JPH026871B2 - - Google Patents
Info
- Publication number
- JPH026871B2 JPH026871B2 JP61053575A JP5357586A JPH026871B2 JP H026871 B2 JPH026871 B2 JP H026871B2 JP 61053575 A JP61053575 A JP 61053575A JP 5357586 A JP5357586 A JP 5357586A JP H026871 B2 JPH026871 B2 JP H026871B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- yarn
- polybutylene terephthalate
- spinning
- crimped
- 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
Links
- -1 polybutylene terephthalate Polymers 0.000 claims description 32
- 229920001707 polybutylene terephthalate Polymers 0.000 claims description 28
- 238000009987 spinning Methods 0.000 claims description 21
- 239000000839 emulsion Substances 0.000 claims description 15
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 description 11
- 239000004744 fabric Substances 0.000 description 8
- 238000009940 knitting Methods 0.000 description 7
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002216 antistatic agent Substances 0.000 description 3
- 239000003995 emulsifying agent Substances 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 2
- 238000002788 crimping Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical class [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 238000000944 Soxhlet extraction Methods 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 150000008051 alkyl sulfates Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Description
<産業上の利用分野>
本発明はポリブチレンテレフタレート捲縮糸及
びその製造方法に関する。
<従来技術>
従来よりポリエステル、ポリアミド等の捲縮糸
は嵩高、伸縮織編物の製造に広く用いられている
が、近年は更に捲縮糸の高品質化、低価格化が強
く要求されている。従つて、捲縮糸の高伸縮性能
と共に織編物製造工程でのトラブルのない捲縮糸
が強く望まれている。例えば、織編物製造工程に
おいて、マルチフイラメントの単糸切れ、スカム
が発生しない捲縮糸である。
そして、このようなニーズはポリエステルのな
かでも、特にポリブチレンテレフタレート捲縮糸
についても同様である。つまり、ポリブチレンテ
レフタレート捲縮糸はポリエチレンテレフタレー
ト捲縮糸にない優れた伸縮性能と色彩鮮明性、ポ
リアミド捲縮糸にない優れた感触を有している
為、前記問題の解決が強く望まれている。
<目的>
本発明の目的は前記問題の内、特に織編物製造
時のスカム発生のないポリブチレンテレフタレー
ト捲縮糸及びその製造方法を提供する事にある。
<解決手段>
本発明者らは織編物製造時にスカム発生のない
ポリブチレンテレフタレート捲縮糸を得るために
鋭意検討した結果、ポリブチレンテレフタレート
捲縮糸上の付着油剤のPHによつてスカムの発生量
が大きく事なる事を見い出し、更に研究を重ねる
ことにより本発明に到達した。
<構成及び作用>
すなわち本発明は
(1) 糸重量を基準として0.2〜3.0%の範囲で油剤
が付着され、且つ該糸条付着油剤のPHが6.2以
上であることを特徴とするポリブチレンテレフ
タレート捲縮並びに
(2) 紡糸時の付与油剤エマルジヨンのPHを7.5以
上として紡出されたポリブチレンテレフタレー
ト糸に付着させてから延伸、仮撚加工すること
を特徴とするポリブチレンテレフタレート捲縮
糸の製造方法
を主たる内容とするものである。
本発明においてポリブチレンテレフタレート捲
縮糸に対する油剤付与率は0.2ないし3.0%の範囲
にあることが必要である。
0.2%未満では糸上の油剤付着が不均一、及び
油剤被膜が薄くなり、織編物製造時の異常張力、
糸の損傷、更にはスカム発生となる。一方、この
付着率が3.0%を越えると糸の油剤保持限界から
生じる油剤飛散が生じる為3.0%以下更に好まし
くは2.5%以下に押える必要がある。
本発明の最も特徴とする所は、ポリブチレンテ
レフタレート捲縮糸付与油剤のPHを6.2以上に保
