JPH0814058B2 - Polyphenylene sulfide meltblown nonwoven fabric and method for producing the same - Google Patents

Polyphenylene sulfide meltblown nonwoven fabric and method for producing the same

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Publication number
JPH0814058B2
JPH0814058B2 JP62149766A JP14976687A JPH0814058B2 JP H0814058 B2 JPH0814058 B2 JP H0814058B2 JP 62149766 A JP62149766 A JP 62149766A JP 14976687 A JP14976687 A JP 14976687A JP H0814058 B2 JPH0814058 B2 JP H0814058B2
Authority
JP
Japan
Prior art keywords
polyphenylene sulfide
producing
polymer
woven fabric
nonwoven fabric
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP62149766A
Other languages
Japanese (ja)
Other versions
JPS63315655A (en
Inventor
栄一 西浦
勝敏 安藤
由治 奥村
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP62149766A priority Critical patent/JPH0814058B2/en
Publication of JPS63315655A publication Critical patent/JPS63315655A/en
Publication of JPH0814058B2 publication Critical patent/JPH0814058B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は,取り扱い易くて,耐熱性,耐薬品性に優れ
た不織布用シート,特にフィルター基材として有用なポ
リフェニレンサルファイド(以下PPSと略す)メルトブ
ロー不織布およびその製法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is a sheet for nonwoven fabric which is easy to handle and has excellent heat resistance and chemical resistance, particularly polyphenylene sulfide (hereinafter abbreviated as PPS) useful as a filter substrate. The present invention relates to a melt blown nonwoven fabric and a method for producing the same.

更に詳しくは,繊維の一部の少なくとも融着もしくは
絡合してなり,巻取,巻返し,裁断などでシートの乱れ
がなくかつ,目付分布が均一で高性能なダスト補集性を
有した,しかもポリマ玉の少ないPPSメルトブロー不織
布およびその製法に関するものである。
More specifically, at least part of the fibers were fused or entangled, and there was no disturbance of the sheet due to winding, rewinding, cutting, etc., and the basis weight distribution was uniform, and it had a high-performance dust collecting property. Moreover, the present invention relates to a PPS melt blown non-woven fabric containing few polymer balls and a method for producing the same.

[従来の技術] PPS不織布の製法として,一般的な溶融紡糸後延伸
し,けん縮を付与しカットし,カーディグ後にニードル
パンチ,ウォータパンチ,カーディグ時に融着繊維を混
合して熱処理する方法,あるいはバインダーをスプレー
加工する方法,あるいはスパンボンド法で紡糸し同様な
シート化方法で製造する方法などが提唱されている。
[Prior Art] As a method for producing a PPS nonwoven fabric, a general method after melt-spinning is followed by drawing, crimping and cutting, and needle-punching, water-punching after carding, and mixing heat-bonded fibers during carding, or heat treatment, or A method in which a binder is spray-processed, or a method in which a spunbond method is used for spinning and a similar sheet-forming method is proposed.

また極細PPS繊維を得るために複合紡糸を行った後紡
糸後延伸し,けん縮を付与し,カーディグ後にニードル
パンチ,ウォータパンチ,を施こし,その後海成分を脱
海するシート化方法が提唱されている。
In addition, a sheeting method has been proposed in which composite spinning is performed to obtain ultrafine PPS fibers, which is then stretched and then stretched, crimped, needle punched and water punched after carding, and then sea components are desalted. ing.

いずれの方法でも紡糸後に何等かの後処理を施こさな
い限り不織布として取り扱いが出来にくいこと,またバ
インダー,油剤,あるいは海成分などが不織布に残存す
るといった欠点がある。
Either method has the drawback that it is difficult to handle as a non-woven fabric unless some post-treatment is applied after spinning, and that the binder, oil agent, sea component, etc. remain in the non-woven fabric.

