JP2010077544A - Polyphenylene sulfide fiber for papermaking and method for producing the same - Google Patents
Polyphenylene sulfide fiber for papermaking and method for producing the same Download PDFInfo
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- 239000000835 fiber Substances 0.000 title claims abstract description 84
- 239000004734 Polyphenylene sulfide Substances 0.000 title claims abstract description 57
- 229920000069 polyphenylene sulfide Polymers 0.000 title claims abstract description 57
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims description 22
- 238000002425 crystallisation Methods 0.000 claims description 15
- 230000008025 crystallization Effects 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 12
- 238000009998 heat setting Methods 0.000 claims description 6
- 238000002074 melt spinning Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 14
- 238000001035 drying Methods 0.000 description 17
- 239000004745 nonwoven fabric Substances 0.000 description 14
- 230000037303 wrinkles Effects 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- 239000011230 binding agent Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000002788 crimping Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- SOHCOYTZIXDCCO-UHFFFAOYSA-N 6-thiabicyclo[3.1.1]hepta-1(7),2,4-triene Chemical group C=1C2=CC=CC=1S2 SOHCOYTZIXDCCO-UHFFFAOYSA-N 0.000 description 1
- XWUCFAJNVTZRLE-UHFFFAOYSA-N 7-thiabicyclo[2.2.1]hepta-1,3,5-triene Chemical group C1=C(S2)C=CC2=C1 XWUCFAJNVTZRLE-UHFFFAOYSA-N 0.000 description 1
- ODPYDILFQYARBK-UHFFFAOYSA-N 7-thiabicyclo[4.1.0]hepta-1,3,5-triene Chemical group C1=CC=C2SC2=C1 ODPYDILFQYARBK-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010036 direct spinning Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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Abstract
Description
本発明は、抄紙用ポリフェニレンサルファイド繊維およびその製造方法に関するものである。 The present invention relates to a polyphenylene sulfide fiber for papermaking and a method for producing the same.
耐熱性、耐薬品性に優れたポリフェニレンサルファイド(以下、PPSという)繊維を用いた不織布は様々な用途に使用されている。特に、湿式不織布では、バインダーとして未延伸PPS繊維(非晶質PPS繊維)を活用した技術が開示されている(特許文献1、2)。 Nonwoven fabrics using polyphenylene sulfide (hereinafter referred to as PPS) fibers having excellent heat resistance and chemical resistance are used in various applications. In particular, for wet nonwoven fabrics, techniques using unstretched PPS fibers (amorphous PPS fibers) as a binder are disclosed (Patent Documents 1 and 2).
しかし、非晶質PPS繊維は高温での熱収縮率が大きい等寸法安定性に劣るため、抄紙工程での乾燥時に収縮するなど、湿式不織布にしわやふくれや乾燥ムラ等が発生してしまい、良好な湿式不織布が得られないという問題があった。
本発明は、非晶質PPS繊維において、熱収縮率の小さく、かつ、水分散性が良好な抄紙用PPS繊維およびその製造方法を提供することを目的とする。 An object of the present invention is to provide a papermaking PPS fiber having a low thermal shrinkage and good water dispersibility in an amorphous PPS fiber, and a method for producing the same.
本発明は、溶融紡糸した後、延伸及び熱固定処理することなく得られた非晶質PPS繊維を80℃〜95℃の温度範囲で熱処理することを特徴とする抄紙用PPS繊維の製造方法、および、当該製造製法で得られたPPS繊維であって、結晶化熱量が10J/g以上、150℃×30分の乾熱収縮率が35%以下であることを特徴とする抄紙用PPS繊維である。 The present invention relates to a method for producing PPS fibers for papermaking, characterized by heat-treating amorphous PPS fibers obtained without melt stretching and heat setting after melt spinning in a temperature range of 80 ° C to 95 ° C, And a PPS fiber obtained by the production method, wherein the heat of crystallization is 10 J / g or more, and the dry heat shrinkage at 150 ° C. × 30 minutes is 35% or less. is there.
