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JPS6261705B2 - - Google Patents
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JPS6261705B2 - - Google Patents

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Publication number
JPS6261705B2
JPS6261705B2 JP5187680A JP5187680A JPS6261705B2 JP S6261705 B2 JPS6261705 B2 JP S6261705B2 JP 5187680 A JP5187680 A JP 5187680A JP 5187680 A JP5187680 A JP 5187680A JP S6261705 B2 JPS6261705 B2 JP S6261705B2
Authority
JP
Japan
Prior art keywords
starch
sizing
polyvinyl alcohol
weight
mol
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
Application number
JP5187680A
Other languages
Japanese (ja)
Other versions
JPS56148971A (en
Inventor
Atsuo Sawada
Masatake Uchida
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP5187680A priority Critical patent/JPS56148971A/en
Publication of JPS56148971A publication Critical patent/JPS56148971A/en
Publication of JPS6261705B2 publication Critical patent/JPS6261705B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は高濃度でかつ低温での糊付が可能な経
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、
5〜12%程度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90〜
120℃で15分ないし3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100〜200%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。 しかしてかかる問題点を克服する試みとして、
デンプンをその糊化温度以下の糊液中に分散させ
た状態とし、この糊液を用いて経糸の糊付を行つ
た後水蒸気と接触させてデンプンを糊化し、さら
に乾燥を行うという方法が提案されている(特公
昭41―7904号公報)なおこの方法においてはポリ
ビニルアルコールを使用してよいとされている。
しかしながらこの方法も糊付後水蒸気処理を必須
とするので、エネルギー上及び装置コスト上、さ
らには装置の占有面積が大きくなる点で工業上不
利である。 本発明は上記のような問題点を根本的に解決し
たものである。 本発明の経糸糊付方法は、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0.02〜15モル
%共重合変性した変性ポリビニルアルコール(A)の
水溶液中にデンプン(B)が分散している状態にあ
り、かつ(A)対(B)の使用比が重量で10:90〜70:30
の範囲内にある固形分濃度3〜40重量%の糊液を
用いて経糸の糊液を行い、糊付後直ちに乾燥工程
に供する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デンプンは膨潤粒子
として分散しており、溶解はしていない。つまり
デンプンの糊化を必要としないので、糊液調製に
あたつての加熱はデンプンの糊化開始温度以下に
するだけでよく、糊液調製に要するエネネルギー
が従来法に比し大巾に節減できる。又糊付時の糊
液温度もデンプンの糊化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
るエネルギーも少くてすむ。さらに本発明におい
てはデンプンが糊液中に分散しているのみで溶解
はしていないのでデンプンによる系の増粘効果は
小さく、従つてたとえば13〜40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30〜100%
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、糊付後水蒸気処理を
行うことなく直ちに乾燥工程に供せられるが、こ
の乾燥工程においてデンプンの膨潤粒子は相当部
分が糊化されて連続皮膜となる。又糊化に至らず
なお粒子状で残つている部分も変性ポリビニルア
ルコール(A)により強固に経糸に接着していて剥落
しない。かくして得られた糊付糸がすぐれた耐摩
性、抱合性を発揮するのであり、この場合変性ポ
リビニルアルコール(A)に代えて通常のポリビニル
アルコールを用いたのでは経糸表面に残存してい
る粒子の未糊化部分の固着の程度が小さく、到底
すぐれた耐摩性や抱合性は示しえない。 本発明における変性ポリビニルアルコール(A)と
しては、カルボキシル基又はスルホン酸基を有す
るコモノマーで変性したポリビニルアルコールが
用いられる。 かかるコモノマーとしては、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
ン酸などの不飽和多価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があげられる。 上記の如きコモノマーの共重合割合は0.02〜15
モル%、なかんづく0.05〜10モル%の範囲から選
択され、その割合が余りに小さいと耐摩性、抱合
性が不充分となり、一方その割合が余りに多くて
もかえつて耐摩性、抱合性が劣るようになる。 変性ポリビニルアルコール(A)は上記コモノマー
と酢酸ビニルとの共重合体の酢酸ビニル成分をケ
ン化することによつて取得されるが、酢酸ビニル
成分のケン化度は特に限定はないものの80モル%
以上、なかんづく85モル%以上とすることが好ま
しく、ケン化度が小さくなると糊付糸の耐摩性が
低下する傾向が見られる。 デンプン(B)としては、小麦デンプン、コーンス
ターチ、米デンプン、馬れいしよデンプン、甘し
よデンプン、タピオカデンプン、サゴ椰子デンプ
ンなどの生デンプンが用いられ、これらの中では
実用上コーンスターチ、タピオカデンプンが特に
重要である。又糊化開始温度が50℃以上の低度に
変性したデンプンも用いられ、このような変性デ
ンプンとしては酢酸エステル化デンプン、酸処理
デンプン、カルボキシメチルエーテル化デンプ
ン、ヒドロキシエチルエーテル化デンプンなどが
あげられる。 変性ポリビニルアルコール(A)とデンプン(B)の使
用比は重量で10:90〜70:30の範囲内から選ばれ
る。(A)の割合が余りに小さ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)
の割合が余りに小さいと有効な高濃度糊付ができ
なくなる。特に好ましい範囲は20:80〜60:40で
ある。 なお糊液中には他にデンプン粒子の膨潤割、水
溶性高分子、各種の油剤、助剤等を添加すること
ができる。このうちデンプン粒子の膨潤剤として
は酢酸、乳酸、リンゴ酸、クエン酸、酒石酸、コ
ハク酸、アジピン酸、アクリル酸、フマール酸な
どの酸又はその塩、炭酸ソーダ、アンモニア、第
三リン酸ソーダなどがあげられ、その添加量はデ
ンプン(B)に対して0.1〜10重量%とするのが普通
である。水溶性高分子としては通常の未変性のポ
リビニルアルコール、(A)以外の共重合変性ポリビ
ニルアルコールや後変性ポリビニルアルコール、
メチルセルロース、カルボキシメチルセルロー
ス、ポリビニルピロリドン、アクリルアミド系重
合体、ポリエチレンオキシド、グアーガム、アル
ギン酸ソーダ、ザンタンガム、寒天、カラジーナ
ンなどがあげられる。 糊液の調製は、変性ポリビニルアルコール(A)の
水溶液を作つた後これにデンプン(B)を添加する方
法、(A)と(B)を水中に投入して加温し、(A)のみを溶
解する方法など任意の方法が採用される。ただし
糊液の温度はデンプン(B)の糊化開始温度より低い
温度に保たなければならない。 糊液中の固形分濃度は3重量%以上、通常は3
〜40重量%に設定される。3重量%未満では低粘
度となるため糊着量のコントロールが難しくな
り、一方40重量%を越えると表面付着となり、糊
付特性を低下させる。3〜40重量%の範囲の中で
は13〜40重量%というように高濃度の方が本発明
の特長がより一層生かされる。 糊付は一整サイジング法、ワーピングサイザー
法など通常の糊付機を用いて行われる。糊付後は
直ちに乾燥工程に供せられる。乾燥温度は80〜
160℃、特に100〜150℃とするのが好ましい。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方法をさらに説明
する。なお糊化開始温度とは、ブラベンダーアミ
ログラフにて未変性デンプンの場合は10重量%、
変性デンプンの場合は15重量%の固形分濃度にて
糊化挙動を測定したとき、温度―粘度曲線が立ち