持する事にある。この点について添付図面によ
り、更に詳述する。
第1図に於いてスカム発生量は付与油剤のPHの
上昇と共に低下するが特にPH6.0〜6.1で大きく低
下し、使用上問題の生じない安定なPH領域は6.2
以上更に好ましくは6.3以上である。
付与油剤のPHを6.2以上にする事によつてスカ
ム発生が激減する理由については未だ充分解明さ
れていないが、本発明者らの研究によればPHを高
くする事により油剤主成分であり平滑剤、乳化
剤、制電剤の非水時の相溶性向上が確認されてい
る。従つてPH6.2以上にする事によりポリブチレ
ンテレフタレート捲縮糸上の油剤成分間の相溶性
が良好の為、スカム発生が抑制されたものと推定
される。一方、付与油剤のPHの上限はスカム発生
の面からは制限されないが、あまりにも高い場合
はポリブチレンテレフタレートの劣化あるいは付
与油剤のカビ発生等の問題を生じる為、高々9.0
更に好ましくは8.0以下にするのが良い。
本発明の特徴とする、ポリブチレンテレフタレ
ート捲縮糸上の付着油剤のPHを6.2以上にする上
で留意すべき事がある。それは紡糸油剤エマルジ
ヨンのPHを7.5以上に調整する事である。
第2図は紡糸油剤エマルジヨンのPHと糸上付着
油剤のPHの関係を示したものである。紡糸油剤エ
マルジヨンのPHと糸上油剤のPHは正相関し、糸上
付着油剤のPH6.2以上を得るには紡糸油剤エマル
ジヨンのPHを7.5以上とする必要がある。
本発明でいうポリブチレンテレフタレートとは
ポリブチレンテレフタレートを70重量%以上含有
するものであり、30重量%以下の他ポリマー、例
えばポリエチレンテレフタレート、ポリアミド、
共重合物あるいは熱安定剤、酸化防止剤、艶消剤
等を含有していても良い。
糸上での油剤付与率を0.3〜3.0%の範囲に保持
するには、ポリブチレンテレフタレート溶融紡糸
後巻取前に紡糸油剤として油剤エマルジヨンを
0.3ないし3.0%となる様に付与する方法が最も一
般的かつ容易であるが、非水油剤であつても良く
更に捲縮加工糸油剤を付与する工程を併用しても
良い。この場合油剤組成、油剤成分については格
別の制限はなく斯界で慣用されているものを使用
すればよい。
捲縮加工後に油剤付与工程を併用する場合は糸
上付着油剤全体として、付与率0.3ないし3.0%、
PH6.2以上となる様に調整すれば良い。
本発明のポリブチレンテレフタレート捲縮糸の
製造工程としては
紡糸、延伸、仮撚加工がそれぞれ独立した工
程
紡糸延伸と仮撚加工が独立した工程
紡糸と延伸仮撚加工が独立した工程
紡糸延伸仮撚加工を連続化した工程
いずれもが採用出来、更に仮撚加工後油剤付与
工程が単独、連続いずれかの方法で付加されてい
ても良い。
ここで、紡糸工程は低速引取りによる低配向未
延伸糸、高速引取りによる高配向未延伸糸、いわ
ゆる部分配向糸の紡糸工程のいずれでも良い。
尚、本発明に於けるポリブチレンテレフタレー
ト捲縮糸の伸縮率は特に限定されるものではな
く、高伸縮性が要求される用途には高伸縮率の捲
縮糸を、低伸縮性が良いものは低伸縮率の捲縮糸
にすれば良い。
本発明に於ける油剤付着率、付着油剤のPH、紡
糸油剤エマルジヨンのPHおよびスカム発生量の測
定は以下の方法による。
(a) 油剤付着率
ポリブチレンテレフタレート捲縮糸3gをソツ
クスレー抽出基を用い、シクロヘキサンにて30分
間油剤を抽出し、抽出液のシクロヘキサンを蒸発
させ、残存油剤重量(W)を測定し、
油剤付着率(%)=(W/3)×100
で算出する。
(b) 付着油剤のPH
ポリブチレンテレフタレート捲縮糸20gを500
gの蒸留水にて40℃で30分間攪拌して油剤を抽出
し、油剤抽出液を20℃に自然冷却し、日立―ホリ
バ製 M―7型 PHメーターにて測定する。
(c) 紡糸油剤エマルジヨンのPH
油剤エマルジヨンを20℃にて日立―ホリバ製
M―7型 PHメーターにて測定する。
(d) スカム発生量
ポリブチレンテレフタレート捲縮糸を20℃、65
%RHで2日間調整した試料を供給張力を0.5g/
deに調整し、直径4mmで粗度5sのクロム梨地ガイ
ド上を接触角90゜引取り速度700m/分で120分走
行させ同一試料5回くり返しガイド上へのスカム
付着量(単位mg)を測定する。
[実施例]
実施例 1
固有粘度[η]0.88で酸化チタンを0.1重量%
含有するポリブチレンテレフタレートを265℃で
溶融し0.3φの孔を6ケ有する紡糸口金を用い吐出
量5.1g/分で吐出して引取り速度1000m/分で
引取り紡糸油剤付与後巻取り未延伸糸を得た。こ
の時使用した紡糸油剤は平滑剤、乳化剤、制電剤
を主成分としたもの(第2表)をイオン交換水に
て総濃度7.5%のエマルジヨンであり、エマルジ
ヨンのPHを苛性ソーダ又は乳酸にて種々変更して
使用した。又紡糸油剤付与量は捲縮加工後の油剤
付着率が0.55〜0.6%となる様に調整した。
ついで未延伸糸を500m/分の速度で2.3倍延伸
し、連続してヒーター温度190℃でシヨアー硬度
93゜のウレタン軸外接摩擦仮撚装置を用いて仮撚
加工をおこない20デニール/6フイラメントの捲
縮糸を得た。
得られた捲縮糸のスカム発生量を第1表に示
す。
