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JPH0565604B2 - - Google Patents
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JPH0565604B2 - - Google Patents

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Publication number
JPH0565604B2
JPH0565604B2 JP27681684A JP27681684A JPH0565604B2 JP H0565604 B2 JPH0565604 B2 JP H0565604B2 JP 27681684 A JP27681684 A JP 27681684A JP 27681684 A JP27681684 A JP 27681684A JP H0565604 B2 JPH0565604 B2 JP H0565604B2
Authority
JP
Japan
Prior art keywords
orifice
viscosity
slit
hollowness
hollow
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 - Lifetime
Application number
JP27681684A
Other languages
Japanese (ja)
Other versions
JPS61152824A (en
Inventor
Yoshihiro Honda
Daizo Kume
Seiichiro Okuda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Ester Co Ltd
Original Assignee
Nippon Ester Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Ester Co Ltd filed Critical Nippon Ester Co Ltd
Priority to JP27681684A priority Critical patent/JPS61152824A/en
Publication of JPS61152824A publication Critical patent/JPS61152824A/en
Publication of JPH0565604B2 publication Critical patent/JPH0565604B2/ja
Granted legal-status Critical Current

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  • Multicomponent Fibers (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) 本発明は、サイドバイサイド型中空複合繊維の
製造法に関するものであり、溶融粘度の異なる二
成分をサイドバイサイド型に接合し、オリフイス
より吐出するに際し、生ずるオリフイス出口で斜
向に吐出される状態になる(以下ニーイングと称
する。)のを防止し、高中空度で捲縮発現性能の
優れたポリエステル中空複合繊維を製造する方法
に関するものである。 (従来の技術) 近年、フトン綿等の詰綿の分野で天然繊維にか
わつて合成繊維が急激に増加している。これは繊
維のコストもさることながら、天然繊維に比べ合
成繊維は嵩高性、防じん性等のすぐれた諸性能を
有していることに起因している。また、合成繊維
の中でもコイルスプリング状の捲縮を有する複合
繊維はさらにすぐれた嵩高性および被覆性を有す
ることは公知であり、さらに加えて該複合繊維の
中心部を空洞にした中空複合繊維は嵩高性、保温
性がさらに一段と向上することも公知である。し
かし、消費者側の要望ではこれらの諸性能をさら
に向上させることを要求しており、諸性能の中で
も嵩高性向上の要望は一段と強い。 嵩高性能を高くするには、捲縮発現性能および
中空度を高くする必要がある。 捲縮発現性能を高くする方法として、サイドバ
イサイド型に接合してなる複合繊維の二成分の極
限粘度差および溶融粘度差を大にすることにより
繊維の内部構造を大きく変化させ、配向および収
縮差を生じさせて、高捲縮性能を有した複合繊維
を得ることは公知である。 (発明が解決しようとする問題点) しかしながら、溶融粘度の異なる二種のポリエ
ステルをあらかじめ接合させ、サイドバイサイド
型にオリフイスより吐出する場合、オリフイスよ
り吐出直後にニーイングが発生し、二成分の粘度
差が大きくなるほどニーイング角度が大きくな
り、紡糸状態が不安定となり、極端な場合はポリ
マー流が口金面に付着し、糸切れが発生し、紡糸
が不可能となる。 ニーイングを防ぐための手段は従来より多く提
案されているが、サイドバイサイド型中空複合繊
維の提案は少なく、非中空複合繊維が主である。
サイドバイサイド型中空複合繊維の場合には、粘
度差を大きくするとニーイングが発生し、中空度
は低下し、中空部が高粘度側に偏心した状態とな
り、捲縮発現性能が低下して非中空繊維に比べて
も嵩高性能が劣る。このように、繊維形成工程で
低粘度成分が存在すると中空部比率を向上させる
ことが困難である。 したがつて、低粘度成分の影響を取り除き中空
度を向上する方法として、二成分共に粘度を増大
させ低粘度成分側の粘度レベルを上げる方法およ
び低粘度側のみの粘度を上げ、両者の粘度差を少
なくする方法があるが、前者は重合反応のコスト
アツプが無視できないし、後者は捲縮の発現能力
が低下し満足する性能を有しない。 (問題点を解決するための手段、発明の構成) 本発明者等は、嵩高性を向上させるために中空
度、すなわち中空複合繊維の中空部の繊維断面積
に占める比率を増大させ(中空度25〜30%が嵩高
性が最も良い。)、中空部の偏心が少なく、しかも
ニーイングの少ない製造方法で嵩高性の優れたポ
リエステル中空複合繊維を製造する方法について
検討した結果、本発明に到達した。 本発明の要旨は次のとおりである。 本発明は、略々半円弧状であつて、外周面に円
弧1と円周面の円弧2が偏心状に位置し、一端が
広幅封止部3、他端が狭幅封止部4で封止された
スリツト二個を、それぞれ広幅封止部と狭幅封止
部を対向させて形成し、溶融紡糸用オリフイスの
広幅スリツト部5には高粘度の溶融ポリエステル
成分を、狭幅スリツト部6には低粘度の溶融ポリ
エステル成分を供給して二種の成分を接合させつ
つスリツト状オリフイスから吐出することを特徴
とするポリエステル中空複合繊維の製造法であ
る。 すなわち、前記の半円弧状のスリツト二個を対
向して形成したときの円周の外側面、すなわち外
径、同内側面、内径の中心点の異なるオリフイス
を使用するのである。 本発明に使用するポリエステルとしては、エチ
レンテレフタレート単位を85モル%以上含むポリ
エステルが好ましく、最も好適なポリエステルは
ポリエチレンテレフタレートであり、該ポリエス
テルは20℃、フエノール・四塩化エタン等量混合
溶媒で測定した粘度より算出した極限粘度が0.4
〜0.8、280℃における溶融粘度が300〜4000ポイ
ズであるものが好ましい。なお、該ポリエステル
は、つや消剤、着色剤等の添加剤を含んでいても
よいことはいうまでもない。 本発明方法を図面を用いて更に詳細に説明す
る。 第1図は本発明を実施するための半円弧状のス
リツトを対向させたオリフイスの一例を示したも
のであり、第2図は本発明の方法で得られた中空
複合繊維の断面図である。第3図は従来方法で得
られた中空複合繊維の断面図である。 第1図においてP1は、オルフイス二個を対向
させたときの外周面1の円の中心点であり、P2
は同内周面2の円の中心点である。オリフイスの
外径(外周円の)をD、内径(内周面の)をd、
P1−P2の距離をlとするとき、本発明において
は(D−d)/2≧l≧(D−d)/10および
1.40≧D/d≧1.08を満すことが好ましく、オリ
フイスのスリツトの狭幅スリツト部6には低粘度
成分Lが配置されなければならない。このオリフ
イスのスリツトの狭幅スリツト部6に高粘度成分
Hを配置するとニーイングが著しいうえ、得られ
る糸の断面は中空部分が高粘度成分の方へ偏心
し、中空度も低下する。 オリフイスの寸法D,dおよび接合部A,Bの
間隔は用いるポリエステルの粘度、目標とする繊
度および中空度により設定すればよいが、D/d
は1.08〜1.40が好ましい。D/dが1.08より小さ
ければオリフイスの加工が難しく、1.40より大で
あれば中空度が低下する。 接合部AおよびBの間隔は、ポリマーの接着お
よびオリフイスの強度の面から0.08〜0.2mmが好
ましい。 低粘度成分Lをオリフイスのスリツトの狭幅ス
リツト部6に配置した場合において、lが(D−
d)/10より小さければニーイングおよび中空度
低下、中空部の偏心が発生し、第3図に示すよう
な形状となり、高中空度で捲縮発現性能の良い糸
が得られない。lが(D−d)/2より大きくな
ると、接合部B付近のスリツトは形成できなくな
