JPS597813B2 - Method and device for producing spun yarn-like yarn - Google Patents
Method and device for producing spun yarn-like yarnInfo
- Publication number
- JPS597813B2 JPS597813B2 JP3865776A JP3865776A JPS597813B2 JP S597813 B2 JPS597813 B2 JP S597813B2 JP 3865776 A JP3865776 A JP 3865776A JP 3865776 A JP3865776 A JP 3865776A JP S597813 B2 JPS597813 B2 JP S597813B2
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- fluid
- thread
- chamber
- core
- 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
- 238000000034 method Methods 0.000 title description 22
- 239000012530 fluid Substances 0.000 claims description 130
- 238000002347 injection Methods 0.000 claims description 32
- 239000007924 injection Substances 0.000 claims description 32
- 238000003756 stirring Methods 0.000 claims description 25
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 230000000694 effects Effects 0.000 description 11
- 238000013016 damping Methods 0.000 description 8
- 230000000717 retained effect Effects 0.000 description 6
- 239000000470 constituent Substances 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010409 ironing Methods 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Landscapes
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Description
【発明の詳細な説明】
本発明は、連続マルチフィラメント糸を構成要素とする
紡績糸風の風合と外観を有する紡績糸風糸の製造方法及
びその装置に関するものであり、更に詳しくは、流体の
作用により芯糸の周囲に連続マルチフィラメント糸を多
重に纏絡せしめて多数のループによって覆われた軽度の
斑と嵩高性とをもつ紡績糸風の糸の製造方法と装置とを
提供するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for producing a spun yarn-like yarn having the texture and appearance of a spun yarn, which has a continuous multifilament yarn as a component, and more specifically relates to To provide a method and apparatus for producing a spun yarn-like yarn having slight unevenness and bulkiness covered by a large number of loops by entangling continuous multifilament yarn around a core yarn in multiple layers by the action of It is.
これまでにも流体の作用によりマルチフィラメント糸を
ループ状に集束して紡績糸風の糸を製造する方法及び装
置が種々提案されている。Various methods and apparatuses have been proposed so far for producing spun yarn-like yarns by converging multifilament yarns into a loop shape using the action of fluid.
例えば、連続マルチフィラメント糸を高速攪乱流体域に
通過せしめてループ、からみ又はもつれなどを不規則に
与える方法がある。For example, a continuous multifilament yarn may be passed through a region of high velocity turbulent fluid to randomly create loops, tangles or entanglements.
これは、いわゆるタスラン方式と呼ばれるところのよく
知られた代表的な方法の1つである。This is one of the well-known representative methods called the so-called Taslan method.
この方法により紡績糸に似た外観をなす糸は製造され得
るが、表面に突出したループを固定するために加撚する
ことが必須であるので、この糸は嵩高性にも乏しくなっ
て紡績糸よりも硬い感触になり、又高圧空気が必要とさ
れるため空気流量が大きく、それに比して加工速度が低
いために、製造コストが高くなるという欠薇がこの方法
にはあり、この方法は実用的に不利であった。This method can produce yarns that look similar to spun yarns, but since twisting is essential to fix the protruding loops on the surface, the yarns also have poor bulk, making them less bulky than spun yarns. This method has the disadvantages that it feels harder than the conventional method, and high pressure air is required, so the air flow rate is large, and the processing speed is relatively low, which increases the manufacturing cost. This was disadvantageous in practical terms.
また他の方法としては高速気流とともに送り出された繊
維を旋回気流管内に供給して管の軸に沿って且つ旋回気
流が管より排出される向きと反対の向きに引き取る方法
(特公昭47−36225)があるが、この方法によっ
て製造された糸は、強力が極めて小さく脆いため、実用
性に乏しい欠点をもっていた。Another method is to supply the fibers sent out with a high-speed airflow into a swirling airflow tube and take them along the axis of the tube and in the opposite direction to the direction in which the swirling airflow is discharged from the tube (Japanese Patent Publication No. 47-36225 ), but the yarn produced by this method has extremely low strength and brittleness, making it impractical.
また1本以上の連続マルチフィラメント糸を高速気流と
ともに旋回気流室内に供給して該室内を軸方向に走行す
る芯糸に対してまきつけ、搦糸の供給速度よりも遅い速
度で引き取る方法(米国特許第3041812号明細書
及び特公昭49−24177)があるが、この方法では
得られた糸の絡合性が非常に悪く、後工程例えば編織す
る段階でこの糸がしごかれると、搦糸が芯糸の上をルー
ズにずれて、スラブ状になったり、ガイドにつまって糸
切れを起したりして、この糸は衣料用の糸としては、使
用に耐えないものであった。Another method is to supply one or more continuous multifilament yarns with a high-speed airflow into a swirling airflow chamber, wrap the yarn around a core yarn running in the axial direction in the chamber, and take it off at a speed slower than the feeding speed of the yarn (U.S. Pat. No. 3041812 and Japanese Patent Publication No. 49-24177), however, the entanglement of the yarn obtained by this method is very poor, and when the yarn is squeezed in the subsequent process, such as knitting and weaving, the threads become loose. This yarn could not be used as a clothing yarn because it slipped loosely on the core yarn, resulting in a slab-like shape, or jammed in the guide, causing yarn breakage.
これに対しては、本発明者は、さきに流体加撚素子によ
り加撚されつ\流体搦み室内のほゾ軸心部を走行する芯
糸に対して、実質的に無撚の連続マルチフィラメントか
らなる搦糸を該流体搦み室内にその糸通路の接線方向に
芯糸走行速度の3倍以上の速度で高速流体とともに噴入
せしめて前記芯糸に合流せしめた後、前記流体加撚素子
によって絡合せしめる紡績糸風糸の製造方法を提案した
。In order to solve this problem, the present inventor has developed a technique for creating a substantially untwisted continuous multi-layer yarn for the core yarn which is first twisted by a fluid twisting element and then runs along the tenon axis in the fluid twisting chamber. After the filament yarn is injected together with a high-speed fluid into the fluid twisting chamber in the tangential direction of the yarn path at a speed of three times or more of the core yarn running speed to merge with the core yarn, the fluid twisting is performed. We proposed a method for producing spun yarn-like yarn that is intertwined with elements.
