JPS6028937B2 - Polyester sewing thread with excellent heat resistance - Google Patents
Polyester sewing thread with excellent heat resistanceInfo
- Publication number
- JPS6028937B2 JPS6028937B2 JP54074413A JP7441379A JPS6028937B2 JP S6028937 B2 JPS6028937 B2 JP S6028937B2 JP 54074413 A JP54074413 A JP 54074413A JP 7441379 A JP7441379 A JP 7441379A JP S6028937 B2 JPS6028937 B2 JP S6028937B2
- Authority
- JP
- Japan
- Prior art keywords
- sewing thread
- heat resistance
- sewing
- thread
- value
- 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
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- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Description
【発明の詳細な説明】
この発明は耐熱性が優れたポリエステルミシン糸に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polyester sewing thread having excellent heat resistance.
ポリエチレンテレフタレートを溶融紡糸、延伸して得ら
れたフィラメント糸を原糸として製造されたポリエステ
ルミシン糸は、強度が大きく、染色性が良好で染色堅牢
度が高く、寸法安定性が優れ、さらに経時的な強力低下
が小さいなどの優れだ性質を備えているので、衣料分野
の縫製作業において従釆からの綿カタン糸に代替えされ
るようになってきた。Polyester sewing thread manufactured from filament yarn obtained by melt-spinning and drawing polyethylene terephthalate has high strength, good dyeability, high color fastness, excellent dimensional stability, and long-term durability. Because it has excellent properties such as less loss of strength, it has come to be used as a substitute for traditional cotton Katan thread in sewing work in the clothing field.
そしてポリエステルミシン糸は安価であるため、工業用
製品の縫糸としても多量に使用されている。,しかしな
がら従来のポリエステルミシン糸は、耐熱性が未だ不十
分であって、400比pm程度の高速縫製の場合や厚地
の縫製の場合に、ミシン糸と織物またはミシン糸と間の
摩擦によってミシン糸が融点近くの高温にまで上昇する
ことがあって、ミシン糸の溶断糸切れが頻発し、縫製能
率を著しく低下させる。・また縫製限界に近い厳しい条
件下で縫製された工業製品は、ミシン糸が縫製時に高温
履歴を形て熱劣化しているため、長時間の使用に耐えら
れずして早期に縫目が破れることがある。上記のように
従来のポリエステルミシン糸は耐熱性が不十分であるの
で、耐熱性を向上することが要望されていた。なお、従
釆のポリエステルミシン糸の高速可総性を向上する手段
として、たとえばミシン糸と構成単糸フラメントとの間
の撚角度を小さくすることによって摩擦を小さくする方
法(特関昭52−27847号公報参照)や、シリコー
ン系油剤を用いて高温動摩擦特性を改善する方法(特関
昭52−8198号公報参照)などが知られているが、
これらの公知の方法はいずれもミシン糸目体の耐熱性を
向上して高速可縫性を改善するものではない。Since polyester sewing thread is inexpensive, it is also used in large quantities as a sewing thread for industrial products. However, conventional polyester sewing thread still has insufficient heat resistance, and when sewing at high speeds of about 400 pm or sewing thick fabrics, the sewing thread may break due to friction between the sewing thread and the fabric or sewing thread. The temperature may rise to a high temperature close to the melting point, resulting in frequent fusing and breakage of sewing thread, which significantly reduces sewing efficiency.・In addition, in industrial products that are sewn under harsh conditions that are close to the sewing limit, the sewing thread has a history of high temperatures during sewing and has deteriorated due to heat, making it impossible to withstand long-term use and causing the seams to tear prematurely. Sometimes. As mentioned above, conventional polyester sewing threads have insufficient heat resistance, so there has been a demand for improved heat resistance. In addition, as a means to improve the high-speed laminability of the secondary polyester sewing thread, for example, a method of reducing friction by reducing the twist angle between the sewing thread and the constituent single yarn filaments (Tokukan Sho 52-27847 However, methods of improving high-temperature dynamic friction characteristics using a silicone oil (see Tokusekki No. 52-8198) are known.
None of these known methods improves the heat resistance of the sewing thread body to improve high-speed sewing performance.
本発明者らは、ポリエステルミシン糸目体の耐熱性を高
めることによってミシン糸の溶断糸切れを減少する方法
について鋭意研究の結果、数々の新しい知見を得た。従
来、ミシン糸の熔断温度を精密に測定する装置はなかっ
たが、本発明者らは先ずミシン糸の溶断温度を測定する
装置を作成した。The inventors of the present invention have obtained a number of new findings as a result of intensive research into a method for reducing fusing thread breakage of sewing thread by increasing the heat resistance of polyester sewing thread bodies. Conventionally, there has been no device that accurately measures the fusing temperature of sewing thread, but the present inventors first created a device that measures the fusing temperature of sewing thread.
以下に溶断温度測定装置の概要を第1図によって説明す
る。第1図において、1は内径8側、長さ15仇帆の円
筒ヒータにして、この円筒ヒータ1内を通してミシン糸
2の一端には滑車3を介して0.1gノdの軍錘4を吊
下し、ミシン糸2の他端を応力検出器5に連結する。そ
して上記円筒ヒータ1内の温度を温度調節器(図示して
いない)につて24oC/分の割合で昇温し、ミシン糸
2が切断して応力検出器5の目盛が0を示したときの温
度が溶断温度である。なお、6は円筒ヒータ1内の温度
を測定するための熱電対であり、上記応力検出器5によ
る糸張力と熱電対6による温度とがX−Y軸としてプロ
ットされる。上記の溶断温度測定装置を使用して、融点
の異なる種々のポリエステルシン糸の溶断温度を測定し
たところ、溶断温度は融点と必しも対応するものでない
ことを見いだしたのであり、この知見は全く予測し得な
いことであった。The outline of the fusing temperature measuring device will be explained below with reference to FIG. In FIG. 1, 1 is a cylindrical heater with an inner diameter of 8 and a length of 15 mm, and a 0.1 g nod army weight 4 is passed through the cylindrical heater 1 and attached to one end of the sewing thread 2 via a pulley 3. The other end of the sewing thread 2 is connected to the stress detector 5. Then, the temperature inside the cylindrical heater 1 is raised at a rate of 24oC/min using a temperature regulator (not shown), and when the sewing thread 2 is cut and the scale of the stress detector 5 shows 0, The temperature is the melting temperature. Note that 6 is a thermocouple for measuring the temperature inside the cylindrical heater 1, and the thread tension measured by the stress detector 5 and the temperature measured by the thermocouple 6 are plotted on the X-Y axis. When they measured the fusing temperatures of various polyester thin threads with different melting points using the above fusing temperature measurement device, they found that fusing temperatures do not necessarily correspond to melting points, and this finding is completely It was something that could not have been predicted.
そこで更に、溶断温度とミシン糸を構成するポリエチレ
ンテレフタレートの特性との依存性について追及するた
め、種々の特性の多くのデータと溶断温度との関係をコ
ンピュータを使用して解析した結果、溶断温度はミシン
糸の極限粘度IVとジェチレングリコールの含有モル%
(DEG)とに蓮して次3XI)で表わされることを知
見したのである。Therefore, in order to further investigate the dependence between the fusing temperature and the properties of polyethylene terephthalate that constitutes the sewing thread, we used a computer to analyze the relationship between a large amount of data on various properties and the fusing temperature. Intrinsic viscosity of sewing thread IV and molar percentage of diethylene glycol
They discovered that (DEG) is combined with 3XI).
溶断温度=46.91V−3.5脚EG十216.7…
・・・(1)なお極限粘度(IV)は、フェノールノテ
トラクロロェタン=6/4の混合溶媒で測定した値であ
る。Fusing temperature = 46.91V - 3.5 leg EG 1216.7...
(1) The intrinsic viscosity (IV) is a value measured using a mixed solvent of phenolnotetrachloroethane=6/4.
またジェチレングリコールの含有モル%(OEG)は、
ポリエチレンテレフタレート中のエチレングリコール成
分に対するジェチレングリコールの含有モル%であって
下記の方法によって測定された値である。すなわち、メ
タノール2ccとポリエチレンテレフタレート(または
ミシン糸原糸)100の9をガラスアンプルに密封し、
このガラスアンプルをオートクレープ中で250qo、
6時間加熱し、冷却したのち取り出してガラスアンプル
を開封し、この分解液をガスクロマトグラフで展開し、
100〜210℃の間を6℃/分の割合で昇温し、得ら
れたチャートからエチレングリコールとジェチレングリ
コールに基づくピーク面積を求め、ジェチレングリコル
面積/エチレングリコール面積の比からDEGを求める
。なお上記ガスクロマトグラフィの条件は、内径3側、
長さ150仇蚊のガラスカラムに、市販の充填剤(坦体
として60〜80メッシュのカメライトCSにPEG2
mMを10%保持さてたもの)を用い、検出器はフレー
ム・イオニゼーション・デイテクタ(Em)を用い、か
つイジェクション温度を22000とした。さて、従来
市販されているポリステルミシン糸の溶断温度を測定し
たところ、その最高値は243℃であるから、溶断温度
243o0を越える耐熱性の優れたミシン糸を得るため
には、上該yl)式は次のように書き換えられる。46
‐91V一.58DEG+216‐7>243従って、
IVとDEGとの関係は下記の{1}式を満足する関係
にあるものでなければならない。46‐91V−3‐5
9DEG>263・・・・・・{11ところで上詩yl
方式で分かるように、溶断温度を大き〈すには、極限粘
度IVが大きく、DEGが小さいミシン糸を選択すれば
よいが、極限粘度およびDEGの実用的な値からみて自
ずと限度がある。In addition, the content mol% (OEG) of diethylene glycol is
This is the mol% content of diethylene glycol based on the ethylene glycol component in polyethylene terephthalate, and is a value measured by the following method. That is, 2 cc of methanol and 9 parts of polyethylene terephthalate (or sewing thread) were sealed in a glass ampoule,
250 qo of this glass ampoule in an autoclave,
After heating for 6 hours and cooling, the sample was taken out, the glass ampoule was opened, and the decomposition liquid was developed using a gas chromatograph.
The temperature was raised between 100 and 210°C at a rate of 6°C/min, the peak areas based on ethylene glycol and ethylene glycol were determined from the obtained chart, and DEG was determined from the ratio of ethylene glycol area/ethylene glycol area. demand. The conditions for the gas chromatography above are:
A commercially available packing material (60-80 mesh Camerite CS as a carrier and PEG2
A flame ionization detector (Em) was used as the detector, and the ejection temperature was set at 22,000. Now, when we measured the fusing temperature of commercially available polyster sewing thread, the highest value was 243°C, so in order to obtain a sewing thread with excellent heat resistance that exceeds the fusing temperature of 243°C, the above yl) The formula can be rewritten as follows. 46
-91V1. 58DEG+216-7>243 Therefore,
The relationship between IV and DEG must satisfy the following formula {1}. 46-91V-3-5
9DEG>263...{11 By the way, the above verse yl
As can be seen from the method, in order to increase the fusing temperature, it is sufficient to select a sewing thread with a large intrinsic viscosity IV and a small DEG, but there is a limit in view of the practical values of the intrinsic viscosity and DEG.
この発明は上記の知見につて達成されたものである。This invention has been achieved based on the above findings.
すなわちこの発明は、ポリエチレンテレフタレートから
なるミシン糸を構成するフィラメントが【1) 46‐
91V−3‐58DEG>26.3‘21 0.5<D
EG<3.0{3’ IV<1.0
(ただし、Vは極限粘度、DEGはシン糸を構成するポ
リエチレンテレフタレート中のエチレングリコール成分
に対するジェチレングリコール含有モル%である)の3
式を満足するIV値とDEC値とを有することを特徴と
する耐熱性が優れたポリエステルミシン糸である。That is, in this invention, the filament constituting the sewing thread made of polyethylene terephthalate is [1) 46-
91V-3-58DEG>26.3'21 0.5<D
EG<3.0{3'IV<1.0 (where, V is the intrinsic viscosity, and DEG is the molar percentage of the ethylene glycol content relative to the ethylene glycol component in the polyethylene terephthalate constituting the thin thread).
This polyester sewing thread has excellent heat resistance and is characterized by having an IV value and a DEC value that satisfy the formula.
ミシン糸の極限粘度IVを1.0以上にすることは、重
合工程の最終段階において減圧度おび温度を非常に高く
しなければならず、また製糸工程において酸化、分解に
よる分子鎖の切断は避けることができず、そのためミシ
ン糸のIVを高く望むとは現実的ではなくコストが高く
なる。In order to set the intrinsic viscosity IV of sewing thread to 1.0 or more, the degree of vacuum and temperature must be extremely high in the final stage of the polymerization process, and molecular chain scission due to oxidation and decomposition must be avoided in the spinning process. Therefore, it is not realistic to desire a high IV of sewing thread, and the cost increases.
従ってIVく1.0、好ましくは0.6〜1.0の範囲
が現実的である。ジエチレングリコールは、ポリエチレ
ンテレフタレートの重合過程において、エチレングリコ
ール同士の反応によって生成する創生物であるが、DE
q値を0.5以下にすることは現在の重合技術からみて
困難であり、DEC>3.0の領域において耐熱性を高
めるためにはIVをかなり大きくしなければならず、経
済的に不利となる。Therefore, a realistic range of IV is 1.0, preferably 0.6 to 1.0. Diethylene glycol is a product produced by the reaction between ethylene glycols during the polymerization process of polyethylene terephthalate, but DE
It is difficult to reduce the q value to 0.5 or less based on current polymerization technology, and in order to improve heat resistance in the region of DEC > 3.0, the IV must be considerably increased, which is economically disadvantageous. becomes.
従って上記のように0.5<DEG<3.0と限定され
る。第2図は、前記(1)式にて算出した各熔断温度に
おけるIVとDEGとの関係を示したグラフであり、点
線で囲まれた部分がこの発明における範囲を示しててい
る。上記に説明した(1)式における46.91V−3
.5脚EGの値(以下にA値という)が大きいほどミシ
ン糸の耐熱性は向上するが、上記IVとDEGとの組合
せは、ミシン糸の使用目的に応じて要求される耐熱性と
、その製造コストとの関連によって選択されるべきもの
である。Therefore, as mentioned above, it is limited to 0.5<DEG<3.0. FIG. 2 is a graph showing the relationship between IV and DEG at each melting temperature calculated using the above formula (1), and the area surrounded by the dotted line shows the range according to the present invention. 46.91V-3 in equation (1) explained above
.. The larger the value of pentapod EG (hereinafter referred to as A value), the better the heat resistance of the sewing thread. However, the combination of the above IV and DEG is suitable for the heat resistance required depending on the purpose of use of the sewing thread, and its heat resistance. The choice should be made in relation to manufacturing costs.
例えば厚手の工業用縫製品の場合には、IV=0.78
〜0.81、DEG=0.8〜0.9の組合せが耐熱性
、強度、製造コストの見地から好適であり、また薄手の
衣料縫製品の場合には、IV=0.磯〜0.70、DE
G=0.9〜1.2の組合せが好適である。上記のよう
にポリエチレンテレフタレートの極限粘度IVおよびジ
ェチレングリコールの含有モル%(DEC)を所望の範
囲に粗合せるには、ポリエチレンテフタレートの重合工
程における公知の重合条件を適宜設定することによって
得られる。For example, in the case of thick industrial sewn products, IV=0.78
~0.81, DEG = 0.8 ~ 0.9 is suitable from the viewpoint of heat resistance, strength, and manufacturing cost, and in the case of thin sewn clothing products, IV = 0. Iso~0.70, DE
A combination of G=0.9 to 1.2 is suitable. As mentioned above, in order to roughly adjust the intrinsic viscosity IV of polyethylene terephthalate and the content mol% of diethylene glycol (DEC) within the desired range, it can be obtained by appropriately setting the known polymerization conditions in the polymerization process of polyethylene terephthalate. .
極限粘度は、重合時間、重合温度、雛梓速度、重合時の
減圧度、触媒の種類、添加量などに依存し、重合時間、
重合温度、鷹拝速度、触媒の添加量を大きくするほど極
限粘度が大きくなる傾向にある。また園相重合によって
も極限粘度を大きくすることができる。DEG値は、末
端酸価、添加剤のプロトン濃度、触媒の種類などに依存
し、末端酸価、添加剤のプロトン濃度を低くするとDE
G値は小さくなり、また触媒としてアンチモン、ゲルマ
ニウム、チタニウムなどの化合物を用するとDEG値は
小さくなる。The intrinsic viscosity depends on the polymerization time, polymerization temperature, hatching speed, degree of pressure reduction during polymerization, type of catalyst, amount added, etc.
The intrinsic viscosity tends to increase as the polymerization temperature, speed, and amount of catalyst added increase. The intrinsic viscosity can also be increased by phase polymerization. The DEG value depends on the terminal acid value, the proton concentration of the additive, the type of catalyst, etc., and when the terminal acid value and the proton concentration of the additive are lowered, the DEG value increases.
The G value becomes small, and when a compound such as antimony, germanium, titanium, etc. is used as a catalyst, the DEG value becomes small.
以上に説明したようにこの発明は、ミシン糸のIV値お
よびDEq値を適当に組合せることによってミシン糸目
体の耐熱性を向上し、高速可縫性を満足するものである
が、更にミシン糸の油剤の改良、樹脂加工処理等を併用
すれば耐熱性は相乗的に一層向上される。As explained above, the present invention improves the heat resistance of the sewing machine thread by appropriately combining the IV value and DEq value of the sewing thread, and satisfies high-speed sewing performance. Heat resistance can be further improved synergistically by improving the oil agent, resin processing, etc.
以下この発明の実施例を説明する。Examples of the present invention will be described below.
実施例
‘1’ ポリエチレンテレフタレートの製造テレフタル
酸166部(重量部、以下同じ)、ェチレングリコール
124部に、テレフタル酸に対して0.3モル%のトリ
エチルアミンおよび0.03モル%の三酸化アンチモン
を添加し、これらを蝿梓機、蒸留塔および圧力調整器を
備えたオートクレープに仕込み、3k9/鮒の一定加圧
下に保持しながら240oo、95分間ェステル化反応
させ、次いで0.1柳Hgの減圧下で280oCで68
分間重縮合反応させ、得られたポリマーを試料舷.1と
した。Example '1' Production of polyethylene terephthalate 166 parts (by weight, same below) of terephthalic acid, 124 parts of ethylene glycol, 0.3 mol% triethylamine and 0.03 mol% antimony trioxide based on terephthalic acid. These were charged into an autoclave equipped with a fly mill, a distillation column, and a pressure regulator, and esterification was carried out at 240oo for 95 minutes while maintaining a constant pressure of 3k9/carp, and then 0.1 Yanagi Hg was added. 68 at 280oC under reduced pressure of
The polycondensation reaction was carried out for a minute, and the obtained polymer was placed on the side of the sample. It was set to 1.
またジメチルテレフタレート194部、エチレングリコ
ール135部に、テレフタル酸に対して0.03モル%
の酢酸マンガン、0.05モル%の三酸化アンチモンを
添加し、これらを鰯杵機および蒸留塔を備えたオートク
レープに仕込み、常圧下で180〜190q0、2畑時
間ェステル交換反応させ、次いでトリメチルホスフェー
ト0.04モル%を添加し、0.1側Hgの減圧下で2
8000、50分時重縮合反させてIV値0.62、D
EG値0.9のポリマーを得た。In addition, 194 parts of dimethyl terephthalate, 135 parts of ethylene glycol, and 0.03 mol% based on terephthalic acid.
of manganese acetate and 0.05 mol% of antimony trioxide were added, and these were charged into an autoclave equipped with a sardine pestle and a distillation column, and transesterification was carried out at 180 to 190q0 for 2 field hours under normal pressure, and then trimethyl 0.04 mol% of phosphate was added and 2
8000, polycondensation reaction for 50 minutes, IV value 0.62, D
A polymer with an EG value of 0.9 was obtained.
次いでこのポリマーを0.1側Hg減圧下、240℃で
固相重合させ、固相重合時間が、8時間のものを試料N
o.2、1幼時間のものを試料No.3とした。なお比
較のために上記試料M.1の製造において重縮合時間を
50分間にとどめたものを比較試料とした。■ ミシン
糸の製造
上記試料No.1、2、3および比較試料を用いて下表
の条件にて紡糸、延伸して75デニール、24フィラメ
ントのミシン糸原糸を得た。Next, this polymer was subjected to solid phase polymerization at 240°C under a 0.1 side Hg vacuum, and the solid phase polymerization time of 8 hours was designated as sample N.
o. 2. Sample No. 1 from early childhood. It was set as 3. For comparison, the above sample M. A comparison sample was prepared by keeping the polycondensation time to 50 minutes in the production of Example No. 1. ■ Manufacturing of sewing thread The above sample No. Using Samples 1, 2, 3 and comparative samples, spinning and drawing were performed under the conditions shown in the table below to obtain 75 denier, 24 filament sewing thread yarn.
これらのミシン糸原糸に80■/mの下撚を掛け、これ
を3本合糸して70仇ノmの上撚をかけたのち、ヒート
セットし、次いで染色(13000、40分)工程を経
たのち、シIJコーン系オイルを3%付着さた仕上げ処
理を行ない、次いでミシン糸用ボビンに巻取った。{3
1 ミシン糸の可縫性試験
シンガーミシン社製の本縫77皿1型の高速縫製シンを
便し、シン針DBI#14、ミシン回転数400仇pm
、ステッチ数15ステチ/3伽、上糸張力10雌、下糸
張力25gの条件で、綿布(目付量280gノの)を2
枚重ねて長さ幻hを3回続けて縫い、この間に糸切れが
なければ更に綿布1枚を加えて3枚の綿布を重ねて上記
と同様にして3回縫い、順次に重ね枚数を増加して糸切
れが生ずるまで続けて縫製した。These sewing machine threads were first twisted at 80mm/m, then three threads were combined and twisted at 70mm/m, heat set, and then dyed (13000mm, 40 minutes). After that, it was finished with 3% IJ cone oil and then wound onto a sewing thread bobbin. {3
1 Sewability test of sewing thread A high-speed sewing machine with a lockstitch 77 plate type 1 manufactured by Singer Sewing Machine Co., Ltd. was used, the machine needle was DBI #14, and the sewing machine rotation speed was 400 pm.
, the number of stitches is 15 stitches/3 stitches, the needle thread tension is 10 threads, and the bobbin thread tension is 25 g.
Stack the pieces and sew the length phantom h 3 times in a row.If there is no thread breakage during this time, add 1 more piece of cotton cloth, stack 3 pieces of cotton cloth, sew 3 times in the same way as above, and increase the number of layers in sequence. Then, sewing was continued until thread breakage occurred.
そしてahを完全に縫えた重ね枚数と、3回縫って少な
くとも1回が幻叫こ達し得かつた重ね枚数の縫い長さの
換算値を端数に加えた枚数とをもって可健性枚数とした
。お、この可縫性試験においては、3種の市販品を比較
例として併わせて試験した。‘4’耐熱性試験
上記ミシン糸を、田葉井製作所製循環式乾圃乾燥機にい
れて定長状態で240こ0、2分間保持して加熱処理を
行ない、加熱処理前に対する加熱処理後の強力保持率を
もって耐熱性として示した。Then, the number of healthy sheets was calculated by adding the converted value of the sewing length of the number of stacks that could be sewn completely with ah and the sewing length of the number of stacks that could be sewn at least once out of 3 times to create a phantom stitch. In this sewability test, three types of commercially available products were also tested as comparative examples. '4' Heat Resistance Test The above sewing thread was placed in a circulating dryer manufactured by Tabai Seisakusho and heated at a constant length of 240°C for 2 minutes. It is shown as heat resistance with a strength retention rate of .
表なお、強度保持率(%)について比較試料および市販
品は融着していたので測定できなかった。Note that the strength retention rate (%) could not be measured for the comparison sample and the commercially available product because they were fused together.
上表でみられるように、ミシン糸の融点は、本発明およ
び比較試料、市販品とともに大差がなかったが、溶断温
度に差異があり、溶断温度が高いと可縫I性枚数が多い
ことを示している。As seen in the table above, there was no significant difference in the melting points of the sewing threads of the present invention, comparative samples, and commercially available products, but there was a difference in the fusing temperature, and it was found that the higher the fusing temperature, the greater the number of threads that could be sewn. It shows.
第1図は溶断温度測定装置の概要側面図、第2図は各熔
断温度における極限粘度とDEGモル%との関係を示す
グラフである。
第1図
第2図FIG. 1 is a schematic side view of the melting temperature measuring device, and FIG. 2 is a graph showing the relationship between the intrinsic viscosity and DEG mol% at each melting temperature. Figure 1 Figure 2
Claims (1)
成するフイラメントが(1)46.9IV−3.58D
EG>26.3(2)0.5<DEG<3.0 (3)IV<1.0 (ただしIVは極限粘度、DEGはミシン糸を構成する
ポリエチレンテレフタレート中のエチレングリコール成
分に対するジエチレングリコール含有モル%である)の
3式を満足するIV値とDEG値とを有することを特徴
とする耐熱性が優れたポリエステルミシン糸。[Claims] 1. The filament constituting the sewing thread made of polyethylene terephthalate is (1) 46.9IV-3.58D.
EG>26.3 (2) 0.5<DEG<3.0 (3) IV<1.0 (where IV is the intrinsic viscosity and DEG is the molar content of diethylene glycol relative to the ethylene glycol component in the polyethylene terephthalate that constitutes the sewing thread) A polyester sewing thread with excellent heat resistance, characterized in that it has an IV value and a DEG value that satisfy formula 3 (%).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54074413A JPS6028937B2 (en) | 1979-06-12 | 1979-06-12 | Polyester sewing thread with excellent heat resistance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54074413A JPS6028937B2 (en) | 1979-06-12 | 1979-06-12 | Polyester sewing thread with excellent heat resistance |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56329A JPS56329A (en) | 1981-01-06 |
| JPS6028937B2 true JPS6028937B2 (en) | 1985-07-08 |
Family
ID=13546474
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54074413A Expired JPS6028937B2 (en) | 1979-06-12 | 1979-06-12 | Polyester sewing thread with excellent heat resistance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6028937B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59211638A (en) * | 1983-05-11 | 1984-11-30 | 東レ株式会社 | Polyester filament for stitch yarn |
| JP5992238B2 (en) * | 2012-07-18 | 2016-09-14 | 日本エステル株式会社 | Latent crimped polyester composite fiber yarn and its woven or knitted fabric |
| JP5992239B2 (en) * | 2012-07-18 | 2016-09-14 | 日本エステル株式会社 | Latent crimped polyester composite short fiber and non-woven fabric thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS499112A (en) * | 1972-05-11 | 1974-01-26 | ||
| DE2530294C3 (en) * | 1975-07-07 | 1982-10-28 | Siemens AG, 1000 Berlin und 8000 München | Electric washing machine drive |
| JPS5218302A (en) * | 1975-08-01 | 1977-02-10 | Fuji Photo Film Co Ltd | Magnetic sheet recording/playing method |
| JPS5837418B2 (en) * | 1975-11-18 | 1983-08-16 | 帝人株式会社 | Polyester sewing machine |
-
1979
- 1979-06-12 JP JP54074413A patent/JPS6028937B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56329A (en) | 1981-01-06 |
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