また,これらの紡糸に用いるポリマの溶融粘度は,製
糸上少なくとも1000ポイズ以上が必要で溶融粘度を上げ
るため分子量を大きくしたり,熱架橋,あるいはトリク
ロロベンゼンなどを共重合して3次元化する必要があっ
た。
In addition, the melt viscosity of the polymers used in these spinning processes must be at least 1000 poise or higher in the spinning process, and the molecular weight must be increased to increase the melt viscosity, or it must be three-dimensionalized by thermal crosslinking or copolymerization with trichlorobenzene. was there.

[発明が解決しようとする問題点] 本発明の目的は,かかる従来品の有する欠点を解消
し,巻取,巻返し,裁断などでシートの乱れがない均一
なPPSメルトブロー不織布およびその製法を提供するも
のである。
[Problems to be Solved by the Invention] An object of the present invention is to solve the drawbacks of the conventional products, and to provide a uniform PPS meltblown non-woven fabric in which the sheet is not disturbed by winding, rewinding, cutting or the like, and a method for producing the same. To do.

[問題点を解決するための手段] 前記の問題点を解決するため本発明は,次の構成を有
する。
[Means for Solving Problems] In order to solve the above problems, the present invention has the following configuration.

(1)平均繊度が0.5デニール以下の繊維からなり,繊
維の一部が少なくとも融着もしくは絡合している不織布
で,目付変動率が7%以下、引張り強度が1kg/5cm以上
であることを特徴とするPPSメルトブロー不織布。
(1) A non-woven fabric composed of fibers having an average fineness of 0.5 denier or less, and at least a part of the fibers being fused or entangled, and having a basis weight variation rate of 7% or less and a tensile strength of 1 kg / 5 cm or more. Characteristic PPS melt blown non-woven fabric.

(2)PPSポリマをメルトブローして繊維化するに際
し,重量平均分子量が2万〜7万のPPSポリマを用いる
ことを特徴とするPPSメルトブロー不織布の製法。
(2) A method for producing a PPS meltblown non-woven fabric, which comprises using a PPS polymer having a weight average molecular weight of 20,000 to 70,000 when melt-blowing the PPS polymer into fibers.

以下,本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail.

PPSポリマは融点が比較的高く,分解温度が融点に近
く,かつゲル化しやすいことから,メルトブロー紡糸に
は不向きなポリマである。
PPS polymer has a relatively high melting point, its decomposition temperature is close to the melting point, and it easily gels, making it unsuitable for melt blown spinning.

本発明に係るPPSメルトブロー不織布紡糸用のPPSポリ
マは分子量が比較的小さいもので,重量平均分子量で2
万〜7万程度の直鎖状物を選ぶ。望ましくは重量平均分
子量で3〜6万が好ましい。
The PPS polymer for spinning PPS meltblown nonwoven fabric according to the present invention has a relatively small molecular weight and has a weight average molecular weight of 2
Choose a linear product of about 10,000 to 70,000. Desirably, the weight average molecular weight is preferably 30,000 to 60,000.

重量平均分子量が2万未満の場合は融点よりわずかに
高い紡糸条件としただけで非常に低溶融粘度化するた
め,紡糸条件のコントロール範囲が非常に狭い。又シー
ト強度の弱い不織布になる。
When the weight average molecular weight is less than 20,000, the melt viscosity becomes extremely low only by making the spinning condition slightly higher than the melting point, so that the control range of the spinning condition is very narrow. Also, it becomes a non-woven fabric having a weak sheet strength.

一方,重量平均分子量が7万を越える場合は,融点よ
りかなり高温の紡糸条件とする必要が有り,ポリマ分
解,ゲル化を生じ,結果的にノズル詰りなどで紡糸安定
性を欠くことになる。
On the other hand, if the weight average molecular weight exceeds 70,000, it is necessary to set the spinning conditions at a temperature considerably higher than the melting point, resulting in polymer decomposition and gelation, resulting in nozzle clogging and lack of spinning stability.

PPS不織布は,次のようにして製造される。 The PPS nonwoven fabric is manufactured as follows.

具体的な製造装置の1例として,第1図のごとき装置
が用いられる。
As an example of a specific manufacturing apparatus, the apparatus shown in FIG. 1 is used.

