JPH02259189A - Sheet-shaped molded product with excellent alkali resistance - Google Patents
Sheet-shaped molded product with excellent alkali resistanceInfo
- Publication number
- JPH02259189A JPH02259189A JP1078019A JP7801989A JPH02259189A JP H02259189 A JPH02259189 A JP H02259189A JP 1078019 A JP1078019 A JP 1078019A JP 7801989 A JP7801989 A JP 7801989A JP H02259189 A JPH02259189 A JP H02259189A
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- fiber
- fibers
- molded product
- weight
- 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
Links
- 239000003513 alkali Substances 0.000 title claims description 25
- 239000000835 fiber Substances 0.000 claims abstract description 111
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 19
- 229920000915 polyvinyl chloride Polymers 0.000 claims abstract description 19
- 239000000203 mixture Substances 0.000 claims abstract description 18
- 239000004695 Polyether sulfone Substances 0.000 claims abstract description 16
- 229920002492 poly(sulfone) Polymers 0.000 claims abstract description 16
- 229920006393 polyether sulfone Polymers 0.000 claims abstract description 16
- 239000011230 binding agent Substances 0.000 claims abstract description 14
- 230000004927 fusion Effects 0.000 claims description 8
- 239000007788 liquid Substances 0.000 abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 17
- 238000009987 spinning Methods 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 14
- 239000002904 solvent Substances 0.000 abstract description 14
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 abstract description 12
- -1 polyethylene Polymers 0.000 abstract description 8
- 239000004698 Polyethylene Substances 0.000 abstract description 5
- 229920000573 polyethylene Polymers 0.000 abstract description 5
- 238000002166 wet spinning Methods 0.000 abstract description 5
- 230000001112 coagulating effect Effects 0.000 abstract 1
- 230000014759 maintenance of location Effects 0.000 description 33
- 238000002156 mixing Methods 0.000 description 11
- 239000011550 stock solution Substances 0.000 description 10
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 9
- 229920000642 polymer Polymers 0.000 description 9
- 238000006116 polymerization reaction Methods 0.000 description 9
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 8
- 239000004744 fabric Substances 0.000 description 8
- 230000015271 coagulation Effects 0.000 description 7
- 238000005345 coagulation Methods 0.000 description 7
- 239000004745 nonwoven fabric Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 230000035699 permeability Effects 0.000 description 6
- 238000000465 moulding Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 4
- 239000004926 polymethyl methacrylate Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000004580 weight loss Effects 0.000 description 4
- 239000004743 Polypropylene Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000004925 Acrylic resin Substances 0.000 description 2
- 229920000178 Acrylic resin Polymers 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- FDPIMTJIUBPUKL-UHFFFAOYSA-N dimethylacetone Natural products CCC(=O)CC FDPIMTJIUBPUKL-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- QELJHCBNGDEXLD-UHFFFAOYSA-N nickel zinc Chemical compound [Ni].[Zn] QELJHCBNGDEXLD-UHFFFAOYSA-N 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910001923 silver oxide Inorganic materials 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
- B01D39/163—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin sintered or bonded
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
- Nonwoven Fabrics (AREA)
- Woven Fabrics (AREA)
- Paper (AREA)
- Cell Separators (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、耐アルカリ性の要求されるフィルター、電池
用セパレーク−1工業用ワイパーに有用なシート状成型
物に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a sheet-like molded product useful for filters requiring alkali resistance and battery separator-1 industrial wipers.
〈従来の技術〉
近年シート状成型物の用途が拡大され、種々の工業用途
、例えば工業用フィルター1、電池用セパレーター、工
業用ワイパーなどに多く使用されている。<Prior Art> In recent years, the applications of sheet-like molded products have expanded, and they are now widely used in various industrial applications, such as industrial filters 1, battery separators, and industrial wipers.
周知のようにフィルター、セパレーター、ワイパー等に
使用されるシー1〜状成型物は適度な通気性、通液性、
適切な強度、厚み、密度および高度な保液性等の性能が
要求され、更に近年産業の高度化に伴って、耐薬品性が
要求されている。例えば、廃酸、廃アルカリ処理フィル
ターまたは電池用セパレーター等については強酸、強ア
ルカリ液中で用いてもほとんど溶出したり、劣化したり
しない高度の耐薬品性が要求されている。As is well known, the sea-shaped molded products used for filters, separators, wipers, etc. have appropriate air permeability, liquid permeability,
Performance such as appropriate strength, thickness, density, and high liquid retention properties are required, and with the recent advancement of industry, chemical resistance is also required. For example, waste acid and waste alkali treatment filters, battery separators, and the like are required to have a high degree of chemical resistance that hardly dissolves or deteriorates even when used in strong acid or strong alkaline solutions.
しかし、従来のスパンボンド不織布、乾式不織布、湿式
不織布等のシート状成型物においては、耐薬品性に優れ
るものの、通気性、通液性、保液性、紙強度などの面で
不十分であったり、また逆に十分な通気性、通液性、保
液性を有するものの十分な耐薬品性がないなど、いまだ
十分満足すべき耐アルカリ性を有するシート状成型物か
えられていないのが現状である。However, although conventional sheet-like molded products such as spunbond nonwoven fabrics, dry nonwoven fabrics, and wet nonwoven fabrics have excellent chemical resistance, they are insufficient in terms of air permeability, liquid permeability, liquid retention, paper strength, etc. On the other hand, although it has sufficient air permeability, liquid permeability, and liquid retention, it does not have sufficient chemical resistance.Currently, sheet-shaped molded products with satisfactory alkali resistance have not been replaced. be.
特に電池用セパレーターについては高温時の耐アルカリ
性に優れ、しかも高い保液性を有することが要求される
などより改良が望まれている。In particular, battery separators are desired to be improved as they are required to have excellent alkali resistance at high temperatures and high liquid retention.
