JP4852374B2 - Separating polyester filament and palatable beverage extraction filter obtained therefrom - Google Patents
Separating polyester filament and palatable beverage extraction filter obtained therefrom Download PDFInfo
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- JP4852374B2 JP4852374B2 JP2006223199A JP2006223199A JP4852374B2 JP 4852374 B2 JP4852374 B2 JP 4852374B2 JP 2006223199 A JP2006223199 A JP 2006223199A JP 2006223199 A JP2006223199 A JP 2006223199A JP 4852374 B2 JP4852374 B2 JP 4852374B2
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- 238000000605 extraction Methods 0.000 title claims description 58
- 229920000728 polyester Polymers 0.000 title claims description 44
- 235000013361 beverage Nutrition 0.000 title claims description 32
- 239000000835 fiber Substances 0.000 claims description 51
- 239000002759 woven fabric Substances 0.000 claims description 17
- 238000002844 melting Methods 0.000 claims description 14
- 230000008018 melting Effects 0.000 claims description 14
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 claims description 12
- 229910052751 metal Inorganic materials 0.000 claims description 11
- 229920000642 polymer Polymers 0.000 claims description 11
- 230000005484 gravity Effects 0.000 claims description 9
- 239000010936 titanium Substances 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 8
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 229910052698 phosphorus Inorganic materials 0.000 claims description 6
- 239000011574 phosphorus Substances 0.000 claims description 6
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- MMINFSMURORWKH-UHFFFAOYSA-N 3,6-dioxabicyclo[6.2.2]dodeca-1(10),8,11-triene-2,7-dione Chemical group O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-UHFFFAOYSA-N 0.000 claims description 3
- 229920001634 Copolyester Polymers 0.000 claims description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000003786 synthesis reaction Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 description 22
- 238000007789 sealing Methods 0.000 description 16
- 244000269722 Thea sinensis Species 0.000 description 11
- 235000019629 palatability Nutrition 0.000 description 11
- -1 polypropylene Polymers 0.000 description 11
- 239000004744 fabric Substances 0.000 description 10
- 229920001778 nylon Polymers 0.000 description 9
- 239000008188 pellet Substances 0.000 description 6
- 235000006468 Thea sinensis Nutrition 0.000 description 5
- 235000020279 black tea Nutrition 0.000 description 5
- 235000013616 tea Nutrition 0.000 description 5
- 239000004753 textile Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 4
- 229920000139 polyethylene terephthalate Polymers 0.000 description 4
- 239000005020 polyethylene terephthalate Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000004677 Nylon Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical compound OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 description 2
- 239000002685 polymerization catalyst Substances 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- 150000003609 titanium compounds Chemical class 0.000 description 2
- GGUBFICZYGKNTD-UHFFFAOYSA-N triethyl phosphonoacetate Chemical compound CCOC(=O)CP(=O)(OCC)OCC GGUBFICZYGKNTD-UHFFFAOYSA-N 0.000 description 2
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 2
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000006081 fluorescent whitening agent Substances 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 235000009569 green tea Nutrition 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Artificial Filaments (AREA)
- Woven Fabrics (AREA)
Description
本発明は嗜好性飲料抽出フィルター用に適したポリエステルフィラメント及びそれを用いた嗜好性飲料抽出フィルターに関する。特に、ポリエステル製造用触媒として比重5g/cm3以上の重金属を実質的に含まないポリエステルであってポリマー成分の20モル%以下の割合でイソフタル酸等が共重合されており、融点が200℃〜240℃の範囲にある異形断面フィラメントであって、分繊後のモノフィラメントが嗜好性飲料抽出フィルターとしての安全性に優れ、織物での成形性に優れた嗜好性飲料抽出フィルターとなし得るポリエステルフィラメント、並びに、該モノフィラメントからなる嗜好性飲料抽出フィルターに関する。 The present invention relates to a polyester filament suitable for a palatable beverage extraction filter and a palatable beverage extraction filter using the same. In particular, it is a polyester that does not substantially contain a heavy metal having a specific gravity of 5 g / cm 3 or more as a catalyst for producing polyester, and is copolymerized with isophthalic acid or the like at a ratio of 20 mol% or less of the polymer component, and has a melting point of 200 ° C. to Polyester filament that is an irregular cross-section filament in the range of 240 ° C., and the monofilament after splitting is excellent in safety as a palatability beverage extraction filter, and can be used as a palatability beverage extraction filter excellent in moldability in fabrics, The present invention also relates to a palatable beverage extraction filter comprising the monofilament.
従来、嗜好性飲料抽出フィルター、特に紅茶等に使用される嗜好性飲料抽出フィルターは紙やポリプロピレン又はポリエチレンの不織布が主流として用いられているが、近年の傾向としては、嗜好性飲料抽出バッグ中の紅茶等の茶葉が見える高級感嗜好品として織物製の嗜好性飲料抽出バッグの要求が増えてきている。かかる織物の構成としては嗜好性飲料抽出バッグ中の紅茶等の茶葉が見え易く、中の茶葉が外に出ないという目的から、モノフィラメントを平織りにしたシャー織物が主流である。 Conventionally, palatable beverage extraction filters, particularly palatable beverage extraction filters used for black tea and the like, are mainly used for paper, polypropylene or polyethylene nonwoven fabrics. There is an increasing demand for a taste-extracting beverage extraction bag made of textiles as a luxury taste product that can see tea leaves such as black tea. As the structure of such a woven fabric, for the purpose of easily seeing tea leaves such as black tea in the palatable beverage extraction bag and preventing the tea leaves inside from coming out, a shear woven fabric with monofilaments made into a plain weave is the mainstream.
織物の嗜好性飲料抽出バッグに用いられる嗜好性飲料抽出フィルターの素材繊維としてはナイロンが主流であり、ナイロン繊維からなる抽出用フィルター或いは抽出用バッグは立体形状の保持性に優れ、また変形した場合の弾性回復力にも富んでおり、織物の柔らかさの点での風合いに優れている。しかし、ナイロン繊維からなる抽出用バッグは熱湯中でのナイロン繊維の膨潤による抽出用バッグの寸法変化や嗜好性飲料成分の吸収による色調変化、抽出後容器からナイロン抽出バッグを取り出す際の液切れが悪い事、また、ナイロンの比重の関係で熱湯中での抽出用バッグの沈降性に劣る事等の問題が以前から指摘されていた。 Nylon is the mainstream material fiber for palatable beverage extraction filters used in palatable beverage extraction bags for textiles, and the filter or extraction bag made of nylon fibers has excellent three-dimensional shape retention and is deformed It is also rich in elastic resilience and has an excellent texture in terms of the softness of the fabric. However, an extraction bag made of nylon fiber has a dimensional change due to swelling of the nylon fiber in boiling water, a color change due to absorption of a taste beverage component, and liquid drainage when the nylon extraction bag is taken out from the container after extraction. It has been pointed out before that problems such as badness and inferior settling properties of the extraction bag in hot water due to the specific gravity of nylon.
このようなナイロン繊維の問題点を改善する目的で、ポリエステル繊維による嗜好性飲料抽出フィルター等が研究されてきており、特許第3459951号では融点差が100℃以上ある芯・鞘2重構造を有するポリエステル系繊維からなる織物の嗜好性飲料抽出フィルターが提案されている。しかしながら、該技術ではポリエステル繊維中にポリエステル製造用触媒として用いられる金属触媒については考慮されておらず、ポリエステル繊維による嗜好性飲料抽出フィルターの環境安全性が求められている。
本発明の主たる目的は、嗜好性飲料抽出フィルターとしての安全性に優れ、織物での成形性に優れた嗜好性飲料抽出フィルター用モノポリエステルフィラメントとなし得る分繊用マルチフィラマントを提供することにある。本発明の他の目的は、該マルチフィラメントを分繊した嗜好性飲料抽出フィルター用のモノフィラメントを提供することにあり、さらなる目的は、該モノフィラメントの織物からなる嗜好性飲料抽出フィルターを提供することにある。 The main object of the present invention is to provide a multifilament for splitting that can be made as a monopolyester filament for a taste-extracting beverage extraction filter that is excellent in safety as a taste-extracting beverage extraction filter and excellent in moldability in textiles. is there. Another object of the present invention is to provide a monofilament for a tasteful beverage extraction filter obtained by splitting the multifilament, and a further object is to provide a tasteful beverage extraction filter made of a woven fabric of the monofilament. is there.
本発明者らは上記従来技術に鑑み鋭意検討を重ねた結果、本発明の、嗜好性飲料抽出フィルター用として好適な分繊用マルチフィラメント、それを分繊した嗜好性飲料抽出フィルター用モノフィラメント、ならびに、それを用いた嗜好性飲料抽出フィルターを完成するに至った。 As a result of intensive studies in view of the above-described conventional techniques, the inventors of the present invention have a multifilament suitable for use as a taste-extracting beverage extraction filter according to the present invention, a monofilament for taste-satisfying beverage extraction filter obtained by separating the multifilament, and And it came to complete the palatability drink extraction filter using it.
すなわち、本発明の分繊用マルチフィラメントは、繊維を構成するポリマー繰り返し単位の80モル以上%がエチレンテレフタレート単位であり、全酸成分の5〜20モル%の割合でイソフタル酸が共重合された共重合ポリエステルで構成され、真比重5.0以上の金属元素の含有量が0.5重量ppm以下であるポリエステルで構成されたマルチフィラメントであって、かつ、下記(1)〜(5)の条件を同時に満足することを特徴とする嗜好性飲料抽出フィルター用として好適な分繊用ポリエステルマルチフィラメントである。
(1)繊維断面が扁平であること
(2)伸度が20〜40%であること
(3)単糸繊度が10〜40デシテックスであること
(4)フィラメント数が4本以上20本以下であること
(5)繊維の融点が200〜240℃の範囲にあること
That is, minute繊用multifilament of the present invention, 80 mol% of the polymer repeating units constituting the fibers Ri ethylene terephthalate units der, isophthalic acid is copolymerized at a ratio of 5 to 20 mole percent of total acid component A multifilament made of polyester having a true specific gravity of 5.0 or more and a metal element content of 0.5 ppm by weight or less, and the following (1) to ( 5 ) It is a polyester multifilament for splitting suitable for use in a palatable beverage extraction filter characterized by satisfying the above conditions simultaneously.
(1) The fiber cross section is flat (2) The elongation is 20 to 40% (3) The single yarn fineness is 10 to 40 dtex (4) The number of filaments is 4 or more and 20 or less There is
(5) Melting | fusing point of a fiber exists in the range of 200-240 degreeC.
さらに、本発明の分繊用ポリエステルマルチフィラメントは、繊維断面おける扁平形状が、長軸方向に丸断面単糸の3〜6個が直線状に接合したような形状を有し、扁平断面繊維の最大径の長さA(長軸)と該長軸に直交する最大径の長さB(短軸)の比、すなわち扁平度A/Bが3〜6であるものが好適である。 Furthermore, the polyester multifilament for splitting of the present invention has a shape in which the flat shape in the fiber cross section is such that 3-6 pieces of the round cross section single yarn are linearly joined in the long axis direction, The ratio of the maximum diameter length A (major axis) to the maximum diameter length B (minor axis) orthogonal to the major axis, that is, the flatness A / B is preferably 3-6.
そして、該分繊用ポリエステルマルチフィラメントを構成する共重合ポリエステルが、その合成時に、下記一般式(I)で表されるホスホネート化合物を使用し、
また、本発明の嗜好性飲料抽出フィルター用モノフィラメントは、上記の如き本発明の分繊用ポリエステルマルチフィラメントを分繊して得られた嗜好性飲料抽出フィルター用ポリエスモノテルフィラメントである。
そして、嗜好性飲料抽出フィルターは、上記のポリエステルモノフィラメントを少なくとも経糸又は緯糸のいずれか一方として含む織物からなる嗜好性飲料抽出フィルターである。
Moreover, the monofilament for palatability | flavor extraction filters of this invention is the polyester monotel filament for palatability | flavor extraction filters obtained by splitting the polyester multifilament for the segregation of the present invention as mentioned above.
And a palatability drink extraction filter is a palatability drink extraction filter which consists of textiles which contain the above-mentioned polyester monofilament as at least one of a warp or a weft.
かかる本発明によれば、嗜好性飲料抽出フィルターとしての環境安全性に優れ、織物での抽出バッグの成形性、風合等にも優れた嗜好性飲料抽出フィルター用ポリエステルフィラメントを提供することが出来る。 According to the present invention, it is possible to provide a polyester filament for a palatability beverage extraction filter which is excellent in environmental safety as a palatability beverage extraction filter and excellent in moldability and texture of an extraction bag made of fabric. .
本発明の分繊用ポリエステルマルチフィラメント及びそれを分繊して得られたモノフィラメントでは、繊維を構成するポリマーが、少なくとも80モル%以上がエチレンテレフタレート単位で構成され、かつ、20モル%以下の割合で他のポリマー繰り返し単位を含むPET系共重合ポリエステルであって、真比重5.0以上の金属元素の含有量が0〜0.5重量ppmであることが必要である。 In the polyester multifilament for splitting of the present invention and the monofilament obtained by splitting it, the polymer constituting the fiber is composed of at least 80 mol% of ethylene terephthalate units and a proportion of 20 mol% or less. In addition, it is necessary that the PET copolymer polyester containing other polymer repeating units has a metal element content of true specific gravity of 5.0 or more of 0 to 0.5 ppm by weight.
さらに具体的には、比重5.0以上の金属元素、特にアンチモン、ゲルマニウム等の含有量が0.5重量ppm以下と極めて少ないことが環境安全性の観点から重要であり、このため、該ポリエステル製造用の触媒としてはトリメリット酸チタンが好適に用いられる。さらに、リン化合物として、下記一般式(I)で表されるホスホネート化合物を使用し、
本発明のマルチフィラメントでは、繊維形成ポリマーとして、ポリエチレンテレフタレート(PET)系の共重合ポリエステルを使用するが、中でも、ポリマーを構成する全酸成分の5〜20モル%の割合でイソフタル酸が共重合されており、融点が200〜240℃の範囲にある共重合ポリエステルが必要である。 In the multifilament of the present invention, a polyethylene terephthalate (PET) copolymer polyester is used as a fiber-forming polymer. Among them, isophthalic acid is copolymerized in a proportion of 5 to 20 mol% of all acid components constituting the polymer. And a copolyester having a melting point in the range of 200 to 240 ° C. is required .
ホモポリエステル繊維(融点255〜260℃)からなるフィルターは、ナイロン繊維からなるフィルターと比べて織物での抽出用バッグを形成する際に用いられる超音波シール法やヒートシール法による溶着性が乏しく、また、一旦溶着しても剥離し易い難点があり、これが従来この分野でポリエステル繊維が多く使用されていない理由でもあった。しかし、繊維の融点が200〜240℃の範囲になるようイソフタル酸を上記の割合で共重合させたポリエチレンテレフタレート系繊維では、超音波シール法等による加工性がナイロン繊維とほぼ同程度まで高く出来る。ただし、繊維の融点が240℃を超える場合は、超音波シール法やヒートシール法による溶着性が乏しく、また、一旦溶着しても剥離し易いため、抽出バックを形成する際のシール部にて糸の解れが発生するため抽出用バッグとして使用に適さない。一方、融点が220℃未満の場合は、超音波シール法やヒートシール法等による溶着性は高く、一旦溶着した後も剥離し難いが、繊維の強度が弱く、分繊工程での糸切れが多くなり工程通過性が悪くなる。したがって、繊維の融点は200〜240℃がよく、特に200〜220℃が好ましい。 A filter made of a homopolyester fiber (melting point: 255 to 260 ° C.) has poor weldability by an ultrasonic sealing method or a heat sealing method used when forming an extraction bag with a woven fabric, compared to a filter made of nylon fiber. In addition, there is a difficulty in easily peeling once welded, and this is also the reason why many polyester fibers have not been used in this field. However, polyethylene terephthalate fiber in which isophthalic acid is copolymerized in the above proportion so that the melting point of the fiber is in the range of 200 to 240 ° C. can be processed to the same extent as nylon fiber by the ultrasonic sealing method. . However, when the melting point of the fiber exceeds 240 ° C., the weldability by the ultrasonic sealing method or the heat sealing method is poor, and it is easy to peel off even once welded. Since unwinding of the yarn occurs, it is not suitable for use as an extraction bag. On the other hand, when the melting point is less than 220 ° C., the weldability by the ultrasonic sealing method or the heat sealing method is high, and it is difficult to peel off even after being once welded, but the strength of the fiber is weak, and the yarn breakage in the fiber separation process Increases the process passability. Therefore, the melting point of the fiber is preferably 200 to 240 ° C, particularly preferably 200 to 220 ° C.
また、本発明の分繊用マルチフィラメントにあっては、繊度、物性もまた重要である。まず、伸度が20〜40%の範囲内にあることが必要であり、中でも25〜35%が好ましい。伸度が20%を下回ると紡糸工程での糸切れや分繊工程での糸切れが多くなり工程通過性が悪くなる。また、伸度が40%を上回ると延伸斑による未延伸部分が発生し、その部分が濃染化されることにより染め品位が著しく低下する。 In the multifilament for splitting of the present invention, the fineness and physical properties are also important. First, it is necessary that the elongation is in the range of 20 to 40%, and preferably 25 to 35%. If the elongation is less than 20%, the yarn breakage in the spinning process and the yarn breakage in the splitting process increase, and the process passability deteriorates. On the other hand, when the elongation exceeds 40%, an unstretched portion due to stretch spots is generated, and the dyeing quality is remarkably lowered by deepening the portion.
さらに、本発明により製造される分繊用ポリエステルマルチフィラメントの分繊後の単糸繊度は10〜40デシテックスであることが必要であり、20〜30デシテックスが好ましい。単糸繊度が上記の下限よりも小さくなると分繊が難しくなり、逆に上限より大きくなると巻き取り中にパッケージの型崩れや綾外れが発生して工程通過性が著しく悪くなる。また、マルチフィラメント糸の単糸数は4〜20本、特に4〜10本、であることが分繊性及び分繊工程での工程通過性を確保する観点から好ましい。 Further, the single yarn fineness after splitting of the polyester multifilament for splitting manufactured according to the present invention needs to be 10 to 40 dtex, and preferably 20 to 30 dtex. If the single yarn fineness is smaller than the above lower limit, it becomes difficult to separate the fibers, and conversely, if the single yarn fineness is larger than the upper limit, the package loses its shape or goes out during winding and the process passability is remarkably deteriorated. In addition, the number of single filaments of the multifilament yarn is preferably 4 to 20, particularly 4 to 10 from the viewpoint of securing the separation property and the process passability in the separation step.
本発明においては、各単糸(単繊維)の断面は、扁平断面であって、その扁平形状が、長軸方向に丸断面単糸の3〜6個が直線状に接合したような形状を有するのが好ましい。図2にこのような扁平断面形状の一例を示す。上記の扁平断面繊維では、断面の最大径の長さA(長軸)と該長軸に直交する最大径の長さB(短軸)の比で表される扁平度A/Bが3〜6であることが特に好ましい。本発明では、このような特異な繊維断面形状にすることにより、織物での経糸と緯糸の交点の部分における繊維断面の接触点が、丸断面(円形断面)繊維の場合より多くなり、織物での抽出用バッグを形成する際に用いられる超音波シール法やヒートシール法による溶着性が向上する。また、通常のポリエステル繊維からなる織物等に較べて著しく柔らかくなりまた風合いも優れるため、嗜好性飲料抽出フィルター又は抽出バッグに適した物性を有する。さらに、この扁平断面繊維からなる織物は、丸断面繊維と同じ織物密度構成であっても丸断面繊維の織物に比べ、織物での目開き(メッシュ)が小さく、これにより嗜好性飲料抽出フィルターの性能が向上する。しかも、抽出バッグの中にある紅茶等の茶葉が熱湯中にこぼれ難いという効果が見られる。 In the present invention, the cross-section of each single yarn (single fiber) is a flat cross-section, and the flat shape is a shape such that 3 to 6 round cross-section single yarns are joined linearly in the long axis direction. It is preferable to have. FIG. 2 shows an example of such a flat cross-sectional shape. In the above-mentioned flat cross-section fiber, the flatness A / B represented by the ratio of the length A (long axis) of the maximum diameter of the cross section to the length B (short axis) of the maximum diameter orthogonal to the long axis is 3 to 3. 6 is particularly preferred. In the present invention, by making such a unique fiber cross-sectional shape, the number of contact points of the fiber cross section at the intersection of the warp and weft in the woven fabric becomes larger than that in the case of a round cross-section (circular cross-section) fiber. The weldability by the ultrasonic sealing method and the heat sealing method used when forming the extraction bag is improved. In addition, since it is remarkably softer than fabrics made of ordinary polyester fibers and has an excellent texture, it has physical properties suitable for palatable beverage extraction filters or extraction bags. Furthermore, the woven fabric composed of flat cross-section fibers has a smaller mesh opening than the woven fabric of the round cross-section fibers even with the same fabric density configuration as the round cross-section fibers. Performance is improved. In addition, there is an effect that tea leaves such as black tea in the extraction bag are hardly spilled into hot water.
本発明におけるマルチフィラメントを構成するポリエステルの固有粘度(ο−クロロフェノール、35℃で測定)は0.40〜0.80の範囲にあることが好ましく、さらに0.45〜0.75、特に0.50〜0.70、の範囲が好適である。固有粘度が0.40未満であると、繊維の強度が不足するため好ましくない。他方、固有粘度が0.80を超えると、原料ポリマーの固有粘度を過剰に引き上げる必要があるため不経済である。 The intrinsic viscosity (ο-chlorophenol, measured at 35 ° C.) of the polyester constituting the multifilament in the present invention is preferably in the range of 0.40 to 0.80, more preferably 0.45 to 0.75, particularly 0. A range of .50 to 0.70 is preferred. An intrinsic viscosity of less than 0.40 is not preferable because the strength of the fiber is insufficient. On the other hand, if the intrinsic viscosity exceeds 0.80, it is uneconomical because it is necessary to excessively increase the intrinsic viscosity of the raw material polymer.
本発明におけるポリエステルマルチフィラメントは、必要に応じて、繊維中に少量の添加剤、例えば滑剤、顔料、染料、酸化防止剤、固相重合促進剤、蛍光増白剤、帯電防止剤、抗菌剤、紫外線吸収剤、光安定剤、熱安定剤、遮光剤、艶消剤等を含んでいてもよい。 The polyester multifilament in the present invention, if necessary, a small amount of additives in the fiber, such as lubricants, pigments, dyes, antioxidants, solid phase polymerization accelerators, fluorescent whitening agents, antistatic agents, antibacterial agents, An ultraviolet absorber, a light stabilizer, a heat stabilizer, a light-shielding agent, a matting agent, and the like may be included.
また、本発明に係る嗜好性飲料抽出フィルター用モノフィラメントは、上記の如きポリエステルマルチフィラメントを従来公知の方法で分繊したものであり、したがって、その繊度は単糸繊度が10〜40デシテックスである。この際、上記の分繊用マルチフィラメントは、フラットヤーンのままで分繊してもよく、仮撚加工後に分繊してもよい。このように分繊したモノフィラメントを経糸又は緯糸あるいはその両方に用いて製織して織物として嗜好性飲料抽出フィルターとして好適に使用することができる。また、必要に応じ、これをバックに成形することで、良好な嗜好性飲料抽出バッグとすることができる。いずれの場合も、得られたモノフィラメントからなる織物は、紅茶、緑茶、その他の嗜好飲料用のフィルターとして有用であるが、特に経糸に丸(円形)断面繊維を用い、緯糸に上記の扁平断面繊維を用いた織物構成にするのが好ましい。織物の組織としては一般に平織物が適当であるが、綾織物やその他の組織であっても構わない。得られた織物を適当なサイズに裁断して所定部分を超音波シール、ヒートシール等の方法で融着させることで、袋状とすることもできる。 Moreover, the monofilament for palatability | flavor extraction filter which concerns on this invention is what divided the polyester multifilaments as mentioned above by a conventionally well-known method, Therefore, the fineness is a single yarn fineness of 10-40 decitex. At this time, the multifilament for splitting may be split with a flat yarn as it is, or may be split after false twisting. The monofilaments thus split can be woven using warps and / or wefts, or both, and can be suitably used as a liquor extraction filter as a fabric. Moreover, it can be set as a favorable taste drink extraction bag by shape | molding this in a bag as needed. In any case, the resulting woven fabric composed of monofilaments is useful as a filter for black tea, green tea, and other favorite beverages. In particular, round (circular) cross-section fibers are used for warps and the above-mentioned flat cross-section fibers are used for wefts. It is preferable to use a woven fabric structure using A plain woven fabric is generally suitable as the woven fabric structure, but it may be a twill woven fabric or other structures. The obtained woven fabric is cut into an appropriate size, and a predetermined portion is fused by a method such as ultrasonic sealing or heat sealing to form a bag.
本発明の分繊用ポリエステルマルチフィラメントの製造方法は、特に限定されるものではないが、例えば、図1に示すように、紡糸口金1より吐出した溶融マルチフィラメントを、紡糸口金直下に設けた50〜200℃の雰囲気温度に保持した長さ50〜200mmの保温領域10を通過させて急激な冷却を抑制した後、冷却風11によりこの溶融マルチフィラメントを急冷して固体マルチフィラメントに変え、オイリングローラー2にてモノフィラメントの状態でオイリングを施し、糸分けガイド3を通った後、集束してマルチフィラメントの状態にして70℃〜120℃に加熱した第一ゴデットローラー4とそのセパレートローラー5に巻き付けで、500〜2000m/分の速度で引取り、引き続き、巻き取ることなく130〜160℃に加熱した、第一ゴデットローラー4よりも速い周速で回転する第二ゴデットローラー6とそのセパレートローラー7に巻き付け、上記第一ゴデットローラー4と第二ゴデットローラー6との間で2.0〜5.0倍に延伸し、続いて、巻き取り機8により第二ゴデットローラー6よりも低速で巻き取ってマルチフィラメントパッケージを得る方法を採用することができる。
The method for producing the polyester multifilament for splitting of the present invention is not particularly limited. For example, as shown in FIG. 1, a melted multifilament discharged from the spinneret 1 is provided directly under the spinneret. After passing through a heat-retaining
本発明の分繊用ポリエステルマルチフィラメントはそのまま分繊工程に供給し、分繊して使用されたり、仮撚加工を施して捲縮を付与した後に分繊して、フィルター用途に使用される。 The polyester multifilament for splitting of the present invention is supplied to the splitting process as it is and used after splitting, or after being crimped by false twisting and splitting and used for a filter.
以下、実施例により、本発明をさらに具体的に説明する。なお、実施例における各項目は次の方法で測定した。 Hereinafter, the present invention will be described more specifically with reference to examples. In addition, each item in an Example was measured with the following method.
(1)繊維中の比重5.0以上の金属成分の分析(真比重5.0以上の金属元素の含有量)
繊維サンプルを硫酸アンモニウム、硫酸、硝酸、過塩素酸とともに混合して約300℃で9時間湿式分解後、蒸留水で希釈し、理学製ICP発光分析装置(JY170 ULTRACE)を用いて定性分析し、比重5.0以上の金属元素の存在の有無を確認した。そして、1重量ppm以上の存在が確認された金属元素について、その元素含有量を示した。
(2)伸度
JIS−L−1013に基づいて定速伸長引張試験機であるオリエンテック(株)社製テンシロンを用いて、つかみ間隔20cm、引張速度20cm/分にて測定した。
(3)固有粘度
ポリエステルポリマーの固有粘度は、オルソクロロフェノール溶液について、35℃において測定した粘度の値から求めた。
(4)分繊断糸率(%)
分繊用ポリエステルマルチフィラメントを巻き取った10kg巻ドラム状パッケージを、単糸1本1本に糸切れなく分繊速度500m/分にて分繊できた分繊用マルチフィラメントの割合を満管率(%)で表す。なお、分繊されたモノフィラメントの巻量は1kg巻とする。合否判定基準は80%以上を合格とした。
(5)熱処理(200℃)での織物の交点溶着性、抽出バッグ形成時の超音波シール性
抽出バック製造の専門家によるテストにより評価した。
(6)風合い
織物の専門家による官能検査等により、良否を判定した。
(1) Analysis of metal components having a specific gravity of 5.0 or more in the fiber (content of metal elements having a true specific gravity of 5.0 or more)
The fiber sample is mixed with ammonium sulfate, sulfuric acid, nitric acid and perchloric acid, wet-decomposed at about 300 ° C for 9 hours, diluted with distilled water, qualitatively analyzed using a scientific ICP emission analyzer (JY170 ULTRACE), and specific gravity The presence or absence of 5.0 or more metal elements was confirmed. And the element content was shown about the metal element by which presence of 1 weight ppm or more was confirmed.
(2) Elongation Based on JIS-L-1013, it was measured at a gripping interval of 20 cm and a tensile speed of 20 cm / min using Tensilon manufactured by Orientec Co., Ltd., which is a constant speed extension tensile tester.
(3) Intrinsic viscosity The intrinsic viscosity of the polyester polymer was determined from the viscosity value measured at 35 ° C for an orthochlorophenol solution.
(4) Split yarn rate (%)
The percentage of multifilaments for splitting that can be split at a speed of 500m / min without breaking the yarn into a single yarn of a 10kg drum package that winds up polyester multifilaments for splitting (%) The split amount of monofilament is 1 kg. The pass / fail criterion was 80% or higher.
(5) Interstitial weldability of fabric during heat treatment (200 ° C.), ultrasonic sealability when forming extraction bag Evaluation was performed by a test by an extraction bag manufacturing specialist.
(6) Texture The quality was judged by a sensory test by a textile specialist.
[実施例1]
重合触媒としてチタン化合物としてトリメット酸チタンを5mmol%及びリン化合物としてトリエチルホスホノアセテートを30mmol%含有し、イソフタル酸成分をポリマー成分の17mol%の割合で共重合させた固有粘度0.650のポリエチレンテレフタレートイソフタレート共重合体(PETI)のペレットを140℃で5時間乾燥した。しかる後、溶融紡糸工程で、吐出孔径0.55mmの孔5ホールが同心円状に配列されている2個の紡糸口金から、それぞれ、ポリマー吐出温度280℃で、単一吐出孔当りの吐出量が8.0g/分となるように押し出して、モノフィラメントの状態でオイリングを施し、2つの紡糸口金から吐出されたモノフィラメントを合糸してフィラメント本数10本のマルチフィラメントとして、100℃に加熱した第一ゴデットローラーで16ターンさせて、700m/分で引き取りつつ、第一ゴデットローラーの4.4倍の速度で第二ゴデットローラーに10ターンさせ4.4倍に延伸した後、フィラメント本数10本のマルチフィラメントとして巻き取った。
この条件で丸断面繊維と扁平度4の長軸方向に丸断面単糸の4個が直線状に接合した扁平断面繊維の2種のマルチフィラメントを製造した。得られた各マルチフィラメントの物性は表1に示すとおりであった。
[Example 1]
Polyethylene terephthalate having an intrinsic viscosity of 0.650, containing 5 mmol% of titanium trimetate as a titanium compound as a polymerization catalyst and 30 mmol% of triethylphosphonoacetate as a phosphorus compound, and copolymerizing an isophthalic acid component at a ratio of 17 mol% of the polymer component. The pellets of isophthalate copolymer (PETI) were dried at 140 ° C. for 5 hours. Thereafter, in the melt spinning process, the discharge amount per single discharge hole is set at a polymer discharge temperature of 280 ° C. from two spinnerets in which 5 holes each having a discharge hole diameter of 0.55 mm are arranged concentrically. Extruded to 8.0 g / min, oiled in the form of a monofilament, monofilaments discharged from two spinnerets were combined into a multifilament with 10 filaments, and heated to 100 ° C. After making 16 turns with a godet roller and pulling it at 700 m / min, the second godet roller makes 10 turns at a speed 4.4 times that of the first godet roller, and after drawing 4.4 times, the number of filaments is 10 It was wound up as a multifilament of books.
Under these conditions, two types of multifilaments of flat cross-section fibers in which round cross-section fibers and four round cross-section single yarns were joined linearly in the major axis direction with a flatness of 4 were produced. Table 1 shows the physical properties of the obtained multifilaments.
次いで、各マルチフィラメントについて、それぞれ分繊を行い、得られたモノフィラメントで経糸を丸断面繊維とし、緯糸を扁平断面繊維として平織物[タフタ、27dTexモノフィラメント、打込数(97×97/インチ)]を製織し、精錬を行った後、水洗い乾燥後、テンションをかけた状態で加熱空気中(200℃)で熱処理し、糸の交点に軽い溶着を付与して得られた平織物を、超音波シール法より抽出バッグを形成した。
この条件で巻き取られた丸断面繊維と扁平度4の長軸方向に丸断面単糸の4個が直線状に接合した扁平断面繊維のマルチフィラメントは表1に示すとおり、ともに分繊性も良好であった。また、上記の平織物は超音波シール法による溶着性が良好であり、織物の風合いも柔らかく嗜好性飲料抽出フィルター又は抽出バッグに適したものであった。
Next, for each multifilament, each of the multifilaments was split, and the resulting monofilament was used to form a warp as a round cross-section fiber and a weft as a flat cross-section fiber to obtain a plain fabric [taffeta, 27dTex monofilament, number of driven (97 × 97 / inch)] Weaving, refining, washing with water, drying, heat treatment in heated air (200 ° C) with tension applied, and giving a light weld to the intersection of yarns An extraction bag was formed by the sealing method.
As shown in Table 1, the multifilaments of the flat cross-section fibers in which the round cross-section fibers wound under these conditions and four round cross-section single yarns joined in a straight line in the major axis direction with a flatness of 4 are both finely divided. It was good. Further, the above-mentioned plain woven fabric has good weldability by the ultrasonic sealing method, and the texture of the woven fabric is soft and suitable for a palatability beverage extraction filter or an extraction bag.
[比較例1]
繊維断面を経糸及び緯糸共に丸断面繊維を使用した以外は実施例1と同じ条件で抽出バッグを形成した。その結果を表1に併記する。
[Comparative Example 1]
An extraction bag was formed under the same conditions as in Example 1 except that round cross-section fibers were used for both the warp and the weft. The results are also shown in Table 1.
[比較例2]
重合触媒としてチタン化合物としてトリメット酸チタンを5mmol%及びリン化合物としてトリエチルホスホノアセテートを30mmol%含有し、固有粘度0.650のポリエチレンテレフタレートペレット(PET)を使用した以外は実施例1と同じ条件で抽出バッグを形成した。その結果を表1に併記する。
[Comparative Example 2]
Under the same conditions as in Example 1, except that 5 mmol% of titanium trimetate as the titanium compound and 30 mmol% of triethylphosphonoacetate as the phosphorus compound were used as the polymerization catalyst and polyethylene terephthalate pellets (PET) having an intrinsic viscosity of 0.650 were used. An extraction bag was formed. The results are also shown in Table 1.
表1からも明らかなように、繊維融点が205℃で経糸に丸断面、緯糸に扁平断面を使用した実施例1の織物は、超音波シール性も良好であり、抽出バッグとしての風合いも柔らかく良好なものであった。これに対し、繊維融点が205℃で経糸、緯糸ともに丸断面を使用した比較例1の織物は、超音波シール後の解れが何度か見られ、超音波シール性が良好であるとは言えず、抽出バッグとしての風合いも硬く良いものであるとは言い難いものであった。また、繊維融点が256℃のPETフィラメントで経糸に丸断面、緯糸に扁平断面を使用した比較例2の織物は織物の風合いは、比較的柔らかいものであるが、超音波シールが悪く抽出バッグとしては使用出来ないものであった。 As is clear from Table 1, the fabric of Example 1 using a circular melting point for the warp and a flat cross section for the weft at a fiber melting point of 205 ° C. has good ultrasonic sealing properties and soft texture as an extraction bag. It was good. In contrast, the woven fabric of Comparative Example 1 having a fiber melting point of 205 ° C. and having a round cross section for both warp and weft has several unwinding after ultrasonic sealing, and it can be said that the ultrasonic sealing property is good. Furthermore, it was difficult to say that the texture as an extraction bag was hard and good. Further, the fabric of Comparative Example 2 using a PET filament having a fiber melting point of 256 ° C. and having a round cross-section for warp and a flat cross-section for weft has a relatively soft texture, but has a poor ultrasonic seal as an extraction bag. Was unusable.
本発明のポリエステルフィラメントは織物嗜好性飲料抽出フィルター素材として有用であり、特に紅茶等に使用される抽出バッグ用としてきわめて有用である。 The polyester filament of the present invention is useful as a fabric-preferred beverage extraction filter material, and particularly useful for an extraction bag used for tea or the like.
1:紡糸口金
2:オイリングローラー
3:糸分けガイド
4:第一ゴデットローラー
5:第一セパレートローラー
6:第二ゴデットローラー
7:第二セパレートローラー
8:巻き取り機
9:マルチフィラメントパッケージ
10:保温領域
11:冷却風
1: Spinneret 2: Oiling roller 3: Thread separation guide 4: First godet roller 5: First separate roller 6: Second godet roller 7: Second separate roller 8: Winder 9: Multifilament package 10 : Thermal insulation area 11: Cooling air
Claims (5)
(1)繊維断面が扁平であること
(2)伸度が20〜40%であること
(3)単糸繊度が10〜40デシテックスであること
(4)フィラメント数が4本以上20本以下であること
(5)繊維の融点が200〜240℃の範囲にあること 80 mol% of the polymer repeating units constituting the fibers Ri ethylene terephthalate units der, isophthalic acid is composed of copolyester copolymerized in a proportion of 5 to 20 mole percent of total acid component, a true specific gravity of 5. A multifilament composed of a polyester having a content of 0 or more metal elements of 0.5 ppm by weight or less, and satisfying the following conditions (1) to ( 5 ) simultaneously: Splitting polyester multifilament suitable for use as a beverage extract filter.
(1) The fiber cross section is flat (2) The elongation is 20 to 40% (3) The single yarn fineness is 10 to 40 dtex (4) The number of filaments is 4 or more and 20 or less There is
(5) Melting | fusing point of a fiber exists in the range of 200-240 degreeC.
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JP2009202932A (en) * | 2008-02-29 | 2009-09-10 | Teijin Fibers Ltd | Filter for extracting luxury beverage, its manufacturing method, and bag for extraction |
JP6976092B2 (en) * | 2017-07-05 | 2021-12-08 | Kbセーレン株式会社 | Multifilament for tasteful beverage extraction filter |
CN110446668A (en) | 2017-07-05 | 2019-11-12 | Kb世联株式会社 | Hobby property drinks extraction filtration members fibril and the hobby drinks extraction filtration members fabric including it |
JP6783414B1 (en) | 2019-01-09 | 2020-11-11 | Kbセーレン株式会社 | Preference Beverage Extraction Filter Multifilament for Textiles |
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