紡出ノズル1から吐出されたポリマはそのサイズに設
けられたガス噴射口2から噴射されるガスで繊維化す
る。この紡出繊維3を保温噴射ガス,随伴空気を制御し
ながら補集装置4で補集する。
The polymer discharged from the spinning nozzle 1 is made into fibers by the gas injected from the gas injection port 2 provided in that size. The spun fiber 3 is collected by the collecting device 4 while controlling the heat-insulating blast gas and the accompanying air.

さらにプレスロール6で圧力を加えた後,PPSメルトブ
ロー不織布シート5を巻取装置8で巻取る。
After further applying pressure with a press roll 6, the PPS meltblown nonwoven fabric sheet 5 is wound by a winding device 8.

なお7は後述するが,ポリマを保温するためのトラン
スベクターである。
As will be described later, 7 is a trans vector for keeping the polymer warm.

前記ポリマの紡糸時の溶融粘度は50〜700ポイズが好
ましい。望ましくは60〜500ポイズであり,さらに望ま
しくは70〜300ポイズである。
The melt viscosity of the polymer during spinning is preferably 50 to 700 poise. It is preferably 60 to 500 poise, and more preferably 70 to 300 poise.

50ポイズ未満の場合,短繊維長からなるシートとなり
強度の弱い不織布になる。このため加熱ガス流を少なく
すると,繊維が脆くなる。
If it is less than 50 poise, it will be a sheet consisting of short fiber length and will be a non-woven fabric with weak strength. Therefore, if the heating gas flow is reduced, the fiber becomes brittle.

一方溶融粘度が700ポイズを越えると高温の加熱ガス
が大量に必要なだけでなく,気流の乱れを生じポリマ玉
の発生をともなう。
On the other hand, if the melt viscosity exceeds 700 poise, not only a large amount of high-temperature heating gas is required, but also the turbulence of the air flow causes the generation of polymer balls.

ポリマの吐出量は,0.1〜30g/分/ノズルの吐出量でよ
いが,紡糸ノズル形態で最適値が変わる。すなわち,特
開昭49−10258,特開昭49−48921などで示されている様
に,ノズルの両サイドから加熱ガスを噴射せしめるタイ
プの口金では,ポリマの繊維化機構より0.1〜1.0g/分/
ノズルが望ましく,さらに望ましくは0.2〜0.5g/分/ノ
ズルである。
The polymer discharge amount may be 0.1 to 30 g / min / nozzle discharge amount, but the optimum value varies depending on the spinning nozzle configuration. That is, as shown in JP-A-49-10258, JP-A-49-48921, etc., in a die of a type in which heated gas is injected from both sides of a nozzle, 0.1-1.0 g / Min /
A nozzle is desirable, and more preferably 0.2 to 0.5 g / min / nozzle.

又,実公昭62−1260の様に,ポリマと加圧状態の加熱
ガスが共通孔から常圧下に噴射せしめるタイプの口金で
は,ポリマの繊維化機構より0.5〜30g/分/ノズルが望
ましく,さらに望ましくは1〜20g/分/ノズルである。
Further, as in Japanese Utility Model Publication No. 62-1260, in a die of a type in which a heating gas of a polymer and a pressurized state can be jetted from a common hole under normal pressure, 0.5 to 30 g / min / nozzle is preferable due to the fiberizing mechanism of the polymer. Desirably 1 to 20 g / min / nozzle.

ノズルの両サイドから加熱ガスを噴射せしめるタイプ
の場合,0.1g/分/ノズル以下,およびポリマと加圧状態
の加熱ガスを共通孔から常圧下に噴射せしめるタイプの
場合,0.5g/分/ノズル以下の吐出量ではポリマの滞留時
間が長くなり,ポリマ分解,炭化物の発生,ノズル詰り
の原因となり好ましくない。一方,ノズルの両サイドか
ら加熱ガスを噴射せしめるタイプの1.0g/分/ノズル,
およびポリマと加圧状態の加熱ガスを共通孔から常圧下
に噴射せしめるタイプの30g/分/ノズル以上の場合も融
点よりかなり高温の紡糸条件とする必要が有り,結果的
にこの場合もポリマ分解,ゲル化を生じ紡糸安定性を欠
くことになる。
0.1 g / min / nozzle or less for the type that ejects heated gas from both sides of the nozzle, and 0.5 g / min / nozzle for the type that ejects heated gas in the polymer and pressurized state from a common hole under normal pressure The following discharge amounts are not preferable because the residence time of the polymer becomes long, which causes polymer decomposition, carbide generation, and nozzle clogging. On the other hand, 1.0g / min / nozzle of the type that jets heated gas from both sides of the nozzle,
Also, in the case of 30 g / min / nozzle of a type in which heated gas of polymer and pressurized state is ejected from a common hole under normal pressure, it is necessary to make spinning conditions considerably higher than the melting point. As a result, polymer decomposition is also caused in this case. However, gelation occurs and spinning stability is lost.

ポリマを繊維化するための加熱ガスの噴射量は加熱さ
れたガスをポリマ1gに対し,2.0Nm3/Hr以上噴射せしめて
繊維化するのがよい。加熱ガスの噴射量が2.0Nm3/Hr未
満ではドラフトが不十分で繊維強度が低く,脆い不織布
シートになる。このため望ましくは,3.0Nm3/Hr以上噴射
せしめ繊維化するのがよい。加熱ガスの噴射量は,気流
の乱れを生じてポリマ玉の発生が生じない程度ならば糸
物性,シート物性の面からは多い方が好ましい。しかし
10.0Nm3/Hr以上で噴射せしめて繊維化すると,気流の乱
れを生じてポリマ玉の発生が認められる。これはノズル
設計がポイントになっており,精度が上がれば更に噴射
量を増すことができると考えられる。
As for the injection amount of the heating gas for fiberizing the polymer, it is preferable to inject the heated gas at 2.0 Nm 3 / Hr or more per 1 g of the polymer to fiberize it. When the amount of heated gas injected is less than 2.0 Nm 3 / Hr, the draft is insufficient and the fiber strength is low, resulting in a brittle non-woven sheet. For this reason, it is desirable to inject fibers of 3.0 Nm 3 / Hr or more to form fibers. It is preferable that the injection amount of the heating gas is large from the viewpoint of yarn physical properties and sheet physical properties as long as the turbulence of the air flow does not occur and the generation of polymer balls does not occur. However
When fibrous by injecting at 10.0 Nm 3 / Hr or more, turbulence of air flow occurs and generation of polymer beads is recognized. This is due to the nozzle design, and it is thought that the injection amount can be further increased if the accuracy increases.

上述の方法でPPSメルトブロー繊維は得られるが,直
接不織布を製造する場合,PPSは融点が高くノズルから約
15cm以上離れた所で補集すると,随伴空気でかなり冷却
されシート形態を保つだけの自己融着,絡合はない。
Although PPS meltblown fibers can be obtained by the above-mentioned method, when directly manufacturing non-woven fabric, PPS has a high melting point,
When collected at a distance of 15 cm or more, there is no self-fusion or entanglement enough to maintain the sheet form by cooling with the accompanying air.

このためサクションによりシートの飛散を防止すると
ともに捕集から巻取までにシートの取り扱い性を改良す
べく従来方法を含む工夫が必要であった。
Therefore, it has been necessary to devise a method including a conventional method in order to prevent the sheet from scattering by suction and to improve the handleability of the sheet from collecting to winding.

この方法として,繊維を捕集直後に0.1kg/10cm以上の
線圧を加えることで,形態安定性があり,取り扱い性の
よいPPSメルトブロー不織布の製造が可能となった。
As a method for this, by applying a linear pressure of 0.1 kg / 10 cm or more immediately after collecting the fibers, it became possible to produce a PPS meltblown nonwoven fabric with morphological stability and good handleability.

特に紡糸繊維の補集面の繊維温度を150℃以上に保つ
ことでその効果は著しい。
In particular, the effect is remarkable when the fiber temperature on the collecting surface of the spun fiber is maintained at 150 ° C or higher.

紡出繊維の捕集面の繊維温度を150℃以上に保つ方法
としては捕集距離を近くにする。加熱ガス温度を高くす
る。また第1図のごとくノズルから捕集の間に両サイド
から加熱されたガスを噴射せしめるようなトランスベク
ター装置7などを設けて保温するなどの方法が有り,い
ずれでも良いが,ノズルから捕集の間に両サイドから加
熱されたガスを噴射せしめ,保温するなどの方法が随伴
空気の制御作用も有り均一なシートとなり望ましい方法
である。
As a method of keeping the fiber temperature on the collection surface of the spun fiber at 150 ° C or higher, the collection distance should be short. Increase the heating gas temperature. As shown in FIG. 1, there is a method of keeping heat by providing a transvector device 7 for injecting heated gas from both sides between the nozzle and the collection. A desirable method is to inject a heated gas from both sides during this period to keep the temperature warm, etc., as well as to control the entrained air so that a uniform sheet is obtained.

このシートを特にフィルター用途に使用する場合,そ
のシートの平均繊度は0.5デニール以下で目付変動率(C
V値:以後の略称とする)が7%以下、シートの引張強
度が1kg/5cm以上が好ましい。
When this sheet is used for filter applications, the average fineness of the sheet is 0.5 denier or less and the weight variation (C
V value: abbreviated below) is 7% or less, and the tensile strength of the sheet is preferably 1 kg / 5 cm or more.

繊度において望ましくは0.2デニール以下,更に望ま
しくは0.1デニール以下がよい。
The fineness is preferably 0.2 denier or less, more preferably 0.1 denier or less.

0.5デニール以上では,繊維間の間隙が大きくなり,
ミクロな目付ムラとなり好ましくない。
Above 0.5 denier, the gap between fibers becomes large,
It is not preferable because it causes microscopic unevenness of weight.

ただし0.005デニール以下では繊維の強度が低く好ま
しくない。
However, if it is less than 0.005 denier, the strength of the fiber is low, which is not preferable.

目付変動率は7%以下が好ましい,望ましくは0.5%
以下がよい。
The unit weight variation is preferably 7% or less, preferably 0.5%
The following is good.

7%を越ると品質の安定性を欠くことがある。 If it exceeds 7%, the stability of quality may be lost.

このようにして作成されたPPSメルトブロー不織布
は,構成している繊維の一部が少なくとも融着もしくは
絡合しており,形態安定性,取り扱い性がよく,耐熱
性,耐薬品性があるムラのすくない不織布シートが得ら
れた。
The PPS meltblown non-woven fabric produced in this way has at least some of the constituent fibers fused or entangled, and has good morphological stability, handleability, heat resistance, and chemical resistance. A thin nonwoven sheet was obtained.

以下に実施例に従い本発明を説明する。 The present invention will be described below with reference to examples.

なお重量平均分子量,CV値,平均繊度の測定方法,引
張り強度は次の通りである。
The weight average molecular weight, CV value, measuring method of average fineness, and tensile strength are as follows.

(1)重量平均分子量 ゲル浸透クロマトグラフ法(GPC)でおこなう。(1) Weight average molecular weight Performed by gel permeation chromatography (GPC).

(2)CV値 作成した不織布から10cm角の試料を幅方向,長さ方向
にそれぞれ10枚ずつ,計100枚の試料から2元配置によ
る分散分析をおこなう。
(2) CV value From the created non-woven fabric, a 10 cm square sample is analyzed for 10 samples in the width direction and 10 samples in the length direction.

(3)平均繊度 不織布10ヵ所をランダムにサンプリングし,500倍の倍
率で位置を変え,それぞれ3枚(合計30枚)電子顕微鏡
(SEM)写真をとる。
(3) Average fineness Ten non-woven fabrics are randomly sampled, the position is changed at a magnification of 500 times, and three electron microscope (SEM) photographs are taken for each (30 in total).

写真1枚から繊維10本の側面の径を測定し,繊度分布
表を作成し,その中位径を平均繊度とする。
Measure the diameter of the side of 10 fibers from 1 sheet of the photograph, make a fineness distribution table, and take the median diameter as the average fineness.

(4)引張り強度 不織布を幅5cm,長さ15cmに5枚サンプリングし,試長
5cm,引張り速度5cm/minでオートグラフで引張り,破断
強力の平均値とする。
(4) Tensile strength 5 non-woven fabric samples with a width of 5 cm and a length of 15 cm are sampled and tested.
The average value of breaking strength is obtained by pulling with an autograph at 5 cm and a pulling speed of 5 cm / min.

[実施例] 実施例1 ジクロロベンゼンと硫化ナトリウムを重合し,重量平
均分子量5万のPPSポリマを得た。
Example 1 Example 1 Dichlorobenzene and sodium sulfide were polymerized to obtain a PPS polymer having a weight average molecular weight of 50,000.

このPPSポリマを下記の条件でメルトブローした。 This PPS polymer was melt blown under the following conditions.

紡糸温度 320℃ エアー温度 360℃ エアー量 1150Nm3/Hr 吐出量 300g/min ノズル径 0.2mm ノズルピッチ 1.2mm ノズル数 834個 捕集距離 15cm 捕集直後の線圧 2kg/100cm メルトブロー紡糸は安定しており,得られたシートは
目付30g/m2,平均繊維径3ミクロンのPPSからなる部分的
に融着,絡合したメルトブロー不織布シートでCV値が6.
4%,であった。
Spinning temperature 320 ℃ Air temperature 360 ℃ Air volume 1150Nm 3 / Hr Discharge rate 300g / min Nozzle diameter 0.2mm Nozzle pitch 1.2mm Nozzle number 834 Collection distance 15cm Linear pressure immediately after collection 2kg / 100cm Melt blow spinning is stable The obtained sheet is a partially fused and entangled melt-blown non-woven sheet made of PPS having a basis weight of 30 g / m 2 and an average fiber diameter of 3 microns, and has a CV value of 6.
It was 4%.

またこの不織布の強度は5kg/5cmであり,巻取,巻返
し,裁断などの取り扱い性に優れていた。
The strength of this non-woven fabric was 5 kg / 5 cm, and it was easy to handle such as winding, rewinding, and cutting.

実施例2 実施例1において,エアー温度を320℃,エアー量650
Nm3/Hr,補集距離25cm,ノズル3cm下で繊維の吐出方向と
平行に3cm横から,それぞれ250℃のエアーを200Nm3/Hr
噴射保温し,合せて随伴空気の制御作用も行った。
Example 2 In Example 1, the air temperature was 320 ° C. and the air amount was 650.
Nm 3 / Hr, collection distance 25 cm, nozzle 3 cm, parallel to the fiber discharge direction 3 cm from the side, 250 ° C air at 200 Nm 3 / Hr
The injection was kept warm and the associated air was also controlled.

メルトブロー紡糸は安定しており,得られたシートは
目付29g/m2,平均繊維径3.5ミクロンのPPSからなる部分
的に融着,絡合したメルトブロー不織布シートで,均一
性が向上しCV値が3.2%であった。
Meltblown spinning is stable and the resulting sheet is a partially fused and entangled meltblown non-woven sheet made of PPS with a basis weight of 29 g / m 2 and an average fiber diameter of 3.5 microns, with improved uniformity and a CV value. It was 3.2%.

またこの不織布の強度は5.3kg/5cmであり,巻取,巻
返し,裁断などの取り扱い性に優れていた。
The strength of this non-woven fabric was 5.3 kg / 5 cm, and it was easy to handle such as winding, rewinding and cutting.

