JP6753254B2 - Polyethylene spunbonded non-woven fabric - Google Patents
Polyethylene spunbonded non-woven fabric Download PDFInfo
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Description
本発明は柔軟性に優れ、高強度であり、加工性に優れるポリエチレンスパンボンド不織布に関する。 The present invention relates to a polyethylene spunbonded nonwoven fabric having excellent flexibility, high strength, and excellent workability.
ポリオレフィンからなるスパンボンド不職布、特にポリプロピレンスパンボンド不職布は低コストで柔軟性に優れるため、衛生材料用途を中心に幅広く用いられている。 Spunbond non-woven fabric made of polyolefin, especially polypropylene spunbond non-woven fabric, is widely used mainly for sanitary materials because of its low cost and excellent flexibility.
ポリオレフィンスパンボンド不織布の特徴である柔軟性をより高める技術もこれまでに多くの検討がなされており、その中で弾性率がポリプロピレンよりも低い、ポリエチレンを用いる検討がなされている。 Many studies have been conducted on techniques for further enhancing the flexibility, which is a characteristic of polyolefin spunbonded non-woven fabrics, and among them, polyethylene, which has a lower elastic modulus than polypropylene, has been studied.
ポリエチレンスパンボンドは柔軟性に優れるものの、シートの加工性に劣るという課題がある。この原因の一つは、ポリエチレンは製糸性が悪く、糸切れが生じやすいためシート欠点が多く、加工時にこの欠点を起点としてゴム製のニップローラー等に巻き付いてしまうためであり、また繊維強度が低いためシート強度も低く、シート加工時に破れ等が生じやすいためである。この課題のため実用性能を満足するポリエチレンスパンボンドは工業的には未だ得られていない。 Although polyethylene spunbond has excellent flexibility, it has a problem that the workability of the sheet is inferior. One of the reasons for this is that polyethylene has poor silk-reeling properties and is prone to thread breakage, so there are many sheet defects, and this defect is the starting point for wrapping around rubber nip rollers, etc., and the fiber strength is high. This is because the sheet strength is low because it is low, and tearing or the like is likely to occur during sheet processing. Due to this problem, polyethylene spunbonds that satisfy practical performance have not yet been obtained industrially.
また柔軟性向上のために単糸繊度を小さくしようとすると、ポリエチレンでは製糸性がより悪化する傾向にあるため、欠点がさらに増え、加工性がより悪化する課題もある。 Further, if an attempt is made to reduce the fineness of a single yarn in order to improve flexibility, the yarn-forming property of polyethylene tends to be further deteriorated, so that there is a problem that the defects are further increased and the workability is further deteriorated.
単糸繊度が小さく、シート欠点が少ないポリエチレンスパンボンドを得る技術に関し、密度が0.900〜0.940g/cm3、メルトインデックス値が5〜45g/10分であり、融解熱が25cal/g(すなわち104.7J/g)以上である線状低密度ポリエチレンを用いることが開示されている(特許文献1参照)。該技術ではエアーサッカーを用い高速で紡糸を行う技術が開示されているが、単糸繊度については5デニール以下の記載があるものの、実施例で到達している最も小さい単糸繊度は1.9d、すなわち2.1dtexであり2.0dtex以下の十分小さい単糸繊度は得られておらず柔軟性は向上できていない。 Regarding the technology for obtaining polyethylene spunbond with low single yarn fineness and few sheet defects, the density is 0.900 to 0.940 g / cm 3 , the melt index value is 5 to 45 g / 10 minutes, and the heat of fusion is 25 cal / g. (That is, 104.7 J / g) or more is disclosed to use linear low-density polyethylene (see Patent Document 1). In this technique, a technique for spinning at high speed using air soccer is disclosed. Although there is a description of 5 denier or less for single yarn fineness, the smallest single yarn fineness reached in the examples is 1.9d. That is, a sufficiently small single yarn fineness of 2.1 dtex and 2.0 dtex or less has not been obtained, and the flexibility has not been improved.
また密度が0.940g/cm3よりも大きく、約4〜約1000のメルトインデックスを有するポリエチレンを用いる技術も開示されている(特許文献2参照)。該技術においては単糸繊度を小さくすることに関する記載は見られず、スパンボンドの実施例で到達している最も小さい繊維直径は29.4μmである。このときの樹脂密度は0.882g/cm3であるため単糸繊度は6.0dtexとなり2.0dtex以下の十分小さい単糸繊度は得られておらず柔軟性は向上できていない。 Further, a technique using polyethylene having a density of more than 0.940 g / cm 3 and a melt index of about 4 to about 1000 is also disclosed (see Patent Document 2). No description is found in the technique regarding reducing the single yarn fineness, and the smallest fiber diameter reached in the spunbonded examples is 29.4 μm. Since the resin density at this time is 0.882 g / cm 3 , the single yarn fineness is 6.0 dtex, and a sufficiently small single yarn fineness of 2.0 dtex or less has not been obtained, and the flexibility has not been improved.
さらに密度が0.85〜0.97g/cm3のポリエチレンを用いる技術も開示されている(特許文献3参照)。該技術では繊維径、繊度に関し通常5〜30μm(0.2〜7デニール)の記載があるが、実施例で到達している最も小さい単糸繊度は2.5d、すなわち2.8dtexであり2.0dtex以下の十分小さい単糸繊度は得られておらず柔軟性は向上できていない。 Further, a technique using polyethylene having a density of 0.85 to 0.97 g / cm 3 is also disclosed (see Patent Document 3). In the technique, there is usually a description of 5 to 30 μm (0.2 to 7 denier) regarding fiber diameter and fineness, but the smallest single yarn fineness reached in the examples is 2.5 d, that is, 2.8 dtex, which is 2 A sufficiently small single yarn fineness of 0.0 dtex or less has not been obtained, and the flexibility has not been improved.
