JP6898482B2 - Single-layer or multi-layer polyester long-fiber non-woven fabric and food filters using it - Google Patents

Single-layer or multi-layer polyester long-fiber non-woven fabric and food filters using it Download PDF

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JP6898482B2
JP6898482B2 JP2020018048A JP2020018048A JP6898482B2 JP 6898482 B2 JP6898482 B2 JP 6898482B2 JP 2020018048 A JP2020018048 A JP 2020018048A JP 2020018048 A JP2020018048 A JP 2020018048A JP 6898482 B2 JP6898482 B2 JP 6898482B2
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woven fabric
layer
polyester long
fiber non
polyester
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JP2020073751A (en
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山田 裕介
裕介 山田
留美名 小尾
留美名 小尾
一史 加藤
一史 加藤
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Asahi Kasei Corp
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    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/005Synthetic yarns or filaments
    • D04H3/009Condensation or reaction polymers
    • D04H3/011Polyesters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1607Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
    • B01D39/1623Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
    • B01D39/163Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin sintered or bonded
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D77/00Packages formed by enclosing articles or materials in preformed containers, e.g. boxes, cartons, sacks or bags
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/14Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic yarns or filaments produced by welding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/04Additives and treatments of the filtering material
    • B01D2239/0407Additives and treatments of the filtering material comprising particulate additives, e.g. adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/065More than one layer present in the filtering material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12Special parameters characterising the filtering material
    • B01D2239/1241Particle diameter
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W90/00Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
    • Y02W90/10Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics

Description

本発明は、透明性、寸法安定性、粉漏れ性、及び成分抽出性に優れた単層又は複層ポリエステル長繊維不織布、並びにこれを用いた飲料向け抽出用の食品用フィルターに関する。 The present invention relates to a single-layer or multi-layer polyester long-fiber non-woven fabric having excellent transparency, dimensional stability, powder leakage property, and component extractability, and a food filter for beverage extraction using the non-woven fabric.

従来、包装材料として、ポリエチレン、ポリプロピレン、ポリエステル、ポリアミド等の樹脂からなる不織布が使用されている。しかしながら、一般的に不織布のフィルター性等の遮蔽機能を活用するために繊維を緻密にすることが要求され、内部を確認することができない。また、紅茶、緑茶、烏龍茶等の成分抽出を行う場合、簡便な方法としてティーバッグ方式が多く利用されている。ティーバッグ用途に使用されている包装材料には一般に紙が多く用いられているが、透明性が悪くて包装材料の中身が見えないこと、ヒートシール加工できない等の問題点がある。 Conventionally, a non-woven fabric made of a resin such as polyethylene, polypropylene, polyester, or polyamide has been used as a packaging material. However, in general, it is required to make the fibers dense in order to utilize the shielding function such as the filter property of the non-woven fabric, and the inside cannot be confirmed. Further, when extracting components of black tea, green tea, oolong tea, etc., the tea bag method is often used as a simple method. Paper is generally used as a packaging material used for tea bags, but there are problems such as poor transparency, invisible contents of the packaging material, and inability to heat-seal.

以下の特許文献1には、透明性を改良したティーバッグ用不織布が開示されているが、寸法安定性に関する記載は無く、特に留意されたものではない。更に、粉洩れに対する評価としてバブルポイント法(JIS-K-3832)により測定される最大孔径が用いられているが、測定に適した孔径範囲はナノからマイクロメートルオーダーであり、かつ、圧力を換算して孔径を表現しているため、実際に使用される茶葉に対して適した評価手法ではない。
また、以下の特許文献2には、ポリL乳酸からなる繊度が15〜35dtexのティーバッグ用生分解性モノフィラメントが開示されているが、繊度が大きいために透明性は高いが、モノフィラメントの沸水収縮率が20%以下であり、寸法安定性が低いという問題点がある。
さらに、以下の特許文献3には、ポリオレフィン系重合体を鞘成分とし、前記鞘成分よりも融点の高いポリエステル系重合体を芯成分とする芯鞘型の複合長繊維からなるヒートシール性に優れた不織布が開示されているが、寸法安定性が低く、また、透明性に関する記載は無く、特に留意されたものではない。
The following Patent Document 1 discloses a non-woven fabric for tea bags with improved transparency, but there is no description regarding dimensional stability, and no particular attention has been paid to it. Furthermore, the maximum pore diameter measured by the bubble point method (JIS-K-3832) is used as an evaluation for powder leakage, but the pore diameter range suitable for measurement is on the order of nanometers to micrometers, and the pressure is converted. Since the pore size is expressed, it is not a suitable evaluation method for tea leaves that are actually used.
Further, Patent Document 2 below discloses a biodegradable monofilament for tea bags made of poly-Llactic acid and having a fineness of 15 to 35 dtex. Although the monofilament is highly transparent due to its high fineness, the monofilament shrinks in boiling water. There is a problem that the rate is 20% or less and the dimensional stability is low.
Further, in Patent Document 3 below, a core-sheath type composite long fiber having a polyolefin-based polymer as a sheath component and a polyester-based polymer having a higher melting point than the sheath component as a core component is excellent in heat-sealing property. Although the non-woven fabric is disclosed, it has low dimensional stability and there is no description about transparency, so that no particular attention has been paid to it.

特許第3939326号公報Japanese Patent No. 3939326 特開2001−131826号公報Japanese Unexamined Patent Publication No. 2001-131826 特開平11−43855号公報Japanese Unexamined Patent Publication No. 11-43855

本発明は、前記従来技術の問題に鑑み、透明性、寸法安定性、粉漏れ性、及び成分抽出性に優れたポリエステル長繊維不織布、並びにこれを用いた食品用フィルターを提供することである。 In view of the above-mentioned problems of the prior art, the present invention provides a polyester long-fiber non-woven fabric having excellent transparency, dimensional stability, powder leakage property, and component extractability, and a food filter using the same.

本発明者らは、上記の課題を解決すべく鋭意検討し実験を重ねた結果、特定範囲のチタン元素含有量を有するポリエステル系樹脂を選定し、不織布を構成する繊維の構造と繊径、目付、熱圧着面積率の観点から詳細な検討を行い、紡糸性が良好で食品用フィルターとして成分抽出性に優れ、且つ、透明性と寸法安定性の両方が良好である不織布が得られることを見出した。更に粉漏れ性の評価として不織布を直接観察することで算出される孔径を用いて定義することで、本発明を完成するに至ったものである。 As a result of diligent studies and experiments to solve the above problems, the present inventors have selected a polyester resin having a titanium element content in a specific range, and selected a polyester-based resin, and the structure, fiber diameter, and grain size of the fibers constituting the non-woven fabric. A detailed study was conducted from the viewpoint of the heat-bonded area ratio, and it was found that a non-woven fabric having good spinnability, excellent component extractability as a food filter, and good both transparency and dimensional stability can be obtained. It was. Furthermore, the present invention has been completed by defining the pore size calculated by directly observing the non-woven fabric as an evaluation of powder leakage.

すなわち、本発明は以下の通りのものである。
[1]無機系粒子の含有量が0〜100ppmであり、10%点孔径が1000μm未満であり、10%点孔径と2.3%点孔径の差が500以下であり、目付が10〜30g/m2であり、かつ、不織布の面積当たりの表面積が、1.0〜3.25m 2 /m 2 であることを特徴とする、単層又は複層ポリエステル長繊維不織布。
[2]熱圧着面積率が5〜40%であり、且つ、平均見掛け密度が0.1〜0.5g/cm3である、前記[1]に記載の単層又は複層ポリエステル長繊維不織布。
[3]平均繊維径が1340μmである、前記[1]又は[2]に記載の単層又は複層ポリエステル長繊維不織布。
[4]少なくとも1層がラマンスペクトルにおいて観測される1740cm-1付近のC=O基によるピーク巾の半値全幅の平均値が18〜24cm-1の繊維で構成される、前記[1]〜[3]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[5]少なくとも1層が結晶化度が30〜50%である繊維から構成される、前記[1]〜[4]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[6]少なくとも1層が、複屈折率0.04〜0.12の繊維で構成される、前記[1]〜[5]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[7]透明性が65%以上である、前記[1]〜[6]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[8]沸水収縮率が2.0%以下である、前記[1]〜[7]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[9]地合係数が0.5〜2.0である、前記[1]〜[8]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[10]少なくとも1層の引張強度が5N/30mm以上である、前記[1]〜[9]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[11]少なくとも1層が融点240℃以下の低融点繊維を含有する、前記[1]〜[10]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[12]下記a層とb層を熱圧着により一体化された積層不織布からなる、前記[1]〜[11]のいずれかに記載のポリエステル長繊維不織布。
a層:高融点樹脂と融点差が30℃〜150℃の低融点樹脂からなるポリエステル長繊維不織布
b層:前記高融点樹脂からなるポリエステル長繊維不織布
[13]前記ポリエステル長繊維不織布の繊維の配向性が断面方向に異なる構造をもつ、前記[1]〜[12]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[14]少なくとも1層がイソフタル酸を0〜25%含む樹脂からなる、前記[1]〜[13]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[15]前記無機系粒子が酸化チタンである、前記[1]〜[14]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[16]チタン元素含有量0〜0.1ppmの樹脂からなる、前記[15]に記載の単層又は複層ポリエステル長繊維不織布。
[17]不織布とした後の樹脂のIV値が0.6以上である、前記[1]〜[16]のいずれかに記載の単層又は複層ポリエステル長繊維不織布。
[18]前記[1]〜[17]のいずれかに記載の単層又は複層ポリエステル長繊維不織布からなる食品用フィルター。
That is, the present invention is as follows.
[1] The content of inorganic particles is 0 to 100 ppm, the 10% point pore size is less than 1000 μm, the difference between the 10% point hole diameter and the 2.3% point hole diameter is 500 or less, and the grain size is 10 to 30 g / m. 2 der is, and the surface area per area of the nonwoven fabric is characterized in that it is a 1.0~3.25m 2 / m 2, a single-layer or multi-layer polyester long fiber nonwoven fabric.
[2] The single-layer or multi-layer polyester long-fiber non-woven fabric according to the above [1], wherein the thermocompression bonding area ratio is 5 to 40% and the average apparent density is 0.1 to 0.5 g / cm 3.
[3] The average fiber diameter of 13 ~ 40 μ m, the [1] or single layer or multi-layer polyester filament nonwoven fabric according to [2].
[4] The average value of the full width at half maximum of the peak width at least one layer according to C = O groups in the vicinity of 1740 cm -1 observed in the Raman spectra is constituted by fibers of 18~24cm -1, the [1] to [ 3] The single-layer or multi-layer polyester long fiber non-woven fabric according to any one of.
[5] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [4] above, wherein at least one layer is composed of fibers having a crystallinity of 30 to 50%.
[6] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [5] above, wherein at least one layer is composed of fibers having a birefringence of 0.04 to 0.12.
[7] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [6] above, which has a transparency of 65% or more.
[8] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [7] above, wherein the boiling water shrinkage rate is 2.0% or less.
[9] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of the above [1] to [8], which has a formation coefficient of 0.5 to 2.0.
[10] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [9] above, wherein the tensile strength of at least one layer is 5 N / 30 mm or more.
[11] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [10] above, wherein at least one layer contains low melting point fibers having a melting point of 240 ° C. or lower.
[12] The polyester long-fiber non-woven fabric according to any one of [1] to [11] above, which comprises a laminated non-woven fabric in which the following a layer and b layer are integrated by thermocompression bonding.
Layer a: Polyester long-fiber non-woven fabric made of a high-melting point resin and a low-melting point resin with a melting point difference of 30 ° C to 150 ° C.
Layer b: Polyester long-fiber non-woven fabric made of the refractory resin
[13] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [12], which has a structure in which the orientation of the fibers of the polyester long-fiber non-woven fabric is different in the cross-sectional direction.
[14] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [13] above, wherein at least one layer is made of a resin containing 0 to 25% isophthalic acid.
[15] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [14] above, wherein the inorganic particles are titanium oxide.
[16] The single-layer or multi-layer polyester long-fiber non-woven fabric according to the above [15], which comprises a resin having a titanium element content of 0 to 0.1 ppm.
[17] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of [1] to [16] above, wherein the IV value of the resin after being made into a non-woven fabric is 0.6 or more.
[18] A food filter made of the single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of the above [1] to [17].

本発明に係る単層又は複層ポリエステル長繊維不織布を構成する繊維の紡糸性は良好であり、該繊維からなる不織布を用いて製造した食品用フィルターは、成分抽出性に優れ、透明性、寸法安定性、更には耐粉漏れ性も良好である。 The spinnability of the fibers constituting the single-layer or multi-layer polyester long-fiber non-woven fabric according to the present invention is good, and the food filter produced by using the non-woven fabric made of the fibers has excellent component extractability, transparency, and dimensions. It has good stability and powder leakage resistance.

板状の分散板等のような気流を制御する装置の一例を示す概略図である。It is a schematic diagram which shows an example of the device which controls the air flow, such as a plate-shaped dispersion plate. 沸水収縮率と透明性との関係を示すグラフである。It is a graph which shows the relationship between the boiling water shrinkage rate and transparency. ドラフト比と配向結晶性との関係を示すグラフである。It is a graph which shows the relationship between the draft ratio and the orientation crystallinity. 紡糸温度と配向結晶性との関係を示すグラフである。It is a graph which shows the relationship between a spinning temperature and orientation crystallinity. 樹脂IV値と配向結晶性との関係を示すグラフである。It is a graph which shows the relationship between a resin IV value and orientation crystallinity.

