JPS6342007B2 - - Google Patents
Info
- Publication number
- JPS6342007B2 JPS6342007B2 JP12940081A JP12940081A JPS6342007B2 JP S6342007 B2 JPS6342007 B2 JP S6342007B2 JP 12940081 A JP12940081 A JP 12940081A JP 12940081 A JP12940081 A JP 12940081A JP S6342007 B2 JPS6342007 B2 JP S6342007B2
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- less
- elongation
- boiling water
- twist
- 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.)
- Expired
Links
- 238000010438 heat treatment Methods 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 229920000728 polyester Polymers 0.000 claims description 18
- 238000009835 boiling Methods 0.000 claims description 14
- 239000000835 fiber Substances 0.000 claims description 8
- -1 Polyethylene terephthalate Polymers 0.000 claims description 7
- 238000005520 cutting process Methods 0.000 claims description 6
- 238000004804 winding Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 3
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 3
- 229920000874 polytetramethylene terephthalate Polymers 0.000 claims description 2
- 229920002215 polytrimethylene terephthalate Polymers 0.000 claims description 2
- 239000004744 fabric Substances 0.000 description 10
- 238000009941 weaving Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 238000009987 spinning Methods 0.000 description 9
- 238000012805 post-processing Methods 0.000 description 4
- 229920001283 Polyalkylene terephthalate Polymers 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- 229910010413 TiO 2 Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009940 knitting Methods 0.000 description 2
- 239000006224 matting agent Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000010036 direct spinning Methods 0.000 description 1
- 238000004049 embossing Methods 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Description
本発明はポリエステル糸、更に詳しくは高度の
しぼ立て性を有する強撚用ポリエステル原糸の製
造方法に関するものである。
ポリエステル強撚織編物を製造する場合、織編
工程あるいはその準備工程等における糸の取扱い
を容易にするため、強撚糸条は高温で撚固定(撚
止めセツト)されるのが普通である。しかしなが
ら、かかる高温での一時的撚固定処理は該処理自
体がポリエステルの繊維構造を熱変形させ且つシ
ボ発現性も減少させてしまうため、満足のいく品
質のシボ織編物を得るのは困難であつた。
特に、ポリエステル強撚糸を生産性の高いウオ
ーター・ジエツト・ルームで製織しようとする場
合、一般の有杼織機での製織に比べ、更に高度の
撚固定を行わねばならず、従つてその分だけ高温
で撚止めセツトをする事になるので繊維構造の熱
変形は著しくなり、所望のシボ立て性は殆ど得ら
れないのが現状である。
本発明の目的は、上記のような問題点を解決す
るものであり、低温で撚止めセツトするにもかか
わらず撚を充分に固定する事が可能で、しかも織
編物となした場合、シボ立て性、シボの品質が従
来のポリエステル以上に良好なものとなる強撚用
ポリエステル糸を紡糸―工程でいつきよに製造す
る方法を提供することにある。
本発明によればポリエチレンテレフタレート