密度が0.955g/cm3のポリエチレンを用いる技術も開示されている(特許文献4参照)。該技術では繊度に関し0.1〜50デニールの記載があるが、該技術の実施例で得られている単糸繊度は2.5デニール、すなわち2.8dtexであり2.0dtex以下の十分小さい単糸繊度は得られておらず柔軟性は向上できていない。 A technique using polyethylene having a density of 0.955 g / cm 3 is also disclosed (see Patent Document 4). Although there is a description of 0.1 to 50 denier in terms of fineness in the technique, the single yarn fineness obtained in the examples of the technique is 2.5 denier, that is, 2.8 dtex, which is sufficiently small to be 2.0 dtex or less. The thread fineness has not been obtained and the flexibility has not been improved.
密度が0.9〜0.955g/cm3のポリエチレンを用いる技術も開示されている(特許文献5参照)。該技術では繊度に関し2.8dtex未満の記載があるが、該技術の実施例で得られているポリエチレン単独のスパンボンドの単糸繊度は2.5dtexであり2.0dtex以下の十分小さい単糸繊度は得られておらず柔軟性は向上できていない。 A technique using polyethylene having a density of 0.9 to 0.955 g / cm 3 is also disclosed (see Patent Document 5). Although there is a description of the fineness of less than 2.8 dtex in the technique, the single thread fineness of the polyethylene-only spunbond obtained in the examples of the technique is 2.5 dtex, which is sufficiently small as 2.0 dtex or less. Has not been obtained and flexibility has not been improved.
本発明の課題は、柔軟性に優れ、高強度であり、加工性に優れるポリエチレンスパンボンド不織布を提供することにある。 An object of the present invention is to provide a polyethylene spunbonded nonwoven fabric having excellent flexibility, high strength, and excellent workability.
前記した本発明の課題は以下の手段により達成される。
密度が0.945〜0.965g/cm3の線状低密度ポリエチレンからなり、単糸繊度が0.5dtex以上、2.0dtex以下であり、単糸のΔnが0.035以上、0.038以下であることを特徴とするポリエチレンスパンボンド不織布。
The above-mentioned problem of the present invention is achieved by the following means.
It is made of linear low-density polyethylene with a density of 0.945 to 0.965 g / cm 3 , a single yarn fineness of 0.5 dtex or more and 2.0 dtex or less, and a single yarn Δn of 0.035 or more and 0.038. A polyethylene spunbonded non-woven fabric characterized by the following .
本発明のポリエチレンスパンボンド不織布により、柔軟性をより向上させることができ、かつ単糸繊度が細いため触感も向上し、繊維の強度も高まるためシート加工時の破れ等もなく、さらにシート欠点が少ないため加工性をより向上させることができる。 The polyethylene spunbonded non-woven fabric of the present invention can further improve the flexibility, and since the single yarn fineness is thin, the tactile sensation is also improved, and the strength of the fiber is also increased, so that there is no tearing during sheet processing, and there are further sheet defects. Since the amount is small, the workability can be further improved.
以下、本発明のポリエチレンスパンボンド不織布について詳細に説明する。
本発明のポリエチレン(以下、PEとも言う)スパンボンド不織布はポリエチレン樹脂の繊維からなる。ポリエチレン樹脂とは繰り返し単位としてエチレン単位を有するポリマーを意味する。ポリエチレン樹脂を用いることで柔軟性に優れた不織布とすることができる。
Hereinafter, the polyethylene spunbonded nonwoven fabric of the present invention will be described in detail.
The polyethylene (hereinafter, also referred to as PE) spunbonded nonwoven fabric of the present invention is made of polyethylene resin fibers. The polyethylene resin means a polymer having an ethylene unit as a repeating unit. By using a polyethylene resin, a non-woven fabric having excellent flexibility can be obtained.
スパンボンド不織布を構成するポリエチレン繊維はポリエチレン単成分の繊維であることが好ましい。ポリエチレンの繊維化においては他ポリマーとの複合(芯鞘、海島、サイドバイサイド)も可能であるが、本願発明ではポリエチレンの特性を十分に発現させ、かつ複合紡糸では到達しがたい細繊度化を達成するためポリエチレン単成分が好ましい。 The polyethylene fiber constituting the spunbonded non-woven fabric is preferably a polyethylene single component fiber. In the fiberization of polyethylene, it is possible to combine it with other polymers (core sheath, sea island, side-by-side), but in the present invention, the characteristics of polyethylene are fully expressed and fineness that is difficult to reach by composite spinning is achieved. Therefore, a polyethylene single component is preferable.
PE樹脂には少量の他成分ポリマーがブレンドされていても良い。他成分ポリマーとしては融点がPEに近いポリプロピレン、ポリ4メチル1ペンテンなどのポリオレフィン系ポリマーの他、低融点ポリエステル、低融点ポリアミドが挙げられる。ただしポリエチレンの特性を十分発現させるため、ブレンド物の重量比率は5wt%以下が好ましく、2wt%以下がより好ましい。
またPE樹脂には着色のための顔料、酸化防止剤、ポリエチレンワックス等の滑剤、耐熱安定剤等が添加されていても良い。
A small amount of other component polymer may be blended with the PE resin. Examples of the other component polymer include polyolefin-based polymers having a melting point close to PE, such as polypropylene and poly4-methylpentene, as well as low-melting polyester and low-melting polyamide. However, in order to fully express the characteristics of polyethylene, the weight ratio of the blend is preferably 5 wt% or less, more preferably 2 wt% or less.
Further, a pigment for coloring, an antioxidant, a lubricant such as polyethylene wax, a heat-resistant stabilizer and the like may be added to the PE resin.
本発明で用いるPE樹脂は線状低密度ポリエチレン(以下、LLDPEとも言う)である。PEには製法、物性の違いにより区分される高密度ポリエチレン(HDPE)、低密度ポリエチレン(LDPE)、LLDPEがあり、それぞれ繊維用に検討されている。本発明ではLLDPEを用いることで細繊度、高強度が実現できる。 The PE resin used in the present invention is linear low density polyethylene (hereinafter, also referred to as LLDPE). PE includes high-density polyethylene (HDPE), low-density polyethylene (LDPE), and LLDPE, which are classified according to differences in manufacturing method and physical properties, and are being studied for fibers. In the present invention, fineness and high strength can be realized by using LLDPE.
また本発明で用いるPE樹脂の密度は0.945〜0.965g/cm3である。LLDPEの密度は共重合するモノマーの種類、量により変化するが、LLDPEとしては高密度である0.945〜0.965g/cm3とすることで適度な結晶性を発現し、高強度化が達成できる。この観点から密度は0.950〜0.960g/cm3がより好ましい。 The density of the PE resin used in the present invention is 0.945 to 0.965 g / cm 3 . The density of LLDPE varies depending on the type and amount of monomer to be copolymerized, but by setting the density of LLDPE to 0.945 to 0.965 g / cm 3 , which is a high density, appropriate crystallinity is exhibited and the strength is increased. Can be achieved. From this viewpoint, the density is more preferably 0.950 to 0.960 g / cm 3 .
本発明で用いるLLDPEには、本発明の目的を満足する限度で他のオレフィン類モノマー、スチレン類モノマーが共重合されていても良い。共重合成分としてはヘプテン、オクテンがシート欠点低減、細繊度の観点から好ましく、オクテンがより好ましい。また共重合比率は高強度化の観点から3.0mol%以下とすることが好ましく、1.0mol%以下とすることがより好ましい。 The LLDPE used in the present invention may be copolymerized with other olefin monomers and styrene monomers as long as the object of the present invention is satisfied. As the copolymerization component, heptene and octene are preferable from the viewpoint of reducing sheet defects and fineness, and octene is more preferable. The copolymerization ratio is preferably 3.0 mol% or less, and more preferably 1.0 mol% or less from the viewpoint of increasing the strength.
本発明のポリエチレンスパンボンド不織布の目付けは5〜50g/m2とすることが好ましい。目付が上記範囲であることで不織布の柔軟性を好適に発現することができる。この観点から目付けは10〜30g/m2とすることがより好ましい。 The basis weight of the polyethylene spunbonded non-woven fabric of the present invention is preferably 5 to 50 g / m 2 . When the basis weight is in the above range, the flexibility of the non-woven fabric can be suitably exhibited. From this point of view, the basis weight is more preferably 10 to 30 g / m 2 .
本発明のポリエチレンスパンボンド不織布を構成する繊維の断面形状は丸が好ましい。扁平や異形断面では曲げる方向によっては同一断面積の丸断面に対し断面2次モーメントが大きくなることから繊維が固くなり、ポリエチレンの持つ柔軟性を損なう可能性があるため、丸断面が好ましい。 The cross-sectional shape of the fibers constituting the polyethylene spunbonded nonwoven fabric of the present invention is preferably round. In a flat or irregular cross section, the geometrical moment of inertia is larger than that of a round cross section having the same cross-sectional area depending on the bending direction, so that the fibers may become hard and the flexibility of polyethylene may be impaired.
本発明のポリエチレンスパンボンド不織布を構成する繊維の単糸繊度は2.0dtex以下である。本発明でいう単糸繊度とは実施例記載の方法により測定された値を指す。単糸繊度を2.0dtex以下とすることで、ポリエチレンが持つ柔軟性に加え、単糸繊度が小さいことによる断面2次モーメントの低下も発現することで柔軟性がさらに向上し、かつ触感も向上する。この観点から単糸繊度は1.8dtex以下が好ましく、1.5dtex以下がより好ましい。なお単糸繊度の下限は0.5dtex程度である。 The single yarn fineness of the fibers constituting the polyethylene spunbonded nonwoven fabric of the present invention is 2.0 dtex or less. The single yarn fineness referred to in the present invention refers to a value measured by the method described in Examples. By setting the single yarn fineness to 2.0 dtex or less, in addition to the flexibility of polyethylene, the decrease in the moment of inertia of area due to the small single yarn fineness is also exhibited, further improving the flexibility and improving the tactile sensation. To do. From this viewpoint, the single yarn fineness is preferably 1.8 dtex or less, more preferably 1.5 dtex or less. The lower limit of the single yarn fineness is about 0.5 dtex.
同様の理由でポリエチレンスパンボンド不織布を構成する繊維の繊維直径は17.0μm以下が好ましく、16.0μm以下がより好ましく、15.0μm以下がさらに好ましい。本発明でいう繊維直径とは実施例記載の方法により測定された値を指す。繊維直径の下限は8.0μm程度である。 For the same reason, the fiber diameter of the fibers constituting the polyethylene spunbonded non-woven fabric is preferably 17.0 μm or less, more preferably 16.0 μm or less, still more preferably 15.0 μm or less. The fiber diameter referred to in the present invention refers to a value measured by the method described in Examples. The lower limit of the fiber diameter is about 8.0 μm.
本発明のポリエチレンスパンボンド不織布を構成する単糸のΔnは0.035以上である。本発明でいうΔnとは実施例記載の方法により測定された値を指す。Δnが0.035以上であることで分子配向が高くでき繊維の強度が高まる。この観点からΔnは0.037以上が好ましい。 The Δn of the single yarn constituting the polyethylene spunbonded nonwoven fabric of the present invention is 0.035 or more. Δn in the present invention refers to a value measured by the method described in Examples. When Δn is 0.035 or more, the molecular orientation can be increased and the strength of the fiber can be increased. From this viewpoint, Δn is preferably 0.037 or more.
本発明のポリエチレンスパンボンド不織布を構成する単糸強度は120MPa以上が好ましい。本発明でいう単糸強度とは実施例記載の方法により測定された値を指す。単糸強度が120MPa以上であることで加工時の糸切れが抑制でき加工性が優れる。この観点から単糸強度は130MPa以上がより好ましい。 The single yarn strength constituting the polyethylene spunbonded nonwoven fabric of the present invention is preferably 120 MPa or more. The single yarn strength referred to in the present invention refers to a value measured by the method described in Examples. When the single yarn strength is 120 MPa or more, yarn breakage during processing can be suppressed and the workability is excellent. From this viewpoint, the single yarn strength is more preferably 130 MPa or more.
本発明のポリエチレンスパンボンド不織布の融点は127℃〜131℃であることが好ましい。本発明でいう融点とは実施例記載の方法により測定された値を指す。PE樹脂の融点は一般的には130〜135℃程度であり、分岐、他種モノマーの共重合により結晶性が低下し、融点も低下する。融点が127℃〜131℃であることで適切な結晶化度を持ち、繊維強度が向上する。 The melting point of the polyethylene spunbonded non-woven fabric of the present invention is preferably 127 ° C to 131 ° C. The melting point referred to in the present invention refers to a value measured by the method described in Examples. The melting point of the PE resin is generally about 130 to 135 ° C., and the crystallinity is lowered by branching and copolymerization of other kinds of monomers, and the melting point is also lowered. When the melting point is 127 ° C to 131 ° C, the crystallinity is appropriate and the fiber strength is improved.
本発明のポリエチレンスパンボンド不織布の結晶融解熱量は160〜175J/gが好ましく、165〜175J/gがより好ましい。本発明でいう結晶融解熱量とは実施例記載の方法により測定された値を指す。結晶融解熱量も融点と同様、分岐、他種モノマーの共重合により結晶性が低下し、結晶融解熱量も低下する。結晶融解熱量が160〜175J/gであることで適切な結晶化度を持ち、繊維強度が向上する。 The heat of crystal melting of the polyethylene spunbonded nonwoven fabric of the present invention is preferably 160 to 175 J / g, more preferably 165 to 175 J / g. The amount of heat of crystal melting referred to in the present invention refers to a value measured by the method described in Examples. Similar to the melting point, the amount of heat of crystal melting also decreases due to branching and copolymerization of other types of monomers, and the amount of heat of crystal melting also decreases. When the amount of heat for melting the crystal is 160 to 175 J / g, the crystallinity is appropriate and the fiber strength is improved.
本発明のポリエチレンスパンボンド不織布は医療衛生材料、生活資材、工業資材等に幅広く用いることができるが、柔軟性に優れ、触感も良好であり、強度も高く、製品欠点も少ないため加工性が良好であることから、特に衛生材料に好適に用いることができる。具体的には使い捨ておむつ、生理用品、湿布材の基布等である。 The polyethylene spunbonded non-woven fabric of the present invention can be widely used for medical hygiene materials, daily life materials, industrial materials, etc., but has excellent flexibility, good tactile sensation, high strength, and few product defects, so that it has good workability. Therefore, it can be particularly preferably used as a sanitary material. Specifically, they are disposable diapers, sanitary napkins, and base cloths for poultices.
次に、本発明のポリエチレンスパンボンド不織布の製造方法の具体例を説明する。
用いる原料はLLDPE樹脂であり、その密度、共重合種と量、その他の添加物は前記したとおりである。
Next, a specific example of the method for producing the polyethylene spunbonded nonwoven fabric of the present invention will be described.
The raw material used is LLDPE resin, and its density, copolymerization species and amount, and other additives are as described above.
PE樹脂の融点も不織布の融点とほぼ同一であり、127℃〜131℃であることが好ましい。またPE樹脂はメルトインデックス(MI)が10〜100g/10分であることが好ましく、20〜40g/10分であることがより好ましい。なお、ここでいうメルトインデックスとはASTM D1238に準拠して、190℃、荷重2.16kgで測定した値を指す。 The melting point of the PE resin is also substantially the same as the melting point of the non-woven fabric, and is preferably 127 ° C. to 131 ° C. Further, the PE resin preferably has a melt index (MI) of 10 to 100 g / 10 minutes, and more preferably 20 to 40 g / 10 minutes. The melt index referred to here refers to a value measured at 190 ° C. and a load of 2.16 kg in accordance with ASTM D1238.
このような範囲のLLDPE樹脂を用いることで、高速で牽引しても曳糸性に優れるためシート欠点が少なく、かつ細繊度化が可能であり、高速牽引により分子配向を高めて繊維の強度を高めることができる。 By using LLDPE resin in such a range, even if it is towed at high speed, it has excellent spinnability, so there are few sheet defects and fineness can be achieved, and high-speed towing enhances the molecular orientation and increases the strength of the fiber. Can be enhanced.
