JPS61119737A - Polyamide interlaced multifilament - Google Patents
Polyamide interlaced multifilamentInfo
- Publication number
- JPS61119737A JPS61119737A JP24279984A JP24279984A JPS61119737A JP S61119737 A JPS61119737 A JP S61119737A JP 24279984 A JP24279984 A JP 24279984A JP 24279984 A JP24279984 A JP 24279984A JP S61119737 A JPS61119737 A JP S61119737A
- Authority
- JP
- Japan
- Prior art keywords
- nylon
- polyamide
- entanglement
- multifilament
- filaments
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000004952 Polyamide Substances 0.000 title claims description 23
- 229920002647 polyamide Polymers 0.000 title claims description 23
- 229920003189 Nylon 4,6 Polymers 0.000 claims description 18
- 239000000835 fiber Substances 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- 239000004744 fabric Substances 0.000 description 15
- 229920002292 Nylon 6 Polymers 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 9
- 239000012530 fluid Substances 0.000 description 6
- 229920002302 Nylon 6,6 Polymers 0.000 description 5
- 230000009477 glass transition Effects 0.000 description 5
- 238000009941 weaving Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009987 spinning Methods 0.000 description 3
- 238000004804 winding Methods 0.000 description 3
- 235000013351 cheese Nutrition 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- -1 poly(hexamethylene adipamide) Polymers 0.000 description 2
- 238000007665 sagging Methods 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 241001589086 Bellapiscis medius Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 125000004836 hexamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000010137 moulding (plastic) Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 230000035900 sweating Effects 0.000 description 1
- MHSKRLJMQQNJNC-UHFFFAOYSA-N terephthalamide Chemical compound NC(=O)C1=CC=C(C(N)=O)C=C1 MHSKRLJMQQNJNC-UHFFFAOYSA-N 0.000 description 1
- DJZKNOVUNYPPEE-UHFFFAOYSA-N tetradecane-1,4,11,14-tetracarboxamide Chemical compound NC(=O)CCCC(C(N)=O)CCCCCCC(C(N)=O)CCCC(N)=O DJZKNOVUNYPPEE-UHFFFAOYSA-N 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
Landscapes
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、ポリアミド絡合マルチフィラメントに関し、
更に詳しくは無糊、無撚で製織可能なポリアミド絡合マ
ルチフィラメントに関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a polyamide entangled multifilament,
More specifically, the present invention relates to an entangled polyamide multifilament that can be woven without glue or twist.
(従来の技術) ポリアミドマルチフィラメントからなる織物は。(Conventional technology) Fabric made of polyamide multifilament.
そのタフネス、鮮明染色性などより各種の分野、例えば
裏地、傘地、レインコート地、ジャンノく−、下着など
に使用されている。そしてこれらの織物は一般に糊付さ
れ、ウォータージェットルームにより製織されるが、最
近糊付工程を省略する目的でインターレースされたポリ
アミドマルチフィラメントでウォータージェットルーム
で製織されることが多くなってきている。しかし一般に
これまでのこれらの衣料用に使用されるポリアミドマル
チフィラメントはナイロン6、ナイロン66であり、ウ
ォータージェットルームで水分を多量に含んだ状態で間
欠的に張力がかけらj、て製織されると、糸が可塑化さ
れてイレギュラーに伸ばされ、欠点になったり、交絡が
ほどけ易く、強い交絡を与えないと製織性に問題が生じ
た。又交絡Kを高くするとインターレースマークと称す
るモアレ斑も出易く織物の品位が著しく低下する。更に
ナイロン6は通常の延伸機で延伸すると熱水収縮率が高
く、捲糸体の内外層で応力が異な夛、しかもガラス転移
温度が低いためにその状態で熱セットされ易く、捲糸体
の内外層差も大きくなって、欠点が生じた。これを防止
するためには一旦延伸したあと連続的又は非連続にリラ
ックス熱処理して熱水収縮率を低くするなどの必要があ
