JPH09279446A - Biodegradable short fiber nonwoven fabric and its production - Google Patents
Biodegradable short fiber nonwoven fabric and its productionInfo
- Publication number
- JPH09279446A JPH09279446A JP8092115A JP9211596A JPH09279446A JP H09279446 A JPH09279446 A JP H09279446A JP 8092115 A JP8092115 A JP 8092115A JP 9211596 A JP9211596 A JP 9211596A JP H09279446 A JPH09279446 A JP H09279446A
- Authority
- JP
- Japan
- Prior art keywords
- component
- sheath
- melting point
- core
- short
- 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
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- Biological Depolymerization Polymers (AREA)
- Multicomponent Fibers (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、医療・衛生材料、
生活資材あるいは一般産業資材など、生分解性能が要望
される幅広い用途に好適な生分解性短繊維不織布及びそ
の製造方法に関するものである。TECHNICAL FIELD The present invention relates to a medical / hygiene material,
The present invention relates to a biodegradable short-fiber nonwoven fabric suitable for a wide range of applications where biodegradability is required, such as daily life materials and general industrial materials, and a method for producing the same.
【0002】[0002]
【従来の技術】従来から、生分解性能を有する不織布と
しては、例えば乾式法あるいは溶液浸漬法により得られ
るビスコース短繊維不織布、湿式法により得られるキュ
プラレーヨン長繊維不織布やビスコースレーヨン長繊維
不織布、キチンやコラーゲンのような天然物の化学繊維
からなる不織布、コットンからなるスパンレース不織布
等が知られている。しかしながら、これらの生分解性不
織布は機械的強度が低くかつ親水性であるため吸水・湿
潤の時の機械的強度の低下が著しい。さらに、これらの
不織布は素材自体が非熱可塑性であることから、熱接着
性や熱成形性を有しない等の問題を有していた。BACKGROUND OF THE INVENTION Conventionally, as non-woven fabrics having biodegradability, for example, viscose short fiber non-woven fabrics obtained by a dry method or a solution dipping method, cupra rayon long fiber non-woven fabrics and viscose rayon long fiber non-woven fabrics obtained by a wet method. Nonwoven fabrics made of natural chemical fibers such as chitin and collagen, spunlace nonwoven fabric made of cotton, and the like are known. However, since these biodegradable nonwoven fabrics have low mechanical strength and are hydrophilic, the mechanical strength upon water absorption / wetting is significantly reduced. Further, since these non-woven fabrics are non-thermoplastic in nature, they have problems such as lack of thermal adhesiveness and thermoformability.
【0003】このような問題を解決する生分解性不織布
として、特開平5−93318号公報または特開平5−
195407号公報に生分解性を有する熱可塑性重合体
を用いた不織布が開示されている。しかし、これらは、
製造の際の紡出糸条の冷却性及び可紡性、延伸性に劣
り、しかも熱圧接工程等において全融タイプとなるので
得られた不織布の機械的特性及び柔軟性に劣るものであ
った。As a biodegradable non-woven fabric which solves such a problem, there is disclosed in Japanese Patent Laid-Open No. 93318/1993 or Japanese Patent Laid-Open No. 5-93318.
Japanese Patent No. 195407 discloses a non-woven fabric using a biodegradable thermoplastic polymer. But these are
The spun yarn during production was inferior in the cooling property, spinnability, and stretchability, and, since it was a fully melted type in the hot pressing process, the resulting nonwoven fabric was inferior in mechanical properties and flexibility. .
【0004】生分解性不織布の製造工程においてこのよ
うな問題が生じるのは、一般的に生分解性を有する重合
体の融点及び結晶化温度が低く、しかも結晶化速度が遅
いことに起因する。すなわち、溶融紡出後の冷却・細化
において糸条間に密着が発生し、次工程での延伸・捲縮
付与工程において操業性を著しく損なうものであった。
しかも、前述のような従来の製造方法では、生分解性能
の制御は、適用する重合体の種類、繊度、繊維の配向度
などを変更することにより幾分かは可能ではあるが、微
妙な制御は不可能であった。Such problems occur in the process of producing a biodegradable nonwoven fabric because the melting point and crystallization temperature of a biodegradable polymer are generally low and the crystallization rate is slow. That is, adhesion between yarns occurs during cooling / thinning after melt spinning, and operability is significantly impaired in the drawing / crimping step in the next step.
Moreover, in the conventional manufacturing method as described above, control of biodegradation performance is possible to some extent by changing the type of polymer to be applied, fineness, orientation degree of fiber, etc., but delicate control is possible. Was impossible.
【0005】[0005]
【発明が解決しようとする課題】本発明は、前記の問題
を解決し、紡出糸条の冷却性及び可紡性、延伸性に優
れ、良好な生分解性能を有するとともにその制御が可能
であり、さらに優れた機械的特性を有する生分解性短繊
維不織布及びその製造方法を提供しようとするものであ
る。DISCLOSURE OF THE INVENTION The present invention solves the above problems, has excellent cooling properties, spinnability and stretchability of spun yarns, has good biodegradability, and is controllable. In addition, the present invention aims to provide a biodegradable short fiber nonwoven fabric having further excellent mechanical properties and a method for producing the same.
【0006】[0006]
【課題を解決するための手段】本発明者らは上記課題を
解決すべく、鋭意検討の結果本発明に至った。すなわ
ち、本発明は以下の構成を要旨とするものである。Means for Solving the Problems The inventors of the present invention have made intensive studies to solve the above problems, and as a result, have reached the present invention. That is, the present invention has the following structures.
【0007】(1)複合短繊維からなる短繊維ウエブが
三次元交絡により一体化されており、前記複合短繊維が
生分解性を有する第1の脂肪族ポリエステルからなる芯
成分とこの芯成分よりも融点の低い生分解性を有する第
2の脂肪族ポリエステルからなる鞘成分とから形成され
る芯鞘型複合断面を有してなることを特徴とする生分解
性短繊維不織布。(1) A staple fiber web composed of composite staple fibers is integrated by three-dimensional entanglement, and the composite staple fiber comprises a core component composed of a first aliphatic polyester having biodegradability and the core component. A biodegradable short-fiber nonwoven fabric having a core-sheath type composite cross section formed from a sheath component made of a second aliphatic polyester having a low melting point and having biodegradability.
【0008】(2)生分解性を有する第1の脂肪族ポリ
エステルからなる芯成分とこの芯成分よりも融点の低い
生分解性を有する第2の脂肪族ポリエステルからなる鞘
成分とを用いて、芯鞘型複合繊維を溶融複合紡糸し、次
いで延伸し、得られた延伸糸条に機械捲縮を付与した後
に所定長に切断して短繊維となし、この短繊維をカーデ
ィングすることにより短繊維ウエブを形成し、この短繊
維ウエブに加圧液体流処理を施して構成繊維を三次元交
絡させ一体化することを特徴とする生分解性短繊維不織
布の製造方法。(2) Using a core component made of a first aliphatic polyester having biodegradability and a sheath component made of a second aliphatic polyester having a lower melting point than that of the core component, The core-sheath type composite fiber is melt-combined and then drawn, and the resulting drawn yarn is mechanically crimped and then cut into a predetermined length to form a short fiber. A method for producing a biodegradable short fiber non-woven fabric, which comprises forming a fiber web and subjecting the short fiber web to a pressurized liquid flow treatment to three-dimensionally entangle and integrate the constituent fibers.
【0009】以上のように、本発明の生分解性短繊維不
織布は、生分解性を有し融点の異なる2成分を複合して
なる芯鞘型複合短繊維により形成されていることによ
り、紡出糸条の冷却性及び可紡性、延伸性と生分解性能
とのいずれにも優れるとともに、制御可能な生分解性能
を具備するものとなるのである。As described above, the biodegradable short fiber nonwoven fabric of the present invention is formed by the core-sheath type composite short fibers which are composed of two components which are biodegradable and have different melting points. It has excellent coolability, spinnability, stretchability, and biodegradability of the spinning yarn, and has controllable biodegradability.
【0010】さらに、本発明の生分解性短繊維不織布
は、三次元交絡により一体化されてなるので、不織布の
機械的特性および地合いに優れるものである。Furthermore, since the biodegradable short fiber nonwoven fabric of the present invention is integrated by three-dimensional entanglement, it has excellent mechanical properties and texture.
