JPS6114194B2 - - Google Patents

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Publication number
JPS6114194B2
JPS6114194B2 JP58227584A JP22758483A JPS6114194B2 JP S6114194 B2 JPS6114194 B2 JP S6114194B2 JP 58227584 A JP58227584 A JP 58227584A JP 22758483 A JP22758483 A JP 22758483A JP S6114194 B2 JPS6114194 B2 JP S6114194B2
Authority
JP
Japan
Prior art keywords
ethylenically unsaturated
neutralizing agent
acid
item
agent according
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
JP58227584A
Other languages
Japanese (ja)
Other versions
JPS60120773A (en
Inventor
Hironobu Sakaguchi
Koichi Ito
Shigeyuki Sadanari
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.)
Matsumoto Yushi Seiyaku Co Ltd
Original Assignee
Matsumoto Yushi Seiyaku 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 Matsumoto Yushi Seiyaku Co Ltd filed Critical Matsumoto Yushi Seiyaku Co Ltd
Priority to JP22758483A priority Critical patent/JPS60120773A/en
Publication of JPS60120773A publication Critical patent/JPS60120773A/en
Publication of JPS6114194B2 publication Critical patent/JPS6114194B2/ja
Granted legal-status Critical Current

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  • Paints Or Removers (AREA)

Description

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

本発明は、アルカリ糊化澱粉糊の中和剤に関す
る。 製織の準備工程として行なう経糸糊化け、特に
紡績糸においては毛羽伏せ効果と製織時に受ける
張力と、衝撃、摩擦の繰返しに耐える繊維強伸度
を保持するために、一般にコーンスターチ、小麦
澱粉などの天然糊料が使用される。 しかしながら、このような澱粉糊は一般に、低
温において粘度が高く扱いにくので、特公昭57−
57081号公報に記載されているごとく、水酸化ア
ルカリで糊化し、次いで酸で中和して得られる糊
化澱粉糊が使用されている。 このようにして得られた糊化澱粉糊は、乾燥皮
膜の引張強度や屈曲性等が不足することから、十
分に満足できる耐摩耗強度が得られず、実際には
得られた糊液に各種の添加剤が配合されているの
が実状である。さらに、この糊は低温(室温)で
も糊付け出来る利点があるものの保存安定性が十
分でない。 本発明者らは、アルカリ糊化した澱粉を中和す
るに際し、従来のごとき無機酸や低級カルボン酸
に代えて、エチレン系不飽和カルボン酸の単重合
体、もしくは共重合体で中和したところ、上記欠
点を解消し得ることを見出し、さらに糊剤そのも
のの性質も向上することを見出し、本発明を成す
に到つた。 即ち本発明は、エチレン系不飽和モノカルボン
酸の単重合体もしくは共重合体の未中和物または
それらの熱揮散性有機塩基との塩を含有する経糊
付用アルカリ糊化澱粉糊の中和剤に関する。 本発明に用いるエチレン系不飽和モノカルボン
酸の例としては、例えばアクリル酸、メタクリル
酸、クロトン酸、イタコン酸、スチレンカルボン
酸等が挙げられる。好ましくは、アクリル酸、メ
タクリル酸、等である。 上記エチレン系不飽和モノカルボン酸の重合体
は、一般的な重合方法で製造される。例えば、ア
クリル酸を水溶液中で過硫酸アンモニウム等の開
始剤により重合すればよい。 本発明の中和剤には、上記のエチレン系不飽和
モノカルボン酸と他のモノマーとの共重合体を用
いてもよい。上記酸に共重合し得るモノマーの例
としては、エチレン系不飽和エステル類、例えば
メチルメタクリレート、エチルメタクリレート、
メチルアクリレート、エチルアクリレート;重合
性アルケンモノマー類、例えばエチレン、プロピ
レン、ブチレン、ペンテン、ヘキセン、ヘプテ
ン、スチレンおよびそのアルキル置換スチレン;
アクリロニトリル等のエチレン系不飽和ニトリ
ル;アクリルアミド、メタクリルアミド等のエチ
レン系不飽和アミド;β−ヒドロキシアルキルメ
タクリレート等;不飽和カルボン酸、例えばマレ
イン酸、メチルマレイン酸、フマール酸等;酢酸
ビニル等が例示される。 上記エチレン系不飽和モノカルボン酸に共重合
し得るモノマーのカルボキシル基以外の部分のア
ルキルの炭素数は3〜20、好ましくは3〜10であ
る。炭素数20を越えると糊液の特性の改質効果は
殆んど認められなくなる。 上記共重合体は常套の方法で製造する。例え
ば、乳化剤と上記モノマーを混合した後、適当な
重合開始剤により重合させてもよい。 上記共重合体中のエチレン系不飽和モノカルボ
ン酸モノマーの量は、モノマー全量の5重量%以
上、好ましくは50重量%以上である。5重量%以
下では、製織後、糊抜きが困難である。また酸含
有量が少ないほど中和剤としての効果も薄れるの
で多量の添加が非要となり、経済性を欠く。さら
にゲル化防止作用や糊液特性の改質作用も小さく
なる。 上記重合体は熱揮散性の有機塩、例えばアンモ
ニウム塩、アミン塩であつてもよい。 上記揮散性の塩は糊付け・乾燥工程で揮散し、
未中和のカルボキシル基含有ポリマーと同様に作
用する。 本発明のアルカリ糊化澱粉糊の中和剤は、澱粉
を糊化する時に用いた水酸化アルカリに対して中
和当量添加するのが好ましい。もちろん、従来使
用していた中和剤(例えば、硫酸等)と併用して
もよい。 本発明に用いる澱粉糊の例としては、一般にコ
ーンスターチ、小麦澱粉等の天然糊料が用いられ
る。 これらの澱粉を水に添加した後、水酸化アルカ
リ等のアルカリによりアルカリ糊化させる。アル
カリ糊化の温度は通常、室温〜40℃の低温で行な
われる。本発明の中和剤は上記アルカリ糊化され
た澱粉糊を中和するのに用いられる。中和された
澱粉糊は希釈の後、糊剤として用いる。得られた
糊剤は常套の方法によりサイジングが行なわれ
る。 本発明の中和剤を添加して得た糊液に通常の他
の改者剤、例えば、ポリビニルアルコール、カル
ボキシメチルセルロース、アクリル系糊剤、併用
油剤等を添加してサイジング用の糊剤として用い
てもよい。 本発明による中和剤を用いて中和したアルカリ
糊化澱粉糊は、従来の無機、有機酸等で中和した
ものに比較して、糊付け糸の伸度、耐摩耗強度が
増加し製織性が向上する。また、従来用いている
酸等の中和剤により生ずる塩類が、糊の物性に悪
影響を与えるが、本発明による中和剤ではそのよ
うな物性に対する悪影響はほとんどない。さらに
本発明の中和剤を用いると、糊液粘度の安定化作
用が大幅に向上する。例えば、従来の中和方式に
よれば、生成した糊はチクソトロピツク性を有し
ているので、自然放置するとゲル状になるが、本
発明による中和剤を添加するとチクソトロピツク
な性質が殆んどなくなり、自然放置しても流動性
の液状を維持させることができる。従つて、生成
した糊をたえず撹拌下で保存しないとパイプ輸送
できない従来のものに比べて、静置して保存でき
るところから、工程の合理化、簡素化をなし得
る。さらに従来の中和剤による澱粉糊は糊化時の
水酸化アルカリ添加量が少ない場合、高い温度、
例えば、60℃以上の温度での粘度変化が著しく、
糊付着量管理が困難であつたが、本発明の中和剤
によれば、60℃以上の温度での粘度の変化が極め
て小さく、温度管理が容易である特徴を有する。 本発明を実施例によりさらに詳細に説明する。
実施例中%は特に指示しない限り重量に基づく。実施例1および2、比較例1 中和剤Aの調製: 還流冷却器、滴下ロート、温度計、撹拌器を取
付けた4つ口丸底フラスコに、軟水250gを仕込
み、窒素ガスを通じて酸素を除きながら、撹拌下
で80℃まで加熱昇温した。アクリル酸150gを軟
水340gに希釈し、滴下ロートに仕込んだ。過硫
酸アンモニウム0.3gをフラスコに添加し、ただ
ちに滴下重合を開始した。重合温度を80℃に維持
し、1時間で滴下を終了した。滴下終了後、過硫
酸アンモニウム0.05gを軟水2gに希釈してフラ
スコ中に添加し、80℃で1時間重合の後、さらに
過硫酸アンモニウム0.05gを軟水2gに希釈して
添加した。添加後、85℃に昇温し、1時間重合し
てポリアクリル酸を得た(これを中和剤A)とす
る。 中和剤Bの調製: 実施例と同様の装置を用い、フラスコに軟水
200g、滴下ロートにアクリル酸126g、メタクリ
ル酸84g、メタクリル酸メチル30g、アクリル酸
エチル20g、酢酸ビニル30g、アクリル酸−2−
エチルヘキシル6g、アクリロニトリル4gの単
量体に、ラウリルサルフエートNa2.0gと過硫酸
カリウム1.5g、ラウリルメルカプタン0.6g、さ
らに軟水200gを仕込み撹拌混合した。滴下終了
までモノマーが乳化分散状態を保つように撹拌を
持続した。フラスコ内で撹拌加熱された軟水が85
℃に達したとき、滴下ロートから50gのモノマー
乳化液を瞬時に添加し、5分間予備重合を行なつ
た後、85℃に温度をコントロールしながら、残量
のモノマー乳化液を1時間かけて滴下重合した。
滴下終了後、過硫酸カリウム0.05gを軟水2gに
溶解して添加し、85℃で1.5時間重合した。その
後、40℃まで冷却して、25%アンモニア水37gを
滴下して中和した(このものを中和剤Bとす
る)。 コーンスターチのアルカリ糊化糊の調製: 水400g、コーンスターチ100gを捏和槽に入
れ、撹拌混合して分散液とした。次いで、水酸化
ナトリウム7.2gを水50gに溶解してから、上記
分散液に加えた。混練10分後、水50gを加えた。
その後、40分間混練撹拌してアルカリ糊化を行な
う。その後、特公昭57−57081号公報に記載の酸
(硫酸)または前記中和剤A、中和剤Bを中和剤
としてPH8.0〜8.5に調整した。 糊液の調整: 表−1に示すように糊液を調整した。得られた
糊液の純分比率(%)と糊液濃度(%)を表−1
に記載する。