上りはじめる温度を言うものとする。 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 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の変性ポリビニルアルコール 5.1% タピオカデンプン(糊化開始温度67℃) 11.9% 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 上記各成分を50〜60℃で混合。変性ポリビニル
アルコールは溶解しているが、デンプンはスラリ
ー状に分散している。固形分18.0% 対象糸 ポリエンテル/綿=65/35混紡糸 織物組織=45S×45S/110×60×巾47
11×5121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
Sucker社製11C(マルチシリンダー)型 乾燥温度 ホツトエアー 100℃ シリンダー 120℃ 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295g、伸度8.4%、製織効
率94%、TM式抱合度試験機による耐摩性2級と
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 重合度1700、ケン化度87モル%のポリビニル
アルコール 4.8% コーンスターチ(糊化開始温度73℃) 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% (糊付ロール絞り圧、糊付機、乾燥温度は実施
例1と同条件) 製織条件 実施例1と同じ 結果は、糊付糸強度291g、伸度8.0、製織効率
88%、耐摩性4級であつた。 対象例 2 糊処方 実施例1で用いた変性ポリビニルアルコール
4.8% タピオカデンプン(糊化開始温度67℃)
3.7% 油剤(実施例1で用いたもの) 0.7% 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、熱水で希釈して固形分9.0
%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13.4
%、絞り率を149%とした。 結果は、糊付糸強度288g、伸度8.4%、製織効
率90%、耐摩性3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に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 method that allows sizing at high concentrations and at low temperatures. 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.
A method is used in which starch is applied as an aqueous solution with a concentration of about 5 to 12%, but in this method, in order to gelatinize the starch component, a steam-blown stirring dissolving device or a high-pressure cooker is used to cook the starch. Temperature 90~
The energy (steam) required to cook the glue is that it must be done at 120℃ for about 15 minutes to 3 hours.
is large. In the sizing process, the sizing liquid obtained as described above is kept at 80 to 95°C, and the squeezing rate, i.e., sizing amount/sizing liquid concentration x 100 (%), is in the range of 100 to 200%. 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. However, in an attempt to overcome these problems,
A method has been proposed in which starch is dispersed in a size liquid at a temperature below its gelatinization temperature, the warp threads are sized using this size liquid, the starch is gelatinized by contact with steam, and then dried. (Japanese Patent Publication No. 7904/1983), it is said that polyvinyl alcohol may be used in this method.
However, since this method also requires steam treatment after pasting, it is industrially disadvantageous in terms of energy and equipment costs, as well as the fact that the area occupied by the equipment becomes large. The present invention fundamentally solves the above problems. In the warp sizing method of the present invention, starch (B) is dispersed in an aqueous solution of modified polyvinyl alcohol (A) copolymerized with 0.02 to 15 mol% of a comonomer having a carboxyl group or a sulfonic acid group. , and the usage ratio of (A) to (B) is 10:90 to 70:30 by weight.
The warp yarns are sized using a sizing solution with a solid content concentration of 3 to 40% by weight within the range of 3 to 40% by weight, and the warp threads are immediately subjected to a drying process after sizing. In the present invention, starch in the size liquid is dispersed as swollen particles and is not dissolved. In other words, since there is no need to gelatinize the starch, the heating required to prepare the size solution only needs to be below the gelatinization starting temperature of the starch, and the energy required for the size solution preparation is significantly reduced compared to the conventional method. can. Furthermore, since it is sufficient to maintain the temperature of the size solution at the time of sizing at a temperature below the gelatinization start temperature of starch, less energy is required to maintain the temperature of the size solution during sizing. Furthermore, in the present invention, since the starch is only dispersed in the size liquid and not dissolved, the thickening effect of the starch on the system is small, and therefore it is difficult to use a high concentration liquid such as 13 to 40% by weight. However, there is no problem in gluing operation. In the present invention, the aperture ratio is 30 to 100%.