【0011】[0011]
【発明の実施の形態】まず、本発明の短繊維ウエブにつ
いて説明する。本発明において適用される短繊維は、生
分解性を有する第1の脂肪族ポリエステルからなる芯成
分とこの芯成分よりも融点の低い生分解性を有する第2
の脂肪族ポリエステルからなる鞘成分とから形成される
複合短繊維である。First, the short fiber web of the present invention will be described. The staple fiber applied in the present invention includes a core component made of the first aliphatic polyester having biodegradability and a second biodegradability having a melting point lower than that of the core component.
Is a composite short fiber formed from a sheath component composed of the aliphatic polyester of.
【0012】芯成分及び鞘成分を構成する第1及び第2
の生分解性脂肪族ポリエステルとしては、例えば、ポリ
グリコール酸やポリ乳酸のようなポリ(α−ヒドロキシ
酸)またはこれらを構成する繰り返し単位要素による共
重合体が挙げられる。また、ポリ(ε−カプロラクト
ン)、ポリ(β−プロピオラクトン)のようなポリ(ω
−ヒドロキシアルカノエート)が、さらに、ポリ−3−
ヒドロキシプロピオネート、ポリ−3−ヒドロキシブチ
レート、ポリ−3−ヒドロキシカプロエート、ポリ−3
−ヒドロキシヘプタノエート、ポリ−3−ヒドロキシオ
クタノエートのようなポリ(β−ヒドロキシアルカノエ
ート)及びこれらを構成する繰り返し単位要素とポリ−
3−ヒドロキシバリレートやポリ−4−ヒドロキシブチ
レートを構成する繰り返し単位要素との共重合体が挙げ
られる。また、ジオールとジカルボン酸の縮重合体から
なるものとして、例えば、ポリエチレンオキサレート、
ポリエチレンサクシネート、ポリエチレンアジペート、
ポリエチレンアゼテート、ポリブチレンオキサレート、
ポリブチレンサクシネート、ポリブチレンアジペート、
ポリブチレンセバケート、ポリヘキサメチレンセバケー
ト、ポリネオペンチルオキサレートまたはこれらを構成
する繰り返し単位要素による共重合体が挙げられる。ま
た、以上の脂肪族ポリエステルを複数ブレンドして用い
ることもできる。以上の脂肪族ポリエステルのなかで
は、製糸性及び生分解性能の観点から、ポリブチレンサ
クシネート、ポリエチレンサクシネートならびにポリブ
チレンアジペートが特に好ましく、さらに特に、ブチレ
ンサクシネートを主繰り返し単位としてこれにエチレン
サクシネートあるいはブチレンアジペートを共重合せし
めた共重合ポリエステルが好適である。本発明において
は、以上の脂肪族ポリエステルの中から選択された2種
の重合体のうち、融点が高い方の重合体を芯部に配し、
融点が低い方の重合体を鞘部に配するのである。First and second constituents of the core and sheath components
Examples of the biodegradable aliphatic polyester include poly (α-hydroxy acid) such as polyglycolic acid and polylactic acid, or a copolymer of repeating unit elements constituting them. In addition, poly (ω-caprolactone), poly (ω-propionate such as poly (β-propiolactone),
-Hydroxyalkanoate) and poly-3-
Hydroxypropionate, poly-3-hydroxybutyrate, poly-3-hydroxycaproate, poly-3
-Poly (β-hydroxyalkanoate) such as hydroxyheptanoate and poly-3-hydroxyoctanoate, and repeating unit elements and poly-constituting them
Examples thereof include copolymers with repeating unit elements constituting 3-hydroxyvalerate and poly-4-hydroxybutyrate. In addition, as a polycondensate of diol and dicarboxylic acid, for example, polyethylene oxalate,
Polyethylene succinate, polyethylene adipate,
Polyethylene azetate, polybutylene oxalate,
Polybutylene succinate, polybutylene adipate,
Examples thereof include polybutylene sebacate, polyhexamethylene sebacate, polyneopentyl oxalate, and copolymers of repeating unit elements constituting these. Further, a plurality of the above aliphatic polyesters may be blended and used. Among the above-mentioned aliphatic polyesters, polybutylene succinate, polyethylene succinate and polybutylene adipate are particularly preferable from the viewpoint of spinnability and biodegradability, and more particularly, butylene succinate as a main repeating unit and ethylene succinate. A copolyester obtained by copolymerizing nate or butylene adipate is preferable. In the present invention, of the two polymers selected from the above aliphatic polyesters, the polymer with the higher melting point is placed in the core,
The polymer with the lower melting point is placed in the sheath.
【0013】ところで、脂肪族ポリエステルは一般に、
融点が高い程、紡出糸条の冷却性及び可紡性、延伸性に
は優れるものの、結晶化度が高いため生分解性能には劣
り、逆に、融点が低い程、紡出糸条の冷却性及び可紡
性、延伸性には劣るものの、結晶化度が低いため生分解
性能には優れる。例えば、繊維横断面が比較的融点の高
い成分単相からなる場合には、製糸性及び不織布化には
優れるものの、目標とする生分解性能を得ることができ
ない。一方、繊維横断面が比較的融点の低い成分単相か
らなる場合には、溶融紡糸に際し紡出糸条の冷却性に劣
り不織布を得ることができない。Incidentally, the aliphatic polyester is generally
The higher the melting point, the better the cooling properties, spinnability and stretchability of the spun yarn, but the poorer the biodegradability due to the higher crystallinity. Conversely, the lower the melting point, the higher the melting point of the spun yarn. Although it is inferior in cooling property, spinnability and stretchability, it has excellent biodegradability due to its low crystallinity. For example, when the fiber cross section is composed of a component single phase having a relatively high melting point, the target biodegradability cannot be obtained, although the spinnability and the non-woven fabric are excellent. On the other hand, when the cross-section of the fiber is composed of a single component phase having a relatively low melting point, the meltability of the spun yarn is inferior in the cooling property during melt spinning, and a nonwoven fabric cannot be obtained.
【0014】本発明においては、例えば、鞘成分が冷却
性、延伸性に劣る重合体であっても、比較的融点の高い
重合体を芯成分として用いることにより、紡出糸条の冷
却性、延伸性を向上させることができるのである。ま
た、芯成分が生分解性能に劣る重合体であっても、比較
的融点の低い生分解性能に優れる重合体を複合すること
により、芯成分が細繊度の状態で経時的に取り残される
こととなり、不織布としての生分解性能には優れる結果
となる。In the present invention, for example, even if the sheath component is a polymer having inferior cooling properties and drawability, by using a polymer having a relatively high melting point as the core component, the cooling properties of the spun yarn, The stretchability can be improved. Further, even if the core component is a polymer having poor biodegradability, by compositing a polymer having a relatively low melting point and excellent biodegradability, the core component will be left behind in the state of fineness over time. The result is excellent biodegradability as a nonwoven fabric.
【0015】このことから、芯成分として、ポリブチレ
ンサクシネートを用い、鞘成分として、ブチレンサクシ
ネートの共重合量比が70〜90モル%となるようにブ
チレンサクシネートにエチレンサクシネートあるいはブ
チレンアジペートを共重合せしめた共重合ポリエステル
を用いることが好ましい。ブチレンサクシネートの共重
合量比が70モル%未満であると、生分解性能には優れ
るものの、紡出糸条の冷却性及び可紡性、延伸性に劣
り、目的とする短繊維が得られないこととなる。逆に、
90モル%を超えると、紡出糸条の冷却性及び可紡性、
延伸性には優れるものの、生分解性能に劣り本発明の目
的とするものではない。From this, polybutylene succinate is used as the core component, and ethylene succinate or butylene adipate is added to butylene succinate so that the copolymerization ratio of butylene succinate is 70 to 90 mol% as the sheath component. It is preferable to use a copolyester obtained by copolymerizing the above. When the copolymerization amount ratio of butylene succinate is less than 70 mol%, the biodegradability is excellent, but the cooling property, spinnability and stretchability of the spun yarn are poor, and the target short fibers can be obtained. There will be no. vice versa,
If it exceeds 90 mol%, the cooling and spinnability of the spun yarn,
Although it is excellent in stretchability, it is inferior in biodegradability and is not the object of the present invention.