該方法によって、ほゾ前記欠点を解消し、容易に連続マ
ルチフィラメント糸を構成要素とする紡績糸風の風合と
外観を有する紡績糸風糸の製造が可能とされたが、更に
本発明者は糸斑の減少と搦糸の絡合性の向上を図った結
果、本発明に到達したものである。By this method, the above-mentioned drawbacks of the tenon can be solved, and it has become possible to easily produce a spun yarn-like yarn having the texture and appearance of a spun yarn, which has a continuous multifilament yarn as a constituent element. The present invention was achieved as a result of efforts to reduce thread unevenness and improve the entanglement of threads.
すなわち、本発明は、流体加撚素子の上流側で該流体加
撚素子によって加撚されつ5流体搦み室のほゾ軸心部を
走行する芯糸に対して実質的に無撚の連続マルチフィラ
メント糸から成る搦糸を該流体搦み室内にその糸通路の
接線方向に沿って該芯糸走行速度の3倍以上の速度で流
体とともに噴入し、搦糸噴入孔の底部の開孔率45%以
下O%以上の多孔面の底面を有する小室にて一時的に滞
留せしめた後、該芯糸に合流せしめ、続いて前記流体加
撚素子を通過せしめ、芯糸を解撚することにより該芯糸
に搦糸を絡合せしめることを特徴とする紡績糸風糸の製
造方法及びこの方法を実施するに好適な装置として、流
体搦み室と流体加撚素子とが走行する芯糸の進行方向に
沿って順に配列され、該流体搦み室には搦糸噴入孔がそ
の糸通路の接線方向に曲孔し、該搦糸噴入孔の底部は開
孔率45%以下O%以上の多孔面の底面を有する小室を
なすことを特徴とする紡績糸風糸の製造装置である。That is, the present invention provides a substantially untwisted continuous core yarn that is twisted by the fluid twisting element on the upstream side of the fluid twisting element and runs in the tenon shaft center of the five fluid twisting chambers. A thread made of multifilament yarn is injected along with a fluid along the tangential direction of the thread path into the fluid damping chamber at a speed that is more than three times the running speed of the core thread, and the thread is opened at the bottom of the thread injection hole. After being temporarily retained in a small chamber having a porous bottom with a porosity of 45% or less and 0% or more, it is merged with the core yarn, and then passed through the fluid twisting element to untwist the core yarn. A method for producing a spun yarn-like yarn characterized by intertwining a filament with the core yarn, and an apparatus suitable for carrying out this method include a core in which a fluid twisting chamber and a fluid twisting element run. They are arranged in order along the traveling direction of the yarn, and the fluid stirring chamber has a yarn injection hole curved in the tangential direction of the yarn passage, and the bottom of the yarn injection hole has an aperture ratio of 45% or less. This is an apparatus for producing spun yarn-like yarn characterized by forming a small chamber having a bottom surface with a porous surface of 0% or more.
次に図面を用いて更に本発明を詳細に説明する。Next, the present invention will be further explained in detail using the drawings.
第1図は、本発明の製造装置の斜視図、第2図及び第3
図は第1図の■一…線に沿う流体搦み室の1〜2例の水
平断面図、第4図は、第1図のIV−It/線に沿う流
体搦み室の縦断面図、第5図は第1図の■一V線に沿う
流体加撚素子の縦断面図である。FIG. 1 is a perspective view of the manufacturing apparatus of the present invention, FIG.
The figure is a horizontal sectional view of one or two examples of the fluid swell chamber along line 1 in Fig. 1, and Fig. 4 is a vertical sectional view of the fluid swell chamber along line IV-It/ in Fig. 1. , FIG. 5 is a longitudinal sectional view of the fluid twisting element taken along line 1-V in FIG.
第6図は、流体搦み室と流体加撚素子を一体化したもの
の縦断面図である。FIG. 6 is a longitudinal sectional view of an integrated fluid twisting chamber and fluid twisting element.
第1図において、適当なパッケージ1から引き出された
実質的に無撚の連続マルチフィラメント糸からなる搦糸
2は、ガイド3を通り供給ローラー4によって積極的に
送り出され、該供給ローラー4の下方に設けられたエジ
エクタ−5によって流体流とともに搦糸噴入孔22を通
って流体搦み室6の糸通路28の接線方向に供給され、
該搦糸噴入孔22の底部に設けられた小室27に一時的
に滞留される。In FIG. 1, a thread 2 consisting of a substantially untwisted continuous multifilament thread drawn from a suitable package 1 is actively fed out by a feed roller 4 through a guide 3 and below the feed roller 4. The fluid is supplied along with the fluid stream through the thread injection hole 22 in the tangential direction of the thread passage 28 of the fluid damping chamber 6 by the ejector 5 provided in the
The thread is temporarily retained in a small chamber 27 provided at the bottom of the thread injection hole 22.
他方芯糸8は、パッケージ7より取り出され、ガイド9
を通り、供給ローラー10により送り出され、流体加撚
素子11により加撚されつX流体搦み室6の上面ほゾ中
央に設けられている芯糸導入孔15を通り該流体搦み室
6のほぼ軸心部を通過する際、搦糸噴入孔22の底部に
滞留されている搦糸2をその周囲にまきつけながら、流
体搦み室6の下面から引き出されて絡合糸19となり、
引き続いて流体加撚素子11を経て糸斑と絡合性が飛躍
的に向上された糸25となり、デリベリローラー12に
よって積極的に送りだされ、ガイド26を通って駆動ド
ラム13によって表面駆動されるパッケージ24にまき
とられる。On the other hand, the core yarn 8 is taken out from the package 7 and guided through the guide 9.
The yarn is sent out by the supply roller 10, twisted by the fluid twisting element 11, and passed through the core introduction hole 15 provided at the center of the tenon on the upper surface of the fluid twisting chamber 6. When passing approximately the axial center, the thread 2 retained at the bottom of the thread injection hole 22 is wrapped around it and pulled out from the lower surface of the fluid stirring chamber 6 to become an entangled thread 19.
