JPS6335747B2 - - Google Patents
Info
- Publication number
- JPS6335747B2 JPS6335747B2 JP57063950A JP6395082A JPS6335747B2 JP S6335747 B2 JPS6335747 B2 JP S6335747B2 JP 57063950 A JP57063950 A JP 57063950A JP 6395082 A JP6395082 A JP 6395082A JP S6335747 B2 JPS6335747 B2 JP S6335747B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- woven
- yarn
- polyester filament
- heat treatment
- 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
- 229920000728 polyester Polymers 0.000 claims description 31
- 239000004744 fabric Substances 0.000 claims description 27
- 238000010438 heat treatment Methods 0.000 claims description 22
- 238000009987 spinning Methods 0.000 claims description 16
- 230000002269 spontaneous effect Effects 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 11
- 238000005520 cutting process Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 10
- 230000000704 physical effect Effects 0.000 description 5
- 239000002759 woven fabric Substances 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 238000009940 knitting Methods 0.000 description 2
- 230000002040 relaxant effect Effects 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Description
本発明は、ドレープ性が良好で極めて優れた風
合を有するポリエステル織編物の製造方法に関す
る。
従来より、織編物の風合改良、ドレープ性改良
のために種々の提案がなされているが、未だ充分
なものは得られていない。
本発明者らは、高速紡糸されたポリエステルフ
イラメント糸の延伸条件およびその後の熱処理条
件によつて該ポリエステルフイラメント糸が僅か
に自発伸長性を生み出すことに着目し、又、自発
伸長発現過程での該ポリエステルフイラメント糸
の物性を巧みに利用しながら、本発明に致つたも
のである。
即ち、本発明は、高速紡糸・低温延伸して得ら
れる沸水収謝率が10％以上、切断伸度が80％以下
である自発伸長性を付与し得るポリエステルフイ
ラメント糸を用いて織編成し、次いで、該織編物
を弛緩熱処理して織編物中の前記ポリエステルフ
イラメント糸を充分収縮せしめると共に自発伸長
性を付与し、しかる後、該弛緩熱処理温度以上の
温度で熱処理して該ポリエステルフイラメント糸
を自発伸長させることを特徴とする織編物の製造
方法にある。
以下、本発明を詳細に説明する。
本発明方法は、自発伸張性を付与し得るポリエ
ステルフイラメント糸を用いて織編成するもので
あり、この場合、該ポリエステルフイラメント糸
の沸水収縮率が10％以上、切断伸度が80％以下と
する必要がある。
自発伸張性を有するポリエステルフイラメント
糸は、例えば特公昭41−12052号公報に記載され
ている如く、高い結晶度を生じないような条件下
で、縮重合体を紡出し、同時にまたは後で延伸し
て配向させ、さらに、高い結晶度を生ぜしめるこ
となく、少なくとも20％の構造物の収縮を許容す
る条件下である時間加熱してフイラメントを収縮
させて自発伸長性のポリエステルフイラメント糸
を得ることが提案されている。しかしながら、
かゝる方法による糸は、収縮が糸の段階で行われ
る結果、沸水収縮率が10％以上のものを望むべく
もなく、収縮するよりは、逆に伸長するものであ
り、又、その切断伸度も100％以上有り、織編成
の作業性の低下を来たし、かつ、得られる織編物
は「ひけ」や「張力不揃ひ」等による品位の低下
をもたらす。これに対して、本発明方法に用いら
れる自発伸長性を付与し得るポリエステルフイラ
メント糸は、以下のようにして得られる。
即ち、線状テレフタレートポリエステル類から
なるフイラメント糸を紡糸速度1500ｍ／分〜4500
ｍ／分の範囲で紡糸し、次いで低温延伸する。延
伸温度としては、20℃〜80℃の範囲のものが有効
に用いられ、さらに好ましくは２次転位点−20℃
の温度で行なうことであり、又、延伸倍率として
は未延伸糸の切断伸度×0.7前後の範囲が有効に
使用される。
前記紡糸速度が1500ｍ／分未満の場合には、延
伸前の糸の配向が低く、且つ、無定形であるため
に、かゝる糸を結晶度を上げないよう低温延伸し
ても、得られた延伸糸は非常に不安定で、室温で
放置するだけで、物性の変化が起り、かゝる経時
変化のため、延伸工程とは通常、不連続である織
編成の工程に安定した品質のものを供給すること
が出来ないので好ましくない。
又、前記の紡糸速度が4500ｍ／分を超える場合
には、得られる糸の沸水収縮率が低く、かゝる糸
を低温延伸しても、得られる延伸糸の沸水収縮率
が10％以上とならず、本発明の目的を達成するこ
とが出来ない。
延伸温度としては、結晶化度高々35％程度にす
るため80℃までの温度で行なうのがよく、かくし
て得られる糸は、後の処理によつて自発伸長を示
すようになる。即ち、この自発伸長性を付与し得
るポリエステルフイラメント糸は、高速紡糸によ
り得られた糸を低温延伸することにより得られる
ために、その結晶化度は20％と低く、且つ、配向
が複屈折度△ｎ＝0.10〜0.12の範囲にあると同時
に、沸水収縮率が10％以上、切断伸度が80％以下
を満足するものとなる。
尚、前記の低温延伸に先立つて、予じめポリエ
ステルフイラメント糸を温度２次転位点以上〜
130℃で熱処理し、次いで低温延伸したものは、
得られる延伸糸の物性がより安定なものになり、
良好な品質の織編物に供することが出来る。
紡糸速度1200ｍ／分〜5000ｍ／分で得られたポ
リエステルフイラメント糸を温度105℃で熱処理
し（一部の糸についてはこの熱処理をせず、延伸
した）、次いで未延伸糸の切断伸度の70％に相当
する延伸が出来るような延伸倍率を選び、第１表
記載の温度で低温延伸をした。得られたポリエス
テルフイラメント糸の沸水収縮率と切断伸度とを
測定すると同時に、該ポリエステルフイラメント
糸を綛に採り、該綛を温度100℃の熱水中で30分
