JPH01201519A - Production of polyethylene terephthalate based polyester fiber - Google Patents
Production of polyethylene terephthalate based polyester fiberInfo
- Publication number
- JPH01201519A JPH01201519A JP2461288A JP2461288A JPH01201519A JP H01201519 A JPH01201519 A JP H01201519A JP 2461288 A JP2461288 A JP 2461288A JP 2461288 A JP2461288 A JP 2461288A JP H01201519 A JPH01201519 A JP H01201519A
- Authority
- JP
- Japan
- Prior art keywords
- fiber
- specific gravity
- organic solvent
- ethylene terephthalate
- highly oriented
- 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.)
- Granted
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 58
- 229920000728 polyester Polymers 0.000 title claims abstract description 36
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- -1 polyethylene terephthalate Polymers 0.000 title description 5
- 229920000139 polyethylene terephthalate Polymers 0.000 title description 5
- 239000005020 polyethylene terephthalate Substances 0.000 title description 5
- 230000005484 gravity Effects 0.000 claims abstract description 25
- 239000003960 organic solvent Substances 0.000 claims abstract description 13
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical compound C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 claims abstract description 9
- 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 abstract description 5
- 239000000470 constituent Substances 0.000 claims abstract description 5
- 230000001747 exhibiting effect Effects 0.000 claims abstract 2
- 238000000034 method Methods 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 9
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 abstract description 12
- 239000000243 solution Substances 0.000 abstract description 10
- 238000007598 dipping method Methods 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 239000007864 aqueous solution Substances 0.000 abstract description 5
- 239000012770 industrial material Substances 0.000 abstract description 3
- 238000002844 melting Methods 0.000 abstract description 2
- 230000008018 melting Effects 0.000 abstract description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 238000009987 spinning Methods 0.000 abstract 1
- 230000000704 physical effect Effects 0.000 description 10
- 238000007654 immersion Methods 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 238000010791 quenching Methods 0.000 description 4
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 230000009477 glass transition Effects 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 230000002522 swelling effect Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- WXNZTHHGJRFXKQ-UHFFFAOYSA-N 4-chlorophenol Chemical compound OC1=CC=C(Cl)C=C1 WXNZTHHGJRFXKQ-UHFFFAOYSA-N 0.000 description 1
- 229920008790 Amorphous Polyethylene terephthalate Polymers 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- SRSXLGNVWSONIS-UHFFFAOYSA-N benzenesulfonic acid Chemical compound OS(=O)(=O)C1=CC=CC=C1 SRSXLGNVWSONIS-UHFFFAOYSA-N 0.000 description 1
- 229940092714 benzenesulfonic acid Drugs 0.000 description 1
- 235000019445 benzyl alcohol Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- RXOHFPCZGPKIRD-UHFFFAOYSA-N naphthalene-2,6-dicarboxylic acid Chemical compound C1=C(C(O)=O)C=CC2=CC(C(=O)O)=CC=C21 RXOHFPCZGPKIRD-UHFFFAOYSA-N 0.000 description 1
- LYGJENNIWJXYER-UHFFFAOYSA-N nitromethane Chemical compound C[N+]([O-])=O LYGJENNIWJXYER-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 230000003595 spectral effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Chemical Or Physical Treatment Of Fibers (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Artificial Filaments (AREA)
- Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、エチレンテレフタレート系ポリエステル繊維
の製造法に関するものであり、更に詳しくは高配向低比
重ポリエステル繊維の延伸方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing ethylene terephthalate polyester fibers, and more particularly to a method for drawing highly oriented low specific gravity polyester fibers.
本発明の製造方法は、特に高強力高弾性率ポリエステル
繊維を得る方法として好適であり、本発明の方法で得ら
れた繊維は産業資材用に主として用いられる。The production method of the present invention is particularly suitable as a method for obtaining high-strength, high-modulus polyester fibers, and the fibers obtained by the method of the present invention are mainly used for industrial materials.
(従来の技術)
エチレンテレフタレート系ポリエステル繊維は、通常工
業的には、極限粘度■が1.2未満のポリマーを融点以
上の温度で溶融紡糸し、熱延伸、熱処理することにより
得られる。(Prior Art) Ethylene terephthalate polyester fibers are usually obtained industrially by melt-spinning a polymer having an intrinsic viscosity of less than 1.2 at a temperature above the melting point, followed by hot drawing and heat treatment.
このような従来技術で得られる延伸糸の物性値は産業資
材用高強力フィラメントで、破断強度6〜10g/d、
初期弾性率80〜160g/dであり、実質的には、破
断強度9.5g/d、初期弾性率120g/dのものが
、工業的に得られ得る最高のレベルの物性値である。The physical properties of the drawn yarn obtained by such conventional techniques are high strength filaments for industrial materials, with a breaking strength of 6 to 10 g/d,
The initial elastic modulus is 80 to 160 g/d, and substantially the highest level of physical property values that can be obtained industrially is a breaking strength of 9.5 g/d and an initial elastic modulus of 120 g/d.