比較例1 実施例1において,重量平均分子量1万のPPSポリマ
を同条件で紡糸したが,短い繊維となり繊維の吹飛びが
はげしく,シート強度の弱い不織布となった。また繊維
長を長くするためには,紡糸温度を300℃以下とする必
要がありポリマの融点に近く,紡糸条件の制御が非常に
困難であった。
Comparative Example 1 In Example 1, a PPS polymer having a weight average molecular weight of 10,000 was spun under the same conditions, but short fibers were formed, and the fibers were blown off easily, resulting in a non-woven fabric having a weak sheet strength. In addition, in order to lengthen the fiber length, it is necessary to keep the spinning temperature below 300 ° C, which is close to the melting point of the polymer, making it very difficult to control the spinning conditions.

比較例2 実施例1において,重量平均分子量10万のPPSポリマ
を同条件で紡糸したが,太繊度の不織布となった。平均
繊度0.5デニール以下の不織布とするためには,360℃以
上の紡糸温度を必要とし,ポリマの分解ガスがかなり発
生し作業環境が悪いばかりでなく,3Hr以内でノズル詰り
が発生した。
Comparative Example 2 In Example 1, a PPS polymer having a weight average molecular weight of 100,000 was spun under the same conditions, but a non-woven fabric having a large fineness was obtained. A spinning temperature of 360 ° C or higher was required to obtain a non-woven fabric with an average fineness of 0.5 denier or less. Not only was the working environment poor due to polymer decomposition gas, but nozzle clogging occurred within 3 hours.

[発明の効果] 本発明に係るPPSメルトブロー不織布は,繊維の一部
が少なくとも融着もしくは絡合されているので,巻取,
巻返し,裁断などでシートの乱れがなく取り扱い易い。
このため耐熱性,耐薬品性を生かした不織布用シート基
材として各種産業用途に有用である。
EFFECTS OF THE INVENTION Since the PPS meltblown nonwoven fabric according to the present invention has at least part of the fibers fused or entangled,
Easy to handle without disturbing the sheet due to rewinding or cutting.
Therefore, it is useful for various industrial applications as a non-woven sheet base material that makes good use of heat resistance and chemical resistance.

特に目付分布が均一で高性能なフィルター用不織布基
材として最適である。
In particular, it is most suitable as a high-performance non-woven fabric substrate for filters with a uniform basis weight distribution.

また,特別な重量平均分子量の物を選択することによ
り,高品位のPPSメルトブロー不織布を製造することが
出来る。
Also, by selecting a material having a special weight average molecular weight, a high-quality PPS meltblown nonwoven fabric can be manufactured.

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

第1図は,本発明に係るPPSメルトブロー不織布の製法
の1例を示す概略図である。 1:ノズル 2:ガス噴射口 3:紡糸された繊維 4:捕集装置 5:メルトブロー不織布シート 6:プレスロール 7:トランスベクター装置 8:巻取装置
FIG. 1 is a schematic view showing an example of a method for producing a PPS meltblown nonwoven fabric according to the present invention. 1: Nozzle 2: Gas injection port 3: Spun fiber 4: Collection device 5: Meltblown nonwoven sheet 6: Press roll 7: Transvector device 8: Winding device