以下、本発明の実施形態について詳細に説明する。
本実施形態のポリエステル長繊維不織布を構成するポリエステル長繊維を構成するポリエステル系樹脂としては、熱可塑性ポリエステルとして、ポリエチレンテレフタレート、ポリブチレンテレフタレートやポリトリメチレンテレフタレートが代表例として挙げられるが、エステルを形成する酸成分としてイソフタル酸やフタル酸等が重合又は共重合されたポリエステルであってもよい。熱可塑性ポリエステルは、更には、生分解性を有する樹脂、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)、又はこれらを主たる繰り返しの単位要素とする共重合体であってもよい。これらの樹脂は、単独で用いてもよく又は2種以上を組み合わせてもよい。
Hereinafter, embodiments of the present invention will be described in detail.
Typical examples of the polyester-based resin constituting the polyester filaments constituting the polyester filamentous fibers of the present embodiment include polyethylene terephthalate, polybutylene terephthalate, and polytrimethylene terephthalate as thermoplastic polyesters, which form an ester. Polyester may be a polyester obtained by polymerizing or copolymerizing isophthalic acid, phthalic acid, or the like as an acid component. The thermoplastic polyester is further a biodegradable resin, for example, a poly (α-hydroxy acid) such as polyglycolic acid or polylactic acid, or a copolymer containing these as a main repeating unit element. May be good. These resins may be used alone or in combination of two or more.

本実施形態のポリエステル長繊維不織布は、透明性が高い(隠蔽性が低い) 程好ましいので、熱可塑性合成繊維不織布に通常艶消し剤として用いられる無機系粒子の含有率は低い程好ましい。
艶消し剤として用いられる無機粒子としては、合成品及び天然産物のいずれでも、特に限定なく用いることができる。無機粒子としては、例えば、アルミナ、シリカ、チタニア、ジルコニア、マグネシア、セリア、イットリア、酸化亜鉛及び酸化鉄などの酸化物系セラミックス、窒化ケイ素、窒化チタン及び窒化ホウ素等の窒化物系セラミックス、シリコンカーバイド、炭酸カルシウム、硫酸アルミニウム、水酸化アルミニウム、水酸化マグネシウム、チタン酸カリウム、タルク、カオリンクレー、カオリナイト、ディカイト、ナクライト、ハロイサイト、パイロフィライト、オーディナイト、モンモリロナイト、バイデライト、ノントロナイト、ボルコンスコアイト、サポナイト、ソーコナイト、スインホルダイト、バーミキュライト、バーチェリン、セリサイト、アメサイト、ケリアイト、フレイポナイト、ブリンドリアイト、ベントナイト、ゼオライト、黒雲母、金雲母、鉄雲母、イーストナイト、シデロフィライトテトラフェリ鉄雲母、鱗雲母、ポリリシオナイト、白雲母、セラドン石、鉄セラドン石、鉄アルミノセラドン石、ケイ酸カルシウム、ケイ酸マグネシウム、ケイ藻土及びケイ砂等の、セラミックス及びガラス繊維が挙げられる。これらの無機粒子は、1種を単独で又は2種以上を組み合わせて用いられる。樹脂への反応活性の観点から、用いる無機粒子は酸化チタン、ステアリン酸マグネシウム、ステアリン酸カルシウム等の不活性無機粒子が好ましい。
Since the polyester long-fiber non-woven fabric of the present embodiment is preferable as having high transparency (low hiding property), it is preferable that the content of inorganic particles usually used as a matting agent in the thermoplastic synthetic fiber non-woven fabric is low.
As the inorganic particles used as the matting agent, either synthetic products or natural products can be used without particular limitation. Examples of the inorganic particles include oxide-based ceramics such as alumina, silica, titania, zirconia, magnesia, ceria, itria, zinc oxide and iron oxide, nitride-based ceramics such as silicon nitride, titanium nitride and boron nitride, and silicon carbide. , Calcium carbonate, aluminum sulfate, aluminum hydroxide, magnesium hydroxide, potassium titanate, talc, kaolin clay, kaolinite, dikite, nacrite, haloysite, pyrophyllite, audinite, montmorillonite, biderite, nontronite, volcon score Ito, saponite, saconite, sineholdite, vermiculite, ceramicin, sericite, amesite, kaolinite, frayponite, brindriaite, bentonite, zeolite, black mica, gold mica, iron mica, yeast night, siderophyllite tetra Examples include ceramics and glass fibers such as ferri iron mica, scale mica, polylysionite, muscovite, celadon stone, iron celadon stone, iron aluminoceradon stone, calcium silicate, magnesium silicate, diatomaceous earth and silica sand. .. These inorganic particles may be used alone or in combination of two or more. From the viewpoint of the reaction activity to the resin, the inorganic particles used are preferably inert inorganic particles such as titanium oxide, magnesium stearate, and calcium stearate.

本実施形態のポリエステル長繊維を構成するポリエステル系樹脂の無機系粒子の好適な粒子径の範囲は1.0μm以下であり、好ましくは0.8μm以下、より好ましくは0.7μm以下である。粒子径が1.0μmを超えると、不織布として透明性が低くなるだけではなく、紡糸の安定性も悪くなるため、糸切れなどの紡糸欠点も増加する。 The range of preferable particle size of the inorganic particles of the polyester resin constituting the polyester filaments of the present embodiment is 1.0 μm or less, preferably 0.8 μm or less, and more preferably 0.7 μm or less. When the particle size exceeds 1.0 μm, not only the transparency of the non-woven fabric is lowered, but also the stability of spinning is deteriorated, so that spinning defects such as yarn breakage increase.

本実施形態のポリエステル長繊維を構成するポリエステル系樹脂に無機系粒子の好適な含有量は0〜100ppmであり、好ましくは0〜50ppmであり、より好ましくは0〜0.1ppmである。繊維中の無機粒子の含有量を上記の範囲内とすることで、不織布の透明性を十分に確保することが可能となる。さらに、無機系粒子を触媒として用いた場合、上記の範囲内とすることで、溶融押出時の樹脂の分解反応が抑制され、糸切れなどの紡糸欠点を抑制することができる。 The preferable content of the inorganic particles in the polyester resin constituting the polyester filaments of the present embodiment is 0 to 100 ppm, preferably 0 to 50 ppm, and more preferably 0 to 0.1 ppm. By setting the content of the inorganic particles in the fiber within the above range, it is possible to sufficiently secure the transparency of the non-woven fabric. Further, when inorganic particles are used as a catalyst, the decomposition reaction of the resin at the time of melt extrusion is suppressed and spinning defects such as yarn breakage can be suppressed by setting the particles within the above range.

本実施形態のポリエステル長繊維を構成するポリエステル系樹脂に艶消し剤として用いる無機系粒子としては、安価で汎用的であることから、反応活性を失活させた酸化チタンなどのチタン系粒子を用いることが好ましい。本実施形態のポリエステル長繊維を構成するポリエステル系樹脂に無機系粒子としてチタン元素を用いる場合、好適な含有量は0〜100ppmであり、好ましくは0〜50ppmであり、より好ましくは0〜0.1ppmである。
具体的には、艶消し剤として用いる二酸化チタン等の無機系不活性粒子の添加をしない無色透明であるスーパーブライト樹脂、更にはチタン化合物を触媒として用いていない樹脂であることが好ましい。チタン化合物を触媒として用いないことにより、溶融押出時の樹脂の分解反応が抑制され、糸切れなどの紡糸欠点を抑制することができる。
As the inorganic particles used as a matting agent for the polyester resin constituting the polyester filaments of the present embodiment, titanium-based particles such as titanium oxide whose reaction activity has been deactivated are used because they are inexpensive and versatile. Is preferable. When titanium element is used as the inorganic particles in the polyester resin constituting the polyester filament of the present embodiment, the preferable content is 0 to 100 ppm, preferably 0 to 50 ppm, and more preferably 0 to 0.1 ppm. Is.
Specifically, it is preferable that the super bright resin is colorless and transparent without the addition of inorganic inert particles such as titanium dioxide used as a matting agent, and further is a resin that does not use a titanium compound as a catalyst. By not using the titanium compound as a catalyst, the decomposition reaction of the resin at the time of melt extrusion is suppressed, and spinning defects such as yarn breakage can be suppressed.

本実施形態のポリエステル長繊維不織布を包装材とした際の内包物の漏れ性は孔径の分布により定義できる。
孔径の代表値は、不織布画像中の各孔の面積について、最大面積から小さい面積に順に積算した際の面積率10%点での孔径で表現することができ、1000μm以下である必要がある。好ましい範囲は30μ以上6000μm以下、より好ましい範囲は400μm以下、更に好ましい範囲は300μm以下、最も好ましくは250μm以下である。この範囲以上では布帛の目が粗くなるため、内包物の粉漏れを抑止できなくなる。他方、この範囲以下では布帛の目が細かくなるため、フィルターの透明性が低くなる。また、フィルターの流体抵抗が上がる為、食品用フィルターとして用いた時に抽出時間が多くなり、実用的ではない。
The leakability of inclusions when the polyester long fiber non-woven fabric of the present embodiment is used as a packaging material can be defined by the distribution of pore diameters.
The representative value of the pore diameter can be expressed by the pore diameter at an area ratio of 10% when the area of each pore in the non-woven fabric image is integrated in order from the maximum area to the smaller area, and must be 1000 μm or less. The preferred range is 30 μm or more and 6000 μm or less, the more preferable range is 400 μm or less, the more preferable range is 300 μm or less, and the most preferable is 250 μm or less. Above this range, the texture of the fabric becomes coarse, and it becomes impossible to prevent powder leakage from the inclusions. On the other hand, below this range, the fineness of the fabric becomes fine, so that the transparency of the filter becomes low. In addition, since the fluid resistance of the filter increases, the extraction time increases when it is used as a food filter, which is not practical.

径の大きな孔径分布を最大孔径から積算した際の2.3%と10%点の差は0μm以上500μm以下である必要がある。好ましい範囲は300μm以下、より好ましい範囲は200μm以下、更に好ましい範囲は150μm以下である。不織布の様な孔径分布の大きい布帛の場合、径の大きな孔の頻度をこの範囲内とすることで、粉漏れ性の優れた不織布とすることができる。更に、前記10%孔径の範囲と併せることで、茶葉を包装するために最適な孔径分布を定義することができる。 The difference between the 2.3% and 10% points when the large-diameter pore diameter distribution is integrated from the maximum pore diameter must be 0 μm or more and 500 μm or less. The preferred range is 300 μm or less, the more preferred range is 200 μm or less, and the more preferred range is 150 μm or less. In the case of a fabric having a large pore diameter distribution such as a non-woven fabric, a non-woven fabric having excellent powder leakage property can be obtained by setting the frequency of holes having a large diameter within this range. Furthermore, by combining with the above range of 10% pore size, the optimum pore size distribution for packaging tea leaves can be defined.

また、同じ孔面積の孔の場合、形状は真円より楕円の様に長い径と短い径が存在する方が好ましい。茶葉等の内容物を包装する場合、表面が滑らかな真球ではないので同じ孔面積であっても長い径と短い径が存在する孔の場合は孔周辺に茶葉がひっかかり、漏れにくくなる。特に、茶葉等の漏れに影響が大きいのは、該不織布に含まれる比較的大きな孔の形状である。この孔の形状は、2.3%孔径から10%孔径までの孔の長径の平均を、2.3%孔径から10%孔径までの孔径の平均で割った値で示すことができる。該値が、1.3以上であることが好ましい。一般的に樹脂の透明性が同一であれば、透明性を保ちながら内容物の漏れを抑制しようとすると、トレードオフの関係にあり、透明性は一定面積内に含まれる繊維表面積、すなわち繊維径が細く目付が大きいほど悪くなるが、内容物の漏れ性は小さくなる。この関係より透明性を確保しながら内容物の漏れ性を抑制する一つの方法は、不織布に含まれる大孔径を少なくすることであり、もう一つの方法は孔の形状を内容物の漏れにくい形にすることである。この二つの方法を併せ持つことで、より透明性と内容物の漏れ性抑制の両方を満たす不織布を得ることができる。 Further, in the case of holes having the same hole area, it is preferable that the shape has a long diameter and a short diameter like an ellipse rather than a perfect circle. When packaging contents such as tea leaves, the surface is not a smooth sphere, so even if the hole area is the same, if the holes have a long diameter and a short diameter, the tea leaves will be caught around the holes and will not leak easily. In particular, it is the shape of the relatively large pores contained in the non-woven fabric that has a great influence on the leakage of tea leaves and the like. The shape of this hole can be shown by dividing the average of the major diameters of the holes from 2.3% hole diameter to 10% hole diameter by the average of the hole diameters from 2.3% hole diameter to 10% hole diameter. The value is preferably 1.3 or more. Generally, if the transparency of the resin is the same, there is a trade-off relationship when trying to suppress leakage of the contents while maintaining the transparency, and the transparency is the fiber surface area included in a certain area, that is, the fiber diameter. The finer the grain and the larger the texture, the worse it becomes, but the leakability of the contents becomes smaller. From this relationship, one method of suppressing the leakage of the contents while ensuring transparency is to reduce the large pore diameter contained in the non-woven fabric, and the other method is to make the shape of the holes less leaky. Is to do. By combining these two methods, it is possible to obtain a non-woven fabric that is more transparent and suppresses leakage of the contents.