This can be reduced to about half that of the conventional method. This means that when applying the same amount as the conventional method, the amount of water that must be evaporated is about half, which means that the energy required for drying can be halved, or the drying speed, which is the rate-limiting step in the gluing process, can be doubled. This has the advantage of improving productivity. In the present invention, after sizing, the starch is immediately subjected to a drying process without steam treatment, and in this drying process, a considerable portion of the swollen starch particles is gelatinized to form a continuous film. In addition, the particulate portions that have not yet become gelatinized are firmly adhered to the warp threads by the modified polyvinyl alcohol (A) and do not fall off. The sized yarn thus obtained exhibits excellent abrasion resistance and binding properties, and in this case, if ordinary polyvinyl alcohol was used instead of modified polyvinyl alcohol (A), particles remaining on the surface of the warp yarns would be removed. The degree of adhesion of the ungelatinized portion is small, and it cannot exhibit excellent abrasion resistance or conjugation. As the modified polyvinyl alcohol (A) in the present invention, polyvinyl alcohol modified with a comonomer having a carboxyl group or a sulfonic acid group is used. Such comonomers include unsaturated monocarboxylic acids or their salts such as acrylic acid, methacrylic acid, and crotonic acid, unsaturated polycarboxylic acids such as maleic acid, fumaric acid, and itaconic acid, or their salts, partial esters, and anhydrides; Examples include unsaturated sulfonic acids such as ethylene sulfonic acid, allyl sulfonic acid, meta-allylsulfonic acid, and salts thereof. The copolymerization ratio of the above comonomers is 0.02 to 15
mol%, especially from the range of 0.05 to 10 mol%; if the proportion is too small, the wear resistance and conjugation properties will be insufficient, while if the proportion is too high, the abrasion resistance and conjugation properties will be deteriorated. Become. Modified polyvinyl alcohol (A) is obtained by saponifying the vinyl acetate component of a copolymer of the above comonomer and vinyl acetate, and the degree of saponification of the vinyl acetate component is not particularly limited, but is 80 mol%.
Above all, it is preferable that the content is 85 mol% or more, and as the degree of saponification decreases, there is a tendency for the wear resistance of the sized yarn to decrease. As starch (B), raw starches such as wheat starch, corn starch, rice starch, horse starch, amashiyo starch, tapioca starch, and sago coconut starch are used, and among these, corn starch and tapioca starch are particularly useful for practical purposes. is important. Low-modified starches with a gelatinization initiation temperature of 50°C or higher are also used, and examples of such modified starches include acetate esterified starch, acid-treated starch, carboxymethyl etherified starch, and hydroxyethyl etherified starch. It will be done. The ratio of modified polyvinyl alcohol (A) to starch (B) used is selected within the range of 10:90 to 70:30 by weight. If the ratio of (A) is too small, the abrasion resistance of the sized yarn during weaving will be impaired, leading to a decrease in weaving efficiency, while (B)
If the ratio is too small, effective high-density gluing cannot be achieved. A particularly preferred range is 20:80 to 60:40. In addition, swelling fractions of starch particles, water-soluble polymers, various oils, auxiliaries, etc. can be added to the size liquid. Among these, the swelling agents for starch particles include acids such as acetic acid, lactic acid, malic acid, citric acid, tartaric acid, succinic acid, adipic acid, acrylic acid, and fumaric acid, or their salts, soda carbonate, ammonia, tribasic sodium phosphate, etc. The amount added is usually 0.1 to 10% by weight based on starch (B). Water-soluble polymers include ordinary unmodified polyvinyl alcohol, copolymerized modified polyvinyl alcohol other than (A), post-modified polyvinyl alcohol,
Examples include methylcellulose, carboxymethylcellulose, polyvinylpyrrolidone, acrylamide polymers, polyethylene oxide, guar gum, sodium alginate, xanthan gum, agar, and carrageenan. The size solution can be prepared by making an aqueous solution of modified polyvinyl alcohol (A) and then adding starch (B) to it, or by pouring (A) and (B) into water and heating it. Any method can be used, such as a method of dissolving. However, the temperature of the size liquid must be kept lower than the gelatinization initiation temperature of starch (B). The solid content concentration in the size liquid is 3% by weight or more, usually 3% by weight or more.
