Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0555639B2 - - Google Patents
[go: Go Back, main page]

JPH0555639B2 - - Google Patents

Info

Publication number
JPH0555639B2
JPH0555639B2 JP22965984A JP22965984A JPH0555639B2 JP H0555639 B2 JPH0555639 B2 JP H0555639B2 JP 22965984 A JP22965984 A JP 22965984A JP 22965984 A JP22965984 A JP 22965984A JP H0555639 B2 JPH0555639 B2 JP H0555639B2
Authority
JP
Japan
Prior art keywords
latex
weight
paper
fibers
monomer
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 - Fee Related
Application number
JP22965984A
Other languages
Japanese (ja)
Other versions
JPS61108798A (en
Inventor
Katsuo Hagiwara
Jun Hasegawa
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.)
Zeon Corp
Original Assignee
Nippon Zeon 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 Zeon Co Ltd filed Critical Nippon Zeon Co Ltd
Priority to JP22965984A priority Critical patent/JPS61108798A/en
Publication of JPS61108798A publication Critical patent/JPS61108798A/en
Publication of JPH0555639B2 publication Critical patent/JPH0555639B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Paper (AREA)
  • Sealing Material Composition (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

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

(産業上の利用分野) 本発明は、耐水性のすぐれた各種繊維内添用ラ
テツクスに関し、さらに詳しくは、耐水性のすぐ
れた看取繊維内添用のエポキシ基を含む不飽和化
合物を共重合した共役ジエン系ラテツクスに関す
るものである。 (従来の技術) 従来、主としてガスケツト類等に、各種繊維を
抄造したシートが用いられているが、繊維のみで
抄造しても、繊維が物理的にからみ合うのみで、
繊維同士の科学的結合力が極めて弱い為、満足す
べき強度を、有するガスケツト等は得られない。 従つて繊維同士の結合力を増大する為、一般
に、天然、或いは合成の高分子物質のラテツクス
をバインダーとして用いた内添法により製造され
ている。 (発明が解決しようとする問題点) 抄造紙の強度向上、耐油性の付与等の目的のた
めに、従来からバインダーとしてアクリロニトリ
ル−ブタジエン共重合体のラテツクスが使用され
ている。 しかしながら、このラテツクスには重合時に使
用した海面活性剤、各種無機塩類等の重合薬剤が
含まれており、これらが抄造紙中に存在するため
に充分な耐水性が得られず、改善が望まれてい
る。 (問題点を解決するための手段) 本発明者らは、前記欠点を解決すべく鋭意研究
の結果、エボキシ基を含む不飽和化合物を、乳化
重合により共役ジエン系単量体及びエチレン系ニ
トリル単量体と共重合させたラテツクスを用いて
内添すれば、従来のアクリロニトリル−ブタジエ
ン共重合体ラテツクスにより内添したものに比べ
抄造紙の耐水性が改良されることを見い出し、こ
の知見に基づいて本発明を完成するに到つた。 即ち本発明は、エポキシ基含有単量体、共役ジ
エン系単量体、及びエチレン系ニトリル単量体を
乳化共重合して成る抄造紙内添用ラテツクスの提
供にある。 本発明に用いられるエポキシ基を含む単量体
は、抄造紙の耐水性を向上させるのに必須の単量
体である。エポキシ基を含む単量体は、本発明の
共重合体を構成する他の単量体とラジカル共重合
性のあるものであれば良く、例えば、ビニルグリ
シジルエーテル、アリルグルシジルエーテル、メ
タリルグリシジルエーテル、グリシジルアクリレ
ート、グリシジルメタクリレート等の一種類、ま
たは、二種類以上が使用される。使用量は、単量
体混合物中(以下も同様)少なくとも0.1重量%
であり、0.1重量%未満では、抄造紙の耐水性は
改善されない。10重量%を越えると、耐水性は飽
和してしまうので、これ以上の使用は必要でな
い。好ましくは1〜5重量%である。 本発明に用いられる共役ジエン系単量体とは、
例えば、イソプレン、1,3−ブタジエン、2−
メチル−1,3−ブタジエン、2−クロロ−1,
3−ブタジエン、1,3−ペンタジエン等であり
これらの一種以上が使用される。使用量は通常35
〜98.9重量%の範囲である。35重量%未満では抄
造紙の可撓性が劣り、又、重合反応速度が低下す
る98.9重量%を越えると、抄造紙の強度が低下す
る。好ましくは50〜84重量%である。 エチレン系ニトリル単量体としては、アクリロ
ニトリル、メタクリロニトリル、α−クロロ−ア
クリロニトリル等の一種地上が使用される。使用
量は通常1〜55重量%であり、1重量%未満では
抄造紙の強度、耐油性が不充分となり、55重量%
を越えると抄造紙の可撓性が低下し、又、重合反
応速度が低下するので好ましくない。好ましくは
15〜50重量%である。 また必要に応じて全単量体混合物中20重量%以
下の範囲で、アクリル酸、メタクリル酸等の不飽
和カルボン酸単量体、または、そのアルキルエス
テルをも含むことができる。ラテツクスの安定性
を高めるうえで、不飽和カルボン酸単量体の使用
は特に望ましい。 本発明のラテツクスは、上記の各単量体を、通
常の乳化重合により共重合させることによつて得
られるが、製造法は通常実施されている回分式、
連続式等のいずれでもよく、特に限定されない。
また、使用される乳化剤、重合開始剤、分子量調
整剤、その他の重合用薬剤も通常の乳化重合で使
用されるもので良く、特に限定されない。 抄造紙を製造する為に使用される繊維として
は、石綿、セルロース繊維、芳香族ポリアミド繊
維、炭素繊維、フエノール繊維、セラミツクス繊
維、石綿以外の無機繊維等を挙げることができ、
場合により緻密なシートを作る為に、上記繊維に
無機物を加えることもできる。無機物としては、
クレータルク、珪酸、珪酸アルミニウム、炭酸カ
ルシウム等を挙げることができる。 本発明のラテツクスを用い抄造紙を製造するに
当つては本発明のラテツクスをバインダーとして
固形分で繊維に対し通常、0.5〜100重量%、好ま
しくは1〜30重量%の範囲で用い、ビーター或い
はボーチヤー等の工程で繊維を加え充分撹拌した
後、必要に応じ、無機塩類好ましくは硫酸バン
土、あるいは高分子凝集剤を0.5〜10重量%加え
て、繊維へのバインダー定着を完了させた後、抄
造機で紙状物とされる。 かくして、本発明によれば、従来のエポキシ基
を含まむアクリロニトリル−ブタジエン共重合体
のラテツクスをバインダーとして用いた抄造紙と
比較して、強度特性、対油性は同等であるが耐水
性に優れた抄造紙を得ることができる。 本発明のラテツクスを用いた抄造紙は主として
耐油性を必要とするガスケツト類に有用である。 以下に実施例を挙げて本発明を更に具体的に説
明する。 実施例 1 撹拌機付きオートクレーブに表1の重合処方に
従がい、水、ブタジエン、アクリロニトリル、グ
リシジルメタクリレート、ラウリル硫酸ソーダ、
t−ドデシルメルカプタンを仕込んだ後、35℃に
加温し、過硫酸アンモニウウを添加し反応を開始
させた。重合転化率98%以上(重量法に測定)に
て、室温までオートクレーブを冷却して反応を停
止させた。反応中は、オートクレーブを35℃に保
つた。得られた共重合体ラテツクスをラテツクス
Aとする。同様にしてグリシジルメタクリレート
のかわりにアリルグリシジルエーテルを用いた共
重合体ラテツクス(ラテツクスB)ならびにエポ
キシ機を含まないラテツクス(ラテツクスC)を
得た。
(Industrial Application Field) The present invention relates to latexes for use as internal additives in various types of fibers that have excellent water resistance, and more particularly, to latexes that have excellent water resistance and are used as internal additives in fibers. This invention relates to conjugated diene latexes. (Prior art) Conventionally, sheets made from various types of fibers have been used mainly for gaskets, etc., but even when paper is made from only fibers, the fibers are only physically entangled.
Since the chemical bonding force between fibers is extremely weak, gaskets etc. with satisfactory strength cannot be obtained. Therefore, in order to increase the bonding strength between fibers, fibers are generally produced by an internal addition method using a natural or synthetic polymeric latex as a binder. (Problems to be Solved by the Invention) Acrylonitrile-butadiene copolymer latex has been used as a binder for the purpose of improving the strength of papermaking and imparting oil resistance. However, this latex contains polymerization agents such as surfactants and various inorganic salts used during polymerization, and because these are present in papermaking, sufficient water resistance cannot be obtained, and improvements are desired. ing. (Means for Solving the Problems) As a result of intensive research in order to solve the above-mentioned drawbacks, the present inventors have developed a method for converting unsaturated compounds containing epoxy groups into conjugated diene monomers and ethylene nitrile monomers by emulsion polymerization. It was discovered that internal addition using a latex copolymerized with acrylonitrile-butadiene copolymer improves the water resistance of papermaking compared to internal addition using a conventional acrylonitrile-butadiene copolymer latex. The present invention has now been completed. That is, the present invention provides a latex for internal addition to paper making, which is obtained by emulsion copolymerizing an epoxy group-containing monomer, a conjugated diene monomer, and an ethylene nitrile monomer. The epoxy group-containing monomer used in the present invention is an essential monomer for improving the water resistance of papermaking. The monomer containing an epoxy group may be any monomer that is radically copolymerizable with other monomers constituting the copolymer of the present invention, such as vinyl glycidyl ether, allyl glucidyl ether, methallyl glycidyl One or more types of ether, glycidyl acrylate, glycidyl methacrylate, etc. are used. The amount used is at least 0.1% by weight in the monomer mixture (hereinafter the same)
If the amount is less than 0.1% by weight, the water resistance of papermaking will not be improved. If it exceeds 10% by weight, the water resistance will be saturated, so further use is not necessary. Preferably it is 1 to 5% by weight. The conjugated diene monomer used in the present invention is
For example, isoprene, 1,3-butadiene, 2-
Methyl-1,3-butadiene, 2-chloro-1,
3-butadiene, 1,3-pentadiene, etc., and one or more of these may be used. Usage is usually 35
