JPS58203770A - Mask - Google Patents

Mask

Info

Publication number
JPS58203770A
JPS58203770A JP57087199A JP8719982A JPS58203770A JP S58203770 A JPS58203770 A JP S58203770A JP 57087199 A JP57087199 A JP 57087199A JP 8719982 A JP8719982 A JP 8719982A JP S58203770 A JPS58203770 A JP S58203770A
Authority
JP
Japan
Prior art keywords
mask
organic
wet
weight
fibrils
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.)
Pending
Application number
JP57087199A
Other languages
Japanese (ja)
Inventor
誠 吉田
董 平川
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP57087199A priority Critical patent/JPS58203770A/en
Publication of JPS58203770A publication Critical patent/JPS58203770A/en
Pending legal-status Critical Current

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  • Respiratory Apparatuses And Protective Means (AREA)
  • Paper (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は高性能マスクに関し、さらにくわし少ない、着
用性のすぐれた高性能マスクに関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a high-performance mask, and more particularly, to a high-performance mask that is easy to wear and requires little wear.

従来、病院の手術室・待合室、医薬、生物学研究室、製
薬工場のように人間の呼気中に含まれている病源菌、雑
菌によって雰囲気が汚染されるのを防止することを必要
とする分野や微粉体内に入るのを防止する必要のある分
野では、質例えばガラスマイクロクールで構成され九不
織布状シートを有機繊維不織布で被覆したマスりが用い
られている。
Traditionally, fields such as hospital operating rooms and waiting rooms, pharmaceutical and biological laboratories, and pharmaceutical factories require prevention of atmospheric contamination by pathogenic bacteria and germs contained in human breath. In fields where it is necessary to prevent particles from entering fine particles, a mass made of a material such as glass microcool and covered with an organic fiber nonwoven fabric is used.

しかしながら、かかるマスクは柔軟性が非常に乏しい剛
直なガラス繊・維で構成されるために、着用中破壊しや
すく、それにより崩壊マイクロウールが飛散して、更に
は呼吸によって人体に入り、人間の健康を害する危険性
が大きいのではないかということが危惧されている。又
、かかるマスクは麺への装着性を上げるため、ひだ加工
、成型加工が施こされているが、同様な理由から加工、
が難しく、加工上のトラブルも多いつまた、マスク全体
のドレープ性が悪いために装着性が悪く着用感の劣った
ものとなる。
However, since such masks are composed of rigid glass fibers with very little flexibility, they tend to break while being worn, causing the disintegrated microwool to scatter and even enter the human body through breathing. There are concerns that there is a great risk of harm to health. In addition, such masks are pleated and molded to improve the ease of attachment to the noodles, but for the same reason, processing,
It is difficult to make the mask, and there are many processing problems.Furthermore, the drape of the entire mask is poor, resulting in poor wearability and poor wearing comfort.

その上、これらガラスマイクロウ−k tri if 
ラスマイクロウール化するために大量のエネルギーを必
要とし、また峨喉径が非常に太いものから細いものまで
含まれるため、分別を必要とするが、十分満足できる種
変に分別するには極めて高度の技術を必要とし、また、
該マイクロウール表面が平滑であるために単独ではシー
ト状に抄造することが雅しく、ガラスマイクロウール表
面の粗面化、抄造液のPH調整、バインダの添加等が必
要とされ製造コストが著しく高くなる。
Moreover, these glass micro-
It requires a large amount of energy to turn into lath microwool, and since the diameter of the wool varies from very thick to very thin, it requires separation, but it takes extremely high level of precision to separate it into satisfactory species. technology, and
Because the surface of the micro wool is smooth, it is easy to make it into a sheet by itself, but it requires roughening the surface of the glass micro wool, adjusting the pH of the paper making solution, adding a binder, etc., and the manufacturing cost is extremely high. Become.

