸押出機に入れ、135〜160℃の条件の下で押出し、空冷にして造粒して得る工程(2)と、を含む、
ことを特徴とする超薄型完全生分解性フィルム用増強増靭増透マスターバッチを応用して製造される超薄超透明型完全生分解性フィルムブロー成形フィルム級材料の製造方法。 A method for producing an ultra-thin ultra-transparent fully biodegradable film blow-molded film grade material produced by applying an enhanced toughening and transparency masterbatch for ultrathin fully biodegradable film,
A step of adding polyadipate/butylene terephthalate, polylactic acid, and an ultra-thin ultra-transparent type fully enhanced biodegradable film enhanced toughening/transparency masterbatch into a high-speed mixer and stirring at a speed of 700 to 1000 r/min for 5 to 8 minutes (1 )When,
A step (2) in which the above-mentioned homogeneously mixed mixture is put into a twin-screw extruder, extruded under the condition of 135 to 160° C., air-cooled and granulated to obtain.
A method for producing an ultra-thin ultra-transparent fully biodegradable film blow-molded film grade material produced by applying an enhanced toughening/transparency masterbatch for an ultrathin fully biodegradable film.
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CN111040395B (en) * | 2019-05-24 | 2022-04-05 | 包头稀土研究院 | Reinforced and toughened composite material and preparation method thereof |
CN110964298A (en) * | 2019-12-20 | 2020-04-07 | 深圳市祥鸿辉科技有限公司 | Biodegradable modified material and preparation method thereof |
CN111138812B (en) * | 2019-12-31 | 2022-08-26 | 中国科学院理化技术研究所 | Ultrathin degradable mulching film special for beets and preparation method thereof |
CN111534066B (en) * | 2020-05-13 | 2022-07-05 | 江西广源新材料有限公司 | Functional master batch for reinforcing and toughening polylactic acid fiber, preparation method thereof and reinforcing and toughening polylactic acid material |
CN111647183A (en) * | 2020-06-22 | 2020-09-11 | 浙江理工大学 | Preparation method of inorganic micropowder/PBAT full-degradable composite film |
CN112662147A (en) * | 2020-12-23 | 2021-04-16 | 青岛润兴塑料新材料有限公司 | High-performance ternary compound biodegradable film |
CN112900149B (en) * | 2021-01-16 | 2022-07-12 | 北京金印联国际供应链管理有限公司 | White cardboard for food packaging and production process thereof |
CN113843999B (en) * | 2021-09-26 | 2023-07-04 | 中国科学技术大学先进技术研究院 | Preparation method of poly (adipic acid)/poly (butylene terephthalate) film |
CN114031904A (en) * | 2021-12-03 | 2022-02-11 | 辽宁东盛塑业有限公司 | Antibacterial modified atmosphere preservation degradable fruit net cover and preparation method thereof |
CN114381100A (en) * | 2021-12-24 | 2022-04-22 | 贵州省材料产业技术研究院 | Flame-retardant toughening modified polylactic acid composite material and preparation method thereof |
CN115322533A (en) * | 2022-08-23 | 2022-11-11 | 康辉新材料科技有限公司 | Special polyester master batch for MLCC release film and preparation method thereof |
CN115584109B (en) * | 2022-11-08 | 2024-06-21 | 山东联欣环保科技有限公司 | Composite material, preparation method and application thereof, and degradable mulching film |
CN116239874B (en) * | 2023-02-24 | 2024-01-23 | 大禾科技发展(南京)有限公司 | Special hydrophobic biodegradable agricultural mulching film for rice as well as preparation method and application thereof |
CN116253911B (en) * | 2023-04-21 | 2023-10-24 | 海南师范大学 | Preparation method of ultrathin high-strength high-light-transmittance biodegradable food inner packaging film |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009221336A (en) * | 2008-03-14 | 2009-10-01 | Mitsubishi Chemicals Corp | Resin composition, and molded article and film comprising the resin composition |
JP2011522950A (en) * | 2008-06-13 | 2011-08-04 | ロケット・フルーレ | Starch-containing thermoplastic or elastomeric compositions and methods for preparing such compositions |
US20120107630A1 (en) * | 2009-06-26 | 2012-05-03 | Krishnaswamy Rajendra K | Branched Aliphatic-Aromatic Polyester Blends |
WO2013038770A1 (en) * | 2011-09-12 | 2013-03-21 | 東レ株式会社 | Film |
CN103756270A (en) * | 2013-12-31 | 2014-04-30 | 山东农业大学 | Full biodegrade mulch master batch as well as preparation method and application thereof |
CN104479304A (en) * | 2014-12-10 | 2015-04-01 | 金发科技股份有限公司 | Full-biodegradable composite as well as preparation method and application of full-biodegradable composite |
JP2017002253A (en) * | 2015-06-16 | 2017-01-05 | ユニチカ株式会社 | Polyester resin composition and molded body obtained by using the same |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103709631A (en) * | 2012-09-29 | 2014-04-09 | 青岛欣展塑胶有限公司 | Nanocomposite toughened and flame-retardant modified polybutylene terephthalate |
US10100159B2 (en) * | 2013-07-12 | 2018-10-16 | Polyone Corporation | Polyester compounds having enhanced hydrophobic surface properties |
CN104479301A (en) * | 2014-12-10 | 2015-04-01 | 金发科技股份有限公司 | Inorganic filler full-biodegradable composite as well as preparation method and application of inorganic filler full-biodegradable composite |
CN107365482B (en) * | 2017-07-13 | 2019-11-05 | 山东农业大学 | A kind of special reinforced toughened anti-reflection master batch of ultra-thin whole life cycle design |
CN107383796B (en) * | 2017-07-13 | 2019-11-05 | 山东农业大学 | A kind of special reinforced toughened anti-reflection master batch of ultra-thin full-biodegradable film and preparation method thereof |
CN107345053B (en) * | 2017-07-13 | 2019-11-05 | 山东农业大学 | Ultra-thin super transparent full-biodegradable film blown film grade material of one kind and preparation method thereof |
-
2018
- 2018-07-03 JP JP2019563811A patent/JP6942323B2/en active Active
- 2018-07-03 WO PCT/CN2018/094176 patent/WO2019011152A1/en active Application Filing
-
2019
- 2019-09-02 ZA ZA2019/05793A patent/ZA201905793B/en unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009221336A (en) * | 2008-03-14 | 2009-10-01 | Mitsubishi Chemicals Corp | Resin composition, and molded article and film comprising the resin composition |
JP2011522950A (en) * | 2008-06-13 | 2011-08-04 | ロケット・フルーレ | Starch-containing thermoplastic or elastomeric compositions and methods for preparing such compositions |
US20120107630A1 (en) * | 2009-06-26 | 2012-05-03 | Krishnaswamy Rajendra K | Branched Aliphatic-Aromatic Polyester Blends |
WO2013038770A1 (en) * | 2011-09-12 | 2013-03-21 | 東レ株式会社 | Film |
CN103756270A (en) * | 2013-12-31 | 2014-04-30 | 山东农业大学 | Full biodegrade mulch master batch as well as preparation method and application thereof |
CN104479304A (en) * | 2014-12-10 | 2015-04-01 | 金发科技股份有限公司 | Full-biodegradable composite as well as preparation method and application of full-biodegradable composite |
JP2017002253A (en) * | 2015-06-16 | 2017-01-05 | ユニチカ株式会社 | Polyester resin composition and molded body obtained by using the same |
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