<Industrial Application Field> The present invention relates to a polybutylene terephthalate crimped yarn and a method for producing the same. <Prior art> Crimped yarns made of polyester, polyamide, etc. have traditionally been widely used in the production of bulky, stretchable woven and knitted fabrics, but in recent years there has been a strong demand for higher quality and lower prices for crimped yarns. . Therefore, there is a strong desire for a crimped yarn that has high elasticity and is free from trouble in the weaving and knitting fabric manufacturing process. For example, it is a crimped yarn that does not cause multifilament single yarn breakage or scum in the weaving or knitting fabric manufacturing process. These needs also apply to polyesters, especially polybutylene terephthalate crimped yarns. In other words, polybutylene terephthalate crimped yarn has excellent elasticity and color clarity that polyethylene terephthalate crimped yarn does not have, and excellent feel that polyamide crimped yarn does not have, so there is a strong desire to solve the above problems. There is. <Objective> Among the above-mentioned problems, the object of the present invention is to provide a polybutylene terephthalate crimped yarn and a method for producing the same, which do not cause scum to occur during the production of woven or knitted fabrics. <Solution> As a result of intensive studies by the present inventors to obtain a polybutylene terephthalate crimped yarn that does not generate scum during the production of woven or knitted fabrics, we found that scum was generated due to the pH of the oil agent attached to the polybutylene terephthalate crimped yarn. They discovered that the amount makes a big difference, and through further research, they arrived at the present invention. <Structure and operation> That is, the present invention provides (1) a polybutylene terephthalate to which an oil agent is attached in a range of 0.2 to 3.0% based on the yarn weight, and the pH of the oil agent attached to the yarn is 6.2 or more; Crimp and (2) Production of polybutylene terephthalate crimped yarn, characterized in that the pH of the oil emulsion applied during spinning is set to 7.5 or higher, and the oil emulsion is attached to the spun polybutylene terephthalate yarn, and then stretched and false-twisted. The main content is methods. In the present invention, it is necessary that the oil agent application rate to the polybutylene terephthalate crimped yarn be in the range of 0.2 to 3.0%. If it is less than 0.2%, the oil adhesion on the yarn will be uneven, the oil coating will become thin, and abnormal tension will occur during the production of woven or knitted fabrics.
Damage to the yarn and even scum will occur. On the other hand, if this adhesion rate exceeds 3.0%, oil scattering occurs due to the oil retention limit of the yarn, so it is necessary to keep it below 3.0%, more preferably below 2.5%. The most distinctive feature of the present invention is that the pH of the polybutylene terephthalate crimped thread-imparting oil is maintained at 6.2 or higher. This point will be explained in more detail with reference to the accompanying drawings. In Figure 1, the amount of scum generated decreases as the pH of the applied oil increases, but it decreases particularly significantly at pH 6.0 to 6.1, and the stable pH range that does not cause problems in use is 6.2.
More preferably, it is 6.3 or more. The reason why scum generation is drastically reduced by increasing the pH of the applied oil to 6.2 or higher is still not fully understood, but according to research by the present inventors, increasing the pH of the applied oil improves the smoothness of the main component of the oil. Improved compatibility of agents, emulsifiers, and antistatic agents in non-aqueous conditions has been confirmed. Therefore, it is presumed that by setting the pH to 6.2 or higher, the compatibility between the oil components on the polybutylene terephthalate crimped yarn is good, and thus the generation of scum is suppressed. On the other hand, the upper limit of the pH of the applied oil is not limited in terms of scum generation, but if it is too high, problems such as deterioration of polybutylene terephthalate or mold growth of the applied oil will occur, so it is at most 9.0.
More preferably, it is 8.0 or less. There are some things to keep in mind when setting the pH of the oil agent attached to the polybutylene terephthalate crimped yarn to 6.2 or higher, which is a feature of the present invention. The goal is to adjust the pH of the spinning oil emulsion to 7.5 or higher. Figure 2 shows the relationship between the PH of the spinning oil emulsion and the PH of the oil adhering to the yarn. There is a positive correlation between the PH of the spinning oil emulsion and the PH of the yarn oil, and in order to obtain a PH of 6.2 or higher for the oil attached to the yarn, the PH of the spinning oil emulsion must be 7.5 or higher. Polybutylene terephthalate as used in the present invention refers to polybutylene terephthalate containing 70% by weight or more, and 30% by weight or less of other polymers such as polyethylene terephthalate, polyamide,
It may contain a copolymer, a heat stabilizer, an antioxidant, a matting agent, etc. In order to maintain the oil application rate on the yarn within the range of 0.3 to 3.0%, an oil emulsion is added as a spinning oil after polybutylene terephthalate melt spinning and before winding.
The most common and easiest method is to apply it at a concentration of 0.3 to 3.0%, but a non-aqueous oil may also be used, and a step of applying a crimped yarn oil may also be used. In this case, there are no particular restrictions on the oil composition and oil components, and those commonly used in this field may be used. If an oil application process is used after crimping, the overall oil application rate on the yarn should be 0.3 to 3.0%,
Just adjust it so that the pH is 6.2 or higher. The manufacturing process of the polybutylene terephthalate crimped yarn of the present invention includes: A process in which spinning, drawing, and false twisting are independent processes A process in which spinning and drawing and false twisting are independent A process in which spinning and drawing and false twisting are independent Spinning and drawing false twisting Any process that makes processing continuous can be adopted, and an oil agent application process after false twisting may be added either singly or continuously. Here, the spinning process may be either a spinning process of a low-oriented undrawn yarn by taking off at a low speed, a spinning process of a highly oriented undrawn yarn by taking off at a high speed, or a so-called partially oriented yarn spinning process. Note that the stretch rate of the polybutylene terephthalate crimped yarn in the present invention is not particularly limited, and for applications that require high stretchability, crimped yarns with a high stretch rate may be used, while crimped yarns with low stretchability may be used. A crimped yarn with a low elasticity may be used. In the present invention, the oil adhesion rate, the PH of the adhering oil, the PH of the spinning oil emulsion, and the amount of scum generated are measured by the following methods. (a) Oil adhesion rate Extract the oil from 3 g of polybutylene terephthalate crimped yarn with cyclohexane for 30 minutes using a Soxhlet extraction group, evaporate the cyclohexane in the extract, measure the weight (W) of the remaining oil, and determine the oil adhesion. Calculate by ratio (%) = (W/3) x 100. (b) PH of attached oil agent 20g of polybutylene terephthalate crimped yarn
Extract the oil by stirring with g of distilled water at 40°C for 30 minutes, naturally cool the oil extract to 20°C, and measure with a Hitachi-Horiba M-7 PH meter. (c) PH of spinning oil emulsion Oil emulsion manufactured by Hitachi-Horiba at 20℃
Measure with M-7 type PH meter. (d) Amount of scum generated Polybutylene terephthalate crimped yarn at 20℃, 65℃
Supply the sample adjusted at %RH for 2 days with a tension of 0.5 g/
The same sample was run 5 times on a chromium matte guide with a diameter of 4 mm and a roughness of 5 seconds at a contact angle of 90 degrees and a take-up speed of 700 m/min for 120 minutes, and the amount of scum attached to the guide (unit: mg) was measured. Measure. [Example] Example 1 Titanium oxide 0.1% by weight with intrinsic viscosity [η] 0.88
The polybutylene terephthalate contained therein was melted at 265°C, discharged at a rate of 5.1 g/min using a spinneret with 6 holes of 0.3φ, and taken off at a take-up speed of 1000 m/min.After applying a spinning oil, the product was wound and unstretched. Got the thread. The spinning oil used at this time was an emulsion whose main components were a leveling agent, an emulsifier, and an antistatic agent (Table 2) with ion-exchanged water to a total concentration of 7.5%, and the pH of the emulsion was adjusted with caustic soda or lactic acid. It was used with various changes. The amount of spinning oil applied was adjusted so that the oil adhesion rate after crimping was 0.55 to 0.6%. Then, the undrawn yarn was drawn 2.3 times at a speed of 500 m/min, and the Shore hardness was continuously adjusted at a heater temperature of 190°C.
A 20 denier/6 filament crimped yarn was obtained by false twisting using a 93° urethane shaft circumscribed friction false twisting device. Table 1 shows the amount of scum generated in the obtained crimped yarn.
【表】【table】
【表】
第2表
平滑剤
ラウリルアルコール(EO 4モル付加)のイソ
ステアリン酸エステル …70重量%
乳化剤
ノニルフエニル(EO 9モル付加)エーテル
…10重量%
ラウリル(EO 10モル付加)エーテル
…10重量%
制電剤
アルキルサルフエートのNa金属塩 …5重量%
金属石けん …5重量%
実施例 2
実施例1で得た捲縮糸テストNo.2,4,5,
6,8を永田機械製KT―4型ストツキング編機
を用い600rpmでストツキング編立テストを行な
つた。その結果本発明による捲縮糸(テストNo.
5,6,8)は24時間連続編立を行なつても編針
へのスカム付着は認められず、編地には目切れ、
目飛び、段斑、経筋等のない良好なものであつ
た。
一方本発明以外の捲縮糸(テストNo.2)は6時
間経過後から編針へのスカム付着が認められ同時
に編地に経筋が発生した。また、テストNo.4につ
いても18時間経過後からテストNo.2と同様な問題
が発生した。[Table] Table 2 Smoothing agent Isostearate ester of lauryl alcohol (4 moles of EO added)...70% by weight Emulsifier Nonyl phenyl (9 moles of EO added) ether
…10% by weight lauryl (EO 10 mole addition) ether
…10% by weight Antistatic agent Sodium metal salt of alkyl sulfate …5% by weight Metal soap …5% by weight Example 2 Crimped yarn test No. 2, 4, 5 obtained in Example 1,
A stocking knitting test was conducted using a KT-4 type stocking knitting machine manufactured by Nagata Kikai Co., Ltd. at 600 rpm. As a result, the crimped yarn according to the present invention (Test No.
5, 6, and 8) showed no scum adhering to the knitting needles even after continuous knitting for 24 hours, and the knitted fabrics did not have any cuts or cuts.
It was in good condition with no skipped stitches, step spots, warp lines, etc. On the other hand, with the crimped yarn other than the present invention (Test No. 2), scum adhesion to the knitting needles was observed after 6 hours, and at the same time, warp lines were generated in the knitted fabric. Further, in Test No. 4, the same problem as Test No. 2 occurred after 18 hours.
第1図はポリブチレンテレフタレート捲縮糸に
関して付着油剤PHとスカム発生量との関係を示す
グラフ、第2図は同様に紡糸油剤エマルジヨンPH
と付着油剤PHとの関係を示すグラフである。
Figure 1 is a graph showing the relationship between the attached oil PH and the amount of scum generated for polybutylene terephthalate crimped yarn, and Figure 2 is a graph showing the relationship between the PH of the spinning oil emulsion and the amount of scum produced.
It is a graph showing the relationship between and the adhering oil agent PH.
Claims (1)
剤が付着され、且つ該糸上付着油剤のPHが6.2以
上であることを特徴とするポリブチレンテレフタ
レート捲縮糸。 2 糸上付着油剤のPHが9.0以下である特許請求
の範囲第1項記載のポリブチレンテレフタレート
捲縮糸。 3 紡糸時の付与油剤エマルジヨンのPHを7.5以
上として、紡出されたポリブチレンテレフタレー
ト糸に0.3〜3.0%付着させてから、延伸仮撚加工
することを特徴とするポリブチレンテレフタレー
ト捲縮糸の製造方法。[Scope of Claims] 1. A crimped polybutylene terephthalate yarn, characterized in that an oil agent is attached to the yarn in an amount of 0.2 to 3.0% based on the weight of the yarn, and the pH of the oil agent deposited on the yarn is 6.2 or more. 2. The polybutylene terephthalate crimped yarn according to claim 1, wherein the pH of the oil adhering to the yarn is 9.0 or less. 3 Production of polybutylene terephthalate crimped yarn, characterized in that the pH of the oil emulsion applied during spinning is set to 7.5 or higher, and 0.3 to 3.0% of the oil emulsion is applied to the spun polybutylene terephthalate yarn, and then stretched and false-twisted. Method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5357586A JPS62215071A (en) | 1986-03-13 | 1986-03-13 | Polybutylene terephthalate crimped yarn and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5357586A JPS62215071A (en) | 1986-03-13 | 1986-03-13 | Polybutylene terephthalate crimped yarn and its production |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62215071A JPS62215071A (en) | 1987-09-21 |
JPH026871B2 true JPH026871B2 (en) | 1990-02-14 |
Family
ID=12946628
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5357586A Granted JPS62215071A (en) | 1986-03-13 | 1986-03-13 | Polybutylene terephthalate crimped yarn and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62215071A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60231826A (en) * | 1984-04-24 | 1985-11-18 | Toray Ind Inc | Production of polyester fiber for false twisting |
JPS61677A (en) * | 1984-06-12 | 1986-01-06 | 帝人株式会社 | Production of thermoplastic synthetic crimped processed yarn |
-
1986
- 1986-03-13 JP JP5357586A patent/JPS62215071A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60231826A (en) * | 1984-04-24 | 1985-11-18 | Toray Ind Inc | Production of polyester fiber for false twisting |
JPS61677A (en) * | 1984-06-12 | 1986-01-06 | 帝人株式会社 | Production of thermoplastic synthetic crimped processed yarn |
Also Published As
Publication number | Publication date |
---|---|
JPS62215071A (en) | 1987-09-21 |
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