JP3396263B2 - Aqueous dispersion resin composition - Google Patents
Aqueous dispersion resin compositionInfo
- Publication number
- JP3396263B2 JP3396263B2 JP20387293A JP20387293A JP3396263B2 JP 3396263 B2 JP3396263 B2 JP 3396263B2 JP 20387293 A JP20387293 A JP 20387293A JP 20387293 A JP20387293 A JP 20387293A JP 3396263 B2 JP3396263 B2 JP 3396263B2
- Authority
- JP
- Japan
- Prior art keywords
- aqueous dispersion
- dispersion resin
- ppm
- added
- resin composition
- 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 - Lifetime
Links
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- Compositions Of Macromolecular Compounds (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Paper (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は水分散体樹脂、例えば塗
被紙,塗料,化粧品,接着剤等の分野に利用されている
水分散体樹脂の貯蔵安定性を改良し、各分野で要求され
ている品質に悪影響を与えない水分散体組成物に関する
ものである。
【0002】
【従来技術及び発明が解決しようとする課題】近年、大
気の汚染やオゾン層の破壊を始めとする環境問題や、石
油系資源の節約等の観点から有機溶剤の使用規制が強化
されている。係る規制問題と取扱い作業性の面から水希
釈可能な水分散体樹脂への切り換えが増加している。し
かし水分散体樹脂は水中に合成樹脂の粒子を分散させて
いるものであり、貯蔵しておくと分離や凝集を起こすこ
とがしばしばあった。分離や凝集のメカニズムは、概略
重力による沈降分離、ファンデアワールス力による凝集
分離等が言われており、一般にこれら不安定要因を取り
除くには、ブラウン運動を高めるために粒子径を小さく
したり、粒子の衝突をなくすために粒子にカルボン酸等
の官能基を導入し、電気二重層を形成させイオン反発を
させたり、ノニオン基の導入で水和層を厚くしたり、保
護コロイド剤を使用する方法であった。しかしこれらは
用途や使用方法によっては、目的とする性能を低下させ
ることがある。一例を示すとキャスト紙用塗被組成物に
用いる合成ゴムラテックスに於いては、貯蔵安定性効果
の大きいカルボン酸を粒子に導入するとキャスト紙の離
形性が低下し結果として作業性が損なわれる。又塗被紙
組成物中のプラスチックピグメントに於いては、粒子径
が0.5〜1μの領域で塗被紙の物性が向上するため、
粒子径を小さくすることに物性上の制限があり、貯蔵安
定性には問題があった。以上のように貯蔵安定性を改良
する方法については種々検討されているが、未だ充分で
はなく、貯蔵安定性の良好な水分散体樹脂組成物の開発
が嘱望されている。
【0003】
【課題を解決するための手段】発明者らは、貯蔵安定性
の良好な水分散体樹脂組成物について種々検討を重ねた
結果、水分散体樹脂にニトロアルコール類を含有させる
ことにより飛躍的に貯蔵安定性を向上せしめることを見
出し、本発明を完成するに至った。即ち本発明は、水分
散体樹脂中に特定のニトロアルコール化合物を10〜5
000ppm含有していることを特徴とする水分散体樹
脂組成物である。
【0004】
【0005】以下、本発明について詳述する。水分散体
樹脂の例としては、酢ビエマルジョン、エチレン酢ビエ
マルジョン、アクリルエマルジョン、合成ゴムラテック
ス、プラスチックピグメントエマルジョン等である。又
本発明で用いられるニトロアルコ−ル類としては、2,
2−ジブロモ−2−ニトロ−1−エタノールおよび2−
クロロ−2−ニトロエタノールが好ましい。又上記化合
物は単独でも、又併用して用いても良い。ニトロアルコ
ール類の添加は、水分散体樹脂の製造工程中であって
も、また製造後であってもよく、使用方法には制約を受
けない。又水分散体樹脂中には、公知の添加剤等を併用
してもよいが、ニトロアルコール類の使用量は水分散体
樹脂に対し10〜5000ppm、好ましくは50〜1
000ppmの範囲であるべきであり、使用量が10p
pm以下では貯蔵安定性は改善されないし又5000p
pmを越えて用いも貯蔵安定性は改善されない。以下に
実施例により本発明を更に詳細に説明するが、本発明は
これらの実施例により何ら限定されるものではない。
【0006】
【実施例】本発明に使用する水分散体樹脂は以下に示す
方法により製造した。
水分散体樹脂(合成ゴムラテックス)の製造例
製造例−1
100L撹拌機付きのオートクレーブにイオン交換水3
8.53kg、ラウリル硫酸ナトリウム0.38kg、
及び平均粒子径0.05μ、固形分濃度25重量%のシ
ード粒子3.02kg、過硫酸カリウム0.76kg、
苛性カリウム76gを仕込み窒素で系内を置換した。そ
の後、系内にブタジエン13.23kg、メタクリル酸
メチル24.57kg、ターシャリードデシルメルカプ
タン113gを仕込み150rpmで撹拌しながら60
分間で室温から70℃に内温を上昇させ、この温度で1
0時間反応させた。その後、室温まで冷却して固形分濃
度48.7重量%,pH7.5,平均粒子径0.19μ
の水分散体樹脂1を得た。
【0007】製造例−2
100L撹拌機付きのオートクレーブにイオン交換水4
6kg、ラウリル硫酸ナトリウム157gを仕込み窒素
で系内を置換した。その後、200rpmの撹拌を行い
ながら内温を上昇させ80℃に保ち、(A)ブタジエン
18.81kg、スチレン11.28kg、アクリル酸
1.25kg、ターシャリードデシルメルカプタン28
2gの混合液、(B)ラウリル硫酸ナトリウム31g、
過硫酸ナトリウム188g、イオン交換水1975gと
の水溶液をそれぞれ調整し、混合液(A)は6時間,水
溶液(B)は6.5時間をかけて反応系内に添加した。
添加終了後、さらに残モノマー重合として1時間反応さ
せた。その後、室温まで冷却して固形分濃度38.9重
量%,pH1.9のゴムラテックスをえた。このゴムラ
テックスは水酸化ナトリウムにより、pHを8に調節
し、スチームストリッピング及び濃縮を行って、平均粒
子径0.1μ、固形分濃度50重量%の水分散体樹脂2
を得た。
【0008】
プラスチックピグメントエマルジョンの製造例
製造例−3
10Lコンデンサー付きフラスコにイオン交換水354
7g,平均粒子径0.25μ、固形分濃度40重量%の
シード粒子452g、ラウリル硫酸ナトリウム3.6g
を仕込み窒素で系内を置換した。その後、200rpm
の撹拌を行いながら内温を上昇させ80℃に保ち、
(A)スチレン3544g,アクリル酸72.3gの混
合液、(B)イオン交換水159g,ラウリル硫酸ナト
リウム3.6g、過硫酸ナトリウム18.1gとの水溶
液をそれぞれ調整し、混合液(A)は5時間,水溶液
