JPH05125665A - Deodorizing fiber and its production - Google Patents

Deodorizing fiber and its production

Info

Publication number
JPH05125665A
JPH05125665A JP3286716A JP28671691A JPH05125665A JP H05125665 A JPH05125665 A JP H05125665A JP 3286716 A JP3286716 A JP 3286716A JP 28671691 A JP28671691 A JP 28671691A JP H05125665 A JPH05125665 A JP H05125665A
Authority
JP
Japan
Prior art keywords
fiber
deodorant
deodorizing
paraffin wax
pores
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
JP3286716A
Other languages
Japanese (ja)
Other versions
JP3165485B2 (en
Inventor
Isamu Takahashi
勇 高橋
Shigeki Hayashi
茂樹 林
Yoshio Iida
祥夫 飯田
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.)
Ube Exsymo Co Ltd
Original Assignee
Ube Nitto Kasei Co 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 Ube Nitto Kasei Co Ltd filed Critical Ube Nitto Kasei Co Ltd
Priority to JP28671691A priority Critical patent/JP3165485B2/en
Priority to US07/852,259 priority patent/US5480712A/en
Priority to PCT/JP1991/001690 priority patent/WO1993009277A1/en
Priority to EP19920900894 priority patent/EP0565720A4/en
Publication of JPH05125665A publication Critical patent/JPH05125665A/en
Application granted granted Critical
Publication of JP3165485B2 publication Critical patent/JP3165485B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Landscapes

  • Artificial Filaments (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Abstract

PURPOSE:To obtain a deodorizing fiber capable of exhibiting large deodorizing effect using a small amount of deodorizing substance by coating the surface of a polyolefin fiber having a number of pores and the inside of the pores with a deodorizing substance. CONSTITUTION:A polyolefin resin such as polyethylene or polypropylene is mixed with paraffin wax and subjected to melt spinning, drawing and heat treatment and then the paraffin wax is removed with a hydrocarbon based solvent such as hexane to afford a porous fiber and the obtained porous fiber is dipped in an alcohol solution of deodorizing substance such as extract of Quercus stenophylla Makino or extract of Chelonopsis moschata Miq. and dried. Thereby the deodorizing agent is applied to the outer surface of the porous fiber and inner surface of pores to provide the objective deodorizing fiber having large deodorizing effect.

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、空気中に拡散した悪臭
成分を吸着消臭する繊維およびその製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fiber for adsorbing and deodorizing malodorous components diffused in the air and a method for producing the same.

【0002】[0002]

【従来の技術】従来より、繊維製品に消臭機能を持たせ
る加工方法は数多く提案されている。この種の加工方法
として代表的なものは、例えば、ゼオライト,活性炭,
シリカゲルなどの吸着性能を有する多孔質物質と、合成
樹脂原料を混合して溶融紡糸した後に、延伸して繊維表
面に多孔質物質を配置した繊維や、通常の製法で製造さ
れた合成繊維の表面に多孔質物質などの消臭性物質をコ
ーティングした繊維などが知られている。しかしなが
ら、これらの消臭繊維には、以下に説明する技術的課題
が指摘されていた。
2. Description of the Related Art Conventionally, many processing methods have been proposed for imparting a deodorizing function to textile products. Typical processing methods of this kind are, for example, zeolite, activated carbon,
The surface of a synthetic material manufactured by a normal manufacturing method, or fibers in which a porous material having adsorption performance such as silica gel and a synthetic resin raw material are mixed and melt-spun, and then stretched to dispose the porous material on the fiber surface. Fibers and the like, which are coated with a deodorant substance such as a porous substance, are known. However, the technical problems described below have been pointed out for these deodorant fibers.

【0003】[0003]

【発明が解決しようとする課題】すなわち、上述した多
孔質物質を混合する消臭繊維の製造方法では、繊維の消
臭性能を向上させるには、多孔質物質の添加量を増すこ
とになる。ところが、このように多孔質物質の添加量を
増加させると、繊維の製造工程で紡糸性や延伸性が低下
し、その結果、比較的大径の繊維しか得られない上に、
内部に埋没している多孔質物質が消臭性能の向上に余り
寄与しないので、添加量の割りにはその消臭性能が低い
繊維しか得られない。
That is, in the method for producing a deodorant fiber in which the above-mentioned porous substance is mixed, in order to improve the deodorant performance of the fiber, the amount of the porous substance added is increased. However, when the amount of the porous substance added is increased in this way, the spinnability and the drawability are lowered in the fiber manufacturing process, and as a result, only fibers having a relatively large diameter are obtained.
Since the porous substance buried inside does not contribute much to the improvement of the deodorizing performance, only fibers having a low deodorizing performance can be obtained for the added amount.

【0004】一方、合成樹脂繊維の表面に消臭物質をコ
ーティングする方法では、繊維の表面積に限りがあるの
で、一定以上の消臭性能の向上が望めないし、加工途中
などでコーティングされた消臭物質が脱落して、消臭性
能が低下するという問題もあった。本発明は、このよう
な従来の問題点に鑑みてなされたものであり、その目的
とするところは、比較的細い繊維であっても大きな消臭
性能が得られる消臭繊維およびその製造方法を提供する
ことにある。
On the other hand, in the method of coating the surface of the synthetic resin fiber with the deodorant substance, since the surface area of the fiber is limited, it is not possible to expect the deodorant performance to be improved beyond a certain level. There is also a problem that the substances are dropped off and the deodorizing performance is lowered. The present invention has been made in view of such conventional problems, and an object thereof is to provide a deodorant fiber and a method for producing the deodorant fiber, which are capable of obtaining a large deodorant performance even with a relatively thin fiber. To provide.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、本発明の消臭繊維は、ポリオレフィン樹脂からなる
繊維本体と、前記ポリオレフィン樹脂とパラフィンワッ
クスとを混合し、溶融紡糸して、延伸,熱処理後に前記
パラフィンワックスを除去することにより形成される多
数の細孔と、前記繊維本体の表面と前記細孔の内面に付
着された消臭物質とからなることを特徴とする。
In order to achieve the above object, the deodorant fiber of the present invention comprises a fiber body composed of a polyolefin resin, a mixture of the polyolefin resin and paraffin wax, melt spinning, and stretching. It is characterized by comprising a large number of pores formed by removing the paraffin wax after heat treatment, and a deodorant substance attached to the surface of the fiber body and the inner surface of the pores.

【0006】また、上記消臭繊維の製造方法として、所
定量のポリオレフィン樹脂とパラフィンワックスとを溶
融下で混合し、この混合物を所定のドラフト率下で溶融
紡糸して未延伸繊維を得、次いで、この未延伸繊維を加
熱下で所定の倍率で延伸して、熱処理を施した後に、前
記パラフィンワックスを除去して多孔質繊維を得る工程
と、得られた多孔質繊維に消臭物質を付着する工程とか
らなることを特徴とする。
As a method for producing the deodorant fiber, a predetermined amount of a polyolefin resin and paraffin wax are mixed under melting, and this mixture is melt-spun under a predetermined draft ratio to obtain an unstretched fiber. The step of drawing the unstretched fiber under heating at a predetermined ratio and subjecting to heat treatment, and then removing the paraffin wax to obtain a porous fiber, and attaching a deodorant substance to the obtained porous fiber And a step of performing.

【0007】本発明に使用できるポリオレフィン樹脂と
しては、ポリエチレン,ポリプロピレンが好適であり、
ポリエチレンの場合は、メルトインデックス(MI)が
0.3〜20g/10分の高密度ポリエチレンが推奨さ
れる。また、ポリプロピレンとしては、密度が概ね0.
90以上のものであって、ASTM D1238に準じ
た測定方法によるメルトフローレート(MFR)値は、
0.5〜9.0 g/10分の範囲が好ましい。
Polyethylene and polypropylene are preferable as the polyolefin resin usable in the present invention.
In the case of polyethylene, high density polyethylene having a melt index (MI) of 0.3 to 20 g / 10 min is recommended. Further, as polypropylene, the density is about 0.
90 or more, and the melt flow rate (MFR) value by the measuring method according to ASTM D1238 is
The range of 0.5 to 9.0 g / 10 minutes is preferable.

【0008】MIないしはMFRが上記範囲を外れる
と、パラフィンワックスと混合した後における溶融紡糸
時の溶融粘度が不適性となり紡糸の際に問題が生じる。
本発明に使用するパラフィンワックスは、飽和脂肪族炭
化水素化合物を主体とするものであって、溶媒による易
溶出性の点から融点が概ね50〜70℃程度のものが好
ましい。
If the MI or MFR is out of the above range, the melt viscosity at the time of melt spinning after mixing with paraffin wax becomes unsuitable, causing a problem during spinning.
The paraffin wax used in the present invention is mainly composed of a saturated aliphatic hydrocarbon compound and preferably has a melting point of about 50 to 70 ° C. from the viewpoint of easy elution with a solvent.

【0009】上記ポリオレフィン樹脂とパラフィンワッ
クスとを、ポリオレフィン樹脂100重量部に対してパ
ラフィンワックス30〜300重量部の割合で溶融して
混合し溶融紡糸用の原料とすることにより好適な結果が
得られる。溶融紡糸温度は上記混合原料の溶融粘度に応
じて決められる。溶融紡糸機は、ポリオレフィン樹脂と
パラフィンワックスとの混合混練を促進するため、スク
リュウ式押出機を使用することが望ましい。溶融紡糸時
のドラフト、すなわち未延伸繊維の巻取速度と紡糸ノズ
ルからの吐出線速度との比は、400以下にすることが
望ましい。
Suitable results can be obtained by melting and mixing the above-mentioned polyolefin resin and paraffin wax at a ratio of 30 to 300 parts by weight of paraffin wax with respect to 100 parts by weight of the polyolefin resin to prepare a raw material for melt spinning. .. The melt spinning temperature is determined according to the melt viscosity of the mixed raw material. The melt spinning machine preferably uses a screw type extruder in order to promote mixing and kneading of the polyolefin resin and the paraffin wax. It is desirable that the draft during melt spinning, that is, the ratio of the winding speed of the undrawn fiber to the linear velocity of the discharge from the spinning nozzle is 400 or less.

【0010】ドラフトが400を越えるとポリプロピレ
ン結晶のサイズが小さくなり、最終的に得られる多孔質
繊維の細孔径が小さくなりすぎて空隙率も低くなる。上
述の条件で得られた未延伸繊維は、引き続いて延伸され
るが、延伸条件は60〜120℃の範囲で歪速度、すな
わち、供給ローラー速度をGF (m/分)、延伸側ロー
ラー速度をGT (m/分)、これらのローラー間の距離
をL(m)とするときに次式で定義される値が400%
以下であることが望ましい。
If the draft exceeds 400, the size of the polypropylene crystal becomes small, and the pore diameter of the finally obtained porous fiber becomes too small, resulting in a low porosity. The unstretched fibers obtained under the above conditions are subsequently stretched. The stretching conditions are strain rate in the range of 60 to 120 ° C., that is, the supply roller speed is GF (m / min) and the stretching side roller speed is GT (m / min), when the distance between these rollers is L (m), the value defined by the following formula is 400%
The following is desirable.

【0011】 歪速度(%/分)=(GT −GF )/L×100 歪速度が400%/分を越えると、得られる多孔質繊維
の細孔径が不均一となり孔の潰れた箇所がかなり発生す
る。延伸温度が上記の範囲を外れる場合、すなわち、6
0℃未満では、冷延伸となりパラフィンワックス抽出後
の収縮率が大きくなって空隙率が低下する。また、12
0℃を越えると、未延伸繊維が軟化しすぎるので有効な
延伸ができず繊維強度が低くなる。延伸倍率は、1.4
〜4.5倍の範囲とすることが好ましい。延伸倍率が
1.4倍未満では、空隙率が低くなり、4.5倍を越え
ると延伸により細孔が潰れた状態になる。
Strain rate (% / min) = (GT −GF) / L × 100 When the strain rate exceeds 400% / min, the pore diameter of the obtained porous fiber becomes non-uniform and the crushed locations of the pores are considerably large. Occur. When the stretching temperature is out of the above range, that is, 6
If the temperature is lower than 0 ° C., the film is cold-stretched and the shrinkage ratio after extraction of the paraffin wax is large and the porosity is reduced. Also, 12
If the temperature exceeds 0 ° C, the unstretched fibers are too soft, and effective stretching cannot be performed, resulting in low fiber strength. The draw ratio is 1.4
It is preferable to set the range to 4.5 times. If the stretching ratio is less than 1.4 times, the porosity becomes low, and if it exceeds 4.5 times, the pores are collapsed by the stretching.

【0012】上記延伸に引き続いて熱処理を施すが、こ
の熱処理は以降においてパラフィンワックスを溶剤によ
り抽出した後に、繊維が径方向及び軸方向に収縮して実
質的に空隙率を低下させるのを防ぐもので、熱処理温度
は上記延伸温度付近ないしそれ以上で行なうことが好ま
しい。パラフィンワックスの抽出はヘキサン、ヘプタン
等の炭化水素系溶剤で行なうことが、取扱い上、低毒性
などの点から好ましい。
A heat treatment is carried out subsequent to the above-mentioned drawing, and this heat treatment prevents the fibers from shrinking in the radial and axial directions to substantially reduce the porosity after the paraffin wax is extracted with a solvent. The heat treatment temperature is preferably around the drawing temperature or higher. Extraction of paraffin wax is preferably performed with a hydrocarbon solvent such as hexane or heptane from the viewpoint of handling and low toxicity.

【0013】[0013]

【作用】本発明の消臭繊維の製造方法では、ポリオレフ
ィン樹脂とパラフィンワックスとを所定の範囲の割合で
溶融混合し、これを所定のドラフト率で紡糸した未延伸
繊維を所定の延伸条件下で延伸し、熱処理を施した後に
パラフィンワックスを抽出除去している。
In the method for producing a deodorant fiber of the present invention, a polyolefin resin and paraffin wax are melt-mixed in a ratio within a predetermined range, and the undrawn fiber spun at a predetermined draft ratio is subjected to a predetermined drawing condition. After stretching and heat treatment, the paraffin wax is extracted and removed.

【0014】未延伸繊維は、ポリオレフィン樹脂(ポリ
エチレン,ポリプロピレン)の結晶間にパラフィンワッ
クスの層を充填した状態になっている。この未延伸繊維
の熱延伸によって得られる延伸繊維では、この結晶間が
拡げられ、延伸繊維の熱処理後にパラフィンワックスを
抽出すると、押し拡げられた結晶間に比較的大きい細孔
が数多く形成される。従って得られた多孔質繊維は、そ
の製法により非常に特殊な構造を有している。
The unstretched fiber is in a state of being filled with a layer of paraffin wax between crystals of a polyolefin resin (polyethylene, polypropylene). In the drawn fiber obtained by hot drawing of the undrawn fiber, the spaces between the crystals are expanded, and when the paraffin wax is extracted after the heat treatment of the drawn fiber, many relatively large pores are formed between the expanded crystals. Therefore, the obtained porous fiber has a very special structure due to its manufacturing method.

【0015】つまり、熱延伸によってラメラ晶がジグザ
グに変形し、その後これらの結晶間に形成されたパラフ
ィンワックスの層が抽出除去されるため、細孔は繊維断
面において広くなったり狭くなったりを繰り返しなが
ら、あたかもへちまの孔のような形態で表面から内部ま
で連なった細孔を形成している。このため空隙率が高く
比表面積も大きな繊維が得られる。
That is, the lamellae are transformed into zigzags by hot drawing, and the layer of paraffin wax formed between these crystals is then extracted and removed, so that the pores repeatedly widen and narrow in the fiber cross section. However, it forms pores that are continuous from the surface to the inside, as if they were pores of a hechima. Therefore, a fiber having a high porosity and a large specific surface area can be obtained.

【0016】このような形態の多孔質繊維に消臭物質を
付着すると、消臭物質が繊維本体の表面および細孔の内
面に薄く広がり、少ない量の消臭物質でも大きな消臭効
果が得られる。
When the deodorant substance is attached to the porous fiber having such a form, the deodorant substance spreads thinly on the surface of the fiber body and the inner surface of the pores, and a large deodorant effect can be obtained even with a small amount of the deodorant substance. ..

【0017】[0017]

【実施例】以下、本発明の実施例について説明するが、
本発明はこれら実施例にのみ限定されるものではない。
なお、実施例中に示した物性値の測定方法を予め示して
おく。
EXAMPLES Examples of the present invention will be described below.
The invention is not limited to these examples.
The methods for measuring the physical properties shown in the examples will be shown in advance.

【0018】空隙率 繊維径から算出した直径デニール(D1)と重量から求
めた重量デニール(D2)とで次式により空隙率を算出
した。 D1=繊維の断面積(cm2 )×9×105 cm×密度
(g/cm3 ) D2=9000mの繊維の重量 空隙率(%)=(直径デニール−重量デニール)/直径
デニール×100 比表面積 JIS Z 8830に規定の窒素ガス吸着法により測
定した。
Porosity The porosity was calculated by the following equation using the diameter denier (D1) calculated from the fiber diameter and the weight denier (D2) calculated from the weight. D1 = fiber cross-sectional area (cm 2 ) × 9 × 10 5 cm × density (g / cm 3 ) D2 = weight of fiber of 9000 m Porosity (%) = (diameter denier−weight denier) / diameter denier × 100 ratio Surface area: Measured by the nitrogen gas adsorption method specified in JIS Z 8830.

【0019】アンモニアおよびトリメチルアミン脱臭性
能試験 300mlフラスコに、アンモニアは1000ppm、
トリメチルアミンは30ppmの濃度に調整し、繊維2
gをその中に投入して、所定時間経過後のフラスコ内の
ガス濃度を北川式ガス検知器を用いて測定した。
Ammonia and trimethylamine deodorizing performance test Ammonia was added at 1000 ppm in a 300 ml flask.
Trimethylamine was adjusted to a concentration of 30ppm, and fiber 2
g was charged therein and the gas concentration in the flask after a lapse of a predetermined time was measured using a Kitagawa gas detector.

【0020】実施例1 MI値が5.5g/10分のHDPE(三井石油化学株
式会社製:ハイゼックス2200J)100重量部と、
パラフィンワックス(日本石油株式会社製:145°パ
ラフィン)100重量部とが機械的に混合された原料
を、スクリュウ径25mm、0.40mmφ×160ホ
ールのノズルを取り付け、145℃〜180℃に設定さ
れた溶融紡糸機に供給し、巻取速度V1が200m/m
inで、紡糸ドラフト率80で10デニールの未延伸繊
維を得た。
Example 1 100 parts by weight of HDPE (Mitsui Petrochemical Co., Ltd .: Hi-Zex 2200J) having an MI value of 5.5 g / 10 min.
A raw material mechanically mixed with 100 parts by weight of paraffin wax (145 ° paraffin manufactured by Nippon Oil Co., Ltd.) was installed with a nozzle having a screw diameter of 25 mm and 0.40 mmφ × 160 holes and set at 145 ° C. to 180 ° C. And the winding speed V1 is 200 m / m.
In, 10 denier undrawn fiber was obtained at a spinning draft rate of 80.

【0021】得られた未延伸繊維からなるマルチフィラ
メントを12本集めローラー延伸機を用い、110℃の
雰囲気下で全延伸倍率3.0倍、歪速度40%/min
として延伸して巻き取った。引続き、この繊維を紙管に
巻いた状態で、110℃のオーブン中で1時間定長熱処
理し、さらに機械捲縮加工をして15個/インチの捲縮
を付与し、51mmにカットしてステープルファイバー
とした後、これらを室温のヘキサン中に浸漬してパラフ
ィンワックスを抽出した。
Twelve multifilaments composed of the unstretched fibers obtained were collected and using a roller stretching machine, the total stretching ratio was 3.0 times and the strain rate was 40% / min in an atmosphere of 110 ° C.
Was stretched and wound up. Subsequently, in a state in which this fiber is wound around a paper tube, it is heat-treated for a fixed length in an oven at 110 ° C. for 1 hour, further mechanically crimped to give 15 crimps / inch, and cut into 51 mm. After forming staple fibers, these were immersed in hexane at room temperature to extract paraffin wax.

【0022】得られた多孔質繊維は、中実のものであっ
て、空隙率は45%、比表面積は39m2 /g、重量デ
ニールは2.3デニールで、繊維表面の細孔径は0.5
〜1μmであった。
The resulting porous fiber was solid, had a porosity of 45%, a specific surface area of 39 m 2 / g, a weight denier of 2.3 denier, and a pore diameter of the fiber surface of 0. 5
Was about 1 μm.

【0023】このようにして得られたポリエチレン系多
孔質繊維2gをエタノール200mlで親水化し、次い
で、消臭物質としブナ科植物の抽出液であるウラジロガ
シエキス(大洋香料株式会社製:商品名オークリンE
X)の1.5%エタノール溶液200mlを入れた50
0mlビーカー中に加え、3分間放置した後、3分間遠
心脱水し、さらに55°Cに設定されたオーブン中で1
時間乾燥して多孔質繊維の外表面および細孔の内表面
が、それぞれウラジロガシエキスでコーティングされた
多孔質ポリエチレン系消臭繊維を得た。
2 g of the polyethylene-based porous fiber thus obtained was hydrophilized with 200 ml of ethanol, and then used as a deodorant substance, an extract of beech plants, Vladimir oak extract (manufactured by Taiyo Koryo Co., Ltd .: trade name Oaklin E).
50) containing 200 ml of a 1.5% ethanol solution of X)
Add to 0 ml beaker, leave it for 3 minutes, spin-dry for 3 minutes, and put it in an oven set at 55 ° C for 1 minute.
After drying for a period of time, a porous polyethylene-based deodorant fiber was obtained, in which the outer surface of the porous fiber and the inner surface of the pores were coated with V. perilla extract.

【0024】このようにして得られた消臭繊維のウラジ
ロガシエキスの付着量は0.7%であった。図1には得
られた消臭繊維の脱臭性能の試験結果を示している。
The deodorant fiber thus obtained had an adhering amount of V. occidentalis extract of 0.7%. FIG. 1 shows the test results of the deodorizing performance of the obtained deodorant fiber.

【0025】実施例2 MFR値が3g/10分のポリプロピレン(宇部興産株
式会社製:YK121)100重量部とパラフィンワッ
クス(日本石油株式会社製:145°パラフィン)10
0重量部とが機械的に混合された原料を、スクリュウ径
25mm、0.4mmφ×160ホールのノズルを取り
付け、170℃〜200℃に設定された溶融紡糸機に供
給し、巻取速度V1が200m/minで紡糸ドラフト
率80で10デニールの未延伸繊維を得た。
Example 2 100 parts by weight of polypropylene (YK121 manufactured by Ube Industries, Ltd.) having a MFR value of 3 g / 10 min and paraffin wax (145 ° paraffin manufactured by Nippon Oil Co., Ltd.) 10
The raw material mechanically mixed with 0 parts by weight was supplied to a melt spinning machine set at 170 ° C to 200 ° C with a screw diameter of 25 mm, a nozzle of 0.4 mmφ x 160 holes attached, and a winding speed V1. An undrawn fiber having a spinning draft of 80 and a denier of 10 denier was obtained at 200 m / min.

【0026】得られた未延伸繊維をローラー延伸機を用
い、110℃の雰囲気下で、歪み速度40%/分、延伸
倍率2.9倍の条件で延伸し巻き取った。引続き、この
繊維を紙管に巻いた状態で、130℃のオーブン中で1
時間定長熱処理し、さらに機械捲縮加工をして15個/
インチの捲縮を付与し、51mmにカットしてステープ
ルファイバーとした後、これらを室温のヘキサン中に浸
漬してパラフィンワックスを抽出した。
The obtained unstretched fiber was stretched and wound using a roller stretching machine in an atmosphere of 110 ° C. under the conditions of a strain rate of 40% / min and a stretching ratio of 2.9 times. Continue to roll the fiber around a paper tube in an oven at 130 ° C for 1
15 pieces /
After the crimp of inch was applied and the staple fiber was cut into 51 mm, it was immersed in hexane at room temperature to extract the paraffin wax.

【0027】得られた多孔質繊維は、中実のものであっ
て、空隙率は26%、比表面積は55m2 /g、重量デ
ニールは2.9デニールであった。
The resulting porous fiber was solid and had a porosity of 26%, a specific surface area of 55 m 2 / g and a weight denier of 2.9 denier.

【0028】このようにして得られたポリプロピレン系
多孔質繊維2gをエタノール200mlで親水化し、次
いで、消臭物質としブナ科植物の抽出液であるウラジロ
ガシエキス(大洋香料株式会社製:商品名オークリンE
X)の1.0%エタノール溶液200mlを入れた50
0mlビーカー中に加え、3分間放置した後、3分間遠
心脱水し、さらに55°Cに設定されたオーブン中で1
時間乾燥して多孔質繊維の外表面および細孔の内表面
が、それぞれウラジロガシエキスでコーティングされた
多孔質ポリプロピレン系消臭繊維を得た。
2 g of the polypropylene-based porous fiber thus obtained was hydrophilized with 200 ml of ethanol, and then used as a deodorant substance, an extract of beech family plants, Vladivore oak extract (trade name: Oaklin E, manufactured by Taiyo Koryo Co., Ltd.).
50) containing 200 ml of a 1.0% ethanol solution of X)
Add to 0 ml beaker, leave it for 3 minutes, spin-dry for 3 minutes, and put it in an oven set at 55 ° C for 1 minute.
After drying for a period of time, a porous polypropylene deodorant fiber was obtained, in which the outer surface of the porous fiber and the inner surface of the pores were coated with Vladimir vulgaris extract.

【0029】このようにして得られた消臭繊維のウラジ
ロガシエキスの付着量は0.4%であった。図1には得
られた消臭繊維の脱臭性能の試験結果を示している。
The deodorant fiber thus obtained had an adhering amount of V. persicae extract of 0.4%. FIG. 1 shows the test results of the deodorizing performance of the obtained deodorant fiber.