った。Due to its toughness and bright dyeability, it is used in various fields such as linings, umbrella fabrics, raincoat fabrics, jackets, and underwear. These fabrics are generally pasted and woven in a water jet loom, but recently interlaced polyamide multifilaments have been increasingly woven in a water jet loom in order to omit the pasting process. However, the polyamide multifilaments currently used for these garments are generally nylon 6 and nylon 66, and when woven in a water jet loom under intermittent tension while containing a large amount of moisture, , the threads were plasticized and stretched irregularly, resulting in defects, and the entanglement was easy to unravel, causing problems in weavability unless strong interlacement was applied. Furthermore, when the entanglement K is increased, moiré spots called interlace marks are likely to appear, and the quality of the fabric is significantly degraded. Furthermore, when nylon 6 is drawn with a normal drawing machine, it has a high hot water shrinkage rate, and the stress is different between the inner and outer layers of the thread, and its glass transition temperature is low, so it is easily heat-set in that state, and the winding has a high shrinkage rate. The difference between the inner and outer layers also increased, creating a drawback. In order to prevent this, it is necessary to perform continuous or discontinuous relaxing heat treatment after stretching to lower the hot water shrinkage rate.
(発明が解決しようとする問題点)
本発明は、かかる従来のポリアミド絡合マルチフィラメ
ントの欠点を解消し、鮮明染色性にすぐれ、且つヌメリ
感もなく、ウォータージェットルームの製織性及び、品
位にすぐれた織物の得られるポリアミド絡合マルチフィ
ラメントを提供することを目的とする。(Problems to be Solved by the Invention) The present invention eliminates the drawbacks of the conventional polyamide entangled multifilament, has excellent bright dyeing properties, does not have a slimy feel, and has excellent water jet loom weavability and quality. The object of the present invention is to provide a polyamide entangled multifilament that provides an excellent fabric.
(問題点を解決するだめの手段)
本発明は、かかる目的を達成するために次のような構成
を有する。すなわち本発明は、実質的にナイロン46繊
維のフィラメントからなる絡合マルチフィラメントであ
って該絡合マルチフィラメントは10本以上のフィラメ
ントからなり、該フィラメントは互いに交絡、交錯して
おり、且つ交絡度が少なくとも10であることを特徴と
するポリアミド絡合マルチフィラメントである。(Means for solving the problem) The present invention has the following configuration to achieve the above object. That is, the present invention provides an entangled multifilament consisting essentially of filaments of nylon 46 fibers, the entangled multifilament consisting of 10 or more filaments, the filaments being intertwined and intertwined with each other, and having a degree of entanglement. is at least 10.
以下に本発明の詳細な説明する。The present invention will be explained in detail below.
本発明においてポリアミド繊維としてナイロン46繊維
を選んだのは必須のことである。ナイロン46繊維は工
業製品として例えばプラスチックの成形例(例えば特開
昭56−149429 )や産業資材用途としてタイヤ
コード原糸の製造法(例えば特開昭59−88911
)があるが衣料用#&維と゛しては実用化されていなか
った。本発明者がナイロン46橡維について種々検討し
た結果これ捷でに知られていたポリアミド繊維に比べて
、水中での可塑化も少なく、布帛での吸湿性も良好で、
熱収縮率も小さくガラス転移温度も高いだめ常温では安
定しており、しかもポリアミド繊維の鮮明染色性を有し
ながら特有のヌメリ感もないなどウォータージェットル
ーム製織用として非常にすぐれていることを見出したの
である。すなわち吸湿性で、例えば20°065%RH
のときの水分率はナイロン6の4.0チ、ナイロン66
の4.8%に比ベナイロン46は6.4係と格段に大き
くこれがサヮヤカな感触が得られる一つの原因なのであ
る。In the present invention, it is essential to select nylon 46 fiber as the polyamide fiber. Nylon 46 fibers are used as industrial products, such as in plastic molding examples (e.g., JP-A-56-149429), and as industrial materials, in methods for manufacturing tire cord yarn (e.g., JP-A-59-88911).
), but it had not been put to practical use as a material for clothing. The present inventor conducted various studies on nylon 46 fibers, and found that compared to the previously known polyamide fibers, this fiber undergoes less plasticization in water and has good moisture absorption in fabrics.
It has been found that it is excellent for water jet loom weaving, as it has a low heat shrinkage rate and a high glass transition temperature, so it is stable at room temperature, and has the vivid dyeing properties of polyamide fibers without the characteristic slimy feeling. It was. That is, hygroscopic, for example 20°065%RH
When the moisture content is 4.0% for nylon 6, nylon 66
Benylon 46 has a much larger ratio of 6.4% compared to 4.8%, which is one of the reasons why it feels so good.
又理由は明確ではないが、ナイロン6、ナイロン66な
どに比べてヌメリ感がなくサラットした風合が得られる
のである。さらに水中での可塑化が小さく、例えばJI
S法(L1073)で測定した(定速伸長型の引張試験
機)標準状態とウェット時の破断伸度の変化もナイロン
6の乾42チ→瀞53係に比ベナイロン46は乾45チ
→湿48チとなり、水中や発汗時などの湿状態でのへタ
リが格段に小さく、ナイロン6やナイロン66で問題と
なったウォータージェットルーム製織中を含む湿状態で
のへタリを著しく改善するのである。Although the reason is not clear, it does not feel slimy and has a smooth texture compared to nylon 6, nylon 66, etc. Furthermore, plasticization in water is small, such as JI
The change in fracture elongation measured by the S method (L1073) (constant speed elongation type tensile tester) between the standard state and the wet state was 42 inches dry → 53 inches for Nylon 6, while Nylon 46 was 45 inches dry → wet. 48 inches, and the sagging in wet conditions such as underwater or sweating is much smaller, and it significantly improves the sagging in wet conditions, including during water jet loom weaving, which was a problem with nylon 6 and nylon 66. .
このような特性を与える非捲縮のナイロン46繊維は、
分子鎖のくり返し単位が70重量係以上6N H(CH
2)4N HCO(CH2)4 COうで構成さiす
る実質的にポリ(テトラメチレンアジノくミド)からな
るポリアミド繊維であって、′ε−カプラミド成分、ヘ
キサメチレンアジパミド成分、ヘキサメ以下共重合した
もの、或はこれらから成るポリマ、すなわちポリ(ε−
カプラミド)、ポリ(ヘキサメチレンアジパミド)、ポ
リ(ヘキサメチレンチレフタラミド)、ポリ(ウンデカ
メチレンテレフタラミド)などを30重重量板下ブレン
ドしたものを含んでも良い。また必要に応じて艶消し剤
、顔料、光安定剤、熱安定剤、酸化防止剤、帯電防止剤
、染色性向上剤或は接着性向上剤等を配合することがで
き、配合−の如何によって本発明の特性に重大な悪影響
を与えるもの以外は、全て利用できる。The non-crimped nylon 46 fiber that provides these properties is
The repeating unit of the molecular chain is 70 weight coefficient or more, 6N H (CH
2) A polyamide fiber consisting essentially of poly(tetramethylene azinamide) consisting of 4N HCO(CH2)4CO, including a 'ε-capramide component, a hexamethylene adipamide component, and a hexamethylene component. Polymerized products or polymers composed of these, namely poly(ε-
It may also contain a 30-weight blend of poly(hexamethylene adipamide), poly(hexamethylene ethylene adipamide), poly(undecamethylene terephthalamide), and the like. In addition, matting agents, pigments, light stabilizers, heat stabilizers, antioxidants, antistatic agents, dyeability improvers, adhesion improvers, etc. can be added as necessary, depending on the combination. All can be used except those that have a significant adverse effect on the properties of the present invention.
又フィラメントの断面も特に限定されず、必要に応じて
丸、3葉、4葉以上の多葉断面、中空、及びこれらの組
合されたものでも可能であり、又フィラメントの側面に
細孔、経溝を有するものであってもよい。Furthermore, the cross section of the filament is not particularly limited, and may be round, three-lobed, multi-lobed cross-section with four or more leaves, hollow, or a combination thereof, as required. It may also have grooves.
又フィラメント本数は少なくとも10本以上が必要であ
不がこれは充分にフィラメント間で交絡、交錯を生じせ
しめるためである1、10本未満のようにフィラメント
本数の少ないものは無作為にフィラメントが懲り合され
る、いわゆる交絡が生じ難いからである。更にフィラメ
ントの繊度は好′ましくは10デニール以下、さらに好
ましくは5デニール以下である。これは流体ノズルでフ
ィラメントを交絡せしめるためには、フィラメントがね
じれ易いことが必要だからである。ただ余りフィラメン
トデニールが細いと流体処理のさいフィラメント切れが
生じ易く奸才しく11′i0.5デニール以−ヒ、さら
に好ましくは1デニ一ル以上のものがよい。ヤーンデニ
ールは用途により適宜選択はれればよい。In addition, the number of filaments must be at least 10, but this is in order to cause enough intertwining and crossing between the filaments.If the number of filaments is small, such as less than 1, the filaments will be randomly arranged. This is because it is difficult for so-called confounding to occur. Furthermore, the fineness of the filament is preferably 10 deniers or less, more preferably 5 deniers or less. This is because in order to entangle the filaments with the fluid nozzle, the filaments must be easily twisted. However, if the filament denier is too thin, the filament will easily break during fluid treatment, so it is best to use a filament of 11'i0.5 denier or more, more preferably 1 denier or more. The yarn denier may be selected as appropriate depending on the application.
次に交絡度(ケ/m)ti製織性を決めるとともなるが
ナイロン6では少なくとも20以上必要であり、これに
比較してナイロン46は非常に少な(へのである。本発
明で交絡度が小さくても充分な製織性が得られるのは、
これ寸でに述べて来たようにナイロン46はナイロン6
などのこれまでに公知のポリアミド繊維に比べて水中で
の可塑化が小さく、又ガラス転移温度もナイロン6の4
0〜60’C!に比べて80°Cと高いために常温では
糸は安定しているのでワーピング、ビーミングなどの準
備工程やウォータージェットルームでの交絡度低下が少
なく、糸としての交絡度を低くしても充分な製織性が確
保出来るのである。更に高速化も可能となるのである。Next, the degree of entanglement (k/m) ti is determined, and nylon 6 requires at least 20 or more, and compared to this, nylon 46 has a very low degree of entanglement. The reason why sufficient weavability can be obtained even if the size is small is that
As mentioned earlier, nylon 46 is nylon 6.
Compared to conventional polyamide fibers such as polyamide fibers, plasticization in water is smaller, and the glass transition temperature is 4.
0~60'C! Since the yarn is stable at room temperature due to its high temperature of 80°C compared to This ensures good weavability. Furthermore, it becomes possible to increase the speed.
ここで交絡度は高い方が製織工程も営め後工程の通過性
は良好となるが、余り高くしようとすると流体流廿が多
くなり生産コストが高くなるとともにインターレースマ
ークと叶ばれるモアレ汰が布面に表われるので、好゛ま
しくない。この・「ンターレースマークからみた交絡度
は組織、密度により異なるが、100以下、好廿しくに
50以下が良好な範囲である。The higher the degree of entanglement, the better the weaving process can be carried out, and the better the passability in subsequent processes. However, if it is too high, the fluid flow will increase, which will increase production costs, and will also cause moiré marks, which are realized as interlaced marks, on the fabric surface. This is not desirable because it appears in The degree of entanglement seen from the interlace mark varies depending on the structure and density, but a good range is 100 or less, preferably 50 or less.
次にマルチフィラメントの熱水収縮率は通常のナイロン
6延伸糸の如く12〜16%もあり、かつガラス転移温
度が前述の如く、低い場合には巻糸体の内外層で巻張力
(圧力)が異なるとその状態で固定さfl同−織物中に
隣接して巻糸体の内外層の糸があると筋、スケ、吊りな
どの欠点が多発する。一般にはこれをさけるために延伸
されたマルチフィラメントを連続的又は別個に弛緩熱処
理して熱水収縮率を8〜9係以下にしてかつ巻糸体の内
外層を分割使用するなど頻雑な工程、処理を必要とした
。しかしナイロン46の場合には通常のホットプレート
を有する延伸機で延伸すると8〜9係以下の熱水収縮率
となり、且つガラス転移温度も高いためナイロン6のよ
うな頻雑な処理をしなくてもその″!マ使用出来るが、
熱水収縮率が高いと織物での収縮が大きく面が汚なくな
るので好ましくは10%以下更に好ましくは8係以下が
好ましい範囲である。Next, the hot water shrinkage rate of multifilament is as high as 12 to 16% like ordinary nylon 6 drawn yarn, and when the glass transition temperature is low as mentioned above, the winding tension (pressure) is increased in the inner and outer layers of the wound yarn. If the threads are different, they will be fixed in that state.If there are yarns from the inner and outer layers of the thread body adjacent to each other in the fabric, defects such as streaks, skidding, and hanging will occur frequently. Generally, to avoid this, frequent processes such as continuous or separate relaxation heat treatment of the drawn multifilament to reduce the hot water shrinkage factor to 8 to 9 or less and use the inner and outer layers of the wound body separately are required. , required processing. However, in the case of nylon 46, when stretched using a normal stretching machine with a hot plate, the hot water shrinkage rate is less than 8 to 9, and the glass transition temperature is also high, so it does not need to be subjected to frequent treatments like nylon 6. Mosono”! You can use it, but
If the hot water shrinkage rate is high, the shrinkage of the fabric will be large and the surface will become dirty, so the preferred range is preferably 10% or less, more preferably 8% or less.
尚本発明のポリアミド絡合マルチフィラメントは、実質
的にナイロン46繊維のフィラメントからなる限り、か
ならずしも1種のマルチフィラメントでなくともよく、
染色性、収+a率、その他物性差のあるものを複合した
ものであってもよい。Note that the polyamide entangled multifilament of the present invention does not necessarily have to be one type of multifilament, as long as it consists essentially of filaments of nylon 46 fibers.
It may be a composite of materials with differences in dyeability, yield + a rate, and other physical properties.
更に本発明のマルチフィラメントは特に積極的に加熱す
る必要はないが延撚機などで延伸される場合には加熱さ
れていてもかまわない。また油剤は紡糸、延伸に必要と
され、且つ後工程でスカム、オリゴマーなどの問題とな
らないオイルを必要に応じて付着させればよく、特に本
発明では限定されないが集束性を与えるものの方が好ま
しい。Further, the multifilament of the present invention does not particularly need to be actively heated, but may be heated if it is drawn using a drawing/twisting machine or the like. In addition, as the oil agent, an oil that is necessary for spinning and drawing and does not cause problems such as scum and oligomers in the subsequent process may be attached as necessary, and although it is not particularly limited in the present invention, it is preferable to use an oil that provides cohesiveness. .
ここで本発明のポリアミド絡合マルチフィラメントの製
造方法の一例を図に基づいて説明する。Here, an example of the method for manufacturing the polyamide entangled multifilament of the present invention will be explained based on the drawings.
第1図、第2図は本発明のポリアミド絡合マルチフィラ
メントを製造するだめの延伸機の略側面図である。FIGS. 1 and 2 are schematic side views of a drawing machine for producing the polyamide entangled multifilament of the present invention.