The present invention relates to a neutralizing agent for alkaline gelatinized starch paste. In warp gelatinization, which is carried out as a preparation process for weaving, and especially for spun yarns, natural materials such as cornstarch and wheat starch are generally used to maintain the fluffing effect and to maintain fiber strength and elongation that can withstand repeated impacts and friction, as well as tension during weaving. A glue is used. However, such starch glue is generally difficult to handle due to its high viscosity at low temperatures, so it was
As described in Japanese Patent No. 57081, a gelatinized starch paste is used which is obtained by gelatinizing with an alkali hydroxide and then neutralizing with an acid. The gelatinized starch paste obtained in this way does not have sufficient abrasion resistance due to the lack of tensile strength and flexibility of the dried film, and in reality, the gelatinized starch paste obtained cannot be used in various ways. The reality is that these additives are included. Further, although this glue has the advantage of being able to be glued even at low temperatures (room temperature), it does not have sufficient storage stability. When neutralizing alkali-gelatinized starch, the present inventors used an ethylenically unsaturated carboxylic acid monopolymer or copolymer instead of the conventional inorganic acid or lower carboxylic acid. It was discovered that the above-mentioned drawbacks could be overcome, and that the properties of the adhesive itself were also improved, leading to the completion of the present invention. That is, the present invention provides an alkaline gelatinized starch paste for warp-sizing containing an unneutralized monopolymer or copolymer of an ethylenically unsaturated monocarboxylic acid or a salt thereof with a heat-volatile organic base. Regarding Japanese preparations. Examples of ethylenically unsaturated monocarboxylic acids used in the present invention include acrylic acid, methacrylic acid, crotonic acid, itaconic acid, and styrene carboxylic acid. Preferred are acrylic acid, methacrylic acid, and the like. The above-mentioned polymer of ethylenically unsaturated monocarboxylic acid is produced by a general polymerization method. For example, acrylic acid may be polymerized in an aqueous solution using an initiator such as ammonium persulfate. A copolymer of the above ethylenically unsaturated monocarboxylic acid and another monomer may be used as the neutralizing agent of the present invention. Examples of monomers copolymerizable with the above acids include ethylenically unsaturated esters, such as methyl methacrylate, ethyl methacrylate,
Methyl acrylate, ethyl acrylate; polymerizable alkene monomers such as ethylene, propylene, butylene, pentene, hexene, heptene, styrene and its alkyl-substituted styrenes;
Ethylenically unsaturated nitriles such as acrylonitrile; ethylenically unsaturated amides such as acrylamide and methacrylamide; β-hydroxyalkyl methacrylate, etc.; unsaturated carboxylic acids such as maleic acid, methylmaleic acid, fumaric acid, etc.; vinyl acetate, etc. be done. The alkyl portion other than the carboxyl group of the monomer copolymerizable with the ethylenically unsaturated monocarboxylic acid has 3 to 20 carbon atoms, preferably 3 to 10 carbon atoms. When the number of carbon atoms exceeds 20, the effect of modifying the properties of the size liquid is hardly recognized. The above copolymers are produced by conventional methods. For example, the emulsifier and the monomer may be mixed and then polymerized using a suitable polymerization initiator. The amount of ethylenically unsaturated monocarboxylic acid monomer in the above copolymer is 5% by weight or more, preferably 50% by weight or more of the total amount of monomers. If it is less than 5% by weight, it will be difficult to remove the size after weaving. Furthermore, the lower the acid content, the less effective it is as a neutralizing agent, so it is not necessary to add a large amount, which makes it uneconomical. Furthermore, the gelling prevention effect and the modifying effect on size liquid properties are also reduced. The polymer may be a heat-volatile organic salt, such as an ammonium salt or an amine salt. The volatile salt mentioned above is volatilized during the gluing and drying process,
Acts similarly to unneutralized carboxyl group-containing polymers. The neutralizing agent for the alkali gelatinized starch paste of the present invention is preferably added in an amount equivalent to neutralizing the alkali hydroxide used when gelatinizing the starch. Of course, it may be used in combination with a conventionally used neutralizing agent (for example, sulfuric acid, etc.). As examples of the starch paste used in the present invention, natural pastes such as corn starch and wheat starch are generally used. After adding these starches to water, they are gelatinized with an alkali such as an alkali hydroxide. Alkaline gelatinization is usually carried out at a low temperature of room temperature to 40°C. The neutralizing agent of the present invention is used to neutralize the alkali-gelatinized starch paste. The neutralized starch paste is used as a sizing agent after dilution. The resulting sizing agent is sized by conventional methods. Other usual modifying agents such as polyvinyl alcohol, carboxymethyl cellulose, acrylic thickening