【0016】なお、本発明において、芯成分及び鞘成分
に適用される前述の脂肪族ポリエステルは、数平均分子
量が約20,000以上、好ましくは40,000以
上、さらに好ましくは60,000以上のものが、製糸
性及び得られる糸条の特性の点で良い。また、重合度を
高めるために少量のジイソシアネートやテトラカルボン
酸二無水物などで鎖延長したものでも良い。In the present invention, the above-mentioned aliphatic polyester applied to the core component and the sheath component has a number average molecular weight of about 20,000 or more, preferably 40,000 or more, more preferably 60,000 or more. However, they are good in terms of spinnability and characteristics of the obtained yarn. Further, it may be chain-extended with a small amount of diisocyanate or tetracarboxylic dianhydride in order to increase the degree of polymerization.
【0017】また、本発明においては、前述の芯成分及
び鞘成分の両方またはいずれか一方に、必要に応じて、
例えば艶消し剤、顔料、光安定剤、酸化防止剤等を本発
明の効果を損なわない範囲内で添加することができる。In the present invention, either or both of the core component and the sheath component described above may be added, if necessary.
For example, matting agents, pigments, light stabilizers, antioxidants and the like can be added within a range that does not impair the effects of the present invention.
【0018】特に、本発明においては、短繊維の製造に
際して紡出糸条の冷却性を向上させるうえで、その構成
成分のうちの少なくとも鞘成分中に結晶核剤が添加され
ていることが好ましい。結晶核剤を添加することによ
り、溶融紡出後に固化しにくい低結晶性の重合体であっ
ても、紡出糸条間に密着が発生するのを防止することが
できる。ここで、結晶核剤としては、粉末状の無機物
で、かつ溶融液に溶解したりするものでなければ特に制
限をうけないが、タルク、炭酸カルシウム、酸化チタ
ン、窒化ホウ素、シリカゲル、酸化マグネシウムまたは
これらの混合物が好適に用いられる。Particularly, in the present invention, it is preferable that a crystal nucleating agent is added to at least the sheath component among the constituent components in order to improve the cooling property of the spun yarn in the production of short fibers. . Addition of a nucleating agent can prevent adhesion between spun yarns even for a low-crystalline polymer that is hard to solidify after melt spinning. Here, the crystal nucleating agent is a powdered inorganic substance, and is not particularly limited unless it dissolves in the melt, but talc, calcium carbonate, titanium oxide, boron nitride, silica gel, magnesium oxide or A mixture of these is preferably used.
【0019】また、結晶核剤を添加する際には、芯成分
中への結晶核剤の添加量をQA (重量%)とし、鞘成分
中への結晶核剤の添加量をQB (重量%)としたとき
に、(1)式及び(2)式を満足するように添加されて
いることが好ましい。 [(ΔTA +ΔTB)/100]−2 /3 ≦QA +QB ≦[(ΔTA +ΔTB)/100]+4 …(1) QA ≦QB …(2) 但し、ΔTA =芯成分の融点−芯成分の結晶化温度 ΔTB =鞘成分の融点−鞘成分の結晶化温度 結晶核剤の全添加量QA +QB (重量%)が(1)式で
定義された上限を超えると、紡出糸条の冷却効果は高い
ものの、製糸性が低下するとともに得られた短繊維ひい
ては不織布の機械的性能が劣り好ましくない。逆に、結
晶核剤の全添加量QA +QB (重量%)が(1)式で定
義された下限より低くなると、紡出糸条の冷却性が低下
して紡出糸条間に密着が発生し、目標とする短繊維を得
ることが困難となる。また、芯成分中への結晶核剤の添
加量QA (重量%)が、鞘成分中への結晶核剤の添加量
QB (重量%)よりも多くなると、芯成分の冷却性はさ
らに向上するが、鞘成分の冷却性が低くなり、これによ
って紡出糸条間に密着が発生しやすくなるため好ましく
ない。When the crystal nucleating agent is added, the amount of the crystal nucleating agent added to the core component is QA (% by weight), and the amount of the crystal nucleating agent added to the sheath component is QB (% by weight). It is preferable that it is added so as to satisfy the expressions (1) and (2). [(ΔTA + ΔTB) / 100] −2 / 3 ≦ QA + QB ≦ [(ΔTA + ΔTB) / 100] +4 (1) QA ≦ QB (2) where ΔTA = melting point of core component−crystallization of core component Temperature ΔTB = melting point of sheath component−crystallization temperature of sheath component When the total amount of crystal nucleating agent QA + QB (% by weight) exceeds the upper limit defined by the formula (1), the effect of cooling the spun yarn is high. However, this is not preferable because the spinnability is deteriorated and the mechanical properties of the obtained short fibers and thus the nonwoven fabric are poor. On the contrary, if the total amount of the crystal nucleating agent QA + QB (% by weight) becomes lower than the lower limit defined by the equation (1), the cooling property of the spun yarn is deteriorated and adhesion occurs between the spun yarns. However, it becomes difficult to obtain the target short fiber. When the amount QA (wt%) of the crystal nucleating agent added to the core component is larger than the amount QB (wt%) of the crystal nucleating agent added to the sheath component, the cooling property of the core component is further improved. However, the cooling property of the sheath component is lowered, and this tends to cause adhesion between spun yarns, which is not preferable.
【0020】また、本発明において、芯成分及び鞘成分
の粘度は特に限定しないが、芯成分の粘度が鞘成分の粘
度より高い方が好ましい。これは、一般に熱可塑性樹脂
の複合紡糸においては低粘度成分が高粘度成分を被覆し
ようとする力が働くことに起因する。すなわち、本発明
においては、芯成分を高粘度にすることにより繊維横断
面において芯鞘形態を保持させるのに好適となる。In the present invention, the viscosities of the core component and the sheath component are not particularly limited, but the viscosity of the core component is preferably higher than that of the sheath component. This is because the low-viscosity component generally acts in the composite spinning of the thermoplastic resin so as to cover the high-viscosity component. That is, in the present invention, by making the core component highly viscous, it becomes suitable for maintaining the core-sheath form in the cross section of the fiber.
【0021】従って、本発明で適用する重合体のメルト
フローレート値(以降、MFR値と記す)は、芯成分が
5〜50g/10分であり、鞘成分が10〜70g/1
0分であることが好ましい。但し、本発明におけるMF
R値は、ASTM−D−1238(E)記載の方法に準
じて測定したものである。芯成分のMFR値が5g/1
0分未満及び/または鞘成分のMFR値が10g/10
分未満であると、あまりにも高粘度であるため、紡出糸
条の細化がスムーズに行われず操業性を損なう結果とな
り、しかも得られる繊維は太繊度で均斉度に劣るものと
なる。逆に、芯成分のMFR値が50g/10分及び/
または鞘成分のMFR値が70g/10分を超えると、
あまりにも低粘度であるため、複合断面が不安定となる
ばかりか、紡糸工程において糸切れが発生し操業性を損
なうとともに、得られる不織布の機械的特性が劣る結果
となる。これらの理由により、芯成分のMFR値は10
〜45g/10分、鞘成分のMFR値は15〜65g/
10分であることがさらに好ましい。Therefore, the melt flow rate value (hereinafter referred to as MFR value) of the polymer applied in the present invention is 5 to 50 g / 10 minutes for the core component and 10 to 70 g / 1 for the sheath component.
It is preferably 0 minutes. However, the MF in the present invention
The R value is measured according to the method described in ASTM-D-1238 (E). MFR value of core component is 5g / 1
Less than 0 minutes and / or MFR value of sheath component is 10 g / 10
If the amount is less than the minute, the viscosity is too high, and the spun yarn cannot be thinned smoothly, resulting in impaired operability, and the obtained fiber has a large fineness and poor uniformity. Conversely, the MFR value of the core component is 50 g / 10 minutes and /
Or, when the MFR value of the sheath component exceeds 70 g / 10 minutes,
Since the viscosity is too low, not only the composite cross section becomes unstable, but also yarn breakage occurs in the spinning process, impairing operability, and the resulting nonwoven fabric has poor mechanical properties. For these reasons, the MFR value of the core component is 10
~ 45g / 10min, MFR value of sheath component is 15 ~ 65g /
More preferably, it is 10 minutes.