Subsequently, it passes through the fluid twisting element 11 to become a yarn 25 with dramatically improved yarn unevenness and entanglement, which is then actively sent out by the delivery roller 12, passes through the guide 26, and is driven to the surface by the drive drum 13. It is wrapped in a package 24.
得られた糸は、芯糸8の周囲に搦糸2の構成フィラメン
トが多数のループ状となって多層にしかも堅固に纏絡し
、軽度の糸斑と嵩高性をもった暖かみのある紡績糸風の
感触と極く自然な外観と極めて後工程の取り扱い性に優
れた性能とを有する。The obtained yarn has a large number of loops of the constituent filaments of the yarn 2 around the core yarn 8, and is tightly entwined in multiple layers, giving it a warm spun yarn style with mild unevenness and bulkiness. It has a very natural feel, a very natural appearance, and excellent performance in handling in post-processes.
ここに用いられる搦糸2としては、実質的に無撚の連続
マルチフィラメント糸が好ましく、撚数が5 0 T/
Mを越えるもの又は高度の流体絡合処理を施されたもの
は、フィラメント相互の分離が充分に行われないため、
芯糸8を被覆し、モノフィラメント単位の繊細なループ
を多数形成し、しかも斑の少し堅固な絡合状態を得るこ
とが困難なため、使用には適さない。The yarn 2 used here is preferably a substantially untwisted continuous multifilament yarn, with a twist count of 50 T/
If the filament exceeds M or has been subjected to a high degree of fluid entanglement treatment, the filaments will not be separated sufficiently from each other.
It is not suitable for use because it covers the core thread 8 and forms a large number of delicate loops of monofilament units, and it is difficult to obtain a slightly firm intertwined state with irregularities.
しかし、実質的に無撚のマルチフィラメント糸であれば
、必要により同種又は、異種の光沢、色調、染色性、収
縮性、断面形状その他の性質の異なるもの、繊度若しく
は構成フィラメント本数の異なるものを1乃至2本以上
引き揃え又は甘撚にて合糸して用いても差し支えない。However, if it is a substantially untwisted multifilament yarn, yarns of the same or different luster, color tone, dyeability, shrinkability, cross-sectional shape and other properties, different fineness or number of constituent filaments may be used as necessary. There is no problem even if one or two or more threads are tied together or twisted together.
他方、芯糸8としては、一般に衣料用に用いられるもの
であれば特に限定されず、連続マルチフィラメント糸、
嵩高加工糸、紡績糸又はこれらの中から搦糸2と同様に
性質の異なる若しくは同種のものを1乃至2本以上組み
合わせてもよいが、弾性糸の如く伸張率の著しく大きい
ものは、不適である。On the other hand, the core yarn 8 is not particularly limited as long as it is generally used for clothing, and may include continuous multifilament yarn,
Bulky processed yarns, spun yarns, or one or more yarns of the same type or with different properties similar to those of the filament yarn 2 may be combined, but yarns with a significantly high elongation rate such as elastic yarns are not suitable. be.
この加工方法において、芯糸8の供給ローラー10は、
必らずしも必要とされないが、良好な操業性及び糸質の
安定性を得るためには用いることが好ましい。In this processing method, the supply roller 10 for the core yarn 8 is
Although not necessarily required, it is preferable to use it in order to obtain good operability and stability of the yarn quality.
用いる場合の供給ローラー10の送り出し速度は、デリ
ベリローラー12の引き取り速度よりも早く、すなわち
芯糸8は、若干オーバーフイード状態で加撚域に供給さ
れなければならない。When used, the feeding speed of the supply roller 10 is faster than the take-up speed of the delivery roller 12, that is, the core yarn 8 must be fed to the twisting region in a slightly overfeed state.
本発明では、芯糸8は、流体加撚素子11によって高度
に加撚されねばならずこの加撚効果を得るために加撚域
での芯糸8の張力を低レベルに抑えることが要求される
からである。In the present invention, the core yarn 8 must be highly twisted by the fluid twisting element 11, and in order to obtain this twisting effect, it is required to suppress the tension of the core yarn 8 in the twisting region to a low level. This is because that.
しかし過犬なオーバーフイードは、加撚域でたるみやバ
ルーンを生じて操業が不安定になるため、0〜10%程
度特に1〜4%の範囲が好適である。However, excessive overfeed causes sagging or ballooning in the twisting region, making the operation unstable, so a range of about 0 to 10%, particularly 1 to 4%, is preferable.
このように低張力下で加撚されつN走行する芯糸8は、
流体搦み室6内で芯糸8の供給速度の3倍以上の速度で
流体搦み室6の糸通路28の接線方向に流体流とともに
噴入され、該搦糸噴入孔22の底部の小室27に一時的
に滞留せしめられた搦糸2と接触し、これをその周囲に
まきつけ乍ら、流体搦み室6より引き出される。The core thread 8 that is twisted under low tension and runs in this way is
The fluid is injected along with the fluid flow in the tangential direction of the thread passage 28 of the fluid damping chamber 6 at a speed more than three times the supply speed of the core thread 8 in the fluid dampening chamber 6 , and the thread at the bottom of the thread injection hole 22 is injected. It comes into contact with the thread 2 temporarily retained in the small chamber 27 and is pulled out from the fluid stirring chamber 6 while wrapping it around it.
ここで搦糸噴入孔22は、流体搦み室6の内側壁に対し
、接線方向で、且つその底部は小室27をなすように設
けられることが、芯糸8に対する搦糸2のまきつき斑を
減少せしめ、さらに芯糸8と搦糸2の絡合性を高める上
で必須であるが、該搦糸噴入孔22を通して搦糸2とと
もに流体搦み室6内に噴入される流体によって生ずる乱
流を伴った旋回流の回転方向と流体加撚素子11が芯糸
8を回転せしめる回転方向とが互に逆の関係にある方が
、得られる紡績糸風糸の糸斑を小さくする点で良好であ
る。Here, the thread injection hole 22 is provided in a tangential direction to the inner wall of the fluid stirring chamber 6, and the bottom thereof forms a small chamber 27, so that the winding unevenness of the thread 2 with respect to the core thread 8 can be prevented. This is essential in order to reduce the The yarn unevenness of the obtained spun yarn-like yarn is reduced when the rotational direction of the swirling flow accompanied by the generated turbulent flow and the rotational direction in which the fluid twisting element 11 rotates the core yarn 8 are in an opposite relationship to each other. It is in good condition.