~98.9% by weight. If it is less than 35% by weight, the flexibility of the paper will be poor, and if it exceeds 98.9% by weight, the polymerization reaction rate will be reduced, and the strength of the paper will be reduced. Preferably it is 50 to 84% by weight. As the ethylene-based nitrile monomer, one type of nitrile such as acrylonitrile, methacrylonitrile, and α-chloro-acrylonitrile is used. The amount used is usually 1 to 55% by weight; if it is less than 1% by weight, the strength and oil resistance of the paper will be insufficient;
If it exceeds this amount, the flexibility of the papermaking product will decrease and the polymerization reaction rate will also decrease, which is not preferable. Preferably
It is 15-50% by weight. Further, if necessary, an unsaturated carboxylic acid monomer such as acrylic acid or methacrylic acid, or an alkyl ester thereof may be included in an amount of 20% by weight or less in the total monomer mixture. The use of unsaturated carboxylic acid monomers is particularly desirable in increasing the stability of the latex. The latex of the present invention can be obtained by copolymerizing the above-mentioned monomers by conventional emulsion polymerization.
It may be a continuous type or the like, and is not particularly limited.
Further, the emulsifier, polymerization initiator, molecular weight regulator, and other polymerization agents used may be those used in ordinary emulsion polymerization, and are not particularly limited. Examples of fibers used to produce paper include asbestos, cellulose fibers, aromatic polyamide fibers, carbon fibers, phenol fibers, ceramic fibers, and inorganic fibers other than asbestos.
Optionally, minerals can be added to the fibers to produce dense sheets. As an inorganic substance,
Examples include clay talc, silicic acid, aluminum silicate, calcium carbonate, and the like. When manufacturing papermaking using the latex of the present invention, the latex of the present invention is used as a binder in a solid content of usually 0.5 to 100% by weight, preferably 1 to 30% by weight, based on the fibers, and is used in a beater or After adding the fibers in a process such as bochering and stirring thoroughly, if necessary, add 0.5 to 10% by weight of an inorganic salt, preferably sulfuric acid, or a polymer flocculant to complete fixation of the binder to the fibers. It is made into paper-like material using a paper-making machine. Thus, according to the present invention, compared to conventional paper making using a latex of acrylonitrile-butadiene copolymer containing epoxy groups as a binder, the paper has the same strength properties and oil resistance but has excellent water resistance. Paper making can be obtained. Paper making using the latex of the present invention is mainly useful for gaskets that require oil resistance. EXAMPLES The present invention will be explained in more detail with reference to Examples below. Example 1 In an autoclave equipped with a stirrer, water, butadiene, acrylonitrile, glycidyl methacrylate, sodium lauryl sulfate,
After charging t-dodecyl mercaptan, the mixture was heated to 35°C, and ammonium persulfate was added to start the reaction. At a polymerization conversion rate of 98% or higher (measured gravimetrically), the autoclave was cooled to room temperature to stop the reaction. The autoclave was kept at 35°C during the reaction. The obtained copolymer latex is referred to as latex A. Similarly, a copolymer latex using allyl glycidyl ether instead of glycidyl methacrylate (latex B) and a latex containing no epoxy machine (latex C) were obtained.