【0022】本発明に適用される複合短繊維は、芯成分
/鞘成分の複合比が1/3〜3/1(重量比)であるこ
とが好ましい。複合比がこの範囲を外れると紡出糸条の
冷却性及び可紡性、延伸性と生分解性能とを併せて満足
することができず、さらに、繊維横断面形状の不安定さ
を誘発するため好ましくない。例えば、芯成分/鞘成分
の複合比が1/3を超えると、生分解性能には優れるも
のの、紡出糸条の冷却性及び可紡性、延伸性には劣る結
果となる。逆に、芯成分/鞘成分の複合比が3/1を超
えると、紡出糸条の冷却性及び可紡性、延伸性には優れ
るものの、生分解性能には劣る結果となる。さらに例え
ば、芯成分が生分解性能に劣る重合体であれば、鞘成分
の複合比を上げることにより生分解速度を促進させるこ
とができる。この理由により、さらに好ましくは1/
2.5〜2.5/1(重量比)が良い。The composite short fibers applied to the present invention preferably have a core component / sheath component composite ratio of 1/3 to 3/1 (weight ratio). If the composite ratio is out of this range, the spinnability of the spun yarn cannot be satisfied together with the cooling property, spinnability, stretchability and biodegradability, and further, instability of the fiber cross-sectional shape is induced. Therefore, it is not preferable. For example, when the composite ratio of the core component / the sheath component exceeds 1/3, the biodegradability is excellent, but the cooling property, spinnability and stretchability of the spun yarn are poor. On the other hand, when the composite ratio of the core component / the sheath component exceeds 3/1, the spun yarn has excellent cooling properties, spinnability and stretchability, but poor biodegradability. Further, for example, when the core component is a polymer having poor biodegradability, the biodegradation rate can be accelerated by increasing the composite ratio of the sheath component. For this reason, more preferably 1 /
2.5-2.5 / 1 (weight ratio) is good.
【0023】本発明においては、複合短繊維の単糸繊度
が1.5〜10デニールであることが好ましい。1.5
デニール未満であると、紡糸口金の複雑化、製糸工程に
おける糸切れの増大、生産量の低下及び繊維横断面形状
の不安定さなどを招くため好ましくない。逆に、10デ
ニールを超えると紡出糸条の冷却性に劣るとともに生分
解性能にも劣る結果となる。この理由により、さらに好
ましくは2〜8デニールが良い。In the present invention, the single yarn fineness of the composite short fibers is preferably 1.5 to 10 denier. 1.5
When it is less than denier, the spinneret becomes complicated, the number of yarn breakages in the spinning process increases, the production amount decreases, and the fiber cross-sectional shape becomes unstable. On the other hand, when it exceeds 10 denier, the spun yarn has poor cooling properties and biodegradability. For this reason, 2 to 8 denier is more preferable.
【0024】以上のように、本発明の短繊維不織布は、
融点を異にする生分解性脂肪族ポリエステルからなる芯
成分及び鞘成分で構成された芯鞘型複合短繊維で形成さ
れるウエブであって、両成分の複合比、単糸繊度などを
組み合わせることにより、要求する紡出糸条の冷却性及
び可紡性、延伸性が得られ、さらに生分解性能を制御す
ることができるのである。As described above, the short fiber nonwoven fabric of the present invention is
A web formed of a core-sheath type composite short fiber composed of a core component and a sheath component made of biodegradable aliphatic polyester having different melting points, and combining the composite ratio of both components, single yarn fineness, etc. As a result, the required cooling property, spinnability and stretchability of the spun yarn can be obtained, and the biodegradability can be controlled.
【0025】本発明の生分解性短繊維不織布は、前記の
複合短繊維からなる短繊維ウエブが三次元交絡により一
体化されたものである。すなわち、後述の加圧液体流処
理を施すことにより、短繊維ウエブの構成繊維間が互い
に三次元的に交絡し、一体化されるのである。これによ
り、本発明の短繊維不織布は、実用に耐えうるだけの強
力で一体化することができ、優れた機械的特性を発揮す
ることができる。The biodegradable short fiber nonwoven fabric of the present invention is a short fiber web composed of the above-mentioned composite short fibers integrated by three-dimensional entanglement. That is, the constituent fibers of the short fiber web are three-dimensionally entangled and integrated with each other by performing the pressurized liquid flow treatment described later. As a result, the short-fiber nonwoven fabric of the present invention is strong enough to withstand practical use, can be integrated, and can exhibit excellent mechanical properties.
【0026】次に、本発明の生分解性短繊維不織布の製
造方法について説明する。まず、本発明に適用される短
繊維ウエブの製造は、通常の複合紡糸装置及び延伸装置
を用いて行なうことができる。すなわち、前述の生分解
性を有する重合体からなる芯成分と鞘成分とを溶融して
個別計量し、これを前述の複合比にて、芯鞘型複合断面
を形成可能な複合紡糸口金を介して紡出し、紡出糸条を
冷却空気流などを用いた公知の冷却装置にて冷却する。
次いで、速度800〜2500m/分の引取ロールにて
未延伸糸として捲きとり、この未延伸糸を周速の異なる
延伸ロール間で所定の延伸倍率で延伸を行う。ここで、
延伸工程における延伸ロール個数及び延伸温度は適宜選
択すれば良い。たとえば、太繊度を延伸する場合には延
伸ロール個数を多くし、さらに熱延伸することも必要で
ある。次いで、得られた延伸糸にスタッファーボックス
にて捲縮を付与した後、所定長に切断して短繊維を得る
ことができる。なお、上述したのは、二工程法である
が、一工程法、即ち未延伸糸を一旦捲き取ることなく連
続して延伸するいわゆるスピンドロー法で短繊維を得る
こともできる。Next, a method for producing the biodegradable short fiber nonwoven fabric of the present invention will be described. First, the production of the short fiber web applied to the present invention can be carried out using an ordinary composite spinning apparatus and drawing apparatus. That is, the core component and the sheath component made of the above-mentioned biodegradable polymer are melted and individually weighed, and this is mixed at the above-mentioned composite ratio through a composite spinneret capable of forming a core-sheath composite cross section. And the spun yarn is cooled by a known cooling device using a cooling air flow or the like.
Then, the undrawn yarn is wound up by a take-up roll at a speed of 800 to 2500 m / min, and the undrawn yarn is drawn at a predetermined draw ratio between drawing rolls having different peripheral speeds. here,
The number of drawing rolls and the drawing temperature in the drawing step may be appropriately selected. For example, in the case of stretching the fineness, it is necessary to increase the number of stretching rolls and further perform hot stretching. Then, the obtained drawn yarn is crimped with a stuffer box and then cut into a predetermined length to obtain short fibers. Although the above-described method is a two-step method, short fibers can also be obtained by a one-step method, that is, a so-called spin draw method in which undrawn yarn is continuously drawn without being wound up.
【0027】また、本発明においては、前述のように、
用いる重合体の中に結晶核剤を添加することが好まし
い。これにより、溶融紡糸の際に紡出糸条の冷却性を向
上させることができるのである。結晶核剤の添加は重合
工程あるいは溶融工程で行うが、その際、得られる糸の
機械的性能及び均整度を向上させるため、できる限り均
一分散させておくことが好ましい。Further, in the present invention, as described above,
It is preferable to add a nucleating agent to the polymer used. Thereby, the cooling property of the spun yarn during the melt spinning can be improved. The crystal nucleating agent is added in the polymerization step or the melting step. At this time, it is preferable to disperse the nucleating agent as uniformly as possible in order to improve the mechanical performance and the uniformity of the obtained yarn.
【0028】次いで、得られた短繊維を公知のカード機
によりカーディングして所定目付けの短繊維ウエブを作
成する。そして、得られた短繊維ウエブに加圧液体流処
理を施して構成繊維間に三次元交絡を形成することによ
り一体化させて生分解性短繊維不織布を得る。Then, the obtained short fibers are carded by a known card machine to prepare a short fiber web having a predetermined weight. Then, the obtained short fiber web is subjected to a pressurized liquid flow treatment to form a three-dimensional entanglement between the constituent fibers to integrate them, thereby obtaining a biodegradable short fiber nonwoven fabric.
【0029】本発明における短繊維ウエブは、カード機
の進行方向に配列したパラレルウエブ、パラレルウエブ
のクロスレイドされたウエブ、ランダムに配列したラン
ダムウエブあるいは中程度に配列したセミランダムウエ
ブのいずれであっても良く、使用用途によって適宜選択
することができる。特に、衣料用途に用いる場合には、
不織布としての強力において、縦/横強力比が概ね1/
1となるカードウエブを使用するのが好ましい。The short fiber web in the present invention is either a parallel web arranged in the traveling direction of the card machine, a crosslaid web of parallel webs, a randomly arranged random web or a semi-random web arranged in the middle. It may be selected according to the intended use. Especially when used for clothing,
In terms of strength as a non-woven fabric, the longitudinal / lateral strength ratio is approximately 1 /
It is preferable to use a card web of 1.