本発明者らは、かかる従来のマスクの欠点を解消し、抄
紙適性にすぐれ、微粉塵、細菌の捕集性能にすぐれ、信
頼性の高い、人体に影響の非常に少ない着用性のすぐ扛
た高性能マスクに関し鋭意検討の結果、本発明に到達し
たものである。
The present inventors have solved the drawbacks of such conventional masks, and have developed an easy-to-wear mask that is suitable for paper making, has excellent ability to collect fine dust and bacteria, is highly reliable, and has very little effect on the human body. The present invention was arrived at as a result of extensive research into high-performance masks.

すなわち本発明は、平均繊維径が0.1〜3.0μmで
ある有機繊維径フィブリル5〜40重量%と平均繊維径
が3〜25μmである有機繊維95〜60重量%とを混
合し、湿式抄造した湿式不織布から成ることを特徴とす
るマスクである。
That is, the present invention mixes 5 to 40% by weight of organic fiber fibrils having an average fiber diameter of 0.1 to 3.0 μm and 95 to 60% by weight of organic fibers having an average fiber diameter of 3 to 25 μm, and wet-processes the mixture. This mask is made of a wet-processed nonwoven fabric.

本発明において使用する有機繊維状フィブリルの平均繊
維径は0.1〜3.0μmであることが必要であり、特
に0.3〜2.0μmであることが好ましい。平均繊維
径が太すぎると抄紙の際、湿紙がワイヤメツシュから剥
離しK<<なりiii 遣が難しく、微粉塵を捕集する
効果が低下してしまう。また平均繊維径が細すぎると抄
造の際ワイヤメツシュへの食い込みが著しく、ワイヤメ
ツシュからの剥離が著しく悪くなり、更には戸水度の低
下から生産性も低下するという問題と、マスクとしての
通気抵抗が著しく高くなり、着用時に呼吸がしにくくな
るという問題が生ずる。
The average fiber diameter of the organic fibrous fibrils used in the present invention is required to be 0.1 to 3.0 μm, and particularly preferably 0.3 to 2.0 μm. If the average fiber diameter is too thick, the wet paper will peel off from the wire mesh during paper making, making it difficult to separate the wet paper from the wire mesh and reducing the effectiveness of collecting fine dust. In addition, if the average fiber diameter is too small, there will be a problem that the fibers will dig into the wire mesh during paper making, and peeling from the wire mesh will be extremely difficult.Furthermore, productivity will decrease due to a decrease in water level, and ventilation resistance as a mask will be significant. This causes the problem that it becomes difficult to breathe when worn.

−万、有機繊維の平均繊維径は3〜25μmとすること
が必要で、特に微粉塵等の捕集効率、湿式抄造のしやす
さから4.5〜20μmであることが更に好ましい。ま
た、有機繊維の平均繊維径は1〜tsmであることが、
水中での分散性、得られた不織布の強力及び短職維に切
断するに要するコストの点で好ましく、2〜10111
1であることが艶に好ましい。有機繊維の断面形状は任
意であるが、断面の長径と短径の比(長径/短径)が1
〜2であるような断面の繊維、即ち丸断面、偏平断面の
繊維であることが微粉塵の濾過性能を高めるうえで更に
好ましい。
- It is necessary that the average fiber diameter of the organic fibers is 3 to 25 μm, and more preferably 4.5 to 20 μm from the viewpoint of efficiency in collecting fine dust and ease of wet papermaking. Further, the average fiber diameter of the organic fiber is 1 to tsm,
Preferable in terms of dispersibility in water, strength of the obtained nonwoven fabric, and cost required for cutting into short-length fibers, and 2 to 10111
1 is preferable for gloss. The cross-sectional shape of the organic fiber is arbitrary, but the ratio of the major axis to the minor axis (major axis/minor axis) of the cross section is 1.
It is more preferable to use fibers with a cross section of 2 to 2, that is, fibers with a round cross section or a flat cross section, in order to improve the filtration performance of fine dust.