本実施形態のポリエステル長繊維の形状は、通常の丸断面の他にも中空断面、芯鞘型複合断面、分割型複合断面、扁平断面等、その目的と用途に応じて任意の繊維断面形状を選択することができる。
本実施形態のポリエステル長繊維不織布は、ティーバッグ等の袋形状にして用いるために、製袋機によるヒートシール加工で接着強度が高いことが好ましい。接着強度の良好なヒートシール性を得るためには、ポリエステル長繊維不織布の少なくとも一方の面に、融点240℃以下の低融点樹脂を含む繊維を積層して、融点差を設けることにより、ヒートシール加工時に低融点樹脂成分だけが軟化又は溶融して接着剤として機能し、高いヒートシール強度を効果的に得ることができる。
The shape of the polyester filament of the present embodiment may be any fiber cross-section shape depending on the purpose and application, such as a hollow cross section, a core-sheath type composite cross section, a split type composite cross section, and a flat cross section, in addition to the normal round cross section. You can choose.
Since the polyester long fiber non-woven fabric of the present embodiment is used in the shape of a tea bag or the like, it is preferable that the polyester long-fiber non-woven fabric has high adhesive strength by heat-sealing with a bag making machine. In order to obtain heat-sealing properties with good adhesive strength, fibers containing a low melting point resin having a melting point of 240 ° C. or less are laminated on at least one surface of the polyester long-fiber non-woven fabric to provide a heat sealing difference. During processing, only the low melting point resin component softens or melts and functions as an adhesive, so that high heat seal strength can be effectively obtained.

前記低融点樹脂の融点は、高融点樹脂の融点よりも30〜150℃低温であり、好ましくは30〜100℃低温である。低融点樹脂としては、例えば、テレフタル酸、イソフタル酸、フタル酸、ナフタリンジカルボン酸等の芳香族ジカルボン酸と、エチレングリコール、ジエチレングリコール、1,4−ブタンジオール、シクロヘキサンジメタノール等のジオールとが重合された共重合ポリエステル系樹脂やポリ乳酸などの脂肪族ポリエステル系樹脂等が挙げられる。さらに、繊維構造として単成分の他に、鞘芯構造やサイドバイサイド等の2成分からなる複合繊維構造、例えば、芯が高融点で鞘が低融点の複合繊維構造であり、具体的には、芯がポリエチレンテレフタレートやポリブチレンテレフタレート等の高融点樹脂、鞘が共重合ポリエステルや脂肪族ポリエステル等の低融点樹脂が好ましい。低融点繊維を積層する方法は、例えば、前記樹脂を融解させて、半溶融状態の樹脂又はその繊維状物を不織布に塗布するカーテンスプレー方式、融解した樹脂をノズルより吐出させて不織布に塗布するコーティング方式、または、高融点繊維ウェブと低融点繊維ウェブを積層してから、熱ロール等で接合して積層不織布を得る方法等が挙げられる。 The melting point of the low melting point resin is 30 to 150 ° C. lower than the melting point of the high melting point resin, preferably 30 to 100 ° C. lower. As the low melting point resin, for example, aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, phthalic acid and naphthalindicarboxylic acid are polymerized with diols such as ethylene glycol, diethylene glycol, 1,4-butanediol and cyclohexanedimethanol. Examples thereof include copolymerized polyester resins and aliphatic polyester resins such as polylactic acid. Further, the fiber structure is a composite fiber structure composed of two components such as a sheath core structure and side-by-side in addition to a single component, for example, a composite fiber structure having a core having a high melting point and a sheath having a low melting point. However, a high melting point resin such as polyethylene terephthalate or polybutylene terephthalate, and a low melting point resin having a sheath such as a copolymerized polyester or an aliphatic polyester are preferable. The method of laminating the low melting point fibers is, for example, a curtain spray method in which the resin is melted and a semi-melted resin or a fibrous material thereof is applied to the non-woven fabric, or the melted resin is discharged from a nozzle and applied to the non-woven fabric. Examples thereof include a coating method, a method of laminating a high melting point fiber web and a low melting point fiber web, and then joining them with a hot roll or the like to obtain a laminated non-woven fabric.

低融点樹脂は、例えば、テレフタル酸を主たる芳香族ジカルボン酸を成分とした際に、イソフタル酸、フタル酸、ナフタリンジカルボン酸等の第2種の芳香族ジカルボン酸を共重合して用いられる。この際の全芳香族ジカルボン酸に対する第二種の芳香族ジカルボン酸の量は0〜25%、好ましくは0〜22%、より好ましくは0〜18%である。この範囲を超えた量を添加すると、結晶性低くなり、更に延伸による分子配向が起こらなくなるため、紡糸安定性や不織布にした際の機械的強度や寸法安定性が低くなる。 The low melting point resin is used, for example, when a main aromatic dicarboxylic acid containing terephthalic acid is used as a component, a second type aromatic dicarboxylic acid such as isophthalic acid, phthalic acid, and naphthalindicarboxylic acid is copolymerized. At this time, the amount of the second type aromatic dicarboxylic acid with respect to the total aromatic dicarboxylic acid is 0 to 25%, preferably 0 to 22%, and more preferably 0 to 18%. If an amount exceeding this range is added, the crystallinity will be lowered, and the molecular orientation due to stretching will not occur, so that the spinning stability and the mechanical strength and dimensional stability of the non-woven fabric will be lowered.

本実施形態のポリエステル長繊維不織布は、超音波溶断、又はヒートシールできることが好ましい。シール強度は、0.1N/30mm以上が好ましく、より好ましくは0.2N/30mm以上である。ヒートシール条件は適宜選択することができ、例えば、ヒートシールの温度条件は、シール面の樹脂の融点から5〜80℃低温であることが好ましい。
さらに、所望の効果を損なわない範囲で他の常用の各種添加成分、例えば、各種エラストマー類等の衝撃性改良剤、結晶核剤、着色防止剤、酸化防止剤、熱安定剤、可塑剤、滑剤、耐候剤、抗菌剤、着色剤、顔料、染料等の添加剤を添加することができる。
The polyester long fiber non-woven fabric of the present embodiment is preferably capable of ultrasonic fusing or heat sealing. The seal strength is preferably 0.1 N / 30 mm or more, more preferably 0.2 N / 30 mm or more. The heat-sealing conditions can be appropriately selected. For example, the heat-sealing temperature conditions are preferably 5 to 80 ° C. lower than the melting point of the resin on the sealing surface.
Further, various other commonly used additive components, for example, impact improving agents such as various elastomers, crystal nucleating agents, anticoloring agents, antioxidants, heat stabilizers, plasticizers, lubricants, as long as the desired effects are not impaired. , Weatherproofing agents, antibacterial agents, colorants, pigments, dyes and other additives can be added.

本実施形態のポリエステル長繊維不織布は、スパンボンド法にて効率よく製造することができる。すなわち、前記のポリエステル系樹脂を加熱溶融して紡糸口金から吐出させ、得られた紡出糸条を公知の冷却装置を用いて冷却し、エアーサッカー等の吸引装置にて牽引細化する。引き続き、吸引装置から排出された糸条群を開繊させた後、コンベア上に堆積させてウェブとする。次いで、このコンベア上に形成されたウェブに加熱されたエンボスロール等の部分熱圧着装置を用いて部分的に熱圧着を施すことにより、長繊維スパンボンド不織布が得られる。 The polyester long fiber non-woven fabric of the present embodiment can be efficiently produced by the spunbond method. That is, the polyester-based resin is heated and melted and discharged from the spinneret, the obtained spun yarn is cooled by using a known cooling device, and the spun yarn is traction-thinned by a suction device such as air soccer. Subsequently, the yarn group discharged from the suction device is opened and then deposited on a conveyor to form a web. Next, a long fiber spunbonded non-woven fabric is obtained by partially thermocompression bonding the web formed on the conveyor using a thermocompression bonding device such as a heated emboss roll.

スパンボンド法を用いる場合、特に限定されないが、ウェブの均一性を向上させるために、例えば、特開平11−131355に開示されているようなコロナ設備等により繊維を帯電させる方法や、平板状の分散板等のような気流を制御する装置(図1参照)を用いてエジェクターの噴出し部分の気流の速度分布を調整する等をして繊維を開繊させた後にウェブを吹き付け、ウェブの飛散を抑制しながら捕集面に積層する方法を用いることで更に好ましい製法となる。
スパンボンド法で得られる不織布は、布強度が強く、かつ、ボンディング部の破損による短繊維の脱落がない等の物性上の特徴を有しており、また、低コストで生産性が高いため、衛生、土木、建築、農業・園芸、生活資材を中心に広範な用途で使用されている。
When the spunbond method is used, the fiber is not particularly limited, but in order to improve the uniformity of the web, for example, a method of charging the fiber by a corona facility as disclosed in Japanese Patent Application Laid-Open No. 11-131355, or a flat plate shape is used. After opening the fibers by adjusting the velocity distribution of the airflow at the ejection part of the ejector using a device that controls the airflow (see Fig. 1) such as a dispersion plate, the web is sprayed and the web is scattered. It becomes a more preferable manufacturing method by using the method of laminating on the collecting surface while suppressing the above.
The non-woven fabric obtained by the spunbond method has strong cloth strength, has physical characteristics such as short fibers not falling off due to breakage of the bonding portion, and is low in cost and highly productive. It is used in a wide range of applications, mainly in hygiene, civil engineering, construction, agriculture / horticulture, and living materials.

本実施形態のポリエステル長繊維の繊維径は13〜40μmであり、好ましくは15〜40μmであり、より好ましくは18〜35μm、特に好ましい範囲は21〜30μmである。繊維径が13μm以上であれば、透明性を十分なものに設計できる。また、紡糸時においてエジェクターの張力に繊維が十分に耐えることができずに繊維の一部が切れる恐れが少ない繊維径が40μm以下であれば、不織布化し、食品用フィルターとして用いる際、機械的強度や剛性、成分抽出性、透明性、シール性に優れ、食品用フィルターとして適している。 The fiber diameter of the polyester filaments of the present embodiment is 13 to 40 μm, preferably 15 to 40 μm, more preferably 18 to 35 μm, and particularly preferably 21 to 30 μm. If the fiber diameter is 13 μm or more, the transparency can be designed to be sufficient. In addition, if the fiber diameter is 40 μm or less because the fiber cannot sufficiently withstand the tension of the ejector during spinning and there is little risk of part of the fiber being cut, it is made into a non-woven fabric and has mechanical strength when used as a food filter. It has excellent rigidity, component extractability, transparency, and sealing properties, and is suitable as a food filter.

本実施形態のポリエステル長繊維不織布の面積当たりの表面積(すなわち、長繊維不織布の比表面積m2/g×目付g/m2)は1.0〜3.5(m2/m2)であり、より好ましくは1.2〜3.0(m2/m2)、特に好ましい範囲は1.3〜2.7(m2/m2)である。面積当たりの表面積が3.5(m2/m2)以下であれば、透明性を十分なものに設計できる。また、面積当たりの表面積が1.0以上であれば、不織布化した際に、十分な繊維本数を得ることができるため、食品用フィルターとして用いる際、機械的強度や剛性、成分抽出性、シール性に優れ、食品用フィルターとして適している。 The surface area per area of the polyester long-fiber non-woven fabric of the present embodiment (that is, the specific surface area of the long-fiber non-woven fabric m 2 / g × grain g / m 2 ) is 1.0 to 3.5 (m 2 / m 2 ), more preferably. 1.2 to 3.0 (m 2 / m 2 ), a particularly preferred range is 1.3 to 2.7 (m 2 / m 2 ). If the surface area per area is 3.5 (m 2 / m 2 ) or less, the transparency can be designed to be sufficient. Further, if the surface area per area is 1.0 or more, a sufficient number of fibers can be obtained when the non-woven fabric is formed, so that when used as a food filter, the mechanical strength, rigidity, component extractability, and sealing property are improved. Excellent and suitable as a food filter.

本実施形態のポリエステル長繊維不織布の層構成は、熱的に/化学的に一体化され、不織布となる方法であれば特に限定されないが、積層不織布であることができる。この際、各層の担う役割を分けた層構成にすることが好ましい。例えば、第1層をヒートシール強力の高い層、他方を引張強度、剛性、寸法安定性など機械的強力に優れた層とすることで、製袋時に求められるシール特性に優れ、かつ機械的物性にも優れた不織布とすることができる。また不織布を袋状に製袋する工程において、機械的強力とシール特性を1層のみの構成で両立させた構成の不織布を用いると、熱接着加工により袋物を製造する工程において、高温にて加熱、圧着処理を施すため、製袋設備の熱ロールや熱板ヒーターに熱可塑性樹脂が溶融、付着し、製品品質の低下や加工速度の低下が起こり、これを改善しようとすると、所望のシール強力を得られなくなる。これに対し、本実施形態の不織布構成であれば、シール層を内面に配置することで、良好なシール強力を発現しつつ、品質、生産速度を落とすことなく生産をすることが可能となる。 The layer structure of the polyester long fiber non-woven fabric of the present embodiment is not particularly limited as long as it is a method of thermally / chemically integrating to form a non-woven fabric, but it can be a laminated non-woven fabric. At this time, it is preferable to have a layer structure in which the roles played by each layer are separated. For example, by making the first layer a layer with high heat-sealing strength and the other layer having excellent mechanical strength such as tensile strength, rigidity, and dimensional stability, the sealing characteristics required at the time of bag making are excellent and the mechanical properties are excellent. It can also be an excellent non-woven fabric. Further, in the process of making a bag-shaped non-woven fabric, if a non-woven fabric having a structure in which mechanical strength and sealing characteristics are compatible with only one layer is used, it is heated at a high temperature in the process of manufacturing a bag by heat bonding processing. Since the crimping process is applied, the thermoplastic resin melts and adheres to the heat rolls and hot plate heaters of the bag making equipment, resulting in deterioration of product quality and processing speed. You will not be able to get it. On the other hand, in the case of the non-woven fabric structure of the present embodiment, by arranging the sealing layer on the inner surface, it is possible to produce the product without deteriorating the quality and the production speed while exhibiting good sealing strength.