【0030】加圧液体流処理を施すに際しては、加圧液
体流の噴射孔として、孔径0.05〜1.5mmの噴射
孔が0.4〜5mm間隔で一列ないしは複数列に配置さ
れたオリフィスヘッドを用い、このオリフィスヘッドを
3〜10段に配するのが好ましい。オリフィスヘッドの
配置としては、短繊維ウエブに対して片面あるいは両面
に配置されたもののいずれであっても良い。When performing the pressurized liquid flow treatment, as the injection holes for the pressurized liquid flow, orifices having a diameter of 0.05 to 1.5 mm are arranged in one row or a plurality of rows at 0.4 to 5 mm intervals. It is preferable to use a head and arrange the orifice heads in 3 to 10 stages. The orifice head may be arranged on one side or both sides of the short fiber web.
【0031】加圧液体流処理は、第1回目の液圧を45
kg/cm2 G未満の加圧液体流により予備交絡を施し
た後、引き続き第2回以降の処理として45kg/cm
2 G以上の液圧の加圧液体流により交絡処理を施して行
われる。第1回目の液圧が45kg/cm2 G以上であ
ると、加圧液体流により発生する随伴気流により、ウエ
ブの乱れが発生したり、また、加圧液体流によりウエブ
を構成する短繊維が脱落し、製品となる生分解性短繊維
不織布の品位を保つ上で好ましくない。以上の方法によ
り得られた生分解性短繊維不織布を反転し、第3回目の
交絡処理を第2回目に適用した液圧により交絡処理を施
すことにより表裏共に一体化した生分解性短繊維不織布
を得ることができる。In the pressurized liquid flow process, the first liquid pressure is set to 45.
After pre-entanglement with a pressurized liquid flow of less than kg / cm 2 G, then 45 kg / cm as the second and subsequent treatments.
It is performed by performing an entanglement treatment with a pressurized liquid flow having a hydraulic pressure of 2 G or more. When the first hydraulic pressure is 45 kg / cm 2 G or more, the turbulence of the web occurs due to the accompanying airflow generated by the pressurized liquid flow, and the short fibers constituting the web are generated by the pressurized liquid flow. It is not preferable in terms of maintaining the quality of the biodegradable short-fiber non-woven fabric which is dropped and becomes a product. The biodegradable short fiber non-woven fabric obtained by the above method is inverted, and the front and back are integrated by subjecting the third confounding treatment to the confounding treatment by the hydraulic pressure applied to the second time. Can be obtained.
【0032】加圧液体流処理に際し、短繊維ウエブを載
置する多孔性支持板としては支持板上に載置された短繊
維ウエブを加圧液体流が通過するものであれば、金属
製、ポリエステル製、その他の材質のいずれを用いても
良い。多孔性支持板のメッシュの範囲はその用途によっ
て適宜選択されるものであるが、20〜150メッシュ
のものを用いると良い。20メッシュ未満では、得られ
た生分解性短繊維不織布に実質的に孔が開き、例えば、
家庭用、業務用の廃棄物を入れる等の用途に用いた際、
この孔部分より細かなクズが流れ出し好ましくない。逆
に、150メッシュを超えると短繊維ウエブとネットを
貫通する液体流の液圧を多大にする必要があり、生産コ
スト上好ましくない。以上の理由により、多孔性支持板
のメッシュの範囲は、より好ましくは30〜100メッ
シュが良い。In the treatment of the pressurized liquid flow, the porous support plate on which the short fiber web is placed is made of metal as long as the pressurized liquid flow passes through the short fiber web placed on the support plate. Any of polyester and other materials may be used. The range of the mesh of the porous support plate is appropriately selected depending on the application, but it is preferable to use the mesh of 20 to 150 mesh. When it is less than 20 mesh, the resulting biodegradable short fiber nonwoven fabric is substantially perforated, and for example,
When used for purposes such as household and commercial waste,
Fine scraps flow out from this hole portion, which is not preferable. On the other hand, if it exceeds 150 mesh, it is necessary to increase the liquid pressure of the liquid flow passing through the short fiber web and the net, which is not preferable in terms of production cost. For the above reasons, the range of the mesh of the porous support plate is more preferably 30 to 100 mesh.
【0033】以上の方法により得られた生分解性短繊維
不織布は、余分な水分を既知の水分除去装置であるマン
グル等により除去した後乾燥処理が施される。本発明の
生分解性短繊維不織布の目付けは、使用目的により選択
されるため特に限定されるものではないが、一般的には
10〜150g/m2 の範囲が好ましく、より好ましく
は15〜70g/m2 の範囲とするのが良い。目付けが
10g/m2 未満では柔軟性及び生分解速度には優れる
ものの機械的強力に劣り実用的ではない。逆に、目付け
が150g/m2 を超えると、不織布が硬い風合いのも
のとなり、柔軟性に劣るものとなる。The biodegradable short-fiber non-woven fabric obtained by the above method is subjected to a drying treatment after removing excess water with a known water removing device such as mangle. The basis weight of the biodegradable short fiber non-woven fabric of the present invention is not particularly limited because it is selected according to the purpose of use, but it is generally preferably in the range of 10 to 150 g / m 2 , and more preferably 15 to 70 g. It is better to set it in the range of / m 2 . When the basis weight is less than 10 g / m 2 , flexibility and biodegradation rate are excellent, but mechanical strength is poor and it is not practical. On the other hand, when the basis weight exceeds 150 g / m 2 , the nonwoven fabric has a hard texture and is inferior in flexibility.
【0034】[0034]
【実施例】次に、実施例に基づき本発明を具体的に説明
するが、本発明は、これらの実施例によって何ら限定さ
れるものではない。Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples.
【0035】実施例において、各物性値の測定を次の方
法により実施した。In the examples, each physical property value was measured by the following methods.
【0036】・メルトフローレート値(g/10分);
ASTM−D−1238(E)に記載の方法に準じて温
度190℃で測定した。(以降、MFR値と記す)Melt flow rate value (g / 10 minutes);
The temperature was measured at 190 ° C. according to the method described in ASTM-D-1238 (E). (Hereinafter referred to as MFR value)
【0037】・融点(℃);パーキンエルマ社製示差走
査型熱量計DSC−2型を用い、試料重量を5mg、昇
温速度を20℃/分として測定して得た融解吸熱曲線の
最大値を与える温度を融点(℃)とした。Melting point (° C.); maximum value of melting endotherm curve obtained by measurement using a differential scanning calorimeter DSC-2 type manufactured by Perkin Elma Co., Ltd. with a sample weight of 5 mg and a heating rate of 20 ° C./min. Was given as the melting point (° C.).
【0038】・結晶化温度(℃);パーキンエルマ社製
示差走査型熱量計DSC−2型を用い、試料重量を5m
g、降温速度を20℃/分として測定して得た固化発熱
曲線の最大値を与える温度を結晶化温度(℃)とした。Crystallization temperature (° C.); using a differential scanning calorimeter DSC-2 type manufactured by Perkin Elma Co., and a sample weight of 5 m
g, the temperature giving the maximum value of the solidification exothermic curve obtained by measuring the cooling rate at 20 ° C./min was defined as the crystallization temperature (° C.).
【0039】・冷却性;紡出糸条を目視して下記の3段
階にて評価した。 ○;密着糸が認められない。 △;密着糸がわずかではあるが認められる。 ×;大部分が密着している。Coolability: The spun yarn was visually observed and evaluated according to the following three grades. ◯: No adhesion thread is observed. Δ: A small amount of adhesive thread is recognized. X: Most of them are in close contact.
【0040】・可紡性; ○;糸切れが発生せず、紡糸操業性が良好である。 ×;糸切れが多発し、紡糸操業性が不良である。Spinnability: Good; no yarn breakage occurs, and spinning operability is good. X: Thread breakage occurs frequently and spinning operability is poor.
【0041】・延伸性; ○;延伸毛羽が発生せず、延伸操業性が良好である。 ×;延伸毛羽が多発し、延伸が不可能である。Stretchability: Good: Stretching fluff is not generated and stretching operability is good. X: Stretching fuzz occurs frequently and stretching is impossible.
【0042】・目付け(g/m2 );標準状態の試料か
ら試料長が10cm、試料幅が10cmの試料片10点
を作成し平衡水分にした後、各試料片の重量(g)を秤
量し、得られた値の平均値を単位面積当たりに換算し、
目付け(g/m2 )とした。-Unit weight (g / m 2 ); 10 pieces of a sample having a sample length of 10 cm and a sample width of 10 cm were prepared from a sample in a standard state, equilibrated with water, and then the weight (g) of each sample piece was measured. Then, convert the average value of the obtained values per unit area,
The basis weight (g / m 2 ) was used.
【0043】・不織布の強力(kg/5cm幅);JI
S−L−1096Aに記載の方法に準じて測定した。す
なわち、試料長が20cm、試料幅が5cmの試料片1
0点を作成し、試料片毎に不織布の縦方向について、定
速伸張型引張り試験機(東洋ボールドウイン社製テンシ
ロンUTM−4−1−100)を用いて、引張り速度1
0cm/分で伸張し、得られた切断時荷重値の平均値を
強力(kg/5cm幅)とした。Strength of non-woven fabric (kg / 5 cm width); JI
It was measured according to the method described in S-L-1096A. That is, a sample piece 1 having a sample length of 20 cm and a sample width of 5 cm
A zero point was created, and a tensile speed of 1 was set for each sample piece in the longitudinal direction of the nonwoven fabric using a constant-speed extension-type tensile tester (Tensilon UTM-4-1-100 manufactured by Toyo Baldwin Co., Ltd.).
It was stretched at 0 cm / min, and the average value of the load values at cutting obtained was taken as the strength (kg / 5 cm width).
【0044】・生分解性能;不織布を土中に埋設し、6
ヶ月後に取り出し、不織布がその形態を保持していない
場合、あるいは、その形態を保持していても強力が埋設
前の強力初期値に対して50%以下に低下している場
合、生分解性能が良好(;○)であるとし、強力が埋設
前の強力初期値に対して50%を超える場合、生分解性
能が不良(;×)であると評価した。・ Biodegradability: 6 is obtained by embedding a non-woven fabric in soil.
If the nonwoven fabric does not retain its shape after a month, or if the strength is reduced to 50% or less of the initial strength value before embedding even if it retains its shape, the biodegradation performance is The biodegradability was evaluated as poor (; x) if the strength was more than 50% of the initial strength before embedding.
【0045】実施例1 芯成分として、MFR値が20g/10分で融点114
℃、結晶化温度75℃のポリブチレンサクシネートを、
鞘成分として、MFR値が30g/10分で融点102
℃、結晶化温度52℃のブチレンサクシネート/エチレ
ンサクシネート=85/15モル%の共重合体を用い
て、芯鞘型複合短繊維よりなる短繊維ウエブを製造し
た。すなわち、前記芯成分と鞘成分とを個別のエクスト
ルーダ型溶融押出し機を用いて、温度180℃で溶融
し、芯鞘型複合断面となる紡糸口金を用い、単孔吐出量
=1.02g/分、複合比(芯成分/鞘成分)=1/1
(重量比)の条件下にて溶融紡出した。この紡出糸条を
冷却装置にて冷却した後で油剤を付与し、速度が800
m/分の引き取りロールを介して繊度が11.5デニー
ルの未延伸糸を得た。得られた未延伸糸束を複数集束
し、延伸温度が常温の条件下で延伸倍率4.0倍で延伸
し、次いで、スタッファーボックスにて15個/インチ
の捲縮を付与した後、51mmに切断し、銘柄3d×5
1mmの短繊維を得た。この短繊維をパラレルカード機
に供給して目付けが50g/m2 のカードウエブを作成
した。Example 1 A core component having an MFR value of 20 g / 10 minutes and a melting point of 114
Polybutylene succinate having a crystallization temperature of 75 ° C.
As a sheath component, MFR value is 30g / 10min and melting point is 102
Using a copolymer of butylene succinate / ethylene succinate = 85/15 mol% at a crystallization temperature of 52 ° C. and a crystallization temperature of 52 ° C., a short fiber web composed of core-sheath type composite short fibers was produced. That is, the core component and the sheath component were melted at a temperature of 180 ° C. using separate extruder type melt extruders, and a spinneret having a core-sheath composite cross section was used, and single hole discharge rate = 1.02 g / min. , Composite ratio (core component / sheath component) = 1/1
Melt spinning was performed under the condition of (weight ratio). After cooling this spun yarn with a cooling device, an oil agent is applied, and the speed is 800
An undrawn yarn having a fineness of 11.5 denier was obtained through a take-up roll of m / min. A plurality of the obtained unstretched yarn bundles were bundled, stretched at a stretching ratio of 4.0 times under the condition that the stretching temperature was room temperature, and then crimped with a stuffer box at 15 pieces / inch, and then 51 mm. Cut, brand 3d x 5
1 mm short fibers were obtained. This short fiber was supplied to a parallel card machine to prepare a card web having a basis weight of 50 g / m 2 .
【0046】次いで、得られた短繊維ウエブを移動する
40メッシュの金網上に載置し、短繊維ウエブの上方5
0mmの位置より加圧液体流の噴射孔として、孔径0.
12mm、孔間隔0.6mmで一列に配されたオリフィ
スヘッドが5段に配列された装置を用いて加圧液体流処
理を行い、三次元交絡させた目付けが50g/m2 の生
分解性短繊維不織布を得た。処理条件としては、第1回
目の液圧を35kg/cm2 Gとして予備交絡を施した
後、第2回目以降の液圧を90kg/cm2 Gとして構
成繊維間に三次元交絡を形成した。そして、得られた不
織布の余分な水分をマングルにて除去した後、80℃の
温度に保たれた乾燥機により乾燥処理を行った。芯鞘型
複合短繊維製造の操業性及び生分解性短繊維不織布物
性、生分解性能を表1に示す。Then, the obtained short fiber web is placed on a moving 40-mesh wire mesh, and the upper part of the short fiber web is placed 5
From the position of 0 mm, a hole diameter of 0.
A biodegradable short product with a unit weight of 50 g / m 2 which is three-dimensionally entangled by performing pressurized liquid flow treatment using a device in which orifice heads arranged in a row with 12 mm and hole spacing of 0.6 mm are arranged in 5 stages. A fibrous nonwoven fabric was obtained. As the treatment condition, after the first hydraulic pressure was set to 35 kg / cm 2 G for pre-entanglement, the second and subsequent hydraulic pressures were set to 90 kg / cm 2 G to form three-dimensional entanglement between the constituent fibers. Then, after removing excess water of the obtained non-woven fabric by mangle, a drying treatment was performed by a drier kept at a temperature of 80 ° C. Table 1 shows the operability and biodegradability of the short-fiber nonwoven fabric and the biodegradability of the core-sheath type composite short fiber production.
【0047】実施例2 単孔吐出量=0.40g/分、複合比(芯成分/鞘成
分)=1/3(重量比)で溶融紡糸を行い、単糸繊度が
4.6デニールの未延伸糸を得、延伸倍率3.2倍にて
延伸したこと及び38mmに切断したこと以外は実施例
1と同一条件下にて、芯鞘型複合短繊維を製造した。得
られた短繊維は銘柄1.5d×38mmであった。この
短繊維をパラレルカード機に供給して目付けが50g/
m2 のカードウエブを作成し、実施例1と同一条件下に
て加圧液体流処理を行い、三次元交絡させた生分解性短
繊維不織布を得た。芯鞘型複合短繊維製造の操業性及び
生分解性短繊維不織布物性、生分解性能を表1に示す。Example 2 Melt spinning was performed at a single hole discharge rate of 0.40 g / min and a composite ratio (core component / sheath component) = 1/3 (weight ratio), and a single yarn fineness of 4.6 denier was measured. A core-sheath type composite short fiber was produced under the same conditions as in Example 1 except that a drawn yarn was obtained, drawn at a draw ratio of 3.2 and cut into 38 mm. The obtained short fibers had a brand of 1.5 d × 38 mm. This short fiber is fed to a parallel card machine and the basis weight is 50 g /
Create a card web m 2, subjected to pressurized liquid jet treatment under the same conditions as in Example 1 to obtain a biodegradable staple fiber nonwoven fabric obtained by three-dimensional entanglement. Table 1 shows the operability and biodegradability of the short-fiber nonwoven fabric and the biodegradability of the core-sheath type composite short fiber production.
【0048】実施例3 単孔吐出量=4.10g/分、複合比(芯成分/鞘成
分)=3/1(重量比)で溶融紡糸を行い、単糸繊度が
46デニールの未延伸糸を得、延伸倍率4.8倍にて延
伸したこと及び76mmに切断したこと以外は実施例1
と同一条件下にて、芯鞘型複合短繊維を製造した。得ら
れた短繊維は銘柄10d×76mmであった。この短繊
維をパラレルカード機に供給して目付けが50g/m2
のカードウエブを作成し、実施例1と同一条件下にて加
圧液体流処理を行い、三次元交絡させた生分解性短繊維
不織布を得た。芯鞘型複合短繊維製造の操業性及び生分
解性短繊維不織布物性、生分解性能を表1に示す。Example 3 Single-hole discharge amount = 4.10 g / min, melt-spinning was performed at a composite ratio (core component / sheath component) = 3/1 (weight ratio), and an undrawn yarn having a single yarn fineness of 46 denier Example 1 except that the above was obtained and stretched at a stretch ratio of 4.8 times and cut into 76 mm.
Under the same conditions as above, a core-sheath type composite staple fiber was produced. The obtained short fibers had a brand of 10 d × 76 mm. This short fiber is fed to a parallel card machine and the basis weight is 50 g / m 2
The card web of No. 2 was prepared and subjected to a pressurized liquid flow treatment under the same conditions as in Example 1 to obtain a three-dimensionally entangled biodegradable short fiber nonwoven fabric. Table 1 shows the operability and biodegradability of the short-fiber nonwoven fabric and the biodegradability of the core-sheath type composite short fiber production.
【0049】実施例4 高融点成分および低融点成分に結晶核剤を添加したこと
以外は実施例1と同様にして、芯鞘型複合短繊維よりな
る短繊維不織布を製造した。すなわち、結晶核剤とし
て、平均粒径が1.0μmのタルク/酸化チタン=1/
1(重量比)を20重量%含有させたマスターバッチを
高融点成分重合体および低融点成分重合体ベースであら
かじめ作成し、このマスターバッチとそれに対応する重
合体とをそれぞれブレンドして、高融点成分に添加する
結晶核剤が0.2重量%、低融点成分に添加する結晶核
剤が1.0重量%となるようにして原料とした。芯鞘型
複合短繊維製造の操業性及び生分解性短繊維不織布物
性、生分解性能を表1に示す。Example 4 A short fiber non-woven fabric composed of core-sheath type composite short fibers was produced in the same manner as in Example 1 except that a crystal nucleating agent was added to the high melting point component and the low melting point component. That is, as a crystal nucleating agent, talc / titanium oxide having an average particle size of 1.0 μm = 1 /
A master batch containing 20% by weight of 1 (weight ratio) was prepared in advance based on a high-melting-point component polymer and a low-melting-point component polymer, and the master batch and the corresponding polymer were each blended to obtain a high melting point. The crystal nucleating agent added to the components was 0.2% by weight, and the crystal nucleating agent added to the low melting point component was 1.0% by weight to prepare raw materials. Table 1 shows the operability and biodegradability of the short-fiber nonwoven fabric and the biodegradability of the core-sheath type composite short fiber production.
【0050】比較例1 実施例1と同一の芯成分を用い、繊維横断面が単相型断
面となる紡糸口金を介して、単孔吐出量=0.97g/
分の条件下にて溶融紡出した。すなわち、前記芯成分を
エクストルーダ型溶融押出し機を用いて、温度180℃
で溶融し、単相型断面となる紡糸口金を介して溶融紡出
し、この紡出糸条を冷却装置にて冷却した後で油剤を付
与し、速度が800m/分の引き取りロールを介して繊
度が10.9デニールの未延伸糸を得た。得られた未延
伸糸束を複数集束し、延伸温度が常温の条件下で延伸倍
率3.8で延伸し、次いで、スタッファーボックスにて
14個/インチの捲縮を付与した後、51mmに切断
し、銘柄3d×51mmの短繊維を得た。この短繊維を
パラレルカード機に供給して目付けが25g/m2 のカ
ードウエブを作成し、実施例1と同一条件下にて加圧液
体流処理を行い、三次元交絡させた生分解性短繊維不織
布を得た。芯鞘型複合短繊維製造の操業性及び生分解性
短繊維不織布物性、生分解性能を表1に示す。Comparative Example 1 The same core component as in Example 1 was used, and the single hole discharge rate was 0.97 g / through a spinneret having a fiber cross section of a single phase type cross section.
Melt-spun under the conditions of minutes. That is, the core component was heated at a temperature of 180 ° C. using an extruder type melt extruder.
Melted and melt-spun through a spinneret having a single-phase cross-section, the spun yarn is cooled in a cooling device, and then an oil agent is applied. The speed is 800 m / min and the fineness is obtained through a take-up roll. To obtain 10.9 denier undrawn yarn. A plurality of the obtained unstretched yarn bundles are bundled, stretched at a stretching ratio of 3.8 under a stretching temperature of room temperature, then crimped with a stuffer box at 14 pieces / inch, and then cut into 51 mm. Then, a short fiber of brand 3d × 51 mm was obtained. This short fiber was fed to a parallel card machine to prepare a card web having a basis weight of 25 g / m 2 , and a pressurized liquid flow treatment was carried out under the same conditions as in Example 1, and three-dimensionally entangled biodegradable short fibers. A fibrous nonwoven fabric was obtained. Table 1 shows the operability and biodegradability of the short-fiber nonwoven fabric and the biodegradability of the core-sheath type composite short fiber production.
【0051】比較例2 実施例1と同一の鞘成分を用い、繊維横断面が単相型断
面となる紡糸口金を介して、単孔吐出量=0.97g/
分の条件下にて溶融紡出し、この紡出糸条を冷却装置に
て冷却した後で油剤を付与し、速度が800m/分の引
き取りロールを介して未延伸糸を得たが、得られた未延
伸糸は糸条間で密着していたため、単相型紡出糸条を得
ることができなかった。Comparative Example 2 The same sheath component as in Example 1 was used, and a single hole discharge rate = 0.97 g / through a spinneret having a fiber cross section of a single phase type cross section.
Was melt-spun under the condition of min., The spun yarn was cooled by a cooling device, and then an oil agent was applied to obtain undrawn yarn through a take-up roll having a speed of 800 m / min. Since the undrawn yarn was adhered between the yarns, a single-phase spun yarn could not be obtained.
【0052】[0052]
【表1】 [Table 1]
【0053】表1から明らかなように、実施例1で得ら
れた不織布は、本発明の芯鞘型複合短繊維を適用してい
るので、紡出糸条の冷却性、可紡性、延伸性、および機
械的特性にも優れるものであった。また、この不織布を
6ケ月間土中に埋設し、その後に掘り出して観察したと
ころ、不織布としての形態を保持しておらず良好な生分
解性を有することが認められた。As is clear from Table 1, since the nonwoven fabric obtained in Example 1 uses the core-sheath type composite staple fiber of the present invention, the spun yarn has cooling properties, spinnability and drawing properties. It was also excellent in mechanical properties and mechanical properties. Further, when this non-woven fabric was embedded in soil for 6 months and then excavated and observed, it was confirmed that the non-woven fabric did not retain its form and had good biodegradability.
【0054】実施例2は、鞘成分の比率が大ではある
が、繊度を小さくそして芯鞘型複合短繊維を適用してい
るので、実施例1と同様、紡出糸条の冷却性、可紡性、
延伸性も良好であり、この不織布は機械的特性にも優れ
るものであった。また、生分解性能は鞘成分の比率が大
であるので実施例1で得られた不織布よりさらに良好な
結果が得られた。In Example 2, although the ratio of the sheath component was large, the fineness was small and the core-sheath type composite staple fiber was applied. Spinnability,
The stretchability was also good, and this nonwoven fabric was also excellent in mechanical properties. Further, the biodegradability was higher than that of the nonwoven fabric obtained in Example 1 because the ratio of the sheath component was large.