間処理し、処理後に自然乾燥させた後、綛の原長
l0を測定した。該綛を乾熱温度180℃で再度熱処
理して綛長l1を測定し、
l0−l1／l0×100（％）で自発伸長率を求めた。
又、それぞれの紡糸速度に対応する前記のポリ
エステルフイラメント糸（75de／36fils）を用い
て、経密度42本／cm、緯密度40本／cmの密度で平
織物に織成し、該織物を温度100℃で弛緩熱処理
し、しかる後に、該織物を温度180℃で熱処理し
仕上げた。ポリエステルフイラメント糸の物性お
よびそれを用いた前記織物のドレープ性の評価を
第１表に示す。
The present invention relates to a method for producing a polyester woven or knitted fabric having good drapability and extremely excellent hand feel. Conventionally, various proposals have been made to improve the feel and drape properties of woven and knitted materials, but nothing satisfactory has yet been achieved. The present inventors have focused on the fact that the polyester filament yarn spun at high speed has slight spontaneous elongation properties depending on the drawing conditions and the subsequent heat treatment conditions, and also found that The present invention was achieved by skillfully utilizing the physical properties of polyester filament yarn. That is, the present invention uses polyester filament yarn that can be woven and knitted to provide spontaneous extensibility, with a boiling water yield of 10% or more and a breaking elongation of 80% or less, obtained by high-speed spinning and low-temperature stretching, Next, the woven or knitted fabric is subjected to relaxation heat treatment to sufficiently shrink the polyester filament yarn in the woven or knitted fabric and impart spontaneous elongation, and then heat treated at a temperature higher than the relaxation heat treatment temperature to make the polyester filament yarn spontaneously elongate. A method for producing a woven or knitted fabric characterized by elongation. The present invention will be explained in detail below. The method of the present invention involves weaving and knitting using polyester filament yarn that can impart spontaneous extensibility, and in this case, the boiling water shrinkage rate of the polyester filament yarn is 10% or more and the breaking elongation is 80% or less. There is a need. Polyester filament yarns having spontaneous extensibility are produced by spinning a condensation polymer under conditions that do not cause high crystallinity and then stretching it simultaneously or afterwards, as described in Japanese Patent Publication No. 41-12052. The filaments can be oriented by heating for a period of time to obtain a spontaneously extensible polyester filament yarn under conditions that permit at least 20% structural shrinkage without producing high crystallinity. Proposed. however,
Since the yarn produced by such a method shrinks at the yarn stage, it is undesirable for the boiling water shrinkage rate to be more than 10%, and the yarn will elongate rather than shrink. The elongation is also 100% or more, which reduces the workability of weaving and knitting, and the quality of the resulting woven or knitted fabric is degraded due to "sink marks" and "uneven tension." On the other hand, the polyester filament yarn capable of imparting spontaneous extensibility used in the method of the present invention can be obtained as follows. That is, filament yarn made of linear terephthalate polyester is spun at a spinning speed of 1500 m/min to 4500 m/min.