第1図においてナイロン46の未延伸パッケージP、か
ら解脅された未延伸糸Y、はガイド1.2を経てフィー
ドローラー3により延伸風に供給されドローローラー6
との間で所定の延伸をされ、必要に応じてその間にホッ
トローラー4、ホットプレート5で延伸点固定、熱処理
される。ついでドローローラー6とデリベリ−ローラー
9との間で所定の張力になるように速度比を調整し、流
体ノズル7で交絡が与えられカイト10を経てパーン1
1につ巻取られる。尚ドローローラー6とデリベリ−ロ
ーラー9の間にヒーター8を設けて張力を一定化したシ
熱水収縮率を調整してもよい。第2図は第1図の装置の
デリベリ−ローラー9、ヒーター8を取外した製造装置
の例の略側面図である。In FIG. 1, the undrawn yarn Y unstretched from the undrawn package P of nylon 46 passes through the guide 1.2, is fed to the drawing wind by the feed roller 3, and is fed to the draw roller 6.
A predetermined stretching process is carried out between the film and the film, and if necessary, the stretching point is fixed using a hot roller 4 and a hot plate 5, and heat treatment is performed. Next, the speed ratio is adjusted so that a predetermined tension is achieved between the draw roller 6 and the delivery roller 9, and the fluid nozzle 7 imparts entanglement to the pirn 1 via the kite 10.
It is wound up once. Incidentally, a heater 8 may be provided between the draw roller 6 and the delivery roller 9 to keep the tension constant and adjust the shrinkage rate of the hot water. FIG. 2 is a schematic side view of an example of the manufacturing apparatus shown in FIG. 1, with the delivery roller 9 and heater 8 removed.
尚ここで流体ノズルは例えば特公昭59−33694で
示されるものが好適に使用されるが、特公昭36−12
230なども使用出来る。又第1図、第2図ともリング
ツイスタ−での捲取装置を示しているがチーズ形状に捲
上げる、いわゆるチーズワインダーも適宜使用出来る。Here, as the fluid nozzle, for example, the one shown in Japanese Patent Publication No. 59-33694 is suitably used;
230 etc. can also be used. Further, although both FIGS. 1 and 2 show a winding device using a ring twister, a so-called cheese winder that winds up the material into a cheese shape may also be used as appropriate.
でポリアミド(ナイロン46)絡合マルチフィラメント
を得た。尚ナイロン46繊維は、相対粘度2.5のナイ
ロン46チップを原料とし紡糸温度310°C紡糸引取
速度460 m A尿7未延伸糸を得た。A polyamide (nylon 46) entangled multifilament was obtained. The nylon 46 fibers were obtained using nylon 46 chips with a relative viscosity of 2.5 as raw materials at a spinning temperature of 310° C., a spinning take-off speed of 460 m, and an undrawn yarn of A Urine 7.
尚比較例1−6は本発明との差を明らかにするためのも
のである。ここでナイロン46の延伸条件はフィードロ
ーラー3とホットローラー4の間の予備延伸倍率1.0
04、ホットローラー4とドローローラー6の間の延伸
倍率3.47、ホットローラー4の温度40°C、ホッ
トプレート5の温度200°C1流体ノズルのエアー圧
は所定の交絡度(ケ/1rL)になるよう調整・した。Comparative Examples 1-6 are intended to clarify the differences from the present invention. Here, the stretching conditions for nylon 46 are a preliminary stretching ratio of 1.0 between the feed roller 3 and the hot roller 4.
04. Stretching ratio between hot roller 4 and draw roller 6: 3.47; temperature of hot roller 4: 40°C; temperature of hot plate 5: 200°C I adjusted it so that
尚比較例4−6のナイロン6はホットローラー、ホット
プレートとも室温で予備延伸倍率1.004、延伸倍率
3.28としだ。The nylon 6 of Comparative Example 4-6 had a preliminary stretching ratio of 1.004 and a stretching ratio of 3.28 at room temperature for both the hot roller and hot plate.
更に得た絡合マルチフィラメントで、経糸密度104本
/1nch、緯糸密度86本/1nchOタフタを製織
し評価した。Further, using the obtained entangled multifilament, taffeta with a warp density of 104 threads/1 nch and a weft thread density of 86 threads/1 nch was woven and evaluated.
尚ここで交絡度は適当な長さに切った糸の上端をフック
にかけ下端に0.1g/デニールの荷重を吊るす。糸に
針をつきさし毎秒3画の速さでもち上げ荷重がもち上が
ったところで停止し針の移動距離を記録する。この値を
100個求め大きい値。Here, the degree of entanglement is determined by hanging the upper end of the yarn cut to an appropriate length on a hook and hanging a load of 0.1 g/denier from the lower end. A needle is inserted into the thread and raised at a speed of 3 strokes per second, stopping when the load is lifted and recording the distance traveled by the needle. Obtain 100 of these values and select the larger value.
小さい値各10個ずつ捨て80ケの平均を求めlとし、
次式で交絡度を求める。Discard 10 of each small value, find the average of 80, and set it as l.
Calculate the degree of confounding using the following formula.
交絡度(Di)−100/n菌
熱水収縮率はJIS L1073 6.12(I)A法
により求めた。絡合性はマルチフィラメントを水中で約
0.2.!;’/デニールの荷重をかけ100回/分で
100回振動させて絡合性の保持で評価した。Degree of entanglement (Di) -100/n Bacterial hot water shrinkage rate was determined by JIS L1073 6.12(I)A method. The entanglement property of the multifilament in water is approximately 0.2. ! ;'/denier load was applied and the material was vibrated 100 times at a rate of 100 times/min, and the retention of entanglement property was evaluated.
織物欠点はモテレを中心に評価した。ヌメリ感は官能検
査により、有りを×、無しを○とした。感触は、良好を
○、可を△としてあられした。Fabric defects were evaluated mainly on motel. The slimy feeling was evaluated by a sensory test, and the presence was evaluated as ×, and the absence was evaluated as ○. The feel was rated as ○ for good and △ for fair.
第1表
*第1図の装置を使用しドローローラー6とデリベリロ
ーラー9との間のリラックス率を+10%とし、ヒータ
ー8の温度は130°Cとした。Table 1 * The apparatus shown in Figure 1 was used, the relaxation rate between the draw roller 6 and the delivery roller 9 was set to +10%, and the temperature of the heater 8 was set to 130°C.
実施例1.2は絡合性、織物品位もよく、ヌメリ感も少
な′く乾いた触感の織物で好評であった。Examples 1 and 2 were well-received as they had good intertwining properties and fabric quality, and were dry to the touch with little sliminess.
実施例3は交絡度が犬で絡合性は良好だが若干モアレ斑
が発生した。In Example 3, the degree of entanglement was dog, and the entanglement was good, but some moire spots occurred.
1則 1
比較例1は交絡度が小で絡合擬に問題があり小量iL織
でも製織性に問題があった。1 Rule 1 Comparative Example 1 had a low degree of entanglement and had a problem with entanglement, and even with a small amount of iL weave there was a problem with weavability.
比較例2は交絡度は満足しているものの感触がプラスチ
ックライクであった。In Comparative Example 2, the degree of entanglement was satisfactory, but the feel was plastic-like.