(B)は6時間をかけて反応系内に添加した。添加終了
後、さらに残モノマー重合として2時間反応させた。そ
の後、室温まで冷却して固形分重量%48.7,pH
2.1のエマルジョンをえた。次いで水酸化ナトリウム
により、pHを8に調節し、平均粒子径0.7μ、固形
分濃度48.3重量%の水分散体樹脂3を得た。
【0009】実施例1、2
水分散体樹脂1に2、2−ジブロモ−2−ニトロ−1−
エタノールを50ppm添加した場合を実施例1とし、
同じく4000ppm添加した場合を実施例2とした。
実施例3、4
水分散体樹脂2に2、2−ジブロモ−2−ニトロ−1−
エタノールを50ppm添加した場合を実施例3とし、
同じく4000ppm添加した場合を実施例4とした。
実施例5、6
水分散体樹脂3に2、2−ジブロモ−2−ニトロ−1−
エタノールを50ppm添加した場合を実施例5とし、
同じく4000ppm添加した場合を実施例6とした。
【0010】比較例1、2
水分散体樹脂1に2、2−ジブロモ−2−ニトロ−1−
エタノールを5ppm添加した場合を比較例1とし、同
じく6000ppm添加した場合を比較例2とした。
比較例3、4
水分散体樹脂2に2、2−ジブロモ−2−ニトロ−1−
エタノールを5ppm添加し場合を比較例3とし、同じ
く6000ppm添加した場合を比較例4とした。
比較例5、6
水分散体樹脂3に2、2−ジブロモ−2−ニトロ−1−
エタノールを5ppm添加し場合を比較例5とし、同じ
く6000ppm添加した場合を比較例6とした。以上
の実施例及び比較例で得られた各水分散体樹脂組成物に
ついての貯蔵安定性試験を行った。試験方法は以下に示
す。結果は纏めて表1に示した。
【0011】貯蔵安定性試験方法
直径1cm,長さ1.5mのガラス管に各水分散体樹脂
組成物を1.45mの高さになるまで加えた。その後、
一ヶ月置きに6ケ月間、ガラス管の上層部より約1gの
試料を採取し、各試料を乾燥させ、固形分を求めた。
【0012】
【表1】
【0013】
【発明の効果】表1から本発明による水分散体樹脂組成
物は貯蔵安定性に優れている。これに対し、ニトロアル
コール類の使用範囲が本願発明の範囲を外れたもので
は、貯蔵安定性の効果は得られない。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the storage of water-dispersed resins, for example, water-dispersed resins used in the fields of coated papers, paints, cosmetics, adhesives and the like. The present invention relates to an aqueous dispersion composition which improves stability and does not adversely affect the quality required in each field. 2. Description of the Related Art In recent years, regulations on the use of organic solvents have been tightened from the viewpoints of environmental problems such as air pollution and destruction of the ozone layer, and saving of petroleum resources. ing. In view of such regulation problems and handling operability, switching to a water-dilutable water-dispersible resin is increasing. However, the aqueous dispersion resin is obtained by dispersing synthetic resin particles in water, and often causes separation or aggregation when stored. The mechanism of separation and aggregation is roughly called sedimentation separation by gravity, aggregation separation by Van der Waals force, etc.In general, to remove these instability factors, reduce the particle diameter to increase Brownian motion, In order to eliminate the collision of particles, functional groups such as carboxylic acid are introduced into the particles to form an electric double layer to repel ions, to increase the hydrated layer by introducing nonionic groups, and to use a protective colloid agent Was the way. However, these may degrade the intended performance depending on the application and the method of use. As an example, in a synthetic rubber latex used for a coating composition for cast paper, when a carboxylic acid having a large storage stability effect is introduced into the particles, the releasability of the cast paper is reduced, resulting in impaired workability. . In the case of the plastic pigment in the coated paper composition, the physical properties of the coated paper are improved in a particle size range of 0.5 to 1 μm.
There are physical limitations on reducing the particle size, and there is a problem with storage stability. As described above, various methods for improving the storage stability have been studied, but they are not yet sufficient, and development of an aqueous dispersion resin composition having good storage stability has been demanded. [0003] The inventors of the present invention have conducted various studies on an aqueous dispersion resin composition having good storage stability, and as a result, by adding nitro alcohols to the aqueous dispersion resin. The inventors have found that storage stability is dramatically improved, and have completed the present invention. That is, the present invention provides a method in which a specific nitro alcohol compound is added to an aqueous dispersion resin in an amount of 10 to 5 times.
An aqueous dispersion resin composition characterized by containing 000 ppm. Hereinafter, the present invention will be described in detail. Examples of the aqueous dispersion resin include vinyl acetate emulsion, ethylene vinyl acetate emulsion, acrylic emulsion, synthetic rubber latex, and plastic pigment emulsion. or
The nitro alcohols used in the present invention include 2,2
2-dibromo-2-nitro-1-ethanol and 2-
Chloro-2-nitroethanol is preferred. The above compounds may be used alone or in combination. The addition of the nitro alcohol may be during or after the production process of the aqueous dispersion resin, and there is no limitation on the method of use. In the aqueous dispersion resin, known additives and the like may be used in combination, but the amount of nitro alcohol used is 10 to 5000 ppm, preferably 50 to 1 ppm based on the aqueous dispersion resin.
Should be in the range of 000 ppm, and the
pm or less, storage stability is not improved and 5000p
Use above pm does not improve storage stability. Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. The aqueous dispersion resin used in the present invention was produced by the following method. Production Example of Water Dispersion Resin (Synthetic Rubber Latex) Production Example-1 Ion-exchange water 3
8.53 kg, sodium lauryl sulfate 0.38 kg,
And 3.02 kg of seed particles having an average particle size of 0.05 μ and a solid concentration of 25% by weight, 0.76 kg of potassium persulfate,
76 g of caustic potassium was charged and the inside of the system was replaced with nitrogen. Thereafter, 13.23 kg of butadiene, 24.57 kg of methyl methacrylate, and 113 g of tertiary decyl mercaptan are charged into the system, and the mixture is stirred at 150 rpm for 60 minutes.
The internal temperature is raised from room temperature to 70 ° C. in
The reaction was performed for 0 hours. Thereafter, the mixture was cooled to room temperature, and the solid concentration was 48.7% by weight, pH 7.5, and the average particle diameter was 0.19 μ
Aqueous Dispersion Resin 1 was obtained. Production Example 2 Ion-exchanged water 4 in an autoclave equipped with a 100 L stirrer
6 kg and 157 g of sodium lauryl sulfate were charged and the inside of the system was replaced with nitrogen. Thereafter, the internal temperature was increased to 80 ° C. while stirring at 200 rpm, and (A) 18.81 kg of butadiene, 11.28 kg of styrene, 1.25 kg of acrylic acid, and tertiary decyl mercaptan 28
2 g of the mixture, (B) 31 g of sodium lauryl sulfate,
Aqueous solutions of 188 g of sodium persulfate and 1975 g of ion-exchanged water were prepared, and the mixture (A) was added to the reaction system over 6 hours and the aqueous solution (B) over 6.5 hours.
