JPH03199417A - Naturally degradative monofilament - Google Patents
Naturally degradative monofilamentInfo
- Publication number
- JPH03199417A JPH03199417A JP33977689A JP33977689A JPH03199417A JP H03199417 A JPH03199417 A JP H03199417A JP 33977689 A JP33977689 A JP 33977689A JP 33977689 A JP33977689 A JP 33977689A JP H03199417 A JPH03199417 A JP H03199417A
- Authority
- JP
- Japan
- Prior art keywords
- monofilament
- strength
- weight
- polycaprolactone
- ethylenically unsaturated
- 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.)
- Pending
Links
- 230000003413 degradative effect Effects 0.000 title 1
- 229920001610 polycaprolactone Polymers 0.000 claims abstract description 13
- 239000004632 polycaprolactone Substances 0.000 claims abstract description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 11
- 150000001875 compounds Chemical class 0.000 claims abstract description 10
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000005977 Ethylene Substances 0.000 claims abstract description 6
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims abstract description 6
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 claims abstract description 5
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 claims abstract description 5
- -1 polyethylene Polymers 0.000 claims description 20
- 239000004698 Polyethylene Substances 0.000 claims description 19
- 229920000573 polyethylene Polymers 0.000 claims description 19
- 229920001903 high density polyethylene Polymers 0.000 claims description 11
- 239000004700 high-density polyethylene Substances 0.000 claims description 11
- 238000007334 copolymerization reaction Methods 0.000 abstract description 7
- 239000012773 agricultural material Substances 0.000 abstract description 2
- 238000002844 melting Methods 0.000 abstract description 2
- 230000008018 melting Effects 0.000 abstract description 2
- 238000007151 ring opening polymerisation reaction Methods 0.000 abstract description 2
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 abstract description 2
- 241000251468 Actinopterygii Species 0.000 abstract 1
- 230000015556 catabolic process Effects 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- 238000006731 degradation reaction Methods 0.000 abstract 1
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 230000000704 physical effect Effects 0.000 abstract 1
- 230000002265 prevention Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 9
- 244000005700 microbiome Species 0.000 description 8
- 230000000813 microbial effect Effects 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 229910002090 carbon oxide Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000001782 photodegradation Methods 0.000 description 4
- 239000002689 soil Substances 0.000 description 4
- 238000009987 spinning Methods 0.000 description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 3
- 239000012770 industrial material Substances 0.000 description 3
- 238000002074 melt spinning Methods 0.000 description 3
- 238000006303 photolysis reaction Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- NNBZCPXTIHJBJL-UHFFFAOYSA-N decalin Chemical compound C1CCCC2CCCCC21 NNBZCPXTIHJBJL-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 1
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2,2'-azo-bis-isobutyronitrile Substances N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 1
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 229920002978 Vinylon Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- CREMABGTGYGIQB-UHFFFAOYSA-N carbon carbon Chemical compound C.C CREMABGTGYGIQB-UHFFFAOYSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- LSXWFXONGKSEMY-UHFFFAOYSA-N di-tert-butyl peroxide Chemical compound CC(C)(C)OOC(C)(C)C LSXWFXONGKSEMY-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- NHOGGUYTANYCGQ-UHFFFAOYSA-N ethenoxybenzene Chemical compound C=COC1=CC=CC=C1 NHOGGUYTANYCGQ-UHFFFAOYSA-N 0.000 description 1
- MEGHWIAOTJPCHQ-UHFFFAOYSA-N ethenyl butanoate Chemical compound CCCC(=O)OC=C MEGHWIAOTJPCHQ-UHFFFAOYSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 229940117927 ethylene oxide Drugs 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- XJRBAMWJDBPFIM-UHFFFAOYSA-N methyl vinyl ether Chemical compound COC=C XJRBAMWJDBPFIM-UHFFFAOYSA-N 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000002165 photosensitisation Effects 0.000 description 1
- 239000003504 photosensitizing agent Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000007613 slurry method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000000475 sunscreen effect Effects 0.000 description 1
- 239000000516 sunscreening agent Substances 0.000 description 1
- PXXNTAGJWPJAGM-UHFFFAOYSA-N vertaline Natural products C1C2C=3C=C(OC)C(OC)=CC=3OC(C=C3)=CC=C3CCC(=O)OC1CC1N2CCCC1 PXXNTAGJWPJAGM-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、ポリエチレン系自然崩壊性モノフィラメント
に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a polyethylene-based self-disintegrating monofilament.
