JPH059345A - Production of polyolefinic resin molding - Google Patents
Production of polyolefinic resin moldingInfo
- Publication number
- JPH059345A JPH059345A JP26333291A JP26333291A JPH059345A JP H059345 A JPH059345 A JP H059345A JP 26333291 A JP26333291 A JP 26333291A JP 26333291 A JP26333291 A JP 26333291A JP H059345 A JPH059345 A JP H059345A
- Authority
- JP
- Japan
- Prior art keywords
- molding
- glyoxal
- density polyethylene
- present
- composition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000465 moulding Methods 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 229920005989 resin Polymers 0.000 title abstract description 9
- 239000011347 resin Substances 0.000 title abstract description 9
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000000203 mixture Substances 0.000 claims abstract description 16
- 229940015043 glyoxal Drugs 0.000 claims abstract description 15
- YLVACWCCJCZITJ-UHFFFAOYSA-N 1,4-dioxane-2,3-diol Chemical compound OC1OCCOC1O YLVACWCCJCZITJ-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229920005672 polyolefin resin Polymers 0.000 claims description 13
- 229920001684 low density polyethylene Polymers 0.000 claims description 5
- 239000004702 low-density polyethylene Substances 0.000 claims description 5
- 229920001903 high density polyethylene Polymers 0.000 claims description 4
- 239000004700 high-density polyethylene Substances 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 abstract 2
- 238000002844 melting Methods 0.000 abstract 2
- 238000004321 preservation Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 12
- -1 polyethylene Polymers 0.000 description 8
- 238000001125 extrusion Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 229920001577 copolymer Polymers 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 229920000098 polyolefin Polymers 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 229920005992 thermoplastic resin Polymers 0.000 description 5
- 230000003385 bacteriostatic effect Effects 0.000 description 4
- 239000002781 deodorant agent Substances 0.000 description 4
- 239000010813 municipal solid waste Substances 0.000 description 4
- 229920000728 polyester Polymers 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000004952 Polyamide Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 238000000071 blow moulding Methods 0.000 description 2
- 150000001735 carboxylic acids Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- 229920000554 ionomer Polymers 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 229920000092 linear low density polyethylene Polymers 0.000 description 2
- 239000004707 linear low-density polyethylene Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- 229920001083 polybutene Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000005033 polyvinylidene chloride Substances 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000004709 Chlorinated polyethylene Substances 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229930182556 Polyacetal Natural products 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229920006226 ethylene-acrylic acid Polymers 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000002538 fungal effect Effects 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920003225 polyurethane elastomer Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 150000003609 titanium compounds Chemical class 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、消臭性、静菌性更には
鮮度保持性等の機能が付与された、ポリオレフィン系樹
脂成型物の製造法を提供するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention provides a process for producing a polyolefin resin molded product having functions such as deodorant property, bacteriostatic property, and freshness-retaining property.
【0002】[0002]
【従来の技術】ポリエチレン、ポリプロピレン等のポリ
オレフィン系樹脂は良好な成型加工性をもち成型物の外
観、耐湿性、機械的性質が優れているのでフイルム、シ
ート、容器、繊維等の各種用途に多用されている。BACKGROUND OF THE INVENTION Polyolefin resins such as polyethylene and polypropylene have good molding processability and are excellent in the appearance, moisture resistance and mechanical properties of molded products, so they are widely used in various applications such as films, sheets, containers and fibers. Has been done.
【0003】[0003]
【発明が解決しようとする課題】しかしながらポリオレ
フィン系樹脂はその非極性な構造故に、消臭性、静菌
性、鮮度保持性等の多機能な性質に劣るため、ゴミ袋の
用途、酸化を受け変質し易い食品等への包装材として不
満足な点もある。However, due to its non-polar structure, polyolefin resins are inferior in multifunctional properties such as deodorant properties, bacteriostatic properties, and freshness-retaining properties, and are therefore subject to the use of garbage bags and oxidation. There are some unsatisfactory points as a packaging material for foods that are easily deteriorated.