しかし、順の方向であっても充分実用に供し得る良好な
糸が得られるので、特に限定はない。However, even in the forward direction, a yarn of good quality that can be used for practical purposes can be obtained, so there is no particular limitation.
ここで、搦糸噴入孔22の底部の小室27の機能は、流
体搦み室6内に流体とともに芯糸8の走行速度の3倍以
上、好ましくは4〜lO倍の高速で噴入された搦糸2を
一且滞留せしめ、減速甘しめるとともに、開繊効果をも
与えた後、芯糸8に絡合せしめることにあると推定され
る。Here, the function of the small chamber 27 at the bottom of the thread injection hole 22 is to inject the fluid together with the fluid into the fluid damping chamber 6 at a high speed of 3 times or more, preferably 4 to 10 times, the traveling speed of the core thread 8. It is presumed that one of the threads 2 is held there, the speed is reduced, and a fiber opening effect is given, and then the threads 2 are entangled with the core thread 8.
ここでこの搦糸噴入孔22の底部の小室27の効果を高
めるには、該搦糸噴入孔22の軸心は流体搦み室内側壁
よりも外側にある方がよい。Here, in order to enhance the effect of the small chamber 27 at the bottom of the thread injection hole 22, the axis of the thread injection hole 22 is preferably located outside the wall on the side of the fluid stirring chamber.
すなわち、第2図に示す如く流体搦み室6の糸通路28
の半経をR1搦糸噴入孔22の半径をrとし、流体搦み
室6の中心から搦糸噴入孔22の軸心にひいた垂線の長
さをLとすれば、
R<L<R十r
が好ましい範囲である。That is, as shown in FIG.
If the half meridian is R1 and the radius of the thread injection hole 22 is r, and the length of the perpendicular drawn from the center of the fluid stirring chamber 6 to the axis of the thread injection hole 22 is L, then R<L. <R0r is a preferable range.
それは、LがRよりも小さいか又は等しいとき搦糸噴入
孔22の底部に小室27が形成されても、流体搦み室6
への開口部の面積が大きくなるため、搦糸2は小室27
に滞留することなく直接流体搦み室6内へ誘導されるた
めに、小室27の機能が発揮されないためである。That is, even if a small chamber 27 is formed at the bottom of the string injection hole 22 when L is smaller than or equal to R, the fluid stringing chamber 6
Since the area of the opening to
This is because the small chamber 27 does not perform its function because the fluid is guided directly into the fluid stirring chamber 6 without being retained in the fluid chamber 6 .
又LがR十rよりも大きければ搦糸噴入孔22は、流体
搦み室6に開口しない。Further, if L is larger than Rr, the thread injection hole 22 does not open into the fluid damping chamber 6.
従って搦糸2が搦糸噴入孔22の底部に作られた小室2
7に一時的に滞留するためには、搦糸噴入孔22の流体
搦み室6への開口部の面積をある程度小さくしかも搦糸
噴入孔22はエジエクタ−5の流体通路20と連結され
ているのでエジエクタ−5の吸引効果を妨げないように
開口部の面積は、流体通路20の断面積と同じかや一犬
きめにとることが望ましい。Therefore, the small chamber 2 in which the thread 2 is made at the bottom of the thread injection hole 22
7, the area of the opening of the thread injection hole 22 to the fluid stirring chamber 6 is reduced to some extent, and the thread injection hole 22 is connected to the fluid passage 20 of the ejector 5. Therefore, it is desirable that the area of the opening be the same as or slightly equal to the cross-sectional area of the fluid passage 20 so as not to impede the suction effect of the ejector 5.
又更に小室27への搦糸2の滞留効果を高めるために、
第3図の如く、小室27の底面を多孔面30とし搦糸2
とともにエジエクタ−5により噴入された流体の一部を
該多孔面30とその先に設けられた流体排出通路29を
通じて流体搦み室6の外部に排出せしめるとよい。Furthermore, in order to enhance the retention effect of the thread 2 in the small chamber 27,
As shown in FIG. 3, the bottom surface of the small chamber 27 is a porous surface 30, and
At the same time, it is preferable that a part of the fluid injected by the ejector 5 is discharged to the outside of the fluid sumpling chamber 6 through the porous surface 30 and a fluid discharge passage 29 provided beyond the porous surface 30.
この多孔面30の設置により、搦糸2は、スムーズに小
室27に誘導され排出流体流によって該小室27に滞留
されるとともに開繊作用も高められるものと思われる。By providing this porous surface 30, the threads 2 are smoothly guided into the small chambers 27 and retained in the small chambers 27 by the discharged fluid flow, and the opening effect is also enhanced.
しかし、小室27の多孔面30の開孔率があまり大きく
なると、搦糸2とともに噴入された高速流体流の大部分
が、該多孔面30を通して流体搦み室6外へ集中的に排
紙されるため、搦糸2が多孔面30に強く圧着せしめら
れると共に流体搦み室6内での旋回流が消失し、搦糸2
が不規則な運動をするようになるために、激しい糸斑が
発生したり糸切したりして好ましくない。However, if the porosity of the porous surface 30 of the small chamber 27 becomes too large, most of the high-speed fluid flow injected together with the thread 2 is concentratedly discharged to the outside of the fluid stirring chamber 6 through the porous surface 30. As a result, the thread 2 is strongly pressed against the porous surface 30, and the swirling flow within the fluid stirring chamber 6 disappears, causing the thread 2 to
This is undesirable as the threads begin to move irregularly, resulting in severe thread unevenness and thread breakage.
従って、多孔面30の開孔率(総開口面積/底面積)は
45%以下で0%以上におさえる。Therefore, the porosity (total opening area/bottom area) of the porous surface 30 is kept below 45% and above 0%.
好ましい。範囲としては10〜40%である。preferable. The range is 10-40%.