一方、高物性化を目的とする方法として、高度に配向し
、且つ低比重で低結晶性のポリエステル繊維をまず形成
した後、延伸熱処理する方法が古くから考えられており
、たとえば特開昭58−210590号公報によれば、
レーザー光を用いた延伸により、高配向低比重のポリエ
ステル系繊維が得られること及び、高配向低比重のポリ
エステル繊維を熱処理することにより高物性化すること
が知られている。On the other hand, as a method for improving physical properties, a method has long been considered in which highly oriented polyester fibers with low specific gravity and low crystallinity are first formed and then subjected to stretching heat treatment. According to the -210590 publication,
It is known that highly oriented, low specific gravity polyester fibers can be obtained by stretching with laser light, and that physical properties can be improved by heat treating highly oriented, low specific gravity polyester fibers.
また、高度に配向し、且つ低比重のポリエステル繊維は
、ガラス転移温度以下の温度で延伸を行うことによって
得ることが、高分子論文集(vo142、 PP159
〜166.1985)で知られている。In addition, it is reported in Kobunshi Proceedings (Vol. 142, PP 159) that highly oriented polyester fibers with low specific gravity can be obtained by drawing at a temperature below the glass transition temperature.
~166.1985).
さらに、特開昭58−169513号公報によれば、テ
クスチャー加工用の高速紡糸された無定形ポリエチレン
テレフタレート糸の製造に関し、紡出糸条を紡糸口金下
方位置に置かれた液体浴中で急冷することが知られてい
る。Furthermore, according to JP-A-58-169513, regarding the production of high-speed spun amorphous polyethylene terephthalate yarn for texturing, the spun yarn is rapidly cooled in a liquid bath placed below the spinneret. It is known.
(発明が解決しようとする課題)
ポリエステル繊維の高物性化に際し、高配向で且つ低比
重、低結晶性のポリエステル繊維の延伸熱処理を行う際
、わずかな熱を付与するだけで結晶化が急速に進行して
しまい延伸性が低く、十分な高物性化が困難であるとい
う問題があり、本発明はこの問題点を前記従来方法での
問題点を含めて解決することを主要な課題とし、高配向
低比重ポリエステル繊維の高強度高弾性率化を目的とし
た優れた延伸方法を提供せんとするものである。(Problems to be Solved by the Invention) In order to improve the physical properties of polyester fibers, when performing drawing heat treatment on polyester fibers with high orientation, low specific gravity, and low crystallinity, it is necessary to rapidly crystallize the polyester fibers by applying only a small amount of heat. There is a problem in that the stretchability is low and it is difficult to obtain sufficiently high physical properties.The main objective of the present invention is to solve this problem including the problems with the conventional method. It is an object of the present invention to provide an excellent stretching method for increasing the strength and modulus of oriented low-density polyester fibers.
(課題を解決するための手段)
即ち、本発明は、エチレンテレフタレート単位を主構成
単位とするポリエステルであり、複屈折率△nならびに
比重SGが下式(イ)および(ロ)で示される範囲にあ
る高配向低結晶性ポリエステル繊維を7.5〜15.0
の溶解度パラメータを示す有機溶剤を含有する液浴中で
浸漬処理した後、引き続きあるいは一旦前記有機溶剤を
実質的に含まない状態に処理した後、延伸することを特
徴とするエチレンテレフタレート系ポリエステル繊維の
製造法である。(Means for Solving the Problems) That is, the present invention is a polyester having ethylene terephthalate units as a main constituent unit, and having a birefringence Δn and a specific gravity SG in the ranges shown by the following formulas (a) and (b). Highly oriented low crystalline polyester fibers in the range of 7.5 to 15.0
The ethylene terephthalate polyester fiber is immersed in a liquid bath containing an organic solvent having a solubility parameter of It is a manufacturing method.
△n≧55G −6,64−−−−−−(イ)Δn≧0
.100 ・・・・・・・−・・・・・・・・・・
・(ロ)本発明に用いるポリエステル繊維を形成するポ
リエステル成分は、エチレンテレフタレート単位を主構
成単位とするものであって、通常エチレンテレフタレー
ト単位を85モル%以上含むポリエステルもしくはホモ
ポリエステルまたはそれらのポリエステル混合物である
。テレフタール酸、エチレングリコール以外の共重合成
分としては、イソフタール酸、2.6−ナフタリンジカ
ルボン酸、アジピン酸、セバシン酸、シェラ酸、ジエチ
レングリコール、プロピレングリコール、シクロヘキサ
ンジメタツール、P−オキシ安息香酸、3.5−ジ(カ
ルボメトキシ)ベンゼンスホン酸金属塩、あるいはこれ
らの誘導体などが挙げられるが以上の具体例に限定され
るものではない。△n≧55G −6,64−−−−−(a) Δn≧0
.. 100 ・・・・・・・・・-・・・・・・・・・・
(b) The polyester component forming the polyester fiber used in the present invention has ethylene terephthalate units as its main constituent unit, and is usually a polyester or homopolyester or a polyester mixture thereof containing 85 mol% or more of ethylene terephthalate units. It is. Copolymerization components other than terephthalic acid and ethylene glycol include isophthalic acid, 2,6-naphthalene dicarboxylic acid, adipic acid, sebacic acid, sheracic acid, diethylene glycol, propylene glycol, cyclohexane dimetatool, P-oxybenzoic acid, 3 Examples include 5-di(carbomethoxy)benzenesulfonic acid metal salts and derivatives thereof, but are not limited to the above specific examples.
本発明に用いられる繊維は複屈折率Δn(配高度のパラ
メータ)と比重SG (結晶化度のパラメータ)の関係
が(イ)式を満たすと同時に複屈折率(八〇)が(ロ)
式を満たすものである。The fiber used in the present invention has a relationship between birefringence Δn (parameter of orientation degree) and specific gravity SG (parameter of degree of crystallinity) that satisfies equation (a), and at the same time, the birefringence (80) satisfies equation (b).
It satisfies the formula.
(イ)式を満足しない場合、該繊維は配向度、即ちΔn
の上昇に伴う分子鎖バッキング性向上による密度の向上
以上に密度が向上することになり、この場合、配向結晶
化が起きてしまう。If the formula (a) is not satisfied, the fiber has a degree of orientation, that is, Δn
The density increases more than the increase in density due to the improvement in molecular chain backing properties associated with the increase in , and in this case, oriented crystallization occurs.
このような構造を有する本発明に用いられる繊維は、更
に延伸熱処理し高物性化をはかる際に結晶化された部分
が少ないため、通常の配向結晶化した繊維よりもはるか
に容易に高物性化できるという特徴があると考えられる
が、通常の延伸熱処理法では、延伸が起こる前に結晶化
が起ってしまい、本発明の意図する効果が達成できない
。The fibers used in the present invention, which have such a structure, have fewer crystallized parts when further drawn and heat treated to improve physical properties, so it is much easier to improve physical properties than ordinary oriented crystallized fibers. However, in the ordinary stretching heat treatment method, crystallization occurs before stretching occurs, making it impossible to achieve the intended effects of the present invention.
本発明に用いられる繊維の複屈折率(Δn)は(ロ)弐
を満足するもので、好ましくはΔnが100 X 10
−h〜270X10弓テアル。The birefringence index (Δn) of the fiber used in the present invention satisfies (b) 2, and preferably Δn is 100 x 10
-h~270X10 bow teal.
ここでΔnが100XIO−’より低いと力学的特性が
劣るので好ましくない、一方、Δnが0.27を越える
と力学的特性が極端に低下してい(、この理由は明らか
でないが、分子鎖が伸長され過ぎて素抜けするのではな
いかと想像される。If Δn is lower than 100 I imagine that it will be stretched too much and fall through.
本発明に用いられる繊維の好ましい比重(SC)の下限
は1.335である。 1.335より低くなるものは
、繊維中にボイドを生成しており、力学的特性が著しく
低下するので好ましくない、なお、(SG)が適正域の
ものでもボイドを生成しているものは好ましくない。The lower limit of the preferred specific gravity (SC) of the fibers used in the present invention is 1.335. If it is lower than 1.335, voids are generated in the fiber, which significantly reduces the mechanical properties, so it is not preferable.Even if (SG) is within the appropriate range, it is preferable if voids are generated. do not have.
本発明に用いられる繊維は、このようなΔnとSGから
見た高配向非品性を有している。The fiber used in the present invention has high orientation quality as seen from such Δn and SG.
本発明者等は、かかる高配向非品性を有するポリエステ
ル繊維の最も有効な延伸方法を検討した結果、本発明に
至った。The present inventors investigated the most effective method for stretching polyester fibers having such high orientation quality, and as a result, they arrived at the present invention.
本発明では、前記高配向非非品性ポリエステル繊維を延
伸するに際して、該繊維を7.5〜15.0の溶解度パ
ラメーターを示す有機溶剤を含有する液浴中に浸漬する
。In the present invention, when drawing the highly oriented non-defective polyester fibers, the fibers are immersed in a liquid bath containing an organic solvent having a solubility parameter of 7.5 to 15.0.
かかる浸漬処理により、繊維を膨潤せしめて延伸性を高
めるところが最も重要な点である。The most important point is that this dipping treatment swells the fibers and increases their drawability.
ここで浸漬処理に用いられる液浴は、エチレンテレフタ
レート系ポリエステルになじみやすい2容液であること
が必要である0本発明者等は、溶解度パラメーターが7
.5〜15.0の有機溶剤からなる溶ン夜が、8亥ポリ
エステル繊維となじみやすいことを見い出したが、その
メカニズムはまだよくわかっていない。The liquid bath used for the immersion treatment here needs to be a 2-volume liquid that is easily compatible with the ethylene terephthalate polyester.
.. It has been found that a solvent consisting of an organic solvent of 5 to 15.0% is easily compatible with 80% polyester fibers, but the mechanism is not yet well understood.
ポリエチレンテレフタレートの溶解度パラメーターは、
10.7でありポリエチレンテレフタレートを膨潤させ
る有機溶剤の溶解度パラメーターは、9.7及び12.
0付近に膨潤効果の二極大を有している。したがって有
機溶剤の溶解度パラメーターが、9.5以上、12.5
以下のものが好ましく、例えばクロルベンゼン(9,5
:溶解度パラメータ以下数値のみ記入)、ニトロベンゼ
ン(10,0) 、ジクロロメタン(9,7)、ニトロ
メタン(12,30)、アセトン(10,0)、ジオキ
サン(10,05)、ベンジルアルコール(11,97
)、ジメチルホルムアミド(12,1)等が、代表的な
ものであるが、もちろんこれに限定されるものではない
。The solubility parameter of polyethylene terephthalate is
10.7, and the solubility parameters of the organic solvent that swells polyethylene terephthalate are 9.7 and 12.
There are two maxima of the swelling effect near 0. Therefore, the solubility parameter of the organic solvent is 9.5 or more, 12.5
The following are preferred, for example chlorobenzene (9,5
: Solubility parameters (enter only numerical values below), nitrobenzene (10,0), dichloromethane (9,7), nitromethane (12,30), acetone (10,0), dioxane (10,05), benzyl alcohol (11,97)
), dimethylformamide (12,1), etc. are typical examples, but the present invention is not limited thereto.
ここで有機溶剤の溶解度パラメーターが7.5未満の場
合あるいは15.0より高い値を示すものは、膨潤効果
が低下し、目的とする延伸性の向上が得られなくなるの
で好ましくない。If the solubility parameter of the organic solvent is less than 7.5 or higher than 15.0, the swelling effect will decrease and the desired improvement in stretchability will not be achieved, which is not preferred.
ここで言う溶解度パラメーターとは、液体間の混合性の
尺度となる液体の特性値で、J 、 11 。The solubility parameter referred to here is a characteristic value of a liquid that is a measure of miscibility between liquids, and is J, 11.
旧1debrandにより提唱され、δで表される。液
体の分子凝集エネルギーをE、分子容をVとするδ=
(E/V)”
で与えられ、温度だけに依存する物質定数である。It was proposed by the former 1debrand and is represented by δ. δ = where E is the molecular cohesive energy of the liquid and V is the molecular volume.
(E/V)" and is a material constant that depends only on temperature.
さらに本発明に用いられる有機溶剤としては、エチレン
テレフタレート系ポリエステル未延伸糸が有するガラス
転移点温度より低い温度で未延伸糸を膨潤させ、その結
果、そのガラス転移点温度を低下させるものである。さ
らに該溶液の浸漬速度及び膨潤効果を向上させるには、
有機溶剤がアセトンであること、溶液が水溶液であるこ
と、溶液の温度が沸点以下であれば高ければ高い程、好
ましい。Further, the organic solvent used in the present invention is one that swells the undrawn yarn at a temperature lower than the glass transition temperature of the undrawn ethylene terephthalate polyester yarn, thereby lowering its glass transition temperature. Furthermore, to improve the dipping speed and swelling effect of the solution,
It is more preferable that the organic solvent is acetone, that the solution is an aqueous solution, and that the temperature of the solution is lower than the boiling point.
又、エチレンテレフタレート系ポリエステル繊維の中で
は、得られる破断強度、初期弾性重大々のレベルの高さ
から、ポリエチレンテレフタレート繊維が最も好ましい
。Moreover, among the ethylene terephthalate-based polyester fibers, polyethylene terephthalate fibers are most preferable because of the high breaking strength and initial elasticity that can be obtained.
当然、本発明の趣旨からも、浸漬処理された該繊維の中
心部まで、溶液を浸透させることが、最も好ましい。該
繊維の中心部にまで溶液を浸透させるためには該繊維の
複屈折率Δn及び比重SGのレベルに従って、適正な浸
漬時間、浸漬温度及び溶液の化学組成が必要であること
は言うまでもない。Naturally, in view of the spirit of the present invention, it is most preferable to allow the solution to penetrate into the center of the fibers that have been subjected to the soaking treatment. Needless to say, in order to penetrate the solution into the center of the fiber, appropriate dipping time, dipping temperature, and chemical composition of the solution are required according to the birefringence Δn and specific gravity SG level of the fiber.
溶液が該繊維の中心部にまで浸透するに要する浸漬条件
は、処理された繊維を干渉顕微鏡で観察することにより
fli tvできる。The dipping conditions required for the solution to penetrate into the core of the fiber can be determined by observing the treated fiber under an interference microscope.
第2図に(a、b、c、d)未処理系と浸漬処理の程度
による干渉縞の変化挙動を示すが、処理時間を長くする
ことにより、溶液が浸透していく様子がよくわかる。FIG. 2 (a, b, c, d) shows the change behavior of interference fringes depending on the untreated system and the degree of immersion treatment, and it can be clearly seen that the solution penetrates as the treatment time increases.
このようにして、浸漬処理された高配向非品性のポリエ
ステル繊維は、常法に従い、延伸温度100〜350℃
、延伸倍率1.02〜2.00倍で、延伸熱処理される
が、延伸熱処理に際し、加熱ローラー延伸を行うよりは
、常温のフィードローラーと、ローラー間に設置したヒ
ーターと、ドローローラーの組み合せが好ましい。In this way, the highly oriented non-quality polyester fibers subjected to the dip treatment are drawn at a stretching temperature of 100 to 350°C according to a conventional method.
, a stretching heat treatment is performed at a stretching ratio of 1.02 to 2.00 times, but during the stretching heat treatment, rather than performing heated roller stretching, a combination of a feed roller at room temperature, a heater installed between the rollers, and a draw roller is used. preferable.
高物性化するには、2段以上の多段延伸及び、それに引
き続くリラックス処理を行った後、巻き取ることが好ま
しい。In order to improve the physical properties, it is preferable to perform multi-stage stretching of two or more stages, followed by a relaxing treatment, and then wind up.
次に本発明で用いた物性値の測定法について説明する。Next, a method for measuring physical property values used in the present invention will be explained.
〈極限粘度■の測定法〉
本発明において、エチレンテレフタレート系ポリエステ
ルの極限粘度■は、P−クロルフェノール/テトラクロ
ルエタン−3/1混合溶媒を用い、30°Cで測定した
極限粘度〔η〕を次式によりフェノール/テトラクロル
エタン=60/40の極限粘度IVに換算したものであ
る。<Method for measuring intrinsic viscosity (■)> In the present invention, the intrinsic viscosity (■) of ethylene terephthalate polyester is the intrinsic viscosity [η] measured at 30°C using a P-chlorophenol/tetrachloroethane-3/1 mixed solvent. is converted into the intrinsic viscosity IV of phenol/tetrachloroethane=60/40 using the following formula.
rV = 0.8325 X (η) +0.oos〈
繊維の繊度の測定法〉
標準状態(温度20±2°C1相対湿度65±2%の状
態)の試験室で、サーチ■製のオートバイブロ式繊度測
定器DENIERCOMPUT[!R[1C−11B型
を使用して、単繊維の繊度(デニール、d)を測定した
。rV = 0.8325 X (η) +0. oos〈
Measuring method of fiber fineness〉 In a test room under standard conditions (temperature 20 ± 2°C, relative humidity 65 ± 2%), an autobibro type fineness measuring device manufactured by Saatchi ■ DENIERCOMPUT [! The fineness (denier, d) of single fibers was measured using R[1C-11B type.
但し、繊維の測定試料長は、50mmとした。However, the fiber measurement sample length was 50 mm.
〈繊維の強度の測定法〉
繊維の引張強さ(強度)は、JIS−L−1013(1
981)の7.5.1に準じ、標準状態の試験室で、東
洋ボールドウィン■製の定速伸長形万能引張試験機TE
NSILON UTM−IIIを使用して単繊維の引張
強さを測した。<Measurement method of fiber strength> The tensile strength (strength) of fibers is determined according to JIS-L-1013 (1
In accordance with 7.5.1 of 981), in a test room under standard conditions, a constant speed extension type universal tensile tester TE manufactured by Toyo Baldwin ■ was used.
The tensile strength of single fibers was measured using NSILON UTM-III.
但し、測定条件は、5kgfの引張型ロードセルを用い
、つかみ間隔10c+a引張速度10cm/分(1分間
当たりつかみ間隔の100%の伸長速度)、記録紙の送
り速度100cm/分で試料を引張り、試料が切断した
時の荷重(gf)を測定し次の式により引張強さ(gf
/d)を算出し強度(g/d)とした。However, the measurement conditions were as follows: using a 5 kgf tensile load cell, pulling the sample at a gripping interval of 10c+a at a pulling speed of 10cm/min (extension speed of 100% of the gripping interval per minute), and a recording paper feed rate of 100cm/min. Measure the load (gf) when the material is cut, and calculate the tensile strength (gf) using the following formula.
/d) was calculated and defined as the strength (g/d).
繊維の初期引張抵抗度(初期引張弾性率)は、JIS−
L−1013(1981)の7.5.1に準じた上記の
繊維の強度の測定法と同じ方法で試験をおこない記録紙
上に荷重−伸長曲線を描きこの図より、JIS−L−1
013(1981)の7.lOに記載の初期引張抵抗度
算出式により、初期引張抵抗度(gf/d)を算出し、
初期引張弾性率(g/d)とした。The initial tensile resistance (initial tensile modulus) of the fiber is JIS-
The test was conducted using the same method as the above method for measuring fiber strength according to 7.5.1 of L-1013 (1981), and a load-elongation curve was drawn on the recording paper. From this figure, JIS-L-1
7 of 013 (1981). Calculate the initial tensile resistance (gf/d) using the initial tensile resistance calculation formula described in 1O,
It was defined as the initial tensile modulus (g/d).