agent, combined oil agent, etc. are added to the sizing liquid obtained by adding the neutralizing agent of the present invention, and it is used as a sizing agent. It's okay. The alkaline gelatinized starch paste neutralized using the neutralizing agent of the present invention has increased elongation and abrasion resistance strength of the sizing yarn, and has improved weaving properties, compared to those neutralized with conventional inorganic or organic acids. will improve. Furthermore, salts produced by conventionally used neutralizing agents such as acids have an adverse effect on the physical properties of the glue, but the neutralizing agent according to the present invention has almost no such adverse effect on the physical properties. Furthermore, when the neutralizing agent of the present invention is used, the stabilizing effect on the viscosity of the paste liquid is greatly improved. For example, according to the conventional neutralization method, the produced glue has thixotropic properties and becomes gel-like when left alone, but when the neutralizing agent of the present invention is added, the thixotropic properties are almost eliminated. , it is possible to maintain a fluid liquid state even if left to stand naturally. Therefore, compared to the conventional method in which the produced glue cannot be transported through a pipe unless it is constantly stirred, the process can be streamlined and simplified because it can be stored stationary. Furthermore, starch paste made with conventional neutralizing agents requires high temperatures,
For example, the viscosity changes significantly at temperatures above 60℃,
Although it has been difficult to control the amount of glue deposited, the neutralizing agent of the present invention has the characteristic that the change in viscosity at temperatures of 60° C. or higher is extremely small and temperature control is easy. The present invention will be explained in more detail with reference to Examples.
Percentages in the examples are by weight unless otherwise indicated. Examples 1 and 2, Comparative Example 1 Preparation of Neutralizing Agent A: 250 g of soft water was charged into a four-necked round-bottomed flask equipped with a reflux condenser, dropping funnel, thermometer, and stirrer, and oxygen was removed by passing nitrogen gas. While stirring, the temperature was raised to 80°C. 150 g of acrylic acid was diluted with 340 g of soft water and charged into a dropping funnel. 0.3 g of ammonium persulfate was added to the flask and dropwise polymerization was immediately initiated. The polymerization temperature was maintained at 80°C, and the dropwise addition was completed in 1 hour. After completion of the dropwise addition, 0.05 g of ammonium persulfate was diluted with 2 g of soft water and added into the flask, and after polymerization at 80° C. for 1 hour, 0.05 g of ammonium persulfate was further diluted with 2 g of soft water and added. After the addition, the temperature was raised to 85° C. and polymerized for 1 hour to obtain polyacrylic acid (this is referred to as neutralizing agent A). Preparation of neutralizing agent B: Using the same equipment as in the example, add soft water to a flask.
200g, acrylic acid 126g, methacrylic acid 84g, methyl methacrylate 30g, ethyl acrylate 20g, vinyl acetate 30g, acrylic acid-2-
To 6 g of ethylhexyl and 4 g of acrylonitrile monomers, 2.0 g of sodium lauryl sulfate, 1.5 g of potassium persulfate, 0.6 g of lauryl mercaptan, and 200 g of soft water were added and mixed with stirring. Stirring was continued to maintain the monomer in an emulsified and dispersed state until the dropwise addition was completed. Soft water stirred and heated in a flask is 85
When the temperature reached ℃, 50g of the monomer emulsion was instantly added from the dropping funnel, prepolymerized for 5 minutes, and then the remaining amount of the monomer emulsion was added over 1 hour while controlling the temperature at 85℃. Polymerization was carried out by dropping.
After the dropwise addition was completed, 0.05 g of potassium persulfate dissolved in 2 g of soft water was added and polymerized at 85° C. for 1.5 hours. Thereafter, it was cooled to 40°C, and 37 g of 25% aqueous ammonia was added dropwise to neutralize it (this was referred to as neutralizing agent B). Preparation of cornstarch alkaline gelatinization paste: 400g of water and 100g of cornstarch were placed in a kneading tank and mixed with stirring to form a dispersion. Next, 7.2 g of sodium hydroxide was dissolved in 50 g of water and then added to the above dispersion. After 10 minutes of kneading, 50 g of water was added.
Thereafter, the mixture is kneaded and stirred for 40 minutes to perform alkaline gelatinization. Thereafter, the pH was adjusted to 8.0 to 8.5 using the acid (sulfuric acid) described in Japanese Patent Publication No. 57-57081 or the neutralizing agents A and B as neutralizing agents. Adjustment of size liquid: The size liquid was adjusted as shown in Table-1. Table 1 shows the pure content ratio (%) and size concentration (%) of the obtained size liquid.
Describe it in

【表】試験例 1 上記糊剤を用いて、ホツトエアシリンダー併用
式サイジングマシンを用いて、糊付け温度50℃、
速度70m/minおよび巻取方式(PIV方式)で
綿、先染40番単糸4320本に糊付けした。アフター
ワキシングは、パラフインワツクス主体のものを
用い、着油量0.2%に機械設定して付着させた。
織物規格は、経糸40番単糸、緯糸16番単糸で、密
度は、経96本/インチ、緯50本/インチであつ
た。シヤトル織機(165rpm)を用いて布地を得
た。 上記糊付け糸の物性および製織効率の結果を表
−2に示す。
[Table] Test example 1 Using the above adhesive, using a sizing machine combined with a hot air cylinder, the gluing temperature was 50℃,
Glue was applied to 4,320 yarn-dyed cotton yarns, number 40, using a winding method (PIV method) at a speed of 70 m/min. After-waxing was mainly made of paraffin wax, and the machine set the amount of oil deposited to 0.2%.
The fabric specifications were a number 40 single yarn in the warp and a single yarn number 16 in the weft, and the density was 96 yarns/inch for the warp and 50 yarns/inch for the weft. The fabric was obtained using a shuttle loom (165 rpm). Table 2 shows the results of the physical properties and weaving efficiency of the sized yarn.

【表】実施例 3 本実施例は、本発明により得られた糊剤と従来
の糊剤との温度変化による粘度の変化を測定し
た。測定は、ブラベンダーアミログラフにより、
10%濃度の糊液の粘度変化を追跡したものであ
る。糊化時に添加する水酸化ナトリウムの量は両
者とも同一である。結果を第1図に示す。 硫酸中和による糊液1を加温すると、60℃を越
えた時点から粘度が高くなる。それに比べて、本
発明の中和剤を用いた糊液2は粘度変化が少な
く、粘度そのものもより低い値を示す。また、糊
液1を室温で自然放置cするとゲル状になるが、
糊液2は24時間後も流動性を維持した。
[Table] Example 3 In this example, changes in viscosity due to temperature changes were measured between the sizing agent obtained according to the present invention and a conventional sizing agent. Measurements are made using a Brabender amylograph.
This shows the changes in viscosity of a glue solution with a concentration of 10%. The amount of sodium hydroxide added during gelatinization is the same in both cases. The results are shown in Figure 1. When the size liquid 1 obtained by neutralization with sulfuric acid is heated, the viscosity increases from the point at which the temperature exceeds 60°C. In comparison, the size liquid 2 using the neutralizing agent of the present invention shows less change in viscosity, and the viscosity itself shows a lower value. In addition, if the glue solution 1 is allowed to stand at room temperature, it becomes gel-like, but
Size liquid 2 maintained its fluidity even after 24 hours.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明中和剤により中和した糊剤1と
従来の中和剤(硫酸)により中和した糊剤2との
温度による粘度変化を表わすアミログラフであ
る。
FIG. 1 is an amylograph showing changes in viscosity depending on temperature of a sizing agent 1 neutralized with the neutralizing agent of the present invention and a sizing agent 2 neutralized with a conventional neutralizing agent (sulfuric acid).

Claims (1)

【特許請求の範囲】 1 エチレン系不飽和モノカルボン酸の単重合体
もしくは共重合体の共中和物またはそれらの熱揮
散性有機塩基との塩を含有する経糸糊付用アルカ
リ糊化澱粉糊の中和剤。 2 エチレン系不飽和モノカルボン酸がアクリル
酸またはメタクリル酸である第1項記載の中和
剤。 3 エチレン系不飽和カルボン酸に共重合し得る
モノマーが、エチレン系不飽和エステル、エチレ
ン系不飽和アミド、エチレン系不飽和ニトリル、
重合性アルケンモノマー、不飽和ポリカルボン酸
または酢酸ビニルである第1項記載の中和剤。 4 共重合体がエチレン系不飽和モノカルボン酸
を5重量%以上有する第1項記載の中和剤。 5 共重合体がエチレン系不飽和モノカルボン酸
を50重量%以上有する第1項記載の中和剤。 6 有機塩基がアミンまたはアンモニアである第
1項記載の中和剤。
[Scope of Claims] 1. Alkaline gelatinized starch glue for warp sizing containing a co-neutralized product of a homopolymer or copolymer of ethylenically unsaturated monocarboxylic acid or a salt thereof with a heat-volatile organic base neutralizing agent. 2. The neutralizing agent according to item 1, wherein the ethylenically unsaturated monocarboxylic acid is acrylic acid or methacrylic acid. 3. The monomer copolymerizable with ethylenically unsaturated carboxylic acid is an ethylenically unsaturated ester, an ethylenically unsaturated amide, an ethylenically unsaturated nitrile,
2. The neutralizing agent according to item 1, which is a polymerizable alkene monomer, an unsaturated polycarboxylic acid, or vinyl acetate. 4. The neutralizing agent according to item 1, wherein the copolymer contains 5% by weight or more of ethylenically unsaturated monocarboxylic acid. 5. The neutralizing agent according to item 1, wherein the copolymer contains 50% by weight or more of ethylenically unsaturated monocarboxylic acid. 6. The neutralizing agent according to item 1, wherein the organic base is an amine or ammonia.
JP22758483A 1983-12-01 1983-12-01 Neutralizing agent for alkali-gelatinized starch paste Granted JPS60120773A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22758483A JPS60120773A (en) 1983-12-01 1983-12-01 Neutralizing agent for alkali-gelatinized starch paste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22758483A JPS60120773A (en) 1983-12-01 1983-12-01 Neutralizing agent for alkali-gelatinized starch paste

Publications (2)

Publication Number Publication Date
JPS60120773A JPS60120773A (en) 1985-06-28
JPS6114194B2 true JPS6114194B2 (en) 1986-04-17

Family

ID=16863202

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22758483A Granted JPS60120773A (en) 1983-12-01 1983-12-01 Neutralizing agent for alkali-gelatinized starch paste

Country Status (1)

Country Link
JP (1) JPS60120773A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3519477A (en) * 1966-02-01 1970-07-07 Basf Ag Sizing cellulosic and acrylic staple fiber yarns with acrylonitrile/acrylic acid copolymer

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3519477A (en) * 1966-02-01 1970-07-07 Basf Ag Sizing cellulosic and acrylic staple fiber yarns with acrylonitrile/acrylic acid copolymer

Also Published As

Publication number Publication date
JPS60120773A (en) 1985-06-28

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