又、小室27の容積としては、搦糸2のデニール、フィ
ラメント数、開繊され易さ及びダブリング数(芯糸に対
する搦糸の供給速度比)などによっても変化するが、通
常の衣料用途に使用する30〜75Dを搦糸とする場合
には、5〜2omr1程度が好ましいようである。In addition, the volume of the small chamber 27 varies depending on the denier of the thread 2, the number of filaments, the ease with which it is opened, the number of doublings (the ratio of feeding speed of the thread to the core thread), etc., but it is used for normal clothing purposes. When using 30 to 75D as the filament yarn, it seems preferable to use about 5 to 2 omr1.
このように流体搦み室6内に噴入されたエジエクタ−5
の高速流体流を巧みに利用して、小室27の作用効果を
高めることにより、搦糸2のまきつき斑は減少され、絡
合性も更に一段と高められるのである。The ejector 5 injected into the fluid stirring chamber 6 in this way
By skillfully utilizing the high-speed fluid flow to enhance the effect of the small chambers 27, the unevenness of the threads 2 being twisted is reduced and the entanglement property is further improved.
しかし、流体搦み室6へ噴入されたエジエクター5の流
体流は、小室27の底面が第3図の如く多孔面30にな
っている鳩合には、多孔面30を通してその一部が排出
されるが、小室27の底面が多孔面でない場合には、第
4図に示される如く流体搦み室6内に噴入された流体は
流体搦み室6に開口する芯糸導入孔15、流体排出孔1
6及び出口孔18等を通して、外部へ排出される。However, if the bottom of the small chamber 27 is a porous surface 30 as shown in FIG. However, if the bottom surface of the small chamber 27 is not a porous surface, as shown in FIG. Fluid discharge hole 1
6 and the outlet hole 18, etc., and are discharged to the outside.
その際、流体搦み室6の芯糸入口面14に開口する排出
に寄与する開口面積の総和を糸条引出面17の開口面積
より大きくとり、流体搦み室6内へ噴入された搦糸2を
排出される流体流に誘導せしめて流体搦み室6内上方に
密度多く存在せしめ、且つ芯糸導入孔15の孔長さを搦
糸2の噴出を防ぐに充分な長さにとり搦糸2と回転しつ
つ走行する芯糸8との接触チャンスを高めることは、糸
質の向上に重要な要因である。At this time, the total area of the openings that contribute to discharge that open on the core yarn inlet surface 14 of the fluid stirring chamber 6 is set to be larger than the opening area of the yarn drawing-out surface 17, so that the core yarn injected into the fluid stirring chamber 6 is The threads 2 are guided by the discharged fluid flow so that they are densely present in the upper part of the fluid stirring chamber 6, and the length of the core thread introduction hole 15 is set to a length sufficient to prevent the threads 2 from being ejected. Increasing the chance of contact between the yarn 2 and the rotating core yarn 8 is an important factor in improving yarn quality.
しかし流体搦み室d内へ噴入される流体流量によっては
必ずしも流体搦み室6の芯糸入口面14の開口面積を糸
条引畠面17のそれよりも大きくしなければならないこ
とはない。However, depending on the flow rate of the fluid injected into the fluid stirring chamber d, it is not necessarily necessary to make the opening area of the core thread inlet surface 14 of the fluid damping chamber 6 larger than that of the thread drawing surface 17. .
又言うまでもないが、排出可能な開口面積の総和は、搦
糸噴入孔22の流体搦み室6への開口面積より大きくと
り、エジエクタ−5による搦糸2の吸引効果を妨げない
ようにしなければならない。Needless to say, the total opening area that can be discharged must be larger than the opening area of the thread injection hole 22 to the fluid stirring chamber 6 so as not to impede the suction effect of the thread 2 by the ejector 5. Must be.
上述の如く、この加工方法において流体搦み室6に対し
て接線方向に設けられた搦糸噴入孔22の底部が小室2
Tをなし、ここに搦糸2を一時的に滞留せしめることに
より、糸斑を低減し得るが、流体搦み室6のみの絡合効
果ではまだ不充分なものであり、本発明方法が目標とす
る高度の絡合性を得るためには、流体搦み室6から引き
出された後、絡合糸19を直ちに、流体加撚素子11に
よる解撚と同時に流体による旋回作用により、これまで
の何れの方法によっても達し得られなかった均斉な外観
と高度の絡合性を兼ね具え、後加工工程での取り扱い性
に優れ嵩高性に富んだ暖かい感触の紡績糸風の糸が得ら
れるのである。As mentioned above, in this processing method, the bottom of the thread injection hole 22 provided in the tangential direction to the fluid stirring chamber 6 becomes the small chamber 2.
By forming a T and temporarily retaining the threads 2 there, it is possible to reduce thread unevenness, but the entanglement effect of only the fluid threading chamber 6 is still insufficient, and the method of the present invention does not aim to achieve this goal. In order to obtain a high degree of entanglement, after being pulled out from the fluid twisting chamber 6, the entangled yarn 19 is immediately untwisted by the fluid twisting element 11 and at the same time by the swirling action of the fluid. The result is a spun yarn-like yarn with a uniform appearance and a high degree of entanglement that could not be achieved even with the above methods, and which is easy to handle in post-processing steps, is bulky, and has a warm feel.
しかも芯糸8の供給速度に対して搦糸2の供給速度の比
率(ダブリング数)を3倍以上特に4〜10倍と小さい
範囲にしてだ高度の絡合度が失なわれず、充分な耐しご
き性があるため、本発明は得られる糸を細デニール化し
得る上に生産性向上、コスト低減に大きく貢献するもの
である。Moreover, if the ratio of the supply speed of the core yarn 2 to the supply speed of the core yarn 8 (the number of doublings) is set in a small range of 3 times or more, especially 4 to 10 times, a high degree of entanglement is not lost and a sufficient degree of entanglement is maintained. Because of the ironing resistance, the present invention not only allows the yarn to be obtained to have a fine denier, but also greatly contributes to improving productivity and reducing costs.
