JPH0681260A - Nozzle device for interlacing treatment - Google Patents
Nozzle device for interlacing treatmentInfo
- Publication number
- JPH0681260A JPH0681260A JP26070392A JP26070392A JPH0681260A JP H0681260 A JPH0681260 A JP H0681260A JP 26070392 A JP26070392 A JP 26070392A JP 26070392 A JP26070392 A JP 26070392A JP H0681260 A JPH0681260 A JP H0681260A
- Authority
- JP
- Japan
- Prior art keywords
- fluid
- row
- rows
- fluid injection
- nozzle device
- 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.)
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Links
Landscapes
- Nonwoven Fabrics (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は繊維ウエブに流体流、特
に水流を作用させて繊維同士を絡合させるノズル装置に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a nozzle device for entangling fibers by applying a fluid flow, particularly a water stream, to a fiber web.
【０００２】[0002]
【従来の技術】従来から繊維ウエブに高圧水流などの流
体流を作用させて繊維同士を絡合させ、繊維シートを得
る装置が知られているが、繊維ウエブをコンベアで移動
させながら流体流を作用させるため、コンベアの流れ方
向に流体流による縦筋が目立ち、外観上好ましい繊維シ
ートが得られなかった。2. Description of the Related Art Conventionally, a device for obtaining a fiber sheet by entanglement of fibers by applying a fluid flow such as a high-pressure water flow to a fiber web has been known. Because of the action, vertical streaks due to the fluid flow were conspicuous in the direction of flow of the conveyor, and a fiber sheet that was favorable in appearance could not be obtained.
【０００３】そのため、流体流を繊維ウエブの流れ方向
に対して直角方向に揺動させながら作用させたり、二列
以上の流体流を作用させるなど、様々な手段が講じられ
ているが、縦筋が十分に解消した繊維シートは得られて
いない。For this reason, various measures have been taken such as causing the fluid flow to act while oscillating in a direction perpendicular to the flow direction of the fibrous web, or allowing two or more rows of fluid flow to act. However, a fiber sheet that has been sufficiently solved is not obtained.
【０００４】[0004]
【発明が解決しようとする課題】本発明は上記の問題点
を解決するためになされたものであり、コンベアの流れ
方向における縦筋が目立たない繊維シートを得ることを
目的とする。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and an object of the present invention is to obtain a fiber sheet in which vertical streaks in the flow direction of the conveyor are not noticeable.
【０００５】[0005]
【課題を解決するための手段】本発明の絡合処理用ノズ
ル装置は、同一孔径の流体噴射孔列を複数配設し、かつ
隣り合う流体噴射孔列は孔径が異なっており、繊維ウエ
ブの流れ方向に対して重ならない位置にある。なお、前
列の後列に対する流体噴射孔径の比が０.７〜０.９の関
係を満たすか、１.１〜１.４の関係を満たす、隣り合う
流体噴射孔列を有すると、より縦筋の目立たない繊維シ
ートを得ることができる。In the nozzle device for entanglement treatment of the present invention, a plurality of rows of fluid ejecting holes having the same hole diameter are arranged, and adjacent rows of fluid ejecting holes have different hole diameters. It does not overlap with the flow direction. In addition, if the ratio of the diameter of the fluid ejection holes to the rear row of the front row satisfies the relationship of 0.7 to 0.9 or the relation of 1.1 to 1.4, the adjacent fluid injection hole rows have more vertical streaks. The inconspicuous fiber sheet can be obtained.
