JPH0641816A - Fiber for underwater material - Google Patents

Fiber for underwater material

Info

Publication number
JPH0641816A
JPH0641816A JP21368892A JP21368892A JPH0641816A JP H0641816 A JPH0641816 A JP H0641816A JP 21368892 A JP21368892 A JP 21368892A JP 21368892 A JP21368892 A JP 21368892A JP H0641816 A JPH0641816 A JP H0641816A
Authority
JP
Japan
Prior art keywords
fiber
polymer
antifouling
antifouling agent
core
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
Application number
JP21368892A
Other languages
Japanese (ja)
Other versions
JP3150205B2 (en
Inventor
Madoka Hirano
まどか 平野
Naotaka Kanemoto
直貴 金元
Masatsugu Mochizuki
政嗣 望月
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unitika Ltd
Original Assignee
Unitika Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Unitika Ltd filed Critical Unitika Ltd
Priority to JP21368892A priority Critical patent/JP3150205B2/en
Publication of JPH0641816A publication Critical patent/JPH0641816A/en
Application granted granted Critical
Publication of JP3150205B2 publication Critical patent/JP3150205B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Multicomponent Fibers (AREA)

Abstract

PURPOSE:To obtain fiber for underwater materials, capable of preventing organisms such as algae or shellfishes from propagating and sticking thereto and excellent in antifouling effects and durability of the fiber, CONSTITUTION:The objective fiber for underwater materials is composed of conjugate fiber comprising an undecomposable fiber-forming synthetic polymer as a core component and a composition prepared by blending a mixture of the undecomposable fiber-forming synthetic polymer with a decomposable polymer (e.g. polycaprolactone) with an antifouling agent as a sheath component.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、養殖網、定置網等の漁
網や係留ロープ等の水中資材用繊維に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fishing net such as an aquaculture net or a stationary net, and a fiber for an underwater material such as a mooring rope.

【0002】[0002]

【従来の技術】養殖網や定置網等は長期間海水中に浸漬
された状態で使用されるため、藻類や貝類等の海中生物
が付着して繁殖し、網目の閉塞による酸素欠乏からくる
魚類の成育阻害や網重量の増大等が発生し、漁業関係者
にとって深刻な問題となっている。
2. Description of the Related Art Since aquaculture nets and set nets are used in a state of being immersed in seawater for a long period of time, aquatic organisms such as algae and shellfish attach to them and propagate, resulting in fish deficiency due to oxygen deficiency due to occlusion of the net. Growth inhibition and net weight increase have become a serious problem for fisheries personnel.

【0003】この対策として、従来、養殖網や定置網等
に防汚剤を含有した塗料や組成物によるコーティング処
理を施すことが行われている。そして、この防汚剤とし
てトリフェニル錫もしくはトリアルキル錫の酸化物、水
酸化物、塩化物又は有機酸のエステル等の有機錫化合物
が一般に用いられていたが、有機錫化合物は毒性を有
し、海洋汚染や魚体への悪影響等の問題があり、使用が
規制されるようになってきた。
As a countermeasure against this, conventionally, aquaculture nets or stationary nets have been subjected to coating treatment with a paint or composition containing an antifouling agent. As the antifouling agent, an organotin compound such as an oxide, hydroxide, chloride or ester of an organic acid of triphenyltin or trialkyltin is generally used, but the organotin compound has toxicity. However, due to problems such as marine pollution and adverse effects on fish bodies, their use has come to be regulated.