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】平均繊度が0.5デニール以下の繊維からな
り、繊維の一部が少なくとも融着もしくは絡合している
不織布で、目付変動率が7%以下、引張り強度が1kg/5c
m以上であることを特徴とするポリフェニレンサルファ
イドメルトブロー不織布。
1. A non-woven fabric comprising fibers having an average fineness of 0.5 denier or less, and at least a part of the fibers being fused or entangled, having a basis weight variation of 7% or less and a tensile strength of 1 kg / 5c.
A polyphenylene sulfide meltblown non-woven fabric characterized by having a length of at least m.
【請求項2】ポリフェニレンサルファイドポリマをメル
トブローして紡出繊維化するに際し、重量平均分子量が
2万〜7万のポリフェニレンサルファイドポリマを用い
ることを特徴とするポリフェニレンサルファイドメルト
ブロー不織布の製法。
2. A method for producing a polyphenylene sulfide meltblown non-woven fabric, which comprises using a polyphenylene sulfide polymer having a weight average molecular weight of 20,000 to 70,000 when melt-blowing the polyphenylene sulfide polymer to form a spun fiber.
【請求項3】ポリフェニレンサルファイドポリマが、直
鎖状である特許請求の範囲第2項に記載のポリフェニレ
ンサルファイドメルトブロー不織布の製法。
3. The method for producing a polyphenylene sulfide meltblown nonwoven fabric according to claim 2, wherein the polyphenylene sulfide polymer is linear.
【請求項4】紡出繊維化に際し、紡出ノズルから補集の
間に両サイドから加熱されたガスを噴射せしめて保温す
る特許請求の範囲第2項に記載のポリフェニレンサルフ
ァイドメルトブロー不織布の製法。
4. The method for producing a polyphenylene sulfide meltblown non-woven fabric according to claim 2, wherein upon spinning fiber formation, heated gas is jetted from both sides during collection from the spinning nozzle to keep the temperature warm.
【請求項5】紡出繊維の補集面の繊維温度が、150℃以
上である特許請求の範囲第2項に記載のポリフェニレン
サルファイドメルトブロー不織布の製法。
5. The method for producing a polyphenylene sulfide meltblown nonwoven fabric according to claim 2, wherein the fiber temperature on the collecting surface of the spun fiber is 150 ° C. or higher.
【請求項6】紡出繊維が、補集直後に0.1kg/10cm以上の
線圧が加えられる特許請求の範囲第2項に記載のポリフ
ェニレンサルファイドメルトブロー不織布の製法。
6. The method for producing a polyphenylene sulfide meltblown nonwoven fabric according to claim 2, wherein the spun fiber is applied with a linear pressure of 0.1 kg / 10 cm or more immediately after the collection.
JP62149766A 1987-06-16 1987-06-16 Polyphenylene sulfide meltblown nonwoven fabric and method for producing the same Expired - Lifetime JPH0814058B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62149766A JPH0814058B2 (en) 1987-06-16 1987-06-16 Polyphenylene sulfide meltblown nonwoven fabric and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62149766A JPH0814058B2 (en) 1987-06-16 1987-06-16 Polyphenylene sulfide meltblown nonwoven fabric and method for producing the same

Publications (2)

Publication Number Publication Date
JPS63315655A JPS63315655A (en) 1988-12-23
JPH0814058B2 true JPH0814058B2 (en) 1996-02-14

Family

ID=15482267

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0814058B2 (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2859193B2 (en) * 1987-11-12 1999-02-17 旭化成工業株式会社 Polyphenylene sulfide nonwoven fabric, method for producing the same, and filter using the same
JPH01229855A (en) * 1987-11-12 1989-09-13 Asahi Chem Ind Co Ltd Nonwoven fabric of polyarylene sulfide
JP2579658B2 (en) * 1988-02-05 1997-02-05 東燃化学株式会社 Manufacturing method of heat-resistant nonwoven fabric
JPH0280651A (en) * 1988-09-16 1990-03-20 Teijin Ltd Web composed of ultrafine fiber of polyphenylene sulfide and production of the same web
US6110589A (en) * 1995-12-11 2000-08-29 Pall Corporation Polyarylene sulfide melt blown fibers and products
US5690873A (en) * 1995-12-11 1997-11-25 Pall Corporation Polyarylene sulfide melt blowing methods and products
US6130292A (en) * 1995-12-11 2000-10-10 Pall Corporation Polyarylene sulfide resin composition
EP0950691B1 (en) 1996-11-20 2006-06-21 Kureha Corporation Polyarylene sulfide resin composition
JP5832422B2 (en) 2010-03-31 2015-12-16 株式会社クレハ Branched polyarylene sulfide resin and process for producing the same
CN107709646B (en) * 2015-06-30 2021-07-16 株式会社可乐丽 Nonwoven fabric and method for producing same
CN111819245A (en) * 2017-12-28 2020-10-23 3M创新有限公司 Ceramic coated fibers comprising flame retardant polymers and methods of making nonwoven structures

Also Published As

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