本発明におけるマスクに用いる湿式不織布は有85に繊
維状ライブ11ルの混入率が5〜40重量%、好ましく
は15〜35重量%、また有pk偵雑の混入率が95〜
60重量%、好ましくは85〜65重量%であることが
必要であろう有機繊維径フィブリルの混入率が少なすぎ
ると、空気中の微粉塵等の捕集性能が著しく悪くなり、
一方混入率が大きすぎると通気抵抗が著しく高くなり、
マスクとして着用時の呼吸のしやすさを著しく阻害し、
また抄造時の斑が多く、炉水度が著しく小さくなるため
に生産性が低下するという問題が生じてくる。
The wet-laid nonwoven fabric used for the mask of the present invention has a mixing rate of 5 to 40% by weight, preferably 15 to 35% by weight of fibrous live 11, and a mixing rate of 95 to 95% by weight of fibrous live 11.
If the mixing ratio of organic fiber diameter fibrils, which should be 60% by weight, preferably 85 to 65% by weight, is too low, the performance of collecting fine dust etc. in the air will be significantly deteriorated.
On the other hand, if the mixing ratio is too large, the ventilation resistance will increase significantly.
It significantly impedes the ease of breathing when worn as a mask,
In addition, there are many spots during paper making, and the furnace water level becomes extremely low, resulting in a problem of reduced productivity.

本発明のマスクに用いる湿式不織布は目付が10〜10
0 r/i、特に30〜70f7’lであることが望ま
しく、このときの通気饗は5〜6゜cr、/cd/ s
ee 、好ましくは1 s 〜s o cr:、/cd
/secであることが望ましい。
The wet nonwoven fabric used for the mask of the present invention has a basis weight of 10 to 10.
0 r/i, especially 30 to 70 f7'l, and the ventilation hole at this time is 5 to 6° cr, /cd/s
ee, preferably 1 s to s o cr:, /cd
/sec is desirable.

目付が少なすぎると微粉塵等の捕集効率が低下し、更に
は抄造におけるワイヤからの剥離条件が厳しくなり、生
産でのトラブルが増大する。
If the basis weight is too low, the efficiency of collecting fine dust and the like will decrease, and furthermore, the conditions for peeling from the wire during papermaking will become stricter, increasing troubles in production.

また目付が大きすぎると空気の通気抵抗が著しく高くな
り、マスクとして使用したとき、呼吸がしにくくなり、
装着感も悪くなる。
Also, if the fabric weight is too large, the air ventilation resistance will be extremely high, making it difficult to breathe when used as a mask.
The feeling of wearing it also gets worse.

また、通気度は低すぎると空気中の微粉塵の捕集効率を
低下させ、高すぎるとマスク着用時の呼吸のしやすさを
阻害することになる。
Furthermore, if the air permeability is too low, it will reduce the efficiency of capturing fine dust in the air, and if it is too high, it will hinder the ease of breathing when wearing a mask.

本発明において、有機繊維状フィブリルは(1)  二
種以上の非相溶性合成高分子を混合し溶融押し出しくま
たは紡糸)し、切断後機械的な手段で繊維状フィブリル
化する方法(スプリット法:I!#公昭35−9651
号等)、(2)  合成高分子をその溶媒の沸点以上で
、かつ高圧側から低圧側へ爆発的に噴出させたのち叩解
し、繊維状フィブリル化する方法(フラッシュ紡糸法:
特公昭36−16460号等)、(3)  二種以上の
非相溶性合成高分子を混合し。
In the present invention, organic fibrous fibrils are prepared by (1) mixing two or more types of incompatible synthetic polymers, melt-extruding or spinning), cutting them and then forming them into fibrous fibrils by mechanical means (split method: I!# Kosho 35-9651
(2) A method in which a synthetic polymer is ejected explosively from a high pressure side to a low pressure side at a temperature higher than the boiling point of its solvent, and then beaten and turned into fibrous fibrils (flash spinning method:
(3) Mixing two or more types of incompatible synthetic polymers.