【０００６】[0006]
【作用】本発明の絡合処理用ノズル装置は、同一孔径の
流体噴射孔列を複数配設し、かつ隣り合う流体噴射孔列
は孔径が異なっており、繊維ウエブの流れ方向に対して
重ならない位置にある。そのため、前列の流体噴射孔列
の流体流では絡合処理できない部分についても、後列の
流体噴射孔列の流体流で絡合処理できるため、繊維ウエ
ブ全体に亘って絡合処理することができる。また、隣り
合う流体噴射孔列の孔径が異なっている、特に、前列の
後列に対する流体噴射孔径の比が０.７〜０.９の関係を
満たすか、１.１〜１.４の関係を満たす、隣り合う流体
噴射孔列を有すると、後列の流体噴射孔列から噴射され
た流体流は、前列の流体噴射孔列から噴射した流体流と
は、流体の幅、流体量、流体の位置、流体による衝撃な
どが異なるため、各々の流体噴射孔列から噴射される流
体流が繊維ウエブに作用するのに時間差があるにもかか
わらず、全体として縦筋の目立たない繊維シートを得る
ことを見出した。In the nozzle device for entanglement treatment of the present invention, a plurality of rows of fluid injection holes having the same hole diameter are arranged, and adjacent fluid injection hole rows have different hole diameters. It is in a position where it cannot be. Therefore, even a portion that cannot be entangled by the fluid flow of the fluid ejection hole array in the front row can be entangled by the fluid flow of the fluid injection hole array in the rear row, so that the entanglement processing can be performed over the entire fiber web. Further, the diameters of the adjacent fluid ejection hole rows are different, and in particular, the ratio of the fluid ejection hole diameter to the rear row of the front row satisfies the relationship of 0.7 to 0.9 or the relationship of 1.1 to 1.4. When there is a row of adjacent fluid ejection holes that fills, the fluid flow ejected from the fluid ejection hole row in the rear row is the same as the fluid flow ejected from the fluid ejection hole row in the front row. Since the impacts of the fluids are different, there is a difference in the time that the fluid flow ejected from each fluid ejection hole array acts on the fiber web, but it is possible to obtain a fiber sheet in which the vertical stripes are inconspicuous as a whole. I found it.
【０００７】以下、流体噴射孔列を２列有する絡合処理
ノズル装置の模式図である図１（ａ）、（ｂ）及び流体
噴射孔列を３列有する絡合処理ノズル装置の模式図であ
る図２（ａ）、（ｂ）を参照しながら、本発明の絡合処
理用ノズル装置について説明する。なお、図中の矢印は
繊維ウエブの流れ方向を表す。1 (a) and 1 (b) are schematic views of an entanglement processing nozzle device having two rows of fluid injection holes and a schematic view of an entanglement processing nozzle device having three rows of fluid injection holes. The entanglement processing nozzle device of the present invention will be described with reference to FIGS. 2 (a) and 2 (b). In addition, the arrow in a figure represents the flow direction of a fiber web.
【０００８】本発明の絡合処理用ノズル装置の流体噴射
孔列は繊維ウエブの流れ方向に対して直角に配列してい
ても良いし、直角ではなく斜めに配列していても良く、
特に限定するものではない。The array of fluid injection holes of the nozzle device for entanglement treatment of the present invention may be arranged at a right angle to the flow direction of the fiber web, or may be arranged obliquely instead of at a right angle.
It is not particularly limited.