(従来の技術)
従来、漁網、釣り糸、農業用ネット等に用いられる産業
資材用モノフィラメントとしては、主としてポリアミド
、ポリエステル、ビニロン、ポリオレフィン等からなる
ものが使用されている。したがって、これらのモノフィ
ラメント1こは、自己分解性がなく、使用後、海や山野
に放置すると種々の公害を引き起こすという問題がある
。この問題は、使用後、焼却、埋め立て或いは回収再生
により処理すれば解決されるが、これらの処理には多大
の費用を要するため、現実には、海や山野に放置され、
鳥や海洋生物、ダイパー等に絡みついて殺傷したり、船
のスクリューに絡みついて船舶事故を起こしたりする事
態がしばしば発生している。(Prior Art) Conventionally, as monofilaments for industrial materials used in fishing nets, fishing lines, agricultural nets, etc., monofilaments mainly made of polyamide, polyester, vinylon, polyolefin, etc. have been used. Therefore, these monofilaments do not have self-decomposition properties, and if they are left in the sea, mountains or fields after use, they cause various types of pollution. This problem can be solved by incinerating, burying, or collecting and recycling after use, but these treatments require a lot of money, so in reality, they are left abandoned in the sea, mountains, and fields.
Situations often occur in which they become entangled with birds, marine animals, and diapers, killing or injuring them, or become entangled with ships' propellers, causing ship accidents.
このような問題を解決する方法として、光や微生物によ
って自然に分解又は崩壊する素材を用いることが考えら
れる。One possible way to solve these problems is to use materials that naturally decompose or disintegrate when exposed to light or microorganisms.
本発明者らは、このような観点から、先に主鎮に光増感
基であるカルボニル基を導入した変性ポリエチレンから
なる光分解性モノフィラメント及び変性ポリエチレと高
密度ポリエチレンとからなる光崩壊性モノフィラメント
について提案した。From this point of view, the present inventors have previously developed a photodegradable monofilament made of modified polyethylene into which a carbonyl group, which is a photosensitizing group, has been introduced into the main chain, and a photodegradable monofilament made of modified polyethylene and high-density polyethylene. I proposed about.
特に後者の光崩壊性モノフィラメントは、高強度で、産
業資材用繊維として適した特性を有するものであった。In particular, the latter photodegradable monofilament had high strength and had properties suitable as a fiber for industrial materials.
しかし、このモノフィラメントの光崩壊挙動を追跡した
結果、このモノフィラメントは、見掛は上、光によって
細片ないしは粉末状に崩壊するが9分子レベルにまで分
解するものではないため、地上に放置した場合、崩壊し
てできた細片ないしは粉末状物が土中に残存し、土壌に
悪影響を与えるおそれがあるという問題があることが分
かった。However, as a result of tracking the photodegradation behavior of this monofilament, we found that although it looks good, it disintegrates into small pieces or powder when exposed to light, but it does not decompose down to the level of 9 molecules, so if it is left on the ground. It has been found that there is a problem in that fragments or powdery substances formed by the disintegration remain in the soil and may have a negative impact on the soil.
また1本発明者らは、ポリカプロラクトンを配合した高
密度ポリエチレンからなる微生物崩壊性モノフィラメン
トについて提案した。このモノフィラメントは、土壌中
、汚泥中、水中等の微生物が活発に活動している環境下
では自然に崩壊するが、使用後、必ずしも微生物が活発
に活動している環境下に置かれるとは限らず1例えば、
地上に放置されると崩壊するまでに極めて長期間を要す
るという問題があった。The present inventors also proposed a microbially degradable monofilament made of high-density polyethylene blended with polycaprolactone. This monofilament naturally disintegrates in environments where microorganisms are actively active, such as in soil, sludge, and water, but after use, it is not necessarily placed in an environment where microorganisms are actively active. For example,
The problem was that if left on the ground, it would take an extremely long time to collapse.