比較例3はフィラメント数が5本と少なく交絡度が所定
のところまであがらす絡合性ても問題があり、織物の品
位もよくなかった。比較例4.5はナイロン6で比較例
4は交絡度は実施例1と同じだが水中での交絡度低下が
大きく絡合性が悪く、更に製織でも吊りやスケが発生し
織物の品位は悪いものであった。比較例5は交絡度を多
くしているために水中で交絡度が低下してもほぼ良好な
絡合性を示すが、モアレ斑の目立つ部分があり、更に比
較例4.5ともバーン内外層を層別使用しなかったため
節理が目立った。これに対し比較例6は第1図の装置を
使用しドローローラー6とデリベリ−ローラー9の間の
弛緩率を10係、ヒータ−8は非接触式のヒーターで温
度130°Cとし、且つパーン内外層を層別して使用し
たために節理などの問題は解消したが、ヌメリ感などの
風合はナイロン46より劣ったものであった。In Comparative Example 3, the number of filaments was as small as 5, and there was a problem in the entangling ability of increasing the degree of entanglement to a predetermined level, and the quality of the fabric was also poor. Comparative Example 4.5 is nylon 6, and Comparative Example 4 has the same degree of entanglement as Example 1, but the degree of entanglement decreases in water and the entanglement property is poor. Furthermore, hanging and skidding occur during weaving, and the quality of the fabric is poor. It was something. Since Comparative Example 5 has a high degree of entanglement, it shows almost good entanglement even if the degree of entanglement decreases in water. Since stratification was not used, the savings were noticeable. On the other hand, in Comparative Example 6, the apparatus shown in FIG. Since the inner and outer layers were used separately, problems such as joints were resolved, but the texture, such as sliminess, was inferior to that of nylon 46.
(発明の効果)
このように本発明のポリアミド絡合マルチフィラメント
は絡合性にすぐれているため無糊、無撚で後加工性、製
織性にすぐれ織物品位が良好で且つヌメリ感などの感触
を改善し、しかもポリアミド砿維としての鮮明な色相が
得られるという顕著な効果が得られるのである。(Effects of the Invention) As described above, the polyamide entangled multifilament of the present invention has excellent entangling properties, so it has no glue or twist, has excellent post-processability and weaving properties, has good fabric quality, and has a slimy feel. This has the remarkable effect of improving the properties of polyamide fibers and providing a clear hue as a polyamide fiber.
第1図、第2図は本発明のポリアミド絡合マルチフィラ
メントを製造する装置の略側面図であり、第2図は第1
図においてデリベリローラー9を省いたものである。
Pl・・・・・・ナイロン46未延伸パッケージ3・・
・・・・ フィードローラー
5・・・・・・ホットプレート
6・・・・・・ ドローローラー
7・・・・・・流体ノズル
11・・・・・・パーン1 and 2 are schematic side views of an apparatus for producing entangled polyamide multifilament of the present invention, and FIG.
The delivery roller 9 is omitted in the figure. Pl...Nylon 46 unstretched package 3...
... Feed roller 5 ... Hot plate 6 ... Draw roller 7 ... Fluid nozzle 11 ... Pan
Claims (1)
マルチフィラメントであって該絡合マルチフィラメント
は、10本以上のフィラメントからなり、該フィラメン
トは交絡、交錯しており、且つ交絡度が少なくとも10
であることを特徴とするポリアミド絡合マルチフィラメ
ント。An entangled multifilament consisting essentially of filaments of nylon 46 fibers, the entangled multifilament consisting of 10 or more filaments, the filaments being intertwined or intertwined, and having an entanglement degree of at least 10.
A polyamide entangled multifilament characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24279984A JPS61119737A (en) | 1984-11-16 | 1984-11-16 | Polyamide interlaced multifilament |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24279984A JPS61119737A (en) | 1984-11-16 | 1984-11-16 | Polyamide interlaced multifilament |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61119737A true JPS61119737A (en) | 1986-06-06 |
Family
ID=17094457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24279984A Pending JPS61119737A (en) | 1984-11-16 | 1984-11-16 | Polyamide interlaced multifilament |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61119737A (en) |
-
1984
- 1984-11-16 JP JP24279984A patent/JPS61119737A/en active Pending
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