JP2570512Y2 - Complex - Google Patents

Complex

Info

Publication number
JP2570512Y2
JP2570512Y2 JP6136192U JP6136192U JP2570512Y2 JP 2570512 Y2 JP2570512 Y2 JP 2570512Y2 JP 6136192 U JP6136192 U JP 6136192U JP 6136192 U JP6136192 U JP 6136192U JP 2570512 Y2 JP2570512 Y2 JP 2570512Y2
Authority
JP
Japan
Prior art keywords
air permeability
width direction
composite
present
porous membrane
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 - Fee Related
Application number
JP6136192U
Other languages
Japanese (ja)
Other versions
JPH0617929U (en
Inventor
尚也 山口
誉志浩 皆本
成芳 池上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kohjin Holdings Co Ltd
Original Assignee
Kohjin Holdings Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kohjin Holdings Co Ltd filed Critical Kohjin Holdings Co Ltd
Priority to JP6136192U priority Critical patent/JP2570512Y2/en
Publication of JPH0617929U publication Critical patent/JPH0617929U/en
Application granted granted Critical
Publication of JP2570512Y2 publication Critical patent/JP2570512Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本発明は、通気性複合体に関す
る。より詳しくは、例えば使い捨てカイロなどの様に通
気度の均一性が特に要求される用途に使用する幅方向の
通気度の均一な通気性複合体に関する。
The present invention relates to a breathable composite. More specifically, the present invention relates to a gas-permeable composite having uniform air permeability in the width direction used for applications requiring uniform air permeability such as disposable warmers.

【0002】[0002]

【従来の技術】通気性膜の複合化では、ポイントドライ
ラミ、部分融着の熱ラミ、通気部を設けた接着性シート
単独で、または接着層として接着する方法が行われてい
る。これらは、通常、全面を均一に接着する様に加工を
行っている。
2. Description of the Related Art In the composite formation of a gas permeable membrane, a method of bonding a point dry lamination, a heat lamination of partial fusion, an adhesive sheet provided with a ventilation portion alone, or an adhesive layer has been used. These are usually processed so as to uniformly bond the entire surface.

【0003】[0003]

【考案が解決しようとする問題点】しかし、特に低通気
性(通気度が5000sec/100cc以上)の一軸
延伸多孔質膜を用いて複合を行う場合、該多孔質膜は、
ネックインによりフィルム端部の開口状態が著しく悪化
し、この影響でフィルム幅方向に通気度の勾配ができや
すく、従来の方法で複合化すると、複合体の幅方向の位
置によって通気度が異なり、そのために使用する複合体
の部位によって製品の性能が異なるという問題を有して
いた。
However, when the composite is formed using a uniaxially stretched porous membrane having low air permeability (air permeability of 5000 sec / 100 cc or more), the porous membrane is
Due to the neck-in, the opening state of the film end is significantly deteriorated, and the gradient of the air permeability is easily generated in the film width direction due to this effect, and when the composite is formed by the conventional method, the air permeability differs depending on the position of the composite in the width direction, Therefore, there is a problem that the performance of the product differs depending on the part of the composite used.

【0004】[0004]

【問題点を解決するための手段】本考案者等は、上記問
題点を解決すべく鋭意検討を重ねた結果、複合化の際に
多孔質膜の幅方向の通気度状態に合わせた通気部を設け
る事によって、上記問題点が解決されることを見い出
し、本考案を完成するに至ったものである。即ち、本考
案は、幅方向に通気度が異なる多孔質膜(A)と、最大
通気度が(A)の最小通気度の10分の1以下である通
気性膜(B)を複合する際に、(A)及び(B)の幅方
向に、通気度を通気部面積で割ったものが一定になる様
に、通気部面積を変化させて複合を行った、幅方向に通
気均一性が良好な複合体を提供するものである。以下、
本考案を詳細に説明するが、ここで言う幅方向とは、複
合加工時の流れ方向及び厚み方向と直角の方向を指すも
のとする。
[Means for Solving the Problems] The present inventors have made intensive studies to solve the above problems, and as a result, have found that the ventilation portion adapted to the state of the air permeability in the width direction of the porous membrane at the time of compounding. It has been found that the above-mentioned problems can be solved by providing, and the present invention has been completed. In other words, the present invention combines a porous membrane (A) having different air permeability in the width direction with a gas permeable membrane (B) having a maximum air permeability of one-tenth or less of a minimum air permeability of (A). In addition, in the width direction of (A) and (B), compounding was performed by changing the area of the ventilation section so that the value obtained by dividing the air permeability by the area of the ventilation section was constant. This provides a good composite. Less than,
Although the present invention will be described in detail, the width direction referred to here refers to a direction perpendicular to the flow direction and the thickness direction during compound machining.

【0005】本考案に用いられる幅方向に通気性が異な
る多孔質膜(A)とは、幅方向の通気度の分布曲線が任
意の流れ方向において同様の分布曲線を持つものであ
り、例としては、熱可塑性樹脂に微粒子を分散させたシ
ートを、一軸または二軸で延伸したものが挙げられる。
[0005] The porous membrane (A) having different permeability in the width direction used in the present invention is one in which the distribution curve of the permeability in the width direction has the same distribution curve in an arbitrary flow direction. Examples thereof include a sheet in which fine particles are dispersed in a thermoplastic resin, which is uniaxially or biaxially stretched.

【0006】本考案に用いられる通気性膜(B)とは、
最大通気度が(A)の最小通気度の10分の1以下であ
ればよく、例えば、紙、不織布、また、熱可塑性樹脂フ
ィルムに、穿孔を施した有孔フィルム等が挙げられる。
(B)にも、通気度のばらつきが当然存在し得るが、
(B)の最大通気度が(A)の最小通気度の10分の1
以下であれば、(B)の通気度のばらつきは、実質上問
題とはならない。
[0006] The breathable membrane (B) used in the present invention is:
The maximum air permeability may be one-tenth or less of the minimum air permeability of (A), and examples thereof include paper, nonwoven fabric, and a perforated film obtained by perforating a thermoplastic resin film.
(B) naturally also has a variation in air permeability,
The maximum air permeability of (B) is 1/10 of the minimum air permeability of (A)
If it is below, the variation of the air permeability of (B) does not substantially cause a problem.

【0007】本考案における複合化方法は、(A)と
(B)を必要な機能に応じた接着力で複合でき、且つ複
合体の通気部面積を幅方向に変化させ得る方法であれば
よく、例としては、ポイントドライラミネーション、通
気性接着シートを使用した熱ラミネーション、多孔質膜
および通気性膜を部分融着した熱ラミネーションが挙げ
られる。通気部面積を変化させる方法としては、ポイン
トドライラミネーションの場合は、接着剤塗工部の面
積、通気性接着シートを使用する場合は、該シートの通
気部の設け方、部分融着の場合には、融着する面積比を
必要に応じて幅方向に変化させればよい。
The composite method according to the present invention may be any method as long as (A) and (B) can be combined with an adhesive force according to the required function and the area of the ventilation portion of the composite can be changed in the width direction. Examples thereof include point dry lamination, thermal lamination using a permeable adhesive sheet, and thermal lamination in which a porous film and a permeable film are partially fused. As a method of changing the area of the ventilation section, in the case of point dry lamination, the area of the adhesive application section, when using a breathable adhesive sheet, how to provide the ventilation section of the sheet, in the case of partial fusion May be changed in the width direction as necessary.

【0008】[0008]

【考案の作用】本考案における複合体では、複合化する
ことによって(A)の持つ幅方向の通気度のばらつきを
減少させ、幅方向に均一性良好な通気度を得る事がで
き、その結果この複合体のどの部分を使用した製品も通
気度に関わる性能が均一性良好となる。
In the composite of the present invention, the variation in the air permeability in the width direction of (A) can be reduced by compounding, and a uniform air permeability with good uniformity in the width direction can be obtained. Products using any part of this composite have good uniformity in performance related to air permeability.

【0009】[0009]

【実施例】以下、本考案を実施例に基づき詳細に説明す
るが、本考案はこれに限定されるものではない。尚、本
実施例における試験方法は以下の方法によった。 1 通気度 JIS−P8117(ガーレ通気度;64
5.16mm2 の面積を100mlの空気が通過するの
に要する秒数 単位:sec/100cc)。 2 最大孔径 光学顕微鏡観察により測定。 3 平均乾燥塗布量 接着剤塗布後の膜を80℃の熱風
で30秒間乾燥した重量(i)と、溶剤で接着剤を溶解
除去後、同じ温度、時間で乾燥した重量(ii)、さら
にサンプルの面積(iii)から式1を使って求めた。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail based on embodiments, but the present invention is not limited thereto. In addition, the test method in this example was based on the following method. 1 air permeability JIS-P8117 (Gurley air permeability; 64
The number of seconds required for 100 ml of air to pass through an area of 5.16 mm 2 (unit: sec / 100 cc). 2 Maximum pore size Measured by optical microscope observation. 3 Average dry coating weight The weight (i) of drying the film after applying the adhesive with hot air of 80 ° C. for 30 seconds, the weight (ii) of dissolving and removing the adhesive with a solvent and drying at the same temperature and time, and a sample. From the area (iii) of Equation (1).

【0010】[0010]

【式1】 (平均乾燥塗布量)=((i)−(ii))/(iii)[Formula 1] (Average dry coating amount) = ((i)-(ii)) / (iii)

【0011】実施例1 a)多孔質膜(A) 最小通気度が8000sec/1
00ccで表1および図1に示す様な幅方向の通気度勾
配を持ち、最大孔径5μのL−LDPEを主成分とした
厚みが50μmの多孔質一軸延伸フィルム。 b)通気性膜(B) 最大通気度が2sec/100c
c、坪量が40g/m2 である、ナイロン不織布。 上記(A)(B)を用い、図5の様な斜め格子の図柄
で、円形部を塗工部分として、この図柄の円形部の中心
距離を縦横とも4mm一定とし、この円形部分の大きさ
のみを図5の4〜4’の様に中心部の半径を1.1mm
から幅方向に除々に小さくすることによって表2および
図2に示したような開口率(非塗工部面積率)としたグ
ラビアロールを用いて、(A)を塗工側として通常のポ
リエステル系接着剤を使用してドライラミネーションに
より図4の様に複合化した。この時の中央部での接着剤
の平均乾燥塗布量は3.0g/m2 であった。複合体の
通気度を表1および図3に示した。
Example 1 a) Porous membrane (A) Minimum air permeability is 8000 sec / 1
A porous uniaxially stretched film having an air permeability gradient in the width direction at 00 cc as shown in Table 1 and FIG. 1 and comprising L-LDPE having a maximum pore diameter of 5 μm as a main component and a thickness of 50 μm. b) Air permeable membrane (B) Maximum air permeability is 2 sec / 100c
c, Nylon nonwoven fabric having a basis weight of 40 g / m 2 . Using the above (A) and (B), with a pattern of an oblique lattice as shown in FIG. 5, a circular portion is a coating portion, and the center distance of the circular portion of this pattern is constant at 4 mm both vertically and horizontally, and the size of the circular portion Only the center radius is 1.1 mm as in 4 to 4 'in FIG.
By using a gravure roll having an opening ratio (area ratio of non-coated portion) as shown in Table 2 and FIG. The composite was formed by dry lamination using an adhesive as shown in FIG. At this time, the average dry coating amount of the adhesive at the center was 3.0 g / m 2 . The air permeability of the composite is shown in Table 1 and FIG.

【0012】[0012]

【図1】FIG.

【0013】[0013]

【図2】FIG. 2

【0014】[0014]

【図3】FIG. 3

【0015】[0015]

【図4】FIG. 4

【0016】[0016]

【図5】FIG. 5

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【表2】 [Table 2]

【0019】比較例1 多孔質膜(A)、通気性膜
(B)ともに実施例1と同じものを用いて、塗工部面積
率、図柄を実施例1で使用したグラビアロールの中央部
と同じとし、幅方向にも一定としたグラビアロールを用
いて実施例1と同様にドライラミネーションを行ない複
合化した。複合体の通気度を表1および図3に示した。
Comparative Example 1 The same porous film (A) and air permeable film (B) as in Example 1 were used, and the area ratio of the coated part and the design were the same as those of the gravure roll used in Example 1. Dry lamination was carried out in the same manner as in Example 1 by using a gravure roll having a constant width direction, to form a composite. The air permeability of the composite is shown in Table 1 and FIG.