【0055】実施例3は、芯成分の比率が大であり、芯
鞘型複合短繊維を適用しているため、繊度が大きいにも
かかわらず、実施例1と同様、紡出糸条の冷却性、可紡
性、延伸性も良好であった。また、この不織布は機械的
特性および生分解性能にも優れるものであった。In Example 3, since the ratio of the core component was large and the core-sheath type composite short fibers were applied, the spinning yarn was cooled in the same manner as in Example 1 even though the fineness was large. The spinnability, spinnability and stretchability were also good. Further, this non-woven fabric was also excellent in mechanical properties and biodegradability.
【0056】実施例4は、重合体中に結晶核剤が入って
いるので、紡出糸条の冷却性、可紡性、延伸性が実施例
1よりもさらにも良好であった。また、この不織布は機
械的特性および生分解性能にも優れるものであった。In Example 4, since the crystal nucleating agent was contained in the polymer, the spinnability of the spun yarn was better than that of Example 1. Further, this non-woven fabric was also excellent in mechanical properties and biodegradability.
【0057】これに対し、比較例1は、実施例1と同一
の芯成分を用いたものの、繊維横断面が本発明範囲外で
ある単相型であるために、不織布の機械的特性には優れ
るものの、不織布を6ケ月間土中に埋設し、その後に掘
り出して観察したところ不織布形態を維持しており、不
織布強力も埋設前の91%であり、生分解性能には著し
く劣るものであった。On the other hand, in Comparative Example 1, although the same core component as in Example 1 was used, the cross-section of the fiber was a single-phase type which was outside the scope of the present invention, so the mechanical properties of the nonwoven fabric were Although excellent, the non-woven fabric was buried in the soil for 6 months, and then excavated and observed, the non-woven fabric form was maintained, and the non-woven fabric strength was 91% before embedding, which is significantly inferior in biodegradability. It was
【0058】比較例2は、実施例1と同一の鞘成分を用
いたものの、未延伸糸は糸条間で密着していたため、単
相型紡出糸条を得ることができなかった。In Comparative Example 2, although the same sheath component as in Example 1 was used, the single-phase spun yarn could not be obtained because the undrawn yarn was in close contact between the yarns.
【0059】[0059]
【発明の効果】本発明によれば、紡出糸条の冷却性及び
可紡性、延伸性に優れ、良好な生分解性能を有するとと
もにその制御が可能であり、さらに実使用に耐えうるだ
けの充分な機械的特性を有する生分解性短繊維不織布及
びその製造方法を提供することができる。EFFECTS OF THE INVENTION According to the present invention, the spun yarn has excellent cooling properties, spinnability and stretchability, has good biodegradability, and can be controlled, and can withstand practical use. It is possible to provide a biodegradable short fiber non-woven fabric having sufficient mechanical properties and a method for producing the same.
【0060】本発明の生分解性短繊維不織布は、おむつ
や生理用品その他の医療・衛生材料素材、使い捨ておし
ぼりやワイピングクロスなどの拭き取り布、使い捨て包
装材、家庭・業務用の生ごみ捕集用袋その他廃棄物処理
材などの生活関連用素材、あるいは、農業・園芸・土木
用に代表される産業用資材の各素材として好適である。
しかもこの生分解性短繊維不織布は、生分解性を有する
ので、その使用後に完全に分解消失するため、自然環境
保護の観点からも有益であり、あるいは、例えば堆肥化
して肥料とするなど再利用を図ることもできるため資源
の再利用の観点からも有益である。The biodegradable short fiber non-woven fabric of the present invention is used for diapers, sanitary products and other medical and hygiene materials, wipes such as disposable hand towels and wiping cloths, disposable packaging materials, and household / commercial garbage collection. It is suitable as a material for daily life such as bags and other waste treatment materials, or an industrial material typified by agriculture, horticulture and civil engineering.
Moreover, since this biodegradable short-fiber non-woven fabric has biodegradability, it is completely decomposed and lost after its use, which is beneficial from the viewpoint of protecting the natural environment, or reused, for example, by composting it into fertilizer. It is also useful from the viewpoint of resource reuse because it can be achieved.
Claims (6)
元交絡により一体化されており、前記複合短繊維が生分
解性を有する第1の脂肪族ポリエステルからなる芯成分
とこの芯成分よりも融点の低い生分解性を有する第2の
脂肪族ポリエステルからなる鞘成分とから形成される芯
鞘型複合断面を有してなることを特徴とする生分解性短
繊維不織布。1. A staple fiber web composed of composite staple fibers is integrated by three-dimensional entanglement, and the composite staple fiber comprises a core component composed of a first aliphatic polyester having biodegradability and a core component composed of the core component. A biodegradable short-fiber non-woven fabric having a core-sheath composite cross section formed from a sheath component made of a second aliphatic polyester having a low melting point and having biodegradability.
あり、鞘成分が、ブチレンサクシネートの共重合量比が
70〜90モル%となるようにブチレンサクシネートに
エチレンサクシネートあるいはブチレンアジペートを共
重合せしめた共重合ポリエステルであることを特徴とす
る請求項1記載の生分解性短繊維不織布。2. The core component is polybutylene succinate, and the sheath component is copolymerized with ethylene succinate or butylene adipate in butylene succinate so that the copolymerization amount ratio of butylene succinate is 70 to 90 mol%. The biodegradable short fiber non-woven fabric according to claim 1, which is a copolymerized polyester that is polymerized.
なくとも低融点成分に中に結晶核剤が添加されているこ
とを特徴とする請求項1または2記載の生分解性短繊維
不織布。3. The biodegradable short fiber non-woven fabric according to claim 1, wherein a crystal nucleating agent is added to at least the low melting point component of the low melting point component and the high melting point component.
度が1.5〜10デニールであり、芯成分/鞘成分の複
合比が1/3〜3/1(重量比)であることを特徴とす
る請求項1から3までのいずれか1項に記載の生分解性
短繊維不織布。4. A single yarn fineness composed of a core component and a sheath component is 1.5 to 10 denier, and a composite ratio of the core component / the sheath component is 1/3 to 3/1 (weight ratio). The biodegradable short-fiber non-woven fabric according to any one of claims 1 to 3, characterized in that.
テルからなる芯成分とこの芯成分よりも融点の低い生分
解性を有する第2の脂肪族ポリエステルからなる鞘成分
とを用いて、芯鞘型複合繊維を溶融複合紡糸し、次いで
延伸し、得られた延伸糸条に機械捲縮を付与した後に所
定長に切断して短繊維となし、この短繊維をカーディン
グすることにより短繊維ウエブを形成し、この短繊維ウ
エブに加圧液体流処理を施して構成繊維を三次元交絡さ
せ一体化することを特徴とする生分解性短繊維不織布の
製造方法。5. A core comprising a core component made of a first aliphatic polyester having biodegradability and a sheath component made of a second aliphatic polyester having a lower melting point than that of the core component. Melt composite spinning of sheath-type composite fibers is followed by drawing, and the resulting drawn yarn is mechanically crimped and then cut into predetermined lengths to form short fibers, and the short fibers are carded to obtain short fibers. A method for producing a biodegradable short fiber nonwoven fabric, which comprises forming a web and subjecting the short fiber web to a pressurized liquid flow treatment to three-dimensionally entangle and integrate the constituent fibers.
なくとも低融点成分に中に結晶核剤を添加して溶融複合
紡糸を行うことを特徴とする請求項5記載の生分解性短
繊維不織布の製造方法。6. The biodegradable short fiber non-woven fabric according to claim 5, wherein a crystal nucleating agent is added to at least the low melting point component of the low melting point component and the high melting point component to carry out melt composite spinning. Manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8092115A JPH09279446A (en) | 1996-04-15 | 1996-04-15 | Biodegradable short fiber nonwoven fabric and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8092115A JPH09279446A (en) | 1996-04-15 | 1996-04-15 | Biodegradable short fiber nonwoven fabric and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH09279446A true JPH09279446A (en) | 1997-10-28 |
Family
ID=14045446
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8092115A Pending JPH09279446A (en) | 1996-04-15 | 1996-04-15 | Biodegradable short fiber nonwoven fabric and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH09279446A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117737884A (en) * | 2023-12-05 | 2024-03-22 | 东华大学 | Preparation method of biodegradable PBS (Poly Butylene succinate) parallel curled elastic fiber |
-
1996
- 1996-04-15 JP JP8092115A patent/JPH09279446A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117737884A (en) * | 2023-12-05 | 2024-03-22 | 东华大学 | Preparation method of biodegradable PBS (Poly Butylene succinate) parallel curled elastic fiber |
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