PE樹脂は特に乾燥等を行うことなく、溶融紡糸に供する。溶融紡糸では単軸・2軸エクストルーダー型などの押出機を用いた公知の溶融紡糸手法を適用することができる。押し出されたポリマーは配管を経由しギアーポンプなど公知の計量装置により計量され、異物除去のフィルターを通過した後、口金へと導かれる。このときポリマー配管から口金までの温度(紡糸温度)は流動性を高めるため160〜250℃程度とする。 The PE resin is subjected to melt spinning without being particularly dried. For melt spinning, a known melt spinning method using an extruder such as a single-screw or twin-screw extruder can be applied. The extruded polymer is weighed by a known weighing device such as a gear pump via a pipe, passed through a foreign matter removing filter, and then guided to a mouthpiece. At this time, the temperature from the polymer pipe to the base (spinning temperature) is set to about 160 to 250 ° C. in order to improve the fluidity.
吐出において使用する口金は、口金孔の孔径Dを0.10mm以上、0.60mm以下とすることが好ましく、口金孔のランド長L(口金孔の孔径と同一の直管部の長さ)を孔径で除した商で定義されるL/Dは、1.0以上、4.0以下が好ましい。 The mouthpiece used for discharge preferably has a hole diameter D of the mouthpiece hole of 0.10 mm or more and 0.60 mm or less, and has a land length L of the mouthpiece hole (the length of a straight pipe portion same as the hole diameter of the mouthpiece hole). The L / D defined by the quotient divided by the pore size is preferably 1.0 or more and 4.0 or less.
口金孔から吐出した糸条は、空気により冷却固化させる。冷却風の温度は、冷却効率の観点から冷却風速とのバランスで決定すればよいが、繊度均一性の点から50℃以下であることが好ましい。また、冷却気体は糸条にほぼ垂直方向に流すことにより、糸条を冷却させる。その際、冷却風の速度は冷却効率および繊度均一性の点から5m/分以上が好ましく、製糸安定性の点から100m/分以下が好ましい。また、口金から20mm以上、500mm以内で冷却を開始し、冷却固化することが好ましい。20mm未満の距離で冷却を開始すると、口金表面温度が低下し吐出が不安定となることがあり、500mm以内で冷却を開始しない場合には、細化挙動の安定性が維持できず、安定した紡糸ができないことがある。 The yarn discharged from the mouthpiece hole is cooled and solidified by air. The temperature of the cooling air may be determined in balance with the cooling air velocity from the viewpoint of cooling efficiency, but is preferably 50 ° C. or less from the viewpoint of fineness uniformity. Further, the cooling gas is allowed to flow in the direction substantially perpendicular to the yarn to cool the yarn. At that time, the speed of the cooling air is preferably 5 m / min or more from the viewpoint of cooling efficiency and fineness uniformity, and preferably 100 m / min or less from the viewpoint of yarn-making stability. Further, it is preferable to start cooling within 20 mm or more and 500 mm or less from the base to cool and solidify. If cooling is started at a distance of less than 20 mm, the surface temperature of the base may drop and the discharge may become unstable. If cooling is not started within 500 mm, the stability of the thinning behavior cannot be maintained and it becomes stable. You may not be able to spin.
口金孔から吐出した糸条は、口金から400mm以上、7,000mm以内の位置で加速した空気流により牽引される。加速空気流は冷却風を吹かせる領域を密閉とし、紡糸線下流に向かうにしたがって、徐々に密閉領域の断面積を小さくすることにより空気流速を加速させるようにしても良いが、より高い空気流速を得るためにはエジェクターを用いることが好ましい。この空気流速によって糸条は加速され、繊維の走行速度である紡糸速度も空気流速と近い速度に到達する。なお紡糸速度は以下の式により算出する値を指す。
紡糸速度(km/分)=Q・10/D
Q:単孔吐出量(g/分)、D:単糸繊度(dtex)
紡糸速度は3.0km/分以上が細繊度、高強度化のためには好ましく、4.0km/分がより好ましい。なお空気流速も同様に3.0km/分以上が好ましい。また紡糸速度の上限は10.0km/分程度である。
The yarn discharged from the mouthpiece hole is towed by an accelerated air flow at a position of 400 mm or more and 7,000 mm or less from the mouthpiece. The accelerating air flow may be made to seal the region where the cooling air is blown, and the air flow velocity may be accelerated by gradually reducing the cross-sectional area of the sealed region toward the downstream of the spinning line, but the air flow velocity may be higher. It is preferable to use an ejector in order to obtain. The yarn is accelerated by this air flow velocity, and the spinning speed, which is the running speed of the fiber, reaches a speed close to the air flow velocity. The spinning speed refers to the value calculated by the following formula.
Spinning speed (km / min) = Q ・ 10 / D
Q: Single hole discharge amount (g / min), D: Single yarn fineness (dtex)
The spinning speed is preferably 3.0 km / min or more for fineness and high strength, and more preferably 4.0 km / min. Similarly, the air flow velocity is preferably 3.0 km / min or more. The upper limit of the spinning speed is about 10.0 km / min.
空気牽引された糸条は、周囲の空気流速を減じるような開繊部を通過することにより開繊し、その後裏面から空気吸引されるネットコンベアーに着地し、捕集される。捕集されたウェブは10〜1200m/分でコンベアー搬送され、その後エンボス、カレンダー加工を行うことでスパンボンド不織布が得られる。 The air-towed yarn is opened by passing through an opening portion that reduces the flow velocity of the surrounding air, and then lands on a net conveyor that is sucked air from the back surface and is collected. The collected web is conveyed by a conveyor at 10 to 1200 m / min, and then embossed and calendered to obtain a spunbonded non-woven fabric.