(発明が解決しようとする課題)
本発明は、高強度で、かつ、光及び微生物によって自然
に崩壊するポリエチレン系モノフィラメントを提供しよ
うとするものである。(Problems to be Solved by the Invention) The present invention aims to provide a polyethylene monofilament that has high strength and is naturally disintegrated by light and microorganisms.
(課題を解決するための手段) 本発明は、上記の課題を解決するものであり。(Means for solving problems) The present invention solves the above problems.
その要旨は9次のとおりである。The summary is as follows.
エチレンを主たる構成成分とし、1.5〜7.0重量%
の一酸化炭素又はこれと他のエチレン性不飽和化合物と
を共重合した変性ポリエチレン20〜50重量%、ポリ
カプロラクトン3〜30重量%及び高密度ポリエチレン
20〜77重量%とからなり、下記(a)〜(c)の特
性を同時に満足することを特徴とする自然崩壊性モノフ
ィラメント。Main component is ethylene, 1.5-7.0% by weight
It consists of 20-50% by weight of modified polyethylene obtained by copolymerizing carbon monoxide or other ethylenically unsaturated compounds, 3-30% by weight of polycaprolactone, and 20-77% by weight of high-density polyethylene, and contains the following (a) A naturally disintegrating monofilament characterized by simultaneously satisfying the characteristics of ) to (c).
(a) 引張強度 3g/d以上ら)結節強度
2g/d以上
(c) 切断伸度 5%以上
以下1本発明について詳細に説明する。(a) Tensile strength 3g/d or more) Knot strength
2 g/d or more (c) Cutting elongation 5% or more 1 The present invention will be explained in detail.
本発明において用いられる変性ポリエチレンは。The modified polyethylene used in the present invention is:
エチレンを主たる構成成分とし、−酸化炭素又は−酸化
炭素と他のエチレン性不飽和化合物を共重合した光分解
性のものであって、−酸化炭素の割合が 1.5〜76
0重量%、好ましくは2.0〜4.0重量%のものであ
る。−酸化炭素の共重合割合が1.5重量%未満では光
分解速度が著しく小さく、一方。A photodegradable product containing ethylene as a main component and copolymerized with -carbon oxide or -carbon oxide and other ethylenically unsaturated compounds, with a -carbon oxide ratio of 1.5 to 76.
0% by weight, preferably 2.0-4.0% by weight. - If the copolymerization ratio of carbon oxide is less than 1.5% by weight, the photodecomposition rate is extremely low.
7.0重量%を超えるとモノフィラメントの強度が低下
すると共に光崩壊速度が大きくなり過ぎて短期間で強度
が低下してしまうため実用にならない。If it exceeds 7.0% by weight, the strength of the monofilament decreases and the rate of photodegradation becomes too high, resulting in a decrease in strength in a short period of time, making it impractical.
光分解速度は一酸化炭素の共重合割合によって調節する
ことができ、モノフィラメントの使用目的に応じて一酸
化炭素の共重合割合を適当に選定する。The photodecomposition rate can be controlled by the copolymerization ratio of carbon monoxide, and the copolymerization ratio of carbon monoxide is appropriately selected depending on the intended use of the monofilament.
本発明において用いられるエチレン性不飽和化合物とし
ては、酢酸ビニル、酪酸ビニル、(メタ)アクリル酸、
(メタ)アクリル酸メチル、(メタ)アクリル酸エチル
、(メタ)アクリル酸ブチル、マレイン酸、フマル酸、
アクリロニトリル、アクリルアミド、ビニルメチルエー
テル、ビニルフェニルエーテル、スチレン、塩化ビニル
、プロピレン。Ethylenically unsaturated compounds used in the present invention include vinyl acetate, vinyl butyrate, (meth)acrylic acid,
Methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate, maleic acid, fumaric acid,
Acrylonitrile, acrylamide, vinyl methyl ether, vinyl phenyl ether, styrene, vinyl chloride, propylene.
ブテン−1,ヘキセン−1,オクテン−1,デセン−1
,4−メチルペンテン−1等が挙げられるが。Butene-1, Hexene-1, Octene-1, Decene-1
, 4-methylpentene-1 and the like.
紡糸性及び得られるモノフィラメントの機械的特性、耐
熱性、光沢等の点で、特に酢酸ビニル及びアクリル酸エ
チルが好適である。Vinyl acetate and ethyl acrylate are particularly preferred in terms of spinnability and mechanical properties, heat resistance, gloss, etc. of the resulting monofilament.
一酸化炭素と共に酢酸ビニルやアクリル酸エチル等のエ
チレン性不飽和化合物を共重合すると。When ethylenically unsaturated compounds such as vinyl acetate and ethyl acrylate are copolymerized with carbon monoxide.
一定期間経過後の光分解を急激に起こさせることができ
る。エチレン性不飽和化合物を共重合する場合、その共
重合割合は1〜20重量%が好適である。Photodecomposition can be caused rapidly after a certain period of time. When copolymerizing an ethylenically unsaturated compound, the copolymerization ratio is preferably 1 to 20% by weight.
本発明における変性ポリエチレンは1次のような特許公
報に開示された方法で製造することができる。The modified polyethylene in the present invention can be produced by a method disclosed in a patent publication such as Hiroshi.
米国特許
2497323 2641590 3083184 3
2483593530109 3676401 368
9460 36944123780140 38351
23 3929727 39488323948850
3948873 3968082 39843
884024104 4024325 40243
26 40769114143096 41373
g2 4139522 414309643048
87
日本特許公開
昭53−128690 昭53−128691 昭
62−115026平1i53723
日本特許公告
昭50−39705
具体的には2例えば、■高圧法低密度ポリエチレン製造
装置を用いて2反応温度150〜300℃、圧力500
〜3000気圧の条件下に、ジラウロイルパーオキサイ
ド、ターシャリ−ブチルパーオキサイド。US Patent 2497323 2641590 3083184 3
2483593530109 3676401 368
9460 36944123780140 38351
23 3929727 39488323948850
3948873 3968082 39843
884024104 4024325 40243
26 40769114143096 41373
g2 4139522 414309643048
87 Japanese Patent Publication 1986-128690 1982-128691 1982-115026 Hei 1i53723 Japanese Patent Publication 1977-39705 Specifically, 2 For example, , pressure 500
dilauroyl peroxide, tert-butyl peroxide under conditions of ~3000 atm.
ターシャリ−ブチルパーイソブチレート、ターシャリ−
ブチルパーアセテート又はα、α°−アゾビスイソブチ
ロニトリル等のフリーラジカル発生剤をベンゼン、ケロ
セン又は鉱油等の不活性有機溶剤に溶解したものを反応
器に注入し、エチレンと一酸化炭素及び必要に応じて他
のエチレン性不飽和化合物とを共重合させる方法、■中
低圧状高密度ポリエチレン製造装置を用いて2反応温度
50〜300℃、圧力0〜200気圧の条件下に、配位
触媒又は金属触媒(チーグラー型、ナツタ型又はフィリ
ップス型等)の存在下で、スラリー法、溶液法又は気相
法等でエチレンと一酸化炭素及び必要に応じて他のエチ
レン性不飽和化合物とを共重合させる方法で製造するこ
とができる。Tertiary butyl perisobutyrate, tertiary
A free radical generator such as butyl peracetate or α,α°-azobisisobutyronitrile dissolved in an inert organic solvent such as benzene, kerosene or mineral oil is injected into the reactor, and ethylene, carbon monoxide and A method of copolymerizing with other ethylenically unsaturated compounds as necessary; In the presence of a catalyst or metal catalyst (Ziegler type, Natsuta type, Phillips type, etc.), ethylene and carbon monoxide and other ethylenically unsaturated compounds are mixed by a slurry method, solution method, gas phase method, etc. It can be produced by copolymerization.
また、ポリカプロラクトンは、ε−カプロラクトンの開
環重合で得られる融点が約60℃のもので、分子量1万
〜lO万、好ましくは2万〜5万のものが適当である。Further, polycaprolactone is obtained by ring-opening polymerization of ε-caprolactone and has a melting point of about 60° C., and has a molecular weight of 10,000 to 10,000, preferably 20,000 to 50,000.
さらに1本発明において用いられる高密度ポリエチレン
としては1通常の低圧法で製造される密度が0.94
g / cut以上で、メルトフローレートが20以下
、好ましくは2以下のものが適当である。Furthermore, the high-density polyethylene used in the present invention has a density of 0.94 when manufactured by a normal low pressure method.
g/cut or more and a melt flow rate of 20 or less, preferably 2 or less.
本発明のモノフィラメントは、変性ポリエチレン20〜
50重量%、ポリカプロラクトン3〜30重量%及び高
密度ポリエチレン20〜77重量%とからなる組成物で
構成される。変性ポリエチレンの割合が20重量%未満
であると光崩壊速度が小さく。The monofilament of the present invention is made of modified polyethylene 20~
50% by weight, 3-30% by weight of polycaprolactone and 20-77% by weight of high-density polyethylene. When the proportion of modified polyethylene is less than 20% by weight, the rate of photodegradation is low.
方、50重量%を超えるとモノフィラメントの強度が劣
ったものとなる。また、ポリカプロラクトンの割合が3
重量%未満であると微生物分解速度が小さく、一方、3
0重量%を超えるとモノフィラメントの強度が劣ったも
のとなる。さらに、高密度ポリエチレンの割合が20重
量%未満であるとモノフィラメントの強度が著しく劣っ
たものとなり。On the other hand, if it exceeds 50% by weight, the strength of the monofilament will be poor. In addition, the proportion of polycaprolactone is 3
When it is less than 3% by weight, the microbial decomposition rate is low;
If it exceeds 0% by weight, the strength of the monofilament will be poor. Furthermore, if the proportion of high-density polyethylene is less than 20% by weight, the strength of the monofilament will be significantly inferior.
一方、77重量%を超えるとモノフィラメントの光及び
微生物による自然崩壊速度が極めて遅くなり。On the other hand, if it exceeds 77% by weight, the natural disintegration rate of the monofilament due to light and microorganisms becomes extremely slow.
自然崩壊性モノフィラメントとして不十分なものとなる
。It becomes insufficient as a naturally disintegrating monofilament.
モノフィラメントを構成する3成分のの混合方法は特に
限定されない。通常、3成分をエクストルーダーで溶融
混合してチップ化した後、溶融紡糸する方法が採用され
るが、3者を紡糸装置に供給して混合紡糸してもよい。The method of mixing the three components constituting the monofilament is not particularly limited. Usually, a method is adopted in which the three components are melt-mixed in an extruder to form chips and then melt-spun, but the three components may be fed to a spinning device and mixed and spun.
本発明のモノフィラメントは1次のような方法で製造す
ることができる。The monofilament of the present invention can be manufactured by the following method.
まず、変性ポリエチレン、ポリカプロラクトン及び高密
度ポリエチレンの所定割合の混合物(通常、溶融混合チ
ップ)を溶融紡糸に供するが、溶融紡糸は、230〜3
00℃の温度で行うことが望ましい。紡糸温度230℃
未満では溶融押し出しが困難であり、300℃を超える
とポリマーの分解が起こり。First, a mixture of modified polyethylene, polycaprolactone, and high-density polyethylene in a predetermined ratio (usually melt-mixed chips) is subjected to melt spinning.
It is desirable to carry out at a temperature of 00°C. Spinning temperature 230℃
If it is less than 300°C, melt extrusion is difficult, and if it exceeds 300°C, the polymer will decompose.
高強度のモノフィラメントを得ることが困難となる。溶
融紡出されたモノフィラメントは水冷後。It becomes difficult to obtain a high strength monofilament. The melt-spun monofilament is water-cooled.
−旦巻き取った後又は巻き取ることなく連続して熱風又
は加熱された水、グリセリン、エチレングリコール、シ
リコーンオイル等の熱媒中で延伸される。延伸温度及び
延伸倍率等の延伸条件は、目的とするモノフィラメント
の要求性能によって適宜選定されるが1通常、60〜1
10℃程度の温度で。- After being wound up, or without being wound up, it is continuously stretched in hot air or a heating medium such as heated water, glycerin, ethylene glycol, or silicone oil. Stretching conditions such as stretching temperature and stretching ratio are appropriately selected depending on the required performance of the target monofilament, but usually 60 to 1
At a temperature of about 10℃.