【表】【table】

【表】 抄造紙用繊維として石綿を選び、これらのラテ
ツクスをバインダーとする石綿紙の抄造を次の通
りに行つた。 クリスタイル石綿(6D−5)100gを水15dm3
とともに3dm3の離解機(テスター産業株式会社
製)に添加して2分間撹拌した後、ラテツクス60
g(固形分濃度25%)を添加した。添加した後30
秒撹拌し、硫酸バン土を1.5cm3(濃度5%)添加
し、ラテツクスを完全に石綿に定着させ、更に30
秒撹拌した。得られたアスベストスラリー1dm3
を手抄試験機(テスター産業株式会社製)にて抄
造し、5Kg/cm2で10分間プレスして水を切り、そ
の後オーブンにて130℃、10分間乾燥させた。得
られた石綿紙を5×2cmの試験片とし、その重量
を測定した。耐水性を評価するために蒸留水を入
れた還硫冷却管付き大型試験官に試験片をそれぞ
れが触れないように針金に固定して浸漬させ、
100℃オイルバス中で5時間加熱した。試験片を
取り出し、タオルペーパー(十條キンバリ社製)
にて軽く水を吸いとつた後、試験片の重量を測
り、浸漬による重量増分浸漬前重量にて割り、重
量変化率とした。ラテツクスA、B、Cを用いて
抄造された石綿抄造紙の蒸留水浸漬による重量変
化率を表2に示す。表2の値は、試験片4枚の平
均値である。
[Table] Asbestos was selected as the fiber for papermaking, and asbestos paper was produced using these latexes as a binder as follows. Crystalline asbestos (6D-5) 100g in water 15dm 3
After adding it to a 3dm3 disintegrating machine (manufactured by Tester Sangyo Co., Ltd.) and stirring for 2 minutes, the latex
g (solid content concentration 25%) was added. After adding 30
Stir for 2 seconds, add 1.5 cm 3 (concentration 5%) of sulfuric acid, allow the latex to completely settle on the asbestos, and then add
Stir for seconds. Obtained asbestos slurry 1dm 3
was made into a paper using a hand paper testing machine (manufactured by Tester Sangyo Co., Ltd.), pressed at 5 kg/cm 2 for 10 minutes to remove water, and then dried in an oven at 130°C for 10 minutes. The obtained asbestos paper was made into a 5 x 2 cm test piece, and its weight was measured. In order to evaluate water resistance, each test piece was fixed to a wire and immersed in a large tester equipped with a sulfuric cooling tube filled with distilled water.
It was heated in a 100°C oil bath for 5 hours. Take out the test piece and wrap it with towel paper (manufactured by Jujo Kimbali Co., Ltd.)
After lightly absorbing water, the weight of the test piece was measured, and the weight change rate was calculated by dividing the weight increase due to immersion by the weight before immersion. Table 2 shows the weight change rate of asbestos paper made using latexes A, B, and C when immersed in distilled water. The values in Table 2 are the average values of four test pieces.