こ\で使用される流体加撚素子11は流体搦み室6と別
々に、又は一体的に構成されてもよいが、該流体加撚素
子11は、高速流体の旋回作用により糸通路を通過する
糸に旋回力を及ぼす如き構造のものであれば特に制約さ
れないが、通常は流体噴入孔23が糸通路に対し、接線
方向に開口されたものが好適である。The fluid twisting element 11 used here may be configured separately or integrally with the fluid twisting chamber 6, but the fluid twisting element 11 can be configured to pass through the yarn path due to the swirling action of high-speed fluid. There is no particular restriction as long as the structure is such that it can exert a turning force on the yarn, but it is usually preferable that the fluid injection hole 23 is opened in the tangential direction with respect to the yarn passage.
使用する流体は、特に限定されないが、環境衛生、安全
性などの面から取り扱いが容易な空気を用いるのが最も
実用的である。The fluid to be used is not particularly limited, but it is most practical to use air, which is easy to handle in terms of environmental hygiene and safety.
そして、この流体加撚素子11に噴入された流体が糸に
旋回力を与えた後の排出は、糸通路を通して行なわれる
が、この排出流体流の方向は、本発明方法においては、
主に流体搦み室6へ向けてすなわち走行する糸の進行と
逆方向であることが好ましい。After the fluid injected into the fluid twisting element 11 imparts a turning force to the yarn, it is discharged through the yarn passage, but in the method of the present invention, the direction of the discharged fluid flow is as follows:
It is preferable that the direction is mainly directed toward the fluid stirring chamber 6, that is, in the direction opposite to the traveling direction of the yarn.
流体加撚素子11の例を第5図に示すが、糸通路31に
流体噴入孔23が開口し、絞り部33は糸の走行方向か
ら見て該流体噴入孔23の直後に設けられた方が、芯糸
8と搦糸2の絡合がよく、得られた糸の周縁に突出した
ループも小さく密になる。An example of the fluid twisting element 11 is shown in FIG. 5, in which a fluid injection hole 23 is opened in a yarn passage 31, and a constriction portion 33 is provided immediately after the fluid injection hole 23 when viewed from the yarn running direction. The more the core yarn 8 and the filament yarn 2 are intertwined, the more the loops protruding from the periphery of the resulting yarn will be smaller and denser.
しかし、これとは逆に糸の進行方向に沿って排気する場
合に、方向性なく、糸通路31を通ってほゾ均等に排出
されるようなときでも上述の場合に比べてや\効果は劣
るものメ充分使用に耐える糸が得られるのである。However, on the contrary, when the yarn is discharged along the traveling direction of the yarn, even when the yarn is discharged evenly through the yarn passage 31 without directionality, the effect is less than in the case described above. Even if the yarn is inferior, a thread that can withstand use can be obtained.
本発明の紡績糸風糸を製造するに用いられる流体搦み室
6及び流体加撚素子11は、第1図の如く、別個に分れ
た形態であっても一体化されていても差し支えない。The fluid twisting chamber 6 and the fluid twisting element 11 used to produce the spun yarn-like yarn of the present invention may be in separate forms or integrated as shown in FIG. .
一体化された構造の例を第6図に示すが、多孔性の円筒
34の両端に適当な間隔をおいて、流体搦み室6と流体
加撚素子11とを配置したもので、これら各部には糸通
しに便利なように嵌合自在にするために接合部35.3
6を製作するのがよい。An example of an integrated structure is shown in FIG. 6, in which a fluid twisting chamber 6 and a fluid twisting element 11 are arranged at appropriate intervals at both ends of a porous cylinder 34. There is a joint part 35.3 in order to make it fit freely for convenient threading.
It is better to make 6.
この装置で重要なことは、流体搦み室6と流体加撚素子
11からの排出流体が双方の機能を妨げないようにする
ことで、そのためには多孔性の円筒34が充分な開孔面
積をもち、特に流体加撚素子11の糸通路31の始端3
7の形状を上に末広がり状として多孔性の円筒34の開
孔38からの排出を促進するとよい。What is important in this device is to ensure that the fluid discharged from the fluid twisting chamber 6 and the fluid twisting element 11 does not interfere with the functions of both, and for this purpose, the porous cylinder 34 has a sufficient opening area. In particular, the starting end 3 of the yarn passage 31 of the fluid twisting element 11
It is preferable that the shape of 7 is flared upward to facilitate discharge from the opening 38 of the porous cylinder 34.
又、多孔性の円筒34の内径は、芯糸8の周囲にルーズ
に搦糸2のループがまきついた形態の糸が回転しながら
走行するため、流体搦み室6の内径及び流体加撚素子1
1の糸通路径よりも大きくとる方がよい。In addition, the inner diameter of the porous cylinder 34 is determined by the inner diameter of the fluid twisting chamber 6 and the fluid twisting chamber 6, since the thread in which the loop of the thread 2 is loosely wound around the core thread 8 runs while rotating. Element 1
It is better to set the diameter to be larger than the diameter of the thread passage in step 1.
そして、多孔性の円筒34の長さとしては、特に制限は
ないが、10〜30R程度のものが通常の衣料用用途糸
の範囲には用いられ、開孔38も円形に限らず充分な排
出が行なわれるのであれば、他の形状でも例えば縦長の
又は横長のスリット等でもよい結果が得られる。There is no particular limit to the length of the porous cylinder 34, but a length of about 10 to 30R is commonly used for yarns used for clothing, and the openings 38 are not limited to circular shapes to ensure sufficient drainage. If this is done, other shapes such as vertically or horizontally long slits may also be used to achieve good results.
第6図には流体搦み室6と流体加撚素子11とが鉛直線
上に配置されているが、これに限定されず、糸通路の多
少の屈曲は許される。Although the fluid twisting chamber 6 and the fluid twisting element 11 are arranged on a vertical line in FIG. 6, the present invention is not limited to this, and some bending of the yarn path is allowed.