つて接合部Bの間隔が広くなり、低粘度成分が接
合できなくなつたり、異常接合を起こし、中空度
の低い不安定な断面形状を有した糸となる。 本発明を有効にするためには、高粘度成分およ
び低粘度成分の極限粘度がそれぞれ0.65〜0.75お
よび0.45〜0.6のポリエステルを用い、粘度差を
0.08〜0.22、好ましくは0.1〜0.2、280℃における
溶融粘度の差を1000〜3000ポイズ、好ましくは
1500〜2500ポイズにすることが望ましい。 中空度が20〜30%になるようにDおよびdを設
定し、lが(D−d)/2≧l≧(D−d)/10
になるように設計したオリフイスを用いた場合、
ニーイングの発生が少なく、しかも偏心のない高
捲縮性能の糸条が得られるのである。 得られた糸条は低温で延伸することが好まし
い。すなわち、延伸温度はガラス転移点温度±20
℃の範囲の温度が好ましく、また延伸倍率は最高
延伸倍率の65〜95%が好適である。捲縮発現処理
は無緊張下で140〜180℃の処理温度が好ましい。 (実施例) 以下、実施例により本発明の方法を具体的に説
明する。 実施例中の嵩高性の評価値は試料綿をカード機
で開繊して積層したウエブ(20cm×20cm、重さ80
g)を無荷重(測定板20cm×20cm、荷重170g)
時、加重時(5Kg)および除重時(無荷重時と同
様の荷重)で高さを測定した値である。 A1:無荷重時の高さ A2:荷重時の高さ A3:除重時の高さ 中空度は次式のようにして求めた。 中空率(%)=中空部の断面積/全断面積×100 ニーイング角度はオリフイスより吐出されたポ
リマーの流出角度である。 実施例 極限粘度が0.69であるポリエチレンテレフタレ
ートを高粘度成分(280℃、溶融粘度3200ポイズ)
とし、極限粘度が0.57であるポリエチレンテレフ
タレートを低粘度成分(280℃、溶融粘度1200ポ
イズ)として、オリフイスのDが1.6mm、dが1.3
mm、lが0.05mm、スリツト幅最広部の接合部Aの
間隔が0.1mm、スリツト幅最狭部の接合部Bの間
隔が0.2mmからなるオリフイスを使用し、スリツ
トの狭幅側6に低粘度成分が配置されるようにポ
リマーを吐出し、紡糸温度280℃、オリフイス単
孔吐出量2.2g/min、紡糸速度1050m/minで紡
糸した後、延伸温度85℃、延伸倍率3.9で延伸し、
無緊張下で160℃の熱処理を施した後、切断して
単糸繊度6デニール、繊維長51mmのポリエステル
中空複合短繊維を得た。 糸条の断面形状は第2図のような形状である。
紡糸時ニーイング、糸条の中空度、ウエブ嵩高性
の測定結果を第1表に示す。 比較例 l=0であるオリフイスを用いること以外は実
施例と同様の方法で行つた結果を同じく第1表に
示す。糸条の断面形状は第3図のような形状であ
る。
(Industrial Application Field) The present invention relates to a method for manufacturing side-by-side type hollow composite fibers, in which two components having different melt viscosities are joined side-by-side and discharged from an orifice. The present invention relates to a method for producing polyester hollow conjugate fibers that are prevented from being discharged (hereinafter referred to as kneeing) and have a high degree of hollowness and excellent crimp development performance. (Prior Art) In recent years, synthetic fibers have been rapidly replacing natural fibers in the field of cotton padding such as futon cotton. This is due not only to the cost of the fibers, but also to the fact that synthetic fibers have superior properties such as bulkiness and dust resistance compared to natural fibers. Furthermore, among synthetic fibers, it is known that composite fibers with coil spring-like crimps have even better bulkiness and covering properties, and in addition, hollow composite fibers with a hollow center are It is also known that the bulkiness and heat retention properties are further improved. However, consumers are demanding further improvements in these various performances, and among these performances, there is an even stronger demand for improved bulkiness. In order to increase bulk performance, it is necessary to increase crimp development performance and hollowness. As a method to improve crimp performance, the internal structure of the fibers is greatly changed by increasing the intrinsic viscosity difference and melt viscosity difference between the two components of composite fibers joined side-by-side, thereby reducing the orientation and shrinkage difference. It is known to produce composite fibers with high crimp performance. (Problem to be solved by the invention) However, when two types of polyesters with different melt viscosities are bonded in advance and discharged from an orifice in a side-by-side manner, kneeing occurs immediately after discharge from the orifice, and the difference in viscosity between the two components As the kneeing angle increases, the spinning state becomes unstable, and in extreme cases, the polymer flow adheres to the spinneret surface, causing yarn breakage and making spinning impossible. Although many means for preventing kneeing have been proposed, there have been few proposals for side-by-side type hollow composite fibers, and non-hollow composite fibers have been mainly proposed.
In the case of side-by-side type hollow composite fibers, when the viscosity difference is increased, kneeing occurs, the degree of hollowness decreases, and the hollow part becomes eccentric toward the high viscosity side, resulting in a decrease in crimp performance and the formation of non-hollow fibers. Even when compared, bulk and performance are inferior. As described above, if a low viscosity component is present in the fiber forming process, it is difficult to improve the hollow portion ratio. Therefore, as a method to remove the influence of the low viscosity component and improve the hollowness, there are two methods: increasing the viscosity of both components to raise the viscosity level of the low viscosity component, and increasing the viscosity of only the low viscosity component to reduce the viscosity difference between the two components. Although there are methods for reducing the amount of crimping, the former method involves a non-negligible increase in the cost of the polymerization reaction, and the latter method does not have satisfactory performance because the ability to develop crimp is reduced. (Means for Solving the Problems, Structure of the Invention) In order to improve the bulkiness, the present inventors increased the degree of hollowness, that is, the ratio of the hollow part of the hollow composite fiber to the cross-sectional area of the fiber (the degree of hollowness 25 to 30% is the best bulkiness.) As a result of research into a method for producing polyester hollow composite fibers with excellent bulkiness using a production method with less eccentricity in the hollow part and less kneeing, the present invention was arrived at. . The gist of the present invention is as follows. The present invention has a substantially semi-circular arc shape, with a circular arc 1 on the outer circumferential surface and a circular arc 2 on the circumferential surface located eccentrically, with a wide sealing part 3 at one end and a narrow sealing part 4 at the other end. Two sealed slits are formed with a wide sealing part and a narrow sealing part facing each other, and a high viscosity molten polyester component is applied to the wide slit part 5 of the melt spinning orifice, and the narrow slit part 6 is a method for producing polyester hollow composite fibers characterized by supplying a low-viscosity molten polyester component and discharging it from a slit-like orifice while bonding the two components. That is, when the two semicircular arc-shaped slits are formed facing each other, orifices having different outer diameters, that is, inner diameters, and center points of the inner diameters are used. The polyester used in the present invention is preferably a polyester containing 85 mol% or more of ethylene terephthalate units, and the most suitable polyester is polyethylene terephthalate. Intrinsic viscosity calculated from viscosity is 0.4
~0.8, and preferably has a melt viscosity of 300 to 4000 poise at 280°C. It goes without saying that the polyester may contain additives such as a matting agent and a coloring agent. The method of the present invention will be explained in more detail using the drawings. Fig. 1 shows an example of an orifice in which semicircular arc-shaped slits are opposed to each other for carrying out the present invention, and Fig. 2 is a cross-sectional view of a hollow composite fiber obtained by the method of the present invention. . FIG. 3 is a cross-sectional view of a hollow composite fiber obtained by a conventional method. In Fig. 1, P 1 is the center point of the circle on the outer peripheral surface 1 when two Orphis chairs are placed facing each other, and P 2
is the center point of the circle on the inner peripheral surface 2. The outer diameter (of the outer circumferential circle) of the orifice is D, the inner diameter (of the inner circumferential surface) is d,
When the distance P 1 - P 2 is l, in the present invention, (D-d)/2≧l≧(D-d)/10 and
It is preferable to satisfy 1.40≧D/d≧1.08, and the low viscosity component L must be placed in the narrow slit portion 6 of the orifice slit. If the high viscosity component H is placed in the narrow slit portion 6 of the orifice slit, kneeing will be significant, and in the cross section of the resulting yarn, the hollow portion will be eccentric toward the high viscosity component, and the degree of hollowness will also decrease. The dimensions D and d of the orifice and the spacing between the joints A and B can be set depending on the viscosity of the polyester used, the target fineness and hollowness, but D/d
is preferably 1.08 to 1.40. If D/d is smaller than 1.08, it will be difficult to process the orifice, and if it is larger than 1.40, the degree of hollowness will decrease. The distance between the joints A and B is preferably 0.08 to 0.2 mm from the viewpoint of polymer adhesion and orifice strength. When the low viscosity component L is placed in the narrow slit part 6 of the orifice slit, l is (D-
d) If it is smaller than /10, kneeing, a decrease in hollowness, and eccentricity of the hollow part will occur, resulting in a shape as shown in FIG. 3, and a yarn with high hollowness and good crimp performance cannot be obtained. When l is larger than (D-d)/2, slits near joint B cannot be formed and the interval between joints B becomes wider, making it impossible to join low-viscosity components or causing abnormal joints, resulting in hollow The result is a thread with a highly unstable cross-sectional shape. In order to make the present invention effective, polyesters with intrinsic viscosities of 0.65 to 0.75 and 0.45 to 0.6 are used for the high viscosity component and the low viscosity component, respectively, and the viscosity difference is reduced.
0.08-0.22, preferably 0.1-0.2, the difference in melt viscosity at 280°C is 1000-3000 poise, preferably
It is desirable to set it to 1500 to 2500 poise. Set D and d so that the degree of hollowness is 20 to 30%, and l is (D-d)/2≧l≧(D-d)/10
When using an orifice designed to
A yarn with high crimp performance and less occurrence of kneeing and no eccentricity can be obtained. It is preferable to draw the obtained yarn at a low temperature. In other words, the stretching temperature is ±20
The temperature is preferably in the range of .degree. C., and the stretching ratio is preferably 65 to 95% of the maximum stretching ratio. The crimp development treatment is preferably carried out at a treatment temperature of 140 to 180°C under no tension. (Example) Hereinafter, the method of the present invention will be specifically explained using Examples. The bulkiness evaluation value in the examples is a web (20 cm x 20 cm, weight 80
g) without load (measuring plate 20cm x 20cm, load 170g)
This is the value measured for the height when loaded (5 kg) and when unloaded (same load as when no load is applied). A 1 : Height when no load is applied A 2 : Height when loaded A 3 : Height when unloaded The degree of hollowness was determined using the following formula. Hollowness ratio (%)=cross-sectional area of hollow part/total cross-sectional area×100 The kneeing angle is the outflow angle of the polymer discharged from the orifice. Example Polyethylene terephthalate with an intrinsic viscosity of 0.69 is used as a high viscosity component (280℃, melt viscosity 3200 poise)
The D of the orifice is 1.6 mm and the d of the orifice is 1.3.
Use an orifice with mm and l of 0.05 mm, an interval of 0.1 mm between joints A at the widest part of the slit, and 0.2 mm between joints B at the narrowest part of the slit. The polymer was discharged so that the low viscosity components were arranged, and after spinning at a spinning temperature of 280°C, a single orifice discharge rate of 2.2 g/min, and a spinning speed of 1050 m/min, it was stretched at a stretching temperature of 85°C and a draw ratio of 3.9. ,
After heat treatment at 160°C under no tension, it was cut to obtain polyester hollow composite short fibers with a single fiber fineness of 6 denier and a fiber length of 51 mm. The cross-sectional shape of the yarn is as shown in FIG.
Table 1 shows the measurement results for kneeing during spinning, yarn hollowness, and web bulkiness. Comparative Example Table 1 also shows the results obtained in the same manner as in the example except that an orifice with l=0 was used. The cross-sectional shape of the yarn is as shown in FIG.

【表】 (発明の効果) 以上述べたように、本発明方法(実施例)を用
いれば、従来方法(比較例)に比べニーイングが
少なく、紡糸状態が安定し、中空度も高く、中空
部の偏心もなく、断面形状が安定しており、捲縮
発現性能も良好である。そして無荷重時の嵩、重
加重時の嵩および除重時の嵩も高い優れた嵩高性
能を示すポリエステル中空複合繊維が得られる。
[Table] (Effects of the invention) As described above, if the method of the present invention (example) is used, there will be less kneeing compared to the conventional method (comparative example), the spinning state will be stable, the degree of hollowness will be high, and the hollow portion There is no eccentricity, the cross-sectional shape is stable, and the crimp development performance is also good. A polyester hollow conjugate fiber is obtained which exhibits excellent bulk performance, with high bulk under no load, high bulk under heavy load, and high bulk when unloaded.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明を実施するための半円弧状のス
リツトを対向させたオリフイスの形状の一例を示
す概略図であり、第2図は本発明方法によつて得
られた複合繊維の断面図であり、第3図は従来法
によつて得られた複合繊維の断面図である。 図中、1は半円弧状スリツトの外周面の円弧、
2は内周面の円弧、3は広幅封止部、4は狭幅封
止部、5は広幅スリツト部、6は狭幅スリツト部
を示す。
FIG. 1 is a schematic view showing an example of the shape of an orifice with semicircular arc-shaped slits facing each other for carrying out the present invention, and FIG. 2 is a cross-sectional view of a composite fiber obtained by the method of the present invention. FIG. 3 is a cross-sectional view of a composite fiber obtained by a conventional method. In the figure, 1 is the circular arc of the outer peripheral surface of the semicircular arc-shaped slit;
Reference numeral 2 indicates an arc of the inner peripheral surface, 3 indicates a wide sealing portion, 4 indicates a narrow sealing portion, 5 indicates a wide slit portion, and 6 indicates a narrow slit portion.

Claims (1)

【特許請求の範囲】[Claims] 1 略々半円弧状であつて、外周面の円弧1と円
周面の円弧2が偏心状に位置し、一端が広幅封止
部3、他端が狭幅封止部4で封止されたスリツト
二個を、それぞれ広幅封止部と狭幅封止部を対向
させて形成した溶融紡糸用オリフイスの広幅スリ
ツト部5には高粘度の溶融ポリエステル成分を、
狭幅スリツト部6には低粘度の溶融ポリエステル
成分を供給して二種の成分を接合させつつ、スリ
ツト状オリフイスから吐出することを特徴とする
ポリエステル中空複合繊維の製造法。
1 It has a substantially semicircular arc shape, and the arc 1 on the outer circumferential surface and the arc 2 on the circumferential surface are eccentrically located, and one end is sealed with a wide sealing part 3 and the other end is sealed with a narrow sealing part 4. A high-viscosity molten polyester component is placed in the wide slit portion 5 of the melt-spinning orifice, which is formed by forming two slits with a wide sealing portion and a narrow sealing portion facing each other.
A method for producing polyester hollow composite fibers, which comprises supplying a low-viscosity molten polyester component to the narrow slit portion 6 and discharging it from a slit-like orifice while bonding the two components.
JP27681684A 1984-12-27 1984-12-27 Production of polyester hollow conjugated fiber Granted JPS61152824A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27681684A JPS61152824A (en) 1984-12-27 1984-12-27 Production of polyester hollow conjugated fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27681684A JPS61152824A (en) 1984-12-27 1984-12-27 Production of polyester hollow conjugated fiber

Publications (2)

Publication Number Publication Date
JPS61152824A JPS61152824A (en) 1986-07-11
JPH0565604B2 true JPH0565604B2 (en) 1993-09-20

Family

ID=17574788

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27681684A Granted JPS61152824A (en) 1984-12-27 1984-12-27 Production of polyester hollow conjugated fiber

Country Status (1)

Country Link
JP (1) JPS61152824A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010028161A (en) * 1999-09-18 2001-04-06 조민호 Method for manufacturing hollow, side-by-side type conjugated yarn, spineret therefor and side-by-side type conjugated yarn thereby

Also Published As

Publication number Publication date
JPS61152824A (en) 1986-07-11

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