本実施形態のポリエステル長繊維不織布として積層不織布を用いる場合、シール性を担う層の構造は、スパンボンド法、メルトブロウン法などの単繊維構造や鞘芯構造やサイドバイサイド、分割割繊等の2成分からなる複合繊維構造を用いることができるが、シール性能を担う低融点樹脂が繊維表面に配置されている構造であるほうが好ましい。例えば、芯が高融点で鞘が低融点の複合繊維構造であり、具体的には、芯がポリエチレンテレフタレートやポリブチレンテレフタレート等の高融点樹脂、鞘が共重合ポリエステルや脂肪族ポリエステル等の前述した低融点樹脂で構成される鞘芯構造の不織布である。 When a laminated non-woven fabric is used as the polyester long-fiber non-woven fabric of the present embodiment, the structure of the layer responsible for the sealing property is a single fiber structure such as a spunbond method or a melt blown method, a sheath core structure, a side-by-side structure, a split split fiber, or the like. Although a composite fiber structure made of the above can be used, it is preferable that the structure is such that the low melting point resin which is responsible for the sealing performance is arranged on the fiber surface. For example, it has a composite fiber structure in which the core has a high melting point and the sheath has a low melting point. Specifically, the core is a high melting point resin such as polyethylene terephthalate or polybutylene terephthalate, and the sheath is a copolymerized polyester or an aliphatic polyester as described above. It is a non-woven fabric having a sheath core structure composed of a low melting point resin.

本実施形態のポリエステル長繊維不織布として積層不織布を用いる場合、機械的強力を担う層の製法は特に限定はされないが、生産性などの観点から、スパンボンド法であることが好ましい。
特に、本実施形態のポリエステル長繊維不織布として積層不織布を用いる場合、機械的強力を担う層の製法、物性は前記方法で生産することで、より寸法安定性、機械的強力に優れた不織布とすることができる。
When a laminated non-woven fabric is used as the polyester long-fiber non-woven fabric of the present embodiment, the method for producing the layer that bears mechanical strength is not particularly limited, but the spunbond method is preferable from the viewpoint of productivity and the like.
In particular, when a laminated non-woven fabric is used as the polyester long fiber non-woven fabric of the present embodiment, the non-woven fabric having more excellent dimensional stability and mechanical strength can be obtained by producing the layer that bears mechanical strength by the above method. be able to.

本実施形態のポリエステル長繊維不織布として積層不織布を用いた場合の圧着方法は、繊維同士を一体化させ、不織布化可能であれば特に限定されないが、各層を積層させた後に熱ロールなどで熱圧着させて不織布化することが好ましい。各層を積層させた後に熱圧着することで、層間の接着強力をより強固にすることができ、機械的強力やシール性能をより効果的に発現可能とすることができる。 The crimping method when a laminated non-woven fabric is used as the polyester long-fiber non-woven fabric of the present embodiment is not particularly limited as long as the fibers can be integrated into a non-woven fabric, but after laminating each layer, thermocompression bonding is performed with a thermal roll or the like. It is preferable to make the non-woven fabric. By thermocompression bonding after laminating each layer, the adhesive strength between the layers can be further strengthened, and the mechanical strength and sealing performance can be more effectively exhibited.

本実施形態における積層不織布の層構成を前述の様な積層構成とすることで、シール強力は更に好適な範囲とすることができる。具体的なシール強力としては、1.5N/30mm以上であり、好ましくは2.0 N/30mm以上、より好ましくは2.5 N/30mm以上である。
また、機械的強力、即ち引張強度も更に好適な範囲とすることができ、その範囲は15N/30mm以上であり、好ましくは20N/30mm以上、より好ましくは23N/30mm以上である。
By setting the layer structure of the laminated non-woven fabric in the present embodiment to the above-mentioned laminated structure, the sealing strength can be further set in a more suitable range. The specific seal strength is 1.5 N / 30 mm or more, preferably 2.0 N / 30 mm or more, and more preferably 2.5 N / 30 mm or more.
Further, the mechanical strength, that is, the tensile strength can be further set in a more preferable range, and the range is 15 N / 30 mm or more, preferably 20 N / 30 mm or more, and more preferably 23 N / 30 mm or more.

本実施形態のポリエステル長繊維不織布の熱圧着は、不織布の糸と糸を熱で圧着させる方法であれば特に限定されないが、凹凸の表面構造を有するエンボスロールとフラットロールからなる一対の加熱ロール間に不織布を通過させ、不織布全体に均等に分散された熱圧着部を形成させることにより好適に行うことができる。エンボスロールにより熱圧着を行う場合、不織布全面積に対して5〜40%の範囲における熱圧着面積率での熱圧着が行われることが好ましく、より好ましくは7〜30%であり、さらに好ましくは7〜20%である。
熱圧着面積率がこの範囲内であると良好な繊維相互間の熱圧着処理を行うことができ、得られる不織布の適度な機械的強度や剛性、透明性、成分抽出性、寸法安定性を図る上で好ましい。熱圧着処理温度及び圧力は、供給されるウェブの目付、速度等の条件によって適宜選択されるべきものであり、一概には定められないが、ポリエステル系樹脂の融点よりも10〜90℃低い温度であることが好ましく、より好ましくは20〜60℃低い温度である。
The thermocompression bonding of the polyester long fiber non-woven fabric of the present embodiment is not particularly limited as long as it is a method of thermocompression-bonding the threads of the non-woven fabric, but between a pair of heating rolls composed of an embossed roll having an uneven surface structure and a flat roll. This can be preferably performed by passing the non-woven fabric through the non-woven fabric to form thermocompression-bonded portions evenly dispersed throughout the non-woven fabric. When thermocompression bonding is performed by embossing roll, it is preferable that thermocompression bonding is performed at a thermocompression bonding area ratio in the range of 5 to 40% with respect to the total area of the non-woven fabric, more preferably 7 to 30%, still more preferably. It is 7 to 20%.
When the thermocompression bonding area ratio is within this range, good thermocompression bonding between fibers can be performed, and appropriate mechanical strength, rigidity, transparency, component extractability, and dimensional stability of the obtained non-woven fabric are achieved. Preferred above. The thermocompression bonding temperature and pressure should be appropriately selected depending on the conditions such as the basis weight and speed of the supplied web, and are not unconditionally determined, but are 10 to 90 ° C lower than the melting point of the polyester resin. The temperature is preferably 20 to 60 ° C. lower.

前記熱圧着工程でエンボスロールを用いる以外に、熱風をウェブに通過させることで糸と糸を熱で圧着するエアスルー法を用いることができる。エアスルー法で熱圧着した場合、布帛表面にエンボス形状の様な部分的な凹凸が無くなるため、不織布の見た目の透明感をより高くすることができる。 In addition to using the embossed roll in the thermocompression bonding step, an air-through method in which the threads are thermocompression-bonded by passing hot air through the web can be used. When thermocompression bonding is performed by the air-through method, the surface of the fabric is not partially uneven like an embossed shape, so that the appearance of the non-woven fabric can be made more transparent.

本実施形態のポリエステル長繊維不織布の沸水収縮率は、2.0%以下であることが好ましく、より好ましくは1.6%以下、更に好ましくは1.0%、特に好ましい範囲は0.5%以下である。沸水収縮率が2.0%以下であると熱成型加工等での収縮がほとんど無く、工程安定性に優れ、また、100℃近い高温環境下にさらされるような使用形態でも形態保持性に優れる。下限は0%が好ましいが、現実的には0.2%以上である。 The boiling water shrinkage rate of the polyester long fiber nonwoven fabric of the present embodiment is preferably 2.0% or less, more preferably 1.6% or less, still more preferably 1.0%, and a particularly preferable range is 0.5% or less. When the boiling water shrinkage rate is 2.0% or less, there is almost no shrinkage in thermoforming, process stability is excellent, and morphological retention is excellent even in a usage form exposed to a high temperature environment close to 100 ° C. The lower limit is preferably 0%, but in reality it is 0.2% or more.

本実施形態のポリエステル長繊維不織布の透明性は、好ましくは60%以上であり、より好ましくは65%以上、さらに好ましくは70%以上である。透明性が60%未満では、不織布を通じて中身の状態が見えにくく、不鮮明になる。 The transparency of the polyester long fiber non-woven fabric of the present embodiment is preferably 60% or more, more preferably 65% or more, still more preferably 70% or more. If the transparency is less than 60%, the state of the contents is difficult to see through the non-woven fabric and becomes unclear.

本実施形態のポリエステル長繊維不織布の目付は、10〜30g/m2であり、好ましくは12〜25g/m2である。目付が10g/m2以上であれば、透明性・成分抽出性を保ちながら機械的強度も充分確保できる。一方、目付が30g/m2以下であれば、透明性・成分抽出性を得ることができる。 The basis weight of the polyester long fiber non-woven fabric of the present embodiment is 10 to 30 g / m 2 , preferably 12 to 25 g / m 2 . If the basis weight is 10 g / m 2 or more, sufficient mechanical strength can be secured while maintaining transparency and component extractability. On the other hand, if the basis weight is 30 g / m 2 or less, transparency and component extractability can be obtained.

本実施形態のポリエステル長繊維不織布の厚みは、0.02〜0.50mmが好ましく、より好ましくは0.03〜0.30mmである。目付と厚みがこの範囲内にあると食品用フィルターとして使用する際に優れた透明性、機械的強度、成分抽出性が得られる。 The thickness of the polyester long fiber non-woven fabric of the present embodiment is preferably 0.02 to 0.50 mm, more preferably 0.03 to 0.30 mm. When the basis weight and thickness are within this range, excellent transparency, mechanical strength, and component extractability can be obtained when used as a food filter.

本実施形態のポリエステル長繊維不織布の平均見掛け密度は、0.10〜0.50g/cm3が好ましく、より好ましくは0.12〜0.30g/cm3である。平均見掛け密度は、不織布の剛性、透明性、粉漏れ性及び成分抽出性に関係し、上記の範囲であると繊維間隙が適度であるため、食品用フィルターとして適している。平均見掛け密度が0.10g/cm3以上であれば、繊維間隙を調整し粉漏れ量を適度に抑えながら、機械的強度も充分にできる。一方、平均見掛け密度が0.50g/cm3以下であれば繊維間隙を小さくしすぎず、成分抽出性を適度に保ち、製品品位を充分にできる。 The average apparent density of the polyester long fiber non-woven fabric of the present embodiment is preferably 0.10 to 0.50 g / cm 3 , and more preferably 0.12 to 0.30 g / cm 3 . The average apparent density is related to the rigidity, transparency, powder leakage property and component extractability of the non-woven fabric, and the fiber gap is appropriate in the above range, so that it is suitable as a food filter. If the average apparent density is 0.10 g / cm 3 or more, the mechanical strength can be sufficiently obtained while adjusting the fiber gaps and appropriately suppressing the amount of powder leakage. On the other hand, if the average apparent density is 0.50 g / cm 3 or less, the fiber gaps are not made too small, the component extractability can be maintained appropriately, and the product quality can be sufficiently obtained.

本実施形態のポリエステル長繊維不織布のMD方向の引張強度は5〜40N/30mmであることが好ましく、6〜40N/30mmであることがより好ましく、更に好ましくは7〜40N/30mmである。引張強度がこの範囲以上であると製袋加工時の生産安定性や食品用フィルターとしての使用時に破れ防止等に優れる。 The tensile strength of the polyester long fiber nonwoven fabric of the present embodiment in the MD direction is preferably 5 to 40 N / 30 mm, more preferably 6 to 40 N / 30 mm, and even more preferably 7 to 40 N / 30 mm. If the tensile strength is equal to or higher than this range, it is excellent in production stability during bag making and prevention of tearing when used as a food filter.

本実施形態のポリエステル長繊維不織布の地合係数は、0.5〜2.0が好ましく、より好ましくは0.5〜1.5である。地合係数は、不織布の均一性を示すため、強度、剛性、透明性、粉漏れ性及び成分抽出性に関係する。上記の範囲であると不織布の均一性が最適であるため、食品用フィルターとしての強度、剛性、透明性、袋形状への加工適性及び粉漏れ性に優れる。 The formation coefficient of the polyester long fiber non-woven fabric of the present embodiment is preferably 0.5 to 2.0, more preferably 0.5 to 1.5. The formation coefficient is related to strength, rigidity, transparency, powder leakage property and component extractability because it indicates the uniformity of the non-woven fabric. Within the above range, the uniformity of the non-woven fabric is optimal, so that it is excellent in strength, rigidity, transparency, processability into a bag shape, and powder leakage property as a food filter.