このように本発明は、ローラー以外の回転部を特にもた
ないため、従来の機械に取付けて本発明を適用し、付加
価値を高めることも容易であり、例えば延伸機などに設
置して、搦糸2として、未延伸糸又は半延伸糸と呼ばれ
る高配向未延伸糸を用いて延伸した後、直ちにあらかじ
め準備された芯糸8に絡合せしめるなど手軽に応用し得
る有用な発明である。As described above, since the present invention does not have any rotating parts other than rollers, it is easy to apply the present invention by attaching it to a conventional machine and increase added value. For example, by installing it in a drawing machine, This is a useful invention that can be easily applied, such as by using a highly oriented undrawn yarn called an undrawn yarn or semi-drawn yarn as the drawn yarn 2, and then immediately intertwining it with a core yarn 8 prepared in advance after drawing it.
実施例
第1図に示した製造装置を用いて、ポリエステルマルチ
フィラメント糸100D−24fを芯糸とし、約2 0
T/Mの原糸撚をもつポリエステルマルチフィラメン
ト糸50D−24fを搦糸として紡績糸風糸を加工した
。Example Using the manufacturing apparatus shown in FIG. 1, polyester multifilament yarn 100D-24f was used as the core yarn,
A spun yarn-like yarn was processed using polyester multifilament yarn 50D-24f with a T/M original yarn twist as a filament yarn.
その際、種々の仕様の異なる流体搦み室を用いた結果を
別表に示したが、共通条件として流体搦み室内径37H
IIlφ、高さ5履、芯糸導入孔長さ13 71!,芯
糸導入孔の内径1.27taφ、流体搦み室の上下面排
出孔面積比■、流体としては流体加撚素子とも共通して
高圧空気を用い、流体搦み室への噴入時圧力1wcIr
LG1流体加撚素子としては第5図に示す形式のものを
用い、使用空気圧”S’/crlt G,芯糸供給速度
8 2. 4 rn/yttin、搦糸供給速度5 0
0 mA一、芯糸オーバーフイード率+3%、捲取り
速度8 0 m/vtin、で加工した。At that time, the results using various fluid pumping chambers with different specifications are shown in the attached table, but the common condition is that the fluid pumping chamber diameter is 37H.
IIlφ, height 5 shoes, core thread introduction hole length 13 71! , The inner diameter of the core yarn introduction hole is 1.27taφ, the area ratio of the upper and lower discharge holes of the fluid straining chamber is ■, and the fluid used is high-pressure air, which is common to the fluid twisting element, and the pressure when injected into the fluid straining chamber is 1wcIr
As the LG1 fluid twisting element, one of the type shown in Fig. 5 was used, and the air pressure used was ``S'/crlt G, the core thread supply speed was 82.4 rn/yttin, and the core thread supply speed was 50.
Processing was carried out at 0 mA, a core yarn overfeed rate of +3%, and a winding speed of 80 m/vtin.
表中の操業性は、×(糸加工不可能)、△(不安定)、
○(安定)で評価し、得られた糸の糸斑は、ウースター
・イーブネステスター(スイス、ツエルベーガー社製B
型)で測定し、絡合性は2連式抱合力試験機(前田製機
社製)を使用して30ダ/本の荷重を吊した試料を10
本並列的に配列し、屈曲角度145゜で100回繰り返
し後の搦糸のほつれ状態より、下記の4ランクに分類し
た。The operability in the table is × (unable to process yarn), △ (unstable),
The thread unevenness of the obtained thread was evaluated as ○ (stable), and the unevenness of the obtained thread was evaluated using the Worcester Evenness Tester (B manufactured by Zellweger, Switzerland).
The entanglement property was measured using a double-type tethering force tester (manufactured by Maeda Seiki Co., Ltd.), and a sample suspended with a load of 30 da/piece was tested for 10
After arranging the threads in parallel and repeating them 100 times at a bending angle of 145°, the frayed threads were classified into the following four ranks.
表に見られる如く
サンプル番号2は、本発明の方法で搦糸噴入孔底部に約
10−の小室を設けたもので、得られた糸の糸斑、絡合
性共に小室をもたないサンプル番号1の例のものに比べ
て明らかに向上していることがわかる。As shown in the table, sample number 2 is a sample in which approximately 10 cells are provided at the bottom of the thread injection hole using the method of the present invention, and the resulting yarn has no cells in terms of yarn unevenness and entanglement. It can be seen that this is clearly improved compared to the example No. 1.
又、サンプル番号3,6,9.10は、小室の底面を多
孔面にした場合の開孔率の比較をしたもので、開孔率が
大きくなるに従い糸斑も絡合性も向上するが、開孔率2
7%をピークとして次第に低下し、45%を越えると操
業ができなくなることを示している。In addition, sample numbers 3, 6, and 9.10 compare the porosity when the bottom of the chamber is made porous. As the porosity increases, thread unevenness and entanglement improve, but Open area ratio 2
It shows that it gradually decreases after peaking at 7%, and when it exceeds 45%, it becomes impossible to operate.
すなわち底面を多孔面にすることは、本発明の効果を高
めるに有効であるが、適切な範囲に止めることが好まし
い。In other words, making the bottom surface porous is effective in enhancing the effects of the present invention, but it is preferable to keep it within an appropriate range.
サンプル番号3,4.5は、搦糸噴入孔軸心と流体搦み
室軸心との距離を変更した場合の比較であるが、搦糸噴
入孔軸心が流体搦み室内側面に一致した場合のサンプル
番号4は流体搦み室への開孔面積が非常に広く操業が困
難であった。Sample numbers 3 and 4.5 are compared when the distance between the axis of the thread injection hole and the axis of the fluid stirring chamber is changed, but the axis of the thread injection hole is on the side surface of the fluid stirring chamber. Sample No. 4, in which the results matched, had a very large opening area to the fluid stirring chamber and was difficult to operate.
しかし、搦糸噴入孔を流体搦み室の外側へ移行せしめる
に従って流体搦み室への開孔面積が小さくなり、小室の
機能が発揮されるようになる。However, as the thread injection hole is moved to the outside of the fluid damping chamber, the opening area to the fluid damping chamber becomes smaller, and the function of the small chamber is exerted.