【０００９】この絡合処理用ノズル装置の流体噴射孔列
は、図１（ａ）、（ｂ）のように２列の場合には、繊維
ウエブの流れ方向に対して、１列目の流体噴射孔列１の
間、好適には１列目の流体噴射孔同士の中間の位置、に
２列目の各流体噴射孔列２が重ならないように位置して
いるので、繊維ウエブ全体に亘って絡合処理を施すこと
ができる。また、図２（ａ）、（ｂ）のように３列の場
合には、１列目の流体噴射孔列１の間に２列目の流体噴
射孔列２が重ならないように位置し、更に、２列目の流
体噴射孔列２の間に３列目の流体噴射孔列３が重ならな
いように位置すれば良い。この場合、３列目の流体噴射
孔列３は１列目の流体噴射孔列１と重なる位置にあって
も良いが、縦筋が目立ちにくいように、重ならない位置
にあるのがより好ましい。なお、図示はしていないが、
孔が４列以上の場合についても上記と同様の関係が成り
立つの好ましい。In the case of two rows of fluid ejection holes of this entanglement treatment nozzle device as shown in FIGS. 1 (a) and 1 (b), the fluid in the first row with respect to the flow direction of the fibrous web. Since the fluid ejection hole arrays 2 of the second row do not overlap with each other, preferably at an intermediate position between the fluid ejection holes of the first row, between the ejection hole rows 1, the entire fibrous web is covered. Entanglement processing can be performed. In the case of three rows as shown in FIGS. 2A and 2B, the second fluid ejection hole row 2 is positioned so as not to overlap the first fluid ejection hole row 1, Furthermore, the third fluid ejection hole array 3 may be positioned so as not to overlap between the second fluid ejection hole array 2. In this case, the third fluid ejecting hole array 3 may be located at a position overlapping the first fluid ejecting hole array 1, but it is more preferred that the third fluid ejecting hole array 3 is not located so that the vertical stripes are not conspicuous. Although not shown,
It is preferable that the same relationship as above holds even in the case of four or more rows of holes.
【００１０】この同列における流体噴射孔のピッチは２
５孔／cmよりも短いと、隣接する流体流同士が干渉して
しまい、流体噴射孔のピッチが１０孔／cmよりも長い
と、縦筋がでやすく、しかも流体噴射孔列の列を多くす
る必要があるので、２５〜１０孔／cmが適当であり、よ
り好ましくは２０〜１５孔／cmである。The pitch of the fluid injection holes in this row is 2
If it is shorter than 5 holes / cm, adjacent fluid streams will interfere with each other, and if the pitch of the fluid injection holes is longer than 10 holes / cm, vertical streaks will appear easily, and more rows of fluid injection holes will be provided. 25 to 10 holes / cm is suitable, and more preferably 20 to 15 holes / cm.
【００１１】また、同列における流体噴射孔の孔径は、
同列における流体流による絡合作用が同じように作用す
るように、同一孔径をもつように設計される。なお、流
体噴射孔の孔径が０.０５mmよりも小さいと、噴射され
る流体流のエネルギーが小さいため、交絡処理が効率的
に行なえず、他方、０.２mmよりも大きいと、繊維同士
が絡み難いので、０.０５〜０.２mmが適当であり、より
好ましくは、０.０８〜０.１５mmである。The diameter of the fluid injection holes in the same row is
It is designed to have the same hole diameter so that the entanglement action by the fluid flow in the same row acts in the same way. If the diameter of the fluid injection hole is smaller than 0.05 mm, the energy of the injected fluid flow will be small, and the confounding process cannot be performed efficiently. On the other hand, if it is larger than 0.2 mm, the fibers will become entangled. Since it is difficult, 0.05 to 0.2 mm is suitable, and more preferably 0.08 to 0.15 mm.
【００１２】更に、隣り合う流体噴射孔列の孔径は同一
ではなく異なっているため、流体流の幅、流体量、流体
の位置、流体による衝撃など、状態の異なる流体流が各
列で得られるため、縦筋の目立たない繊維シートを得る
ことが可能となった。特に、図１（ａ）、（ｂ）のよう
に２列の場合には、１列目の流体噴射孔径（ｄ1）の２
列目の流体噴射孔径（ｄ2）に対する比（ｄ1／ｄ2）が
０.７〜０.９であるか、１.１〜１.４であると顕著な効
果が得られる。この流体噴射孔径比（ｄ1／ｄ2）が０.
７未満であると、２列目の流体流による縦筋が目立ち、
１.４を越えると１列目の流体流による縦筋が目立ち、
更に、０.９〜１.１であると、流体流による縦筋が目立
つためである。なお、この流体噴射孔径比（ｄ1／ｄ2）
が０.７〜０.９の場合と１.１〜１.４の場合があるの
は、絡合処理する繊維ウエブによって、１列目の流体流
が２列目の流体流よりも弱い方が好ましい場合と、１列
目の流体流が２列目の流体流よりも強い方が好ましい場
合があるためである。前者の場合は繊維ウエブが絡合し
ていないか、絡合の度合いが低い場合であり、１列目の
流体流を２列目の流体流よりも強く作用させると、絡合
作用が強すぎて、縦筋やむらができやすいためであり、
後者の場合は、繊維ウエブの絡合の度合いが高い場合で
あり、２列目の流体流を１列目の流体流よりも強く作用
させると、縦筋が目立ちやすくなるためである。Further, since the diameters of the adjacent fluid ejection hole rows are not the same but different, fluid streams having different states such as the width of the fluid flow, the amount of fluid, the position of the fluid, and the impact due to the fluid can be obtained in each row. Therefore, it becomes possible to obtain a fiber sheet in which vertical streaks are inconspicuous. Particularly, in the case of two rows as shown in FIGS. 1A and 1B, the fluid injection hole diameter (d 1 ) of the first row is 2
A remarkable effect can be obtained when the ratio (d 1 / d 2 ) to the fluid ejection hole diameter (d 2 ) in the row is 0.7 to 0.9 or 1.1 to 1.4. This fluid injection hole diameter ratio (d 1 / d 2 ) is 0.
If it is less than 7, vertical streaks due to the fluid flow in the second row are conspicuous,
When it exceeds 1.4, the vertical streaks due to the fluid flow in the first row are conspicuous,
Further, if it is 0.9 to 1.1, the vertical streaks due to the fluid flow are conspicuous. This fluid injection hole diameter ratio (d 1 / d 2 )
Is 0.7 to 0.9 and 1.1 to 1.4 in some cases because the fluid flow in the first row is weaker than the fluid flow in the second row due to the fiber web to be entangled. Is preferable, and it may be preferable that the fluid flow in the first row is stronger than the fluid flow in the second row. In the former case, the fibrous webs are not entangled or the degree of entanglement is low, and if the fluid flow in the first row is made stronger than the fluid flow in the second row, the entanglement action is too strong. Because it is easy for vertical streaks and unevenness,
In the latter case, the degree of entanglement of the fibrous web is high, and if the fluid flow in the second row is made to act more strongly than the fluid flow in the first row, the vertical streaks are easily noticeable.
【００１３】図２（ａ）、（ｂ）に示すような流体噴射
孔列の配列が３列の場合も同様に、１列目の流体噴射孔
径（ｄ1）の２列目の流体噴射孔径（ｄ2）に対する比
（ｄ1／ｄ2）が０.７〜０.９或いは１.１〜１.４であ
り、２列目の流体噴射孔径（ｄ2）の３列目の流体噴射
孔径（ｄ3）に対する比（ｄ2／ｄ3）が０.７〜０.９或
いは１.１〜１.４であるのが好ましい。なお、１列目の
流体噴射孔径（ｄ1）の３列目の流体噴射孔径（ｄ3）に
対する比（ｄ1／ｄ3）が、上記の関係を満たす必要はな
い。なお、流体噴射孔列が４列以上の場合も上記と同様
の関係が成り立つと、同様の効果が得られる。In the case where there are three rows of fluid ejection hole arrays as shown in FIGS. 2A and 2B, similarly, the fluid ejection hole diameter of the second row of the fluid ejection hole diameter (d 1 ) of the first row is the same. (d 2) the ratio (d 1 / d 2) is 0.7 to 0.9 or 1.1 to 1.4, the third column of fluid jet in the second column of fluid ejection hole diameter (d 2) pore size ratio (d 3) (d 2 / d 3) is preferably a 0.7 to 0.9 or 1.1 to 1.4. The ratio for the three row of fluid ejection hole diameter of the first column of fluid ejection hole diameter (d 1) (d 3) (d 1 / d 3) need not satisfy the above relationship. Even when the number of rows of fluid ejection holes is four or more, the same effect can be obtained if the same relationship as above holds.