〈発明が解決しようとする課題〉
本発明は、耐アルカリ性に優れたシート状成型物を提供
し、耐アルカリ性、特に高温時で要求される工業用フィ
ルター、工業用ワイパー等にまた、保液性を高めること
によって電池用セパレーターに有用なシート状成型物を
提供することにある。<Problems to be Solved by the Invention> The present invention provides a sheet-like molded product with excellent alkali resistance, and is suitable for use in industrial filters, industrial wipers, etc. that require alkali resistance, especially at high temperatures, and also has liquid retention properties. The object of the present invention is to provide a sheet-like molded product useful as a battery separator by increasing the
〈課題を解決するための手段〉
本発明は、ポリサルホンおよび/またはポリエーテルザ
ルホンを少なくとも15重量%、ポリ塩化ビニルを少な
くとも20重量%含有する組成物で構成された繊維50
重量%以上からなる耐アルカリ性に優れたシート状成型
物にある。<Means for Solving the Problems> The present invention provides fibers 50 made of a composition containing at least 15% by weight of polysulfone and/or polyethersulfone and at least 20% by weight of polyvinyl chloride.
It is a sheet-like molded product with excellent alkali resistance consisting of % by weight or more.
本発明のシート状成型物の形状は、乾式または湿式の不
織布あるいは紙、編織物などであり、用途に応じ最良の
選択が可能である。たとえば工業用フィルター用途には
成型物の強度を向上するうえで織物が最適であり、また
電池用セパレーターについては均一性の面から湿式抄紙
による紙が最も望ましい。The shape of the sheet-like molded product of the present invention may be dry or wet nonwoven fabric, paper, knitted fabric, etc., and the best choice can be made depending on the application. For example, woven fabrics are most suitable for industrial filter applications in terms of improving the strength of molded products, and for battery separators, paper made by wet papermaking is most desirable from the standpoint of uniformity.
本発明のシート状成型物はポリサルホンおよび/または
ポリエーテルサルホンを少なくとも15重量%、ポリ塩
化ビニルを少なくとも20重量%含有する組成物からな
る繊維が50重量%以上含んで構成されることが必要で
ある。The sheet-like molded product of the present invention must contain at least 50% by weight of fibers made of a composition containing at least 15% by weight of polysulfone and/or polyethersulfone and at least 20% by weight of polyvinyl chloride. It is.
ポリサルホンおよび/またはポリエーテルサルホンを少
なくとも15重量%、ポリ塩化ビニルを少なくとも20
重量%含有する組成物で構成された繊維(以下PSv繊
維と称す)は、耐アルカリ性に優れしかも高い保液性を
有するものである。このためPSv繊維を主成分とする
シート状成型物は十分な耐アルカリ性および保液性を有
し、シート状成型物中におけるpsv繊維の含有率が5
0重量%以上であれば本発明の目的を達成することがで
きる。At least 15% by weight of polysulfone and/or polyethersulfone, at least 20% by weight of polyvinyl chloride
Fibers (hereinafter referred to as PSv fibers) composed of a composition containing % by weight have excellent alkali resistance and high liquid retention properties. Therefore, a sheet-like molded product containing PSv fiber as a main component has sufficient alkali resistance and liquid retention, and the content of PSV fiber in the sheet-like molded product is 5.
If the amount is 0% by weight or more, the object of the present invention can be achieved.
PSv繊維を主成分とするシート状成型物としては上述
したごとく不織布、紙、編織物等があるが、不織布、紙
とする場合には熱融着によってシート状成型物としての
強度を与えることが耐アルカリ性を保持する上で好まし
い。PSv繊維自体を熱融着させてシート状成型物を得
ることも可能であるが、psv繊維自体が有する空隙の
みならず、得られたシート状成型物の空隙をなくしシー
ト状成型物の保液性を損なう結果となる。このため適切
なバインダー繊維を混合し熱融着成型を行なうことがの
ぞましい。As mentioned above, there are nonwoven fabrics, paper, knitted fabrics, etc. as sheet-like molded products whose main component is PSv fibers, but in the case of non-woven fabrics or paper, it is possible to give the strength of the sheet-like molded product by heat fusion. This is preferable in terms of maintaining alkali resistance. Although it is possible to obtain a sheet-like molded product by thermally fusing the PSv fibers themselves, it is possible to eliminate not only the voids in the PSV fibers themselves but also the voids in the resulting sheet-like molded product to improve liquid retention in the sheet-like molded product. This results in loss of sexuality. For this reason, it is desirable to mix appropriate binder fibers and perform heat-fusion molding.
本発明のシート状成型物に用いられるバインダー繊維は
熱融着温度が125℃以下、好ましくは120℃以下の
繊維で、その混合比として10〜50重量%、好ましく
は15〜50重景%用重量れる。The binder fiber used in the sheet-like molded product of the present invention has a heat-fusion temperature of 125°C or lower, preferably 120°C or lower, and the mixing ratio thereof is 10 to 50% by weight, preferably 15 to 50% by weight. It's heavy.
バインダー繊維の熱融着温度が125℃を超えるとps
v繊維の熱融着温度に近くなり、熱融着成型時にpsv
繊維も熱融着を起こし得られたシート状成型物の保液性
を損なう。バインダー繊維の混合比が10重量%未満で
は得られるシート状成型物の強度が不十分となる。バイ
ンダー繊維の混合比が10重量%未満でも熱融着成型温
度を高く設定することによってシート状成型物の強度を
維持することが可能であるが、反面シート状成型物の空
隙を低下し保液性を損なう結果となる。以上の如くバイ
ンダー繊維の熱融着温度と混合比は得られるシート状成
型物の強度と保液性の関係から考慮されるものである。If the heat fusion temperature of the binder fiber exceeds 125℃, ps
It is close to the heat fusion temperature of V fibers, and the psv during heat fusion molding.
The fibers also cause thermal fusion, impairing the liquid retention properties of the resulting sheet-like molded product. If the blending ratio of binder fibers is less than 10% by weight, the strength of the resulting sheet-like molded product will be insufficient. Even if the blending ratio of binder fibers is less than 10% by weight, it is possible to maintain the strength of the sheet-like molded product by setting the heat-fusion molding temperature high, but on the other hand, it reduces the voids of the sheet-like molded product and reduces liquid retention. This results in loss of sexuality. As described above, the heat fusion temperature and mixing ratio of the binder fibers are taken into consideration from the relationship between the strength and liquid retention properties of the resulting sheet-like molded product.
本発明のシート状成型物に用いられるバインダー繊維と
してはポリエチレン系繊維、ポリ塩化ビニル系繊維等が
あるが、これらバインダー繊維も耐アルカリ性を有する
ことが好ましく、得られたシート状成型物の耐アルカリ
性を満足できるものであれば特に限定されるものではな
い。Binder fibers used in the sheet-like molded product of the present invention include polyethylene fibers and polyvinyl chloride fibers, but it is preferable that these binder fibers also have alkali resistance, and the resulting sheet-like molded product has alkali resistance. There is no particular limitation as long as it satisfies the following.
編織物として使用する場合は上記のようなハインダー繊
維は必ずしも必要ではない。When used as a knitted fabric, the above-mentioned hinder fibers are not necessarily required.
本発明のシート状成型物のその他の成分としては、シー
ト状成型物の耐アルカリ性、保液性を満足させるもので
あれば特に制限するものではないが、耐アルカリ性を有
するものが好ましく、たとえばポリエチレン、ポリプロ
ピレン、ポリ塩化ビニル等の繊維があげられる。Other components of the sheet-like molded product of the present invention are not particularly limited as long as they satisfy the alkali resistance and liquid retention properties of the sheet-like molded product, but those having alkali resistance are preferred, such as polyethylene Examples include fibers such as , polypropylene, and polyvinyl chloride.
本発明のシート状成型物は耐アルカリ性を有することが
重要であるが、具体的には、30重量%KOI+水溶液
に浸せきし、常圧沸騰中1時間後の繊維減量が2.0重
量%以下であり、この値は同一手法により測定されるポ
リプロピレン繊維からなる不織布の値を下回るものであ
る。It is important for the sheet-like molded product of the present invention to have alkali resistance. Specifically, when immersed in a 30 wt% KOI + aqueous solution, the fiber loss after 1 hour in normal pressure boiling is 2.0 wt% or less. This value is lower than the value of a nonwoven fabric made of polypropylene fibers measured by the same method.
さらに本発明のシート状成型物は高い保液性を有するが
この目安としては、以下の測定法による値が220重量
%以上である。この保液性はシート状成型物自体の空隙
によって得られるものだけでなく、psv繊維自体が有
する空隙によって得られるものであり、高い保液性を必
要とする用途に優れた効果を発揮する。Further, the sheet-like molded product of the present invention has a high liquid retention property, and as a guideline, the value determined by the following measurement method is 220% by weight or more. This liquid retention property is obtained not only by the voids in the sheet-like molded product itself, but also by the voids in the PSV fiber itself, and exhibits an excellent effect in applications requiring high liquid retention property.
シート状成型物の保液性(重量%)評価法シートの任意
の部分より5 cm X 5 cmの試験片を3枚切り
出し、秤量(旧)する。この試験片を水中(20℃)に
1時間漫せき後、十分液滴を切り重量(wi)を測定し
、以下の式より算出した。Evaluation method for liquid retention (weight %) of sheet-like molded product: Cut out three test pieces of 5 cm x 5 cm from any part of the sheet and weigh them (old). After soaking this test piece in water (20° C.) for 1 hour, a droplet was thoroughly cut off, the weight (wi) was measured, and the weight (wi) was calculated using the following formula.
さらにより保液性を向上させる目的で本発明のシート状
成型物に界面活性剤などによる表面処理を施すことも可
能であり、本発明シート状成型物の保液性をより向上さ
せることが出来る。Furthermore, for the purpose of further improving the liquid retention property, it is possible to subject the sheet-like molded product of the present invention to surface treatment with a surfactant, etc., and the liquid-retention property of the sheet-like molded product of the present invention can be further improved. .
本発明のシート状成型物に使用されるpsv繊維は、ポ
リサルホンおよび/またはポリエーテルサルホンとポリ
塩化ビニルを含有する組成物をジメチルアセトアミド、
ジメチルホルムアミド、ジメチルスルホキシド、または
アセトンに溶解分散させ、好ましくは湿式紡糸方式で繊
維賦型することによって得られる。The PSV fiber used in the sheet-like molded product of the present invention is prepared by dimethylacetamide, a composition containing polysulfone and/or polyethersulfone, and polyvinyl chloride.
It is obtained by dissolving and dispersing it in dimethylformamide, dimethyl sulfoxide, or acetone, and forming the fiber into fibers, preferably by a wet spinning method.
PSv繊維の組成物はポリサルホンおよび/またはポリ
エーテルサルホンとポリ塩化ビニルさらに必要に応じそ
の他の重合体を混合することができるが、繊維中にポリ
サルホンおよび/またはポリエーテルサルホンを少なく
とも15重量%含有することが必要である。The composition of PSv fibers includes polysulfone and/or polyethersulfone, polyvinyl chloride, and if necessary, other polymers may be mixed, but the fiber contains at least 15% by weight of polysulfone and/or polyethersulfone. It is necessary to contain
PSv繊維の構成成分であるポリサルホン、ポリエーテ
ルサルホンは下記に示す分子構造を有するものであり、
重合度は特に限定するものではない。Polysulfone and polyethersulfone, which are the constituent components of PSv fiber, have the molecular structure shown below.
The degree of polymerization is not particularly limited.