【0030】実施例3 実施例1と同じ方法によって得られたポリエチレン系多
孔質繊維に、上記と同じ方法によりウラジロガシエキス
を付着させ、このときの付着量が0.4%になるように
調整した消臭繊維を得た。この消臭繊維の脱臭性能も図
1に示している。
Example 3 To the polyethylene-based porous fiber obtained by the same method as in Example 1, was adsorbed V. lacunae extract by the same method as described above, and the adhesion amount at this time was adjusted to 0.4%. A deodorant fiber was obtained. The deodorizing performance of this deodorant fiber is also shown in FIG.

【0031】比較例1 表面がほぼ平滑な2デニールの通常のポリプロピレン系
繊維に上記実施例と同様な方法によりウラジロガシエキ
スを付着させた。付着されたウラジロガシエキスは、実
施例1と同じ0.7%であった。この消臭繊維の脱臭性
能も図1に示している。
COMPARATIVE EXAMPLE 1 A velvet extract was adhered to a 2 denier ordinary polypropylene fiber having a substantially smooth surface by the same method as in the above-mentioned example. The adhering Vladimir beet extract was 0.7% as in Example 1. The deodorizing performance of this deodorant fiber is also shown in FIG.

【0032】図1に示した脱臭性能試験の結果からも明
らかなように、本発明にかかる消臭繊維によれば、短時
間で悪臭物質を除去できることがわかる。この理由は、
本発明の多孔質繊維の細孔は、繊維断面において広くな
ったり狭くなったりを繰り返しながら、あたかもへちま
の孔のような形態で表面から内部まで連なった細孔を形
成しており、このため空隙率が高く比表面積も大きなっ
ている。
As is clear from the results of the deodorizing performance test shown in FIG. 1, the deodorant fiber according to the present invention can remove malodorous substances in a short time. The reason for this is
The pores of the porous fiber of the present invention form pores that are continuous from the surface to the inside in a form like pores of Hemima while repeating widening and narrowing in the fiber cross section, and thus voids. The rate is high and the specific surface area is also large.

【0033】このような形態の多孔質繊維に消臭物質を
付着すると、消臭物質が繊維本体の表面および細孔の内
面に薄く広がる。ところが、比較例に示した繊維では、
消臭物質を同じ量だけ付着させたとしても、表面積が限
られているので、消臭物質はかなり厚く付着し、初期消
臭性能において、内部側の消臭物質が有効に機能しない
ため、悪臭物質の除去性能が劣ることになる。
When the deodorant substance is attached to the porous fiber having such a form, the deodorant substance spreads thinly on the surface of the fiber body and the inner surfaces of the pores. However, in the fiber shown in the comparative example,
Even if the same amount of deodorant substance is attached, the surface area is limited, so the deodorant substance attaches considerably thickly, and the deodorant substance on the internal side does not function effectively in the initial deodorant performance, so it does not The substance removal performance is inferior.

【0034】これに対して、本発明の消臭繊維では、消
臭物質が薄い膜状に広く付着しているので、少ない量の
消臭物質でも大きな消臭効果が得られるものと考えられ
る。
On the other hand, in the deodorant fiber of the present invention, since the deodorant substance is widely adhered in the form of a thin film, it is considered that a large deodorant effect can be obtained even with a small amount of the deodorant substance.

【0035】なお、上記実施例では、消臭物質としてウ
ラジロガシエキスを例示したが、本発明の実施はこれに
限定されることはなく、例えば、ジャコウソウエキスな
どの植物抽出油なども適用できる。また、高い消臭性能
が要求されない用途では、繊維表面処理剤として用いら
れている界面活性剤でも消臭効果は得られる。さらに、
本発明の消臭繊維に付着させる消臭物質は、繊維に対し
て0.1〜10重量部%の範囲が実用的である。
[0035] In the above-mentioned examples, Vladimir oupti extract was exemplified as the deodorant substance, but the practice of the present invention is not limited to this, and for example, plant extract oil such as musk root extract can also be applied. In addition, in applications where high deodorizing performance is not required, a deodorizing effect can be obtained even with a surfactant used as a fiber surface treatment agent. further,
The deodorant substance attached to the deodorant fiber of the present invention is practically in the range of 0.1 to 10 parts by weight based on the fiber.