Set to ~40% by weight. If it is less than 3% by weight, the viscosity will be low and it will be difficult to control the amount of glue, while if it exceeds 40% by weight, it will stick to the surface and reduce the gluing properties. Within the range of 3 to 40% by weight, the features of the present invention are more effectively utilized at higher concentrations such as 13 to 40% by weight. Gluing is carried out using a regular gluing machine such as the one-size sizing method or the warping sizer method. After pasting, it is immediately subjected to a drying process. Drying temperature is 80~
The temperature is preferably 160°C, particularly 100-150°C. The drying method may be either hot air drying or cylinder drying. Both spun yarn and filament yarn are used as target raw yarn. Next, the method of the present invention will be further explained with reference to Examples. The gelatinization start temperature is 10% by weight for unmodified starch using Brabender amylograph.
In the case of modified starch, it refers to the temperature at which the temperature-viscosity curve begins to rise when gelatinization behavior is measured at a solid content concentration of 15% by weight. Example 1 The warp yarns were sized and dried under the following conditions, and further weaving was performed. Glue formulation Modified polyvinyl alcohol with a degree of polymerization of 1700 obtained by saponifying 92 mol% of the vinyl acetate component of a monomethyl maleate-vinyl acetate copolymer with a monomethyl maleate content of 2.0 mol% 5.1% tapioca starch (gelatinization start temperature 67℃) 11.9% Oil agent (Cytecs No. manufactured by Gooh Chemical Industry Co., Ltd.)
315) 1.0% water remaining Mix the above ingredients at 50-60℃. The modified polyvinyl alcohol is dissolved, but the starch is dispersed in a slurry form. Solid content 18.0% Target yarn Polyentel/cotton = 65/35 blended yarn Textile structure = 45 1 S x 45 1 S/110 x 60 x Width 47
11 x 5121 sticks Gluing conditions Gluing temperature 50~55℃ Gluing speed 100 Yd/min Gluing roll squeezing pressure 1.0~1.2 Kg/cm 2 Gluing machine
Sucker 11C (multi-cylinder) type drying temperature Hot air 100℃ Cylinder 120℃ Sizing rate 13.5% Drawing rate 75% Weaving conditions Loom TOYODA automatic loom GL-8 Rotation speed 180rpm Loom room conditions 25-30℃, 70-80% The RH results were favorable, with a sized yarn strength of 295 g, elongation of 8.4%, weaving efficiency of 94%, and wear resistance of class 2 according to 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 recipe Polyvinyl alcohol with a polymerization degree of 1700 and a saponification degree of 87 mol% 4.8% Corn starch (gelatinization start temperature 73°C) 3.7% Oil agent (Solvil, manufactured by Yushiro Chemical Co., Ltd.)
Watkusu SX-135A) 0.5% water remaining Heat mix the above ingredients at 90-95℃ for 2 hours to prepare a uniform paste solution, dilute with hot water to obtain a solid content of 9.0%
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% (Sizing roll squeezing pressure, sizing machine, and drying temperature are the same as Example 1) Conditions) Weaving conditions Same as Example 1 Results: Sized yarn strength 291g, elongation 8.0, weaving efficiency
The wear resistance was 88%, grade 4. Target example 2 Modified polyvinyl alcohol used in glue formulation example 1
4.8% tapioca starch (gelatinization start temperature 67℃)
3.7% Oil (used in Example 1) 0.7% Water Remaining The above ingredients were heated and mixed at 80 to 90°C for 1.5 hours to prepare a uniform paste solution, and diluted with hot water to give a solid content of 9.0.
%. 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 13.4
%, and the aperture ratio was set to 149%. As a result, the strength of the sized yarn was 288 g, the elongation was 8.4%, the weaving efficiency was 90%, and the abrasion resistance was grade 3. Comparing Example 1 and Comparative Examples 1 and 2, apart from the sizing yarn physical properties and weavability, there are differences in the required energy as shown in the following table.