溶融押し出しくまたは紡糸)し、切断後溶剤浸漬して、
−万の高分子を溶剤し、繊維状フィブリル化する方法(
ポリマーブレンド溶解法:米国特許第3382305号
等ン、(4)  ポリエステル系高分子Kmポリエステ
ルに非相溶のアルカリ溶液可溶成分をブレンドし、アル
カリにより減量後叩解し、繊維状フィブリル化する方法
(アルカリ減量叩解法:特開昭56−315号等)、 などによって製造されるが、このうちアルカリ減量叩解
法によれば、抄紙適性、熱的安定性。
(melt extrusion or spinning), cut and soaked in solvent,
- A method of converting ten thousand polymers into fibrous fibrils using a solvent (
Polymer blend dissolution method: U.S. Patent No. 3,382,305, etc. (4) A method in which an incompatible alkali solution soluble component is blended with a polyester polymer Km polyester, the weight is reduced with an alkali, and then beaten to form a fibrous fibrillation ( Alkaline weight loss beating method: JP-A No. 56-315, etc.), etc.) However, according to the alkali weight loss beating method, papermaking suitability and thermal stability are improved.

微粉塵の捕集性能2強力等に優れた有機繊維状フィブリ
ルが得られるので特に好ましいアルカリ減量叩解法によ
って有機繊維状フィブリルを製造するには、線状芳香族
ポリエステルと該ポリエステルに相溶性がなく、アルカ
リ性溶液に可溶の有機化合物、例えば有機スルホン酸金
属塩、ポリアルキレングリコール等との混合物を溶融紡
糸、延伸し、得られた繊維を適当な繊維長に切断後、ア
ルカリ性溶液で処理し、次いで叩解してフィブリル化す
る方法が好適である。
Fine dust collection performance 2 In order to produce organic fibrous fibrils by the alkali weight loss beating method, which is particularly preferred because organic fibrous fibrils with excellent strength etc. can be obtained, linear aromatic polyester and the polyester are incompatible. , a mixture with an organic compound soluble in an alkaline solution, such as an organic sulfonic acid metal salt, polyalkylene glycol, etc., is melt-spun and drawn, the resulting fibers are cut into appropriate fiber lengths, and then treated with an alkaline solution; A method in which the material is then beaten and fibrillated is preferred.

かかる線状芳香族ポリエステルとしては、具体的にはポ
リエチレンテレフタレート、ポリエチレンテレフタレー
ト/イソフタ゛レート、ポリエチレンテレフタレート/
ヘキサヒドロテレフタレート、ポリエチレンテレ7タレ
ー)/S−(ナトリウムスルホ)イソフタレート、ポリ
(p−へキサヒドロギン。リレン・テレフタレート)、
ポリ(ジフェニロール・プロパンインフタレート)及び
ポリエチレンナフタレンジカルボキシレート類(%に2
,6および2,7異性体誘導体ならびにへ午丈メチレン
ビペンゾエト)等があるが、このうちでもテレフタル酸
、イノフタル酸、ナフタリンジカルボン酸、ジフェニル
ジカルボン酸など、二官能性芳香族カルボン酸を酸成分
とし、エチレングリコール、トリメチレングリコール、
テトラメチレングリコール。
Specifically, such linear aromatic polyesters include polyethylene terephthalate, polyethylene terephthalate/isophthalate, and polyethylene terephthalate/isophthalate.
Hexahydroterephthalate, polyethylene terephthalate)/S-(sodium sulfo)isophthalate, poly(p-hexahydrogine.rylene terephthalate),
Poly(diphenylol propane inphthalate) and polyethylene naphthalene dicarboxylate (2% in %)
, 6- and 2,7-isomer derivatives, and hematopoietic methylene bipenzoate), among which difunctional aromatic carboxylic acids such as terephthalic acid, inophthalic acid, naphthalene dicarboxylic acid, diphenyl dicarboxylic acid, etc. As acid components, ethylene glycol, trimethylene glycol,
Tetramethylene glycol.