又流体搦み室への搦糸噴入方向を芯糸の回転方向に一致
(順)せしめたサンプル番号7,8のものは、逆のサン
プル番号5,6のものに比べ糸斑は悪くなっているもの
、小室をもたないサンプル番号1に比べて絡合性は明ら
かに向上している。In addition, samples Nos. 7 and 8, in which the direction in which the threads were injected into the fluid stirring chamber matched (in order) with the direction of rotation of the core thread, had worse thread unevenness than those in Samples Nos. 5 and 6, which had the opposite direction. However, the entanglement property is clearly improved compared to sample number 1, which does not have cells.
又サンプル番号11.12は小室の容積を変更したもの
であるが、5ア15md程度であれば非常に好ましい糸
質を示した。Sample Nos. 11 and 12 were samples in which the volume of the small chamber was changed, but if the volume was about 5A and 15 md, it showed a very preferable thread quality.
第1図は、本発明を実施するための製造装置を示す斜視
図、第2図は第1図の■−■線に沿う流体搦み室の水平
断面図、第3図は他の例の水平断面図、第4図は第1図
のIV−IV線に沿う流体搦み室の縦断面図、第5図は
、第1図の■−■線に沿う流体加撚素子の縦断面図、第
6図は、流体搦み室と流体加撚素子を一体化したときの
縦断面図である。
2・・・・・・搦糸、5・・・・・・エジエクター、6
・・・・・・流体搦み室、8・・・・・・芯糸、11・
・・・・・流体加撚素子、14・・・・・・芯糸入口面
、15・・・・・・芯糸導入孔、16・・・・・・流体
排出孔、17・・・・・・糸条引出面、18・・・・・
・糸出口孔、19・・・・・・絡合糸、20・・・・・
・流体通路、21・・.・・・・搦糸導糸孔、22・・
・・・・搦糸噴入孔、26・・・・・・ガイド、27・
・・・・・小室、28・・・・・・糸通路、29・・・
・・・流体排出通路、30・・・・・・多孔面、31・
・・・・・糸通路、32・・・・・・流体噴入孔、33
・・・・・・絞り部、34・・・・・・多孔性の円筒、
35,36・・・・・・連結部、37・・・・・・流体
加撚素子の糸通路始端、38・・・・・・開孔。FIG. 1 is a perspective view showing a manufacturing apparatus for carrying out the present invention, FIG. 2 is a horizontal cross-sectional view of the fluid stirring chamber along the line ■-■ in FIG. 1, and FIG. 3 is a diagram showing another example. 4 is a vertical sectional view of the fluid twisting chamber along the line IV-IV in FIG. 1, and FIG. 5 is a vertical sectional view of the fluid twisting element along the line ■-■ in FIG. 1. , FIG. 6 is a longitudinal sectional view when the fluid twisting chamber and the fluid twisting element are integrated. 2... Ushiito, 5... Egictor, 6
...Fluid stirring chamber, 8... Core yarn, 11.
...Fluid twisting element, 14... Core thread inlet surface, 15... Core thread introduction hole, 16... Fluid discharge hole, 17... ... Yarn pull-out surface, 18...
- Thread exit hole, 19...Tangled thread, 20...
・Fluid passage, 21... ...Fine thread guide hole, 22...
・・・・Shiri injection hole, 26・・Guide, 27・
...Small room, 28...Thread passage, 29...
... Fluid discharge passage, 30 ... Porous surface, 31.
... Thread passage, 32 ... Fluid injection hole, 33
・・・・・・Aperture part, 34 ・・・Porous cylinder,
35, 36... Connecting portion, 37... Starting end of yarn passage of fluid twisting element, 38... Opening.
Claims (1)
軸心部を走行する芯糸に対して、実質的に無撚の連続マ
ルチフィラメント糸から成る搦糸を該流体搦み室内にそ
の糸通路の接線方向に該芯糸供給速度の3倍以上の速度
で流体と共に噴入し、搦糸噴入孔の底部の開孔率45%
以下0%以上の多孔面の底面を有する小室にて一時的に
滞留せしめた後、該芯糸に合流せしめ、絖いて前記流体
加撚素子を通過せしめ、芯糸を解撚することにより該芯
糸に搦糸を絡合せしめることを特徴とする紡績糸風糸の
製造方法。 2 その糸通路に対して接線方向に開孔された搦糸噴入
孔をもつ流体搦み室と流体加撚素子とが走行する芯糸の
進行方向にその糸通路を沿わせて順に配列させ該搦糸噴
入孔の底部は開孔率45%以下O%以上の多孔面の底面
を有する小室をなすことを特徴とする紡績糸風糸の製造
装置。[Scope of Claims] 1. The core yarn, which is twisted by a fluid twisting element and runs approximately at the axial center of the fluid twisting chamber, is made of a substantially untwisted continuous multifilament yarn. The fluid is injected into the fluid stirring chamber in the tangential direction of the yarn passage at a speed that is more than three times the core yarn supply speed, and the opening rate at the bottom of the yarn injection hole is 45%.
After temporarily staying in a small chamber having a bottom surface with a porous surface of 0% or more, the core yarn is merged with the core yarn, passed through the fluid twisting element, and the core yarn is untwisted. A method for producing spun yarn-like yarn, which is characterized by intertwining filaments with yarn. 2. A fluid twisting chamber having a thread injection hole opened tangentially to the thread passage and a fluid twisting element are arranged in order along the thread passage in the traveling direction of the running core thread. An apparatus for producing spun yarn-like yarn, characterized in that the bottom of the yarn injection hole forms a small chamber having a porous bottom surface with a porosity of 45% or less and 0% or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3865776A JPS597813B2 (en) | 1976-04-05 | 1976-04-05 | Method and device for producing spun yarn-like yarn |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3865776A JPS597813B2 (en) | 1976-04-05 | 1976-04-05 | Method and device for producing spun yarn-like yarn |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52121550A JPS52121550A (en) | 1977-10-13 |
| JPS597813B2 true JPS597813B2 (en) | 1984-02-21 |
Family
ID=12531319
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3865776A Expired JPS597813B2 (en) | 1976-04-05 | 1976-04-05 | Method and device for producing spun yarn-like yarn |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS597813B2 (en) |
-
1976
- 1976-04-05 JP JP3865776A patent/JPS597813B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52121550A (en) | 1977-10-13 |
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