The fibers are spun in the range of m/min and then drawn at a low temperature. As the stretching temperature, a range of 20°C to 80°C is effectively used, and more preferably a temperature of -20°C, which is the secondary dislocation point.
The stretching ratio is effectively used at a temperature of approximately 0.7 times the cutting elongation of the undrawn yarn. If the spinning speed is less than 1500 m/min, the orientation of the yarn before drawing is low and it is amorphous, so even if the yarn is drawn at a low temperature without increasing the crystallinity, it will not be possible to obtain the yarn. The drawn yarn is very unstable, and its physical properties change just by leaving it at room temperature.Because of this change over time, the drawing process is usually discontinuous. This is not desirable because it cannot provide supplies. In addition, when the above-mentioned spinning speed exceeds 4500 m/min, the resulting yarn has a low boiling water shrinkage rate, and even if such a yarn is drawn at a low temperature, the resulting drawn yarn has a boiling water shrinkage rate of 10% or more. Otherwise, the object of the present invention cannot be achieved. The stretching temperature is preferably up to 80° C. in order to achieve a crystallinity of at most 35%, and the yarn thus obtained exhibits spontaneous elongation upon subsequent treatment. In other words, polyester filament yarn that can impart spontaneous extensibility is obtained by low-temperature drawing of yarn obtained by high-speed spinning, so its crystallinity is as low as 20%, and its orientation is similar to the degree of birefringence. Δn is in the range of 0.10 to 0.12, and at the same time satisfies boiling water shrinkage of 10% or more and cutting elongation of 80% or less. In addition, prior to the above-mentioned low-temperature drawing, the polyester filament yarn is heated in advance to a temperature higher than the secondary transition point.
The material was heat treated at 130℃ and then stretched at low temperature.
The physical properties of the resulting drawn yarn become more stable,
It can be used to produce woven or knitted fabrics of good quality. The polyester filament yarn obtained at a spinning speed of 1200 m/min to 5000 m/min was heat treated at a temperature of 105°C (some yarns were drawn without this heat treatment), and then the elongation at break of the undrawn yarn was 70°C. %, and low-temperature stretching was carried out at the temperatures listed in Table 1. At the same time as measuring the boiling water shrinkage rate and cutting elongation of the obtained polyester filament yarn, the polyester filament yarn was taken on a skein, and the skein was treated in hot water at a temperature of 100°C for 30 minutes, and after the treatment, it was allowed to air dry. After that, Rei no Haranaga
l 0 was measured. The skein was heat-treated again at a dry heat temperature of 180° C., the skein length l 1 was measured, and the spontaneous elongation rate was determined as l 0 −l 1 /l 0 ×100 (%). Also, using the polyester filament yarns (75 de/36 fils) corresponding to each spinning speed, a plain weave was woven at a warp density of 42 threads/cm and a weft density of 40 threads/cm, and the woven fabric was heated at a temperature of 100°C. After that, the fabric was heat treated at a temperature of 180°C to finish. Table 1 shows the evaluation of the physical properties of the polyester filament yarn and the drape properties of the fabric using the same.