After completion of the addition, the reaction was further carried out for 1 hour as residual monomer polymerization. Thereafter, the mixture was cooled to room temperature to obtain a rubber latex having a solid content of 38.9% by weight and a pH of 1.9. This rubber latex was adjusted to pH 8 with sodium hydroxide, and subjected to steam stripping and concentration to obtain an aqueous dispersion resin 2 having an average particle size of 0.1 μm and a solid concentration of 50% by weight.
Got. Production Example of Plastic Pigment Emulsion Production Example-3 Ion-exchanged water 354 in a flask with a 10 L condenser
7 g, 452 g of seed particles having an average particle diameter of 0.25 μ and a solid concentration of 40% by weight, and 3.6 g of sodium lauryl sulfate
And the inside of the system was replaced with nitrogen. After that, 200rpm
While stirring, raise the internal temperature to 80 ° C,
(A) A mixed solution of 3544 g of styrene and 72.3 g of acrylic acid, (B) an aqueous solution of 159 g of ion-exchanged water, 3.6 g of sodium lauryl sulfate, and 18.1 g of sodium persulfate were prepared. The aqueous solution (B) was added to the reaction system over 6 hours over 5 hours. After completion of the addition, the mixture was further reacted for 2 hours as residual monomer polymerization. Thereafter, the mixture was cooled to room temperature, and the solid content was 48.7% by weight, pH
An emulsion of 2.1 was obtained. Then, the pH was adjusted to 8 with sodium hydroxide to obtain an aqueous dispersion resin 3 having an average particle size of 0.7 μm and a solid content concentration of 48.3% by weight. Examples 1 and 2 2,2-dibromo-2-nitro-1-
Example 1 was a case where ethanol was added at 50 ppm,
Example 2 was also the case where 4000 ppm was added. Examples 3 and 4 2,2-dibromo-2-nitro-1-
The case where 50 ppm of ethanol was added is referred to as Example 3,
Example 4 was also the case where 4000 ppm was added. Examples 5 and 6 2,2-dibromo-2-nitro-1-
Example 5 in which 50 ppm of ethanol was added,
Example 6 was also the case where 4000 ppm was added. Comparative Examples 1 and 2, 2,2-dibromo-2-nitro-1-
Comparative Example 1 was a case where ethanol was added at 5 ppm, and Comparative Example 2 was a case where ethanol was also added at 6000 ppm. Comparative Examples 3 and 4, 2,2-dibromo-2-nitro-1-
Comparative Example 3 was a case where ethanol was added at 5 ppm, and Comparative Example 4 was a case where ethanol was also added at 6000 ppm. Comparative Examples 5 and 6 2,2-dibromo-2-nitro-1-
Comparative Example 5 was a case where ethanol was added at 5 ppm, and Comparative Example 6 was a case where ethanol was also added at 6000 ppm. A storage stability test was performed for each of the aqueous dispersion resin compositions obtained in the above Examples and Comparative Examples. The test method is shown below. The results are summarized in Table 1. Storage stability test method Each aqueous dispersion resin composition was added to a glass tube having a diameter of 1 cm and a length of 1.5 m until a height of 1.45 m was reached. afterwards,
About 1 g of a sample was taken from the upper part of the glass tube every other month for 6 months, and each sample was dried to obtain a solid content. [Table 1] From Table 1, it can be seen that the aqueous dispersion resin composition of the present invention has excellent storage stability. On the other hand, if the use range of the nitro alcohol is out of the range of the present invention, the effect of storage stability cannot be obtained.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C08K 5/32 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 7 , DB name) C08K 5/32
Claims (1)
2−ニトロ−1−エタノールおよび2−クロロ−2−ニ
トロエタノールから選ばれた化合物を10〜5000p
pm含有していることを特徴とする水分散体樹脂組成
物。(57) [Claim 1] 2,2-dibromo- is contained in an aqueous dispersion resin.
2-nitro-1-ethanol and 2-chloro-2-ni
10 to 5000p of compounds selected from troethanol
An aqueous dispersion resin composition containing pm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20387293A JP3396263B2 (en) | 1993-08-18 | 1993-08-18 | Aqueous dispersion resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20387293A JP3396263B2 (en) | 1993-08-18 | 1993-08-18 | Aqueous dispersion resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0753775A JPH0753775A (en) | 1995-02-28 |
JP3396263B2 true JP3396263B2 (en) | 2003-04-14 |
Family
ID=16481115
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20387293A Expired - Lifetime JP3396263B2 (en) | 1993-08-18 | 1993-08-18 | Aqueous dispersion resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3396263B2 (en) |
-
1993
- 1993-08-18 JP JP20387293A patent/JP3396263B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0753775A (en) | 1995-02-28 |
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