本願のポリエチレンスパンボンド不織布について、原料、プロセスの面から重要な点を下記する。
一つは密度が0.945〜0.965g/cm3のLLDPEを用いる点である。スパンボンドは溶融紡糸かつ高速紡糸のプロセスになるため、従来から曳糸性に優れるLLDPEを用いる技術が提案されていた。ここで重要になるのが密度、すなわち結晶化度である。発明者らは細繊度かつ高強度のポリエチレンスパンボンド不織布を得るため、吐出した糸条の細化と固化の挙動を調べた結果、HDPEでは結晶化が早いため固化が早く高速紡糸で糸切れする一方で、密度が低いLLDPEでも高速紡糸において糸切れすることが分かった。このためLLDPEの中でも密度が0.945〜0.965g/cm3と高いものを用いることで細繊度かつ糸切れの少ないシートを得ることに成功した。これはHDPEとは異なる分岐成分(オクテン、ヘプテン由来)に起因した伸長粘度特性のため曳糸性が向上し細化が緩やかとなり、かつ結晶性はHDPE同等であるため結晶化に起因する固化も速やかに起こるためと推測している。
Regarding the polyethylene spunbonded non-woven fabric of the present application, important points from the viewpoint of raw materials and processes are described below.
One is to use LLDPE having a density of 0.945 to 0.965 g / cm 3 . Since spunbonding is a process of melt spinning and high speed spinning, a technique using LLDPE having excellent spinnability has been conventionally proposed. What is important here is the density, that is, the degree of crystallinity. In order to obtain a polyethylene spunbonded non-woven fabric with fine fineness and high strength, the inventors investigated the thinning and solidification behavior of the discharged yarn. As a result, HDPE crystallizes quickly, so solidification is fast and yarn breaks at high speed spinning. On the other hand, it was found that even low-density LLDPE yarn breaks in high-speed spinning. Therefore, we succeeded in obtaining a sheet with fine fineness and less thread breakage by using a LLDPE having a high density of 0.945 to 0.965 g / cm 3 . This is due to the extensional viscosity characteristics caused by the branched components (derived from octene and heptene) that are different from HDPE, so that the spinnability is improved and the thinning becomes slower, and the crystallinity is equivalent to HDPE, so solidification due to crystallization also occurs. I presume that it will happen quickly.
もう一点は、3km/分以上の紡糸速度での高速紡糸である。スパンボンドは高速紡糸プロセスであるが、固化した後に繊維を引き伸ばすことはないため、繊維の強度は固化するまでに形成される繊維構造に支配される。このため高強度化には細化完了から固化するまでの間に繊維に高い応力を与え、分子鎖を高配向状態で固定することが重要となる。糸条に高い応力を与える手段としてはスパンボンドにおいては高速紡糸が有効であるが、ポリマー種によっては紡糸線上流(口金に近い場所)での細化が進みやすくなり場合によっては糸切れとなる。本願発明ではLLDPEを用いることで細化を緩やかとし、紡糸線上流での糸切れを防ぐとともに、結晶化に起因する固化までの間で十分な応力を付与して分子鎖を配向させ、かつ十分結晶化することで構造を固定できるため高強度化できると推測している。 Another point is high-speed spinning at a spinning speed of 3 km / min or more. Although spunbonding is a high-speed spinning process, it does not stretch the fibers after solidification, so the strength of the fibers is dominated by the fiber structure formed before solidification. Therefore, in order to increase the strength, it is important to apply high stress to the fibers from the completion of thinning to the solidification and to fix the molecular chains in a highly oriented state. High-speed spinning is effective in spunbonding as a means of applying high stress to the yarn, but depending on the polymer type, thinning tends to proceed upstream of the spinning line (a place near the base), and in some cases yarn breakage occurs. .. In the present invention, the use of LLDPE slows down the thinning, prevents yarn breakage upstream of the spinning line, and applies sufficient stress until solidification due to crystallization to orient the molecular chain and is sufficient. It is speculated that the strength can be increased because the structure can be fixed by crystallization.
このように密度が0.945〜0.965g/cm3のLLDPEと3.0km/分以上を超える高速での空気牽引の組み合わせにより、細繊度のため柔軟性により優れ、高強度であり、加工性に優れるポリエチレンスパンボンド不織布が得られるのである。 In this way, the combination of LLDPE with a density of 0.945 to 0.965 g / cm 3 and air traction at a high speed exceeding 3.0 km / min makes it more flexible due to its fineness, and has high strength and processing. A polyethylene spunbonded non-woven fabric having excellent properties can be obtained.
以下、実施例により本発明をより具体的に説明する。なお実施例中の各特性値は次の方法で求めた。 Hereinafter, the present invention will be described in more detail with reference to Examples. Each characteristic value in the examples was obtained by the following method.
A.繊維直径、単糸繊度
繊維の側面の顕微鏡観察から繊維の直径を求め、1水準につき10回測定を行い、平均値を繊維直径とした。次に繊維を丸断面として扱い、繊維直径から以下の式を用いて単糸繊度を求めた。
単糸繊度(dtex)=π・ρ・d2/400
ρ:樹脂密度(g/cm3)、d:繊維直径(μm) 。
A. Fiber diameter and single yarn fineness The fiber diameter was determined from the microscopic observation of the side surface of the fiber, measured 10 times per level, and the average value was taken as the fiber diameter. Next, the fiber was treated as a round cross section, and the single yarn fineness was determined from the fiber diameter using the following formula.