【表】 即ち実施例1は対照例1〜2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。 対照例 3 変性ポリビニールアルコールに代えて重合度
1700、ケン化度87モル%のポリビニルアルコール
を用いたほかは実施例1と同様の糊処方とし、各
成分を50〜60℃で混合してポリビニルアルコール
は溶解しているが、デンプンはスラリー状に分散
している糊液を調製し、以下実施例1と同様にし
て実験を行つた。ただし着糊率は14.4%、絞り率
は80%とした。 結果は糊付糸強度279g、伸度7.9%、製織効率
90%、耐摩性3〜4級であり、実施例1に比し劣
つていた。 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 イタコン酸含量3.2モル%のイタコン酸―酢
酸ビニル共重合体の酢酸ビニル成分の96モル
%をケン化して得られた重合度1400のイタコ
ン酸変性ポリビニルアルコール 7.5% コーンスターチ(糊化開始温度73℃) 10.0% リンゴ酸 0.3% 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 3 実施例1で用いたマレイン酸モノメチル変性
ポリビニルアルコール 5.1% タピオカデンプン(糊化開始温度67℃)
11.0% ヒドロキシエチルエーテル化グアーガム
0.9% 油剤(実施例1で用いたもの) 1.0% 水 残り 実施例 4 アリルスルホン酸ソーダ含量0.8モル%のア
リルスルホン酸ソーダ―酢酸ビニル共重合体
の酢酸ビニル成分の82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 10.0% タピオカデンプン(糊化開始温度67℃)
10.0% 乳酸 02% 油剤(松本油脂製株式会社製サイジング・ワ
ツクスV2) 1.0% 水 残り 実施例 5 マレイン酸モノメチル含量2.5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94モル%をケン化して得られ
た重合度1500のマレイン酸モノメチル変性ポ
リビニルアルコール 6.3% コーンスターチ(糊化開始温度73℃) 11.7% 油剤(実施例2で用いたもの) 0.9% 水 残り 実施例 6 フマール酸含量1.2モル%のフマール酸―酢
酸ビニル共重合体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 3.5% 糊化開始温度67℃の変性デンプン(王子コン
ス株式会社製コーフイルム#50 13.0% ソーダ灰 0.3% 油剤(実施例2で用いたもの) 1.0% 水 残り 実施例 7 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 7.6% 糊化開始温度60℃のエステル化デンプン(日
澱化学株式会社製ペトロサイズA) 11.4% 平滑性油剤(実施例2で用いたもの) 1.0% 水 残り 上記実施例2〜7の条件及び結果を次表に示
す。
[Table] In other words, compared to Control Examples 1 and 2, Example 1 can significantly save energy such as steam during size solution preparation, size solution temperature maintenance, and drying, and can also greatly improve productivity. I understand. Control example 3 Polymerization degree instead of modified polyvinyl alcohol
The glue formulation was the same as in Example 1 except that polyvinyl alcohol 1700 and saponification degree of 87 mol% was used, and each component was mixed at 50 to 60°C so that the polyvinyl alcohol was dissolved, but the starch was in the form of a slurry. A paste solution in which the liquid was dispersed was prepared, and an experiment was conducted in the same manner as in Example 1. However, the adhesive rate was 14.4% and the squeezing rate was 80%. The results were a sized yarn strength of 279g, elongation of 7.9%, and weaving efficiency.
90%, wear resistance was 3rd to 4th grade, which was inferior to Example 1. 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 Itaconic acid-modified polyvinyl alcohol with a degree of polymerization of 1400 obtained by saponifying 96 mol% of the vinyl acetate component of an itaconic acid-vinyl acetate copolymer with an itaconic acid content of 3.2 mol% 7.5% corn starch (gelatinization start temperature 73℃) 10.0% Malic acid 0.3% Oil agent (TY manufactured by Kyoeisha Yushi Kagaku Kogyo Co., Ltd.)
653) 1.0% Water Remaining Example 3 Monomethyl maleate-modified polyvinyl alcohol used in Example 1 5.1% Tapioca starch (gelatinization start temperature 67°C)
11.0% Hydroxyethyl etherified guar gum
0.9% oil agent (used in Example 1) 1.0% water Remaining Example 4 82 mol% of the vinyl acetate component of a sodium allylsulfonate-vinyl acetate copolymer with a sodium allylsulfonate content of 0.8 mol% was saponified. Obtained sodium allylsulfonate modified polyvinyl alcohol with a degree of polymerization of 600 10.0% tapioca starch (gelatinization start temperature 67°C)
10.0% Lactic acid 02% Oil agent (Sizing Wax V 2 manufactured by Matsumoto Yushi Co., Ltd.) 1.0% Water Remaining Example 5 94 mol of vinyl acetate component of monomethyl maleate-vinyl acetate copolymer with monomethyl maleate content of 2.5 mol% % monomethyl maleate-modified polyvinyl alcohol with a degree of polymerization of 1500 obtained by saponifying 6.3% Corn starch (gelatinization start temperature 73°C) 11.7% Oil agent (used in Example 2) 0.9% Water Remaining Example 6 Fumaric acid 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 content of 1.2 mol% 3.5% Modified starch with a gelatinization initiation temperature of 67°C (Oji) Cofilm #50 manufactured by Cons Co., Ltd. 13.0% Soda ash 0.3% Oil agent (used in Example 2) 1.0% Water Remaining Example 7 Vinyl acetate component of acrylic acid-vinyl acetate copolymer with acrylic acid content of 1.5 mol% Acrylic acid-modified polyvinyl alcohol with a degree of polymerization of 1100 obtained by saponifying 95 mol% of (used in Example 2) 1.0% water remainder The conditions and results of Examples 2 to 7 above are shown in the table below.

【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 実施例4で用いた変性ポリビニルアルコール
2.5% 糊化開始温度53℃の酸処理デンプン(日澱化学
株式会社製N―100) 4.5% 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 110Yd/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 4.1% 絞り率 56% 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411g、伸度14.9%で抱合性
も良好であり、93%の製織効率が得られた。
[Table] Example 8 The warp threads were pasted and weaved under the following conditions. Modified polyvinyl alcohol used in glue formulation Example 4
2.5% Acid-treated starch with a gelatinization start temperature of 53°C (N-100 manufactured by Nippon Star Chemical Co., Ltd.) 4.5% 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 is made using this glue.
Glued, dried, and weaved 120d dobby cloth (3540 pieces). Gluing conditions Gluing temperature 45℃ Gluing speed 110 Yd/min Gluing roll squeezing pressure 2.0 Kg/cm 2 Gluing machine KSJ-H type manufactured by Tsudakoma Kogyo Co., Ltd. Drying temperature Hot air 110℃ Cylinder 100℃ Sizing rate 4.1% Squeezing rate 56% Weaving conditions Loom TOYODA automatic loom GFD 3 (dobby type) Rotation speed 160rpm Loom room conditions 25~30℃, 65~75%RH The results showed that the sized yarn strength was 411g, the elongation was 14.9%, and the conjugation was good. A weaving efficiency of 93% was obtained.

Claims (1)

【特許請求の範囲】 1 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0.02〜15モル%共重合変性した変性ポ
リビニルアルコール(A)の水溶液中にデンプン(B)が
分散している状態にありかつ(A)対(B)の使用比が重
量で10:90〜70:30の範囲内にある固形分濃度3
〜40重量%の糊液を用いて経糸の糊付を行い、糊
付後直ちに乾燥工程に供することを特徴とする経
糸の糊付方法。 2 糊液の固形分濃度が13〜40重量%である特許
請求の範囲第1項記載の方法。 3 (A)のケン化度が85モル%以上である特許請求
の範囲第1項記載の方法。 4 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0.02〜15モル%共重合変性した変性ポ
リビニルアルコール(A)の水溶液中にデンプン(B)が
分散し、しかも該デンプン粒子の膨潤剤が存在し
ている状態にありかつ(A)対(B)の使用比が重量で
10:90〜70:30の範囲内にある固形分濃度3〜40
重量%の糊液を用いて経糸の糊付を行い、糊付後
直ちに乾燥工程に供することを特徴とする経糸の
糊付方法。
[Scope of Claims] 1 Starch (B) is dispersed in an aqueous solution of modified polyvinyl alcohol (A) copolymerized with 0.02 to 15 mol% of a comonomer having a carboxyl group or a sulfonic acid group, and ( Solid content concentration 3 where the usage ratio of A) to (B) is within the range of 10:90 to 70:30 by weight
A method for sizing warp yarns, which comprises sizing the warp yarns using a sizing solution of up to 40% by weight, and immediately subjecting the warp yarns to a drying process after sizing. 2. The method according to claim 1, wherein the solid content concentration of the size liquid is 13 to 40% by weight. 3. The method according to claim 1, wherein the degree of saponification of (A) is 85 mol% or more. 4. Starch (B) is dispersed in an aqueous solution of modified polyvinyl alcohol (A) copolymerized with 0.02 to 15 mol% of a comonomer having a carboxyl group or sulfonic acid group, and a swelling agent for the starch particles is present. condition and the usage ratio of (A) to (B) is by weight.
Solid content concentration 3-40 within the range of 10:90-70:30
A method for sizing warp yarns, characterized in that the warp yarns are sized using a sizing solution of % by weight, and immediately subjected to a drying process after sizing.
JP5187680A 1980-04-18 1980-04-18 Warp yarn sizing method Granted JPS56148971A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5187680A JPS56148971A (en) 1980-04-18 1980-04-18 Warp yarn sizing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5187680A JPS56148971A (en) 1980-04-18 1980-04-18 Warp yarn sizing method

Publications (2)

Publication Number Publication Date
JPS56148971A JPS56148971A (en) 1981-11-18
JPS6261705B2 true JPS6261705B2 (en) 1987-12-23

Family

ID=12899076

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5187680A Granted JPS56148971A (en) 1980-04-18 1980-04-18 Warp yarn sizing method

Country Status (1)

Country Link
JP (1) JPS56148971A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6091639A (en) 1993-08-27 2000-07-18 Kabushiki Kaisha Toshiba Non-volatile semiconductor memory device and data programming method

Also Published As

Publication number Publication date
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