【0020】[0020]

【考案の効果】上記の実施例で明かな通り、本考案にお
ける様に幅方向に異なる通気度を有する多孔質膜(A)
を比較例1に示したような従来の方法により、複合化し
た場合では、幅方向の通気度の相違は、複合体にもその
まま残るが、実施例1の様に(A)の幅方向の通気度の
相違に見合う様に、通気部面積を調整して複合化する
と、複合体としての幅方向の通気度の相違を、多孔質膜
に比べ2分の1以下と著しく減少させる事が出来る。
As is clear from the above embodiment, the porous membrane (A) having different air permeability in the width direction as in the present invention.
In the case of compounding by the conventional method as shown in Comparative Example 1, the difference in air permeability in the width direction remains in the composite as it is, but as in Example 1, the difference in air permeability in the width direction of (A) When the composite is formed by adjusting the area of the ventilation portion to match the difference in the air permeability, the difference in the air permeability in the width direction of the composite can be significantly reduced to one half or less of the porous membrane. .

【図面の簡単な説明】[Brief description of the drawings]

【図1】本考案の実施例1及び比較例1に用いた多孔質
膜(A)の幅方向の通気度分布を表したグラフである。
FIG. 1 is a graph showing the air permeability distribution in the width direction of a porous membrane (A) used in Example 1 and Comparative Example 1 of the present invention.

【図2】本考案の実施例1で用いたグラビアロールの開
口部(非塗工部)の面積率をロール幅方向に示したグラ
フである。
FIG. 2 is a graph showing an area ratio of an opening (uncoated portion) of the gravure roll used in Example 1 of the present invention in a roll width direction.

【図3】本考案の実施例1及び比較例1にで作製した複
合体の幅方向の通気度分布を表したグラフである。
FIG. 3 is a graph showing the air permeability distribution in the width direction of the composites produced in Example 1 and Comparative Example 1 of the present invention.

【図4】複合体の構成例を示す図である。FIG. 4 is a diagram showing a configuration example of a complex.

【図5】本考案の接着剤塗工部のパターンの一例を示す
図である。
FIG. 5 is a view showing an example of a pattern of an adhesive application section of the present invention.

【符号の説明】[Explanation of symbols]

1 通気性膜(B) 2 接着剤塗工部 3 多孔質膜(A) 4、4’ 接着剤塗工部(または、場合により開口部) DESCRIPTION OF SYMBOLS 1 Breathable membrane (B) 2 Adhesive coating part 3 Porous membrane (A) 4, 4 'Adhesive coating part (or opening part depending on the case)

Claims (2)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 幅方向に通気度が異なる多孔質膜(A)
と、最大通気度が(A)の最小通気度の10分の1以下
である通気性膜(B)を複合する際に、(A)及び
(B)の幅方向に通気部面積を変化させて複合を行っ
た、幅方向に通気均一性が良好な複合体。
1. A porous membrane (A) having different air permeability in the width direction.
When the air permeable membrane (B) whose maximum air permeability is 1/10 or less of the minimum air permeability of (A) is combined, the area of the air permeable portion is changed in the width direction of (A) and (B). Composite with good uniform ventilation in the width direction.
【請求項2】 (A)の多孔質膜が、一軸延伸されたフ
ィルムまたはシートである請求項1記載の複合体。
2. The composite according to claim 1, wherein the porous membrane (A) is a uniaxially stretched film or sheet.
JP6136192U 1992-08-10 1992-08-10 Complex Expired - Fee Related JP2570512Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6136192U JP2570512Y2 (en) 1992-08-10 1992-08-10 Complex

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6136192U JP2570512Y2 (en) 1992-08-10 1992-08-10 Complex

Publications (2)

Publication Number Publication Date
JPH0617929U JPH0617929U (en) 1994-03-08
JP2570512Y2 true JP2570512Y2 (en) 1998-05-06

Family

ID=13168953

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6136192U Expired - Fee Related JP2570512Y2 (en) 1992-08-10 1992-08-10 Complex

Country Status (1)

Country Link
JP (1) JP2570512Y2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5925406A (en) * 1997-07-18 1999-07-20 The Procter & Gamble Co. Method of making a gas permeable material
KR101461397B1 (en) * 2012-10-23 2014-11-20 권용도 Tool exchange method using a vertical machining center and the device horizontal rotation of the tool magazine
KR101461399B1 (en) * 2012-11-20 2014-11-20 권용도 Linear flow that the grip of the bar column flow vertically sliding top and bottom plates with vertical machining centers, and the device exchange method using tools

Also Published As

Publication number Publication date
JPH0617929U (en) 1994-03-08

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