【0004】また、防汚剤を含む塗料等による後処理法
は、処理工程を必要とするためコスト高になると共に、
工程中に防汚剤の毒性のため作業員が気分を害したり、
頭痛やめまいを起こす等、作業環境を著しく悪化させる
という安全衛生上大きな問題があった。そればかりか、
使用中に防汚剤が脱落し、藻類や貝類等の生物が繁殖し
て付着するのを防止する防汚効果の耐久性に乏しいとい
う問題があった。
Further, the post-treatment method using a paint containing an antifouling agent requires a treatment step, resulting in high cost and
Workers are offended during the process due to the toxicity of antifouling agents,
There was a major safety and health problem that the work environment was significantly deteriorated, such as headaches and dizziness. Not only that,
There is a problem that the antifouling effect is poor in durability, which prevents the antifouling agent from falling off during use and breeding and adhesion of organisms such as algae and shellfish.

【0005】このような問題を解決するものとして、通
常の非分解性高分子から繊維を製造する際に非有機錫化
合物系の防汚剤を混入した防汚性繊維が、特開平1−17
4609号公報、同2−182912号公報等で提案されている。
しかし、これらの繊維は、防汚剤の溶出が不十分なため
か防汚効果が十分でなく、特に富栄養化の進んだ海域で
は比較的早期に藻類の付着が発生するという問題があっ
た。
As a solution to such a problem, an antifouling fiber containing a nonorganotin compound antifouling agent in the case of producing a fiber from an ordinary non-degradable polymer is disclosed in Japanese Patent Application Laid-Open No. 1-17.
It is proposed in Japanese Patent Nos. 4609 and 2-182912.
However, these fibers do not have sufficient antifouling effect, probably due to insufficient elution of the antifouling agent, and there was a problem that algae adhered relatively early especially in the sea area where eutrophication was advanced. .

【0006】カナダ特許出願公開第 2044512号公報に
は、微生物分解性高分子であるポリカプロラクトンに銅
又は銀イオン放出水溶性ガラスを配合した組成物で構成
された水中資材用繊維が開示されている。この繊維は、
分解性高分子で構成されているため防汚剤の溶出性が良
好で、優れた防汚効果を発揮することが期待されるが、
5カ月で強度が急激に低下し、繊維の耐久性に乏しいと
いう問題があった。
[0006] Canadian Patent Application Publication No. 2044512 discloses a fiber for an underwater material composed of a composition in which copper or silver ion-releasing water-soluble glass is mixed with polycaprolactone which is a microbial degradable polymer. . This fiber is
Since it is composed of degradable polymers, the antifouling agent has good elution properties and is expected to exhibit an excellent antifouling effect.
There was a problem that the strength dropped sharply after 5 months and the durability of the fiber was poor.

【0007】本発明者等は、芯鞘構造の複合繊維とし、
芯成分としては通常の非分解性高分子を用い、鞘成分に
防汚剤を配合した分解性高分子を用いた水中資材用繊維
を先に提案した(特願平3−270060号)。この繊維は、
一定量以上の防汚剤を溶出することにより優れた防汚効
果を発揮し、繊維の耐久性においても優れた効果を示し
たが、鞘成分が分解性高分子からなるため比較的分解が
早く進み、防汚効果の耐久性に問題があることが分かっ
た。
The present inventors have made a composite fiber having a core-sheath structure,
A fiber for an underwater material using an ordinary non-degradable polymer as a core component and a degradable polymer with an antifouling agent mixed in a sheath component was previously proposed (Japanese Patent Application No. 3-270060). This fiber is
It exerted an excellent antifouling effect by eluting a certain amount or more of the antifouling agent, and it also showed an excellent effect on the durability of the fiber, but it decomposes relatively quickly because the sheath component is composed of degradable polymer. It was found that there was a problem with the durability of the antifouling effect.

【0008】[0008]

【発明が解決しようとする課題】本発明は、繊維の製造
時に防汚剤を混入した水中資材用繊維において、防汚効
果の耐久性と繊維の耐久性の両者が共に良好な水中資材
用繊維を提供しようとするものである。
DISCLOSURE OF THE INVENTION The present invention relates to a fiber for an underwater material in which an antifouling agent is mixed during the production of the fiber, and the fiber for the underwater material is excellent in both the antifouling effect durability and the fiber durability. Is to provide.