【表】
長せず、収縮することを示す。
第１表から明らかなように、紡糸速度が1500
ｍ／分未満の場合は、ポリエステルフイラメント
糸の物性の経時変化と見られる色斑が発生し、又
熱処理した糸にも自発伸長性は見られなかつた。
又、紡糸速度が1500ｍ／分〜4500ｍ／分の範囲
の糸であつても、延伸温度が100℃と高いものは、
自発伸長性が得られず、本発明の目的を達成する
ことが出来なかつた。
又、紡糸速度が4500ｍ／分を超えた場合、（第
１表では紡糸速度が5000ｍ／分）には、ポリエス
テルフイラメント糸の沸水収縮率が低く、自発伸
長性の糸とすることが出来ず、本発明の目的を達
成することが出来なかつた。
このように本発明方法では、高速紡糸後、低温
延伸したポリエステルフイラメント糸を用いて織
編成し、次いで該織編物を弛緩熱処理するが、こ
の弛緩熱処理に際しては、該織編物中の該ポリエ
ステルフイラメント糸が充分収縮させることが重
要である。この弛緩熱処理の温度としては、２次
転位点以上〜130℃が有効に使用される。
さらに、かゝる弛緩熱処理の処理時間は、30〜
60分程度が有効である。弛緩熱処理の温度が２次
転位点未満である場合は、織編物中の糸の収縮が
充分に行なわれず、織編物が緻密・屈曲構造とす
ることが困難であるため好ましくない。又、該弛
緩熱処理温度が130℃を超える場合は、結晶化度
が上がり織編物中の糸に自発伸長の性質が付与さ
れ難いので好ましくない。又、弛緩熱処理の時間
は、前記結晶化度が35％を超えない範囲とするこ
とを考慮して、温度との関係で決める必要がある
が、前記の温度範囲では前記のように30〜60分程
度とするのがよい。
本発明方法に用いるポリエステルフイラメント
糸は、沸水収縮率が10％以上の高水準にあり、
又、前記の弛緩熱処理によつて、充分収縮するこ
とが出来る。第１図は、本発明方法により得られ
る織物の断面を模式的に示した断面図であつて、
第１図イは、生機の状態を示すものであつて、未
だ収縮していない状態であるから、織物中におい
て糸の屈曲は大きくない。第１図ロは、弛緩熱処
理後の状態であつて、糸は収縮し織物密度が大と
なると共に織物中の糸は著しく屈曲した構成とす
ることが出来る。
即ち、該織編物は、該ポリエステルフイラメン
ト糸が充分収縮して緻密な構造として得られ、織
編物中の糸が相互に屈曲した構造を有するもので
ある。
以上述べたように本発明方法による織編物は屈
曲、且つ、緻密な構造を有すると共に、織編物を
構成するポリエステルフイラメント糸が自発伸長
性を示すものであるから、後の熱処理に織編物を
構成する糸の相互間の接触圧を低下させるのに役
立ち、前記の屈曲・緻密構造と相乗的に作用し
て、より大きい可撓性が生じ、ドレープ性の良好
な、且つ、反撥性の優れた織編物を得ることが出
来るものである。尚、後の熱処理は、前記の弛緩
熱処理より高い温度で、自発伸長された糸の結晶
度が進み、熱的に安定となる温度で行なうことが
望ましい。
さらに、本発明方法にとつて、好都合なこと
は、切断伸度が80％以下の糸を取扱うことが出来
るため、従来の自発伸長性糸のように取扱い作業
性不良の原因から織編物の品位低下を防止出来る
ものである。
以下、本発明を実施例により説明する。
実施例
紡糸速度3500ｍ／分で高速紡糸したポリエステ
ルフイラメント糸を温度110℃で熱処理し、次い
で1.55倍の延伸倍率で、温度25℃で延伸し、沸水
収縮率25％、切断伸度40％の延伸糸を得た。次い
で該延伸糸を経42本／cm、緯40本／cmの密度の平
織物に織成し、該織物を弛緩熱処理するに際し
て、種々の温度を用いて60分間行ない、しかる後
該弛緩熱処理温度以上の温度で熱処理してドレー
プ性の評価を実施した。
結果を第２表に示す。No.１〜No.４では、良好な
ドレープ性を示したが、No.５では、ドレープ性は
不良であつた。[Table] Indicates that it does not lengthen and contracts.
As is clear from Table 1, the spinning speed is 1500
When the speed was less than m/min, color spots appeared, which appeared to be due to changes in the physical properties of the polyester filament yarn over time, and spontaneous elongation was not observed even in the heat-treated yarn. In addition, even if the spinning speed is in the range of 1500 m/min to 4500 m/min, the drawing temperature is as high as 100°C.
Spontaneous extensibility could not be obtained, and the object of the present invention could not be achieved. In addition, when the spinning speed exceeds 4500 m/min (in Table 1, the spinning speed is 5000 m/min), the boiling water shrinkage rate of the polyester filament yarn is low and it is not possible to make the yarn spontaneously extensible. The object of the present invention could not be achieved. As described above, in the method of the present invention, after high-speed spinning, polyester filament yarn drawn at low temperature is woven and knitted, and then the woven or knitted fabric is subjected to a relaxation heat treatment. It is important that the material is sufficiently shrunk. As the temperature for this relaxation heat treatment, a temperature above the secondary dislocation point to 130° C. is effectively used. Furthermore, the treatment time for such relaxation heat treatment is 30~
Approximately 60 minutes is effective. If the temperature of the relaxation heat treatment is lower than the second-order dislocation point, the yarns in the woven or knitted fabric will not shrink sufficiently and it will be difficult to form the woven or knitted fabric into a dense and bent structure, which is not preferable. Further, if the relaxation heat treatment temperature exceeds 130°C, the degree of crystallinity increases and it is difficult to impart spontaneous elongation properties to the yarn in the woven or knitted fabric, which is not preferable. In addition, the time for the relaxation heat treatment must be determined in relation to the temperature, taking into account that the crystallinity does not exceed 35%. It is best to take about a minute. The polyester filament yarn used in the method of the present invention has a high boiling water shrinkage rate of 10% or more,
Further, sufficient shrinkage can be achieved by the above-mentioned relaxation heat treatment. FIG. 1 is a cross-sectional view schematically showing a cross section of a fabric obtained by the method of the present invention,
Figure 1A shows the state of the gray fabric, which has not yet contracted, so the bending of the threads in the fabric is not large. FIG. 1B shows the state after the relaxation heat treatment, in which the yarns shrink and the fabric density increases, and the yarns in the fabric can be bent significantly. That is, the woven or knitted fabric has a dense structure obtained by sufficiently shrinking the polyester filament yarn, and has a structure in which the yarns in the woven or knitted fabric are mutually bent. As described above, the woven or knitted fabric produced by the method of the present invention has a bent and dense structure, and the polyester filament yarn that makes up the woven or knitted fabric exhibits spontaneous elongation. It helps to reduce the contact pressure between the yarns, and works synergistically with the bending and dense structure to create greater flexibility, resulting in good drapability and excellent resilience. Woven or knitted fabrics can be obtained. The subsequent heat treatment is desirably carried out at a temperature higher than the relaxation heat treatment, at which the crystallinity of the spontaneously elongated thread progresses and becomes thermally stable. Furthermore, the method of the present invention is advantageous because it can handle yarns with a cutting elongation of 80% or less, which reduces the quality of woven and knitted fabrics from the problem of poor handling workability, which is the case with conventional spontaneously extensible yarns. This can prevent the decline. The present invention will be explained below using examples. Example A polyester filament yarn spun at a spinning speed of 3500 m/min was heat treated at a temperature of 110°C, and then stretched at a draw ratio of 1.55 times at a temperature of 25°C, with a boiling water shrinkage rate of 25% and a cutting elongation rate of 40%. Got the thread. Next, the drawn yarn is woven into a plain woven fabric having a density of 42 threads/cm in warp and 40 threads/cm in weft, and the woven fabric is subjected to relaxation heat treatment at various temperatures for 60 minutes. The drapability was evaluated by heat treatment at a certain temperature. The results are shown in Table 2. Nos. 1 to 4 showed good drape properties, but No. 5 had poor drape properties.
【表】
No.１〜４のものは、弛緩熱処理時に、その温度
が比較的低温のため、織物を構成するポリエステ
ルフイラメント糸が自発伸長するような収縮を
し、No.５では、該弛緩熱処理諾に結晶化が促進さ
れ、後の熱処理時に自発伸長しないためと考えら
れる。[Table] In Nos. 1 to 4, the temperature is relatively low during the relaxing heat treatment, so the polyester filament yarns constituting the fabric contract to spontaneously elongate, and in No. 5, the relaxing heat treatment This is thought to be because crystallization is immediately promoted and spontaneous elongation does not occur during subsequent heat treatment.
第１図は、本発明方法により得られる織物の断
面を模式的に示した断面図である。
FIG. 1 is a cross-sectional view schematically showing a cross section of a fabric obtained by the method of the present invention.
Claims (1)
速紡糸し、温度20℃〜80℃の範囲で低温延伸して
得られる沸水収縮率が10％以上、切断伸度が80％
以下である自発伸長性を付与し得るポリエステル
フイラメント糸を用いて織編成し、次いで該織編
物を２次転位点以上〜130℃の温度で弛緩熱処理
して、織編物中の前記ポリエステルフイラメント
糸を充分収縮せしめると共に自発伸長性を付与
し、しかる後該弛緩熱処理温度以上の温度で熱処
理して該ポリエステルフイラメント糸を自発伸長
させることを特徴とする織編物の製造方法。1 High-speed spinning at a spinning speed of 1,500 m/min to 4,500 m/min and low-temperature stretching at a temperature of 20°C to 80°C, resulting in boiling water shrinkage of 10% or more and cutting elongation of 80%.
The following polyester filament yarns capable of imparting spontaneous extensibility are woven and knitted, and then the woven or knitted fabric is subjected to relaxation heat treatment at a temperature of 130°C above the secondary dislocation point to loosen the polyester filament yarns in the woven or knitted fabric. A method for producing a woven or knitted material, which comprises sufficiently shrinking the yarn and imparting spontaneous elongation to the polyester filament yarn, and then heat-treating the filament yarn at a temperature higher than the relaxation heat treatment temperature to make the polyester filament yarn spontaneously elongate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57063950A JPS58180670A (en) | 1982-04-19 | 1982-04-19 | Production of polyester knitted fabric |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57063950A JPS58180670A (en) | 1982-04-19 | 1982-04-19 | Production of polyester knitted fabric |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58180670A JPS58180670A (en) | 1983-10-22 |
| JPS6335747B2 true JPS6335747B2 (en) | 1988-07-15 |
Family
ID=13244117
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57063950A Granted JPS58180670A (en) | 1982-04-19 | 1982-04-19 | Production of polyester knitted fabric |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58180670A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53103018A (en) * | 1977-02-10 | 1978-09-07 | Teijin Ltd | Production of self-stretching polyester staple fiber |
| JPS5493120A (en) * | 1977-12-26 | 1979-07-24 | Teijin Ltd | Production of crimped yarn of self-stretching polyester |
| JPS5562240A (en) * | 1978-10-26 | 1980-05-10 | Teijin Ltd | Production of woven knitted fabric by selffextensible fiber |
-
1982
- 1982-04-19 JP JP57063950A patent/JPS58180670A/en active Granted
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53103018A (en) * | 1977-02-10 | 1978-09-07 | Teijin Ltd | Production of self-stretching polyester staple fiber |
| JPS5493120A (en) * | 1977-12-26 | 1979-07-24 | Teijin Ltd | Production of crimped yarn of self-stretching polyester |
| JPS5562240A (en) * | 1978-10-26 | 1980-05-10 | Teijin Ltd | Production of woven knitted fabric by selffextensible fiber |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58180670A (en) | 1983-10-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3280443A (en) | Method of producing crepe-like fabrics | |
| JPS6335747B2 (en) | ||
| JP4284758B2 (en) | Method for producing polyester composite yarn | |
| US4237108A (en) | Process for producing carbon fabric | |
| JPS6249378B2 (en) | ||
| JPH03180572A (en) | Production of highly elastic woven fabric | |
| KR100234557B1 (en) | Process of polyester mixed for yarn | |
| JPS6346167B2 (en) | ||
| JPH10280231A (en) | Production of low shrinkage ultrafine polyester fiber | |
| JPH0323645B2 (en) | ||
| KR930000249B1 (en) | Manufacturing process of polyester filament yarn | |
| KR940010802B1 (en) | Pile fabric making method | |
| JP3581003B2 (en) | Polyester multifilament different shrinkage mixed yarn | |
| JP3517494B2 (en) | Polyester multifilament yarn, method for producing the same, and mixed fiber yarn | |
| KR100467345B1 (en) | Manufacturing method of polyester composite processing | |
| JPS6136102B2 (en) | ||
| JPH0711513A (en) | Production of polyester fiber with self-elongation nature | |
| JPH022979B2 (en) | ||
| JPH06123058A (en) | Production of bulky fabric | |
| JPS591765A (en) | Production of polyester fabric | |
| JPH062968B2 (en) | Method for producing polyester crimped yarn | |
| JPH0813270A (en) | Particular combined filament yarn | |
| JP2001192948A (en) | Polyester woven or knitted fabric | |
| JPS6142022B2 (en) | ||
| JPH0327650B2 (en) |