【0036】[0036]

【発明の効果】以上詳細に説明したように、本発明にか
かる消臭繊維によれば、少ない量の消臭物質でも大きな
消臭効果が得られるものと考えられとともに、消臭物質
を付着させる多孔質繊維も通常の紡糸機械により製造す
ることができる。
As described in detail above, according to the deodorant fiber of the present invention, it is considered that a large amount of deodorant effect can be obtained even with a small amount of deodorant substance, and the deodorant substance is attached. Porous fibers can also be produced by conventional spinning machines.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施例および比較例の物性値と脱臭性
能試験の結果を示す図表である。
FIG. 1 is a table showing physical property values and results of a deodorizing performance test of Examples and Comparative Examples of the present invention.

フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C08L 91/00 7415−4J D06M 13/02 // D01F 6/04 B 7199−3B Continuation of front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location C08L 91/00 7415-4J D06M 13/02 // D01F 6/04 B 7199-3B

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ポリオレフィン樹脂からなる繊維本体
と、前記ポリオレフィン樹脂とパラフィンワックスとを
混合し、溶融紡糸して、延伸,熱処理後に前記パラフィ
ンワックスを除去することにより形成される多数の細孔
と、前記繊維本体の表面と前記細孔の内面に付着された
消臭物質とからなることを特徴とする消臭繊維。
1. A fiber main body made of a polyolefin resin, and a large number of pores formed by mixing the polyolefin resin and paraffin wax, melt-spinning, and stretching and heat treatment to remove the paraffin wax. A deodorant fiber, comprising a deodorant substance attached to the surface of the fiber body and the inner surface of the pores.
【請求項2】 所定量のポリオレフィン樹脂とパラフィ
ンワックスとを溶融下で混合し、この混合物を所定のド
ラフト率下で溶融紡糸して未延伸繊維を得、次いで、こ
の未延伸繊維を加熱下で所定の倍率で延伸して、熱処理
を施した後に、前記パラフィンワックスを除去して多孔
質繊維を得る工程と、得られた多孔質繊維に消臭物質を
付着する工程とからなることを特徴とする消臭繊維の製
造方法。
2. A predetermined amount of a polyolefin resin and paraffin wax are mixed under melting, and the mixture is melt-spun at a predetermined draft rate to obtain an unstretched fiber, which is then heated. It is characterized in that it comprises a step of obtaining a porous fiber by removing the paraffin wax after being drawn at a predetermined ratio and subjected to a heat treatment, and a step of attaching a deodorant substance to the obtained porous fiber. Method for producing deodorant fiber.
JP28671691A 1991-10-31 1991-10-31 Deodorant fiber and method for producing the same Expired - Fee Related JP3165485B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP28671691A JP3165485B2 (en) 1991-10-31 1991-10-31 Deodorant fiber and method for producing the same
US07/852,259 US5480712A (en) 1991-10-31 1991-12-04 Non-hollow adsorbent porous fiber
PCT/JP1991/001690 WO1993009277A1 (en) 1991-10-31 1991-12-04 Porous fiber and method of making thereof
EP19920900894 EP0565720A4 (en) 1991-10-31 1991-12-04 Porous fiber and method of making thereof.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28671691A JP3165485B2 (en) 1991-10-31 1991-10-31 Deodorant fiber and method for producing the same

Publications (2)

Publication Number Publication Date
JPH05125665A true JPH05125665A (en) 1993-05-21
JP3165485B2 JP3165485B2 (en) 2001-05-14

Family

ID=17708080

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28671691A Expired - Fee Related JP3165485B2 (en) 1991-10-31 1991-10-31 Deodorant fiber and method for producing the same

Country Status (1)

Country Link
JP (1) JP3165485B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07216731A (en) * 1994-02-02 1995-08-15 Zenichi Ogita Antimicrobial processing liquid comprising galenical extract and mixed solution thereof
WO2010041270A3 (en) * 2008-09-12 2011-03-31 Aditya Birla Science & Technology Co. Ltd A process for charging a polymeric product with attribute imparting agent(s)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07216731A (en) * 1994-02-02 1995-08-15 Zenichi Ogita Antimicrobial processing liquid comprising galenical extract and mixed solution thereof
WO2010041270A3 (en) * 2008-09-12 2011-03-31 Aditya Birla Science & Technology Co. Ltd A process for charging a polymeric product with attribute imparting agent(s)

Also Published As

Publication number Publication date
JP3165485B2 (en) 2001-05-14

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