JPH0457911A - Porous actylic yarn having excellent water retention and its production - Google Patents
Porous actylic yarn having excellent water retention and its productionInfo
- Publication number
- JPH0457911A JPH0457911A JP16893990A JP16893990A JPH0457911A JP H0457911 A JPH0457911 A JP H0457911A JP 16893990 A JP16893990 A JP 16893990A JP 16893990 A JP16893990 A JP 16893990A JP H0457911 A JPH0457911 A JP H0457911A
- Authority
- JP
- Japan
- Prior art keywords
- weight
- cellulose acetate
- acrylonitrile
- yarn
- water retention
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 229920002301 cellulose acetate Polymers 0.000 claims abstract description 29
- 238000009987 spinning Methods 0.000 claims abstract description 17
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000002904 solvent Substances 0.000 claims abstract description 12
- 229920002959 polymer blend Polymers 0.000 claims abstract description 4
- 239000000835 fiber Substances 0.000 claims description 44
- 229920002972 Acrylic fiber Polymers 0.000 claims description 13
- 238000001035 drying Methods 0.000 claims description 13
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 12
- 239000011550 stock solution Substances 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 229920000642 polymer Polymers 0.000 abstract description 9
- 230000000704 physical effect Effects 0.000 abstract description 8
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 27
- 206010016807 Fluid retention Diseases 0.000 description 21
- 238000000034 method Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 9
- 238000000605 extraction Methods 0.000 description 9
- 229920001747 Cellulose diacetate Polymers 0.000 description 6
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 2
- 229920002284 Cellulose triacetate Polymers 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical class CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- NNLVGZFZQQXQNW-ADJNRHBOSA-N [(2r,3r,4s,5r,6s)-4,5-diacetyloxy-3-[(2s,3r,4s,5r,6r)-3,4,5-triacetyloxy-6-(acetyloxymethyl)oxan-2-yl]oxy-6-[(2r,3r,4s,5r,6s)-4,5,6-triacetyloxy-2-(acetyloxymethyl)oxan-3-yl]oxyoxan-2-yl]methyl acetate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](OC(C)=O)[C@H]1OC(C)=O)O[C@H]1[C@@H]([C@@H](OC(C)=O)[C@H](OC(C)=O)[C@@H](COC(C)=O)O1)OC(C)=O)COC(=O)C)[C@@H]1[C@@H](COC(C)=O)O[C@@H](OC(C)=O)[C@H](OC(C)=O)[C@H]1OC(C)=O NNLVGZFZQQXQNW-ADJNRHBOSA-N 0.000 description 2
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 description 2
- 206010061592 cardiac fibrillation Diseases 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 230000002600 fibrillogenic effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000002166 wet spinning Methods 0.000 description 2
- NJYFRQQXXXRJHK-UHFFFAOYSA-N (4-aminophenyl) thiocyanate Chemical compound NC1=CC=C(SC#N)C=C1 NJYFRQQXXXRJHK-UHFFFAOYSA-N 0.000 description 1
- VMSBGXAJJLPWKV-UHFFFAOYSA-N 2-ethenylbenzenesulfonic acid Chemical compound OS(=O)(=O)C1=CC=CC=C1C=C VMSBGXAJJLPWKV-UHFFFAOYSA-N 0.000 description 1
- KGIGUEBEKRSTEW-UHFFFAOYSA-N 2-vinylpyridine Chemical compound C=CC1=CC=CC=N1 KGIGUEBEKRSTEW-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000021736 acetylation Effects 0.000 description 1
- 238000006640 acetylation reaction Methods 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- -1 dimethylaminoethyl Chemical group 0.000 description 1
- 238000000578 dry spinning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- UIIIBRHUICCMAI-UHFFFAOYSA-N prop-2-ene-1-sulfonic acid Chemical compound OS(=O)(=O)CC=C UIIIBRHUICCMAI-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Landscapes
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は保水性の良好なアクリル系繊維及びその製造方
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an acrylic fiber with good water retention properties and a method for producing the same.
更に詳しくは、アクリロニトリル系重合体と酢酸セルロ
ースを含有する混合原液を紡糸、延伸、乾燥緩和処理後
、更に酢酸セルロースのみを選択的に溶剤にて抽出除去
することによって得られる、優れた光沢および糸物性を
有し、かつ高保水率を有する多孔性アクリル系繊維およ
びその製造方法に関するものである。More specifically, after spinning, stretching and drying a mixed solution containing an acrylonitrile polymer and cellulose acetate, the yarn has excellent gloss and is obtained by selectively extracting and removing only the cellulose acetate with a solvent. The present invention relates to a porous acrylic fiber having physical properties and a high water retention rate, and a method for producing the same.
[従来の技術]
アクリル系繊維はその優れた発色性、保温性、耐光性等
を生かして肌着、スポーツウェア等の衣料や寝装用に幅
広い商品展開が計られている。[Prior Art] Acrylic fibers are being used in a wide range of products for clothing such as underwear, sportswear, and bedding, taking advantage of their excellent color development, heat retention, and light resistance.
近年ではこれらの特性に加えて制電性・吸水性・保水性
及び消臭性等の機能付与が求められている。一般に合成
繊維は吸水性・保水性の面で天然繊維に劣っておりアク
リル系繊維もその例外ではない。In recent years, in addition to these properties, there has been a demand for additional functions such as antistatic properties, water absorbing properties, water retaining properties, and deodorizing properties. Generally, synthetic fibers are inferior to natural fibers in terms of water absorption and water retention, and acrylic fibers are no exception.
アクリル系繊維の吸水性・保水性の向上に関して従来よ
り種々の検討がなされ、特に湿式紡糸においては特公昭
48−6649号公報、特公昭48−6650号公報の
ように温和な乾燥条件を選択する事により多孔質のアク
リル系繊維を得る方法、また特公昭48−8285号公
報、特公昭48−8286号公報のようにあらかじめ膨
潤ゲルドウ中に充填した水滴性化合物を後工程で溶出さ
せボイドを再生させる方法等が開示されている。Various studies have been made to improve the water absorption and water retention properties of acrylic fibers, and in particular, in wet spinning, mild drying conditions have been selected as in Japanese Patent Publication No. 48-6649 and Japanese Patent Publication No. 48-6650. There is also a method of obtaining porous acrylic fibers, and a method of regenerating voids by dissolving a water droplet compound filled in the swollen gel dow in a post-process as disclosed in Japanese Patent Publication No. 48-8285 and Japanese Patent Publication No. 48-8286. A method for doing so is disclosed.
同じくアクリロニトリル系重合体と酢酸セルロースとか
らなる重合体を混合、溶解、湿式紡糸することにより、
繊維断面にボイドを発生させ吸湿性、吸水性を賦与させ
たものには特公昭31−968号公報、特公昭33−2
317号公報等がある。本発明者等も特願平2−292
04号公報にアクリロニトリル重合体組成等を検討する
ことにより、従来保水性の低かった乾式アクリル系繊維
にて、優れた風合い、糸物性および保水性が得られるこ
とを開示している。Similarly, by mixing, dissolving, and wet spinning a polymer made of acrylonitrile-based polymer and cellulose acetate,
Japanese Patent Publications No. 31-968 and No. 33-2 disclose fibers in which voids are generated in the cross section of the fibers to impart hygroscopicity and water absorption properties.
There are publications such as Publication No. 317. The present inventors also applied for patent application No. 2-292
Publication No. 04 discloses that by examining the composition of acrylonitrile polymer, etc., it is possible to obtain excellent texture, thread properties, and water retention in dry-processed acrylic fibers that conventionally had low water retention.
[発明が解決しようとする課題]
しかしながら、特公昭31−968号公報、特公昭33
−2317号公報に示される方法では、酢酸セルロース
の混合比率を50重量%まで高めても得られる繊維の保
水率は高々25%程度であり、延伸性の低下および乾燥
緩和処理時の収縮性の低下により充分な糸物性が得られ
ず、紡績等後工程通過性にも問題がある。また、特願平
2−29204号公報に示される方法で得られる繊維の
保水率は高々35%である。[Problem to be solved by the invention] However, Japanese Patent Publication No. 31-968, Japanese Patent Publication No. 33
In the method disclosed in Publication No. 2317, even if the mixing ratio of cellulose acetate is increased to 50% by weight, the water retention rate of the fiber obtained is at most about 25%, resulting in decreased stretchability and shrinkage during drying relaxation treatment. Due to the decrease, sufficient yarn physical properties cannot be obtained, and there is also a problem in passing through subsequent processes such as spinning. Further, the water retention rate of the fiber obtained by the method disclosed in Japanese Patent Application No. 2-29204 is at most 35%.
本発明者等は更に検討を重ねた結果、特定の組成範囲に
あるアクリロニトリル系重合体と酢酸セルロースとを溶
解、混合した紡糸原液を紡糸、延伸、乾燥緩和処理して
得られた繊維中の酢酸セルロースのみを選択的に除去す
ることにより従来得られなかった30ないし80%とい
う高保水率を有し、かつ糸物性が向上した繊維を提供す
るに至った。As a result of further studies, the present inventors found that acetic acid in fibers obtained by spinning, stretching, and drying a spinning dope prepared by dissolving and mixing an acrylonitrile polymer and cellulose acetate in a specific composition range. By selectively removing only cellulose, we have been able to provide fibers that have a water retention rate as high as 30 to 80%, which was previously unobtainable, and have improved yarn properties.
[課題を解決するための手段]
すなわち本発明は、
(1)85重量%以上のアクリロニトリルを含有する9
2.5重量%以上のアクリロニトリル系重合体と75重
量%未満の酢酸セルロースとより構成され、保水率30
%以上であることを特徴とする保水性の良好な多孔性ア
クリル系繊維。[Means for Solving the Problems] That is, the present invention provides: (1) 9 containing 85% by weight or more of acrylonitrile;
It is composed of 2.5% by weight or more of acrylonitrile polymer and less than 75% by weight of cellulose acetate, and has a water retention rate of 30%.
% or more of porous acrylic fibers with good water retention properties.
f2185重量%以上のアクリロニトリルを含有するア
クリロニトリル系重合体50ないし85重量%と酢酸セ
ルロース50ないし15重量%とからなる重合体混合物
を溶剤に溶解、混合した紡糸原液を紡糸し、次いで2な
いし5倍に延伸し乾燥緩和処理にて5%以上の収縮を施
し、さらに該繊維中の酢酸セルロースを85%以上溶剤
にて抽出除去することを特徴とする保水性の良好な多孔
性アクリル系繊維の製造方法。f2 A polymer mixture consisting of 50 to 85% by weight of an acrylonitrile polymer containing 185% by weight or more of acrylonitrile and 50 to 15% by weight of cellulose acetate is dissolved in a solvent, a mixed spinning stock solution is spun, and then 2 to 5 times Production of porous acrylic fibers with good water retention, characterized by stretching the fibers, subjecting them to shrinkage of 5% or more through drying relaxation treatment, and further extracting and removing 85% or more of the cellulose acetate in the fibers with a solvent. Method.
を要旨とするものである。The main points are as follows.
以下本発明を更に詳細に説明する。The present invention will be explained in more detail below.
本発明の対象となるアクリロニトリル系重合体は、少な
くとも85重量%のアクリロニトリルを含有することが
必要である。アクリロニトリルの含有率がこれより少な
い場合は、衣料用繊維として必要な繊維物性、とりわけ
形態安定性が低下してしまうので好ましくない。アクリ
ロニトリルと共重合可能な単量体としてはアクリル酸メ
チル、メタアクリル酸メチル等の(メタ)アクリル酸エ
ステル類、酢酸ビニル、スチレン、アクリルアミド類が
上げられる。これらの共重合率は通常の場合3ないし1
0重量%である。また、染色性改良のために(メタ)ア
クリル酸、(メタ)アリルスルホン酸やビニルベンゼン
スルホン酸とそれ等の塩類、ジメチルアミノエチル(メ
タ)アクリレート、ビニルピリジン類を共重合させるこ
ともある。これら単量体の共重合率は通常の場合3重量
%以下である。The acrylonitrile polymer that is the object of the present invention must contain at least 85% by weight of acrylonitrile. If the content of acrylonitrile is less than this, it is not preferable because the physical properties of the fiber necessary for clothing fibers, especially the shape stability, will deteriorate. Examples of monomers copolymerizable with acrylonitrile include (meth)acrylic acid esters such as methyl acrylate and methyl methacrylate, vinyl acetate, styrene, and acrylamide. The copolymerization rate of these is usually 3 to 1.
It is 0% by weight. Further, in order to improve dyeability, (meth)acrylic acid, (meth)allylsulfonic acid, vinylbenzenesulfonic acid and their salts, dimethylaminoethyl (meth)acrylate, and vinylpyridine may be copolymerized. The copolymerization rate of these monomers is usually 3% by weight or less.
該重合体は、通常の懸濁重合、溶液重合、乳化重合など
のいかなる方法によっても製造できる。The polymer can be produced by any conventional method such as suspension polymerization, solution polymerization, emulsion polymerization, etc.
重合体の重合度はその比粘度(重合体0.1グラムを0
.1Nのロダンソーダを含有するジメチルホルムアミド
100mβに溶解し、25℃で測定)で表わして0.1
Oないし0.20の範囲が好ましい。The degree of polymerization of a polymer is its specific viscosity (0.1 g of polymer
.. 0.1 (dissolved in 100 mβ of dimethylformamide containing 1N rhodan soda and measured at 25°C)
A range of 0 to 0.20 is preferred.
本発明で使用する酢酸セルロースとは、二酢酸セルロー
ス、三酢酸セルロースである。The cellulose acetate used in the present invention is cellulose diacetate or cellulose triacetate.
さらに、アクリロニトリル系重合体と酢酸セルロースの
ほかに紡糸性・延伸性及び糸物性の改良を目的として可
塑剤物質、自席向上剤、熱安定剤、及び酸化チタン等を
添加しうることはもちろんである。Furthermore, in addition to the acrylonitrile polymer and cellulose acetate, it is of course possible to add plasticizers, self-seistance improvers, heat stabilizers, titanium oxide, etc. for the purpose of improving spinnability, drawability, and yarn properties. .
本発明で使用する紡糸溶剤としては、アクリロニトリル
系重合体および酢酸セルロースの共通溶剤であるジメチ
ルホルムアミド、ジメチルアセトアミド、ジメチルスル
ホキシド等が使用され、これらの有機溶剤は溶剤回収の
容易性の面からも好ましく使用される。As the spinning solvent used in the present invention, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, etc., which are common solvents for acrylonitrile polymers and cellulose acetate, are used, and these organic solvents are preferable from the viewpoint of ease of solvent recovery. used.
アクリロニトリル系重合体と酢酸セルロースとの混合方
法は特に限定されるものではないが、混合原液中の重合
体の濃度は20ないし40重量%であることが必要であ
る。Although the method of mixing the acrylonitrile polymer and cellulose acetate is not particularly limited, it is necessary that the concentration of the polymer in the mixed stock solution be 20 to 40% by weight.
紡糸方法は、通常アクリル系繊維の製造に採用される湿
式、乾湿式、乾式のいずれの方法でもよいが、好ましく
は、紡糸時に緻密な繊維構造が形成され、紡糸工程や後
続の延伸工程等にて繊維表面のフィブリル化およびそれ
に伴う酢酸セルロースの脱落が避けられる乾式紡糸が望
ましい。The spinning method may be any of the wet, dry-wet, and dry methods that are normally employed in the production of acrylic fibers, but it is preferable that a dense fiber structure be formed during spinning, so that it can be easily used in the spinning process, subsequent drawing process, etc. Dry spinning is desirable because it can avoid fibrillation on the fiber surface and the accompanying shedding of cellulose acetate.
紡糸後の未延伸糸中に占める酢酸セルロースの比率が1
5重量%未満の場合は、後続の酢酸セルロースの抽出除
去の際充分な抽出が行えず、本発明に言う30%以上の
高保水性の繊維は得られない。一方50重量%を超えた
場合、保水率はより高くなるが、未延伸糸の延伸性の低
下および乾燥緩和処理時の収縮性の低下により強伸度、
結節強伸度等の糸物性が乏しく、衣料としての使用は困
難である。The ratio of cellulose acetate in the undrawn yarn after spinning is 1
If the amount is less than 5% by weight, sufficient extraction cannot be carried out during the subsequent extraction and removal of cellulose acetate, and fibers with high water retention of 30% or more as defined in the present invention cannot be obtained. On the other hand, if it exceeds 50% by weight, the water retention rate will be higher, but the strength and elongation will be lowered due to a decrease in the drawability of the undrawn yarn and a decrease in shrinkage during drying relaxation treatment.
It has poor yarn properties such as knot strength and elongation, making it difficult to use as clothing.
未延伸糸は熱水中延伸を施すことにより強度が付与され
る。延伸温度は80ないし95℃、延伸倍率は2ないし
5倍が良い。延伸倍率が2倍未満の場合、得られる繊維
に十分な強度が付与されず紡績工程等でケバが頻発し、
後加工性が不良となる。一方5倍を超えると、繊維表面
のフィブリル化が顕著となり糸切れが発生する。未延伸
糸中に占める酢酸セルロースの比率が高いほど、延伸倍
率は低く抑えるのが好ましい。Strength is imparted to the undrawn yarn by drawing it in hot water. The stretching temperature is preferably 80 to 95°C, and the stretching ratio is preferably 2 to 5 times. If the stretching ratio is less than 2 times, sufficient strength will not be imparted to the resulting fibers and fluff will frequently occur during the spinning process, etc.
Post-processability becomes poor. On the other hand, if it exceeds 5 times, fibrillation on the fiber surface becomes noticeable and yarn breakage occurs. The higher the proportion of cellulose acetate in the undrawn yarn, the lower the stretching ratio.
未延伸糸は上記延伸処理と同時あるいはその前後を通じ
て熱水中で洗浄される。洗浄温度は80ないし100℃
が好ましい。延伸洗浄された繊維束は油剤を付与した後
、乾燥及び緩和処理を施す。乾燥及び緩和の方法につい
ては特に限定するものではないが、本発明者らは延伸洗
浄後の繊維束を無緊張下に湿潤状態のまま相対湿度10
ないし40%、温度130ないし160℃の加熱空気下
で処理し乾燥と緩和を同時に施す方法を主として用いた
。上記のごとき方法にて該繊維に5%以上の緩和を施す
。収縮率が5%未満の場合、結節強伸度等の糸物性が劣
り、紡績等の後退構成が不良となる。The undrawn yarn is washed in hot water at the same time as or before or after the drawing process. Washing temperature is 80 to 100℃
is preferred. The stretched and washed fiber bundle is coated with an oil agent and then subjected to drying and relaxation treatment. Although there are no particular limitations on the method of drying and relaxing, the present inventors have tested the fiber bundles after stretching and washing at a relative humidity of 10% in a moist state without tension.
to 40% and a temperature of 130 to 160° C. under heated air to dry and relax at the same time. The fibers are relaxed by 5% or more using the method described above. If the shrinkage rate is less than 5%, the yarn physical properties such as knot strength and elongation are poor, and the retraction structure for spinning etc. becomes poor.
乾燥緩和処理された繊維は乾燥緩和処理直後あるいは紡
績、編織を経た後酢酸セルロースの溶剤抽出除去処理を
行なう。酢酸セルロースの抽出率は85%以上、好まし
くは90%以上であることが必要である。抽出率が85
%未満の場合、繊維表面に酢酸セルロースが残留し、風
合いが固くなり、衣料用には不適なものとなる。The fibers subjected to the dry relaxation treatment are subjected to solvent extraction removal treatment of cellulose acetate immediately after the dry relaxation treatment or after spinning, knitting and weaving. The extraction rate of cellulose acetate needs to be 85% or more, preferably 90% or more. Extraction rate is 85
If the amount is less than %, cellulose acetate remains on the surface of the fibers, resulting in a hard texture and making them unsuitable for clothing.
ここで驚くべきことには、酢酸セルロースの抽出除去後
に得られる繊維の糸物性はほとんど低下せず、結節強伸
度等紡績性に要求される糸質は抽出除去以前のものより
格段に向上していることである。詳細な原因は不明であ
るが、抽出除去後の繊維には繊維断面方向の体積収縮や
アクリロニトリル系重合体によるネットワーク構造が認
められ、これが糸質向上に寄与しているものと推定され
る。Surprisingly, the physical properties of the fiber obtained after the extraction and removal of cellulose acetate hardly deteriorated, and the yarn quality required for spinnability, such as knot strength and elongation, was significantly improved compared to that before the extraction and removal. This is what is happening. Although the detailed cause is unknown, volume shrinkage in the cross-sectional direction of the fibers and a network structure due to the acrylonitrile polymer were observed in the fibers after extraction and removal, and it is presumed that this contributes to the improvement of yarn quality.
本抽出除去処理に使用される溶剤は、酢酸セルロースを
選択的に溶解する溶剤であれば特に制限はなく、具体的
には二酢酸セルロースの場合、アセトン、メチルエチル
ケトン、塩化メチレン、酢酸メチル、ジオキサン等、三
酢酸セルロースの場合、塩化メチレン、クロロホルム、
酢酸メチル、ジオキサン等が挙げられる。The solvent used in this extraction and removal process is not particularly limited as long as it selectively dissolves cellulose acetate; specifically, in the case of cellulose diacetate, acetone, methyl ethyl ketone, methylene chloride, methyl acetate, dioxane, etc. , for cellulose triacetate, methylene chloride, chloroform,
Examples include methyl acetate and dioxane.
以下実施例によって本発明を具体的に説明する。EXAMPLES The present invention will be specifically explained below with reference to Examples.
なお得られた繊維の保水率は以下の方法で測定した。実
施例中の%表示は特に断わらないかぎり重量%を示す。The water retention rate of the obtained fibers was measured by the following method. % in the examples indicates weight % unless otherwise specified.
〈保水率〉
常法により精練した繊維をイオン交換水中に24時間浸
せきした後、100OGの加速度のもとて10分間遠心
脱水した原綿の重量(Wl)を測定する。この繊維を1
05℃で3時間熱風乾燥し、デシケータ−中で30分放
冷した後の重量(W2)を測定し下式に従って保水率を
算出した。<Water retention rate> After scouring fibers by a conventional method and soaking them in ion-exchanged water for 24 hours, the raw cotton was dehydrated by centrifugation for 10 minutes at an acceleration of 100 OG, and the weight (Wl) of the raw cotton was measured. This fiber is 1
After drying with hot air at 05° C. for 3 hours and cooling in a desiccator for 30 minutes, the weight (W2) was measured and the water retention rate was calculated according to the formula below.
[実施例]
実施例1
アクリロニトリル93重量%、酢酸ビニル7重量%から
なる比粘度0.175 (0,1%ジメチルフォルム
アミド(DMF)溶液、25%℃測定)のアクリロニト
リル系共重合体90ないし40重量%と二酢酸セルロー
ス(酸化度55%)10ないし60重量%をジメチルホ
ルムアミドに溶解、混合し固形分濃度28%の原液を調
整した。[Example] Example 1 Acrylonitrile copolymer 90 to 90 and having a specific viscosity of 0.175 (0.1% dimethylformamide (DMF) solution, measured at 25% °C) consisting of 93% by weight of acrylonitrile and 7% by weight of vinyl acetate. 40% by weight and 10 to 60% by weight of cellulose diacetate (oxidation degree 55%) were dissolved in dimethylformamide and mixed to prepare a stock solution with a solid content concentration of 28%.
上記の原液を1)0℃に加熱した後、孔数600、孔径
015mlffφのオリフィスより230℃に加熱され
た不活性ガス中に吐出し未延伸糸を得た。この未延伸糸
を収束し20万デニールの繊維束とし、熱水中で2.0
ないし4.0倍に延伸し、更に熱水中で洗浄、油剤付与
を施した後得られた繊維束を無緊張下に相対湿度40%
、温度150℃で乾燥・緩和処理を行なった。更に、得
られた繊維をアセトン浴にて十分に洗浄し、得られた各
繊維の糸物性、保水率を第1表に示した。1) The above stock solution was heated to 0° C. and then discharged into an inert gas heated to 230° C. through an orifice having 600 holes and a hole diameter of 015 mlffφ to obtain an undrawn yarn. This undrawn yarn was converged into a fiber bundle of 200,000 deniers, and was placed in hot water with a
After stretching the fiber bundle to 4.0 times or more, washing it in hot water, and applying an oil agent, the resulting fiber bundle is heated at a relative humidity of 40% without tension.
A drying/relaxation treatment was performed at a temperature of 150°C. Furthermore, the obtained fibers were thoroughly washed in an acetone bath, and the yarn physical properties and water retention rates of each obtained fiber are shown in Table 1.
実施例2
アクリロニトリル93.5重量%、アクリル酸メチル6
重量%、メタリルスルホン酸ソーダ0.5重量%からな
る比粘度0.161 (0,1%DMF溶液、25%
℃測定)のアクリロニトリル系共重合体90ないし10
重量%と二酢酸セルロース(酢化度55%)10ないし
90重量%をジメチルホルムアミドに溶解、混合し固形
分濃度30%の原液を調整した。Example 2 Acrylonitrile 93.5% by weight, methyl acrylate 6
wt%, specific viscosity 0.161 (0.1% DMF solution, 25%
Acrylonitrile copolymer (measured at ℃) 90 to 10
% by weight and 10 to 90% by weight of cellulose diacetate (degree of acetylation 55%) were dissolved in dimethylformamide and mixed to prepare a stock solution with a solid content concentration of 30%.
上記の原液を130℃に加熱した後、孔数600、孔径
0.15■■φのオリフィスより230℃に加熱された
不活性ガス中に吐出し未延伸糸を得た。この未延伸糸を
収束し20万デニールの繊維束とし、熱水中で2.0な
いし4.0倍に延伸し、更に熱水中で洗浄、油剤付与を
施した後得られた繊維束を無緊張下に相対湿度40%、
温度150℃で乾燥・緩和処理を行なった。更に、得ら
れた繊維を熱アセトン浴にて十分に洗浄し、得られた各
繊維の糸物性、保水率を第2表に示した。The above stock solution was heated to 130° C. and then discharged into an inert gas heated to 230° C. through an orifice with 600 holes and a hole diameter of 0.15 φ to obtain an undrawn yarn. The undrawn yarns are converged to form a fiber bundle of 200,000 denier, stretched 2.0 to 4.0 times in hot water, washed in hot water, and coated with an oil agent. 40% relative humidity under no tension,
Drying/relaxation treatment was performed at a temperature of 150°C. Furthermore, the obtained fibers were thoroughly washed in a hot acetone bath, and the yarn physical properties and water retention rates of each obtained fiber are shown in Table 2.
実施例3
アクリロニトリル93.5重量%、アクリル酸メチル6
重量%、メタリルスルポン酸ソーダ0.5重量%からな
る比粘度0.161 (0,1%DMF溶液、25%
℃測定)のアクリロニトリル系共重合体70ないし50
重量%と二酢酸セルロース(酸化度55%)30ないし
50重量%をジメチルホルムアミドに溶解、混合し固形
分濃度30%の原液を調整した。Example 3 Acrylonitrile 93.5% by weight, methyl acrylate 6
wt%, specific viscosity 0.161 (0.1% DMF solution, 25%
Acrylonitrile copolymer (measured at ℃) 70 to 50
% by weight and 30 to 50% by weight of cellulose diacetate (oxidation degree 55%) were dissolved in dimethylformamide and mixed to prepare a stock solution with a solid content concentration of 30%.
上記の原液を130℃に加熱した後、孔数600゜孔径
0.15i1■φのオリフィスより230℃に加熱され
た不活性ガス中に吐出し未延伸糸を得た。この未延伸糸
を収束し20万デニールの繊維束とし、熱水中で2.0
ないし4.0倍に延伸し、更に熱水中で洗浄、油剤付与
を施した後得られた繊維束を無緊張下に相対湿度40%
、温度150℃で乾燥・緩和処理を行なった。更に、得
られた繊維を熱アセトン浴にて抽出率を変更しなから二
酢酸セルロースを除去し、得られた各繊維の保水率、風
合い評価結果を第3表に示した。The above stock solution was heated to 130° C. and then discharged into an inert gas heated to 230° C. through an orifice having 600° holes and 0.15 i1 φ diameter to obtain an undrawn yarn. This undrawn yarn was converged into a fiber bundle of 200,000 deniers, and was placed in hot water with a
After stretching the fiber bundle to 4.0 times or more, washing it in hot water, and applying an oil agent, the resulting fiber bundle is heated at a relative humidity of 40% without tension.
A drying/relaxation treatment was performed at a temperature of 150°C. Furthermore, cellulose diacetate was removed from the obtained fibers in a hot acetone bath without changing the extraction rate, and Table 3 shows the results of evaluating the water retention rate and texture of each fiber obtained.
[発明の効果]
本発明による繊維は、優れた光沢および糸物性を有し、
かつ従来アクリル系繊維では得られなかった高い保水性
を有する新規な多孔性アクリル系繊維およびその製造方
法を提供するもので、肌着を初め衣料等への幅広い展開
が期待でき、その産業上の意義は大きい。[Effect of the invention] The fiber according to the invention has excellent gloss and thread properties,
Moreover, it provides a new porous acrylic fiber that has high water retention properties that could not be obtained with conventional acrylic fibers, and a method for producing the same.It is expected to be widely used in underwear and clothing, and its industrial significance is high. is big.
Claims (2)
2.5重量%以上のアクリロニトリル系重合体と7.5
重量%未満の酢酸セルロースとより構成され、保水率3
0%以上であることを特徴とする保水性の良好な多孔性
アクリル系繊維。(1) 9 containing 85% by weight or more of acrylonitrile
2.5% by weight or more of acrylonitrile polymer and 7.5% by weight
Composed of less than % by weight of cellulose acetate and has a water retention rate of 3
A porous acrylic fiber with good water retention, characterized by having a water retention capacity of 0% or more.
クリロニトリル系重合体50ないし85重量%と酢酸セ
ルロース50ないし15重量%とからなる重合体混合物
を溶剤に溶解、混合した紡糸原液を紡糸し、次いで2な
いし5倍に延伸し乾燥緩和処理にて5%以上の収縮を施
し、さらに該繊維中の酢酸セルロースを85%以上溶剤
にて抽出除去することを特徴とする保水性の良好な多孔
性アクリル系繊維の製造方法。(2) A spinning stock solution prepared by dissolving and mixing a polymer mixture of 50 to 85% by weight of an acrylonitrile polymer containing 85% by weight or more of acrylonitrile and 50 to 15% by weight of cellulose acetate in a solvent is spun, and then 2 A porous acrylic type material with good water retention, which is characterized by stretching the fiber to 5 times or more, shrinking it by 5% or more through drying relaxation treatment, and further extracting and removing 85% or more of the cellulose acetate in the fiber with a solvent. Fiber manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16893990A JPH0457911A (en) | 1990-06-27 | 1990-06-27 | Porous actylic yarn having excellent water retention and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16893990A JPH0457911A (en) | 1990-06-27 | 1990-06-27 | Porous actylic yarn having excellent water retention and its production |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0457911A true JPH0457911A (en) | 1992-02-25 |
Family
ID=15877346
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16893990A Pending JPH0457911A (en) | 1990-06-27 | 1990-06-27 | Porous actylic yarn having excellent water retention and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0457911A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006109440A1 (en) * | 2005-03-30 | 2006-10-19 | Kaneka Corporation | Process for production of lightweight acrylic synthetic fiber |
JP2007182641A (en) * | 2006-01-05 | 2007-07-19 | Mitsubishi Rayon Co Ltd | Acrylic conjugate fiber and nonwoven fabric containing the same, and method for producing the acrylic conjugate fiber |
USRE47038E1 (en) | 2002-04-19 | 2018-09-11 | Bose Corporation | Multichannel power amplifying |
-
1990
- 1990-06-27 JP JP16893990A patent/JPH0457911A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE47038E1 (en) | 2002-04-19 | 2018-09-11 | Bose Corporation | Multichannel power amplifying |
WO2006109440A1 (en) * | 2005-03-30 | 2006-10-19 | Kaneka Corporation | Process for production of lightweight acrylic synthetic fiber |
JP2007182641A (en) * | 2006-01-05 | 2007-07-19 | Mitsubishi Rayon Co Ltd | Acrylic conjugate fiber and nonwoven fabric containing the same, and method for producing the acrylic conjugate fiber |
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