【0009】[0009]

【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、その要旨は、非分解性繊維形成性
合成高分子を芯成分とし、非分解性繊維形成性合成高分
子と分解性高分子の混合物に防汚剤を配合した組成物を
鞘成分とする複合繊維からなる水中資材用繊維にある。
The present invention is to solve the above-mentioned problems, and the gist thereof is to use a non-degradable fiber-forming synthetic polymer as a core component. And a degradable polymer mixture containing a stainproofing agent in the composition as a sheath component.

【0010】以下、本発明について詳細に説明する。本
発明において芯成分及び鞘成分の非分解性繊維形成性高
分子としては、ポリエチレンテレフタレート、ポリブチ
レンテレフタレート等のポリエステル、ナイロン6、ナ
イロン66、ナイロン46、ナイロン11、ナイロン12等
のポリアミド、ポリエチレン、ポリプロピレン等のポリ
オレフィン等が挙げられる。これらは用途に応じて適当
なものを選定して用いられ、養殖網としてはポリエチレ
ン又はナイロン6、定置網としてはポリエチレンテレフ
タレート又はナイロン6が好ましい。
The present invention will be described in detail below. In the present invention, as the non-degradable fiber-forming polymer for the core component and the sheath component, polyesters such as polyethylene terephthalate and polybutylene terephthalate, polyamides such as nylon 6, nylon 66, nylon 46, nylon 11 and nylon 12, polyethylene, Examples include polyolefins such as polypropylene. These are selected and used appropriately according to the application, and polyethylene or nylon 6 is preferable as the aquaculture net, and polyethylene terephthalate or nylon 6 is preferable as the stationary net.

【0011】また、本発明で用いられる防汚剤として
は、海洋汚染や魚体への悪影響等の問題のない非有機錫
化合物系のもので、耐熱性のあるものが用いられる。防
汚剤の具体例としては、銅粉、亜酸化銅粉、ニッケル/
銅の配合比が10/90であるニッケル銅粉、マンガン粉、
2−メルカプトベンゾチアゾール亜鉛、ジメチルジチオ
カルバミン酸銅等が挙げられる。
As the antifouling agent used in the present invention, a non-organotin compound based anti-fouling agent having no problem of marine pollution and adverse effects on fish bodies and having heat resistance is used. Specific examples of the antifouling agent include copper powder, cuprous oxide powder, nickel /
Nickel copper powder, manganese powder, which has a copper mixture ratio of 10/90,
Examples include 2-mercaptobenzothiazole zinc, copper dimethyldithiocarbamate, and the like.

【0012】防汚剤は、粒子径10μm以下、好ましくは
5μm以下の粉体として用いるのが好ましい。防汚剤の
粒子径が大きいと延伸時にネッキング部分に空隙がで
き、その部分で切断が起こるという問題があり、また、
粒子径が小さい方が表面積が大きくなって防汚効果が良
好となる。
The antifouling agent is preferably used as a powder having a particle size of 10 μm or less, preferably 5 μm or less. When the particle size of the antifouling agent is large, there is a problem that voids are formed in the necking portion during stretching, and cutting occurs at that portion.
The smaller the particle size, the larger the surface area and the better the antifouling effect.

【0013】本発明で用いられる分解性高分子として
は、ポリ−ε−カプロラクトン、ポリ−3−ヒドロキシ
ブチレート/ポリ−3−ヒドロキシバリレート共重合
体、ポリグリコール酸、ポリ乳酸等の脂肪族ポリエステ
ルやポリ−ε−カプロラクトン等の脂肪族ポリエステル
とナイロン6等のポリアミドとの共重合体等が挙げられ
る。これらは、水中において微生物によって分解し、最
終的には二酸化炭素と水になるため、海洋汚染、魚体へ
の悪影響等を与えない。
Examples of the degradable polymer used in the present invention include aliphatic compounds such as poly-ε-caprolactone, poly-3-hydroxybutyrate / poly-3-hydroxyvalerate copolymer, polyglycolic acid and polylactic acid. Examples thereof include copolymers of polyesters and aliphatic polyesters such as poly-ε-caprolactone and polyamides such as nylon 6. These are decomposed by microorganisms in water, and finally become carbon dioxide and water, so that they do not cause marine pollution or adverse effects on fish bodies.