(C2T)が全量の20〜90wt%、ポリトリメチレン
テレフタレート(C3T)又は/およびポリテトラ
メチレンテレフタレート(C4T)が全量の80〜
10wt%の割合でブレンドされてなるポリエステ
ル組成物を溶融吐出し、冷却後、少なくとも1個
の加熱ローラを用いて熱処理し、3500m/分以上
の速度にて、単糸繊度が2.2de以下、切断伸度が
60%以下、沸水収縮率が7%以下のマルチフイラ
メントとして巻取る事を特徴とする強撚用ポリエ
ステル原糸の製造方法が提供される。
本発明中のポリエステル組成における重要な条
件は前記C2TとC3T、又はC2TとC4T、又はC2T
とC3TとC4Tの如く、グリコール成分の炭素数を
変えたポリアルキレンテレフタレートを相互にブ
レンド体として組合せる点にある。
これらのポリアルキレンテレフタレートは類似
した化学構造を有するためにポリマー同士の相溶
性が良く、一般には如何なる比率でも混ぜあわせ
て製糸することが可能である。しかしながら、本
発明においてはC2Tは全量の20〜90wt%を占め
る事が必要である。C2Tの量が20wt%に満たぬ
場合、シボ織物としての風合が悪くなる傾向があ
り、逆に90wt%を越える場合には、本発明の目
的とする低温セツト性が失われてしまう。
更に、C3T又は/およびC4Tについても全量の
80〜10wt%である事が必要である。これらの量
が80wt%を越えるとシボ織物風合にゴム状ぬめ
り感が強くなり好ましくないうえ、撚固定性も悪
くなる。逆に、10wt%に満たぬ場合には低温で
の撚固定性および織編物とした後のシボ発現性が
ともに不充分なものとなる。
更に、本発明のポリエステル糸は切断伸度が60
%以下、沸水収縮率が7%以下である事が必要で
ある。切断伸度が60%を越える場合には織編工程
およびその準備工程における糸の取り扱い性が悪
くなる。又、伸度が60%を越えるか沸水収縮率が
7%を越えるような場合には、ポリエステル原糸
の繊維構造は熱力学的に充分安定したものとなつ
ていないので強撚―撚固定の工程で構造の変形〜
緩和が起り、シボ立ちのための復元力が大半失わ
れてしまう。
本発明のポリエステル糸は前記の如くC2T又
か/およびC3T又は/およびC4Tを主たる成分と
するがその他全量の5wt%以下の割合で種々の目
的のための高分子、低分子又有機、無機の物質が
ブレンド又は/および共重合されていても差支え
ない。
本発明におけるポリアルキレンテレフタレート
同士のブレンドはポリマーの重合過程において行
つても良いし、いつたん各々を重合した後チツプ
ブレンドする事によつても達成する事ができる。
以上の如きポリエステル糸は通常の溶融紡糸―
巻取、延伸―熱処理―巻取のように、別工程に分
けて製糸する事もできる。しかしながら、高速紡
糸―直接製糸により紡糸工程のみで強撚用原糸の
製糸を完了すれば、製織、シボ立て等後加工工程
における合理化に加えて、原糸製造段階でも大幅
な合理化をはかる事ができる。
ポリエチレンテレフタレートの高速紡糸―直接
製糸については従来より多くの報告がなされてお
り、巻取速度5000〜6000m/分において、巻取糸
条の切断伸度は60%程度になる。しかしながら、
本発明で用いるポリエステル組成物においては、
C3T又はC4T分子鎖が高速紡糸過程においてより
効果的に伸長され、その結果4000〜5000m/分の
引取速度においても切断伸度は60%以下とする事
ができる。特に単繊維繊度が2.2de以下の場合に
は、溶融吐出フイラメントの冷却速度が速くな
り、さらに冷却固化したる後も空気との摩擦によ
る分子鎖の延伸効果が相対的に大きくなるため、
3500m/分というようなかなり低い紡速において
も伸度40〜60%の糸とする事ができることが判つ
た。
他方、単繊維が2.2deを越える場合には上記延
伸効果が小さくなる他、強撚織物の風合からも粗
硬感が強くなり好ましくない。又、紡糸の引取速
度が3500m/分に満たぬ場合には、巻取糸条の切
断伸度を60%以下に抑える事が通常困難になる。
紡出糸は冷却固化されたのち巻取られる迄の間
に少なくとも1個の加熱ローラを用いて熱処理を
受ける必要がある。もし、該熱処理を施さない場
合、紡出糸中での結晶形成が不充分となり、巻取
糸の沸水収縮率は7%を越え、その結果強撚糸と
してのシボ発現性が悪くなる。
加熱ローラの表面温度、糸条との接触時間は巻
取速度、目的とするシボ織物品位によつて異なる
が、一般に180℃(好ましくは200℃)以上、およ
び0.01秒(好ましくは0.03秒)以上が望ましい。
この熱処理の態様としては、第1図に示すよう
に種々あるが、これらは共に紡糸時のオイリング
装置(図示せず)とワインダー(W)との間に配
したローラ群のうち、1ケ又はそれ以上を加熱ロ
ーラとしたものである。図中、aはローラ1を、
bはローラ2,3を、又cはローラ1,4を加熱
した例である。勿論本発明は加熱ローラのみによ
る熱処理に限定されるものではなく、例えばcに
示す如く、スリツトヒーター又はプレートヒータ
ー5或いはその他の加熱手段を補助的に採用する
ことは一向に構わない。
本発明により製糸されたポリエステル糸を前記
の如く強撚糸とした場合、従来全く不可能であつ
たウオーター・ジエツト・ルームでの製織が可能
になる。更に、極めて優れたシボ立て性を有する
ため、これ又、全く不可能であつた強撚織編物の
連続シボ立て処理も可能になる。これらは強撚織
編物製造のコストを大幅に引き下げるものであ
る。
以下実施例により本発明を説明する。
実施例 1
固有粘度〔η〕=0.64、艶消剤としてTiO2を
0.05wt%含むC2T(160℃で4時間乾燥)と固有粘
度〔η〕=0.86のC4T(120℃で6時間乾燥)をチ
ツプ状態で種々の割合でブレンドし、285〜295℃
で溶融後、直径0.3mm丸断面孔72個を有する紡糸
口金より吐出した。
該吐出糸条を通常の条件にて冷却、オイリング
後、第1図―Aの装置を用いて75de/72filのマ
ルチフイラメントとして巻取つた。この時、加熱
ローラの設定温度は200℃、糸条の加熱ローラま
わりの巻付け数は12ターン、表面速度は4000m/
分であつた。
次に、上記の巻取糸条をイタリー撚糸材により
撚数S2500T/Mの撚糸を行い蒸熱真空セツター
を用いて、90℃にてスチーム撚止めセツトした。
これらの紡糸巻取糸、および強撚糸について、繊
維物性および撚止めセツト後の残留トルク、沸水
処理による発現トルクを第1表に示す。
但し、沸水収縮率:沸水中にサンプル糸条をフ
リー状態で15分間浸漬した時の収縮率
撚セツト後解撚トルク:撚止めセツト後
の強撚糸を長さ100cm採取し、中央部
に2mg/deの荷重を加えた後、両端
を合わせて発生する2重撚数(T/50
cm)
沸水発現解撚トルク:撚止めセツト後の
強撚糸を長さ100cm採取し、中央部に
2mg/deの荷重を加えた後、両端を
合わせて沸水中に浸漬、この時発生す
る2重撚数(T/50cm)
The present invention relates to a polyester yarn, and more particularly to a method for producing a high-twist polyester yarn having a high degree of wrinkleability. When producing a polyester strongly twisted woven or knitted fabric, the highly twisted yarn is usually twisted at high temperature (twist set) to facilitate handling of the yarn during the weaving and knitting process or its preparation process. However, such temporary twisting and fixing treatment at high temperatures thermally deforms the polyester fiber structure and also reduces grain development, making it difficult to obtain grained woven or knitted fabrics of satisfactory quality. Ta. In particular, when weaving polyester strongly twisted yarn in a water jet room with high productivity, the twist must be fixed to a higher degree than when weaving on a general shuttle loom, and therefore the weaving temperature is correspondingly higher. At present, the fiber structure undergoes significant thermal deformation because the twisting is stopped and the desired texture is almost impossible to obtain. The object of the present invention is to solve the above-mentioned problems, and is capable of sufficiently fixing the twist even though the twist is set at a low temperature, and when it is made into a woven or knitted fabric, it is possible to prevent the grain from forming. The purpose of the present invention is to provide a method for thoroughly producing a high-twist polyester yarn, which has better texture and grain quality than conventional polyester, through a spinning process. According to the present invention, polyethylene terephthalate (C 2 T) is 20 to 90 wt% of the total amount, and polytrimethylene terephthalate (C 3 T) or/and polytetramethylene terephthalate (C 4 T) is 80 to 90 wt% of the total amount.
A polyester composition blended at a ratio of 10 wt% is melted and discharged, cooled, heat treated using at least one heating roller, and cut at a speed of 3500 m/min or more until the single yarn fineness is 2.2 de or less. The elongation
Provided is a method for producing a high-twist polyester yarn, which is characterized in that it is wound as a multifilament with a boiling water shrinkage rate of 60% or less and a boiling water shrinkage rate of 7% or less. An important condition in the polyester composition in the present invention is the above-mentioned C 2 T and C 3 T, or C 2 T and C 4 T, or C 2 T.
The point is that polyalkylene terephthalates with different carbon numbers in the glycol component, such as C 3 T and C 4 T, are combined together as a blend. Since these polyalkylene terephthalates have similar chemical structures, the polymers have good compatibility with each other, and in general, they can be mixed in any ratio to form yarn. However, in the present invention, C 2 T needs to account for 20 to 90 wt% of the total amount. If the amount of C 2 T is less than 20 wt%, the texture of the textured fabric tends to deteriorate, and if it exceeds 90 wt%, the low temperature setting property, which is the objective of the present invention, will be lost. . Furthermore, the total amount of C 3 T and/or C 4 T
It is necessary that it be 80 to 10 wt%. If the amount exceeds 80 wt%, the texture of the textured fabric will have a strong rubbery, slimy feel, which is undesirable, and the twist fixation will also deteriorate. On the other hand, if the amount is less than 10 wt%, both the twist fixation at low temperatures and the appearance of grain after forming into a woven or knitted fabric will be insufficient. Furthermore, the polyester yarn of the present invention has a breaking elongation of 60
% or less, and the boiling water shrinkage rate must be 7% or less. If the cutting elongation exceeds 60%, the handling of the yarn during the weaving and knitting process and its preparation process will be poor. In addition, if the elongation exceeds 60% or the boiling water shrinkage exceeds 7%, the fiber structure of the polyester yarn is not thermodynamically stable enough, so high twist-fixation is not possible. Structural deformation during the process
Relaxation occurs, and most of the restoring power for graining is lost. As mentioned above, the polyester yarn of the present invention has C 2 T and/or C 3 T and/or C 4 T as its main components, but it also contains polymers and low-carbon materials for various purposes in an amount of 5 wt% or less of the total amount. There is no problem even if molecules or organic and inorganic substances are blended and/or copolymerized. Blending of polyalkylene terephthalates in the present invention may be carried out during the polymerization process of the polymers, or may be achieved by chip-blending them after polymerization. The above polyester yarns are ordinary melt-spun yarns.
It is also possible to spin yarn in separate steps, such as winding, stretching, heat treatment, and winding. However, if high-speed spinning - direct reeling is used to complete spinning of high-twist raw yarn only in the spinning process, in addition to streamlining post-processing processes such as weaving and embossing, it is possible to significantly streamline the raw yarn manufacturing stage. can. There have been many reports on high-speed spinning of polyethylene terephthalate - direct spinning, and at a winding speed of 5,000 to 6,000 m/min, the elongation at break of the wound yarn is approximately 60%. however,
In the polyester composition used in the present invention,
The C 3 T or C 4 T molecular chains are elongated more effectively during the high-speed spinning process, and as a result, even at a take-up speed of 4000 to 5000 m/min, the cutting elongation can be kept at 60% or less. In particular, when the single fiber fineness is 2.2 de or less, the cooling rate of the melt-discharged filament becomes faster, and even after cooling and solidifying, the effect of stretching molecular chains due to friction with air becomes relatively large.
It has been found that yarns with an elongation of 40 to 60% can be obtained even at a fairly low spinning speed of 3500 m/min. On the other hand, if the single fiber exceeds 2.2 DE, not only the above-mentioned stretching effect will be reduced, but also the texture of the highly twisted fabric will be undesirable as it will have a strong rough and hard feel. Further, if the spinning speed is less than 3500 m/min, it is usually difficult to suppress the cutting elongation of the wound yarn to 60% or less. After the spun yarn is cooled and solidified, it is necessary to undergo heat treatment using at least one heating roller before it is wound up. If the heat treatment is not performed, crystal formation in the spun yarn will be insufficient, and the boiling water shrinkage rate of the wound yarn will exceed 7%, resulting in poor grain development as a highly twisted yarn. The surface temperature of the heating roller and the contact time with the yarn vary depending on the winding speed and the desired grained fabric quality, but are generally 180°C (preferably 200°C) or higher and 0.01 seconds (preferably 0.03 seconds) or higher. is desirable. There are various ways to carry out this heat treatment, as shown in Figure 1, but they all involve one or more of the rollers placed between the oiling device (not shown) and the winder (W) during spinning. Anything beyond that is a heating roller. In the figure, a indicates roller 1,
b is an example in which rollers 2 and 3 are heated, and c is an example in which rollers 1 and 4 are heated. Of course, the present invention is not limited to heat treatment using only a heating roller; for example, as shown in c, a slit heater, a plate heater 5, or other heating means may be used as an auxiliary heating means. When the polyester yarn spun according to the present invention is made into a strongly twisted yarn as described above, it becomes possible to weave in a water jet room, which was previously impossible. Furthermore, since it has extremely excellent texturing properties, it also becomes possible to perform continuous texturing on highly twisted woven and knitted fabrics, which was previously impossible. These greatly reduce the cost of producing highly twisted woven and knitted fabrics. The present invention will be explained below with reference to Examples. Example 1 Intrinsic viscosity [η] = 0.64, TiO 2 as a matting agent
C 2 T containing 0.05 wt% (dried at 160°C for 4 hours) and C 4 T with an intrinsic viscosity [η] = 0.86 (dried at 120°C for 6 hours) were blended in various proportions in the form of chips and heated at 285 to 295°C.
After melting, it was discharged from a spinneret having 72 round cross-section holes of 0.3 mm in diameter. The discharged yarn was cooled and oiled under normal conditions, and then wound into a 75de/72fil multifilament using the apparatus shown in FIG. 1-A. At this time, the set temperature of the heating roller is 200℃, the number of turns of the yarn around the heating roller is 12 turns, and the surface speed is 4000 m/
It was hot in minutes. Next, the above-mentioned wound yarn was twisted with an Italian twisting material to a number of twists of S2500T/M, and set by steam twisting at 90° C. using a steam-heating vacuum setter.
Table 1 shows the fiber physical properties, residual torque after twist setting, and torque developed by boiling water treatment for these spun wound yarns and highly twisted yarns. However, boiling water shrinkage rate: shrinkage rate when the sample yarn is immersed in boiling water in a free state for 15 minutes Untwisting torque after twisting and setting: A 100cm long piece of highly twisted yarn after twist setting is taken, and 2mg/ After applying a load of de, the number of double twists (T/50
cm) Untwisting torque developed in boiling water: Take a 100cm long piece of highly twisted yarn after untwisting, apply a load of 2 mg/de to the center, and then immerse both ends together in boiling water. Number of twists (T/50cm)
【表】
第1表から判るように、No.1,2の場合
C2T100%であるかC4Tが含まれていても少量に
過ぎるため、紡糸巻取糸の伸度が高くなり、さら
に強撚糸撚セツト後の解撚トルクも大きく、製織
工程その他での取扱い性が極めて悪くなる。逆
に、No.7,8においてはC4T100%であるか、
C2Tが含まれていても少量であるため、C4Tの持
つ高弾性的性格を抑え切れずに撚セツト後の残留
トルクがやはり高くなり、製織性が劣るようにな
る。
これに対しNo.3〜6の場合、紡糸巻取糸の伸度
も小さく、撚セツト後の残留トルクも小さくな
り、後加工での取扱い性が格段に良好になる。こ
の時、沸水収縮率は若干の増加を示すが、沸水発
現トルクは若干の低下に留まつておりシボ発現性
は充分確保できる。
実施例 2
実施例1の強撚糸を緯糸とし、経糸にはルート
のC2Tマルチフイラメント(50de/36fil三角断
面)を用いて日産WJL LW―41(回転数360rpm)
による製織を行つた。織布については弱アルカリ
による精練を行いロータリーワツシヤー(ボイル
×20分)にてシボ立てを行つた結果を第2表に示
す。[Table] As can be seen from Table 1, in the case of No. 1 and 2
Even if C 2 T is 100% or C 4 T is contained, it is only a small amount, so the elongation of the spun yarn becomes high, and the untwisting torque after twisting and setting of the highly twisted yarn is also large, causing problems in the weaving process and other processes. Handling becomes extremely difficult. On the other hand, in No. 7 and 8, is C 4 T 100%?
Even if C 2 T is contained, it is only in a small amount, so the high elasticity of C 4 T cannot be suppressed, and the residual torque after twist setting becomes high, resulting in poor weaving properties. On the other hand, in the case of Nos. 3 to 6, the elongation of the spun wound yarn is small, the residual torque after twisting and setting is also small, and the handleability in post-processing is much better. At this time, the boiling water shrinkage rate shows a slight increase, but the boiling water developing torque remains at a slight decrease, and the ability to develop grain can be sufficiently ensured. Example 2 The highly twisted yarn of Example 1 was used as the weft, and Root's C 2 T multifilament (50de/36fil triangular cross section) was used as the warp to create Nissan WJL LW-41 (rotation speed 360 rpm).
Weaving was carried out by The woven fabric was scoured with a weak alkali and then embossed using a rotary washer (boil x 20 minutes).Table 2 shows the results.
【表】
本発明の場合(No.3〜No.6)はウオーター・ジ
エツト・ルームで製織する事ができシボ立て性も
良好である。
実施例 3
実施例1のC2TとC4Tを70%〜30%の割合でブ
レンドし実施例1と同様の条件で溶融紡糸した。
この場合、加熱ローラおよび巻取機の速度を1000
m/分〜6000m/分の範囲で変更した。このとき
の紡糸巻取糸の伸度を第3表に示す。[Table] In the case of the present invention (No. 3 to No. 6), weaving can be performed in a water jet room, and the texture is also good. Example 3 C 2 T and C 4 T from Example 1 were blended at a ratio of 70% to 30% and melt-spun under the same conditions as Example 1.
In this case, the speed of the heating roller and winder is set to 1000.
It was changed in the range of m/min to 6000 m/min. Table 3 shows the elongation of the spun yarn at this time.
【表】
第3表から判るようにNo.1,2の場合、巻取速
度が低いため切断伸度が大きくなり、後加工工程
における糸の取扱い性が悪い。これに対しNo.3〜
5においては、切断伸度は60%より低くなり取扱
い上特に問題はない。
実施例 4
実施例1のC2TとC4Tを70%―30%の割合でブ
レンドし実施例1と同様にして溶融紡糸した。こ
の場合、吐出量を種々変更し単糸de、トータル
deの異なるマルチフイラメントとした。このと
きの紡糸巻取糸の伸度を第4表に示す。[Table] As can be seen from Table 3, in the case of Nos. 1 and 2, the winding speed was low, so the cutting elongation was large, and the handling of the yarn in the post-processing process was poor. On the other hand, No. 3~
In No. 5, the cutting elongation was lower than 60% and there were no particular problems in handling. Example 4 C 2 T and C 4 T from Example 1 were blended at a ratio of 70% to 30% and melt-spun in the same manner as in Example 1. In this case, by changing the discharge amount variously, the single yarn de, the total
multifilaments with different de. Table 4 shows the elongation of the spun yarn at this time.
【表】
No.1は単糸デニールが大であるため巻取糸の切
断伸度が高い。これに対しNo.2〜5においては伸
度は60%より低くなり、後加工工程における取扱
い上特に問題はない。
実施例 5
実施例1のC2TとC4Tを70%―30%の割合でブ
レンドし、実施例1と同様にして溶融紡糸した。
この場合、加熱ローラの設定温度を室温〜230℃
の範囲で変更した。紡糸巻取糸の伸度および沸水
収縮率を第5表に示す。[Table] No. 1 has a large single yarn denier, so the cut elongation of the wound yarn is high. On the other hand, in Nos. 2 to 5, the elongation was lower than 60%, and there was no particular problem in handling in the post-processing process. Example 5 C 2 T and C 4 T from Example 1 were blended at a ratio of 70% to 30% and melt-spun in the same manner as in Example 1.
In this case, set the heating roller temperature to between room temperature and 230℃.
changed within the range. Table 5 shows the elongation and boiling water shrinkage of the spun yarn.
【表】
本実施例の場合、加熱ローラ設定温度が180℃
以上において初めて本発明の意図する繊維物性を
持つポリエステル糸が得られる。
実施例 6
固有粘度〔η〕=0.64、艶消剤としてTiO2を
0.05wt%含むC2T(160℃で4時間乾燥)と固有粘
度〔η〕=0.65のC3T(120℃で6時間乾燥)をチ
ツプ状態で種々の割合にブレンドし実施例1と同
様にして原糸および強撚糸を得た。このときの原
糸(巻取糸条)物性、強撚糸の撚止めセツト後の
残留トルク、沸水発現トルクを第6表に示す。[Table] In this example, the heating roller setting temperature is 180℃
Only in the above manner can a polyester yarn having the fiber physical properties intended by the present invention be obtained. Example 6 Intrinsic viscosity [η] = 0.64, using TiO 2 as a matting agent
C 2 T containing 0.05 wt% (dried at 160°C for 4 hours) and C 3 T with intrinsic viscosity [η] = 0.65 (dried at 120°C for 6 hours) were blended in various ratios in the form of chips, and the same as in Example 1 was carried out. Raw yarn and highly twisted yarn were obtained. Table 6 shows the physical properties of the raw yarn (wound yarn), the residual torque after the highly twisted yarn was set to stop twisting, and the boiling water development torque.
【表】
本発明の場合(No.3〜6)、撚止めセツト後の
残留トルクは低くなり、エオーター・ジエツト・
ルームでの製織が可能である。同時に沸水処理に
よる発現トルクは相当に高い値を保持しており、
シボ立て性も良好である。[Table] In the case of the present invention (Nos. 3 to 6), the residual torque after twist setting is low, and the airter, jet,
It is possible to weave in the room. At the same time, the torque developed by boiling water treatment maintains a considerably high value.
The texture is also good.
第1図a,b,cはいずれも本発明の実施に使
用する加熱装置の例を示す側面図である。
1,2,3,4……加熱ローラ、5……補助的
加熱手段、W……ワインダー。
FIGS. 1a, 1b, and 1c are side views each showing an example of a heating device used in carrying out the present invention. 1, 2, 3, 4...heating roller, 5...auxiliary heating means, W...winder.
Claims (1)
の20〜90wt%、ポリトリメチレンテレフタレー
ト(C3T)又は/およびポリテトラメチレンテレ
フタレート(C4T)が全量の80〜10wt%の割合
でブレンドされてなるポリエステル組成物をフイ
ラメントとして溶融吐出し、更に冷却固化後加熱
ローラにより熱処理し次いで3500m/分以上の速
度にて、単繊維繊度が2.2de以下、切断伸度が60
%以下、沸水収縮率が7%以下のマルチフイラメ
ントとして巻取る事を特徴とする強撚用ポリエス
テル原糸の製造方法。1 Polyethylene terephthalate (C 2 T) is blended at a ratio of 20 to 90 wt% of the total amount, and polytrimethylene terephthalate (C 3 T) or/and polytetramethylene terephthalate (C 4 T) is blended at a ratio of 80 to 10 wt% of the total amount. The polyester composition is melted and discharged as a filament, further cooled and solidified, and then heat treated with a heating roller, and then processed at a speed of 3500 m/min or more to obtain a filament with a single fiber fineness of 2.2 de or less and a cutting elongation of 60.
% or less, and winding it as a multifilament with a boiling water shrinkage rate of 7% or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12940081A JPS5831114A (en) | 1981-08-20 | 1981-08-20 | Production of polyester yarn for hard twisting |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12940081A JPS5831114A (en) | 1981-08-20 | 1981-08-20 | Production of polyester yarn for hard twisting |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5831114A JPS5831114A (en) | 1983-02-23 |
| JPS6342007B2 true JPS6342007B2 (en) | 1988-08-19 |
Family
ID=15008621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12940081A Granted JPS5831114A (en) | 1981-08-20 | 1981-08-20 | Production of polyester yarn for hard twisting |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5831114A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020230225A1 (en) * | 2019-05-13 | 2020-11-19 | 三菱電機株式会社 | Fuel injection valve |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59211620A (en) * | 1983-05-12 | 1984-11-30 | Teijin Ltd | Preparation of polyester yarn for woven fabric of hard twist yarn |
| JPS6155213A (en) * | 1984-08-21 | 1986-03-19 | Teijin Ltd | Hard spun polyester yarn for woven or knitted fabrics |
| JPH11172526A (en) | 1997-11-26 | 1999-06-29 | Asahi Chem Ind Co Ltd | Polyester fiber having low thermal stress and spinning thereof |
| US6284370B1 (en) | 1997-11-26 | 2001-09-04 | Asahi Kasei Kabushiki Kaisha | Polyester fiber with excellent processability and process for producing the same |
| KR100587118B1 (en) * | 1999-12-18 | 2006-06-07 | 주식회사 휴비스 | Manufacturing method of polyester fiber having a tone effect |
| KR100622204B1 (en) * | 2000-01-10 | 2006-09-07 | 주식회사 휴비스 | Polytrimethylene terephthalate fiber and its manufacturing method |
| US6663806B2 (en) * | 2000-03-03 | 2003-12-16 | E. I. Du Pont De Nemours And Company | Processes for making poly (trimethylene terephthalate) yarns |
| KR20010112541A (en) * | 2000-06-08 | 2001-12-20 | 조 정 래 | Manufacturing of easily dyeable polyester fiber |
| KR100399271B1 (en) * | 2001-02-23 | 2003-09-26 | 주식회사 효성 | Flame retardant polyester fibre |
| KR20030021968A (en) * | 2001-09-10 | 2003-03-15 | 한국섬유개발연구원 | Method for improving alkali solubility of polytrimethylene terephthalate fiber |
| US7005093B2 (en) | 2003-02-05 | 2006-02-28 | E. I. Du Pont De Nemours And Company | Spin annealed poly(trimethylene terephthalate) yarn |
| CN103789869B (en) * | 2014-02-20 | 2016-08-24 | 浙江万凯新材料有限公司 | A kind of method utilizing PET to produce flat filament |
-
1981
- 1981-08-20 JP JP12940081A patent/JPS5831114A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020230225A1 (en) * | 2019-05-13 | 2020-11-19 | 三菱電機株式会社 | Fuel injection valve |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5831114A (en) | 1983-02-23 |
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