く比重の測定法〉
n−へブタンと四塩化炭素よりなる密度勾配管を作成し
、30°C±0.1℃に調温された密度勾配中に十分に
脱泡した試料を入れ、5時間放置後の密度勾配管中の試
料位置を、密度勾配管の目盛りで読みとった値を、標準
ガラスフロートによる密度勾配管目盛〜比重キャリブレ
ーショングラフから比重値に換算し、n=4で測定、比
重値は原則として小数点以下4桁まで読む。Measuring method of specific gravity> Prepare a density gradient tube made of n-hebutane and carbon tetrachloride, place a sufficiently defoamed sample into the density gradient whose temperature is controlled to 30°C ± 0.1°C, and The sample position in the density gradient tube after being left for a while was read on the scale of the density gradient tube, and the value was converted into a specific gravity value from the density gradient tube scale - specific gravity calibration graph using a standard glass float, and measured at n = 4. As a general rule, read specific gravity values to four decimal places.
く複屈折率(Δn)の測定法〉
ニコン偏光顕微鏡Po1l型ライッ社ペレックコンペン
セーターを用い、光源としてはスペクトル光源用起動装
置(東芝5LS−3−B型)を用いた(Na光源)、5
〜6+wm長の繊維軸に対し45″の角度に切断した試
料を、切断面を上にして、スライドグラス上に載せる。Measuring method of birefringence (Δn) A Nikon polarizing microscope Po1l type Lyc Perec compensator was used, and a spectral light source activation device (Toshiba 5LS-3-B type) was used as the light source (Na light source), 5
A sample cut at a 45″ angle to the fiber axis of ~6+wm length is placed on a glass slide with the cut side facing up.
試料スライドグラスを回転載物台にのせ、試料が偏光子
に対して45°になる様、回転載物台を回転させて調節
し、アナライザーを挿入し暗視界とした後、コンペンセ
ーターを30にして縞数を数える(n個)。コンペンセ
ーターを右ネジ方向にまわして試料が最初に暗くなる点
のコンペンセーターの目盛a1コンペンセーターを左ネ
ジ方向にまわして試料が最初に一番暗くなる点のコンペ
ンセーターの目盛すを測定した後(いずれも1/10目
盛まで読む)、コンペンセーターを30にもどしてアナ
ライザーをはずし、試料の直径dを測定し、下記の式に
もとづき複屈折率(八〇)を算出する(測定数20個の
平均値)。Place the sample slide glass on the rotating stage, adjust the rotating stage so that the sample is at a 45° angle to the polarizer, insert the analyzer, set the dark field, and set the compensator to 30°. count the number of stripes (n pieces). Turn the compensator clockwise to measure the scale a1 of the compensator at the point where the sample first becomes darkest.Turn the compensator clockwise to measure the scale of the compensator at the point where the sample first becomes darkest. (read up to 1/10 scale), return the compensator to 30, remove the analyzer, measure the diameter d of the sample, and calculate the birefringence (80) based on the following formula (20 measurements) average value).
Δn=r’/d(1”ニレタープ−ジョン、=nλ。+
ε)
λ。−589,8mμ
82542社のコンペンセーターの説明書のC/100
00とiより求める
1=(a−b)(:コンペンセーターの読みの差)
(実施例)
以下に実施例を示すが、云うまでもなく本発明は、この
実施例に限定されるものではない。Δn=r'/d(1"Ni-Lapsion,=nλ.+
ε) λ. -589,8mμ 82542 compensator manual C/100
1 determined from 00 and i = (a-b) (: difference in compensator reading) (Example) An example is shown below, but it goes without saying that the present invention is not limited to this example. do not have.
実施例1
極限粘度TV1.0のポリエチレンテレフタレートを紡
糸温度310″Cにて、紡糸口金孔直径0,4M、口金
孔数24孔を有する紡糸口金より単孔当り1 、5g/
分、吐出速度Voが11.4m/分で吐出させて引取速
度Vw4200m/分で引取った。Example 1 Polyethylene terephthalate having an intrinsic viscosity of TV 1.0 was spun at a temperature of 310''C, and 1.5 g/per single hole was spun from a spinneret having a spinneret hole diameter of 0.4 M and a spinneret number of 24 holes.
The sample was discharged at a discharge speed Vo of 11.4 m/min and taken up at a take-up speed Vw of 4200 m/min.
紡出糸条は急冷管に導入した。急冷管上端から5 cr
aは、整流機構により極めて流れが緩やかな状態とし、
Hは25c鳳に設定し、上端から25cm下流の急冷管
下端では、流下方向の流体流速は200On+/分にな
るように調節し、紡糸口金直下36cmの位置に急冷管
が位置するように設置した。このときの冷却流体は、常
温(25°C)の水を用いた。The spun yarn was introduced into a quench tube. 5 cr from the top of the quench tube
a is a state in which the flow is extremely slow due to the rectification mechanism;
H was set to 25 cm, and at the lower end of the quenching tube 25 cm downstream from the upper end, the fluid flow rate in the downstream direction was adjusted to 200 On+/min, and the quenching tube was installed at a position 36 cm directly below the spinneret. . The cooling fluid used at this time was water at room temperature (25°C).
得られた糸のΔnは150 X 10−’、比重は1.
3528であった。この糸の糸断面内の複屈折率Δn分
布は、糸中心のΔnに対して、糸表面のΔnの方が15
X 10−3大きくなっていた。The obtained thread has a Δn of 150 x 10-' and a specific gravity of 1.
It was 3528. The birefringence Δn distribution within the cross section of this yarn is such that Δn at the yarn surface is 15% higher than Δn at the yarn center.
It was larger by X 10-3.
次に、かくして得られた糸を95%のアセトン水溶液に
22°Cで30分間浸漬処理した後、後記する第1表に
示す延伸条件で延伸を行なった。得られた延伸糸の糸質
を第1表に示す。Next, the yarn thus obtained was immersed in a 95% acetone aqueous solution at 22°C for 30 minutes, and then stretched under the stretching conditions shown in Table 1 below. The yarn quality of the obtained drawn yarn is shown in Table 1.
実施例2
実施例1で得られた高配向低比重糸(Δn:150X1
0−’、比重: 1.3528)を用いて、延伸の段階
で延伸回数、熱固定回数および延伸倍率を変化させた以
外は実施例1と同一延伸条件で延伸した。Example 2 Highly oriented low specific gravity yarn obtained in Example 1 (Δn: 150X1
0-', specific gravity: 1.3528), and was stretched under the same stretching conditions as in Example 1, except that the number of stretching, the number of heat setting, and the stretching ratio were changed in the stretching stage.
得られた延伸糸の糸質を第1表に示す。The yarn quality of the obtained drawn yarn is shown in Table 1.
比較例1
実施例1で得られた高配向低比重糸(△n:150Xl
O−’、比重: 1.3528)を用いて、アセトン水
溶液浸漬処理を全く行なわないで、後記第1表に示す延
伸条件で延伸を行なった。得られた延伸糸の糸質を第1
表に示す。Comparative Example 1 Highly oriented low specific gravity yarn obtained in Example 1 (△n: 150Xl
O-', specific gravity: 1.3528), and was stretched under the stretching conditions shown in Table 1 below without any acetone aqueous solution immersion treatment. The quality of the drawn yarn obtained is
Shown in the table.
比較例2
実施例1で得られた高配向低比重糸(Δn:150X1
0−”、比重: 1.3528)を用いて、アセトン水
溶液浸漬処理を行なわないで、延伸の段階で延伸回数、
熱固定回数および延伸倍率を変化させた以外は比較例1
と同一延伸条件で延伸を行なった。Comparative Example 2 Highly oriented low specific gravity yarn obtained in Example 1 (Δn: 150X1
0-'', specific gravity: 1.3528), the number of stretching was adjusted at the stretching stage without immersion treatment in acetone aqueous solution.
Comparative Example 1 except that the number of heat fixing times and stretching ratio were changed
Stretching was carried out under the same stretching conditions.
得られた延伸糸の糸質を第1表に示す。The yarn quality of the obtained drawn yarn is shown in Table 1.
以下余白
第 1 表
(発明の効果)
本発明は以上の如く構成されているので、前記具体例か
ら明らかなように従来法による延伸の場合よりも本発明
の方法の方が得られた糸の機械的物性(破断強度、初期
弾性率、タフネス特性)が優れており、従来に見ない、
高配向低比重ポリエステル繊維の高強度高弾性率化を可
能とした新規な延伸方法が提供できる。Table 1 (Effects of the Invention) The present invention is constructed as described above, and as is clear from the above specific examples, the method of the present invention has a better effect on the yarn obtained by drawing than the conventional method. It has excellent mechanical properties (breaking strength, initial elastic modulus, toughness characteristics), and has unprecedented
It is possible to provide a novel stretching method that makes it possible to increase the strength and modulus of highly oriented low specific gravity polyester fibers.
第1図は本発明に用いる高配向低結晶性ポリエステル繊
維の製造装置の概略を示す図である。
第2図のa w dは本発明における有a溶剤液浴中で
の浸漬処理の前後における繊維の干渉顕微鏡観察結果を
示す図である。
1:紡糸口金
2:糸条
3:取引ローラー
4:油剤付与装置
特許出願人 東洋紡績株式会社
欅1 図
1 勅恭四金
2°糸果
3 引取ロー−
4ン台ミ81 イ寸]ラー衷(痴−
欅2I!1
a bε
l : 未処理系 C: 処理中相〕 :
矧l痢 d : 処理終JFIG. 1 is a diagram schematically showing an apparatus for producing highly oriented, low-crystalline polyester fibers used in the present invention. 2 and 2 are diagrams showing the results of interference microscopic observation of fibers before and after immersion treatment in an a-solvent solution bath according to the present invention. 1: Spinneret 2: Thread 3: Transaction roller 4: Oil agent application device Patent applicant Toyobo Co., Ltd. (Keyaki2I!1 abεl: Unprocessed system C: Processing stage):
Microentery d: End of treatment J
Claims (1)
ポリエステルであり、複屈折率Δnならびに比重SGが
下式(イ)および(ロ)で示される範囲にある高配向低
結晶性ポリエステル繊維を7.5〜15.0の溶解度パ
ラメータを示す有機溶剤を含有する液浴中で浸漬処理し
た後、引き続きあるいは一旦前記有機溶剤を実質的に含
まない状態に処理した後、延伸することを特徴とするエ
チレンテレフタレート系ポリエステル繊維の製造法。 Δn≧5SG−6.64‐‐‐‐‐‐‐‐‐‐‐‐(イ
) Δn≧0.100‐‐‐‐‐‐‐‐‐‐‐‐(ロ)(1) Highly oriented low-crystalline polyester fibers that are polyester whose main constituent units are ethylene terephthalate units and whose birefringence Δn and specific gravity SG are within the ranges shown by the following formulas (a) and (b) are 7.5 Ethylene terephthalate characterized by being immersed in a liquid bath containing an organic solvent exhibiting a solubility parameter of ~15.0, then subsequently or once treated to a state substantially free of the organic solvent, and then stretched. Method for manufacturing polyester fibers. Δn≧5SG-6.64------------(a) Δn≧0.100---------(b)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63024612A JP2581129B2 (en) | 1988-02-03 | 1988-02-03 | Method for producing ethylene terephthalate-based polyester fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63024612A JP2581129B2 (en) | 1988-02-03 | 1988-02-03 | Method for producing ethylene terephthalate-based polyester fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01201519A true JPH01201519A (en) | 1989-08-14 |
| JP2581129B2 JP2581129B2 (en) | 1997-02-12 |
Family
ID=12142973
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63024612A Expired - Fee Related JP2581129B2 (en) | 1988-02-03 | 1988-02-03 | Method for producing ethylene terephthalate-based polyester fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2581129B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008308786A (en) * | 2007-06-14 | 2008-12-25 | Teijin Fibers Ltd | Method for producing high toughness fiber |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5953716A (en) * | 1982-09-22 | 1984-03-28 | Toray Ind Inc | Drawing of polyester fiber |
-
1988
- 1988-02-03 JP JP63024612A patent/JP2581129B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5953716A (en) * | 1982-09-22 | 1984-03-28 | Toray Ind Inc | Drawing of polyester fiber |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008308786A (en) * | 2007-06-14 | 2008-12-25 | Teijin Fibers Ltd | Method for producing high toughness fiber |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2581129B2 (en) | 1997-02-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Allen et al. | High-modulus-high-strength poly-(p-phenylene benzobisthiazole) fibres: Part 1 Heat treatment processing | |
| CA2042099C (en) | Polyketone fibers and a process for making same | |
| KR100402838B1 (en) | Polyester multifilament yarns | |
| JPS5947726B2 (en) | Polyester fiber manufacturing method | |
| JPH0210243B2 (en) | ||
| JPS5865008A (en) | Polyamide fiber with high strength and its production | |
| KR920008540B1 (en) | Direct spinning drawing method of polyester fiber | |
| Murase et al. | Structure and properties of high‐speed spun fibers of nylon 6 | |
| Wu et al. | The effect of a liquid isothermal bath in the threadline on the structure and properties of poly (ethylene terephthalate) fibers | |
| US4851508A (en) | Polyester fibers having high strength and high modulus and process for producing the same | |
| Lin et al. | Poly (ethylene terephthalate) melt spinning via controlled threadline dynamics | |
| EP0912778B1 (en) | Ultra-oriented crystalline filaments and method of making same | |
| JPH01201519A (en) | Production of polyethylene terephthalate based polyester fiber | |
| Suh et al. | Melt spinning and drawing of 2‐methyl‐1, 3‐propanediol‐substituted poly (ethylene terephthalate) | |
| Hamidi et al. | Melt spinning of poly (ethylene terephthalate)—structural transitions in a range of spinning speeds | |
| KR100456340B1 (en) | Process for production of a polyester multifilament yarn for the industrial use | |
| Miyata et al. | Effect of liquid isothermal bath in high-speed melt spinning of poly (ethylene 2, 6-naphthalene dicarboxylate) | |
| KR100595607B1 (en) | Polyethylene-2,6-naphthalate fiber by high speed spinning and radial in-out cooling method and preparation method thereof | |
| KR100233305B1 (en) | Polyester filament yarn and tire cord using the same | |
| KR101118849B1 (en) | A technical polyester multi-filament yarn with high toughness and its manufacturing process | |
| EP0295147A2 (en) | High strength polyester yarn | |
| JPS63159518A (en) | Polyester fiber | |
| JPS60162806A (en) | High-tenacity polyamide fiber of fine denier and production thereof | |
| JPS5854020A (en) | polyester fiber | |
| JPS6399322A (en) | Production of drawn material of polyester of ethylene terephthalate type |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |