JPS641586B2 - - Google Patents
Info
- Publication number
- JPS641586B2 JPS641586B2 JP3511580A JP3511580A JPS641586B2 JP S641586 B2 JPS641586 B2 JP S641586B2 JP 3511580 A JP3511580 A JP 3511580A JP 3511580 A JP3511580 A JP 3511580A JP S641586 B2 JPS641586 B2 JP S641586B2
- Authority
- JP
- Japan
- Prior art keywords
- polyvinyl alcohol
- water
- temperature
- sizing
- alcohol resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 51
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 51
- 238000004513 sizing Methods 0.000 claims description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 229920005989 resin Polymers 0.000 claims description 24
- 239000011347 resin Substances 0.000 claims description 24
- 239000000203 mixture Substances 0.000 claims description 18
- 239000002245 particle Substances 0.000 claims description 12
- 229920003169 water-soluble polymer Polymers 0.000 claims description 9
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims 1
- 125000000542 sulfonic acid group Chemical group 0.000 claims 1
- 238000009941 weaving Methods 0.000 description 14
- 239000007788 liquid Substances 0.000 description 13
- 238000001035 drying Methods 0.000 description 12
- 239000003292 glue Substances 0.000 description 12
- 239000003921 oil Substances 0.000 description 12
- 238000004026 adhesive bonding Methods 0.000 description 11
- 238000006116 polymerization reaction Methods 0.000 description 11
- 238000009499 grossing Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 239000000243 solution Substances 0.000 description 9
- 238000007127 saponification reaction Methods 0.000 description 8
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 7
- 229920001577 copolymer Polymers 0.000 description 7
- 238000009472 formulation Methods 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- 229920002472 Starch Polymers 0.000 description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000008107 starch Substances 0.000 description 5
- 235000019698 starch Nutrition 0.000 description 5
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 4
- 238000005299 abrasion Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- JHUFGBSGINLPOW-UHFFFAOYSA-N 3-chloro-4-(trifluoromethoxy)benzoyl cyanide Chemical compound FC(F)(F)OC1=CC=C(C(=O)C#N)C=C1Cl JHUFGBSGINLPOW-UHFFFAOYSA-N 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000021615 conjugation Effects 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- 229920000881 Modified starch Polymers 0.000 description 2
- 239000004368 Modified starch Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 150000008064 anhydrides Chemical class 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 2
- 150000001735 carboxylic acids Chemical class 0.000 description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000001530 fumaric acid Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 235000019426 modified starch Nutrition 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- NBOCQTNZUPTTEI-UHFFFAOYSA-N 4-[4-(hydrazinesulfonyl)phenoxy]benzenesulfonohydrazide Chemical compound C1=CC(S(=O)(=O)NN)=CC=C1OC1=CC=C(S(=O)(=O)NN)C=C1 NBOCQTNZUPTTEI-UHFFFAOYSA-N 0.000 description 1
- FHVDTGUDJYJELY-UHFFFAOYSA-N 6-{[2-carboxy-4,5-dihydroxy-6-(phosphanyloxy)oxan-3-yl]oxy}-4,5-dihydroxy-3-phosphanyloxane-2-carboxylic acid Chemical compound O1C(C(O)=O)C(P)C(O)C(O)C1OC1C(C(O)=O)OC(OP)C(O)C1O FHVDTGUDJYJELY-UHFFFAOYSA-N 0.000 description 1
- 244000215068 Acacia senegal Species 0.000 description 1
- 229920001817 Agar Polymers 0.000 description 1
- 102000009027 Albumins Human genes 0.000 description 1
- 108010088751 Albumins Proteins 0.000 description 1
- 241000416162 Astragalus gummifer Species 0.000 description 1
- 108010076119 Caseins Proteins 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 244000050403 Iris x germanica Species 0.000 description 1
- 235000002971 Iris x germanica Nutrition 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 239000004373 Pullulan Substances 0.000 description 1
- 229920001218 Pullulan Polymers 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 229920001615 Tragacanth Polymers 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical class C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229940048053 acrylate Drugs 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 229940023476 agar Drugs 0.000 description 1
- 235000010419 agar Nutrition 0.000 description 1
- 229940072056 alginate Drugs 0.000 description 1
- 235000010443 alginic acid Nutrition 0.000 description 1
- 229920000615 alginic acid Polymers 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 235000010418 carrageenan Nutrition 0.000 description 1
- 239000000679 carrageenan Substances 0.000 description 1
- 229920001525 carrageenan Polymers 0.000 description 1
- 229940113118 carrageenan Drugs 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 229940099112 cornstarch Drugs 0.000 description 1
- LDHQCZJRKDOVOX-NSCUHMNNSA-N crotonic acid Chemical compound C\C=C\C(O)=O LDHQCZJRKDOVOX-NSCUHMNNSA-N 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- NKHAVTQWNUWKEO-UHFFFAOYSA-N fumaric acid monomethyl ester Natural products COC(=O)C=CC(O)=O NKHAVTQWNUWKEO-UHFFFAOYSA-N 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- -1 konjac mannan Polymers 0.000 description 1
- 229940025902 konjac mannan Drugs 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- NKHAVTQWNUWKEO-IHWYPQMZSA-N methyl hydrogen fumarate Chemical compound COC(=O)\C=C/C(O)=O NKHAVTQWNUWKEO-IHWYPQMZSA-N 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 150000002763 monocarboxylic acids Chemical class 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 238000002360 preparation method 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
- 235000019423 pullulan Nutrition 0.000 description 1
- 238000009790 rate-determining step (RDS) Methods 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 150000003460 sulfonic acids Chemical class 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- LDHQCZJRKDOVOX-UHFFFAOYSA-N trans-crotonic acid Natural products CC=CC(O)=O LDHQCZJRKDOVOX-UHFFFAOYSA-N 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- NLVXSWCKKBEXTG-UHFFFAOYSA-N vinylsulfonic acid Chemical compound OS(=O)(=O)C=C NLVXSWCKKBEXTG-UHFFFAOYSA-N 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Description
本発明は高濃度でかつ低温での糊付が可能な経
糸糊付用組成物及び該組成物を用いた経糸糊付方
法に関するものである。
従来経糸糊付方式としては、たとえば紡績糸の
場合、デンプン、ポリビニルアルコール、アクリ
ル系糊剤、平滑油剤等を適当な比率の組成にし、
一般に15%以下の濃度の水溶液として糊付を行う
方式がとられているが、この方式においてはデン
プン成分の糊化を図るために、糊炊きは蒸気吹込
式撹拌溶解装置又は高圧クツカーを用い温度95〜
120℃で15分ないし2時間程度かけて行わねばな
らないので、糊炊きに要するエネルギー(蒸気)
が大きい。又糊付工程は上記の如くして得られた
糊液を80〜95℃に保ち、絞り率、即ち
糊着量/糊液濃度×100(%)
は100〜150%の範囲とするのが通常であるが、糊
液の温度をこのように比較的高く保つことはエネ
ルギー上不利であるし、絞り率がこのように高い
ことは乾燥工程において蒸発すべき水分量も多く
なり、やはりエネルギー上不利である。
本発明は上記のような従来の問題点を根本的に
解決したものである。
本発明の糊付用組成物は、50℃未満の温度の水
に可溶の水溶性高分子(A)及び50℃以上のある温度
で水に急速に溶解しはじめるポリビニルアルコー
ル系樹脂(B)よりなる。
又本発明の経糸糊付方法は、50℃未満の温度の
水に可溶の水溶性高分子(A)の水溶液中に、50℃以
上のある温度で水に急速に溶解するポリビニルア
ルコール系樹脂(B)の粒子が分散している状態の糊
液を用いて、経糸の糊付を行うことを特徴とする
ものである。
本発明においては糊液中のポリビニルアルコー
ル系樹脂(B)は膨潤粒子として分散しており、溶解
はしていない。つまりポリビニルアルコール系樹
脂(B)の糊化を必要としないので、糊液調製にあた
つての加熱は水溶性高分子(A)が溶解するに足る温
度にするだけでよく、糊液調製に要するエネルギ
ーが少なくてすむ。又糊付時の糊液温度もポリビ
ニルアルコール系樹脂(B)の溶解開始温度以下に保
つだけで充分であるので、糊付中の糊液温度維持
に要するエネルギーも少なくてすむ。さらに本発
明においてはポリビニルアルコール系樹脂(B)が糊
液中に分散しているのみで溶解はしていないので
ポリビニルアルコール系樹脂(B)による系の増粘は
小さく、従つてたとえば15〜30重量%というよう
に高濃度の糊液としても糊付操作上支障は生じな
い。そして本発明においては絞り率は90%以下、
通常は30〜80%と従来法に比し半分程度とするこ
とができる。これは従来法と同程度の着量にする
と蒸発すべき水分量も半分程度となることを意味
し、乾燥に要するエネルギーが半減できること、
或いは糊付工程の律速段階である乾燥速度を倍加
することができるので生産性の向上が図られるこ
となどの利点となる。
そして本発明においてはポリビニルアルコール
系樹脂(B)の粒子は糊液中において適度に膨潤して
おり、糊付後の乾燥工程において膨潤粒子は糊化
され連続皮膜となり、製織性の良好な耐摩性、抱
合性の良い糊付糸が得られる。
本発明の経糸糊付用組成物は
50℃未満の温度の水に可溶の水溶性高分子(A)
50℃以上のある温度で水に急速に溶解しはじめ
るポリビニルアルコール系樹脂(B)
の各成分よりなる。
水溶性高分子(A)としては、50℃未満の温度の水
に可溶の高分子であれば天然高分子又はその変性
物、合成高分子のいずれもが用いられる。このよ
うな高分子としては、ポリビニルアルコール系樹
脂、ポリアクリルアミド、アクリルアミド−アク
リル酸ソーダ共重合体、ポリアクリル酸又はその
塩、アクリル酸エステル−アクリル酸塩共重合
体、ポリビニルピロリドン、ポリエチレンオキシ
ド、メチルセルロース、カルボキシメチルセルロ
ース、化工澱粉、変性澱粉、デキストリン、プル
ラン、ニカワ、ゼラチン、カゼイン、アルブミ
ン、アラビアゴム、トラガントゴム、フノリ、寒
天、コンニヤクマンナン、アルギン酸塩、カラギ
ーナン、ザンタンガム、グアーガムなどがあげら
れる。
これらの中では本発明の経糸糊付の目的にとつ
てポリビニルアルコール系樹脂が望ましく、50℃
未満の温度の水の可溶の範囲で任意の重合度、ケ
ン化度のポリ酢酸ビニルケン化物(ポリビニルア
ルコール)、なかんづく重合度200〜3000、ケン化
度65〜93モル%のポリビニルアルコールのほか、
酢酸ビニルを主体とし、これと他のコモノマー、
たとえば不飽和カルボン酸又はその塩・部分又は
完全エステル・無水物・ニトリル・アミド、不飽
和カルボン酸又はその塩、炭素酸2〜30のα−オ
レフイン、ビニルエーテル、酢酸ビニル以外のビ
ニルエステル、塩化ビニルなどとの共重合体のケ
ン化物(共重合変性ポリビニルアルコール)やポ
リビニルアルコール又は共重合変性ポリビニルア
ルコールをウレタン化、エーテル化、エステル
化、アセタール化、グラフト化したもの(後変性
ポリビニルアルコール)も用いられ、さらにこれ
らの中でもアクリル酸、メタクリル酸、クロトン
酸などの不飽和モノカルボン酸又はその塩、マレ
イン酸、フマール酸、イタコン酸などの不飽和ジ
カルボン酸又はその塩・部分エステル・無水物、
エチレンスルホン酸、アリルスルホン酸、メタア
リルスルホン酸などの不飽和スルホン酸又はその
塩を0.02〜15モル%、なかんづく0.05〜10モル%
共重合しかつ酢酸ビニル成分のケン化度を50〜
100モル%とした不飽酸変性ポリビニルアルコー
ルが特に好ましい。
50℃以上のある温度で水に急速に溶解しはじめ
るポリビニルアルコール系樹脂(B)とは、一般的に
はブラベンダーアミログラフにて5〜20%の固形
分濃度で糊化挙動を測定したとき、その温度−粘
度曲線において粘度が急に上昇しはじめる温度即
ち溶解開始温度が50℃以上であるようなものをい
う。このような性質を示すポリビニルアルコール
系樹脂(B)は、たとえば重合度200〜3000、ケン化
度70モル%以上のポリビニルアルコール又は共重
合変性ポリビニルアルコールや後変性ポリビニル
アルコールを乾熱処理、湿熱処理等の熱処理をす
ることによつて取得される。
かかるポリビニルアルコール系樹脂(B)の粒度は
特に限定はないが、一般には微粉の方が好まし
く、たとええば10〜100μのものが使われる。
上記水溶性高分子(A)とポリビニルアルコール系
樹脂(B)との配合割合は重量比で10:90〜50:50と
なるような範囲から選ぶことが特に望ましい。(A)
が余りに少ないと製織時糊付糸の耐摩耗性を損な
つて製織効率の低下を招き、一方(B)の割合が余り
に少ないと有効な高濃度糊付用組成物が得られな
いという傾向があるからである。
水溶性高分子(A)とポリビニルアルコール系樹脂
(B)とよりなる糊液の調製は、(A)の粉体と(B)の粉体
との混合粉体を水に投入し加熱撹拌して(A)のみを
溶解する方法、(A)の水溶液中に(B)の粉体を混合す
る方法などが採用される。糊液には必要に応じ各
種の油剤、助剤、その他の公知の添加剤が適宜配
合できる。糊液中の固形分濃度は5〜30重量%と
することができ、この中では10〜30重量%、さら
には15〜30重量%の範囲が特に好ましく、このよ
うに高濃度の糊液とすることができることが本発
明の特長の一つである。固形分濃度が5重量%未
満では低濃度となるため糊着量のコントロールが
難しくなり、一方30重量%を越えるようになると
表面付着となつて糊付特性を低下させる。
糊液は約30℃以上でポリビニルアルコール系樹
脂(B)の溶解開始温度以下に保たれ、糊付操作が行
われる。即ち糊液中では水溶性高分子(A)は溶解し
て溶液となつているが、ポリビニルアルコール系
樹脂(B)の粒子はこの溶液中に分散しているのであ
る。
糊付後の乾燥温度は80〜160℃の条件が選ばれ
るが、ポリビニルアルコール系樹脂(B)の粒子を瞬
間溶解し、皮膜を形成させるためになるべく高い
温度がよく、特に100℃以上の温度とすることが
望まれる。乾燥方式はホツトエアー乾燥、シリン
ダー乾燥のいずれであつても差支えない。
対象とする原糸は紡績糸、フイラメント糸のい
ずれもが用いられる。
次に実施例をあげて本発明の組成物及び方法を
さらに説明する。以下糊処方において単に「%」
とあるのは「重量%」を示すものとする。
なお強度、伸度は、オートグラフにて試料長
500mm、引張速度500mm/minにて測定した。又摩
擦試験は、TM式抱合力試験にて荷重400g/20
本で500回摩擦し、摩擦前後の糊付糸の毛羽状態
を観察し、1級(良)〜5級(悪)で判定した。
実施例 1
次の条件で経糸の糊付、乾燥を行い、さらに製
織を行つた。
糊処方
重合度1700、ケン化度87モル%の水溶性ポリビ
ニルアルコール(A) 5.1%
重合度1400、ケン化度99.4モル%、平均粒子径
20μ、溶解開始温度73℃の熱処理ポリビニルア
ルコール(B) 11.9%
平滑性油剤(互応化学工業株式会社製サイテツ
クスNo.315) 1.0%
水 残り
冷水に(A)の粉末を加えて撹拌後50℃まで昇温し
て溶解し、ついで(B)と油剤を加えて撹拌後50〜60
℃に保つた。(A)は溶解しているが(B)はスラリー状
に分散しており、糊液中の樹脂分は17.0%であ
る。
対象糸
ポリエステル/綿=65/35混紡糸
織物組織=45′S×45′S/110×60×巾47″×5121本
糊付条件
糊温度 50〜55℃
糊付速度 100Yd/min
糊付ロール絞り圧 1.0〜1.2Kg/cm2
糊付機 ズツカー(Sucker)社製11C(マルチ・
シリンダー)タイプ
乾燥温度
シリンダー 120℃〜130℃
着糊率 13.5%
絞り率 75%
製織条件
織 機 TOYODA自動織機GL−8
回転数 180rpm
織機室条件 25〜30℃、70〜80%RH
結果は、糊付糸強度298g、伸度8.3%、製織率
91%、TM式抱合度試験機による耐摩性2級を好
ましいものであつた。
対照例 1
次の条件で経糸の糊付、乾燥を行い、さらに製
織を行つた。この対照例は従来の典型的なポリビ
ニルアルコール/デンプン処方の例である。
糊処方
実施例1で用いたポリビニルアルコール(A)
4.8%
コーンスターチ 3.7%
油剤(ユシロ化学工業株式会社製ソルビル・ワ
ツクスSX−135A) 0.5%
水 残り
上記各成分を90〜95℃で2時間加熱混合して均
一な糊液を調製し、熱水で希釈して固形分9.0%
となるようにした。
対象糸
実施例1と同じ
糊付条件
糊温度 90〜95℃
糊付速度 50Yd/min
着糊率 14.1%
絞り率 157%
(糊ロール絞り圧、糊付機、乾燥温度は実施例1
と同じ条件)
製織条件
実施例1と同じ
結果は、糊糸強度291g、伸度8.0%、製織効率
88%、耐摩性4級であつた。
対照例 2
糊処方
実施例1で用いたポリビニルアルコール(A)
3.0%
実施例1で用いたポリビニルアルコール(B)
7.0%
平滑性油剤(対照例1で用いたもの) 0.5%
水 残り
上記各成分を80〜90℃で1.5時間加熱混合して
均一な糊液を調製し、熱水で希釈して樹脂分10%
となるようにした。
上記糊処方としたほかは対照例1と同様にして
糊付、乾燥、製織を行つた。ただし着糊率を13.6
%、効り率を130%とした。
結果は、糊付糸強度297g、伸度8.3%、製織効
率90%、耐摩性3〜4級であつた。
実施例1と対照例1、2とを比較すると、糊付
糸物性や製織性を別としても所要エネルギーの点
で次表のような差がある。
The present invention relates to a warp sizing composition capable of sizing at high concentrations and at low temperatures, and a warp sizing method using the composition. Conventional warp sizing methods include, for example, in the case of spun yarn, starch, polyvinyl alcohol, acrylic sizing agents, smoothing oils, etc. are mixed in appropriate proportions.
Generally, a method is used in which sizing is carried out as an aqueous solution with a concentration of 15% or less, but in this method, in order to gelatinize the starch component, the sizing is done using a steam-blown stirring dissolving device or a high-pressure cooker. 95~
The energy (steam) required to cook the paste is 15 minutes to 2 hours at 120℃.
is large. In addition, in the sizing process, the sizing liquid obtained as described above is maintained at 80 to 95°C, and the squeezing rate, that is, sizing amount/sizing liquid concentration x 100 (%), is in the range of 100 to 150%. Normally, it is disadvantageous in terms of energy to maintain the temperature of the size liquid at such a relatively high temperature, and a high squeezing ratio means that the amount of water that must be evaporated during the drying process is also large, which also causes an energy disadvantage. It is disadvantageous. The present invention fundamentally solves the conventional problems as described above. The gluing composition of the present invention comprises a water-soluble polymer (A) that is soluble in water at a temperature of less than 50°C and a polyvinyl alcohol resin (B) that rapidly begins to dissolve in water at a temperature of 50°C or higher. It becomes more. In addition, the warp sizing method of the present invention includes adding a polyvinyl alcohol resin that rapidly dissolves in water at a temperature of 50°C or higher into an aqueous solution of a water-soluble polymer (A) that is soluble in water at a temperature of lower than 50°C. This method is characterized in that the warp yarns are sized using a sizing liquid in which the particles of (B) are dispersed. In the present invention, the polyvinyl alcohol resin (B) in the size liquid is dispersed as swollen particles and is not dissolved. In other words, since gelatinization of the polyvinyl alcohol resin (B) is not required, the heating required for preparing the size solution is only required to a temperature sufficient to dissolve the water-soluble polymer (A). It requires less energy. Furthermore, since it is sufficient to maintain the temperature of the size liquid during gluing at a temperature below the melting start temperature of the polyvinyl alcohol resin (B), less energy is required to maintain the temperature of the size liquid during gluing. Furthermore, in the present invention, since the polyvinyl alcohol resin (B) is only dispersed in the size liquid and not dissolved, the increase in viscosity of the system due to the polyvinyl alcohol resin (B) is small. Even if the sizing liquid has a high concentration such as % by weight, there will be no problem in the sizing operation. In the present invention, the aperture ratio is 90% or less,
Usually it is 30 to 80%, which is about half that of the conventional method. This means that the amount of water that must be evaporated is about half that of the conventional method, which means that the energy required for drying can be halved.
Alternatively, the drying rate, which is the rate-determining step in the gluing process, can be doubled, resulting in advantages such as improved productivity. In the present invention, the particles of the polyvinyl alcohol resin (B) are moderately swollen in the size solution, and in the drying process after pasting, the swollen particles are gelatinized to form a continuous film, which has good weavability and abrasion resistance. , a sizing thread with good conjugation properties can be obtained. The warp sizing composition of the present invention consists of a water-soluble polymer (A) that is soluble in water at a temperature of less than 50°C, and a polyvinyl alcohol resin (B) that begins to rapidly dissolve in water at a temperature of 50°C or higher. Consists of each component. As the water-soluble polymer (A), any of natural polymers, modified products thereof, and synthetic polymers can be used as long as they are soluble in water at a temperature of less than 50°C. Examples of such polymers include polyvinyl alcohol resin, polyacrylamide, acrylamide-sodium acrylate copolymer, polyacrylic acid or its salt, acrylic ester-acrylate copolymer, polyvinylpyrrolidone, polyethylene oxide, and methyl cellulose. , carboxymethyl cellulose, modified starch, modified starch, dextrin, pullulan, glue, gelatin, casein, albumin, gum arabic, gum tragacanth, fleur-de-lis, agar, konjac mannan, alginate, carrageenan, xanthan gum, guar gum, etc. Among these, polyvinyl alcohol resin is preferable for the purpose of warp sizing of the present invention, and
In addition to saponified polyvinyl acetate (polyvinyl alcohol) with any degree of polymerization and saponification within the range of water solubility at temperatures below, especially polyvinyl alcohol with a degree of polymerization of 200 to 3000 and a degree of saponification of 65 to 93 mol%,
Mainly vinyl acetate, this and other comonomers,
For example, unsaturated carboxylic acids or their salts, partial or complete esters, anhydrides, nitriles, amides, unsaturated carboxylic acids or their salts, α-olefins with 2 to 30 carbon acids, vinyl ethers, vinyl esters other than vinyl acetate, vinyl chloride. Saponified products of copolymers (copolymerized modified polyvinyl alcohol) and polyvinyl alcohol or copolymerized modified polyvinyl alcohol that is urethanized, etherified, esterified, acetalized, or grafted (post-modified polyvinyl alcohol) are also used. Furthermore, among these, unsaturated monocarboxylic acids or their salts such as acrylic acid, methacrylic acid, and crotonic acid, unsaturated dicarboxylic acids such as maleic acid, fumaric acid, and itaconic acid, or their salts, partial esters, anhydrides,
0.02 to 15 mol%, especially 0.05 to 10 mol% of unsaturated sulfonic acids or salts thereof such as ethylene sulfonic acid, allyl sulfonic acid, metaallylsulfonic acid, etc.
Copolymerized and the degree of saponification of vinyl acetate component is 50~
Particularly preferred is unsaturated acid-modified polyvinyl alcohol containing 100 mol%. Polyvinyl alcohol resin (B), which begins to rapidly dissolve in water at a temperature of 50℃ or higher, generally dissolves when its gelatinization behavior is measured using a Brabender amylograph at a solid content concentration of 5 to 20%. , the temperature at which the viscosity begins to rise suddenly in the temperature-viscosity curve, that is, the melting start temperature, is 50°C or higher. Polyvinyl alcohol resin (B) exhibiting such properties can be obtained by, for example, polyvinyl alcohol with a degree of polymerization of 200 to 3000 and a degree of saponification of 70 mol% or more, or copolymerized modified polyvinyl alcohol, or post-modified polyvinyl alcohol, which is subjected to dry heat treatment, moist heat treatment, etc. It is obtained by heat treatment. Although the particle size of the polyvinyl alcohol resin (B) is not particularly limited, it is generally preferable to use a fine powder, for example, a particle size of 10 to 100 μm is used. It is particularly desirable that the mixing ratio of the water-soluble polymer (A) and the polyvinyl alcohol resin (B) be selected from a range of 10:90 to 50:50 by weight. (A)
If the proportion of (B) is too small, the abrasion resistance of the sizing yarn during weaving will be impaired, leading to a decrease in weaving efficiency, while if the proportion of (B) is too small, an effective high-concentration sizing composition cannot be obtained. Because there is. Water-soluble polymer (A) and polyvinyl alcohol resin
(B) can be prepared by adding a mixed powder of powders (A) and (B) to water and heating and stirring to dissolve only (A); A method such as mixing powder of (B) into an aqueous solution of (B) is adopted. Various oils, auxiliary agents, and other known additives can be appropriately blended into the size liquid, if necessary. The solid content concentration in the size liquid can be 5 to 30% by weight, and within this range, a range of 10 to 30% by weight, and more preferably 15 to 30% by weight, is particularly preferable. One of the features of the present invention is that it can be done. If the solid content concentration is less than 5% by weight, the concentration will be low and it will be difficult to control the amount of adhesive, while if it exceeds 30% by weight, it will adhere to the surface and deteriorate the adhesive properties. The sizing liquid is kept at about 30° C. or higher and below the melting temperature of the polyvinyl alcohol resin (B), and the sizing operation is performed. That is, in the paste liquid, the water-soluble polymer (A) is dissolved to form a solution, but the particles of the polyvinyl alcohol resin (B) are dispersed in this solution. The drying temperature after gluing is selected to be 80 to 160℃, but in order to instantly dissolve the particles of polyvinyl alcohol resin (B) and form a film, it is best to use a temperature as high as possible, especially a temperature of 100℃ or higher. It is desirable that The drying method may be either hot air drying or cylinder drying. Both spun yarn and filament yarn are used as target raw yarn. The composition and method of the present invention will now be further explained with reference to Examples. In the following glue prescriptions, simply "%"
``%'' indicates "% by weight." The strength and elongation are determined based on the sample length in the autograph.
Measured at 500 mm and tensile speed of 500 mm/min. In addition, the friction test is a TM type binding force test with a load of 400g/20
The fibers were rubbed with a book 500 times, and the fuzz condition of the glued yarn before and after the friction was observed and evaluated from grade 1 (good) to grade 5 (bad). Example 1 The warp yarns were sized and dried under the following conditions, and further weaving was performed. Glue recipe Water-soluble polyvinyl alcohol (A) 5.1% with degree of polymerization 1700, degree of saponification 87 mol%, degree of polymerization 1400, degree of saponification 99.4 mol%, average particle size
20 μ, heat-treated polyvinyl alcohol (B) with a melting start temperature of 73°C 11.9% Smoothing oil (Cytecs No. 315 manufactured by Gooh Kagaku Kogyo Co., Ltd.) 1.0% Water Remaining Add the powder of (A) to cold water and stir until 50°C. Raise the temperature to dissolve, then add (B) and oil and stir for 50 to 60 minutes.
It was kept at ℃. (A) is dissolved, but (B) is dispersed in a slurry form, and the resin content in the size solution is 17.0%. Target yarn Polyester/cotton = 65/35 blended yarn Textile structure = 45'S x 45'S/110 x 60 x Width 47'' x 5121 strands Sizing conditions Sizing temperature 50-55℃ Sizing speed 100 Yd/min Sizing roll Squeezing pressure 1.0-1.2Kg/cm 2 Gluing machine Sucker 11C (Multi
Cylinder) type Drying temperature Cylinder 120℃~130℃ Sizing rate 13.5% Squeezing rate 75% Weaving conditions Loom TOYODA automatic loom GL-8 Rotation speed 180rpm Loom room conditions 25~30℃, 70~80%RH The result is glue Yarn strength 298g, elongation 8.3%, weaving rate
The abrasion resistance was 91%, and the wear resistance was 2nd grade by the TM type conjugation degree tester. Comparative Example 1 The warp threads were pasted and dried under the following conditions, and further weaving was performed. This control example is an example of a typical conventional polyvinyl alcohol/starch formulation. Glue formulation Polyvinyl alcohol (A) used in Example 1
4.8% Cornstarch 3.7% Oil agent (Solvil Wax SX-135A manufactured by Yushiro Chemical Co., Ltd.) 0.5% Water Remaining The above ingredients were heated and mixed at 90 to 95℃ for 2 hours to prepare a uniform paste solution, and mixed with hot water. Diluted to 9.0% solids
I made it so that Target yarn Same sizing conditions as Example 1 Sizing temperature 90-95℃ Sizing speed 50 Yd/min Sizing rate 14.1% Squeezing rate 157% (Glue roll squeezing pressure, sizing machine, and drying temperature are the same as in Example 1.
Same conditions as in Example 1) Weaving conditions Same as Example 1 The results were: glue strength 291g, elongation 8.0%, weaving efficiency
The wear resistance was 88%, grade 4. Control example 2 Glue formulation Polyvinyl alcohol (A) used in Example 1
3.0% Polyvinyl alcohol (B) used in Example 1
7.0% Smoothing oil (used in Control Example 1) 0.5% Water Remaining The above ingredients were heated and mixed at 80-90℃ for 1.5 hours to prepare a uniform paste solution, and diluted with hot water to obtain a resin content of 10%. %
I made it so that Sizing, drying, and weaving were carried out in the same manner as in Control Example 1, except that the above-mentioned glue formulation was used. However, the glue rate is 13.6
%, the efficacy rate was set at 130%. As a result, the strength of the sized yarn was 297 g, the elongation was 8.3%, the weaving efficiency was 90%, and the abrasion resistance was grade 3-4. Comparing Example 1 and Comparative Examples 1 and 2, apart from the sizing yarn physical properties and weavability, there are differences in required energy as shown in the following table.
【表】
即ち実施例1によれば対照例2、3に比し、糊
液調製、糊液温度維持、乾燥における蒸気等のエ
ネルギーの節約が大巾に図られ、又生産性が大巾
に向上できることがわかる。
実施例 2〜7
次の糊処方によりポリエステル/綿混紡糸の糊
付を実施例1の場合と同様にして行い、ついで製
織に供した。
実施例 2
アリルスルホン酸ソーダ含量0.8%のアリルス
ルホン酸ソーダー酢酸ビニル共重合体の酢酸ビ
ニル成分の80モル%をケン化して得られた重合
度600のアリルスルホン酸ソーダ変性ポリビニ
ルアルコール(A) 9.0%
実施例1で用いたポリビニルアルコール(B)
11.0%
平滑性油剤(松本油脂製薬株式会社製サイジン
グ・ワツクスV2) 1.0%
水 残り
実施例 3
マレイン酸モノメチル含量2.0モル%のマレイ
ン酸モノメチル−酢酸ビニル共重合体の酢酸ビ
ニル成分の92モル%をケン化して得られた重合
度1700のマレイン酸モノメチル変性ポリビニル
アルコール(A) 4.8%
重合度600、ケン化度96モル%、平均粒子径
35μ、溶解開始温度64℃の熱処理ポリビニルア
ルコール(B) 13.7%
平滑性油剤(共栄社油脂化学工業株式会社製
TY−653) 1.0%
水 残り
実施例 4
フマール酸含量1.2モル%のフマール酸−酢酸
ビニル共重合の酢酸ビニル成分の94モル%をケ
ン化して得られた重合度1400のフマール酸変性
ポリビニルアルコール(A) 6.2%
実施例3で用いたポリビニルアルコール(B)
13.3%
平滑性油剤(実施例3で用いたもの) 1.0%
水 残り
実施例 5
アクリル酸含量1.5モル%のアクリル酸−酢酸
ビニル共重合体の酢酸ビニル成分の95モル%を
ケン化して得られた重合度1100のアクリル酸変
性ポリビニルアルコール(A) 6.5%
重合度500、ケン化度94.0モル%、平均粒子径
80μ、溶解開始温度57℃の熱処理ポリビニルア
ルコール(B) 11.5%
平滑性油剤(実施例2で用いたもの) 1.0%
水 残り
実施例 6
カルボキシメチル化澱粉(西独エムスランド社
製EMSIZE CMS)(A) 5.0%
実施例1で用いたポリビニルアルコール(B)
12.0%
平滑性油剤(実施例1で用いたもの) 1.0%
水 残り
実施例 7
カルボキシメチルセルロース(第一工業製薬株
式会社製セロゲン7A)(A) 4.5%
実施例3で用いたポリビニルアルコール(B)
20.5%
平滑性油剤(実施例1で用いたもの) 1.5%
水 残り
上記実施例2〜7の結果を次表に示す。[Table] That is, according to Example 1, compared to Control Examples 2 and 3, energy such as steam during size solution preparation, size solution temperature maintenance, and drying was greatly saved, and productivity was also greatly improved. I know that I can improve. Examples 2 to 7 Polyester/cotton blend yarns were sized in the same manner as in Example 1 using the following sizing formulations, and then subjected to weaving. Example 2 Sodium allylsulfonate modified polyvinyl alcohol (A) with a degree of polymerization of 600 obtained by saponifying 80 mol% of the vinyl acetate component of a sodium allylsulfonate vinyl acetate copolymer with a sodium allylsulfonate content of 0.8% 9.0 % Polyvinyl alcohol (B) used in Example 1
11.0% Smoothing oil (Sizing Wax V 2 manufactured by Matsumoto Yushi Pharmaceutical Co., Ltd.) 1.0% Water Remaining Example 3 92 mol% of the vinyl acetate component of a monomethyl maleate-vinyl acetate copolymer with a monomethyl maleate content of 2.0 mol% Monomethyl maleate-modified polyvinyl alcohol (A) with a polymerization degree of 1700 obtained by saponifying 4.8% Polymerization degree 600, saponification degree 96 mol%, average particle size
35μ, heat-treated polyvinyl alcohol (B) with a melting start temperature of 64℃ 13.7% smoothing oil (manufactured by Kyoeisha Yushigaku Kogyo Co., Ltd.)
TY-653) 1.0% Water Remaining Example 4 Fumaric acid-modified polyvinyl alcohol with a degree of polymerization of 1400 obtained by saponifying 94 mol% of the vinyl acetate component of a fumaric acid-vinyl acetate copolymer with a fumaric acid content of 1.2 mol% ( A) 6.2% Polyvinyl alcohol (B) used in Example 3
13.3% Smoothing oil (used in Example 3) 1.0% Water Remaining Example 5 Obtained by saponifying 95 mol% of the vinyl acetate component of an acrylic acid-vinyl acetate copolymer with an acrylic acid content of 1.5 mol%. Acrylic acid-modified polyvinyl alcohol (A) 6.5% with a polymerization degree of 1100, polymerization degree of 500, saponification degree of 94.0 mol%, average particle size
80 μ, heat-treated polyvinyl alcohol (B) with a melting start temperature of 57°C 11.5% Smoothing oil (used in Example 2) 1.0% Water Remaining Example 6 Carboxymethylated starch (EMSIZE CMS manufactured by West German Emsland) (A ) 5.0% Polyvinyl alcohol (B) used in Example 1
12.0% Smoothing oil (used in Example 1) 1.0% Water Remaining Example 7 Carboxymethyl cellulose (Celogen 7A manufactured by Daiichi Kogyo Seiyaku Co., Ltd.) (A) 4.5% Polyvinyl alcohol used in Example 3 (B)
20.5% Smoothing oil (used in Example 1) 1.5% Water Residual The results of Examples 2 to 7 are shown in the following table.
【表】
実施例 8
次の条件で経糸の糊付を行い、さらに製織を行
つた。
糊処方
可溶性酢酸化澱粉(サイデン化学工業株式会社
製ツヤノリン)(A) 3.5%
実施例5で用いたポリビニルアルコール(B)
3.5%
柔軟平滑剤(三洋化成工業株式会社製パラレル
AB) 0.3%
水 残り
上記各成分を混合し、50℃にて1時間加熱して
(A)成分のみ溶解し、固形分7.3%となるようにし
た。
この糊液を用いてレーヨン・フイラメント
120dのドビー・クロス(3540本)の糊付、乾燥、
製織を行つた。
糊付条件
糊温度 45℃
糊付速度 120Yd/min
糊付ロール絞り圧 2.0Kg/cm2
糊付機 津田駒工業株式会社製KSJ−H型
乾燥温度
ホツトエアー 110℃
シリンダー 100℃
着糊率 3.9%
絞り率 53%
製織条件
織 機 TOYODA自動織機GFD3(ドビー式)
回転数 160rpm
織機室条件 25〜30℃、65〜75%RH
結果は、糊付糸強度422g、伸度14.5%で抱合
性も良好であり、92%の製織効率が得られた。[Table] Example 8 The warp threads were pasted and weaved under the following conditions. Glue formulation Soluble acetated starch (Tsuyanorin manufactured by Saiden Chemical Industry Co., Ltd.) (A) 3.5% Polyvinyl alcohol used in Example 5 (B)
3.5% Softening and smoothing agent (Parallel manufactured by Sanyo Chemical Industries, Ltd.)
AB) 0.3% water remaining Mix the above ingredients and heat at 50℃ for 1 hour.
Only component (A) was dissolved to give a solid content of 7.3%. Rayon filament using this glue
120d dobby cloth (3540 pieces) glued, dried,
I did some weaving. Gluing conditions Gluing temperature 45℃ Gluing speed 120 Yd/min Gluing roll squeezing pressure 2.0 Kg/cm 2 Gluing machine Tsudakoma Kogyo Co., Ltd. KSJ-H type Drying temperature Hot air 110℃ Cylinder 100℃ Sizing rate 3.9% Squeezing rate 53% Weaving conditions loom TOYODA automatic loom GFD3 (dobby type) rotation speed 160rpm loom room conditions 25~30℃, 65~75%RH The results showed that the sized yarn strength was 422g, the elongation was 14.5%, and the conjugation was good. A weaving efficiency of 92% was obtained.
Claims (1)
の水溶液中に、50℃以上のある温度で水に急速に
溶解しはじめるポリビニルアルコール系樹脂粒子
(B)を、(A)対(B)の割合比が重量で10:90〜50:50と
なる様に分散させてなる経糸糊付用組成物。 2 (A)が50℃未満の温度の水に可溶のポリビニル
アルコール系樹脂である特許請求の範囲第1項記
載の組成物。 3 (A)がカルボキシル基又はスルホン酸基を有す
るコモノマーで0.1〜10モル%共重合変性した変
性ポリビニルアルコールである特許請求の範囲第
1項記載の組成物。 4 (B)が50〜80℃の範囲のある温度で水に急速に
溶解しはじめるタイプのポリビニルアルコール系
樹脂である特許請求の範囲第1項記載の組成物。[Claims] 1. Water-soluble polymer (A) soluble in water at a temperature of less than 50°C
Polyvinyl alcohol resin particles that rapidly begin to dissolve in water at a temperature of 50°C or higher in an aqueous solution of
A warp sizing composition comprising (B) dispersed in a ratio of (A) to (B) of 10:90 to 50:50 by weight. 2. The composition according to claim 1, wherein (A) is a polyvinyl alcohol resin soluble in water at a temperature of less than 50°C. 3. The composition according to claim 1, wherein (A) is a modified polyvinyl alcohol copolymerized with 0.1 to 10 mol% of a comonomer having a carboxyl group or a sulfonic acid group. 4. The composition according to claim 1, wherein (B) is a polyvinyl alcohol resin of a type that begins to dissolve rapidly in water at a certain temperature in the range of 50 to 80°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3511580A JPS56134269A (en) | 1980-03-18 | 1980-03-18 | Warp yarn sizing composition and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3511580A JPS56134269A (en) | 1980-03-18 | 1980-03-18 | Warp yarn sizing composition and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56134269A JPS56134269A (en) | 1981-10-20 |
| JPS641586B2 true JPS641586B2 (en) | 1989-01-12 |
Family
ID=12432923
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3511580A Granted JPS56134269A (en) | 1980-03-18 | 1980-03-18 | Warp yarn sizing composition and method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56134269A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH056943Y2 (en) * | 1985-07-05 | 1993-02-22 | ||
| JPS62231083A (en) * | 1986-03-06 | 1987-10-09 | ユニチカケミカル株式会社 | Sizing of warp yarn |
| JP2670863B2 (en) * | 1989-08-31 | 1997-10-29 | 株式会社ホーネンコーポレーション | Glue |
| EP0498892B1 (en) * | 1990-08-29 | 1995-11-15 | Kuraray Co., Ltd. | Fiber sizing agent |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53103092U (en) * | 1977-01-26 | 1978-08-19 | ||
| JPS54160882A (en) * | 1978-06-08 | 1979-12-19 | Nippon Synthetic Chem Ind | Fiber sizing composition |
| JPS5530413A (en) * | 1978-08-18 | 1980-03-04 | Goo Kagaku Kogyo Kk | Powdery sizing agent for fiber |
-
1980
- 1980-03-18 JP JP3511580A patent/JPS56134269A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56134269A (en) | 1981-10-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2239689C (en) | Method for externally sizing fibrous materials | |
| JPS5959997A (en) | High strength pigment binder for paper coating containing carboxylated vinyl ester alkylacrylic copolymer | |
| KR960009085B1 (en) | Fiber sizing agent | |
| JPS641586B2 (en) | ||
| KR900003355B1 (en) | Polymer composition and protective agent for fibers prepared using the same | |
| CN107075791B (en) | Sizing agent for fiber | |
| WO1994013881A1 (en) | Wet nonwoven cloth and method of manufacturing the same | |
| JPS6312195B2 (en) | ||
| US4248755A (en) | Composition and method for sizing textiles | |
| JP2019105008A (en) | Paste for fiber | |
| JPS6261705B2 (en) | ||
| JPH069845A (en) | Water-base polyvinyl alcohol suspension | |
| JP3204467B2 (en) | Composition for warp paste | |
| JPH0663199B2 (en) | Pigment coating composition for paper | |
| JP3136059B2 (en) | Sizing composition for warp and method for producing the same | |
| US3585070A (en) | Method for sizing textiles | |
| JP2566352B2 (en) | Fiber sizing agent | |
| JPS6360153B2 (en) | ||
| JPS59199867A (en) | Preparation of size liquid for high pressure squeeze | |
| JPH07166472A (en) | Sizing agent for warp | |
| JP3295216B2 (en) | Hot melt sizing agent | |
| JPS6160196B2 (en) | ||
| JP3647208B2 (en) | Textile glue | |
| JPH07102482A (en) | Warp paste | |
| JPS62231083A (en) | Sizing of warp yarn |