本実施形態のポリエステル長繊維を得る際の紡糸温度は、ポリエステル系樹脂の融点よりも10〜60℃高い温度であることが好ましく、より好ましくは10〜30℃高い温度である。紡糸温度がこの範囲であると単糸切れ等の発生が無く、配向結晶性が適度で、機械的強度や寸法安定性に優れた不織布が得られる。 The spinning temperature at the time of obtaining the polyester filaments of the present embodiment is preferably a temperature 10 to 60 ° C. higher than the melting point of the polyester resin, and more preferably 10 to 30 ° C. higher. When the spinning temperature is in this range, no single yarn breakage or the like occurs, the orientation crystallinity is appropriate, and a non-woven fabric having excellent mechanical strength and dimensional stability can be obtained.

本実施形態のポリエステル長繊維不織布の不織布とした後の樹脂の固有粘度(IV値)は、0.6以上であることが好ましく、より好ましくは0.65以上、更に好ましくは0.7以上である。樹脂ペレットを溶融押出しする際に、溶融時の熱負荷や混練時のせん断負荷などで樹脂が分解する。溶融した後、即ち不織布とした後の樹脂のIV値がこの範囲以上の場合であれば、樹脂の分解を好適に抑制でき、紡糸時の樹脂の延伸、結晶化を促進することができるため、機械的強度、寸法安定性に優れた不織布とすることができる。 The intrinsic viscosity (IV value) of the resin after making the non-woven fabric of the polyester long fiber non-woven fabric of the present embodiment is preferably 0.6 or more, more preferably 0.65 or more, and further preferably 0.7 or more. When the resin pellets are melt-extruded, the resin decomposes due to the heat load during melting and the shear load during kneading. When the IV value of the resin after melting, that is, after making it into a non-woven fabric is in this range or more, the decomposition of the resin can be suitably suppressed, and the stretching and crystallization of the resin during spinning can be promoted. A non-woven fabric having excellent mechanical strength and dimensional stability can be obtained.

本実施形態のポリエステル長繊維を得る際の紡糸速度は、3000〜6000m/minが好ましく、より好ましくは3500〜5000m/minである。紡出糸条を牽引細化する際の牽引速度が上記の範囲内であると、ポリエステル長繊維の配向結晶化が十分で機械的特性や寸法安定性に優れた不織布が得られ、且つ、紡糸中に糸切れが発生する可能性が少なく、不織布の生産性の点からも好ましい。 The spinning speed for obtaining the polyester filaments of the present embodiment is preferably 3000 to 6000 m / min, more preferably 3500 to 5000 m / min. When the traction speed at the time of traction thinning of the spun yarn is within the above range, a non-woven fabric having sufficient orientation crystallization of polyester filaments and excellent mechanical properties and dimensional stability can be obtained, and spinning. There is little possibility that thread breakage will occur inside, which is preferable from the viewpoint of the productivity of the non-woven fabric.

本実施形態のポリエステル長繊維を得る際のドラフト比は、400〜2500が好ましく、より好ましくは700〜2200である。紡出糸条を牽引細化する際のドラフト比が上記の範囲内であると、ポリエステル長繊維の配向結晶化が十分で機械的特性や寸法安定性に優れた不織布が得られ、且つ、紡糸中に糸切れや、熱圧着時の「ロール取られ」が発生する可能性が低いため、不織布の生産性の点からも好ましい。 The draft ratio for obtaining the polyester filaments of the present embodiment is preferably 400 to 2500, more preferably 700 to 2200. When the draft ratio at the time of pulling and thinning the spun yarn is within the above range, a non-woven fabric having sufficient orientation crystallization of polyester filaments and excellent mechanical properties and dimensional stability can be obtained, and the spun yarn is spun. It is also preferable from the viewpoint of the productivity of the non-woven fabric because it is unlikely that thread breakage or "roll removal" during thermocompression bonding will occur inside.

本実施形態のポリエステル長繊維の複屈折率Δnは、0.04〜0.12であり、好ましくは0.06〜0.1である。複屈折率がこの範囲であると、繊維の配向性が適度で、機械的強度や寸法安定性に優れた不織布が得られる。 The birefringence Δn of the polyester filaments of the present embodiment is 0.04 to 0.12, preferably 0.06 to 0.1. When the birefringence is in this range, a non-woven fabric having appropriate fiber orientation and excellent mechanical strength and dimensional stability can be obtained.

結晶性を評価する方法は特に限定されないが、例えば、DSCによる結晶化度測定や、ラマン分光測定法などで測定できる。 The method for evaluating the crystallinity is not particularly limited, and for example, the crystallinity can be measured by DSC, Raman spectroscopy, or the like.

本実施形態のポリエステル長繊維の結晶化度は、30〜50%であり、好ましくは、40〜50%である。結晶化度がこの範囲内であると、機械的強度や寸法安定性に優れた繊維が得られる。 The crystallinity of the polyester filaments of the present embodiment is 30 to 50%, preferably 40 to 50%. When the crystallinity is within this range, fibers having excellent mechanical strength and dimensional stability can be obtained.

本実施形態のポリエステル長繊維の結晶性をラマン分光法により実施する場合、繊維断面のラマンスペクトルにおいて観測される1740cm-1付近のC=O基によるピーク巾の半値全幅の平均値で評価することができる。ピーク巾の半値全幅の平均値は、18〜24cm-1であり、好ましくは、19〜24cm-1であり、より好ましい範囲は20〜23cm-1である。ピーク巾の半値全幅の平均値がこの範囲にあると、機械的強度や寸法安定性に優れた繊維が得られる。 When the crystallinity of the polyester filaments of the present embodiment is carried out by Raman spectroscopy, it is evaluated by the average value of the full width at half maximum of the peak width due to the C = O group near 1740 cm -1 observed in the Raman spectrum of the fiber cross section. Can be done. The average value of the full width at half maximum of the peak width is 18 to 24 cm -1 , preferably 19 to 24 cm -1 , and the more preferable range is 20 to 23 cm -1 . When the average value of the full width at half maximum of the peak width is in this range, a fiber having excellent mechanical strength and dimensional stability can be obtained.

本実施形態のポリエステル長繊維は繊維の半径方向に異なった結晶性、例えば、外周部の結晶性を高く、内部の結晶性を低くすることができる。外周部の結晶性を高くすることで収縮しにくく機械的強度に優れた繊維とすることができ、かつ、内部の結晶性を低くすることで、熱圧着時に繊維同士の圧着強度を十分にえることができ、その結果機械的強度や寸法安定性に優れた不織布とすることができる。これはDSCによる結晶化度測定時に融解ピークを評価することで確認することができる。 The polyester filaments of the present embodiment have different crystallinity in the radial direction of the fiber, for example, the crystallinity of the outer peripheral portion can be increased and the crystallinity of the inside can be decreased. By increasing the crystallinity of the outer peripheral portion, it is possible to obtain fibers that are less likely to shrink and have excellent mechanical strength, and by lowering the crystallinity of the inside, sufficient pressure bonding strength between the fibers can be obtained during thermocompression bonding. As a result, a non-woven fabric having excellent mechanical strength and dimensional stability can be obtained. This can be confirmed by evaluating the melting peak when measuring the crystallinity by DSC.

図2に、本発明の実施例におけるポリエステル長繊維不織布の沸水収縮率と透明性との関係を示す。繊径を大きくすると透明性を高くできるが、配向結晶化が進みにくいために沸水収縮率が大きくなり、寸法安定性が低くなる。 FIG. 2 shows the relationship between the boiling water shrinkage rate and the transparency of the polyester long fiber non-woven fabric in the examples of the present invention. Although the transparency can be increased by increasing the fiber diameter, the boiling water shrinkage rate increases and the dimensional stability decreases because the orientation crystallization does not proceed easily.

図3と4に、本発明の実施例におけるポリエステル長繊維不織布の、それぞれ、ドラフト比及び紡糸温度と、複屈折率(Δn)及び結晶化度で示される配向結晶性との関係を示す。ドラフト比を大きくするほど、繊維の配向結晶性が増加する。また、太繊径の紡糸条件では、紡糸温度を低温化するほど、冷却性が高まることで延伸効率が上がり、繊維の配向結晶化を進行させることができる。 FIGS. 3 and 4 show the relationship between the draft ratio and the spinning temperature of the polyester long fiber non-woven fabric in the examples of the present invention and the orientation crystallinity indicated by the birefringence (Δn) and the crystallinity, respectively. The larger the draft ratio, the greater the orientation crystallinity of the fibers. Further, under the spinning conditions of a large fiber diameter, the lower the spinning temperature, the higher the cooling property, the higher the drawing efficiency, and the more the alignment and crystallization of the fibers can be promoted.

図5に、本発明の実施例におけるポリエステル長繊維不織布の樹脂の固有粘度(IV値)と複屈折率(Δn)及び結晶化度で示される配向結晶性との関係を示す。樹脂のIV値を高くすることで、樹脂の配向結晶化が促進され、繊維の配向結晶化を進行させることができる。 FIG. 5 shows the relationship between the intrinsic viscosity (IV value) of the resin of the polyester long fiber non-woven fabric in the examples of the present invention and the orientation crystallinity indicated by the birefringence (Δn) and the crystallinity. By increasing the IV value of the resin, the orientation crystallization of the resin is promoted, and the orientation crystallization of the fibers can be promoted.

これらのデータから、本発明の所望の効果を奏するよう鋭意研究した結果、本願発明者らは、紡糸温度の低温化とドラフト比拡大により太繊径を維持しつつ、配向結晶性を高めることで、透明性と沸水収縮率の向上の両立を達成した。即ち、不織布において透明性の向上と沸水収縮率に表わされる寸法安定性の向上とは相反する関係にあるが、本発明者らは繊維の太繊径化と配向結晶性とを最適範囲とすることによって透明性の向上と寸法安定性の向上の両立を達成した。 From these data, as a result of diligent research to achieve the desired effect of the present invention, the inventors of the present invention have improved the oriented crystallinity while maintaining the large fiber diameter by lowering the spinning temperature and increasing the draft ratio. Achieved both transparency and improved boiling water shrinkage. That is, although there is a contradictory relationship between the improvement of transparency and the improvement of dimensional stability expressed by the boiling water shrinkage rate in the non-woven fabric, the present inventors set the optimum range of fiber diameter increase and orientation crystallinity. As a result, both improvement in transparency and improvement in dimensional stability have been achieved.

さらに、本発明では用いる樹脂の固有粘度(IV値)を最適化することでも配向結晶の最適範囲を達成することができる。本目的を達成するためのIV値の範囲は0.7以上であり、好ましくは0.85以下であり、さらに好ましくは0.72〜0.8の範囲である。この範囲に固有粘度があれば、単糸切れなどが発生せず安定した生産性を確保でき、かつ、溶融した樹脂を牽引細化した際に高い配向結晶性をえることで、更に高い寸法安定性及び機械的強力を得ることができる。 Further, in the present invention, the optimum range of the oriented crystal can be achieved by optimizing the intrinsic viscosity (IV value) of the resin used. The range of IV values for achieving this purpose is 0.7 or more, preferably 0.85 or less, and more preferably 0.72 to 0.8. If the intrinsic viscosity is in this range, stable productivity can be ensured without single thread breakage, and higher dimensional stability can be obtained by obtaining high orientation crystallinity when the molten resin is towed and thinned. Sexual and mechanical strength can be obtained.

本実施形態のポリエステル長繊維不織布は、お湯の中に入れた際に、表面に浮くことなく、速やかに沈むように、親水性に優れていることが好ましい。親水剤としては、食品用として用いられる界面活性剤、例えば、ソルビタン脂肪酸エステル、ポリグリセリン脂肪酸エステル、ショ糖脂肪酸エステルなどの水溶液、エチルアルコール溶液、又はエチルアルコールと、水の混合溶液等が好ましい。塗布する方法は、グラビアロール方式、キスロール方式、浸漬方式、スプレー方式などの公知の方法を適用することができる。 The polyester long-fiber non-woven fabric of the present embodiment is preferably excellent in hydrophilicity so that when it is put in hot water, it does not float on the surface and sinks quickly. As the hydrophilic agent, a surfactant used for foods, for example, an aqueous solution such as sorbitan fatty acid ester, polyglycerin fatty acid ester, sucrose fatty acid ester, an ethyl alcohol solution, or a mixed solution of ethyl alcohol and water is preferable. As a method of coating, a known method such as a gravure roll method, a kiss roll method, a dipping method, or a spray method can be applied.

本実施形態のポリエステル長繊維不織布には、本発明の所望の効果を損なわない範囲で、常用の後加工、例えば、消臭剤、抗菌剤等の付与をしてもよいし、染色、撥水加工、透水加工等を施してもよい。
本実施形態のポリエステル長繊維不織布は、透明性に優れているために中身が鮮明に見えるので意匠性に優れ、かつ、寸法安定性に優れているために緑茶、紅茶、コーヒー等の食品用フィルターとして非常に適した特性を有している。食品用フィルターとしては、平袋でもよいが、立体形状であると、中身が一層良く見え、抽出が効果的に行われるので好ましい。立体形状としては、四面体形状、三角錐立体形状等が好ましい。
The polyester long fiber non-woven fabric of the present embodiment may be subjected to regular post-processing, for example, a deodorant, an antibacterial agent, etc., as long as the desired effect of the present invention is not impaired, and may be dyed or water repellent. Processing, water permeable processing, etc. may be performed.
The polyester long-fiber non-woven fabric of the present embodiment has excellent transparency, so that the contents can be seen clearly, so that it has excellent design, and because it has excellent dimensional stability, it has excellent filters for foods such as green tea, black tea, and coffee. It has very suitable properties as. The food filter may be a flat bag, but a three-dimensional shape is preferable because the contents can be seen better and extraction can be performed effectively. As the three-dimensional shape, a tetrahedron shape, a triangular pyramid three-dimensional shape, or the like is preferable.