10〜17倍に延伸するのが適当である。また、延伸は
2段以上の多段で行うことが望ましく、1段延伸では、
十分延伸することが困難で、高強度のモノフィラメント
を得ることが困難である。延伸されたモノフィラメント
は1次いで、50〜110℃の温度の雰囲気中で弛緩熱
処理され2所望の強伸度特性を有するモノフィラメント
とされる。この際の弛緩率は1〜5%が適当である。It is appropriate to stretch the film 10 to 17 times. In addition, it is desirable to perform the stretching in multiple stages of two or more stages, and in one stage stretching,
It is difficult to draw the monofilament sufficiently, making it difficult to obtain a high-strength monofilament. The drawn monofilament is then subjected to a relaxation heat treatment in an atmosphere at a temperature of 50 to 110°C to obtain a monofilament having desired strength and elongation characteristics. The appropriate relaxation rate at this time is 1 to 5%.
このようにして得られる本発明のモノフィラメントは、
前述のような優れた強伸度特性と自然崩壊性とを有する
ものである。The monofilament of the present invention obtained in this way is
It has excellent strength and elongation properties and natural disintegration properties as described above.
なお、前記の強伸度特性を有しないものでは。In addition, those that do not have the above-mentioned strong elongation characteristics.
産業資材用モノフィラメントとして不適当である。It is unsuitable as a monofilament for industrial materials.
また9本発明のモノフィラメントの繊度は、用途により
適宜選定されるが1通常、50d以上である。Further, the fineness of the monofilament of the present invention is appropriately selected depending on the use, but is usually 50 d or more.
なお1本発明のモノフィラメントには、必要に応じて、
高圧法低密度ポリエチレン、エチレン−酢酸ビニル共重
合体、エチレン−アクリル酸エチル共重合体、アイオノ
マー、直鎮状低密度エチレン−α−オレフィン共重合体
等のポリマーや酸化促進剤、顔料、滑剤、帯電防止剤1
日焼は防止剤等の添加剤を含有させることができる。Note that the monofilament of the present invention may include, if necessary,
Polymers such as high-pressure low-density polyethylene, ethylene-vinyl acetate copolymer, ethylene-ethyl acrylate copolymer, ionomer, straight-line low-density ethylene-α-olefin copolymer, oxidation promoters, pigments, lubricants, Antistatic agent 1
Additives such as sunscreen inhibitors can be included.
(作 用)
本発明のモノフィラメントは光分解性の変性ポリエチレ
ン、微生物分解性のポリカプロラクトン及び通常の高密
度ポリエチレンで構成されており。(Function) The monofilament of the present invention is composed of photodegradable modified polyethylene, microbially degradable polycaprolactone, and ordinary high-density polyethylene.
光によって変性ポリエチレンが分解し、微生物によって
ポリカプロラクトンが分解するので、光及び/又は微生
物が存在すれば、モノフィラメントが崩壊する。Since light decomposes the modified polyethylene and microorganisms decompose polycaprolactone, the presence of light and/or microorganisms causes the monofilament to disintegrate.
そして1本発明においては、変性ポリエチレンが光崩壊
性、ポリカプロラクトン微生物崩壊性。In the present invention, the modified polyethylene is photodegradable, and the polycaprolactone is biodegradable.
高密度ポリエチレンが強度特性にそれぞれ寄与し。High-density polyethylene contributes to its strength properties.
高強度で、かつ、自然崩壊性を有するモノフィラメント
が得られる。A monofilament with high strength and self-disintegrating properties can be obtained.
(実施例) 以下1本発明を実施例によりさらに具体的に説明する。(Example) The present invention will be explained in more detail below with reference to Examples.
なお1本発明における測定法又は評価法は次のとおりで
ある。Note that the measurement method or evaluation method in the present invention is as follows.
強伸度特性 JIS L 1013に準じて測定した。Strength and elongation properties Measured according to JIS L 1013.
自然崩壊性
次の光崩壊試験と微生物崩壊試験とを独立して行い、何
れも良好であった場合を良好と評価した。Natural disintegration The following photo-disintegration test and microbial disintegration test were conducted independently, and cases where both were good were evaluated as good.
■光崩壊試験
スガ試験機社製すンシャインウエザオメーター(肝L−
5UN−HC−)1)を用い、63℃で40時間光を照
射し。■Photodegradation test Sunshine Weatherometer manufactured by Suga Test Instruments Co., Ltd. (Liver L-
Using 5UN-HC-)1), light was irradiated at 63°C for 40 hours.
照射後の引張強度を測定して、初期強度に対する強度保
持率を求め1強度保持率が60〜90%の場合を光崩壊
性良好と評価した。The tensile strength after irradiation was measured, and the strength retention rate with respect to the initial strength was determined, and a case where the 1 strength retention rate was 60 to 90% was evaluated as having good photodegradability.
■微生物崩壊試験
試料を10〜25℃の土壌中に6カ月間埋めておいた後
取り出して、モノフィラメントの形状を失っている場合
、あるいはモノフィラメントの形状は保っているものの
引張強度が当初の50%以下に低下している場合を微生
物崩壊性が良好であると評価した。■ Microbial decay test If the sample is buried in soil at 10-25℃ for 6 months and then taken out, the monofilament shape has been lost, or the monofilament shape has been maintained but the tensile strength is 50% of the original value. The microbial disintegration property was evaluated to be good when the microbial disintegration property decreased to below.
実施例1〜17及び比較例1〜6
高圧法により製造した一酸化炭素を1.5〜7.0重量
%共重合した変性ポリエチレンAI、平均分子量が約4
万のポリカプロラクトンB及びメルトフローレー)
(JIS K 6760に準じて測定)が約1.1g/
10分の高密度ポリエチレンCを第1表に示した組!(
重量比)となるように3軸の混練用エクストルーダーに
供給し、溶融混合してチップ化した。Examples 1 to 17 and Comparative Examples 1 to 6 Modified polyethylene AI produced by copolymerizing 1.5 to 7.0% by weight of carbon monoxide produced by a high pressure method, with an average molecular weight of about 4
10,000 polycaprolactone B and melt flowray)
(measured according to JIS K 6760) is approximately 1.1g/
10 minutes of high-density polyethylene C set shown in Table 1! (
The mixture was supplied to a three-screw extruder for kneading so that the weight ratio of the mixture was obtained (weight ratio), and the mixture was melted and mixed to form chips.
このチップをエクストルーダー型溶融紡糸機に供給し、
紡糸温度290℃で溶融紡出し、10℃の水浴中で冷却
した後、直ちに80℃のデカリン浴中に導き、延伸倍率
8〜12倍の第1段延伸を行い、引き続いて95℃のグ
リセリン洛中で延伸倍率1.3〜1.7倍の第2段延伸
を行い、さらに95℃の加熱雰囲気中で弛緩率3〜6%
で熱処理し、直径0.2〜0.3μのモノフィラメント
を得た。This chip is fed to an extruder type melt spinning machine,
After melt-spinning at a spinning temperature of 290°C and cooling in a 10°C water bath, it is immediately introduced into a decalin bath at 80°C and subjected to first-stage stretching at a draw ratio of 8 to 12 times, followed by spinning in a glycerin bath at 95°C. 2nd stage stretching was performed at a stretching ratio of 1.3 to 1.7 times, and the relaxation rate was further increased to 3 to 6% in a heated atmosphere at 95°C.
A monofilament with a diameter of 0.2 to 0.3 μm was obtained.
得られたモノフィラメントの特性値等を第1表に示す。Table 1 shows the characteristic values of the obtained monofilament.
実施例18〜25
前記実施例における変性ポリエチレン八1の代わりに一
酸化炭素7.0重量%と酢酸ビニル(実施例18〜21
)又はアクリル酸エチル(実施例22〜25)20重量
%とを共重合した変性ポリエチレン八2を用いて前記実
施例と同様な試験を行った。Examples 18-25 7.0% by weight of carbon monoxide and vinyl acetate (Examples 18-21
) or 20% by weight of ethyl acrylate (Examples 22 to 25) and a modified polyethylene 82 copolymerized with the same test as in the above example.
結果を第2表に示す。The results are shown in Table 2.
第2表
注:C○は変性ポリエチレンA1の一酸化炭素共重合割
合を示す。Table 2 Note: C○ indicates the carbon monoxide copolymerization ratio of modified polyethylene A1.
(発明の効果)
本発明によれば1通常のポリエチレンモノフィラメント
にほぼ匹敵する強伸度特性を有し、かつ適度の自然崩壊
性を有するポリエチレン系モノフィラメントが提供され
る。(Effects of the Invention) According to the present invention, a polyethylene monofilament is provided which has strength and elongation properties almost comparable to those of ordinary polyethylene monofilament and has appropriate natural disintegration properties.
そして1本発明のモノフィラメントは、漁網。And one monofilament of the present invention is a fishing net.
釣り糸6農業用資材等として好適であり、使用後光及び
/又は微生物が存在する環境に放置しておけば、一定期
間後には自然に崩壊してしまうため。Fishing line 6 Suitable as agricultural materials, etc., because if left in an environment where light and/or microorganisms exist after use, it will naturally disintegrate after a certain period of time.
本発明のモノフィラメントを使用すれば、特別な廃棄物
処理を必要とすることなく、公害を防止することができ
る。By using the monofilament of the present invention, pollution can be prevented without requiring special waste treatment.
Claims (2)
重量%の一酸化炭素又はこれと他のエチレン性不飽和化
合物とを共重合した変性ポリエチレン20〜50重量%
、ポリカプロラクトン3〜30重量%及び高密度ポリエ
チレン20〜77重量%とからなり、下記(a)〜(c
)の特性を同時に満足することを特徴とする自然崩壊性
モノフィラメント。 (a)引張強度3g/d以上 (b)結節強度2g/d以上 (c)切断伸度5%以上(1) Ethylene is the main component, 1.5 to 7.0
20 to 50% by weight of modified polyethylene copolymerized with carbon monoxide or other ethylenically unsaturated compounds
, 3 to 30% by weight of polycaprolactone and 20 to 77% by weight of high-density polyethylene, and the following (a) to (c)
) A naturally disintegrating monofilament characterized by simultaneously satisfying the following characteristics. (a) Tensile strength of 3 g/d or more (b) Knot strength of 2 g/d or more (c) Cutting elongation of 5% or more
ル酸エチルである請求項1記載の自然崩壊性モノフィラ
メント。(2) The self-disintegrating monofilament according to claim 1, wherein the ethylenically unsaturated compound is vinyl acetate or ethyl acrylate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33977689A JPH03199417A (en) | 1989-12-27 | 1989-12-27 | Naturally degradative monofilament |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33977689A JPH03199417A (en) | 1989-12-27 | 1989-12-27 | Naturally degradative monofilament |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03199417A true JPH03199417A (en) | 1991-08-30 |
Family
ID=18330701
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33977689A Pending JPH03199417A (en) | 1989-12-27 | 1989-12-27 | Naturally degradative monofilament |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03199417A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05105771A (en) * | 1991-10-16 | 1993-04-27 | Gunze Ltd | Improvement in melting point of polycaprolactone |
| WO2016108154A1 (en) * | 2014-12-31 | 2016-07-07 | Orfit Industries N.V. | Immobilisation element and additive manufacturing method for making same |
-
1989
- 1989-12-27 JP JP33977689A patent/JPH03199417A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05105771A (en) * | 1991-10-16 | 1993-04-27 | Gunze Ltd | Improvement in melting point of polycaprolactone |
| WO2016108154A1 (en) * | 2014-12-31 | 2016-07-07 | Orfit Industries N.V. | Immobilisation element and additive manufacturing method for making same |
| CN107438512A (en) * | 2014-12-31 | 2017-12-05 | 奥菲特工业公司 | Retaining element and the Additional manufacturing methods for the retaining element to be made |
| US10864099B2 (en) | 2014-12-31 | 2020-12-15 | Orfit Industries N.V. | Immobilisation element and additive manufacturing method for making same |
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