本発明により、非晶質PPS繊維において、熱収縮率の小さく、水分散性も良好な抄紙用PPS繊維およびその製造方法を提供することができる。 INDUSTRIAL APPLICABILITY According to the present invention, it is possible to provide a papermaking PPS fiber having a low thermal shrinkage and good water dispersibility and a method for producing the same in an amorphous PPS fiber.
本発明の抄紙用PPS繊維の製造方法は、溶融紡糸した繊維を延伸も熱固定処理もすることなく得られた非晶質PPS繊維を80℃〜95℃の温度範囲で熱処理することを特徴とするものである。非晶質PPS繊維は、加熱すると容易に軟化するので湿式不織布のバインダーとして用いることができる。 The method for producing PPS fibers for papermaking according to the present invention is characterized in that amorphous PPS fibers obtained without subjecting melt-spun fibers to stretching or heat setting are heat-treated at a temperature range of 80 ° C to 95 ° C. To do. Amorphous PPS fibers soften easily when heated and can be used as a binder for wet nonwoven fabrics.
ここで、PPSは、繰り返し単位としてp−フェニレンサルファイド単位やm−フェニレンサルファイド単位などのフェニレンサルファイド単位を含有するポリマーである。PPSは、これらのいずれかの単位のホモポリマーでもよいし、両方の単位を有する共重合体でもよい。また、他の芳香族サルファイドとの共重合体であってもよい。 Here, PPS is a polymer containing phenylene sulfide units such as p-phenylene sulfide units and m-phenylene sulfide units as repeating units. PPS may be a homopolymer of any of these units, or may be a copolymer having both units. Moreover, the copolymer with another aromatic sulfide may be sufficient.
また、PPSの重量平均分子量としては、40,000〜60,000が好ましい。40,000以上とすることで、PPS繊維として良好な力学的特性を得ることができる。また、60,000以下とすることで、溶融紡糸の溶液の粘度を抑え、特殊な高耐圧仕様の紡糸設備を必要とせずに済む。 Moreover, as a weight average molecular weight of PPS, 40,000-60,000 are preferable. By setting it to 40,000 or more, good mechanical properties as PPS fibers can be obtained. In addition, when the viscosity is 60,000 or less, the viscosity of the melt spinning solution is suppressed, and a special high pressure resistant spinning equipment is not required.
溶融紡糸した繊維であって、延伸及び熱固定処理することなく得られた非晶質PPS繊維とは、PPSポリマーをエクストルダー型紡糸機等で口金を通じて溶融紡糸したものであって、実質的に延伸することなく、かつ、結晶化温度以上で熱固定処理を施すことのないPPS繊維のことをいう。このようにして得られた非晶質PPS繊維を、結晶化温度未満の80℃〜95℃の温度範囲で熱処理することが本発明の製造方法の特徴であり、これにより特に抄紙用として好適なPPS繊維を得ることができる。熱固定処理とは結晶化温度以上で熱処理して非晶質状態から結晶化状態に処理することをいう。また、実質的に延伸することなくとは、製糸工程で工程上自然と発生する延伸は含まない。しかし、乾熱収縮の抑制の観点から、製糸工程での自発的な延伸は1.2倍以下であることが好ましい。 A melt-spun fiber, which is obtained without stretching and heat-setting, is an amorphous PPS fiber obtained by melt-spinning a PPS polymer through a die with an extruder-type spinning machine or the like. It refers to PPS fiber that is not stretched and is not subjected to heat setting treatment at a temperature equal to or higher than the crystallization temperature. It is a feature of the production method of the present invention that the amorphous PPS fiber thus obtained is heat-treated at a temperature range of 80 ° C. to 95 ° C. below the crystallization temperature. PPS fibers can be obtained. The heat setting treatment refers to a treatment from an amorphous state to a crystallized state by heat treatment at a crystallization temperature or higher. Further, the term “without substantially stretching” does not include stretching naturally occurring in the process of yarn production. However, from the viewpoint of suppressing dry heat shrinkage, the spontaneous stretching in the yarn forming process is preferably 1.2 times or less.
熱処理の温度範囲はPPS繊維の結晶化温度未満の80℃〜95℃であることが重要である。この温度範囲で熱処理することにより、非晶質PPS繊維を結晶化させずに予め適度に熱収縮することができる。この熱処理を施して得られたPPS繊維は結晶化していないので、温度を上げたときに軟化しやすく、例えば、抄紙の乾燥工程で軟化して湿式不織布を構成する繊維間同士で融着するので、従来どおりバインダーとして用いることができる。また、予め適度に熱収縮しているため、抄紙の乾燥工程等での収縮が抑制でき、しわ、膨れ等を小さくすることができる。
また、抄紙時には、繊維を水に分散させる必要があり、均一に分散することで地合いの良い紙を得ることができるが、本発明のPPS繊維は95℃以下で熱処理することで繊維間での融着も進んでいないため、繊維の水分散性も良好となり、地合いの良い紙を得ることができることから、本発明のPPS繊維は特に抄紙に適しているのである。
It is important that the temperature range of the heat treatment is 80 ° C. to 95 ° C. below the crystallization temperature of the PPS fiber. By performing heat treatment in this temperature range, the amorphous PPS fiber can be appropriately thermally contracted in advance without being crystallized. Since the PPS fibers obtained by this heat treatment are not crystallized, they tend to soften when the temperature is raised. For example, the fibers are softened in the paper-making drying process and fused between the fibers constituting the wet nonwoven fabric. As usual, it can be used as a binder. In addition, since it is appropriately heat-shrinked in advance, shrinkage in a papermaking drying process or the like can be suppressed, and wrinkles, blisters, and the like can be reduced.
In addition, when making paper, it is necessary to disperse the fibers in water, and evenly dispersed paper can be obtained. However, the PPS fiber of the present invention can be heated between 95 ° C. Since the fusion has not progressed, the water dispersibility of the fibers is improved, and a paper with good texture can be obtained. Therefore, the PPS fibers of the present invention are particularly suitable for papermaking.
熱処理する手段としては、ホットローラー等との接触によるものや、熱風、スチーム等によるバンドドライヤーや乾燥機等による加熱、赤外線照射、湯浴等いかなる手段であってもよい。また、熱処理をする糸の状態としては、トウのように連続した糸の状態でもよいし、予めカットしたカットファイバーの状態で施してもよい。処理工程としては、上記したホットローラーやバンドドライヤーのように連続した工程で行ってもよいし、一定量を乾燥機等に投入するようなバッチ式で行ってもよい。生産効率の良さから連続工程で行うほうが好ましい。 As a means for heat treatment, any means such as contact with a hot roller or the like, heating with a band drier or dryer with hot air or steam, infrared irradiation, hot water bath, etc. may be used. Further, the state of the yarn to be heat-treated may be a continuous yarn state such as a tow, or may be applied in a cut fiber state that has been cut in advance. As a processing process, you may carry out by the continuous process like the above-mentioned hot roller and a band dryer, and may carry out by the batch type which throws a fixed quantity into a dryer etc. It is more preferable to carry out by a continuous process from the standpoint of production efficiency.
本発明の熱処理は、PPS繊維に概ね張力を付与せずに行うことが重要である。張力を付与して熱処理すると、熱処理時の熱収縮が十分でなく、抄紙工程の乾燥などで高温になったときの熱収縮が大きくなるので、しわ、膨れ等が発生してしまう。概ね張力を付与しないとは、バンドドライヤーや乾燥機等で熱処理する場合には、ネットやバットなどの上に無張力の状態で置くことをいい、また、ホットローラーや湯浴等に繊維を通過させときには繊維がたるんで工程を通過しなくならない程度に調整することをいう。 It is important that the heat treatment of the present invention is performed without substantially applying tension to the PPS fiber. When heat treatment is applied with tension, the heat shrinkage during the heat treatment is not sufficient, and the heat shrinkage when the temperature becomes high due to drying or the like in the paper making process is increased, so that wrinkles, blisters and the like are generated. When applying heat with a band dryer or dryer, it means that the tension is not applied, and it means that it is placed on a net or bat without tension, and the fiber passes through a hot roller or hot water bath. In this case, the adjustment is made so that the fibers do not sag and do not pass through the process.
また、熱処理時間は、熱処理装置の能力および繊維への熱伝導効率によって決定されるが、本発明の物性を損なわない範囲であれば問題ない。結晶化抑制効果を十分に発現させるためには高温時は出来るだけ短時間にしたほうが好ましい。しかし、短時間過ぎると熱処理による低収縮化の効果が発現しないため、好ましい熱処理時間は0.01sec以上2時間以下である。 The heat treatment time is determined by the ability of the heat treatment apparatus and the efficiency of heat conduction to the fiber, but there is no problem as long as the physical properties of the present invention are not impaired. In order to sufficiently exhibit the effect of suppressing crystallization, it is preferable to make the temperature as short as possible at high temperatures. However, if the time is too short, the effect of reducing shrinkage due to heat treatment does not appear, so that the preferable heat treatment time is 0.01 sec or more and 2 hours or less.
上記のようにして結晶化熱量10J/g以上で、140℃×30分の乾熱収縮率が35%以下である抄紙用PPS繊維を得ることができる。 As described above, a PPS fiber for papermaking having a heat of crystallization of 10 J / g or more and a dry heat shrinkage of 140 ° C. × 30 minutes of 35% or less can be obtained.
結晶化熱量は、10J/g以上、さらには15J/g以上、さらに好ましくは20J/g以上がよい。結晶化熱量が10J/g未満では、結晶化していない部分が少なすぎて乾燥工程等で軟化が不十分で融着しにくく、抄紙のバインダーとしての機能が十分でない。 The amount of crystallization heat is 10 J / g or more, further 15 J / g or more, and more preferably 20 J / g or more. If the amount of heat of crystallization is less than 10 J / g, there are too few non-crystallized parts, the softening is insufficient in the drying process and the like, and it is difficult to fuse, and the function as a papermaking binder is not sufficient.
ここで、結晶化熱量の測定はPPS繊維サンプルを約2mg精秤し、示差走査熱量計(島津製作所製、DSC−60)で窒素下、昇温速度10℃/分で昇温し、観察される主発熱ピークの発熱量を測定することにより行った。 Here, about 2 mg of PPS fiber sample was precisely weighed, and the heat of crystallization was measured with a differential scanning calorimeter (manufactured by Shimadzu Corporation, DSC-60), heated at a heating rate of 10 ° C./min under nitrogen. The calorific value of the main exothermic peak was measured.
乾熱収縮率は35%以下が良く、さらに好ましくは20%以下、さらには15%以下がよい。35%よりも大きい場合は、乾熱収縮率が大きすぎて、乾燥工程などで温度が上がったときの収縮が大きくなりすぎて、しわ・膨れが発生したりして、良好な湿式不織布を得ることができない。乾熱収縮率の下限は特に限定するものではなく、小さければ小さいほどよい。よって、0〜35%であることが良い。 The dry heat shrinkage is preferably 35% or less, more preferably 20% or less, and further preferably 15% or less. When it is larger than 35%, the dry heat shrinkage rate is too large, and the shrinkage when the temperature rises in the drying process becomes too large, and wrinkles and blisters are generated to obtain a good wet nonwoven fabric. I can't. The lower limit of the dry heat shrinkage rate is not particularly limited, and the lower the better. Therefore, it is good that it is 0 to 35%.
乾熱収縮率は、JIS L 1013:1999 8.18.2 かせ収縮率(A法)に拠って測定した。 The dry heat shrinkage was measured according to JIS L 1013: 1999 8.18.2 skein shrinkage (Method A).
すなわち、枠周1.125mの検尺機を用いて、120回/minの速度で試料を巻き返し、巻き数20回の小かせを作り、0.088cN/dtexの荷重をかけてかせ長を測った。次に荷重を外し、収縮が妨げられないような方法で140℃の乾燥機中に吊り下げ30分間放置後取り出し、室温まで放置後、再び0.088cN/dtexの荷重をかけてかせ長を測り、次の式によって乾熱収縮率(%)を求め、5回の平均値を算出した。
Sd=[(L―L1)/L]×100
ここに、Sd:乾熱収縮率(%)
L:乾燥前の長さ(mm)
L1:乾燥後の長さ(mm)
本発明のPPS繊維の直径は、抄紙原液中での繊維の分散性を向上し、地合いの良い紙を得る目的で30μm以下が好ましい。より好ましくは25μm以下、最も好ましくは20μm以下である。なお、通常の直接紡糸法によって得られる繊維直径の下限としては5μm程度である。
In other words, using a measuring instrument with a frame circumference of 1.125 m, the sample was rewound at a speed of 120 times / min, a small skein of 20 turns was made, and a load of 0.088 cN / dtex was applied to measure the skein length. It was. Next, remove the load, hang it in a dryer at 140 ° C. for 30 minutes in a way that does not prevent shrinkage, leave it for 30 minutes, leave it to room temperature, apply a load of 0.088 cN / dtex again, and measure the length. The dry heat shrinkage rate (%) was obtained by the following formula, and the average value of 5 times was calculated.
Sd = [(L−L1) / L] × 100
Where, Sd: dry heat shrinkage (%)
L: Length before drying (mm)
L1: Length after drying (mm)
The diameter of the PPS fiber of the present invention is preferably 30 μm or less for the purpose of improving the dispersibility of the fiber in the papermaking stock solution and obtaining a paper with good texture. More preferably, it is 25 μm or less, and most preferably 20 μm or less. In addition, the lower limit of the fiber diameter obtained by a normal direct spinning method is about 5 μm.
また、PPS繊維の捲縮の有無は限定されない。また、捲縮を有する繊維と有しない繊維を混合してもよい。捲縮の有無については、有するものと有しないものとのそれぞれに利点があるためである。捲縮を有するPPS繊維は、繊維同士の絡合性が向上して強度の優れた湿式不織布を得るのに適している。一方、捲縮を有しないPPS繊維は、ムラが小さい均一な湿式不織布を得るのに適している。したがって、用途に応じてPPS繊維に捲縮を施すか否か判断すればよい。捲縮を付与する場合には、一般的に用いられる押し込み式クリンパー等を用いて付与することができる。紙の強度向上と抄紙原液中での繊維同士の絡まりを抑制する目的で捲縮数としては4山/25mm以上、18山/25mm以下が好ましい。なお、捲縮の付与は、80〜95℃の熱処理の前に行ってもよいし、熱処理の後に行ってもよい。 Moreover, the presence or absence of crimp of PPS fiber is not limited. Moreover, you may mix the fiber which has a crimp, and the fiber which does not have. This is because the presence or absence of crimp has advantages in each of those having and not having. PPS fibers having crimps are suitable for obtaining a wet nonwoven fabric having improved strength due to improved entanglement between fibers. On the other hand, PPS fibers that do not have crimps are suitable for obtaining a uniform wet nonwoven fabric with little unevenness. Therefore, it is sufficient to determine whether or not to crimp the PPS fiber according to the application. When crimping is applied, it can be applied using a generally used push-in crimper or the like. The number of crimps is preferably 4 or more / 25 mm or more and 18 or 25 or less for the purpose of improving the strength of the paper and suppressing entanglement between fibers in the papermaking stock solution. The crimping may be performed before the heat treatment at 80 to 95 ° C. or after the heat treatment.
また、繊維長としては1〜15mmが好ましい。より好ましくは1〜7mmである。1mm以上とすることで、繊維同士の絡合力が増し、湿式不織布の強度を高くすることができる。また15mm以下とすることで、繊維同士が絡合してダマになるなどして目付けムラ等が生じるのを防ぐことができる。 The fiber length is preferably 1 to 15 mm. More preferably, it is 1-7 mm. By setting it as 1 mm or more, the entanglement force of fibers increases and the intensity | strength of a wet nonwoven fabric can be made high. Moreover, by setting it as 15 mm or less, it is possible to prevent unevenness of fabric weight and the like from occurring due to entanglement of fibers with each other.
さらに、工程通過性を向上するためや抄紙用に水分散性を向上するために油剤等を付与しても構わない。 Furthermore, an oil agent or the like may be added to improve process passability or to improve water dispersibility for papermaking.
[測定・評価方法]
(1)結晶化熱量
PPS繊維サンプルを約2mg精秤し、示差走査熱量計(島津製作所製、DSC−60)で窒素下、昇温速度10℃/分で昇温し、観察される主発熱ピークの発熱量を測定することにより行った。
[Measurement and evaluation method]
(1) Amount of heat of crystallization About 2 mg of PPS fiber sample is precisely weighed and heated by a differential scanning calorimeter (manufactured by Shimadzu Corporation, DSC-60) at a temperature rising rate of 10 ° C./min. This was done by measuring the peak exotherm.
(2)乾熱収縮率
JIS L 1013:1999 8.18.2 かせ収縮率(A法)に拠って測定した。
枠周1.125mの検尺機を用いて、120回/minの速度で試料を巻き返し、巻き数20回の小かせを作り、0.088cN/dtexの荷重をかけてかせ長を測った。次に荷重を外し、収縮が妨げられないような方法で140℃の乾燥機中に吊り下げ30分間放置後取り出し、室温まで放置後、再び0.088cN/dtexの荷重をかけてかせ長を測り、次の式によって乾熱収縮率(%)を求め、5回の平均値を算出した。
Sd=[(L―L1)/L]×100
ここに、Sd:乾熱収縮率(%)
L:乾燥前の長さ(mm)
L1:乾燥後の長さ(mm)。
(2) Dry heat shrinkage rate Measured according to JIS L 1013: 1999 8.18.2 skein shrinkage rate (Method A).
Using a measuring machine having a frame circumference of 1.125 m, the sample was rewound at a speed of 120 times / min, a small skein with 20 turns was made, and a load of 0.088 cN / dtex was applied to measure the skein length. Next, remove the load, hang it in a dryer at 140 ° C. for 30 minutes in a way that does not prevent shrinkage, leave it for 30 minutes, leave it to room temperature, apply a load of 0.088 cN / dtex again, and measure the length. The dry heat shrinkage rate (%) was obtained by the following formula, and the average value of 5 times was calculated.
Sd = [(L−L1) / L] × 100
Where, Sd: dry heat shrinkage (%)
L: Length before drying (mm)
L1: Length after drying (mm).
(3)水分散性
約1リットルの水に約1gのPPS繊維サンプルを投入し、ミキサー(オスター社製「オスターブレンダーOB−1」)に投入し、13600rpmで攪拌し、繊維束の有無を目視で確認した。
○:15秒間攪拌した後、ほぼ繊維束がなくなっていた。
×:15秒間攪拌した後、繊維束が残った状態であった。
(3) Water dispersibility About 1 g of PPS fiber sample is put into about 1 liter of water, put into a mixer ("Oster Blender OB-1" manufactured by Oster), stirred at 13600 rpm, and visually checked for fiber bundles. Confirmed with.
○: After stirring for 15 seconds, the fiber bundle was almost gone.
X: After stirring for 15 seconds, the fiber bundle remained.
(4)抄紙性テスト
東レ(株)社製‘トルコン(登録商標)’、品番S301(PPS延伸糸、熱固定あり、単繊維繊度1dtex、捲縮数13山/25mm、カット長6mm)と実施例または比較例で得られたPPS繊維とを15:85の重量比率で混合し、繊維濃度約1重量%の水分散液を調合し、手漉き抄紙機(熊谷理機工業(株)社製角型シートマシン自動クーチン付き)を用い目付100g/m2の湿式不織布を得、クーチング処理をした。該不織布を、未乾燥のまま熊谷理機工業(株)社製KRK回転型乾燥機(標準型)に投入し、温度120℃、処理時間約2.5min/回で処理を行い湿式不織布のシワ(乾燥工程通過性)と乾燥後の紙力(紙力)を確認した。乾燥工程通過性では乾燥時のシワについて、収縮シワが少なく連続抄紙可能な程度のものは○、収縮シワや剥がれが発生し連続抄紙不可と推測されるものは×とした。また、紙力についても繊維間で融着して連続抄紙可能と思われるもの○、紙力弱く切断さ推測され連続抄紙不可と推測されるものは×とした。
(4) Papermaking test “Torucon (registered trademark)” manufactured by Toray Industries, Inc., product number S301 (PPS drawn yarn, heat-fixed, single fiber fineness 1 dtex, crimped 13 threads / 25 mm, cut length 6 mm) The PPS fibers obtained in the examples or comparative examples were mixed at a weight ratio of 15:85, an aqueous dispersion having a fiber concentration of about 1% by weight was prepared, and a handmade paper machine (Kumagaya Riki Kogyo K.K. A wet sheet nonwoven fabric with a basis weight of 100 g / m 2 was obtained using a mold sheet machine with automatic couching) and subjected to a couching treatment. The non-woven fabric is put into a KRK rotary dryer (standard type) manufactured by Kumagaya Riki Kogyo Co., Ltd., and is processed at a temperature of 120 ° C. and a processing time of about 2.5 min / time. (Drying process passability) and paper strength (paper strength) after drying were confirmed. In the drying process passability, wrinkles at the time of drying were evaluated as ○ when there was little shrinkage wrinkle and continuous papermaking was possible, and when it was estimated that shrinkage wrinkles or peeling occurred and continuous papermaking was impossible. Also, the paper strength was evaluated as “○”, which was considered to be capable of continuous papermaking by fusing between fibers, and “×” was assumed to be a paper strength weakly cut and inferior continuous papermaking.
[実施例1〜4、比較例1〜5]
(熱処理)
東レ(株)社製‘トルコン(登録商標)’、品番S111(PPS未延伸糸、熱固定処理なし、単繊維繊度3dtex、捲縮数6山/25mm)50gを表1に記載された所定の温度に予めセットした熱風乾燥機(ヤマト科学(株)社製送風定温恒温機DKN601)に投入し、所定の時間熱処理し取り出したあと、水分散性、抄紙性を評価すべく6mmの長さにギロチンカッターでカットした。乾熱収縮率は長繊維の状態で用いた。
[Examples 1 to 4, Comparative Examples 1 to 5]
(Heat treatment)
50 g of “Torcon (registered trademark)” manufactured by Toray Industries, Inc., product number S111 (PPS undrawn yarn, no heat-fixing treatment, single fiber fineness 3 dtex, crimp number 6 crests / 25 mm) It is put into a hot air dryer (Yamato Kagaku Co., Ltd. blast constant temperature thermostatic machine DKN601) set in advance, and after heat treatment for a predetermined time and taken out, the length is 6 mm in order to evaluate water dispersibility and papermaking properties. Cut with a guillotine cutter. Dry heat shrinkage was used in the state of long fibers.
なお、比較例1はS111に特に熱処理を施さなかったものを用いた。 In Comparative Example 1, S111 that was not subjected to heat treatment was used.
比較例5は、30cm角の木枠に一定量のS111を巻きつけて固定し、熱収縮を抑制して定長状態で熱処理を施した。 In Comparative Example 5, a fixed amount of S111 was wound around a wooden frame of 30 cm square and fixed, and heat treatment was performed in a constant length state while suppressing thermal shrinkage.
(評価結果)
上記のようにして熱処理した繊維サンプルについて、カットファイバーを用いて結晶化熱量、水分散性、抄紙性(乾燥工程通過性、紙力)を、長繊維を所定の長さに切り、乾熱収縮率を測定し、その結果を表1にまとめた。
(Evaluation results)
For fiber samples heat-treated as described above, cut fibers are used for crystallization heat, water dispersibility, papermaking properties (drying process passability, paper strength), long fibers are cut to a predetermined length, and dry heat shrinkage The rate was measured and the results are summarized in Table 1.
実施例1〜5の熱処理温度では、結晶化熱量も大きく、乾熱収縮率も小さく、かつ、水分散性も良好な抄紙用PPS繊維を得ることができ、得られた湿式不織布も乾燥工程でのしわが改善でき、かつ、得られた湿式不織布の紙力も十分に強かった。一方、比較例1〜6は、比較例1、2は乾熱収縮率が大きすぎ、乾燥工程でしわが発生した。比較例3〜5は繊維同士の融着が進み、水分散性が悪かった。さらに、結晶化熱量も小さく繊維間の接着力が小さく、得られた紙の紙力が弱く連続抄紙は不可と考えられる。比較例6は、乾熱収縮率が大きく、乾燥工程でしわが発生した。 At the heat treatment temperatures of Examples 1 to 5, it is possible to obtain PPS fibers for papermaking that have a large amount of crystallization heat, a small dry heat shrinkage, and a good water dispersibility. The wrinkle was improved, and the paper strength of the obtained wet nonwoven fabric was sufficiently strong. On the other hand, in Comparative Examples 1 to 6, Comparative Examples 1 and 2 had too large a dry heat shrinkage, and wrinkles were generated in the drying process. In Comparative Examples 3 to 5, fusion of fibers progressed and water dispersibility was poor. Furthermore, the amount of heat of crystallization is small, the adhesive strength between fibers is small, the paper strength of the obtained paper is weak, and continuous papermaking is considered impossible. In Comparative Example 6, the dry heat shrinkage ratio was large, and wrinkles were generated in the drying process.
本発明の抄紙用PPS繊維は、湿式不織布に用いるPPS繊維、特に、湿式不織布のバインダーとして利用可能である。 The PPS fiber for papermaking of the present invention can be used as a PPS fiber used for a wet nonwoven fabric, particularly as a binder for a wet nonwoven fabric.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014080716A (en) * | 2012-09-27 | 2014-05-08 | Toray Ind Inc | Polyphenylene sulfide fiber for nonwoven fabric |
WO2020066815A1 (en) | 2018-09-27 | 2020-04-02 | 東レ株式会社 | Copolymerized polyphenylene sulfide fibers |
WO2024018828A1 (en) * | 2022-07-20 | 2024-01-25 | 東レ株式会社 | Ultrafine polyphenylene sulfide fiber, nonwoven fabric, and methods for producing same |
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2008
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014080716A (en) * | 2012-09-27 | 2014-05-08 | Toray Ind Inc | Polyphenylene sulfide fiber for nonwoven fabric |
WO2020066815A1 (en) | 2018-09-27 | 2020-04-02 | 東レ株式会社 | Copolymerized polyphenylene sulfide fibers |
KR20210060458A (en) | 2018-09-27 | 2021-05-26 | 도레이 카부시키가이샤 | Copolymerized polyphenylene sulfide fiber |
WO2024018828A1 (en) * | 2022-07-20 | 2024-01-25 | 東レ株式会社 | Ultrafine polyphenylene sulfide fiber, nonwoven fabric, and methods for producing same |
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