ポリサルホン;
H3
ポリエーテルサルホン;
ポリサルホンおよび/またはポリエーテルサルホンの含
有量が15重量%未満になると得られた繊維の耐熱寸法
安定性が低下し、熱融着成型時における工程通過性の低
下または編織物とした場合の熱寸法安定性を低下させる
要因となる。具体的には清水収縮率が25%以下である
ことが必要であり、この数値を下回る場合は、上述した
バインダー繊維を使用し、組成比を変更することにより
目的とするシート状成型物をえることが可能である。ま
た編織物として供する場合においても実用上十分といえ
る。Polysulfone; H3 Polyethersulfone; When the content of polysulfone and/or polyethersulfone is less than 15% by weight, the heat-resistant dimensional stability of the obtained fiber decreases, and process passability during heat fusion molding decreases. Alternatively, it becomes a factor that reduces thermal dimensional stability when made into a knitted fabric. Specifically, it is necessary that the fresh water shrinkage rate is 25% or less, and if it is less than this value, the desired sheet-like molded product can be obtained by using the above-mentioned binder fiber and changing the composition ratio. Is possible. It can also be said that it is practically sufficient when used as a knitted fabric.
ポリ塩化ビニルの含有量が20重量%未満では得られた
繊維の強度が十分でな(シート状成型物を得る上で実用
に供しがたくなる。If the content of polyvinyl chloride is less than 20% by weight, the strength of the obtained fibers will not be sufficient (it will be difficult to put it to practical use in obtaining sheet-like molded products).
PSv繊維に用いられるポリ塩化ビニルの重合度(JI
S−6721による測定)は、800〜2500、好ま
しくは900〜1800である。Polymerization degree of polyvinyl chloride used for PSv fiber (JI
S-6721) is 800-2500, preferably 900-1800.
重合度800未満では繊維強度が1.2g/d未満とな
りシート状成型物を生成する上で不十分であり、また重
合度が2500を超えると紡糸原液のゲル化が発生しや
すくなり、安定に繊維を製造することが困難になる。If the degree of polymerization is less than 800, the fiber strength will be less than 1.2 g/d, which is insufficient for producing a sheet-like molded product, and if the degree of polymerization exceeds 2,500, gelation of the spinning dope is likely to occur, making it unstable. It becomes difficult to manufacture fibers.
PSv繊維のポリサルホンおよび/またはポリエーテル
サルホンおよびポリ塩化ビニル以外の組成成分としては
耐アルカリ性に優れ、しかも紡糸溶媒であるジメチルア
セトアミド、ジメチルホルムアミ下、ジメチルスルホキ
。シトまたはアセトンに溶解可能な重合体から選択され
る。Compositional components other than polysulfone and/or polyethersulfone and polyvinyl chloride of PSv fibers include excellent alkali resistance and spinning solvents such as dimethylacetamide, dimethylformamide, and dimethylsulfochloride. selected from polymers that are soluble in acetone or acetone.
これらの重合体としては、ポリメチルメタクリレート等
のアクリル樹脂、ポリスチレン、ABS樹脂、スチレン
/アクリル酸エステル共重合体等があげられるが、繊維
賦型を行なう上ではポリメチルメタクリレート等のアク
リル樹脂が最も好ましい。更にこれらの重合体の含有量
は65重量%を超えないことが好ましい。These polymers include acrylic resins such as polymethyl methacrylate, polystyrene, ABS resins, styrene/acrylic acid ester copolymers, etc., but acrylic resins such as polymethyl methacrylate are the most suitable for fiber shaping. preferable. Furthermore, it is preferred that the content of these polymers does not exceed 65% by weight.
本発明のシート状成型物の耐アルカリ性を維持するため
にはpsv繊維も耐アルカリ性を有することが必要であ
り、具体的には上述したKOH30重景%水溶液中に浸
せきし、常圧沸騰状態で1時間放置後の繊維減量が2.
0重量%以下、好ましくは1.5重量%以下である。In order to maintain the alkali resistance of the sheet-like molded product of the present invention, it is necessary that the PSV fibers also have alkali resistance. Specifically, the PSV fibers must be immersed in the above-mentioned KOH 30% aqueous solution and boiled at normal pressure. The fiber weight loss after leaving for 1 hour is 2.
It is 0% by weight or less, preferably 1.5% by weight or less.
更に本発明のシート状成型物の保液性を高めるためにP
Sv繊維の保液性として、以下に示す測定方式による保
液率が25重量%以上であることが重要である。このP
Sv繊維の保液性は主に湿式紡糸方式によって得られる
繊維中の空隙によって与えられるものであり、これはシ
ート状成型物の保液性を高めるのに有効である。Furthermore, in order to improve the liquid retention property of the sheet-like molded product of the present invention, P
Regarding the liquid retention property of the Sv fiber, it is important that the liquid retention rate as measured by the measurement method shown below is 25% by weight or more. This P
The liquid retention properties of Sv fibers are mainly provided by voids in the fibers obtained by wet spinning, and this is effective in increasing the liquid retention properties of sheet-like molded products.
繊維の保液率の測定方法
繊維を水中に24時間浸せき後、加重LOGで10分間
遠心脱水機で脱水し、その繊維重量(W、)を測定する
。この繊維の乾燥重量(W2)を測定し、保液率を以下
の式より算出する。Method for Measuring Liquid Retentivity of Fibers After soaking fibers in water for 24 hours, they are dehydrated using a centrifugal dehydrator for 10 minutes using weighted LOG, and the fiber weight (W) is measured. The dry weight (W2) of this fiber is measured, and the liquid retention rate is calculated using the following formula.
PSv繊維の断面形状は特に限定されるものではなく、
耐アルカリ性、保液性、繊維物性を損なうものでなけれ
ば種々選択が可能である。本発明のシーI・状成型物の
保液性を高める目的で繊維断面を7字、十字等の異形断
面に変え繊維間の空隙を増すことは有効なことである。The cross-sectional shape of the PSv fiber is not particularly limited,
Various selections can be made as long as they do not impair alkali resistance, liquid retention, and fiber properties. In order to improve the liquid retention of the C-shaped molded product of the present invention, it is effective to change the cross section of the fibers to an irregularly shaped cross section such as a figure 7 or a cross to increase the voids between the fibers.
またpsv繊維の繊度は、シート状成型物の厚みを薄く
する上では細デニールであることが好ましい、好ましく
は3デニール以下、更に好ましくは2デニール以下であ
るが、シート状成型物の用途に応じて適時選択される。In addition, the fineness of the PSV fiber is preferably a fine denier in order to reduce the thickness of the sheet-like molded product, preferably 3 deniers or less, more preferably 2 deniers or less, but it depends on the use of the sheet-like molded product. selected in a timely manner.
psv繊維は好ましくは湿式紡糸方式によって製造され
るが、湿式紡糸における溶剤としてはジメチルアセトア
ミド、ジメチルホルムアミドが有利に用いられるが、そ
の他ジメチルスルホキシド、アセトンも利用できる。PSV fibers are preferably produced by a wet spinning method, and dimethylacetamide and dimethylformamide are advantageously used as solvents in wet spinning, but dimethyl sulfoxide and acetone can also be used.
これらの溶媒にポリサルホンおよび/またはポリエーテ
ルサルホンとポリ塩化ビニル更に適宜他の重合体を混合
溶解分散し、紡糸原液が調製される。紡糸原液の50℃
における粘度としては100〜2000ポイズ、好まし
くは150〜1000ポイズとすることがよく、これら
の値になるように原液固形分濃度が調製されるが、固形
分濃度はゲル化を防止する上で50重量%以下が好まし
い。A spinning stock solution is prepared by mixing and dispersing polysulfone and/or polyethersulfone, polyvinyl chloride, and other appropriate polymers in these solvents. 50℃ of spinning dope
The viscosity of the stock solution is preferably 100 to 2000 poise, preferably 150 to 1000 poise, and the solid content concentration of the stock solution is adjusted to these values. It is preferably less than % by weight.
これらの重合体の他に耐熱安定剤等を少量添加すること
も可能である。In addition to these polymers, it is also possible to add a small amount of a heat stabilizer or the like.
得られた紡糸原液は紡糸口金より凝固浴中に押し出され
繊維に賦型される。紡糸口金の大きさは目標とする繊維
の繊度に応じ適時選択される。凝固浴中の凝固剤として
は重合体の非溶媒である水、アルコール等が使用される
が工業的には水が最も好ましい。凝固浴中の凝固剤と溶
剤の比率および温度は重合体組成に応じ適宜設定が可能
である。凝固浴をでた未延伸糸は洗浄、延伸を行ない機
械的な性質を付与され乾燥または未乾燥のまま補集され
、本発明のシート状成型物の原料として使用される。The obtained spinning dope is extruded from a spinneret into a coagulation bath and shaped into fibers. The size of the spinneret is appropriately selected depending on the target fineness of the fiber. As the coagulant in the coagulation bath, water, alcohol, etc., which are non-solvents of the polymer, are used, but water is most preferred from an industrial standpoint. The ratio and temperature of the coagulant and solvent in the coagulation bath can be set as appropriate depending on the polymer composition. The undrawn yarn that has left the coagulation bath is washed, stretched, imparted with mechanical properties, collected dry or undried, and used as a raw material for the sheet-like molded product of the present invention.
シート状成型物の製造方式としては種々選択が可能であ
るが、PSv繊維の特徴および製造方式から湿式抄紙が
好ましい。湿式抄紙方式は繊維を乾燥することなく適切
な長さに切断し、バインダー繊維と水中で分散し、抄紙
することによってシート状成型物を得ることができ、繊
維の製造工程中に乾燥工程を必要とせずエネルギーコス
トが軽減されるとともに、均一なシート状成型物が得ら
れるためである。PSv繊維のカット長は通常合成繊維
を湿式抄紙する場合に適用される長さのものが用いられ
る。Various methods can be selected as the manufacturing method for the sheet-like molded product, but wet papermaking is preferred from the characteristics of PSv fibers and the manufacturing method. In the wet papermaking method, a sheet-like molded product can be obtained by cutting the fibers to an appropriate length without drying them, dispersing them in water with binder fibers, and making paper, which requires a drying process during the fiber manufacturing process. This is because energy costs can be reduced without causing damage, and a uniform sheet-like molded product can be obtained. The cut length of the PSv fibers is usually a length that is applied when wet-processing synthetic fibers.
さらにPSv繊維を乾燥しフィラメントとじて巻き取り
、編織物としてシート状成型物を得ることも可能である
。Furthermore, it is also possible to dry the PSv fibers and wind them up into filaments to obtain a sheet-like molded product as a knitted fabric.
〈実施例〉 以下、本発明を実施例により説明する。<Example> The present invention will be explained below using examples.
実施例1
溶剤としてジメチルアセトアミドを用い、重合度110
0のポリ塩化ビニル(以下PvCという)と重合度98
0のポリメチルメタクリレート(以下P聞Aという)、
ポリサルホン(以下PSFという)を30150/20
の混合比(重量%)で溶剤に溶解分散させ、紡糸原液を
えた。この時の固形分濃度は50℃における粘度が20
0ポイズ付近になるように調製した。この紡糸原液をジ
メチルアセトアミド60重量%、脱イオン水40重量%
、温度30℃の凝固浴中へ吐出し、未延伸糸を得た。こ
の未延伸糸を沸水中で約3倍延伸を行ない、さらに沸水
中で洗浄を行い、繊度0.93デニール、強度1.29
g/d、伸度33.1%の繊維(以下psv繊維No、
1という)を得た。この繊維のKOI+処理後の減量
率は0.93重量%、保液率は45.0%、導水収縮率
は18.。Example 1 Using dimethylacetamide as a solvent, the degree of polymerization was 110.
0 polyvinyl chloride (hereinafter referred to as PvC) and a polymerization degree of 98
0 polymethyl methacrylate (hereinafter referred to as P-A),
Polysulfone (hereinafter referred to as PSF) 30150/20
The mixture was dissolved and dispersed in a solvent at a mixing ratio (wt%) to obtain a spinning stock solution. At this time, the solid content concentration has a viscosity of 20 at 50°C.
It was adjusted to be around 0 poise. This spinning stock solution was mixed with 60% by weight of dimethylacetamide and 40% by weight of deionized water.
The mixture was discharged into a coagulation bath at a temperature of 30° C. to obtain an undrawn yarn. This undrawn yarn was stretched approximately 3 times in boiling water, and then washed in boiling water, resulting in a fineness of 0.93 denier and a strength of 1.29.
g/d, fiber with elongation of 33.1% (hereinafter referred to as psv fiber No.
1) was obtained. The weight loss rate of this fiber after KOI+ treatment is 0.93% by weight, the liquid retention rate is 45.0%, and the water conduction shrinkage rate is 18. .
%であった。%Met.
この繊維を乾燥することなく補集し、湿潤状態で6an
に切断し、バインダー繊維として熱融着温度110℃の
塩化ビニル/酢酸ビニル共重合体繊維(2デニール、カ
ット長6胴、以下VA織繊維いう)と第1表に示す混合
比(重量%)で湿式抄紙し、115℃で熱融着成型し目
付50g/rrrの第1表に示すシート状成型物(シー
トNo、 1〜5)を得た。The fibers are collected without drying, and 6an is collected in a wet state.
Vinyl chloride/vinyl acetate copolymer fiber (2 denier, cut length 6 body, hereinafter referred to as VA woven fiber) with a heat fusing temperature of 110°C was used as a binder fiber and the mixing ratio (wt%) shown in Table 1. The paper was wet-paper-formed at 115° C. and then heat-fused and molded at 115° C. to obtain sheet-like molded products (sheet Nos. 1 to 5) shown in Table 1 having a basis weight of 50 g/rrr.
第1表 実施例2 実施例1と同様な方法で製造したpsv繊維N。Table 1 Example 2 PSV fiber N produced in the same manner as in Example 1.
1とポリプロピレン繊維(繊度1.3デニール、カット
長6mm)およびVA織繊維第2表に示す混合比(重量
%)で湿式抄紙し、115℃で熱融着成型し目付5(I
g/n?の第2表に示すシート状成型物(シー) No
、 2〜9)を得た。1, polypropylene fiber (fineness 1.3 denier, cut length 6 mm) and VA woven fiber at the mixing ratio (wt%) shown in Table 2.
g/n? Sheet-like molded products (sheets) shown in Table 2 No.
, 2-9) were obtained.
実施例3 実施例1と同様な方法で製造したpsv繊維No。Example 3 PSV fiber No. manufactured by the same method as Example 1.
1とVA織繊維80/20の混合比(M量%)で湿式抄
紙し、第3表に示す熱融着温度で熱融着成型し目付50
g/rrrの第3表に示すシート状成型物(シートNo
、 10〜13)を得た。1 and VA woven fibers in a mixing ratio (M amount%) of 80/20, and was heat-fused and molded at the heat-fusion temperature shown in Table 3 to obtain a fabric weight of 50.
Sheet-like molded products shown in Table 3 of g/rrr (sheet No.
, 10-13) were obtained.
第3表 実施例4 実施例1と同様な方法で製造したpsv繊維N。Table 3 Example 4 PSV fiber N produced in the same manner as in Example 1.
1とVA織繊維替わりに熱融着温度120℃のポリエチ
レン合成パルプを80/20の混合比えた。この時の固
形分濃度は50℃における粘度が200ポイズ付近にな
るように調製した。1 and a polyethylene synthetic pulp having a heat fusing temperature of 120° C. instead of VA woven fiber was mixed in an 80/20 ratio. The solid content concentration at this time was adjusted so that the viscosity at 50°C was around 200 poise.
この紡糸原液をジメチルアセトアミド70重量%、脱イ
オン水30重量%、温度30℃の凝固浴中へ吐出し、未
延伸糸を得た。この未延伸糸を70℃の温水中で約4倍
延伸を行ない、さらに導水中で洗浄を行い、繊維(PS
V繊維No、 2〜5)を得た。得られた繊維の性能を
第4表に示した。This spinning stock solution was discharged into a coagulation bath containing 70% by weight of dimethylacetamide and 30% by weight of deionized water at a temperature of 30°C to obtain an undrawn yarn. This undrawn yarn was drawn approximately 4 times in warm water at 70°C, and then washed in water to produce fibers (PS).
V fibers No. 2 to 5) were obtained. The performance of the obtained fibers is shown in Table 4.
第4表
(重量%)で湿式抄紙し、125℃で熱融着成型し目付
50g/r4のシート状成型物(シートNo、 I 4
)を得た。このシート4Je成型物の保液率は323
%で強度も実用に耐え得るものであった。A sheet-like molded product with a basis weight of 50 g/r4 was made by wet paper making according to Table 4 (wt%) and heat-sealed at 125°C (Sheet No. I 4
) was obtained. The liquid retention rate of this sheet 4Je molded product is 323
%, the strength was also suitable for practical use.
比較例1 実施例1と同様な方法で製造したpsv繊w、N。Comparative example 1 PSV fibers w and N produced in the same manner as in Example 1.
1とVA織繊維替わりに熱融着温度132℃のポリエチ
レン合成パルプを80/20の混合比で湿式抄紙し、1
35℃で熱融着成型し目付50g/rrrのシート状成
型物を得た。このシート状成型物の強度は十分であった
が、保液率は130%と低水準であった。In place of 1 and VA woven fibers, polyethylene synthetic pulp with a heat fusing temperature of 132°C was wet-paper-made at a mixing ratio of 80/20, and 1
A sheet-like molded product with a basis weight of 50 g/rrr was obtained by heat-fusion molding at 35°C. Although the strength of this sheet-like molded product was sufficient, the liquid retention rate was at a low level of 130%.
また同様な組成で混合抄紙し、115℃で熱融着成型を
試みたが繊維は融着せず十分な強度を有するシート状成
型物は得られなかった。In addition, an attempt was made to make a mixed paper with the same composition and heat-fusion mold it at 115°C, but the fibers did not fuse and a sheet-like molded product with sufficient strength could not be obtained.
実施例5
溶剤としてジメチルアセトアミドを用い、重合度110
0のpvcとPSFを第4表に示す組成比(重量%)で
溶剤に溶解分散させ、紡糸原液を実施例6
PVC/ポリエーテルサルホン組成比(重量%)を70
/30として実施例5と同様な方法で繊度1.01デニ
ール、強度2.1g/d、伸度24%、湧水収縮率18
.2%の繊維(PSV繊維N06)を得た。この繊維の
KOH処理後の減量率および保液率を測定したところ、
それぞれ1.4重量%、61%であった。Example 5 Using dimethylacetamide as a solvent, the degree of polymerization was 110.
PVC of 0 and PSF were dissolved and dispersed in a solvent at the composition ratio (wt%) shown in Table 4, and the spinning stock solution was prepared using Example 6 PVC/polyethersulfone composition ratio (wt%) of 70.
/30 in the same manner as in Example 5, with a fineness of 1.01 denier, a strength of 2.1 g/d, an elongation of 24%, and a spring shrinkage rate of 18.
.. A 2% fiber (PSV fiber N06) was obtained. When the weight loss rate and liquid retention rate of this fiber after KOH treatment were measured,
They were 1.4% by weight and 61%, respectively.
実施例7
溶剤としてジメチルアセトアミドを用い、重合度110
0(7)PVCとPMMA、 PSI’を第5表ニ示ス
組成比(重量%)で溶剤に溶解分散させ、紡糸原液をえ
た。この時の固形分濃度は50℃における粘度が200
ボイズ付近になるように調製した。Example 7 Using dimethylacetamide as a solvent, the degree of polymerization was 110.
0(7)PVC, PMMA, and PSI' were dissolved and dispersed in a solvent at the composition ratios (wt%) shown in Table 5 to obtain a spinning dope. At this time, the solid content concentration has a viscosity of 200 at 50°C.
It was adjusted so that it was near Boise.
この紡糸原液をジメチルアセトアミド60重量%、脱イ
オン水40重量%、温度30゛Cの凝固浴中へ吐出し、
未延伸糸を得た。この未延伸糸を導水中で約3倍延伸を
行ない、さらに導水中で洗浄を行い、繊維1.0デニー
ルの繊維(PSV繊維No、 7〜9)を得た。得られ
た繊維の性能を第5表に示した。This spinning stock solution was discharged into a coagulation bath containing 60% by weight of dimethylacetamide and 40% by weight of deionized water at a temperature of 30°C.
An undrawn yarn was obtained. This undrawn yarn was drawn approximately 3 times in flowing water and further washed in flowing water to obtain fibers (PSV fibers No. 7 to 9) having a denier of 1.0. The performance of the obtained fibers is shown in Table 5.
実施例8
溶剤としてジメチルアセトアミドを用い、PvC/PM
MA/PSFのポリマー組成比(重量%)を30150
/20とし、pvcの重合度を第6表に示す様に変更し
て、溶剤に溶解分散させ、紡糸原液を調製し、実施例7
における同じ方法で紡糸、繊維賦型をおこなった。Example 8 Using dimethylacetamide as a solvent, PvC/PM
The polymer composition ratio (wt%) of MA/PSF was 30150.
Example 7
Spinning and fiber shaping were performed using the same method as in .
得られた繊維(PSV繊維No10〜12)の性能を第
6表に示した。Table 6 shows the performance of the obtained fibers (PSV fibers No. 10 to 12).
第6表
実施例9
溶剤としてジメチルアセトアミドを用い、重合度110
0のpvcとポリスチレンとPSFを50/30/20
の組成比(重量%)で溶解分散させ、紡糸原液をえた。Table 6 Example 9 Using dimethylacetamide as a solvent, degree of polymerization 110
0 pvc and polystyrene and PSF 50/30/20
A spinning stock solution was obtained by dissolving and dispersing at a composition ratio (wt%) of .
この時の固形分濃度は50℃における粘度が200ボイ
ズ付近になるように8周製した。At this time, the solid content concentration was 8 times so that the viscosity at 50° C. was around 200 voids.
この紡糸原液を実施例7と同様な手法で、繊度1.03
デニール、強度1.22、伸度27.8%、湧水収縮率
21.5%の繊維(PSV繊維No、 13 )を得た
。得られた繊維のに011処理後の減量率および保液率
を測定したところ、それぞれ1.09重量%、71.2
%であった。This spinning stock solution was processed using the same method as in Example 7 to obtain a fineness of 1.03.
A fiber (PSV fiber No. 13) having a denier, a strength of 1.22, an elongation of 27.8%, and a spring shrinkage rate of 21.5% was obtained. When the weight loss rate and liquid retention rate of the obtained fibers were measured after Ni-011 treatment, they were 1.09% by weight and 71.2% by weight, respectively.
%Met.
実施例10
実施例5.6.7.9で得られるpsv繊維をそれぞれ
乾燥することなく補集し、湿潤状態で6mmに切断し、
VA織繊維80/20の混合比(重量%)で湿式抄紙し
、115℃で熱融着成型し目付50 g/r+(の第7
表に示すシート状成型物(シートNo、15〜21)を
得た。Example 10 The PSV fibers obtained in Example 5.6.7.9 were collected without drying, cut into 6 mm pieces in a wet state, and
Wet paper is made with a mixing ratio (wt%) of VA woven fibers of 80/20, and is heat-fused and molded at 115°C to give a fabric weight of 50 g/r+ (7th paper).
Sheet-like molded products (sheet Nos. 15 to 21) shown in the table were obtained.
比較例2
実施例5で得られたpsv繊維No、 4を使用し、実
施例10と同様な手法でシート状成型物の製造を試みた
。湿式方式での成型はできたが熱融着時紙が収縮し製造
が困難であった。Comparative Example 2 Using the PSV fiber No. 4 obtained in Example 5, an attempt was made to manufacture a sheet-like molded product in the same manner as in Example 10. Although it was possible to mold using the wet method, the paper shrunk during heat-sealing, making manufacturing difficult.
比較例3
実施例5および7で得られたPSV繊維No、 5およ
びNo、 7を使用し、実施例10と同様な手法でシー
ト状成型物の製造を試みた。得られたシート状成型物は
耐アルカリ性、保液性とも十分であったが強度が低く実
用に供しないものであった。Comparative Example 3 Using the PSV fibers No. 5 and No. 7 obtained in Examples 5 and 7, an attempt was made to produce a sheet-like molded product in the same manner as in Example 10. The obtained sheet-like molded product had sufficient alkali resistance and liquid retention properties, but its strength was low and it could not be put to practical use.
実施例11
実施例1で得られたシー1− No、 2を界面活性剤
で親水化処理を行なったところ、保液率が465%に向
上した。Example 11 When Sea 1-No. 2 obtained in Example 1 was subjected to hydrophilic treatment with a surfactant, the liquid retention rate was improved to 465%.
〈発明の効果〉
本発明のシート状成型物は耐アルカリ性に優れることか
ら、廃アルカリ処理用フィルター等の工業用フィルター
、および高い保液性を有することから酸化銀電池、水銀
電池、空気電池、アルカリ−マンガン電池、ニッケルー
亜鉛電池、ニッケルーカドミウム電池、アルカリ蓄電池
等の電池用セパレーターとしてきわめて有用なるもので
ある。<Effects of the Invention> Since the sheet-like molded product of the present invention has excellent alkali resistance, it can be used as industrial filters such as filters for waste alkali treatment, and because it has high liquid retention properties, it can be used in silver oxide batteries, mercury batteries, air batteries, It is extremely useful as a separator for batteries such as alkaline-manganese batteries, nickel-zinc batteries, nickel-cadmium batteries, and alkaline storage batteries.
特許出願人 三菱レイヨン株式会社Patent applicant: Mitsubishi Rayon Co., Ltd.
Claims (2)
ホンを少なくとも15重量%、ポリ塩化ビニルを少なく
とも20重量%含有する組成物で構成された繊維50重
量%以上からなる耐アルカリ性に優れたシート状成型物
。(1) A sheet-like molded product with excellent alkali resistance, consisting of 50% by weight or more of fibers made of a composition containing at least 15% by weight of polysulfone and/or polyethersulfone and at least 20% by weight of polyvinyl chloride.
ホンを少なくとも15重量%、ポリ塩化ビニルを少なく
とも20重量%含有する組成物で構成された繊維50〜
90重量%および熱融着温度が125℃以下であるバイ
ンダー繊維50〜10重量%からなる耐アルカリ性に優
れたシート状成型物。(2) Fibers composed of a composition containing at least 15% by weight of polysulfone and/or polyethersulfone and at least 20% by weight of polyvinyl chloride.
A sheet-like molded product having excellent alkali resistance, comprising 90% by weight of binder fibers and 50 to 10% by weight of binder fibers having a heat fusion temperature of 125°C or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1078019A JPH02259189A (en) | 1989-03-31 | 1989-03-31 | Sheet-shaped molded product with excellent alkali resistance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1078019A JPH02259189A (en) | 1989-03-31 | 1989-03-31 | Sheet-shaped molded product with excellent alkali resistance |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02259189A true JPH02259189A (en) | 1990-10-19 |
Family
ID=13650089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1078019A Pending JPH02259189A (en) | 1989-03-31 | 1989-03-31 | Sheet-shaped molded product with excellent alkali resistance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02259189A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5888916A (en) * | 1994-12-28 | 1999-03-30 | Asahi Kasei Kogyo Kabushiki Kaisha | Wet-laid nonwoven fabric for battery separator, its production method and sealed type secondary battery |
| JP2010500718A (en) * | 2006-08-07 | 2010-01-07 | コリア インスティテュート オブ サイエンス アンド テクノロジー | Separation membrane having heat-resistant ultrafine fiber layer and secondary battery using the same |
| JP2010500717A (en) * | 2006-08-07 | 2010-01-07 | コリア インスティテュート オブ サイエンス アンド テクノロジー | Heat-resistant ultrafine fiber separation membrane and secondary battery using the same |
| WO2010020736A1 (en) * | 2008-08-19 | 2010-02-25 | Sergei Botov | Filter elements and filter |
| WO2012017954A1 (en) * | 2010-08-04 | 2012-02-09 | ダイセル化学工業株式会社 | Non-woven fabric comprising cellulose fibers and process for production thereof, and separator |
| GB2488624A (en) * | 2011-12-09 | 2012-09-05 | Sergei Botov | Filter element |
-
1989
- 1989-03-31 JP JP1078019A patent/JPH02259189A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5888916A (en) * | 1994-12-28 | 1999-03-30 | Asahi Kasei Kogyo Kabushiki Kaisha | Wet-laid nonwoven fabric for battery separator, its production method and sealed type secondary battery |
| JP2010500718A (en) * | 2006-08-07 | 2010-01-07 | コリア インスティテュート オブ サイエンス アンド テクノロジー | Separation membrane having heat-resistant ultrafine fiber layer and secondary battery using the same |
| JP2010500717A (en) * | 2006-08-07 | 2010-01-07 | コリア インスティテュート オブ サイエンス アンド テクノロジー | Heat-resistant ultrafine fiber separation membrane and secondary battery using the same |
| US8815432B2 (en) | 2006-08-07 | 2014-08-26 | Korea Institute Of Science And Technology | Heat resisting ultrafine fibrous separator and secondary battery using the same |
| WO2010020736A1 (en) * | 2008-08-19 | 2010-02-25 | Sergei Botov | Filter elements and filter |
| WO2012017954A1 (en) * | 2010-08-04 | 2012-02-09 | ダイセル化学工業株式会社 | Non-woven fabric comprising cellulose fibers and process for production thereof, and separator |
| GB2488624A (en) * | 2011-12-09 | 2012-09-05 | Sergei Botov | Filter element |
| GB2488624B (en) * | 2011-12-09 | 2012-12-19 | Sergei Botov | Filter elements and filter |
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