【表】 表2より、エポキシ基含有単量体を共重合した
ラテツクスA、Bを用いた場合は、エポキシ基含
有量単量体を共重合していないラテツクスCを用
いた場合に比べて、蒸留水浸漬後の重変化率にお
いて改良されているのがわかる。又、耐水性以外
の引裂強度、耐油性等の特性についても試験した
が、エポキシ基の存在による差異は認められなか
つた。 実施例 2 表3の重合処方に従つて、実施例1と同様の重
合操作にて重合を行ない得られたラテツクスD、
E、F、Gを用いて、石綿紙の抄造を実施例1と
同様な方法にて行つた。それぞれの石綿紙の蒸留
水浸漬後の重量変化率を測定した。結果を表4に
示す。
[Table] From Table 2, when latexes A and B in which epoxy group-containing monomers were copolymerized were used, compared to latex C in which epoxy group-containing monomers were not copolymerized, It can be seen that the weight change rate after immersion in distilled water was improved. Furthermore, properties other than water resistance, such as tear strength and oil resistance, were tested, but no differences were observed due to the presence of epoxy groups. Example 2 Latex D obtained by polymerization in the same polymerization operation as in Example 1 according to the polymerization recipe in Table 3,
Using E, F, and G, asbestos paper was made in the same manner as in Example 1. The weight change rate of each asbestos paper after immersion in distilled water was measured. The results are shown in Table 4.

【表】【table】

【表】 表4より明らかなようにグリシジルメタクリレ
ートの量と共に、重量変化率が低くなり、エポキ
シ基の効果があらわれていることがわかる。また
グリシジルメタクリレートを13部共重合したもの
は、その効果が飽和してしまつている。 実施例 3 表5の重合処方に従つて、実施例1と同様の重
合操作にて集合を行い、得られたラテツクスH、
I、J、K、Lを用いて、石綿紙の抄造を実施例
1と同様な方法にて行なつた。それぞれの石綿紙
の蒸留水浸漬後の重量変化率を測定した。結果を
表6に示す。
[Table] As is clear from Table 4, the weight change rate decreases as the amount of glycidyl methacrylate increases, indicating that the effect of the epoxy group appears. Furthermore, the effect of the product copolymerized with 13 parts of glycidyl methacrylate has been saturated. Example 3 According to the polymerization recipe in Table 5, aggregation was carried out in the same polymerization operation as in Example 1, and the obtained latex H,
Asbestos paper was made using I, J, K, and L in the same manner as in Example 1. The weight change rate of each asbestos paper after immersion in distilled water was measured. The results are shown in Table 6.

【表】【table】

【表】 表6より、ラテツクスHとKを用いた場合の比
較、ラテツクスJとLを用いた場合の比較より、
ブタジエンとアクリロニトリルの使用割合を大幅
に変えた場合にも、グリシジルメタクリレートを
共重合することにより耐水性が著しく改善される
ことが分る。 実施例 4 バルブ(NBKP)18gを水1.15dm3とともに実
施例1と同様の離解機に添加し5分間撹拌した。
その後、タルク(日本タルク株式会社製SS)82
gを加え、1分間撹拌した後、実施例1で得たラ
テツクスA60g(固形分濃度25重量%)を添加し
た。30秒撹拌し硫酸バン土を5cm3(濃度10重量
%)添加し、ラテツクスを完全に定着させ、更に
30秒撹拌した。得られたスラリー450cm3に水を加
え5dm3とした後、実施例1と同様の手抄試験機
にて抄造し、10Kg/cm2で10分間プレスして水を切
り、その後オーブンにて130℃、10分間乾燥させ
た。得られたシートを5×2cmの試験片として、
実施例1と同様な方法にて耐水性を評価した。ラ
テツクスCを用いて得た抄造紙についても耐水性
を評価した。評価を表7に示す。
[Table] From Table 6, from the comparison when using latex H and K, and from the comparison when using latex J and L,
It can be seen that water resistance is significantly improved by copolymerizing glycidyl methacrylate even when the ratio of butadiene and acrylonitrile used is significantly changed. Example 4 18 g of Bulb (NBKP) and 1.15 dm 3 of water were added to the same disintegrator as in Example 1 and stirred for 5 minutes.
Then, talc (SS manufactured by Nippon Talc Co., Ltd.) 82
After stirring for 1 minute, 60 g of latex A obtained in Example 1 (solid content concentration 25% by weight) was added. Stir for 30 seconds, add 5 cm 3 of sulfuric acid (concentration 10% by weight) to completely fix the latex, and then
Stir for 30 seconds. After adding water to 450 cm 3 of the obtained slurry to make it 5 dm 3 , it was made into a paper using the same hand paper testing machine as in Example 1, pressed at 10 Kg/cm 2 for 10 minutes to drain the water, and then placed in an oven for 130 cm. ℃ for 10 minutes. The obtained sheet was used as a 5 x 2 cm test piece.
Water resistance was evaluated in the same manner as in Example 1. The paper made using Latex C was also evaluated for water resistance. The evaluation is shown in Table 7.