【００１４】また、流体噴射孔列の列間距離が０.５mm
未満であると、隣り合う流体流が干渉し、他方、２mmを
越えると前列と後列の流体流による絡合処理の時間差が
大きくなりすぎて縦筋が目立つため、０.５mm〜２mmで
あるのが好ましい。より好ましくは０.５〜１mmであ
る。なお、流体噴射孔列の列間距離とは、前列の流体噴
射孔の中心を通る直線と、後列の流体噴射孔の中心を通
る直線との距離である。Further, the distance between the fluid injection hole rows is 0.5 mm.
If it is less than 2, the adjacent fluid flows interfere with each other, while if it exceeds 2 mm, the time difference between the entanglement treatment by the fluid flows in the front row and the back row becomes too large and the vertical streaks stand out, so it is 0.5 mm to 2 mm. Is preferred. More preferably, it is 0.5 to 1 mm. The inter-row distance of the fluid ejection hole row is the distance between the straight line passing through the center of the fluid ejection hole in the front row and the straight line passing through the center of the fluid ejection hole in the rear row.
【００１５】以上のように複数の流体噴射孔列を配設し
た本発明の絡合処理用ノズル装置は、繊維ウエブに対し
て１回だけ作用させるのではなく、２回以上作用させて
も良い。この場合、１回目に処理する際の１列目の流体
噴射孔径を小さくして縦筋や皺が生じにくいようにし、
最終回の最終列の流体噴射孔径を小さくして縦筋や皺が
生じにくいようにするのがより好ましい。As described above, the entanglement treatment nozzle device of the present invention, in which a plurality of fluid injection hole arrays are arranged, may be applied to the fiber web not only once but twice or more. . In this case, the diameter of the fluid ejection holes in the first row at the time of the first treatment is reduced so that vertical streaks and wrinkles are less likely to occur,
It is more preferable to reduce the diameter of the fluid injection hole in the last row of the last time so that vertical streaks and wrinkles are less likely to occur.
【００１６】以下に、本発明の絡合処理用ノズル装置の
実施例を示すが、本発明はこれらの実施例に限定される
ものではない。Examples of the entanglement treatment nozzle device of the present invention are shown below, but the present invention is not limited to these examples.
【００１７】[0017]
（実施例１）繊度１.５デニール、繊維長５１mmのポリ
エステル繊維をカーディングして得た目付６０g/m2の繊
維ウエブを、下記のような繊維ウエブの流れ方向に対し
て直角に２列の流体噴射孔列を配設したノズル装置から
水を噴射させて、繊維同士が絡合した不織布を得た。こ
の不織布は水流による縦筋の目立たず、表面状態も均一
であった。(Example 1) A fiber web having a basis weight of 60 g / m 2 obtained by carding polyester fiber having a fineness of 1.5 denier and a fiber length of 51 mm was provided in two rows at right angles to the following flow direction of the fiber web. Water was jetted from the nozzle device provided with the row of fluid jet holes to obtain a nonwoven fabric in which the fibers were entangled with each other. This non-woven fabric had no vertical streaks due to water flow and had a uniform surface condition.
【００１８】記 各列の流体噴射孔のピッチ：１４孔／cm（２列目の流体
噴射孔は１列目の流体噴射孔の中点） 流体噴射孔列の列間距離：０.７mm １列目の流体噴射孔径（ｄ1）：０.１５mm ２列目の流体噴射孔径（ｄ2）：０.１３mm 流体噴射孔径比（ｄ1／ｄ2）：１.１５ 水流の吐出圧力：１００barNote: The pitch of the fluid ejection holes in each row: 14 holes / cm (the fluid ejection holes in the second row are the midpoints of the fluid ejection holes in the first row) Distance between the fluid ejection hole rows: 0.7 mm 1 th column of fluid ejection hole diameter (d 1): 0.15mm 2 row of the fluid ejection hole diameter (d 2): 0.13mm fluid injecting hole diameter ratio (d 1 / d 2): 1.15 flow of discharge pressure: 100 bar
【００１９】（実施例２）２列目の流体噴射孔径
（ｄ2）を０.１１mmとし、流体噴射孔径比（ｄ1／ｄ2）
を１.３６としたこと以外は、実施例１と全く同様にし
て、繊維同士が絡合した不織布を得た。この不織布は水
流による縦筋の目立たず、表面状態も均一であった。[0019] (Example 2) the second column of fluid ejection hole diameter (d 2) of a 0.11 mm, the fluid injecting hole diameter ratio (d 1 / d 2)
A non-woven fabric in which fibers were entangled with each other was obtained in exactly the same manner as in Example 1 except that the ratio was 1.36. This non-woven fabric had no vertical streaks due to water flow and had a uniform surface condition.
【００２０】（実施例３）１列目の流体噴射孔径
（ｄ1）を０.１３mm、２列目の流体噴射孔径（ｄ2）を
０.１５mmとし、流体噴射孔径比（ｄ1／ｄ2）を０.８７
としたこと以外は、実施例１と全く同様にして、繊維同
士が絡合した不織布を得た。この不織布は水流による縦
筋の目立たず、表面状態も均一であった。[0020] (Example 3) the first column of fluid ejection hole diameter (d 1) of 0.13 mm, 2 column of fluid ejection hole diameter of (d 2) and 0.15 mm, the fluid injecting hole diameter ratio (d 1 / d 2 ) to 0.87
A non-woven fabric in which fibers were entangled with each other was obtained in the same manner as in Example 1 except that the above was adopted. This non-woven fabric had no vertical streaks due to water flow and had a uniform surface condition.
【００２１】（比較例）２列目の流体噴射孔径（ｄ2）
を０.１５mmとし、流体噴射孔径比（ｄ1／ｄ2）を１と
したこと以外は、実施例１と全く同様にして、繊維同士
が絡合した不織布を得た。この不織布は水流による縦筋
が目立ち、表面状態も不均一であった。(Comparative Example) Fluid injection hole diameter (d 2 ) in the second row
Was 0.15 mm and the fluid ejection hole diameter ratio (d 1 / d 2 ) was 1, and a nonwoven fabric in which fibers were entangled with each other was obtained in the same manner as in Example 1. The non-woven fabric had conspicuous vertical streaks due to the water flow, and the surface condition was not uniform.
【００２２】[0022]
【発明の効果】本発明の絡合処理用ノズル装置は、同一
孔径の流体噴射孔列を複数配設しており、しかも繊維ウ
エブの流れ方向に対して重ならない位置にあるため、前
列の流体噴射孔列の流体流では絡合処理できない部分に
ついても、後列の流体噴射孔列の流体流で絡合処理でき
るため、繊維ウエブ全体に亘って絡合処理することがで
きる。In the nozzle device for entanglement treatment of the present invention, a plurality of fluid injection hole arrays having the same hole diameter are arranged, and moreover, they are located at positions where they do not overlap with the flow direction of the fibrous web. Even the portion that cannot be entangled by the fluid flow of the injection hole array can be entangled by the fluid flow of the fluid injection hole array in the rear row, so that the entanglement processing can be performed over the entire fiber web.
【００２３】また、隣り合う流体噴射孔列の孔径が異な
っている、特に、前列の後列に対する流体噴射孔径比が
０.７〜０.９関係を満たすか、１.１〜１.４の関係を満
たす場合、縦筋の目立たない繊維シートを得ることがで
きる。Further, the diameters of the adjacent fluid injection hole rows are different, and in particular, the fluid injection hole diameter ratio with respect to the rear row of the front row satisfies the relationship of 0.7 to 0.9, or the relationship of 1.1 to 1.4. When the above condition is satisfied, it is possible to obtain a fiber sheet in which vertical stripes are inconspicuous.
【図１】（ａ） 流体噴射孔列が２列の場合の配置を示
す図 （ｂ） 流体噴射孔列が２列の場合の配置を示す図FIG. 1A is a diagram showing an arrangement when there are two rows of fluid ejection holes. FIG. 1B is a diagram showing an arrangement when there are two rows of fluid ejection holes.
【図２】（ａ） 流体噴射孔列が３列の場合の配置を例
示する図 （ｂ） 流体噴射孔列が３列の場合の配置を例示する図FIG. 2A is a diagram illustrating an arrangement in the case of three rows of fluid injection holes. FIG. 2B is a diagram illustrating an arrangement in the case of three rows of fluid injection holes.
１ １列目の流体噴射孔列 ２ ２列目の流体噴射孔列 ３ ３列目の流体噴射孔列 1 1st row fluid ejection hole row 2 2nd row fluid ejection hole row 3 3rd row fluid ejection hole row
Claims (3)
士を絡合させるノズル装置において、同一孔径の流体噴
射孔列を複数配設し、かつ隣り合う流体噴射孔列は孔径
が異なっており、繊維ウエブの流れ方向に対して重なら
ない位置にあることを特徴とする絡合処理用ノズル装
置。1. A nozzle device for effecting a fluid flow on a fiber web to entangle fibers with each other, wherein a plurality of fluid injection hole arrays having the same hole diameter are arranged, and adjacent fluid injection hole arrays have different hole diameters. , A nozzle device for entanglement treatment, wherein the nozzle device is in a position where it does not overlap with the flow direction of the fiber web.
０.７〜０.９の関係を満たす、隣り合う流体噴射孔列を
有することを特徴とする請求項１記載の絡合処理用ノズ
ル装置。2. A nozzle for entanglement treatment according to claim 1, wherein adjacent nozzles for fluid injection are provided so that the ratio of the diameter of the fluid injection holes for the rear row of the front row satisfies the relationship of 0.7 to 0.9. apparatus.
１.１〜１.４の関係を満たす、隣り合う流体噴射孔列を
有することを特徴とする請求項１記載の絡合処理用ノズ
ル装置。3. A nozzle for entanglement treatment according to claim 1, wherein adjacent nozzles for fluid injection are provided so that the ratio of the diameter of the fluid injection holes to that of the rear row of the front row satisfies the relationship of 1.1 to 1.4. apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26070392A JP3142088B2 (en) | 1992-09-03 | 1992-09-03 | Nozzle device for entanglement processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26070392A JP3142088B2 (en) | 1992-09-03 | 1992-09-03 | Nozzle device for entanglement processing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0681260A true JPH0681260A (en) | 1994-03-22 |
| JP3142088B2 JP3142088B2 (en) | 2001-03-07 |
Family
ID=17351601
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26070392A Expired - Fee Related JP3142088B2 (en) | 1992-09-03 | 1992-09-03 | Nozzle device for entanglement processing |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3142088B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009531563A (en) * | 2006-03-28 | 2009-09-03 | ノース・キャロライナ・ステイト・ユニヴァーシティ | System and method for reducing jet streaks in hydroentangled fibers |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5093851B2 (en) * | 2008-09-08 | 2012-12-12 | ユニチカ株式会社 | Manufacturing method of spunlace nonwoven fabric |
-
1992
- 1992-09-03 JP JP26070392A patent/JP3142088B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009531563A (en) * | 2006-03-28 | 2009-09-03 | ノース・キャロライナ・ステイト・ユニヴァーシティ | System and method for reducing jet streaks in hydroentangled fibers |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3142088B2 (en) | 2001-03-07 |
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