ベキサメテレ/グリコールなどのグリコールをグリコー
ル成分とする線状芳香族ポリエステルが好ましく、とく
に一般式 〔nは2〜6の整数を示す。〕 で示される繰り返し単位を主たる構成成分とするポリエ
ステルが用いられる。その酸成分、グリコール成分の一
部をそれぞれ他の三官能カルボン酸、他のグリコール成
分で置きかえてもよいことは言うまでもない。これらの
ポリエステルは、所望ならばつや消し剤、増粘剤、顔料
等の添加剤を含んでいてもよい。
Linear aromatic polyesters containing glycol such as bexamethele/glycol as a glycol component are preferred, particularly those of the general formula [n represents an integer of 2 to 6]. ] A polyester whose main constituent is a repeating unit represented by the following is used. It goes without saying that part of the acid component and glycol component may be replaced with other trifunctional carboxylic acids and other glycol components, respectively. These polyesters may contain additives such as matting agents, thickeners, pigments, etc., if desired.

また、有機繊維としては任意の天然繊維、化学繊維9合
成繊維を用いることができるが、特にポリアミド繊維、
ポリエステル繊維、ボリグロピレン繊維等の熱可胆性合
成繊維が抄紙時における湿紙のワイヤーメツシュからの
剥離性を向上させ、シート状物の強力を高めるうえで好
ましく、なかでも有機繊維状フィブリルに用いたのと同
様゛の線状芳香族ポリエステルが最適である。
In addition, as the organic fiber, any natural fiber, chemical fiber9 or synthetic fiber can be used, but in particular, polyamide fiber,
Thermobile synthetic fibers such as polyester fibers and polyglopyrene fibers are preferred because they improve the peelability of wet paper from wire mesh during paper making and increase the strength of sheet materials, and are particularly useful for organic fibrous fibrils. A linear aromatic polyester similar to the one used above is most suitable.

本発明のマスクは前記有機繊維状フィブリルと前記有機
繊維を短く切断したものを所定の割合で混合し、湿式抄
紙法により抄造した湿式不織布からなるが、その抄紙特
性を高め、製品強力を高めるための湿潤紙力増強剤、乾
燥紙力増強剤、内添バインダ、繊維状バインダ、外添バ
イノダなどを使用することは好ましい実施態様である。
The mask of the present invention is made of a wet-laid nonwoven fabric made by mixing the organic fibrous fibrils and the organic fibers cut into short pieces at a predetermined ratio and using a wet paper-making method. It is a preferred embodiment to use a wet paper strength agent, a dry paper strength agent, an internally added binder, a fibrous binder, an externally added binder, etc.

この湿式不織布のみでマスクにしてもよいが、通常は快
適な着用感を与えるために湿式不織布の表面を肌ざわり
の良好な有機繊維織編物、不織布等の布帛で被覆して用
いられる。
Although this wet-laid nonwoven fabric alone may be used as a mask, the surface of the wet-laid nonwoven fabric is usually covered with a fabric such as organic fiber woven or knitted fabric or non-woven fabric that is comfortable to the touch in order to provide a comfortable wearing feeling.

この被覆布帛は有機繊維2主とするものであればいかな
るものでもよいが、できるだけ通気度の高い、通気度1
o o tx/cd/sec 以上のものが好ましい。
This covering fabric may be of any type as long as it is made mainly of organic fibers, but it may be made of a fabric with as high an air permeability as possible.
o o tx/cd/sec or more is preferred.

不織布を用いる場合の被覆法としては、抄き合わせ法、
被覆不織布への抄造、湿紙でのラミネート法、抄造転紙
でのラミネート法等をあげることができる。
Covering methods when using non-woven fabric include paper-combining method,
Examples include forming a coated nonwoven fabric, laminating with a wet paper, and laminating with a rolled paper.

本発明のマスクは、空気中の病原菌、雑菌。The mask of the present invention protects against pathogens and germs in the air.