【表】 表7より明らかに、パルプ−タクルの抄造紙に
おいても、グリシジルメタクリレートを共重合さ
せたラテツクスが耐水性にすぐれていることがわ
かる。
[Table] It is clear from Table 7 that the latex copolymerized with glycidyl methacrylate has excellent water resistance even in pulp-tackle paper making.

Claims (1)

【特許請求の範囲】[Claims] 1 エポキシ基含有単量体、共役ジエン系単量
体、及びエチレン系ニトリル単量体を乳化共重合
して成る抄造紙内添用ラテツクス。
1. A latex for internal addition to paper making made by emulsion copolymerization of an epoxy group-containing monomer, a conjugated diene monomer, and an ethylene nitrile monomer.
JP22965984A 1984-10-31 1984-10-31 Latex for internal addition to paper making Granted JPS61108798A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22965984A JPS61108798A (en) 1984-10-31 1984-10-31 Latex for internal addition to paper making

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22965984A JPS61108798A (en) 1984-10-31 1984-10-31 Latex for internal addition to paper making

Publications (2)

Publication Number Publication Date
JPS61108798A JPS61108798A (en) 1986-05-27
JPH0555639B2 true JPH0555639B2 (en) 1993-08-17

Family

ID=16895666

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22965984A Granted JPS61108798A (en) 1984-10-31 1984-10-31 Latex for internal addition to paper making

Country Status (1)

Country Link
JP (1) JPS61108798A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0229441U (en) * 1988-08-11 1990-02-26
CN109400805A (en) * 2018-10-24 2019-03-01 安庆华兰科技有限公司 One kind is with epoxy group liquid nitrile rubber and preparation method thereof
KR102928057B1 (en) * 2018-12-19 2026-02-20 아란세오 도이치란드 게엠베하 Electrode composition for a cathode of a lithium ion battery cell, cathode slurry composition, cathode and battery incorporating the same
ES2994088T3 (en) * 2019-05-28 2025-01-17 Daikin Ind Ltd Oil-resistant agent for paper

Also Published As

Publication number Publication date
JPS61108798A (en) 1986-05-27

Similar Documents

Publication Publication Date Title
FI96426C (en) composite board
FI86988B (en) Process for producing film-forming, systematically structured latex particles and a film which has been formed from these particles
JPH0342360B2 (en)
JPS6335760B2 (en)
CN1085716C (en) Latex composition and its prep.
FI67866C (en) FOERFARANDE FOER FRAMSTAELLNING AV EN KARBOXYLERAD LATEX
JPH0555639B2 (en)
JPS628443B2 (en)
US5629047A (en) Method of making functionalized styrene butadiene type latex binders
US4209562A (en) Latex blend binder compositions for asbestos sheets
US4378272A (en) Water purifying latex binder
US20220380581A1 (en) Rubber composition and production method therefor
EP0075529A2 (en) Improved continuous emulsion polymerization process of a diene latex
JPS61108797A (en) Latex for internal addition to paper making
JP3277647B2 (en) Paper impregnating composition and impregnated paper
KR840001832B1 (en) Process for producing copolymer latex
JPS61261302A (en) Method for producing cationic polymer latex
JP4731660B2 (en) Paper making method
JPH0351839B2 (en)
JP3115837B2 (en) Method for producing copolymer latex
US3338862A (en) Oil resistant nitrile rubbers and rubber cements prepared therefrom
US3144379A (en) Process of precipitating chloroparene polymer latex onto chrysotile asbestos fibers in a slurry using magnesium chloride as sole precipitating agent
JP3472922B2 (en) Reactive emulsifier for paper coating latex, copolymer latex for paper coating, and composition for paper coating
JPH0541756B2 (en)
JP3718568B2 (en) Polymer emulsion and method for producing the same

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees