JPS5831114A - Production of polyester yarn for hard twisting - Google Patents
Production of polyester yarn for hard twistingInfo
- Publication number
- JPS5831114A JPS5831114A JP12940081A JP12940081A JPS5831114A JP S5831114 A JPS5831114 A JP S5831114A JP 12940081 A JP12940081 A JP 12940081A JP 12940081 A JP12940081 A JP 12940081A JP S5831114 A JPS5831114 A JP S5831114A
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- less
- elongation
- terephthalate
- polyester
- 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
Landscapes
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Abstract
Description
【発明の詳細な説明】
不発明はポリエステル糸、更に詳しくは高度のしぼ立て
竹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。DETAILED DESCRIPTION OF THE INVENTION The invention relates to a method for producing a polyester yarn, more particularly a high twist polyester yarn having a highly grained bamboo.
ポリエステル強撚絨編物を製造する場合、織編工程ある
いはその準イl18工程等における糸の増扱いを容易に
するため、強撚糸条は高温で撚固定(撚止めセット)さ
れるのが普通である。しかしながら、かかる高温での一
時的換固定処理は該処理自体がポリエステルの4#74
維構造を熱変形させ且つシボ発句性も減少させてL−:
F ウため、満足のいく品質のシボmb物を得るのは困
翰1であった。When producing polyester strongly twisted carpet knitted fabrics, the highly twisted yarns are usually twisted and fixed at high temperatures (twist set) to facilitate the handling of yarn in the weaving and knitting process or similar processes. be. However, such temporary exchange and fixation treatment at high temperatures is limited to polyester 4#74.
By thermally deforming the fiber structure and reducing the graininess, L-:
Therefore, it was difficult to obtain a textured material of satisfactory quality.
特に、ポリエステル強撚糸を生産性の、1病いウォータ
ー・ジェット・ルームで′製織しようとする場合、一般
の有杼紗機での製織に比べ、更に高度の撚固定を行わね
ばtCらず、彼ってイーの分だけ高温で撚市めセットを
する事になるので繊維構造の熱弯形は著しくなり、所望
のシボ立て性は殆ど得られないのが3i 9 v 、i
、る。In particular, when attempting to weave polyester highly twisted yarn in a highly productive water jet loom, a higher degree of twist fixation is required compared to weaving with a general shuttle machine. Since the twisting and setting process is carried out at a high temperature corresponding to E, the thermal curvature of the fiber structure becomes significant, and it is almost impossible to obtain the desired texture.
,ru.
本発明の目的は、上記のような問題恢を解決するもので
))す、低温で撚市めセッ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、
シボ立で性、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一工程でい
つきよに製造する方法を提供することにある。The purpose of the present invention is to solve the above-mentioned problems, and is capable of sufficiently fixing the twist even though it is twisted and set at a low temperature, and moreover, when it is made into a woven or knitted fabric. ,
To provide a method for consistently producing a high-twist polyester yarn in which the graininess and grain quality are better than those of conventional polyester in one spinning step.
本発明によればポリエチレンテレフタレート(C,T)
が全量の20〜90wt%、ポリトリメチレンチレフタ
レ−)(CAT)又は/およびポリテトラメチレンテレ
フタレート(C,T)が全量の80〜10wt%の割合
で共重合又は/および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
ーラな用いて熱処理し、asoom/分以上の速度にて
、単糸繊度が2.2de以下、切断伸度が60係以下、
溶水収縮率が7チ以下のマルチフィラメントとして巻取
る事を特徴とする強健用ポリエステル原糸の製造方法が
提供される。According to the invention polyethylene terephthalate (C,T)
is copolymerized or/and blended in a proportion of 20 to 90 wt% of the total amount, and polytrimethylene terephthalate (CAT) or/and polytetramethylene terephthalate (C, T) in a proportion of 80 to 10 wt% of the total amount. The polyester composition is melted and discharged, and after cooling, it is heat-treated using at least one heating roller at a speed of asoom/min or more, so that the single yarn fineness is 2.2 de or less, the cutting elongation is 60 modulus or less,
Provided is a method for producing a strong polyester yarn, which is characterized in that it is wound as a multifilament having a water shrinkage rate of 7 inches or less.
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
C官TとCsT、又はC,TとC4T、又はCITとC
sTとCa Tの如(、グリフ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7+、/ンド
体又は/」、マよひ共jIL合体として組合せる点にあ
る。An important condition in the polyester composition of the present invention is the above-mentioned C-T and CsT, or C, T and C4T, or CIT and C
The point is that polyalkylene terephthalates such as sT and CaT (or polyalkylene terephthalates with different carbon numbers in the gryfur component) are combined with each other as a 7+, /nd or /'' compound.
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
構造を廟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」tが可能
である。しかし乙「がら、本発明においてはCATけ全
yの20〜9゜wt%を占める墨が必をである。C7T
の1が2゜wt%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!l +l wt%を越え
る場合には、本発明の目的とする低温セット伯が失われ
てしまし
更に、cs’r又は2およびC4Tについても全景の8
0〜IOwt%である事が必箒でルー、る。こf]らの
量が80wt%を越えるとシボ織物風合にゴム状のめり
感か強(なり好寸しく lrいうえ、撚固定性も悪<
1する。逆に、10wt%に満たぬ場合にはイ斤潟での
供回定性す、;よび織編1物とした後のシボ発現性がと
もに不充分t【ものと)「4.。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, ink that accounts for 20 to 9 wt% of the total y of the CAT is essential.C7T
If 1 is less than 2 wt%, the texture of the grained fabric tends to deteriorate; on the contrary! If it exceeds l + l wt%, the low-temperature set ratio that is the objective of the present invention is lost, and furthermore, for cs'r or 2 and C4T, the
It is essential that it is between 0 and IOwt%. If the amount exceeds 80 wt%, the texture of the grained fabric will have a strong rubber-like feel (not only will the texture be unsatisfactory, but the twist fixation will also be poor).
Do 1. On the other hand, if the content is less than 10 wt%, both the transferability in the lagoon and the grain development after making into a woven or knitted product are insufficient.
更に、本発明のポリエステル糸は切断伸度が60チ以下
、溶水収縮率が7%以下である事が必要である。切断伸
度が6,0%を越える場合には紗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6
0チを越えるか溶水収縮率が7%を越えるような場合に
は、ボリヱステル原糸の繊維構造は熱力学的に充分安定
したものとなっていないので強撚−撚固定の工程で構造
の変形〜緩和が起り、シボ立ちのための今元力が大半失
われてしまう。Furthermore, the polyester yarn of the present invention must have a breaking elongation of 60 inches or less and a water solution shrinkage rate of 7% or less. If the cutting elongation exceeds 6.0%, the handling of the yarn during the gauze knitting process and its preparation process will be poor. Also, the elongation is 6
If the shrinkage rate exceeds 0% or the water shrinkage rate exceeds 7%, the fiber structure of the polyester yarn is not thermodynamically stable enough, so the structure cannot be changed during the strong twist-fixing process. Deformation and relaxation occur, and most of the original strength needed to create grain is lost.
本発明のポリエステル糸は前記の如<CxT又は/およ
びCsT又は/およびCa Tを主たる成分とするがそ
の他全量の5 wt%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。The polyester yarn of the present invention has CxT or/and CsT or/and CaT as its main components, but it also contains polymers, low molecules or organic compounds for various purposes in a proportion of 5 wt% or less of the total amount. There is no problem even if the inorganic substances are blended and/or copolymerized.
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
レンド又は/および共重合化はポリマーの重合過程にお
いて行っても也いし、いったん各々を重合した後チップ
ブレンドする事に−5=
よっても(紡糸工程でエステル杓分配反応が起るため)
達成する事ができる。Blending and/or copolymerization of polyalkylene terephthalates in the present invention may be carried out during the polymerization process, or may be carried out by once polymerizing each and then chip blending (-5= ester ladle distribution in the spinning process). (because a reaction occurs)
It can be achieved.
以上の如きポリエステル糸は通常の浴融紡糸−巻取、f
伸−熱処理−巻取のように、別工程に分けて製糸する事
もできろ。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f+は、製織、
シボ立て等後加工工程における合理化に加★て、原糸製
造段階でも大幅な合理化をはかる串ができる。The polyester yarn as described above is prepared by normal bath melt spinning and winding.
It would also be possible to split the yarn into separate processes, such as stretching, heat treatment, and winding. However, f+, which completes the spinning of high-twist raw yarn only in the spinning process by high-speed spinning and direct spinning, is not suitable for weaving,
In addition to streamlining post-processing processes such as embossing, it is possible to create a skewer that significantly streamlines the yarn manufacturing stage.
ポリエチレンプレフタレートの高速紡糸−16接製糸に
ついては従来より多くの報告がt「されており、巻取法
度5000〜6000m/分において、巻取糸条の切断
伸度は60チ程度に−i「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、CsT又はC4
T分子鎖が高速紡糸過程においてより効呆的に伸畏され
、その結果4000〜5000 m /分の引取速M’
においても切断伸度は60チリ−■とする事ができる
。特に単繊紐締11が2.2ds以下の場合には、溶融
吐出フィラメントの冷却速IQ’が速くなり、 6−
さらに冷却固化したる級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、3soom/分と
いうようなか?Cり低い紡速においても伸度40〜60
チの糸とする事ができることが判った。There have been many reports on high-speed spinning-16 yarn of polyethylene prephthalate, and at a winding speed of 5000 to 6000 m/min, the cutting elongation of the wound yarn is about 60 inches. However, in the polyester composition used in the present invention, CsT or C4
The T molecular chains are more effectively stretched during the high-speed spinning process, resulting in a take-up speed M' of 4000-5000 m/min.
Also, the cutting elongation can be set to 60 mm. In particular, when the single fiber tying 11 is 2.2 ds or less, the cooling speed IQ' of the molten and discharged filament increases, and the effect of stretching the molecular chains due to friction with air is relatively high even in the case of solidified filament by cooling. Is it like 3 soom/minute because it increases in size? Elongation of 40-60 even at low spinning speed
It turns out that it can be used as a thread.
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、強排除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η速度が3500Tn
Z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。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 roughness and hardness will be strong due to the texture of the strong exclusion material, which is not preferable. In addition, the spinning speed is 3500Tn.
If it is less than Z, it is usually difficult to suppress the cutting elongation of the wound yarn to 60% or less.
紡出糸は冷却固化されたのち巻重Vられる迄の間に少f
、c (とも1個の加熱ローラを用いて熱部P11を受
ける必要がある。もし、′#、熱処理を施さた・い場合
、紡出糸中での結晶形成が不充分となり、巻増糸の潜水
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。After the spun yarn is cooled and solidified, a small amount of
, c (it is necessary to use one heating roller to receive the hot part P11. If heat treatment is not performed, crystal formation in the spun yarn will be insufficient and the winding will increase. The submersion shrinkage rate of the yarn exceeds 7%, and as a result, the grain development as a highly twisted yarn becomes poor.
加熱ローラの表面N度、糸条との接触時間は巻増速度、
目的とするシボ織物品位によって異なるが、一般に18
0℃(好ましくは200℃)以上、および001秒(好
4′シ〈は003抄)以上が望ましい。The surface N degree of the heating roller, the contact time with the yarn is the winding speed,
It varies depending on the desired grained fabric quality, but generally 18
The temperature is preferably 0° C. (preferably 200° C.) or higher and 001 seconds (preferably 003 seconds) or higher.
この熱部fil・の12+、+ 4+1!とじては、第
1図に示1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)とワイングー(W)との間に
配したp−ラf1f−のうち、1ケ又はそれJソ上を加
#p−ラとしたものである。図中、(atけローラIを
、(b)けローラ2,3を、又(c)けローラ1.4を
加熱した例である。勿論4・発明は加熱ローラのみによ
る熱処理に限定さf+るものではtc < 、例えば(
c)に示す如く、スリットヒーター又はプレートヒータ
ー5或いはその仙の加熱手段を補助的に伴用することは
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っ
たウォーター・ジェット・ルームでの製織が可能になる
。四に、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71+1つた強撚紗糾物の連続シボ立て
卯理も可能にt「る。これらは強撚織編物製造のコスト
を大幅に引λ下げるものである。This hot part fil・12+, +4+1! There are various types of closing methods as shown in Fig. 1, but all of these are one of the p-ra f1f- placed between the oiling device (not shown) and the wine goo (W) during spinning. Or add #p-ra to J-so. In the figure, (b) rollers 2 and 3 are heated, and (c) rollers 1.4 are heated.Of course, the invention is limited to the heat treatment using only the heating rollers. For those with tc <, for example (
As shown in c), there is no problem with supplementary use of a slit heater or a plate heater 5 or other heating means.When the polyester yarn spun according to the present invention is made into a strong twist yarn as described above, it is completely different from conventional methods. Weaving using a water jet loom, which was previously impossible, becomes possible. Fourth, it has extremely excellent graining properties, which also makes it possible to create continuous grains on highly twisted gauze materials, which is completely impossible. This significantly reduces λ.
以下実施例により本発明を説明する。The present invention will be explained below with reference to Examples.
実施例1
固有粘度〔η) = 0.64 、艶消剤としてTie
sをo、 o s wt%含むCtT(160℃で4時
間乾燥)と固有粘度〔η) = 0.86の04T(1
20℃で6時間乾燥)をチップ状詐で種々の割合でブレ
ンドl、285〜295°Cで溶融後、直径03冨罠丸
断面孔72個を有する紡糸口金より吐出した。Example 1 Intrinsic viscosity [η) = 0.64, Tie as a matting agent
CtT containing o, o s wt% of s (dried at 160°C for 4 hours) and 04T (1
After drying at 20° C. for 6 hours) was blended in various proportions in the form of chips and melted at 285 to 295° C., it was discharged from a spinneret having 72 holes with a diameter of 03 and a round cross section.
該吐出糸条な通常の争件にて冷却、オイリングL≦・、
第1図−Aの装置を用いて7 s de/ 722fi
/のマルチフィラメントとして巻地った。この時、加熱
p−ラの設電温度は200℃、糸条の加曽、1−ラまわ
りの巻付は数は12ターン。Cooling, oiling L≦・, in the usual case of discharged yarn.
7 s de/722fi using the apparatus of Figure 1-A
/ was wound as a multifilament. At this time, the heating temperature of the heating p-ra was 200°C, and the number of windings around the yarn Kaso and 1-ra was 12 turns.
表m1速度は4oooTn/分であった。Table m1 speed was 4oooTn/min.
次に、上記の巻取糸条なイタリー撚糸材により撚数S
2500 T/Mの撚糸を行い蒸v、X空セッターを用
いて、90℃にてスチーム撚止めセットした。これらの
紡糸巻取糸、および強撚糸 9−
について、繊維物性および撚止めセラl後の残留トルク
、排水処理による発3JJ、 )ルクを第1表に示す。Next, the number of twists S is
The yarn was twisted at 2,500 T/M and set at 90° C. using a steam setter. Table 1 shows the fiber physical properties, the residual torque after twist-stopping, and the torque developed by wastewater treatment for these spun wound yarns and highly twisted yarns.
但し、排水収縮率:沸水中にザンブル糸条なフリー状態
で15分間#漬した時
の収縮率
撚セット後解撚)・ルク:4然11−0めセット後の強
撚糸を4tさ100側採取し、
中央部に2〜/d eθ)荷重を加えた稜、両端を合わ
せて発生する2重
撚数(T150α)
排水発現解撚トルク:撚出めセット後
の強撚糸を持さTOO>採増し、
中央部K 2 kk? /deの荷重を加えた徒、両端
を合わせて排水中にI11痘、この時発生する2重撚数
(T150
鑞)
10−
第1表
第1fiから判るように、AI、2の場合CsT100
%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
の解燃トルクも大きく、製織工程その他での取扱い性が
極めて悪くなる。However, drainage shrinkage rate: Shrinkage rate when soaked in boiling water for 15 minutes in a free state (untwisted after twisting)・Lux: 4 to 11-0 Strongly twisted yarn after setting to 4t and 100 side The number of double twists (T150α) generated by applying a load of 2~/d eθ) to the center and both ends (T150α) Drainage development untwisting torque: Holding the strongly twisted yarn after twisting and setting TOO> Increase in central part K 2 kk? /de load is applied, both ends are combined during drainage, and the number of double twists generated at this time (T150) is 10- As can be seen from Table 1, No. 1fi, in the case of AI, 2, CsT100
% or even if C4T is included, it is too small,
The elongation of the spun yarn becomes high, and the decombustion torque after the highly twisted yarn is set is also large, resulting in extremely poor handling in the weaving process and other processes.
逆に、A7.8においてはC4T100チであるか、C
露T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。Conversely, in A7.8, it is C4T100chi or C
Even if dew T is contained, it is in a small amount, so the high elasticity of C4T cannot be suppressed, and the residual torque after twist setting becomes high, resulting in poor weaving properties.
これに対しA3〜6のj、(9合、紡糸巻1〜糸の仲良
も小さく、撚セラ)・後の残留トルクも小さくlぷり、
後加工での取」んいflか格段に良好になる。On the other hand, J of A3 to 6 (9 go, spun winding 1 ~ thread relationship is small, twisting cellar), the residual torque after is also small,
The removal rate in post-processing is much better.
この時、排水収縮率は若干のj&加を>s−Jが、排水
発現トルクは若干の低下に留th″′)−(おリシホ発
埃性は光分仰保でき゛る。At this time, the drainage contraction rate is slightly increased by >s-J, but the drainage torque is only slightly reduced.
実施例2
実施例Iの強撚糸を緯糸とし、lI7糸にはルートのC
!Tマルチフィラメント(50de/′36 fil三
角断面)を用いて日産WJ L LW−41(Ir!1
転数36 Orpm )による製織を行った1、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ッシ
ャー(ボイル×20分)にてシボ立てを行った結果を第
2表に示す。Example 2 The highly twisted yarn of Example I was used as the weft yarn, and the lI7 yarn had a root C.
! Nissan WJ LW-41 (Ir!1
Table 2 shows the results of the woven fabric 1, which was woven using a rotation speed of 36 orpm), and the woven fabric was scoured with a weak alkali and then embossed using a rotary washer (boil x 20 minutes).
嶽 製織性 ××製織不可△製織一応可× 製織性
不良 ○良好
※壷シボ立て性 ○ 良好 ◎極めて良好、本発明
の場合(43〜扁6)はウォーター・ジェット・ルーム
で製織する事ができシボ立て性も白灯である。Dake Weaving property × × Unable to weave △ Weaving is possible × Poor weaving property ○ Good * Urn texture ○ Good ◎ Very good. In the case of the present invention (43 to 6), it is possible to weave in a water jet loom. The texture is also white.
実施例3
実施f+11のC鵞TとC4Tを70%〜30チの割
13−
合でブレンドし実施例1と同様の条件で溶瀞紡糸1−た
。この場合、加熱p−ラおよび巻取機の速度を1ooo
+71/分〜6ooorn/分の範囲で変更しt:。こ
のときの紡糸巻j代糸の伸度な第3表に示す。Example 3 C-T and C4T of implementation f+11 are divided by 70% to 30
The mixture was blended and melt-spun under the same conditions as in Example 1. In this case, the speed of the heating p-ra and winding machine is set to 1ooo
Changed in the range of +71/min to 6ooorn/min. Table 3 shows the elongation of the substitute yarn of the spinning winding J at this time.
第3表
第3表から判るようにA1.2の場合、巻取速度が低い
ため切断伸度が太き(なり、後加工工程における糸の取
扱い性が慾い。これに対し扁3〜5においては、切断伸
度け6oqAより低くなり増(及い上%に問題はない。Table 3 As can be seen from Table 3, in the case of A1.2, the winding speed is low, so the cutting elongation is large (which makes it difficult to handle the yarn in the post-processing process. In this case, the cutting elongation is lower than 6 oqA (and there is no problem with the upper %).
14−
実施例4
実施例1のC!TとC4Tを70tl)−30チの割合
でブレンドし実施例1と同様にして溶融紡糸しムー。こ
の場合、吐出量な種々変更し単糸de。14- Example 4 C of Example 1! T and C4T were blended at a ratio of 70 tl) to 30 tl and melt-spun in the same manner as in Example 1 to obtain a mu. In this case, the discharge amount was changed in various ways.
l・−タルdeの異なるマルチフィラメントとした。Multifilaments with different l·-tal de were used.
このときの紡糸巻Jll/糸の伸度な第4我に示す。The spinning volume Jll/yarn elongation at this time is shown in Figure 4.
第4表
屓1は卸糸テニールが犬であるため巻取糸の切断伸度が
高い。これに対し屈2〜5においては伸度は60チより
低くなり、後加工工程における取扱い一ヒ特に問題はな
い。In the fourth aspect 1, since the yarn tenier is dog, the cutting elongation of the winding yarn is high. On the other hand, at bends 2 to 5, the elongation is lower than 60 inches, and there is no particular problem in handling in the post-processing process.
実施例5
実施例1のCyTとC4Tを704−:(0φ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r(y糸の伸度および製水収縮率を第
5表に示す。Example 5 CyT and C4T of Example 1 were blended at a ratio of 704-:(0φ) and melt-spun in the same manner as Example 1. In this case, the temperature setting of the heating roller was changed in the range of room temperature to 230°C. Table 5 shows the elongation and water production shrinkage of the spun yarn.
第5表
本実施例の場合、加熱ローラ設定温1(1’が180℃
以上において初めて本発明の倉図する繊細物性を持つポ
リエステル糸が111もれる。Table 5 In this example, heating roller set temperature 1 (1' is 180°C
In the above process, the polyester yarn 111 having the delicate physical properties of the present invention is leaked for the first time.
実施例6
固有粘度〔η) −o、 64 、艶消剤としてTi1
tをo、 o s wt%含むC!T(160℃で4時
間乾燥)と固有粘度〔η) = 0.65のC5T(1
20℃で6時間乾燥)をチッ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なイnた
。このときの原糸(巻取糸条)物性1強撚糸の撚止めセ
ット後の残留トルク、製水発現トルクを第6表に示す。Example 6 Intrinsic viscosity [η) −o, 64, Ti1 as a matting agent
C containing o, o s wt% of t! C5T (1
(dried at 20° C. for 6 hours) were blended in various proportions in the form of chips, and in the same manner as in Example 1 were made into raw yarns and highly twisted yarns. Table 6 shows the physical properties of the raw yarn (wound yarn) and the residual torque and water production torque after twist setting of the 1 strongly twisted yarn.
17一
本発明の場合(篇3〜6)、撚止め七ツト後の残留トル
クは低りl「す、ウォーター・ジェット・ルームでの製
織が”]’ (jl’で七・る。同時に製水処理による
発jJJ l・ルクは相当に高いイ1?1をイV持1−
ており、シボ立て性も也信である。171 In the case of the present invention (parts 3 to 6), the residual torque after twisting is low. The amount of water produced by water treatment is quite high.
The texture is also excellent.
第1図(al (bl (c)けいすかも4発明のツ施
に使用する加熱装置dの例をホす側面図で羽、ろ。
1.2.3.4・・・・・・・・・加熱ローラ5 ・
・・・・・・・・・・0・・神助的加熱手段W ・・・
・・・・・・・・・・・・ワインダー 18−
(戊)(b)
u/LN
(Q)
/ WFigure 1 (al (c) is a side view showing an example of the heating device d used for heating according to the invention. 1.2.3.4...・Heating roller 5 ・
・・・・・・・・・・・・0... Divinely assisted heating means W...
・・・・・・・・・・・・ Winder 18- (戊)(b) u/LN (Q) / W
Claims (1)
b”k量の20〜90wt%、ポリトリメチレンテレ
フタレート(C1T)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チ
の1合で共重合又は/およびブレンドされてなるポリエ
ステル組成物をフィ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3500雇/
分以上の速度にて、単繊維繊度が2−2de以下、切断
伸度が60チ以下、沸水収lR率が7チ以下のマルチフ
ィラメントとして巻取る事を%徴とする強り用ポリエス
テル原糸の製造方法。fi+ polyethylene tereph clay) (C!T)
A polyester composition obtained by copolymerizing or/and blending polytrimethylene terephthalate (C1T) or/' and polytetramethylene terephthalate (C4T) in a proportion of 80 to 10 wt% of the total amount of b''k. The material is melted and discharged as a filament, further cooled and solidified, and then heat treated with a heating roller, and then 3500/
Polyester raw yarn for strength, characterized by being wound as a multifilament with a single fiber fineness of 2-2 de or less, a cutting elongation of 60 inches or less, and a boiling water yield of 7 inches or less, at a speed of 1 minute or more. manufacturing method.
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 true JPS5831114A (en) | 1983-02-23 |
JPS6342007B2 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 (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 |
WO1999027168A1 (en) * | 1997-11-26 | 1999-06-03 | Asahi Kasei Kogyo Kabushiki Kaisha | Polyester fiber with excellent processability and process for producing the same |
US6284370B1 (en) | 1997-11-26 | 2001-09-04 | Asahi Kasei Kabushiki Kaisha | Polyester fiber with excellent processability and process for producing the same |
KR20010112541A (en) * | 2000-06-08 | 2001-12-20 | 조 정 래 | Manufacturing of easily dyeable polyester fiber |
KR20030021968A (en) * | 2001-09-10 | 2003-03-15 | 한국섬유개발연구원 | Method for improving alkali solubility of polytrimethylene terephthalate fiber |
KR100399271B1 (en) * | 2001-02-23 | 2003-09-26 | 주식회사 효성 | Flame retardant polyester fibre |
US6663806B2 (en) * | 2000-03-03 | 2003-12-16 | E. I. Du Pont De Nemours And Company | Processes for making poly (trimethylene terephthalate) yarns |
US7005093B2 (en) | 2003-02-05 | 2006-02-28 | E. I. Du Pont De Nemours And Company | Spin annealed poly(trimethylene terephthalate) yarn |
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 |
CN103789869A (en) * | 2014-02-20 | 2014-05-14 | 浙江万凯新材料有限公司 | Method for producing flat filaments by using PET (Polyethylene Terephthalate) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PH12021552828A1 (en) * | 2019-05-13 | 2022-10-03 | Mitsubishi Electric Corp | Fuel injection valve |
-
1981
- 1981-08-20 JP JP12940081A patent/JPS5831114A/en active Granted
Cited By (13)
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 |
WO1999027168A1 (en) * | 1997-11-26 | 1999-06-03 | Asahi Kasei Kogyo Kabushiki Kaisha | Polyester fiber with excellent processability and process for producing the same |
US6284370B1 (en) | 1997-11-26 | 2001-09-04 | Asahi Kasei Kabushiki Kaisha | Polyester fiber with excellent processability and process for producing the same |
US6692671B2 (en) | 1997-11-26 | 2004-02-17 | Asahi Kasei Kabushiki Kaisha | Process for producing a polyester fiber |
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 |
CN103789869A (en) * | 2014-02-20 | 2014-05-14 | 浙江万凯新材料有限公司 | Method for producing flat filaments by using PET (Polyethylene Terephthalate) |
Also Published As
Publication number | Publication date |
---|---|
JPS6342007B2 (en) | 1988-08-19 |
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