微粉塵等の捕集性能にすぐれ、製造も容易で、しかも有
機物が主体であるために柔軟性をもつ:・ ていて加工性にすぐれ、人体に悪影響を及ぼすことがな
い着用性のすぐれたマスクである。このため、このマス
クは病院の手術室、待合室、微粉塵の発生する作業場、
クリーンルームの中で使用されるマスクに好適である。
It has excellent performance in capturing fine dust, etc., is easy to manufacture, and is flexible because it is mainly made of organic matter.・ A mask that is easy to wear and has excellent processability and does not have any adverse effects on the human body. It is. For this reason, this mask is suitable for use in hospital operating rooms, waiting rooms, and workplaces where fine dust is generated.
Suitable for masks used in clean rooms.

以下実施例により本発明を具体的に説明するが、本発明
は以下の実施例に限定されるものではない。
EXAMPLES The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to the following Examples.

なお、実施例におけるマスクの特性は下記の方法によっ
て測定したものである。
In addition, the characteristics of the mask in the examples were measured by the following method.

平均繊維径(μm);繊維状フィブリル、有機繊維を単
独で抄紙し、任意の位置を走査型電子顕微鏡で撮影しく
繊維状フィブリル倍率2000倍、有機繊維200倍)
、ランダムに抽出した繊維径を1枚当り10点、計IQ
Q点読み取り算術平均により求めた。
Average fiber diameter (μm): Paper is made from fibrous fibrils and organic fibers individually, and any position is photographed using a scanning electron microscope (magnification: 2000x for fibrous fibrils, 200x for organic fibers)
, 10 randomly extracted fiber diameters per sheet, total IQ
It was determined by the arithmetic mean of the Q-point readings.

目付(y/1ry) :  JIS  L−1079に
基づき測定した。
Fabric weight (y/1ry): Measured based on JIS L-1079.

通気度(CC/ffl/sec ) : J I8 L
−1079に基づきフラジール盟試験機を用いて測定し
たつ圧力損失ΔPC,Hg0):  濾過材に空気を線
速4 、75 cps/ sec で通気させた時の通
気抵抗を水柱マノメータにより求めた。
Air permeability (CC/ffl/sec): J I8 L
Pressure loss ΔPC, Hg0) measured using a Frazier tester based on 1079: The ventilation resistance when air was aerated through the filter material at a linear velocity of 4 and 75 cps/sec was determined using a water column manometer.

透過率η(Co10i ) ;  平均粒径0,3μm
のジオクチルフタレート(DOP)粒子を発生させ、線
速4.75 am/ secでシート状物を通過させ、
その前後での空気゛の一部を採取し、それぞれのDOP
粒子の個数濃度(Co、 Ci )をダン科学■fi4
100型マルチダストカウ/りにより測定し、次式によ
り算出しfc。
Transmittance η (Co10i); average particle size 0.3 μm
dioctyl phthalate (DOP) particles are generated and passed through a sheet at a linear velocity of 4.75 am/sec,
Sample some of the air before and after the DOP of each
The particle number concentration (Co, Ci) is calculated using Dan Science fi4
Measured using a 100-type multi-dust cowl and calculated using the following formula: fc.

・実施例 常法によって得られたポリエチレンテレ7りv−)(3
5℃Oo−クロロフェノール浴液で測定した極限粘度0
.65 )を295℃で溶融し、ギヤポンプで計1した
後285℃で加熱された混線スクリニーに供給し九〇一
方、炭素数8〜20で平均炭素数が14であるアルキル
スルホン酸ソーダ混合物を150℃でギヤポンプで計量
した後285℃に加温された前記混線スクリューに供給
した。アルキルスルホン酸ソーダのポリエチレンテレフ
タレートに対する混合率は4重量%である。混練スクリ
ューで混合したブレンドポリマーを押し出し成型してチ
ップ状の成型吻を得た。
・Example: Polyethylene Tele7 (v-) (3) obtained by a conventional method
5°C Oo - Intrinsic viscosity measured in chlorophenol bath solution 0
.. 65) was melted at 295°C, pumped with a gear pump, and then fed to a mixed wire screenie heated at 285°C. After metering with a gear pump at 150°C, it was supplied to the mixed screw heated to 285°C. The mixing ratio of sodium alkylsulfonate to polyethylene terephthalate was 4% by weight. A chip-shaped molded proboscis was obtained by extrusion molding the blended polymer mixed with a kneading screw.