立体形状の食品用フィルターは、被抽出物を充填し封入した後、袋詰めされて販売されるが、購入した消費者が袋から取り出して使用する時には、速やかに元の立体形状に戻ることが要求される。本発明の長繊維不織布は、コシがあり、適度な剛性を有しているため、上記のような要求を十分に満足することができる。 Three-dimensional food filters are sold after being filled with the extract and sealed in a bag, but when the consumer who purchased the filter takes it out of the bag and uses it, it can quickly return to the original three-dimensional shape. Required. Since the long-fiber non-woven fabric of the present invention is elastic and has appropriate rigidity, the above requirements can be sufficiently satisfied.

以下、実施例により本発明を具体的に説明するが、本発明は、これらにより何ら限定されるものではない。尚、用いた測定方法、評価方法等は下記の通りであった。 Hereinafter, the present invention will be specifically described with reference to Examples, but the present invention is not limited thereto. The measurement method, evaluation method, etc. used were as follows.

(1)チタン元素含有量(ppm)
サーモフィッシャーサイエンティフィック社製のICP発光分析装置を用い、ポリエステル樹脂中のチタン元素含有量を求めた。
(1) Titanium element content (ppm)
The titanium element content in the polyester resin was determined using an ICP emission spectrometer manufactured by Thermo Fisher Scientific.

(2)平均繊維径(μm)
キーエンス社製のマイクロスコープ顕微鏡(VH−8000)を用い、繊維の直径を1000倍に拡大して測定し、各20本の平均値で求めた。
(2) Average fiber diameter (μm)
Using a microscope microscope (VH-8000) manufactured by KEYENCE, the diameter of the fiber was magnified 1000 times and measured, and the average value of each of the 20 fibers was calculated.

(3)複屈折率(Δn)
OLYMPUS社製のBH2型偏光顕微鏡コンペンセーターを用いて、通常の干渉縞法によってレターデーションと繊維径より牽引直後の繊維の複屈折率を求めた。
(3) Birefringence index (Δn)
Using a BH2 type polarizing microscope compensator manufactured by OLYMPUS, the birefringence of the fiber immediately after traction was determined from the retardation and the fiber diameter by the usual interference fringe method.

(4)結晶化度(%)
PerkinElmer社製の示差走査熱量計DSC6000を用い、昇温速度を10℃/minで、40℃から300℃に昇温して結晶化発熱量ΔHc、結晶融解熱量ΔHmを測定した。結晶化度(%)は下記式により求めた:
結晶化度χc(%)=(ΔHm−ΔHc)/126.4×100
*126.4J/gはポリエチレンテレフタレートの完全結晶の融解熱量である。
(4) Crystallinity (%)
Using a differential scanning calorimeter DSC6000 manufactured by PerkinElmer, the temperature was raised from 40 ° C. to 300 ° C. at a heating rate of 10 ° C./min to measure the calorific value of crystallization ΔHc and the calorific value of crystal melting ΔHm. The crystallinity (%) was calculated by the following formula:
Crystallinity χc (%) = (ΔHm−ΔHc) / 126.4 × 100
* 126.4 J / g is the amount of heat of fusion of the perfect crystal of polyethylene terephthalate.

(5)半値全幅(cm-1)
Renishaw社製の顕微ラマン分光装置を用い、励起光532nm、励起光強度10%でスペクトルを測定した。スペクトルにおいて観察される1740cm-1付近のC=O基によるピーク巾の半値全幅を求めた。
(5) Full width at half maximum (cm -1 )
The spectrum was measured with an excitation light of 532 nm and an excitation light intensity of 10% using a microscopic Raman spectroscope manufactured by Renishaw. The full width at half maximum of the peak width due to the C = O group near 1740 cm -1 observed in the spectrum was determined.

(6)固有粘度(IV値)
JIS K−7367−5に準拠して測定した。
(6) Intrinsic viscosity (IV value)
Measured according to JIS K-7637-5.

(7)目付(g/m2
JIS L−1906に準拠して測定した。
(7) Metsuke (g / m 2 )
Measured according to JIS L-1906.

(8)厚み(mm)
JIS L−1906に規定の方法で荷重100g/cm2の厚みを測定した。
(8) Thickness (mm)
The thickness of a load of 100 g / cm 2 was measured by the method specified in JIS L-1906.

(9)平均見掛け密度(g/cm3
JIS L−1906に規定の方法で測定した目付と厚みから単位体積当たりの質量を求めた:
平均見掛け密度(g/cm3)=(目付g/m2)/((厚みmm)×1000)
(9) Average apparent density (g / cm 3 )
The mass per unit volume was determined from the basis weight and thickness measured by the method specified in JIS L-1906:
Average apparent density (g / cm 3 ) = (Metsuke g / m 2 ) / ((Thickness mm) x 1000)

(10)熱圧着面積率(%)
1cm角の試験片をサンプリングして電子顕微鏡で写真を撮影し、その各写真より熱圧着部の面積を測定し、その平均値を熱圧着部の面積とした。また、熱圧着部のパターンのピッチをMD方向及びCD方向において測定し、これらの値により、不織布の単位面積当たりに占める熱圧着面積の比率を熱圧着面積率として算出した。
(10) Thermocompression bonding area ratio (%)
A 1 cm square test piece was sampled and a photograph was taken with an electron microscope, the area of the thermocompression bonding portion was measured from each photograph, and the average value was taken as the area of the thermocompression bonding portion. Further, the pitch of the pattern of the thermocompression bonding portion was measured in the MD direction and the CD direction, and the ratio of the thermocompression bonding area to the unit area of the non-woven fabric was calculated as the thermocompression bonding area ratio from these values.

(11)透明性(%)
マクベス分光光度計(CE-7000A型:サカタインク製)で反射率(L値)を測定し、標準白板のL値(Lw0)と標準黒板のL値(Lb0)の差を求めて基準とし、試料を白板上に置いたL値(Lw)と同様に黒板状に置いたL値(Lb)から下記式に従って透明性を求めた:
透明性(%)={(Lw−Lb)/(Lw0−Lb0)}×100
(11) Transparency (%)
Measure the reflectance (L value) with a Macbeth spectrophotometer (CE-7000A type: manufactured by Sakata Ink), and find the difference between the L value (L w0 ) of the standard whiteboard and the L value (L b0) of the standard blackboard. Then, the transparency was calculated from the L value (L b ) placed on the blackboard in the same way as the L value (L w ) placed on the white board according to the following formula:
Transparency (%) = {(L w −L b ) / (L w0 −L b0 )} × 100

(12)沸水収縮率(%)
JIS L−1906に準拠し、縦25cm×横25cmの試験片を試料の幅1m当たり3箇所採取し、沸騰水中に3分間浸漬し、自然乾燥後にMD方向及びCD方向の収縮率を求めた。それぞれの平均値を算出し、MD方向とCD方向のいずれか大きい方の収縮率をその不織布の沸水収縮率とした。
(12) Boiling water shrinkage rate (%)
According to JIS L-1906, 3 test pieces of 25 cm in length × 25 cm in width were collected per 1 m of width of the sample, immersed in boiling water for 3 minutes, and after natural drying, the shrinkage ratios in the MD direction and the CD direction were determined. The average value of each was calculated, and the shrinkage rate in the MD direction or the CD direction, whichever was larger, was taken as the boiling water shrinkage rate of the non-woven fabric.

(13)引張強度(N/30mm)
島津製作所社製オートグラフAGS−5G型を用いて、30mm幅の試料を把握長100mm、引張速度300mm/minで伸長し、得られる破断時の荷重を強度とし、不織布のMD方向について5回測定を行い、その平均値を求めた。
(13) Tensile strength (N / 30mm)
Using the Shimadzu Autograph AGS-5G type, a sample with a width of 30 mm is grasped and stretched at a length of 100 mm and a tensile speed of 300 mm / min. Was performed, and the average value was calculated.

(14)地合係数
20cm×30cmの試験片を採取し、野村商事製フォーメーションテスター(FMT−MIII)測定器を用い、CCDカメラにより18cm×25cmの範囲を撮影した透過像を128×128の画素に分解し、各々の画素の受ける光の強さを測定し、透過率を算出した。地合係数は、測定サンプルの各微小部位(5mm×5mm)の透過率の標準偏差(σ)を平均透過率(E)で除した値であり、微小単位目付のバラツキを表し、値が小さいほど均一性が高いことを示す。
地合係数=σ/E×100
(14) Formation coefficient
A 20 cm x 30 cm test piece was collected, and a transmission image taken in a range of 18 cm x 25 cm with a CCD camera using a formation tester (FMT-MIII) measuring instrument manufactured by Nomura Shoji was decomposed into 128 x 128 pixels, and each of them was decomposed into 128 x 128 pixels. The intensity of light received by the pixels was measured, and the transmittance was calculated. The formation coefficient is a value obtained by dividing the standard deviation (σ) of the transmittance of each minute part (5 mm × 5 mm) of the measurement sample by the average transmittance (E), and represents the variation in the minute unit grain, and the value is small. The more uniform it is, the higher the uniformity.
Formation coefficient = σ / E × 100

(15)ヒートシール強度(N/30mm)
島津製作所社製オートグラフAGS−5G型を用いて30mm幅の試料のヒートシール部分を約50mm上下方向に剥離して取り付け、把握長50mm、引張速度100mm/minで伸長し、得られる破断時の荷重を強度とし、不織布のMD方向について5回測定を行い、その平均値を求めた。ヒートシール条件は、シール温度210℃、シール時間1秒、圧力0.5MPa、シール面積7mm×25mmであった。
(15) Heat seal strength (N / 30mm)
Using the Shimadzu Autograph AGS-5G type, the heat-sealed part of the sample with a width of 30 mm is peeled off in the vertical direction by about 50 mm and attached, and it is stretched at a grip length of 50 mm and a tensile speed of 100 mm / min. Taking the load as the strength, the measurement was performed 5 times in the MD direction of the non-woven fabric, and the average value was calculated. The heat sealing conditions were a sealing temperature of 210 ° C., a sealing time of 1 second, a pressure of 0.5 MPa, and a sealing area of 7 mm × 25 mm.

(16)ドラフト比
下記式からドラフト比を算出した:
ドラフト比=紡速(m/min)/吐出線速度(m/min)
吐出線速度(m/min)=単孔吐出量(g/min)/{溶融密度(g/cm3)×[紡口径(cm)/2]2×π}
*ポリエステルの溶融密度:1.20g/cm3を使用
(16) Draft ratio The draft ratio was calculated from the following formula:
Draft ratio = Spinning speed (m / min) / Discharge line speed (m / min)
Discharge line velocity (m / min) = Single hole discharge amount (g / min) / {Melting density (g / cm 3 ) x [Spin diameter (cm) / 2] 2 x π}
* Polyester melt density: 1.20 g / cm 3 is used

(17)ポリエステル長繊維不織布の面積当たりの表面積
長繊維不織布の比表面積m2/g×目付g/m2により求めた。
長繊維不織布の比表面積(m2/g)は、島津製作所(株)の自動比表面積測定機ジェミニ2360で求めた。また、比表面積が、0.1m2/gを下回る場合は、下記の式により求めた。
表面積(m2/m2)=4×目付(g/m2)/樹脂の密度(g/cm3)/繊維径(μm)
繊維径が2種類以上のシートの場合、各繊維径の表面積を合計した。
(17) Surface area per area of polyester long-fiber non-woven fabric The specific surface area of the long-fiber non-woven fabric was determined by m 2 / g × grain g / m 2.
The specific surface area (m 2 / g) of the long-fiber non-woven fabric was determined by the automatic specific surface area measuring machine Gemini 2360 manufactured by Shimadzu Corporation. When the specific surface area was less than 0.1 m 2 / g, it was calculated by the following formula.
Surface area (m 2 / m 2 ) = 4 x grain (g / m 2 ) / resin density (g / cm 3 ) / fiber diameter (μm)
In the case of sheets having two or more fiber diameters, the surface areas of each fiber diameter were totaled.

(18)10%孔径
1つのサンプルから2cm角の資料を10枚切り出し、SEM観察用のイオンスパッタリング装置で白金蒸着し、透過光にて100倍の倍率で1試料中10か所の不織布画像を撮影した。画像を画像解析ソフトにて不織布部分を黒色、孔部分を白色に二値化し、画像中のすべての孔の面積と最長径を数値化した。画像解析ソフトは、旭化成エンジニアリング製「A像くん(TM)」を用いた。1つのサンプル画像中の、すべての孔を、最大面積から小さい面積に順に並べて積算し、全孔面積の10%に到達した点の孔面積から、該面積と等しい面積の円の直径として、下記の式により孔径を求めた。
孔径(μm) = ((4×S)/π)^0.5
上記式で、Sは孔面積(μm^2)、「^0.5」は「0.5乗」を意味する。
(18) 10% pore size Ten pieces of 2 cm square material were cut out from one sample, platinum was vapor-deposited with an ion sputtering device for SEM observation, and non-woven fabric images at 10 places in one sample were obtained at a magnification of 100 times with transmitted light. I took a picture. The image was binarized to black for the non-woven fabric and white for the holes using image analysis software, and the areas and longest diameters of all the holes in the image were quantified. As the image analysis software, "A image-kun (TM)" manufactured by Asahi Kasei Engineering Co., Ltd. was used. All the holes in one sample image are arranged in order from the maximum area to the smallest area and integrated, and from the hole area at the point where 10% of the total hole area is reached, the diameter of the circle having the same area as the area is as follows. The hole diameter was calculated by the formula of.
Hole diameter (μm) = ((4 × S) / π) ^ 0.5
In the above formula, S means the hole area (μm ^ 2), and “^ 0.5” means “0.5 power”.