Single yarn fineness (dtex) = π · ρ · d 2/400
ρ: Resin density (g / cm 3 ), d: Fiber diameter (μm).
B.単糸のΔn
不織布から抜き出した単糸を用い、偏光顕微鏡(OLYMPUS社製BH−2)を用いコンペンセーター法により試料1水準につき3回の測定を行い、平均値として求めた。
B. Single yarn Δn
Using a single yarn extracted from the non-woven fabric, measurement was performed three times per sample level by the compensator method using a polarizing microscope (BH-2 manufactured by OLYMPUS), and the average value was obtained.
C.熱特性
示差走査熱量計(TA Instruments社製DSCQ1000)で窒素下、昇温速度16℃/分の条件で示差走査熱量測定を行い、吸熱ピークの温度を融点(Tm)とし、Tmでの融解熱量をΔHm(J/g)とした。
C. Thermal characteristics Differential scanning calorimetry (DSCQ1000 manufactured by TA Instruments) is used to measure differential scanning calorimetry under nitrogen and at a heating rate of 16 ° C./min. Was ΔHm (J / g).
D.単糸強度
カレンダー加工を行う前のウェッブを採取し、ここから単糸を約50mm引き出し、JIS L1013:2010記載の方法に準じて、試料長20mm、引張速度20mm/分の条件で、(株)オリエンテック社製テンシロンUCT−100を用い1水準当たり10回の測定を行い、平均値を強力(cN)とした。またA.で求めた繊維直径を丸断面と仮定して繊維断面積を求め、強力を繊維断面積で除して単糸強度(MPaとした。
D. Single yarn strength A web before calendering is collected, a single yarn is pulled out from this by about 50 mm, and according to the method described in JIS L1013: 2010, the sample length is 20 mm and the tensile speed is 20 mm / min. Tensilon UCT-100 manufactured by Orientec Co., Ltd. was used to perform measurements 10 times per level, and the average value was set to strong (cN). In addition, A. The fiber cross section was obtained by assuming that the fiber diameter obtained in 1 was a round cross section, and the strength was divided by the fiber cross section to obtain the single yarn strength (MPa).
E.シート欠点
スパンボンド不織布の幅(CD)方向の中心で10cm角の領域をルーペで目視観察し、糸切れに起因して繊維径が平均の繊維直径よりも3倍以上太くなっているもの、また繊維の切れ端が丸くなって平均の繊維直径よりも3倍以上太く見えるものを欠点として扱い、その個数を数えた。この観察を不織布の長手(MD)方向に5回繰り返し、合計の個数をシート欠点数とした。
E. Sheet defects A 10 cm square area at the center of the spunbonded non-woven fabric in the width (CD) direction is visually observed with a loupe, and the fiber diameter is three times or more larger than the average fiber diameter due to thread breakage. Those with rounded pieces of fibers that appeared to be three times thicker than the average fiber diameter were treated as defects, and the number was counted. This observation was repeated 5 times in the longitudinal direction (MD) of the non-woven fabric, and the total number was taken as the number of sheet defects.
F.シート柔軟性
シート触感の官能評価を行い、柔軟性に優れるものを5点、劣るものを1点として絶対評価で点数をつけた。これを10名で行い平均点を柔軟性(点)とした。
F. Sheet flexibility The sensory evaluation of the sheet tactile sensation was performed, and a score was given by absolute evaluation, with 5 points being excellent in flexibility and 1 point being inferior. This was done by 10 people and the average score was defined as flexibility (points).
G.シート加工性
シートをゴム製のニップローラーを用いて20m/分で5分間走行させた。このときのロール付着物、シートの状態を観察し、以下の基準で点数付けを行い加工性(点)とした。
5点:ロールに繊維付着物がなく、シートの毛羽、破れも見られない。
4点:ロールに繊維付着物があるが、シートの毛羽、破れは見られない。
3点:ロールに繊維付着物があり、シートの毛羽もあるが、破れは見られない。
2点:ロールに繊維付着物があり、シートの毛羽もあり、破れがある。
1点:シートの破れによりロールにシートが巻きつく。
G. Sheet workability The sheet was run at 20 m / min for 5 minutes using a rubber nip roller. The state of the roll deposits and the sheet at this time was observed, and points were given according to the following criteria to determine workability (points).
5 points: There are no fiber deposits on the roll, and no fluff or tear of the sheet is seen.
4 points: There are fiber deposits on the roll, but no fluff or tear of the sheet is seen.
3 points: There are fiber deposits on the roll and fluff on the sheet, but no tearing is seen.
2 points: There are fiber deposits on the roll, there is fluff on the sheet, and there is tearing.
1 point: The sheet wraps around the roll due to the tearing of the sheet.
実施例1
密度、MIが表1に記載された値を持つLLDPE樹脂(オクテン共重合比率0.3mol%)を用い、単軸エクストルーダーにて溶融押出しし、ギアーポンプで計量しつつ紡糸口金に樹脂を供給した。紡糸温度(口金温度)は230℃とし、孔径Dが0.30mm、ランド長Lが0.70mmの口金孔をCD方向に600個/m有する口金より、単孔吐出量0.6g/分の条件でポリマーを吐出した。なお、口金孔の直上に位置する導入孔はストレート孔とし、導入孔と口金孔の接続部分はテーパーとしたものを用いた。吐出したポリマーは50mmの保温領域を通過させた後、25℃、40m/分の空気流により糸条の外側から冷却し固化させた。その後、口金から550mmの位置に設置したエジェクターにて加速した空気流で牽引した。エジェクターを通過した糸条はネットコンベアー上に捕集させ、20m/分の速度で搬送した。その後、カレンダー加工を行い18g/m2のポリエチレンスパンボンド不織布を得た。
単糸繊度と単孔吐出量から計算した紡糸速度も表1に示す。紡糸速度は4.0km/分となったが、約10分のテスト中、目立った糸切れは見られず曳糸性は良好であった。
得られたシート特性も表1に示す。表1から分かるようにシート欠点が少なく、単糸繊度が2.0dtex以下と細いため柔軟性に優れ、加工性にも優れることが分かる。
Example 1
Using an LLDPE resin (octene copolymerization ratio 0.3 mol%) having a density and MI values shown in Table 1, melt extrusion was performed with a uniaxial extruder, and the resin was supplied to the spinneret while measuring with a gear pump. .. The spinning temperature (base temperature) is 230 ° C., and the single hole discharge rate is 0.6 g / min from a base having 600 base holes with a hole diameter D of 0.30 mm and a land length L of 0.70 mm in the CD direction. The polymer was discharged under the conditions. The introduction hole located directly above the mouthpiece hole was a straight hole, and the connection portion between the introduction hole and the mouthpiece hole was tapered. The discharged polymer was passed through a heat insulating region of 50 mm, and then cooled and solidified from the outside of the yarn by an air flow at 25 ° C. and 40 m / min. After that, it was towed by an accelerated air flow with an ejector installed at a position 550 mm from the base. The threads that passed through the ejector were collected on a net conveyor and transported at a speed of 20 m / min. Then, calendering was performed to obtain a polyethylene spunbonded non-woven fabric of 18 g / m 2 .
Table 1 also shows the spinning speed calculated from the single yarn fineness and the single hole discharge amount. The spinning speed was 4.0 km / min, but during the test for about 10 minutes, no noticeable yarn breakage was observed and the spinnability was good.
The obtained sheet characteristics are also shown in Table 1. As can be seen from Table 1, there are few sheet defects, and since the single yarn fineness is as thin as 2.0 dtex or less, it is excellent in flexibility and workability.
実施例2、3、比較例1
エジェクターでの牽引速度を変更し紡糸速度を変化させた以外は実施例1と同様の条件でテストを行い、ポリエチレンスパンボンド不織布を得た。
単糸繊度と単孔吐出量から計算した紡糸速度を表1に示す。紡糸速度が5.0km/分の実施例2は10分のテスト中、目立った糸切れは見られず曳糸性は良好であった。
得られたシート特性を表1に示す。比較例1では単糸繊度が2.5dtexのため柔軟性に劣り、かつΔnが小さいため単糸強度が低く、加工性にも劣る。実施例2、3では単糸繊度が小さいため柔軟性に優れ、シート欠点が少なく、単糸強度も高く加工性に優れることが分かる。
Examples 2, 3 and Comparative Example 1
The test was carried out under the same conditions as in Example 1 except that the traction speed at the ejector was changed to change the spinning speed, and a polyethylene spunbonded non-woven fabric was obtained.
Table 1 shows the spinning speed calculated from the single yarn fineness and the single hole discharge amount. In Example 2 having a spinning speed of 5.0 km / min, no noticeable yarn breakage was observed during the 10-minute test, and the spinnability was good.
The obtained sheet characteristics are shown in Table 1. In Comparative Example 1, since the single yarn fineness is 2.5 dtex, the flexibility is inferior, and since Δn is small, the single yarn strength is low and the workability is also inferior. It can be seen that in Examples 2 and 3, since the single yarn fineness is small, the flexibility is excellent, there are few sheet defects, the single yarn strength is high, and the workability is excellent.
比較例2、3
PEを表1のように変更した以外は実施例1と同様の条件でテストを行った。いずれも糸切れが多発しシートが得られなかったため、表1の紡糸速度とすることでポリエチレンスパンボンド不織布を得た。
得られたシート特性も表1に示す。比較例2は単糸繊度が2.5dtexのため柔軟性に劣り、かつΔnが小さいため単糸強度が低く、シート欠点も多いため加工性に劣る。比較例3も同様にシート欠点が多いため加工性に劣ることが分かる。
Comparative Examples 2, 3
The test was carried out under the same conditions as in Example 1 except that the PE was changed as shown in Table 1. In each case, thread breakage occurred frequently and a sheet could not be obtained. Therefore, a polyethylene spunbonded non-woven fabric was obtained by using the spinning speeds shown in Table 1.
The obtained sheet characteristics are also shown in Table 1. In Comparative Example 2, since the single yarn fineness is 2.5 dtex, the flexibility is inferior, and since Δn is small, the single yarn strength is low, and there are many sheet defects, so that the workability is inferior. It can be seen that Comparative Example 3 is also inferior in workability because it has many sheet defects.
Claims (1)
It is made of linear low-density polyethylene with a density of 0.945 to 0.965 g / cm 3 , a single yarn fineness of 0.5 dtex or more and 2.0 dtex or less, and a single yarn Δn of 0.035 or more and 0.038. A polyethylene spunbonded non-woven fabric characterized by the following .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2016194239A JP6753254B2 (en) | 2016-09-30 | 2016-09-30 | Polyethylene spunbonded non-woven fabric |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
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| JP2016194239A JP6753254B2 (en) | 2016-09-30 | 2016-09-30 | Polyethylene spunbonded non-woven fabric |
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