【0014】鞘成分に防汚剤を配合した分解性高分子の
みを用いた繊維では、防汚剤の初期の溶出速度は大きい
が、防汚効果の耐久性に乏しかったが、本発明の繊維で
は、非分解性高分子と分解性高分子との混合物に防汚剤
が配合されているため、防汚剤の溶出速度のコントロー
ルが可能であり、分解性高分子がすべて分解された後も
非分解性高分子に含まれた防汚剤により防汚効果の継続
が認められる。繊維の強度は、多少低下がみられるが、
実用上問題はない。
The fiber using only the decomposable polymer containing the antifouling agent in the sheath component has a high initial elution rate of the antifouling agent, but is poor in antifouling effect durability, but the fiber of the present invention. Since the antifouling agent is blended in the mixture of the non-degradable polymer and the degradable polymer, it is possible to control the elution rate of the antifouling agent, and even after the degradable polymer is completely decomposed. Continuation of antifouling effect is recognized by the antifouling agent contained in the non-degradable polymer. Although the strength of the fiber is slightly reduced,
There is no problem in practical use.

【0015】本発明の繊維の芯/鞘複合重量比は1/1
〜5/1が適当であり、およそ4/1が繊維の強度及び
防汚効果の点で最も好ましい。芯/鞘複合重量比が1/
1より小さいと繊維の強度が低く、5/1より大きいと
防汚効果が小さくなると共に複合紡糸が困難になり、実
用上好ましくない。
The core / sheath composite weight ratio of the fiber of the present invention is 1/1.
Approximately 5/1 is suitable, and approximately 4/1 is most preferable in terms of fiber strength and antifouling effect. The core / sheath composite weight ratio is 1 /
When it is less than 1, the strength of the fiber is low, and when it is more than 5/1, the antifouling effect becomes small and the composite spinning becomes difficult, which is not preferable in practice.

【0016】また、鞘成分の組成は、非分解性繊維形成
性高分子30〜85重量%、分解性高分子10〜30重量%及び
防汚剤5〜40重量%とすることが適当である。そして、
鞘成分における非分解性繊維形成性高分子と分解性高分
子との割合は重量比で6/4〜9/1の範囲が好まし
く、この割合があまり小さいと繊維の耐摩耗性が低くな
り、逆に大きすぎると防汚剤の溶出速度が遅くなって防
汚効果が小さくなる。また、鞘成分に対する防汚剤の含
有量が5重量%未満であると防汚効果が小さくなり、一
方、40重量%を超えるとポリマー中への練込みが困難に
なり、好ましくない。
The composition of the sheath component is preferably 30 to 85% by weight of non-degradable fiber-forming polymer, 10 to 30% by weight of degradable polymer and 5 to 40% by weight of antifouling agent. . And
The ratio of the non-degradable fiber-forming polymer and the degradable polymer in the sheath component is preferably in the range of 6/4 to 9/1 by weight ratio, and if this ratio is too small, the abrasion resistance of the fiber becomes low, On the other hand, if it is too large, the elution rate of the antifouling agent becomes slow and the antifouling effect becomes small. Further, if the content of the antifouling agent with respect to the sheath component is less than 5% by weight, the antifouling effect becomes small, while if it exceeds 40% by weight, it is difficult to knead into the polymer, which is not preferable.

【0017】[0017]

【実施例】次に、本発明を実施例により具体的に説明す
る。なお、防汚効果は、次の懸垂試験により判定した。 懸垂試験 糸条を合撚して約 20000デニールの撚糸とし、これを用
いて40cm×40cmの大きさの網を作成し、60cm×60cmのス
テンレス製枠に取り付け、淡路島地区の海中に水深1〜
2mの位置で懸垂し、6、12、18カ月経過後に引き上
げ、生物の付着状況を観察し、次の4段階で評価した。 ◎:付着なし ○:少々付着あり △:半分程度付着あり ×:全面に付着あり また、引張強度は、JIS L 1013 (1981) に準じて測定し
た。
EXAMPLES Next, the present invention will be specifically described by way of examples. The antifouling effect was determined by the following suspension test. Suspension test A yarn of about 20000 denier is twisted into a twisted yarn, and a net with a size of 40 cm x 40 cm is made using this and attached to a stainless steel frame with a size of 60 cm x 60 cm.
Suspended at a position of 2 m, pulled up after 6, 12, and 18 months, observed the state of attachment of organisms, and evaluated in the following four stages. ◎: No adhesion ○: A little adhesion △: About half adhesion ×: Adhesion on the entire surface The tensile strength was measured according to JIS L 1013 (1981).

【0018】実施例1〜4 96%硫酸を溶媒とし、濃度1g/dl、温度25℃で測定し
た相対粘度が 3.4のナイロン6(N6)及びASTM No.E
法(190℃、2.16kg)に準じて測定したメルトインデック
スが4.0g/10minのポリ−ε−カプロラクトン(PC
L)に平均粒子径が3.79μmの微細銅粉(Cu)をそれ
ぞれ30重量%練込み、2種類のマスターチップを得た。
芯成分を相対粘度が 3.4のN6、鞘成分を上記2種類の
マスターチップを表1に示した組成となるように混合し
たものとし、芯/鞘複合重量比4/1の芯鞘複合モノフ
ィラメントを次のようにして製造した。エクストルーダ
ー型溶融紡糸機を用い、ノズル孔径 1.0mmφ、ホール数
4の芯鞘複合紡糸口金を使用し、紡糸温度 275℃で紡出
し、エアーギャップを介して15℃の水浴中で冷却した
後、20m/minの速度で引取り、直ちに、1段目は85℃の
温水バスを用い、延伸倍率3.0〜3.5倍で、2段目は 200
℃、1mの非接触加熱ヒータを用い、全延伸倍率4.8〜
5.2倍で延伸し、400 デニールの芯鞘複合モノフィラメ
ントを得た。
Examples 1 to 4 Nylon 6 (N6) having a relative viscosity of 3.4 measured at a concentration of 1 g / dl and a temperature of 25 ° C. using 96% sulfuric acid as a solvent and ASTM No.E.
Melt index measured according to the method (190 ℃, 2.16kg) of 4.0g / 10min poly-ε-caprolactone (PC
L) was kneaded with 30% by weight of fine copper powder (Cu) having an average particle diameter of 3.79 μm to obtain two types of master chips.
The core component was N6 having a relative viscosity of 3.4, and the sheath component was a mixture of the above two kinds of master chips so as to have the composition shown in Table 1. A core-sheath composite monofilament having a core / sheath composite weight ratio of 4/1 was prepared. It was manufactured as follows. Using an extruder-type melt spinning machine, using a core-sheath composite spinneret with a nozzle hole diameter of 1.0 mm and a number of holes of 4, spinning at a spinning temperature of 275 ° C and cooling in a water bath of 15 ° C through an air gap, At the speed of 20 m / min, immediately draw the first stage using a hot water bath at 85 ° C and draw at a draw ratio of 3.0 to 3.5 times.
Using a non-contact heater at 1 ° C and 1 m, total draw ratio 4.8-
It was drawn at 5.2 times to obtain a 400 denier core-sheath composite monofilament.

【0019】比較例1〜3 比較例1として、鞘成分にPCLを含まないもの、比較
例2(コントロール)として、鞘成分にPCL及びCu
を含まないもの、比較例3として、鞘成分にN6を含ま
ないものを用い、実施例1〜4と同様にして芯鞘複合モ
ノフィラメントを得た。
Comparative Examples 1 to 3 In Comparative Example 1, the sheath component does not contain PCL, and in Comparative Example 2 (control), the sheath component is PCL and Cu.
A core-sheath composite monofilament was obtained in the same manner as in Examples 1 to 4, except that the core component did not contain N6 and the sheath component did not contain N6.

【0020】実施例1〜4及び比較例1〜3で得られた
モノフィラメントの強度及び懸垂試験の結果を表1に示
す。
Table 1 shows the strength and suspension test results of the monofilaments obtained in Examples 1 to 4 and Comparative Examples 1 to 3.

【0021】[0021]

【表1】 [Table 1]

【0022】実施例5〜6 メルトインデックスが1.0g/10minの直鎖状ポリエチレ
ン(PE)及びメルトインデックスが4.0g/10minのP
CLに平均粒子径が3.79μmのCuをそれぞれ30重量%
練込み、2種類のマスターチップを得た。芯成分をメル
トインデックスが1.0g/10minのPE、鞘成分を上記2
種類のマスターチップを表2に示した組成となるように
混合したものとし、芯/鞘複合重量比4/1の芯鞘複合
モノフィラメントを次のようにして製造した。エクスト
ルーダー型溶融紡糸機を用い、ノズル孔径 1.0mmφ、ホ
ール数4の芯鞘複合紡糸口金を使用し、紡糸温度 285℃
で紡出し、エアーギャップを介して5℃の水浴中で冷却
後、10m/minの速度で引取り、直ちに、1段目は85℃の
温水バスを用い、延伸倍率8.0〜10.0倍、2段目は120
℃、1mの非接触加熱ヒータを用い、全延伸倍率9.0〜1
0.5倍で延伸し、400デニールの芯鞘複合モノフィラメン
トを得た。
Examples 5 to 6 Linear polyethylene (PE) having a melt index of 1.0 g / 10 min and P having a melt index of 4.0 g / 10 min
30% by weight of Cu with an average particle size of 3.79 μm in each CL
Two types of master chips were obtained by kneading. The core component is PE with a melt index of 1.0 g / 10 min, and the sheath component is the above 2
A master-sheath composite monofilament having a core / sheath composite weight ratio of 4/1 was prepared as follows by mixing different types of master chips so as to have the composition shown in Table 2. Using an extruder type melt spinning machine, using a core-sheath composite spinneret with a nozzle hole diameter of 1.0 mmφ and 4 holes, the spinning temperature is 285 ° C.
After cooling in a water bath at 5 ° C through an air gap, it is drawn at a speed of 10 m / min. Immediately, the first stage uses a hot water bath at 85 ° C, draw ratio 8.0 to 10.0 times, 2 stages Eyes 120
℃, 1m non-contact heater, total draw ratio 9.0-1
It was stretched 0.5 times to obtain a core-sheath composite monofilament of 400 denier.

【0023】比較例4〜5 比較例4として、鞘成分にPCLを含まないもの、比較
例5(コントロール)として、鞘成分にPCL及びCu
を含まないものを用い、実施例5〜6と同様にして芯鞘
複合モノフィラメントを得た。
Comparative Examples 4 to 5 As Comparative Example 4, one containing no PCL in the sheath component, and as Comparative Example 5 (control), PCL and Cu in the sheath component.
A core-sheath composite monofilament was obtained in the same manner as in Examples 5 to 6 using a material not containing.

【0024】実施例5〜6及び比較例4〜5で得られた
モノフィラメントの強度及び懸垂試験の結果を表2に示
す。
Table 2 shows the strength and suspension test results of the monofilaments obtained in Examples 5-6 and Comparative Examples 4-5.

【0025】[0025]

【表2】 [Table 2]

【0026】実施例7〜8 テトラクロルエタンとフェノールとの等重量混合物を溶
媒とし、濃度 0.5g/dl、温度20℃で測定した相対粘度
が1.47のポリエチレンテレフタレート(PET)及びメ
ルトインデックスが4.0g/10minのPCLに平均粒子径
が 0.9μmの微細亜酸化銅粉(Cu2O)をそれぞれ30
重量%練込み、2種類のマスターチップを得た。芯成分
を相対粘度が1.47のPETとし、鞘成分を上記2種類の
マスターチップを表3に示した組成となるように混合し
たものとし、芯/鞘複合重量比2/1の芯鞘複合マルチ
フィラメントを次のようにして製造した。エクストルー
ダー型溶融紡糸機を用い、ノズル孔径 0.5mmφ、ホール
数24の芯鞘複合紡糸口金を使用し、紡糸温度290℃で紡
出し、200m/minの速度で引取り、直ちに、1段目は90
℃の加熱ローラを用い、延伸倍率3.0〜3.8倍、2段目は
160℃の加熱ローラを用い、全延伸倍率5.0〜5.4倍で延
伸し、 250デニールの芯鞘複合マルチフィラメントを得
た。
Examples 7 to 8 Polyethylene terephthalate (PET) having a relative viscosity of 1.47 measured at a temperature of 20 ° C. and a concentration of 0.5 g / dl and a melt index of 4.0 g, using an equal weight mixture of tetrachloroethane and phenol as a solvent. 30 minutes each of fine cuprous oxide powder (Cu 2 O) with an average particle size of 0.9 μm in PCL of / 10 min.
Two kinds of master chips were obtained by kneading by weight. The core component is PET having a relative viscosity of 1.47, and the sheath component is a mixture of the above two types of master chips so as to have the composition shown in Table 3, and the core / sheath composite weight ratio is 2/1. The filament was manufactured as follows. Using an extruder type melt spinning machine, using a core-sheath composite spinneret with a nozzle hole diameter of 0.5 mm and a number of holes of 24, spinning at a spinning temperature of 290 ° C., drawing at a speed of 200 m / min, immediately the first stage 90
Using a heating roller at ℃, draw ratio 3.0 to 3.8 times, the second stage
Using a heating roller at 160 ° C., it was drawn at a total draw ratio of 5.0 to 5.4 times to obtain a 250 denier core-sheath composite multifilament.

【0027】比較例6〜7 比較例6として、鞘成分にPCLを含まないもの、比較
例7(コントロール)として、鞘成分にPCL及びCu
2Oを含まないものを用い、実施例7〜8と同様にして
芯鞘複合マルチフィラメントを得た。
Comparative Examples 6 to 7 As Comparative Example 6, one containing no PCL in the sheath component, and as Comparative Example 7 (control), PCL and Cu in the sheath component.
A core-sheath composite multifilament was obtained in the same manner as in Examples 7 to 8 using a material not containing 2 O.

【0028】実施例7〜8及び比較例6〜7で得られた
マルチフィラメントの強度及び懸垂試験の結果を表3に
示す。
Table 3 shows the strength and suspension test results of the multifilaments obtained in Examples 7 to 8 and Comparative Examples 6 to 7.

【0029】[0029]

【表3】 [Table 3]

【0030】次に、上記実施例及び比較例で得られた糸
条について、次のようにして銅イオンの溶出量の経時変
化を調べた。長さ2cmに切断した試料20gに水 200mlを
加えて密栓し、1カ月毎に水を入れ換え、銅イオンの濃
度を測定した。なお、銅イオンの濃度の測定は、誘導結
合プラズマによる発光分光分析法に準じて、ICAP−575
IIを使用して行った。結果を表4に示す。(表4におい
て、「3カ月」とは3カ月経過後の1カ月間に溶出した
銅イオンの濃度を意味し、以下同様である。)
Next, with respect to the yarns obtained in the above-mentioned Examples and Comparative Examples, changes in the elution amount of copper ions with time were examined as follows. 200 ml of water was added to 20 g of a sample cut into a length of 2 cm, the container was sealed, water was replaced every month, and the concentration of copper ions was measured. The concentration of copper ions was measured according to the emission spectroscopy analysis method using inductively coupled plasma according to ICAP-575.
Performed using II. The results are shown in Table 4. (In Table 4, "3 months" means the concentration of copper ions eluted in one month after the lapse of three months, and the same applies hereinafter.)

【0031】[0031]

【表4】 [Table 4]

【0032】表4から明らかなように、鞘成分に非分解
性高分子と分解性高分子(PCL)を組み合わせて用い
ることにより長期間安定して銅イオンが溶出し、また、
分解性高分子の混合比を変化させることにより、溶出量
をコントロールできることが分かる。
As is clear from Table 4, by using a non-decomposable polymer and a decomposable polymer (PCL) in combination in the sheath component, copper ions were stably eluted for a long period of time, and
It can be seen that the elution amount can be controlled by changing the mixing ratio of the degradable polymer.

【0033】[0033]

【発明の効果】本発明の繊維は、鞘成分に非分解性の繊
維形成性合成高分子と分解性高分子の混合物を使用し、
これに防汚剤を配合してあるので、防汚剤を長期間安定
して溶出させる効果があり、防汚効果の耐久性に優れて
いる。また、本発明の繊維は、芯成分に非分解性の繊維
形成性合成高分子を使用しているので、繊維の耐久性に
も優れている。
The fiber of the present invention uses a mixture of a non-degradable fiber-forming synthetic polymer and a degradable polymer as the sheath component,
Since the antifouling agent is added to this, it has an effect of eluting the antifouling agent stably for a long period of time, and is excellent in durability of the antifouling effect. Further, the fiber of the present invention uses a non-decomposable fiber-forming synthetic polymer as the core component, and therefore has excellent fiber durability.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 非分解性繊維形成性合成高分子を芯成分
とし、非分解性繊維形成性合成高分子と分解性高分子の
混合物に防汚剤を配合した組成物を鞘成分とする複合繊
維からなる水中資材用繊維。
1. A composite comprising a non-degradable fiber-forming synthetic polymer as a core component, and a composition comprising a mixture of a non-degradable fiber-forming synthetic polymer and a degradable polymer and an antifouling agent as a sheath component. Fiber for underwater materials made of fiber.
【請求項2】 鞘成分の組成物が、非分解性繊維形成性
高分子30〜85重量%、分解性高分子10〜30重量%及び防
汚剤5〜40重量%からなるものである請求項1記載の水
中資材用繊維。
2. The composition of the sheath component is composed of 30 to 85% by weight of non-degradable fiber-forming polymer, 10 to 30% by weight of degradable polymer and 5 to 40% by weight of antifouling agent. The fiber for underwater materials according to Item 1.
JP21368892A 1992-07-16 1992-07-16 Fiber for underwater materials Expired - Fee Related JP3150205B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21368892A JP3150205B2 (en) 1992-07-16 1992-07-16 Fiber for underwater materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21368892A JP3150205B2 (en) 1992-07-16 1992-07-16 Fiber for underwater materials

Publications (2)

Publication Number Publication Date
JPH0641816A true JPH0641816A (en) 1994-02-15
JP3150205B2 JP3150205B2 (en) 2001-03-26

Family

ID=16643342

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21368892A Expired - Fee Related JP3150205B2 (en) 1992-07-16 1992-07-16 Fiber for underwater materials

Country Status (1)

Country Link
JP (1) JP3150205B2 (en)

Also Published As

Publication number Publication date
JP3150205B2 (en) 2001-03-26

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