(19)2.3%孔径
上記10%孔径の代わりに、全孔面積の2.3%に到達した点の孔面積から孔径を求めた。
(19) 2.3% hole diameter Instead of the above 10% hole diameter, the hole diameter was calculated from the hole area at the point where 2.3% of the total hole area was reached.

(20)長径/孔径
1つのサンプル画像中の、すべての孔を、最大面積から小さい面積に順に並べて積算し、全孔面積の2.3%に達する孔から10%に達する孔の間に含まれるすべての孔の、長径の平均と孔径の平均を求め、下記の式により求めた。
長径/孔径 = 長径の平均 / 孔径の平均
(20) Major axis / hole diameter All holes in one sample image are arranged in order from the maximum area to the smallest area and integrated, and all included between the holes reaching 2.3% and the holes reaching 10% of the total hole area. The average of the major axis and the average of the hole diameter of the holes were calculated by the following formula.
Major axis / hole diameter = average major axis / average hole diameter

[実施例1]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比2120にて溶融紡糸して繊径が20.5μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付12g/m2のウェブを作製し、エンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 1]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 20.5 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 2120. Next, using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] to control the air flow in a flat plate shape, the fibers are spread and dispersed to prepare a web with a grain size of 12 g / m 2 , and between the embossed roll and the flat roll. A polyester long fiber non-woven fabric was obtained by thermocompression bonding at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例2]
実施例1においてポリエステル長繊維の繊径が25.7μmとなるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 2]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 1 except that the polyester long fibers were spun so as to have a fiber diameter of 25.7 μm in Example 1. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例3]
実施例1においてポリエステル長繊維の繊径が30.0μmとなるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 3]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 1 except that the polyester long fibers were spun so as to have a fiber diameter of 30.0 μm in Example 1. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例4]
実施例3においてIV値0.8、酸化チタン含有量が12ppmの樹脂を用いたこと以外は、実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 4]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.8 and a titanium oxide content of 12 ppm was used in Example 3. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例5]
実施例3においてIV値0.8、酸化チタン含有量が70ppmの樹脂を用いたこと以外は、実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 5]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.8 and a titanium oxide content of 70 ppm was used in Example 3. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例6]
実施例3においてIV値0.72、酸化チタン含有量が0ppmの樹脂を用いたこと以外は、実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 6]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.72 and a titanium oxide content of 0 ppm was used in Example 3. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例7]
実施例3においてIV値0.77、酸化チタン含有量が0ppmの樹脂を用いたこと以外は、実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 7]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.77 and a titanium oxide content of 0 ppm was used in Example 3. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例8]
実施例3においてポリエステル長繊維不織布の目付が20g/m2となるように紡糸したこと以外は、実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 8]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that the polyester long fiber non-woven fabric was spun so as to have a basis weight of 20 g / m 2 in Example 3. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例9]
実施例1において紡糸速度3770m/min、ドラフト比707にて溶融紡糸し、ポリエステル長繊維の繊径が34.9μmとなるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 9]
A polyester long fiber non-woven fabric was prepared in the same manner as in Example 1 except that the polyester long fibers were melt-spun at a spinning speed of 3770 m / min and a draft ratio of 707 in Example 1 and spun so that the fiber diameter of the polyester long fibers was 34.9 μm. Obtained. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例10]
実施例2においてポリエステル長繊維不織布の目付が20g/m2となるように紡糸し、フラットロールにて全面熱圧着したこと以外は、実施例2と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 10]
A polyester long-fiber non-woven fabric was obtained in the same manner as in Example 2 except that the polyester long-fiber non-woven fabric was spun so as to have a texture of 20 g / m 2 in Example 2 and thermocompression-bonded to the entire surface with a flat roll. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例11]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が246℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4000m/min、且つ、ドラフト比942にて溶融紡糸して繊径が30.1μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付20g/m2のウェブを作製し、エンボスロールとフラットロール間において熱圧着面積率5%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 11]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 30.1 μm was obtained by melt spinning at a spinning speed of 4000 m / min and a draft ratio of 942. Next, using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] to control the air flow in a flat plate shape, the fibers are spread and dispersed to prepare a web having a grain size of 20 g / m 2 , and between the embossed roll and the flat roll. A polyester long fiber non-woven fabric was obtained by thermocompression bonding at a thermocompression bonding area ratio of 5%. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例12]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が246℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4000m/min、且つ、ドラフト比942にて溶融紡糸して繊径が30.0μmのポリエステル長繊維を得た。次に、この繊維を開繊分散して目付12g/m2のウェブを作製し、エンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 12]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 30.0 μm was obtained by melt spinning at a spinning speed of 4000 m / min and a draft ratio of 942. Next, the fibers were spread and dispersed to prepare a web having a grain size of 12 g / m 2 , and a polyester long fiber non-woven fabric was obtained by partially thermocompression bonding between the embossed roll and the flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例13]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が246℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4000m/min、且つ、ドラフト比942にて溶融紡糸して繊径が26.7μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付18g/m2のウェブを作製した。次に、チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4150m/min、且つ、ドラフト比412にて溶融紡糸して繊径が15μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付3g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 13]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A disperser [inclination angle 4 ° with respect to the filament of the flat plate] is used to open polyester filaments with a fiber diameter of 26.7 μm by melt spinning at a spinning speed of 4000 m / min and a draft ratio of 942. A web having a grain size of 18 g / m 2 was prepared by finely dispersing the fibers. Next, a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C to have a spinning hole having a circular cross section. A disperser [inclination angle 4 ° with respect to the filament of the flat plate] is used to control the flat flow of polyester filaments with a fiber diameter of 15 μm by melt spinning from the spinneret at a spinning speed of 4150 m / min and a draft ratio of 412. , A web with a grain of 3 g / m 2 was prepared by spreading and dispersing. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例14]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が246℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4000m/min、且つ、ドラフト比942にて溶融紡糸して繊径が24.6μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付10g/m2のウェブを作製した。次に、チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比895にて溶融紡糸して繊径が20μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付8g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 14]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A disperser [inclination angle 4 ° with respect to the filament of the flat plate] is used to open polyester filaments with a fiber diameter of 24.6 μm by melt spinning at a spinning speed of 4000 m / min and a draft ratio of 942. A web having a grain size of 10 g / m 2 was prepared by finely dispersing the fibers. Next, a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 254 ° C is used as a core, and a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning apparatus and melted at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 895 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 8 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 20 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例15]
実施例1においてポリエステル長繊維不織布の目付が18g/m2となるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 15]
A polyester long-fiber non-woven fabric was obtained in the same manner as in Example 1 except that the polyester long-fiber non-woven fabric was spun so as to have a basis weight of 18 g / m 2. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例16]
実施例2においてポリエステル長繊維不織布の目付が18g/m2となるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 16]
Except that the basis weight of the polyester filament non-woven fabric is spun such that the 18 g / m 2 in Example 2, to obtain a polyester long fiber nonwoven fabric in the same manner as in Example 1. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例17]
実施例3においてポリエステル長繊維不織布の目付が18g/m2となるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 17]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 1 except that the polyester long fiber non-woven fabric was spun so as to have a basis weight of 18 g / m 2 in Example 3. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

参考例18]
実施例1においてポリエステル長繊維不織布の目付が18 g/m2となるようにし、第一層目の不織布とした。その上に、IV値0.65、チタン含有量0ppm、融点217℃のPET樹脂を用いて、紡糸温度260℃、加熱空気500Nm/hr/mの条件下で紡糸し、得られた繊維径10μmのメルトブロウン不織布を上記のスパンボンド不織布上に目付5g/m2で吹き付け不織布の積層体を得た。得られた不織布の物性を以下の表1に示す。
[ Reference Example 18]
In Example 1, the polyester long fiber non-woven fabric had a basis weight of 18 g / m 2, and was used as the first-layer non-woven fabric. A PET resin having an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C. was used for spinning under the conditions of a spinning temperature of 260 ° C. and heated air of 500 Nm 3 / hr / m, and obtained a fiber diameter of 10 μm. A melt-brown non-woven fabric was sprayed onto the above-mentioned spun-bonded non-woven fabric at a meshing point of 5 g / m 2 to obtain a laminate of the non-woven fabric. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例19]
実施例2においてポリエステル長繊維不織布の目付が18 g/m2となるようにし、第一層目の不織布とした。その上に、IV値0.65、チタン含有量0ppm、融点217℃のPET樹脂を用いて、紡糸温度255℃、加熱空気400Nm/hr/mの条件下で紡糸し、得られた繊維径15μmのメルトブロウン不織布を上記のスパンボンド不織布上に目付4g/m2で吹き付け不織布の積層体を得た。得られた不織布の物性を以下の表1に示す。
[Example 19]
In Example 2, the polyester long fiber non-woven fabric had a basis weight of 18 g / m 2, and was used as the first-layer non-woven fabric. A PET resin having an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C. was used for spinning under the conditions of a spinning temperature of 255 ° C. and heated air of 400 Nm 3 / hr / m, and obtained a fiber diameter of 15 μm. A melt-brown non-woven fabric was sprayed onto the above-mentioned spun-bonded non-woven fabric at a meshing point of 4 g / m 2 to obtain a laminate of the non-woven fabric. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例20]
実施例3においてポリエステル長繊維不織布の目付が18 g/m2となるようにし、第一層目の不織布とした。その上に、IV値0.65、チタン含有量0ppm、融点217℃のPET樹脂を用いて、紡糸温度265℃、加熱空気1000Nm/hr/mの条件下で紡糸し、得られた繊維径7μmのメルトブロウン不織布を上記のスパンボンド不織布上に目付4g/m2で吹き付け不織布の積層体を得た。得られた不織布の物性を以下の表1に示す。
[Example 20]
In Example 3, the polyester long fiber non-woven fabric had a basis weight of 18 g / m 2, and was used as the first-layer non-woven fabric. A PET resin having an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C. was used for spinning under the conditions of a spinning temperature of 265 ° C. and heated air of 1000 Nm 3 / hr / m, and obtained a fiber diameter of 7 μm. A melt-brown non-woven fabric was sprayed onto the above-mentioned spun-bonded non-woven fabric at a meshing point of 4 g / m 2 to obtain a laminate of the non-woven fabric. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例21]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比230にて溶融紡糸して繊径が14μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比380にて溶融紡糸して繊径が14μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 21]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 14 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 230. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning apparatus and melted at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 380 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 14 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例22]
チタン元素含有量が12ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比590にて溶融紡糸して繊径が20.1μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比380にて溶融紡糸して繊径が14μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 22]
A polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 20.1 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 590. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning apparatus and melted at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 380 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 14 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例23]
チタン元素含有量が12ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比740にて溶融紡糸して繊径が24.6μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比380にて溶融紡糸して繊径が14μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 23]
A polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 24.6 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 740. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning apparatus and melted at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 380 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 14 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例24]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比550にて溶融紡糸して繊径が20.1μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付10g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比450にて溶融紡糸して繊径が16μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 24]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 20.1 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 550. Next, a web having a basis weight of 10 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning device to melt at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 450 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 16 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] for controlling a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例25]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比590にて溶融紡糸して繊径が20.1μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比450にて溶融紡糸して繊径が16μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 25]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 20.1 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 590. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning device to melt at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 450 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 16 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例26]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比740にて溶融紡糸して繊径が24.6μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比450にて溶融紡糸して繊径が16μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 26]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 24.6 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 740. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning device to melt at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 450 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 16 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例27]
チタン元素含有量が12ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比590にて溶融紡糸して繊径が20.1μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角0°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比450にて溶融紡糸して繊径が16μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角0°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 27]
A polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 20.1 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 590. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 0 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning device to melt at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 450 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 16 μm using a disperser [inclination angle 0 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例28]
平板状の気流を制御する分散装置の平板のフィラメントに対する傾斜角を0°としたこと以外は実施例22と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[Example 28]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 22 except that the inclination angle of the flat plate of the disperser for controlling the flat air flow with respect to the filament was set to 0 °. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

[実施例29]
低融点樹脂を用いた層を鞘芯構造からサイドバイサイド構造としたこと以外は実施例21と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 29]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 21 except that the layer using the low melting point resin was changed from a sheath core structure to a side-by-side structure. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例30]
低融点樹脂を用いた層を鞘芯構造からサイドバイサイド構造としたこと以外は実施例24と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 30]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 24 except that the layer using the low melting point resin was changed from a sheath core structure to a side-by-side structure. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例31]
低融点樹脂を用いた層を鞘芯構造からサイドバイサイド構造としたこと以外は実施例22と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 31]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 22 except that the layer using the low melting point resin was changed from a sheath core structure to a side-by-side structure. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例32]
各層の目付を6g/m2としたこと以外は実施例21と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 32]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 21 except that the basis weight of each layer was 6 g / m 2. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例33]
各層の目付を6g/m2としたこと以外は実施例22と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 33]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 22 except that the basis weight of each layer was 6 g / m 2. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例34]
各層の目付を6g/m2としたこと以外は実施例23と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 34]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 23 except that the basis weight of each layer was 6 g / m 2. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例35]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比590にて溶融紡糸して繊径が20.1μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付12g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比450にて溶融紡糸して繊径が16μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付6g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 35]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 275 ° C. A polyester filament having a fiber diameter of 20.1 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 590. Next, a web having a basis weight of 12 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning device to melt at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 450 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 6 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 16 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例36]
各層の目付を9g/m2としたこと以外は実施例25と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 36]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 25 except that the basis weight of each layer was 9 g / m 2. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

参考例37]
各層の目付を9g/m2としたこと以外は実施例21と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表1に示す。
[ Reference Example 37]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 21 except that the basis weight of each layer was 9 g / m 2. The physical characteristics of the obtained non-woven fabric are shown in Table 1 below.

参考例38]
チタン元素含有量が12ppm、固有粘度(IV)が0.8、融点が247℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して305℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比230にて溶融紡糸して繊径が10μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。次に、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/min、且つ、ドラフト比380にて溶融紡糸して繊径が14μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付7.5g/m2のウェブを作製した。2層のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[ Reference Example 38]
A polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning device and melted at 305 ° C. A polyester filament having a fiber diameter of 10 μm was obtained by melt spinning at a spinning speed of 4500 m / min and a draft ratio of 230. Next, a web having a basis weight of 7.5 g / m 2 was prepared by spreading and dispersing the fibers using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. Next, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The polyester-based resin is used as a sheath and is supplied to a conventional melt-spinning apparatus and melted at 275 ° C., and spin-spun at a spinning speed of 4500 m / min and a draft ratio of 380 from a spinneret having a spinning hole with a circular cross section. A web having a grain size of 7.5 g / m 2 was prepared by spreading and dispersing polyester filaments having a fiber diameter of 14 μm using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] that controls a flat air flow. A polyester long fiber non-woven fabric was obtained by partially thermocompression bonding a two-layer web between an embossed roll and a flat roll at a thermocompression bonding area ratio of 15%. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[実施例39]
各層の繊維径を13μmとしたこと以外は実施例32と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表2に示す。
[Example 39]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 32 except that the fiber diameter of each layer was 13 μm. The physical characteristics of the obtained non-woven fabric are shown in Table 2 below.

[比較例1]
実施例1においてポリエステル系樹脂のチタン元素含有量を3000ppmとし、ポリエステル長繊維の目付が20.0g/m2となるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得たが、不織布の透明性が低く、食品用フィルターとして十分な透明性を得ることができなかった。得られた不織布の物性を以下の表3に示す。
[Comparative Example 1]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 1 except that the polyester resin had a titanium element content of 3000 ppm and was spun so that the polyester filament had a texture of 20.0 g / m 2. However, the transparency of the non-woven fabric was low, and sufficient transparency could not be obtained as a food filter. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例2]
実施例1においてドラフト比545で溶融紡糸したポリエステル長繊維の繊径を12.0μmとし、ポリエステル長繊維の目付が20g/m2となるように紡糸したこと以外は、実施例1と同様にしてポリエステル長繊維不織布を得たが、不織布の透明性が低く、食品用フィルターとして十分な透明性を得ることができなかった。得られた不織布の物性を以下の表3に示す。
[Comparative Example 2]
Polyester in the same manner as in Example 1 except that the fiber diameter of the polyester filaments melt-spun at a draft ratio of 545 was set to 12.0 μm and the polyester filaments were spun so as to have a grain size of 20 g / m 2. A long-fiber non-woven fabric was obtained, but the transparency of the non-woven fabric was low, and sufficient transparency could not be obtained as a food filter. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例3]
チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が253℃であるポリエステル系樹脂を用いたこと以外は実施例1と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 3]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 1 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 253 ° C. was used. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例4]
チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が253℃であるポリエステル系樹脂を用いたこと以外は実施例2と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 4]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 2 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 253 ° C. was used. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例5]
チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が253℃であるポリエステル系樹脂を用いたこと以外は実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 5]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 253 ° C. was used. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例6]
チタン元素含有量が12ppm、固有粘度(IV)が0.65、融点が253℃であるポリエステル系樹脂を用いたこと以外は実施例4と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 6]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 4 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 253 ° C. was used. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例7]
チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が253℃であるポリエステル系樹脂を用いたこと以外は実施例3と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 7]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 253 ° C. was used. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例8]
チタン元素含有量が0ppm、固有粘度(IV)が0.8、融点が246℃であるポリエステル系樹脂を常用の溶融紡糸装置に供給して295℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4000m/min、且つ、ドラフト比191にて溶融紡糸して繊径が30.3μmのポリエステル長繊維を得た。次に、この繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付20/m2のウェブを作製し、エンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得たが、食品用フィルターとして十分な寸法安定性を得ることができなかった。得られた不織布の物性を以下の表3に示す。
[Comparative Example 8]
A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning device and melted at 295 ° C. A polyester filament having a fiber diameter of 30.3 μm was obtained by melt spinning at a spinning speed of 4000 m / min and a draft ratio of 191. Next, using a disperser [inclination angle 4 ° with respect to the filament of the flat plate] to control the air flow in a flat plate shape, the fibers are spread and dispersed to prepare a web with a grain size of 20 / m 2 , and between the embossing roll and the flat roll. A polyester long fiber non-woven fabric was obtained by thermocompression bonding at a thermocompression bonding area ratio of 15%, but sufficient dimensional stability could not be obtained as a food filter. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例9]
比較例8においてドラフト比345で溶融紡糸したポリエステル長繊維の繊径を50.0μmとし、ポリエステル長繊維の目付が20g/m2となるように紡糸したが、ロールでの収縮が大きく、ポリエステル長繊維不織布を得ることができなかった。得られた不織布の物性を以下の表3に示す。
[Comparative Example 9]
In Comparative Example 8, the fiber diameter of the polyester filaments melt-spun at a draft ratio of 345 was set to 50.0 μm, and the polyester filaments were spun so that the grain size was 20 g / m 2 , but the shrinkage on the roll was large and the polyester filaments were spun. The non-woven fabric could not be obtained. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例10]
実施例3においてポリエステル長繊維の目付が40g/m2となるようにウェブを作製したこと以外は、実施例3と同様にしてポリエステル長繊維不織布を得たが、不織布の透明性が低く、食品用フィルターとして十分な透明性を得ることができなかった。得られた不織布の物性を以下の表3に示す。
[Comparative Example 10]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 3 except that the web was prepared so that the grain size of the polyester long fibers was 40 g / m 2 in Example 3, but the transparency of the non-woven fabric was low and the food was prepared. Sufficient transparency could not be obtained as a filter. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例11]
樹脂のチタン含有量を3000ppmとした以外は実施例21と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 11]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 21 except that the titanium content of the resin was 3000 ppm. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例12]
樹脂のIV値を0.7とした以外は比較例11と同様にしてポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。
[Comparative Example 12]
A polyester long fiber non-woven fabric was obtained in the same manner as in Comparative Example 11 except that the IV value of the resin was 0.7. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below.

[比較例13]
チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が254℃であるポリエステル系樹脂を芯とし、チタン元素含有量が0ppm、固有粘度(IV)が0.65、融点が217℃であるポリエステル系樹脂を鞘として、常用の溶融紡糸装置に供給して275℃で溶融し、円形断面の紡糸孔を有する紡糸口金から紡糸速度4500m/minにて溶融紡糸して繊径が14μmのポリエステル長繊維を平板状の気流を制御する分散装置〔平板のフィラメントに対する傾斜角4°〕を用い、開繊分散して目付15g/m2のウェブをエンボスロールとフラットロール間において熱圧着面積率15%で部分熱圧着することによりポリエステル長繊維不織布を得た。得られた不織布の物性を以下の表3に示す。尚、得られた不織布のヒートシールした際に、シーラーに激しく樹脂汚れが発生した。
[Comparative Example 13]
A polyester-based resin with a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C is used as a core, and a polyester having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. A polyester filament with a fiber diameter of 14 μm is melt-spun at a spinning speed of 4500 m / min from a spinneret having a spinning hole with a circular cross section by supplying the based resin as a sheath to a conventional melt-spinning device and melting at 275 ° C. Using a disperser that controls the flat air flow [inclination angle 4 ° with respect to the filament of the flat plate], spread the fibers and disperse the web with a grain size of 15 g / m 2 between the embossed roll and the flat roll with a thermal pressure bonding area ratio of 15%. A polyester long fiber non-woven fabric was obtained by partial heat crimping. The physical characteristics of the obtained non-woven fabric are shown in Table 3 below. When the obtained non-woven fabric was heat-sealed, resin stains were severely generated on the sealer.

[比較例14]
各層の目付を10g/m2としたこと以外は実施例21と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を表3に示す。
[Comparative example 14]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 21 except that the basis weight of each layer was 10 g / m 2. Table 3 shows the physical characteristics of the obtained non-woven fabric.

[比較例15]
各層の目付を4g/m2としたこと以外は実施例26と同様の方法でポリエステル長繊維不織布を得た。得られた不織布の物性を表3に示す。
[Comparative example 15]
A polyester long fiber non-woven fabric was obtained in the same manner as in Example 26 except that the basis weight of each layer was 4 g / m 2. Table 3 shows the physical characteristics of the obtained non-woven fabric.

Figure 0006898482
Figure 0006898482

Figure 0006898482
Figure 0006898482

Figure 0006898482
Figure 0006898482

本発明の単層又は複層ポリエステル長繊維不織布は透明性、寸法安定性、粉漏れ性、及び成分抽出性に優れるため、食品用フィルターとして好適に利用可能である。 The single-layer or multi-layer polyester long-fiber non-woven fabric of the present invention is excellent in transparency, dimensional stability, powder leakage property, and component extractability, and therefore can be suitably used as a food filter.

Claims (16)

無機系粒子の含有量が0〜100ppmであり、10%点孔径が1000μm未満であり、10%点孔径と2.3%点孔径の差が500μm以下であり、目付が10〜30g/m2であり、不織布の面積当たりの表面積が、1.0〜3.25m2/m2であり、かつ、地合係数が0.5〜2.0であることを特徴とする、単層又は複層ポリエステル長繊維不織布。 The content of inorganic particles is 0 to 100 ppm, the 10% point pore size is less than 1000 μm, the difference between the 10% point hole diameter and the 2.3% point hole diameter is 500 μm or less, and the grain size is 10 to 30 g / m 2 . A single-layer or multi-layer polyester long-fiber non-woven fabric, characterized in that the surface area per area of the non-woven fabric is 1.0 to 3.25 m 2 / m 2 and the formation coefficient is 0.5 to 2.0. 熱圧着面積率が5〜40%であり、且つ、平均見掛け密度が0.1〜0.5g/cm3である、請求項1に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to claim 1, wherein the thermocompression bonding area ratio is 5 to 40% and the average apparent density is 0.1 to 0.5 g / cm 3. 平均繊維径が13〜40μmである、請求項1又は2に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to claim 1 or 2, wherein the average fiber diameter is 13 to 40 μm. 少なくとも1層がラマンスペクトルにおいて観測される1740cm-1付近のC=O基によるピーク巾の半値全幅の平均値が18〜24cm-1の繊維で構成される、請求項1〜3のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The average value of the full width at half maximum of the peak width by C = O groups in the vicinity of 1740 cm -1 of at least one layer is observed in the Raman spectra is constituted by fibers of 18~24cm -1, one of claims 1 to 3 1 The single-layer or multi-layer polyester long fiber non-woven fabric according to the item. 少なくとも1層が、結晶化度が30〜50%である繊維から構成される、請求項1〜4のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 4, wherein at least one layer is composed of fibers having a crystallinity of 30 to 50%. 少なくとも1層が、複屈折率0.04〜0.12の繊維で構成される、請求項1〜5のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 5, wherein at least one layer is composed of fibers having a birefringence of 0.04 to 0.12. 透明性が65%以上である、請求項1〜6のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 6, which has a transparency of 65% or more. 沸水収縮率が2.0%以下である、請求項1〜7のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 7, wherein the boiling water shrinkage rate is 2.0% or less. 少なくとも1層の引張強度が5N/30mm以上である、請求項1〜8のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 8, wherein the tensile strength of at least one layer is 5 N / 30 mm or more. 少なくとも1層が融点240℃以下の低融点繊維を含有する、請求項1〜9のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 9, wherein at least one layer contains low melting point fibers having a melting point of 240 ° C. or lower. 前記ポリエステル長繊維不織布の繊維の配向性が断面方向に異なる構造をもつ、請求項1〜10のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 10, which has a structure in which the orientation of the fibers of the polyester long-fiber non-woven fabric is different in the cross-sectional direction. 少なくとも1層がイソフタル酸を0〜25%含む樹脂からなる、請求項1〜11のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 11, wherein at least one layer is made of a resin containing 0 to 25% of isophthalic acid. 前記無機系粒子が酸化チタンである、請求項1〜12のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 12, wherein the inorganic particles are titanium oxide. チタン元素含有量0〜0.1ppmの樹脂からなる、請求項13に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to claim 13, which comprises a resin having a titanium element content of 0 to 0.1 ppm. 不織布とした後の樹脂のIV値が0.6以上である、請求項1〜14のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 14, wherein the IV value of the resin after forming the non-woven fabric is 0.6 or more. 請求項1〜15のいずれか1項に記載の単層又は複層ポリエステル長繊維不織布からなる食品用フィルター。 A food filter made of a single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 15.
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