【0004】従って、該樹脂に何等かの手段を用いてか
かる機能を付与出来れば、その利用価値は益々拡大する
こととなる。かかる対策として、ポリオレフィン系樹脂
にゼオライト等を配合することが行われているが、成型
物の透明性や溶融性を損なったり一長一短があり必ずし
も満足出来る物性が得られないのが実情である。Therefore, if such a function can be imparted to the resin by using some means, its utility value will be further expanded. As a countermeasure for this, a polyolefin or the like is blended with zeolite or the like, but the fact is that the transparency and meltability of the molded product are impaired and there are merits and demerits, so that satisfactory physical properties cannot always be obtained.
【0005】[0005]
【課題を解決するための手段】本発明者はかかる課題を
解決すべく鋭意研究を重ねた結果、ポリオレフィン系樹
脂に粉末状のグリオキザールを配合してなる組成物を、
溶融成型する場合、その目的を達成出来ることを見出し
本発明を完成した。Means for Solving the Problems As a result of intensive studies to solve the above problems, the present inventors have found that a composition obtained by blending a powdery glyoxal with a polyolefin resin is
The present invention has been completed by finding that the object can be achieved in the case of melt molding.
【0006】以下、本発明を詳しく説明する。本発明の
ポリオレフィン系樹脂としては直鎖状低密度・低密度・
高密度ポリエチレン、アイオノマー、エチレン−プロピ
レン共重合体、結晶性ポリプロピレン、ポリブテン、エ
チレン−酢酸ビニル共重合体、エチレン−アクリル酸エ
ステル共重合体などがあげられる。The present invention will be described in detail below. As the polyolefin resin of the present invention, linear low density / low density
Examples thereof include high density polyethylene, ionomer, ethylene-propylene copolymer, crystalline polypropylene, polybutene, ethylene-vinyl acetate copolymer, ethylene-acrylic acid ester copolymer and the like.
【0007】特に、直鎖状低密度ポリエチレン、低密度
ポリエチレン、高密度ポリエチレン、アイソタクチック
ポリプロピレンが実用的に重要である。Particularly, linear low density polyethylene, low density polyethylene, high density polyethylene and isotactic polypropylene are practically important.
【0008】該樹脂としてJISK−6760に基づい
て210℃、荷重2160gで測定したメルトフローレ
ートが0.05〜100g/10分、好ましくは0.1
〜20g/10分のものが使用される。The resin has a melt flow rate of 0.05 to 100 g / 10 minutes, preferably 0.1, measured at 210 ° C. and a load of 2160 g according to JIS K-6760.
The thing of -20g / 10min is used.
【0009】本発明では粉末状のグリオキザールを用い
ることが必須である。グリオキザールは通常水溶液の形
で市販されているので、これを脱水して塊状化し更に粉
砕したものを用いなければならない。かかる粉砕物のみ
でなくグリオキザールとエチレングリコールとの反応物
である2,3−ジヒドロキシ−1,4−ジオキサン(特
開昭53−111079号参照)も、グリオキザールと
同等の効果が得られるので有用である。In the present invention, it is essential to use powdery glyoxal. Since glyoxal is usually marketed in the form of an aqueous solution, it must be dehydrated, lumped, and ground. Not only such a pulverized product, but also 2,3-dihydroxy-1,4-dioxane (see Japanese Patent Application Laid-Open No. 53-111079), which is a reaction product of glyoxal and ethylene glycol, is useful because the same effect as glyoxal can be obtained. is there.
【0010】該グリオキザールの配合割合は、ポリオレ
フィン系樹脂に対して0.2〜15重量%、好ましくは
0.5〜5重量%でなければならない。グリオキザール
の配合量が0.2重量%以下では本発明の効果が得難
く、消臭性や静菌性、鮮度保持性の機能が発揮出来なく
なり、一方グリオキザールの配合量が15重量%以上で
は成形物の透明性が低下する。The content of the glyoxal should be 0.2 to 15% by weight, preferably 0.5 to 5% by weight, based on the polyolefin resin. When the content of glyoxal is 0.2% by weight or less, the effect of the present invention is difficult to obtain, and the functions of deodorant property, bacteriostatic property and freshness-retaining ability cannot be exhibited, while when the content of glyoxal is 15% by weight or more, molding is performed. The transparency of the product decreases.
【0011】かくして、かかる組成物は溶融成形して成
型物とされる。溶融混練によりペレット、フイルム、シ
ート、容器、繊維、棒、管等の各種成型物等に成型され
る。これらの粉砕品(回収物を再使用する時など)やペ
レットを用いて再び溶融成型に供することも多い。溶融
成型方法としては、押出成型(T−ダイ押出、インフレ
ーション押出、ブロー成型、溶融紡糸、異型押出等)、
射出成型法が主として採用される。溶融成型温度は14
5〜220℃の範囲から選ぶことが多い。上記射出成型
法のほか二色成型、インクジェクションブロー成型法な
どを含み、寸法精度の良好な成型物を得ることができ
る。Thus, such a composition is melt-molded into a molded product. By melt-kneading, various molded products such as pellets, films, sheets, containers, fibers, rods, tubes, etc. are molded. In many cases, these crushed products (such as when the collected product is reused) and pellets are used again for melt molding. As the melt molding method, extrusion molding (T-die extrusion, inflation extrusion, blow molding, melt spinning, profile extrusion, etc.),
The injection molding method is mainly adopted. Melt molding temperature is 14
Often selected from the range of 5 to 220 ° C. In addition to the injection molding method, a two-color molding method, an ink jet blow molding method, and the like can be included to obtain a molded product with good dimensional accuracy.
【0012】かかる成型時には可塑剤、安定剤、界面活
性剤、架橋性物質、充填剤、着色剤、補強材としての繊
維(ガラス繊維、炭素繊維など)、等を適当量配合する
ことができる。又、他の熱可塑性樹脂を適当量配合する
こともでき、かかる他の熱可塑性樹脂としては使用した
ポリオレフィンと重複しないポリオレフィン、又はこれ
らを不飽和カルボン酸又はその誘導体でグラフト変性し
た変性ポリオレフィン、ポリアミド、ポリ塩化ビニル、
ポリ塩化ビニリデン、ポリエステル、ポリスチレン、ポ
リアクリロニトリル、ポリウレタン、ポリアセタール、
ポリカーボネートあるいは溶融成型可能なポリビニルア
ルコール系樹脂などが挙げられる。At the time of molding, a suitable amount of a plasticizer, a stabilizer, a surfactant, a crosslinkable substance, a filler, a coloring agent, a fiber as a reinforcing material (glass fiber, carbon fiber, etc.) and the like can be added. Further, other thermoplastic resins may be blended in appropriate amounts, and as such other thermoplastic resins, polyolefins which do not overlap with the polyolefins used, or modified polyolefins and polyamides obtained by graft-modifying these with unsaturated carboxylic acids or derivatives thereof are used. ,PVC,
Polyvinylidene chloride, polyester, polystyrene, polyacrylonitrile, polyurethane, polyacetal,
Examples include polycarbonate and melt-moldable polyvinyl alcohol-based resins.
【0013】本発明の成型物は組成物のみを単層とする
成型物の製造以外に、該組成物を少なくとも一層とする
積層構造物として実用に供せられることもある。積層構
造物を製造するに当たっては、本発明の組成物の層の片
面又は両面に他の基材をラミネートするのであるが、ラ
ミネート方法としては例えば、組成物のフイルム、シー
トに熱可塑性樹脂を溶融押出する方法、逆に熱可塑性樹
脂等の基材に本発明の組成物を溶融押出する方法、本発
明の組成物と他の熱可塑性樹脂とを共押出する方法、更
には本発明の組成物のフイルム、シートと他の基材のフ
イルム、シートとを有機チタン化合物、イソシアネート
化合物、ポリエステル系化合物等の公知の接着剤を用い
てラミネートする方法等が挙げられる。The molded article of the present invention may be put to practical use as a laminated structure having at least one layer of the composition, in addition to the production of the molded article having only the composition as a single layer. In manufacturing a laminated structure, another substrate is laminated on one side or both sides of the layer of the composition of the present invention, and as a laminating method, for example, a composition film or a sheet is melted with a thermoplastic resin. Extrusion method, conversely a method of melt-extruding the composition of the present invention into a substrate such as a thermoplastic resin, a method of co-extruding the composition of the present invention and another thermoplastic resin, further the composition of the present invention The method of laminating the film, sheet and the film of the other substrate with the known adhesive agent such as organic titanium compound, isocyanate compound, polyester compound and the like can be mentioned.
【0014】共押出の場合の相手側樹脂としては直鎖状
低密度ポリエチレン、低密度ポリエチレン、中密度ポリ
エチレン、高密度ポリエチレン、エチレン−酢酸ビニル
共重合体、アイオノマー、エチレン−プロピレン共重合
体、エチレン−アクリル酸エステル共重合体、ポリプロ
ピレン、プロピレン−α−オレフィン(炭素数4〜20
のα−オレフィン)共重合体、ポリブテン、ポリペンテ
ンなどのオレフィンの単独又は共重合体、あるいはこれ
らのオレフィンの単独又は共重合体を、不飽和カルボン
酸又はそのエステルでグラフト変性したものなどの広義
のポリオレフィン系樹脂、ポリエステル、ポリアミド、
共重合ポリアミド、ポリ塩化ビニル、ポリ塩化ビニリデ
ン、アクリル系樹脂、スチレン系樹脂、ビニルエステル
系樹脂、ポリエステルエラストマー、ポリウレタンエラ
ストマー、塩素化ポリエチレン、塩素化ポリプロピレン
などが挙げられる。エチレン−酢酸ビニル共重合体ケン
化物も共押出可能である。In the case of coextrusion, the other resin is linear low density polyethylene, low density polyethylene, medium density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, ionomer, ethylene-propylene copolymer, ethylene. -Acrylic ester copolymer, polypropylene, propylene-α-olefin (having 4 to 20 carbon atoms)
Α-olefin) copolymer, polybutene, homopolymers or copolymers of olefins such as polypentene, or a broad definition of homo- or copolymers of these olefins graft-modified with unsaturated carboxylic acids or their esters. Polyolefin resin, polyester, polyamide,
Copolymerized polyamide, polyvinyl chloride, polyvinylidene chloride, acrylic resin, styrene resin, vinyl ester resin, polyester elastomer, polyurethane elastomer, chlorinated polyethylene, chlorinated polypropylene, etc. may be mentioned. Saponified ethylene-vinyl acetate copolymers can also be coextruded.
【0015】本発明で得られるフィルム、シート、容器
等は食品、医薬品、工業薬品、農薬等各種の包装材、ゴ
ミ袋、手袋等としてして有用である。The film, sheet, container and the like obtained by the present invention are useful as various packaging materials such as foods, pharmaceuticals, industrial chemicals and agricultural chemicals, garbage bags, gloves and the like.
【0016】[0016]
【作用】本発明においては、ポリオレフィンとグリオキ
ザールとよりなる成型物は、ポリオレフィン系樹脂が本
来有する優れた延伸性や柔軟性等の、成型加工物性や機
械的物性を保持しながら消臭性、静菌性や鮮度保持性を
向上させることが可能である。In the present invention, a molded product composed of polyolefin and glyoxal has a deodorizing property and a static property while maintaining the molded physical properties and mechanical properties such as the excellent stretchability and flexibility originally possessed by the polyolefin resin. It is possible to improve fungal properties and freshness retention.
【0017】[0017]
【実施例】次に実施例を挙げて本発明の組成物を更に具
体的に説明する。以下、「部」とあるのは特に断わりの
ない限り重量基準で表わしたものである。
実施例1
密度0.92の低密度ポリエチレン100部と粉末状の
グリオキザール2部との組成物ペレットをヘンシェルミ
キサーを用いて混合し、T−ダイを備えた押出機に供給
して溶融混練し、T−ダイから押出して厚み30μのフ
イルムを製造した。押出成型の条件は次の通りである。EXAMPLES Next, the composition of the present invention will be described more specifically with reference to examples. Hereinafter, “part” is expressed on a weight basis unless otherwise specified. Example 1 A composition pellet of 100 parts of low-density polyethylene having a density of 0.92 and 2 parts of powdery glyoxal was mixed using a Henschel mixer, and the mixture was supplied to an extruder equipped with a T-die and melt-kneaded, A film having a thickness of 30 μm was manufactured by extruding from a T-die. The conditions for extrusion molding are as follows.
【0018】押出機:40mm径押出機
スクリュー:フルフライトタイプ L/D=28、
CR=3
押出温度:C1/C2/C3/C4/H/D1/D2=
170/200/220/220/220/210/2
10
スクリュー回転数:30rpm
得られたフイルムを製袋し家庭の生ゴミを収納し7日間
放置した。その後開封してみたところ悪臭は認められな
かった。Extruder: 40 mm diameter extruder Screw: Full flight type L / D = 28,
CR = 3 Extrusion temperature: C1 / C2 / C3 / C4 / H / D1 / D2 =
170/200/220/220/220/210/2
10 Screw rotation speed: 30 rpm The obtained film was made into a bag, household garbage was stored, and the film was left for 7 days. After opening the bag, no odor was found.
【0019】実施例2
低密度ポリエチレン100部と2,3−ジヒドロキシ−
1,4−ジオキサン3部との組成物を実施例1と同じよ
うにペレット化しヘンシェルミキサーを用いて混合し、
T−ダイを備えた押出機に供給して溶融混練し、T−ダ
イから押出して厚み30μのフイルムを製造した。得ら
れたフイルムを製袋し家庭の生ゴミを収納し10日間放
置した。その後開封してみたところ悪臭は認められなか
った。Example 2 100 parts of low-density polyethylene and 2,3-dihydroxy-
A composition with 3 parts of 1,4-dioxane was pelletized as in Example 1 and mixed using a Henschel mixer,
The film was supplied to an extruder equipped with a T-die, melt-kneaded, and extruded from the T-die to produce a film having a thickness of 30 μm. The obtained film was made into a bag, and household garbage was stored and left for 10 days. After opening the bag, no odor was found.
【0020】[0020]
【発明の効果】本発明のポリオレフィン系樹脂と粉末状
グリオキザールとの組成物から得られる成型物は、ポリ
オレフィン系樹脂のもつ優れた物性を保持しながら、消
臭性、静菌性、鮮度保持性が付与される。The molded product obtained from the composition of the polyolefin resin and the powdery glyoxal of the present invention has deodorant property, bacteriostatic property and freshness retention property while maintaining the excellent physical properties of the polyolefin resin. Is given.
Claims (3)
ザールを配合してなる組成物を、溶融成型することを特
徴とするポリオレフィン系樹脂成型物の製造法。1. A method for producing a polyolefin resin molded product, which comprises melt-molding a composition obtained by blending a powdery glyoxal with a polyolefin resin.
レン又は高密度ポリエチレンであることを特徴とする請
求項1記載の成型物の製造法。2. The method for producing a molded article according to claim 1, wherein the polyolefin resin is low density polyethylene or high density polyethylene.
ドロキシ−1,4−ジオキサンであることを特徴とする
請求項1項記載の成型物の製造法。3. The method for producing a molded article according to claim 1, wherein the powdery glyoxal is 2,3-dihydroxy-1,4-dioxane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26333291A JPH0686555B2 (en) | 1991-07-06 | 1991-07-06 | Manufacturing method for polyolefin resin moldings |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26333291A JPH0686555B2 (en) | 1991-07-06 | 1991-07-06 | Manufacturing method for polyolefin resin moldings |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH059345A true JPH059345A (en) | 1993-01-19 |
| JPH0686555B2 JPH0686555B2 (en) | 1994-11-02 |
Family
ID=17388006
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26333291A Expired - Lifetime JPH0686555B2 (en) | 1991-07-06 | 1991-07-06 | Manufacturing method for polyolefin resin moldings |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0686555B2 (en) |
-
1991
- 1991-07-06 JP JP26333291A patent/JPH0686555B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0686555B2 (en) | 1994-11-02 |
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