この得られたチップを乾燥後環状スリットの一部が開口
した馬蹄形の開口部を持つノズルを有する口金を使用し
て吐出し、常法に従って溶融紡糸し、中空糸を得た。こ
れらの原糸を合糸。
After drying, the obtained chips were discharged using a nozzle having a horseshoe-shaped opening in which a part of an annular slit was opened, and melt-spun according to a conventional method to obtain hollow fibers. Combine these raw threads.

延伸、熱セットし、17万deのトウ(単+1[デニー
ル1.5)を得た。
It was stretched and heat set to obtain a tow of 170,000 de (denier +1 [denier 1.5)].

このトウをギロチンカッターで3mに切断した後、浴比
1:100で98−1℃に保ったカセイソーダ水溶液(
ao y/l )中に投入し、攪拌しながら所定時間処
理し、水洗、乾燥した抜水に分散し、濃度1俤のスラリ
ーとし、能谷理機■製ディスク・リイファイナで叩解し
て繊維状フィブリルのパルプを得た。この場合叩解程度
を調節して平均繊維径の異なる有機繊維状フィブリルを
作成した。
After cutting this tow into 3m lengths with a guillotine cutter, a caustic soda aqueous solution kept at 98-1°C at a bath ratio of 1:100 (
ao y/l), treated with stirring for a predetermined time, washed with water, dispersed in dried drained water, made into a slurry with a concentration of 1 yen, and beaten with a disc refiner manufactured by Noya Riki ■ to form a fibrous material. A fibril pulp was obtained. In this case, organic fibrous fibrils with different average fiber diameters were created by adjusting the degree of beating.

m1、丸断面で繊維径、轍維長を種々変更したポリエチ
レンテレフタレート短繊維を用意し、この短穢維を前記
パルプに所定の混合率になるように混合し、混合された
スラリーにパルプ重整し、東洋精機■製タッピ式スタン
ダードシ一トマ7ノで抄造し、軽い荷重(soop)の
コーチロールにより脱水し、ワイヤメツシュより剥離し
た。
m1, prepare polyethylene terephthalate short fibers with round cross sections and various fiber diameters and rut fiber lengths, mix these short fibers with the pulp at a predetermined mixing ratio, and add pulp to the mixed slurry. Then, it was made into paper using a Tappy type standard sheet machine 7 manufactured by Toyo Seiki ■, dehydrated using a coach roll with a light load (soop), and peeled off from a wire mesh.

この得られた湿紙を通気度150 CC/Cl1l/ 
sec目付252/−のレーヨン湿式不織布にはさみ、
5t/cdの荷重下でIIQ’Cにて乾燥してマスク用
基材を得た。この基材を加工縫製してマスクとした。実
験条件及び結果を次表に示す。
The obtained wet paper was heated to an air permeability of 150 CC/Cl1l/
Sandwiched in rayon wet non-woven fabric with a sec basis weight of 252/-,
It was dried at IIQ'C under a load of 5t/cd to obtain a mask base material. This base material was processed and sewn into a mask. The experimental conditions and results are shown in the table below.

有機繊維状フィブリルの径が0.1μm未シーの扁lけ
パルプのワイヤメツシュの喰い込みのためワイヤメツシ
ュからの剥離が悪く、また通気度が低いためマスク着用
時、の呼吸が阻害された。
The organic fibrous fibrils had a diameter of 0.1 μm and were bitten into the unseeded wire mesh, making it difficult to peel off from the wire mesh.Also, the air permeability was low, which hindered breathing when wearing a mask.

また有機繊維径の細い/I62も同様でちった、−万、
有機繊維状フィブリルの径が3μm2、↓ 静んム3と有機繊維径の太い44は共にDOPの補集性
能が著しく悪く、マスクとしての使用には不適当であっ
た。
The same goes for /I62, which has a small diameter organic fiber.
The diameter of the organic fibrous fibrils was 3 μm 2 ↓ Both the Shimmu 3 and the large organic fiber diameter 44 had extremely poor DOP collection performance and were unsuitable for use as a mask.

また、有機繊維状フィブリルの混入量が5重量%未満で
あるAllは通気度が高すぎてDOP捕集性能が著しく
低く、混入量が40Xt%を越える410は通気度が低
いために呼吸が大きく阻害され、共にマスクとしての使
用には不適当であった。
In addition, All with less than 5% by weight of organic fibrous fibrils has too high air permeability and extremely low DOP collection performance, while 410 with more than 40Xt% has low air permeability and high respiration. Both were unsuitable for use as a mask.

実施例中のA5〜扁9は抄紙性がすぐn 、 o 、3
μmのDOPの捕集効率もある程度あや、また、マスク
としての着用時の呼吸も容易であり、肌ざわりがよく、
フィツト感があり、マスクとして適当であった。
Paper-making properties of A5 to 9 in the examples were just n, o, 3.
The collection efficiency of μm DOP is somewhat high, and it is easy to breathe when worn as a mask, and it feels good on the skin.
It had a good fit and was suitable as a mask.

Claims (1)

【特許請求の範囲】 L 平均繊維径が0.1〜3.0μ雷である有機繊維状
フィブリル5〜40重量%と平均繊維径が3〜25μm
である有機繊維95〜60重量係とを混合し、湿式抄造
した湿式不織布からなることを特徴とするマスク。 2 有機繊維状フィブリルが線状芳香族ポリエステルと
該ポリエステルに相溶性がなく、アルカリ性溶液に可溶
の有機化合物との混合物を成凰し、得られた成型物をア
ルカリ性溶液で処理した後叩解することによシ得られた
ものである特許請求の範囲第1項記載のマスク。 & 有機繊維状フィブリルが一般式 (nは2〜6の整数を示す) で表わされる繰シ返し単位を主たる成分とするポリエス
テルよシ構成されている特許請求の範囲第1項又は第2
項記載のマスクつ
[Scope of Claims] L 5 to 40% by weight of organic fibrous fibrils having an average fiber diameter of 0.1 to 3.0 μm and an average fiber diameter of 3 to 25 μm
A mask characterized by being made of a wet-processed nonwoven fabric mixed with 95 to 60% of organic fiber by weight and wet-processed. 2. Organic fibrous fibrils form a mixture of a linear aromatic polyester and an organic compound that is incompatible with the polyester and is soluble in an alkaline solution, and the resulting molded product is treated with an alkaline solution and then beaten. A mask according to claim 1, which is particularly obtained. & Claim 1 or 2, wherein the organic fibrous fibrils are composed of polyester whose main component is a repeating unit represented by the general formula (n is an integer from 2 to 6).
The mask mentioned in the section
JP57087199A 1982-05-25 1982-05-25 Mask Pending JPS58203770A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57087199A JPS58203770A (en) 1982-05-25 1982-05-25 Mask

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57087199A JPS58203770A (en) 1982-05-25 1982-05-25 Mask

Publications (1)

Publication Number Publication Date
JPS58203770A true JPS58203770A (en) 1983-11-28

Family

ID=13908299

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57087199A Pending JPS58203770A (en) 1982-05-25 1982-05-25 Mask

Country Status (1)

Country Link
JP (1) JPS58203770A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6128009A (en) * 1984-07-18 1986-02-07 旭化成株式会社 Dust protecting mask

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6128009A (en) * 1984-07-18 1986-02-07 旭化成株式会社 Dust protecting mask
JPH0524244B2 (en) * 1984-07-18 1993-04-07 Asahi Chemical Ind

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