JPS6346092B2 - - Google Patents
Info
- Publication number
- JPS6346092B2 JPS6346092B2 JP55014365A JP1436580A JPS6346092B2 JP S6346092 B2 JPS6346092 B2 JP S6346092B2 JP 55014365 A JP55014365 A JP 55014365A JP 1436580 A JP1436580 A JP 1436580A JP S6346092 B2 JPS6346092 B2 JP S6346092B2
- Authority
- JP
- Japan
- Prior art keywords
- aqueous solution
- polyamide polyamine
- reaction
- viscosity
- temperature
- 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
- 229920000768 polyamine Polymers 0.000 claims description 52
- 239000004952 Polyamide Substances 0.000 claims description 44
- 229920002647 polyamide Polymers 0.000 claims description 44
- 239000007864 aqueous solution Substances 0.000 claims description 39
- 238000006243 chemical reaction Methods 0.000 claims description 29
- 239000007787 solid Substances 0.000 claims description 25
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 22
- 239000000047 product Substances 0.000 claims description 18
- 229920005989 resin Polymers 0.000 claims description 15
- 239000011347 resin Substances 0.000 claims description 15
- 125000000467 secondary amino group Chemical group [H]N([*:1])[*:2] 0.000 claims description 12
- 239000002253 acid Substances 0.000 claims description 9
- 229920001281 polyalkylene Polymers 0.000 claims description 9
- 125000001931 aliphatic group Chemical group 0.000 claims description 7
- 229920006395 saturated elastomer Polymers 0.000 claims description 7
- 229920001187 thermosetting polymer Polymers 0.000 claims description 7
- 239000007795 chemical reaction product Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 125000002091 cationic group Chemical group 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 3
- 150000001768 cations Chemical class 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 32
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 24
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 16
- 239000012467 final product Substances 0.000 description 9
- 239000001361 adipic acid Substances 0.000 description 8
- 235000011037 adipic acid Nutrition 0.000 description 8
- 238000003756 stirring Methods 0.000 description 8
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000012295 chemical reaction liquid Substances 0.000 description 5
- MTJGVAJYTOXFJH-UHFFFAOYSA-N 3-aminonaphthalene-1,5-disulfonic acid Chemical compound C1=CC=C(S(O)(=O)=O)C2=CC(N)=CC(S(O)(=O)=O)=C21 MTJGVAJYTOXFJH-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 230000002708 enhancing effect Effects 0.000 description 3
- 230000001965 increasing effect Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000376 reactant Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003623 enhancer Substances 0.000 description 2
- BDJRBEYXGGNYIS-UHFFFAOYSA-N nonanedioic acid Chemical compound OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 2
- WLJVNTCWHIRURA-UHFFFAOYSA-N pimelic acid Chemical compound OC(=O)CCCCCC(O)=O WLJVNTCWHIRURA-UHFFFAOYSA-N 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- TYFQFVWCELRYAO-UHFFFAOYSA-N suberic acid Chemical compound OC(=O)CCCCCCC(O)=O TYFQFVWCELRYAO-UHFFFAOYSA-N 0.000 description 2
- RTBFRGCFXZNCOE-UHFFFAOYSA-N 1-methylsulfonylpiperidin-4-one Chemical compound CS(=O)(=O)N1CCC(=O)CC1 RTBFRGCFXZNCOE-UHFFFAOYSA-N 0.000 description 1
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 description 1
- XYUINKARGUCCQJ-UHFFFAOYSA-N 3-imino-n-propylpropan-1-amine Chemical compound CCCNCCC=N XYUINKARGUCCQJ-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- JFCQEDHGNNZCLN-UHFFFAOYSA-N anhydrous glutaric acid Natural products OC(=O)CCCC(O)=O JFCQEDHGNNZCLN-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000013054 paper strength agent Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
Description
本発明は、貯蔵安定性のよい陽イオン性熱硬化
性樹脂水溶液の製造法に関する。
従来から、湿潤紙力増強剤として有用なポリア
ミドポリアミン−エピクロルヒドリン樹脂は、た
とえば、特公昭35−3547,および特開昭54−
159496の方法により製造しうることが知られてい
る。しかし、これら従来公知の方法によつて得ら
れるポリアミドポリアミン・エピクロルヒドリン
樹脂は貯蔵安定性,湿潤紙力増強効果およびろ水
性向上効果のすべてにおいて必ずしも満足しうる
ものとはいえない。
本発明者らは上記公知方法により製造された樹
脂の欠点に鑑み鋭意検討を重ねた結果、ポリアミ
ドポリアミン・エピクロルヒドリン樹脂を製造す
るための反応条件を特定化することにより湿潤紙
力増強効果に優れかつ貯蔵安定性の高い樹脂を得
ることに成功した。
すなわち本発明は、脂肪族飽和二塩基酸とポリ
アルキレンポリアミンとを加熱縮合させてポリア
ミドポリアミンを合成し、ついでこのポリアミド
ポリアミンを水溶液中でエピクロルヒドリンと反
応させて、陽イオン性熱硬化性樹脂水溶液を製造
する方法において、
(1) 脂肪族飽和二塩基酸とポリアルキレンポリア
ミンとをモル比1:1.0〜1.2で生成するポリア
ミドポリアミンの25℃における50%水溶液の粘
度が300〜1000CPSになるように反応させ
(2) ついで上記ポリアミドポリアミンとその二級
アミノ基に対して1.8〜3.0当量のエピクロルヒ
ドリンとを30〜45℃で30〜120分反応させ、つ
いで25℃における生成物の30%水溶液の粘度が
50〜200CPSになるように50〜90℃で反応させ、
(3) 反応生成物の25℃におけるPHを3〜5に調整
する
ことを特徴とする固形分濃度が30〜40%である陽
イオン性熱硬化性樹脂水溶液の製造法である。
本発明で使用される脂肪族飽和二塩基酸として
はたとえば、マロン酸,グルタル酸,アジピン
酸,ピメリン酸,スベリン酸,アゼライン酸など
があげられるが、工業的にはアジピン酸が好まし
い。ポリアルキレンポリアミンとしては、たとえ
ば、ジエチレントリアミン,トリエチレンテトラ
ミン,テトラエチレンペンタミン,イミノビスプ
ロピルアミンなどがあげられる。脂肪族飽和二塩
基酸とポリアルキレンポリアミンとはモル比1:
1.0〜1.2で反応させられる。ポリアルキレンポリ
アミンが多すぎるとポリアミドポリアミンの重合
度が上昇し難く、最終製品の性能が不十分であつ
たり、所定の重合度まで到達するまで長時間を要
することがある。逆にポリアルキレンポリアミン
が少なすぎるとポリアミドポリアミンは枝分れの
多い構造を有するようになつてポリアミドポリア
ミンのゲル化が生じたり、最終製品の安定性が悪
くなる傾向がある。
ポリアルキレンポリアミンと脂肪族飽和二塩基
酸との反応は、原料仕込時に発生する反応熱を制
御するために好ましくは水存在下で行われ、外部
より加熱して、原料仕込時に添加した水および反
応で生成してくる水を除きながら昇温して反応を
行なう。反応温度は110〜250℃、好ましくは160
〜200℃である。この反応は生成するポリアミド
ポリアミンの25℃における50%水溶液の粘度が
300CPS以上になるまで続けられる。ポリアミド
ポリアミンの25℃における50%水溶液の粘度が
300CPS以下であると最終製品の湿潤紙力増強効
果が不十分であつたり、また、抄紙工程で使用し
た場合強い発泡を伴い作業上、不利である。
300CPS以上であれば、その粘度は一般に高いほ
ど、最終製品の湿潤紙力増強効果はすぐれてお
り、ろ水性向上剤としての有用性も大きくなるが
1000CPSを越えると最終製品の安定性が悪くなる
ため好ましくない。したがつて、望まれる製品の
用途や性能に応じて25℃における50%水溶液の粘
度を300〜1000CPSの範囲から任意に選択するこ
とができる。ポリアミドポリアミンの粘度が所定
の値に達したら、反応を終了し、ポリアミドポリ
アミンは水で希釈されて、50%水溶液に調製され
る。
次に、このようにして調製されたポリアミドポ
リアミンは水溶液中でエピクロルヒドリンと反応
させられる。この反応に使用するエピクロルヒド
リンの量はポリアミドポリアミン中の二級アミノ
基に対して1.8〜3.0当量、好ましくは1.8〜2.4当
量である。エピクロルヒドリンのモル比が1.8よ
り小さいと最終製品の貯蔵安定性が悪く、エピク
ロルヒドリンのモル比が3.0より大きいと、反応
完了まで長時間を要することがあつたり、最終製
品の性能が低下することがある。ポリアミドポリ
アミンとエピクロルヒドリンとの反応は、通常固
形分濃度30−50%の水溶液中で行われる。この場
合、ポリアミドポリアミン水溶液に30℃でエピク
ロルヒドリンを添加後、比較的低温すなわち30〜
45℃で30〜120分保持して反応をおこなつたのち、
比較的高い反応温度すなわち50−90℃に昇温して
反応を続行する。そして生成物の25℃における30
%水溶液の粘度が50〜200CPSに達するまで反応
を行なう。
反応生成物の30%水溶液の粘度が50CPS以下で
あると最終製品の湿潤紙力増強剤としての性能が
十分でないことがあり、また200CPS以上になる
と最終製品の安定性が悪くなることがある。反応
生成物の粘度が所定の範囲に達したら、反応生成
物を45℃以下、好ましくは40℃以下に冷却しても
し必要ならば固形水分濃度が30〜40%になるよう
に水で希釈する。次いで酸を加えてPHを305に調
整する。その間反応生成物の温度を30〜40℃に保
持するのが好ましい。PHを調整するために使用す
る酸は塩酸,硫酸,リン酸,酢酸などがあげられ
るが、塩酸が好ましい。
本発明の方法によつて得られる陽イオン性熱硬
化性樹脂はすぐれた湿潤紙力増強効果およびろ水
性向上効果を有している。また本樹脂水溶液はす
ぐれた貯蔵安定性を有しているため、たとえば固
形分濃度が30〜40%という高濃度の水溶液であつ
ても長期間安定に保持することができる。
本発明の方法によつて得られる陽イオン性熱硬
化性樹脂は湿潤紙力増強剤として用いられるほ
か、製紙工程で使用されるろ水性向上剤や歩留向
上剤として有用であり、またセルロース材料の耐
水化剤,繊維処理剤,結合剤,凝集剤としても用
いることができる。
以下に実施例を記載して本発明をより具体的に
説明する。
実施例 1
温度計,コンデンサー,撹拌機,窒素導入管を
付した2四つ口丸底フラスコにジエチレントリ
アミン487g(4.74モル),水90g,アジピン酸
683g(4.67モル)を仕込み、撹拌下に外部より
加熱して、水を除きながら昇温して180℃で4時
間反応させたのち、水965gを徐々に加えてポリ
アミドポリアミン水溶液を得た。このポリアミド
ポリアミン水溶液は固形分50.1%,粘度455CPS
(25℃)であつた。別のフラスコに、このポリア
ミドポリアミン水溶液150g(二級アミノ基0.33
モル)と水201gを仕込み、30℃でエピクロルヒ
ドリン60.5g(0.65モル)を加える。昇温して、
40℃で100分保持し、次いで65℃に昇温して、こ
の温度で反応を行ない、反応液の粘度が140CPS
(25℃)に到達したところで冷却し、30℃で塩酸
を加えてPHを4.2に調整した。得られた製品は固
形分32.1%で、このものは50℃で3ケ月以上保存
してもゲル化しなかつた。
実施例 2
実施例1と同様の反応装置にジエチレントリア
ミン487g(4.74モル),水90g,アジピン酸683
g(4.67モル)を仕込み、撹拌下に、外部より加
熱して、水を除きながら昇温し180℃で4時間30
分反応させたのち、水970gを徐々に加えてポリ
アミドポリアミン水溶液を得た。このポリアミド
ポリアミン水溶液は固形分49.8%,粘度519CPS
(25℃)であつた。別のフラスコにこのポリアミ
ドポリアミン水溶液180g(二級アミノ基0.41モ
ル)と水231gを仕込み、30℃でエピクロルヒド
リン68.5g(0.74モル)を添加した。昇温して、
40℃で100分保持したのち65℃に昇温してこの温
度で反応を行ない、反応液の粘度が120CPSに到
達したところで冷却し、塩酸を加えてPHを4.0に
調整した。得られた製品は固形分32.3%でこのも
のは50℃で貯蔵しても3カ月以上ゲル化しなかつ
た。
実施例 3
実施例1と同様の反応装置に、ジエチレントリ
アミン487g(4.74モル),水90g,アジピン酸
683g(4.67モル)を仕込み、撹拌下に、外部よ
り加熱して、水を除きながら昇温し、200℃で2
時間反応させたのち、水970gを徐々に加えてポ
リアミドポリアミン水溶液を得た。このポリアミ
ドポリアミン水溶液は固形分49.8%,粘度
438CPS(25℃)であつた。別のフラスコにこのポ
リアミドポリアミン水溶液150g(二級アミノ基
0.33モル)と水188gを仕込み、30℃でエピクロ
ルヒドリン55.0g(0.60モル)を添加した。昇温
して40℃で100分保持したのち、65℃に昇温して、
この温度で反応を行ない、反応液の粘度が
144CPSに到達したところで、冷却し、30℃で塩
酸を加えてPHを4.2に調整した。得られた製品は
固形分32.6%でこのものは50℃で貯蔵しても3ケ
月以上ゲル化しなかつた。
実施例 4
実施例1と同様の反応装置にジエチレントリア
ミン482g(4.67モル),水92g,アジピン酸683
g(4.67モル)を仕込み、撹拌下に、外部より加
熱して、水を除きながら昇温し、180℃で5時間
反応させたのち水975gを加えてポリアミドポリ
アミン水溶液を得た。このポリアミドポリアミン
水溶液は固形分50.2%,粘度806CPS(25℃)であ
つた。別のフラスコに、このポリアミドポリアミ
ン水溶液150g(二級アミノ基0.32モル)と水222
g仕込み、撹拌下に、30℃でエピクロルヒドリン
71g(0.77モル)を添加した。昇温して40℃で
100分保持したのち、70℃に昇温して、この温度
で反応液の粘度が131CPSに到達するまで反応を
行なつたのち、30℃まで冷却し、塩酸を加えてPH
を4.0に調整した。得られた製品は固形分32.1%
でこのものは50℃で貯蔵しても3ケ月以上ゲル化
しなかつた。
実施例 5
実施例1と同様の反応装置にジエチレントリア
ミン491g(4.76モル),水111g,アジピン酸683
g(4.67モル)を仕込み、撹拌下に、外部より加
熱して、水を除きながら昇温し、180℃で1時間
反応させたのち、水990gを加えてポリアミドポ
リアミン水溶液得た。このポリアミドポリアミン
水溶液は固形分50.0%,粘度350CPS(25℃)であ
つた。別のフラスコにこのポリアミドポリアミン
水溶液150g(二級アミノ基0.35モル)と水109g
を仕込み、撹拌下に、30℃でエピクロルヒドリン
58.3g(0.63モル)を添加した。昇温して40℃で
60分保持したのち、65℃に昇温して、この温度で
反応液の粘度が238CPSに到達するまでの反応を
行なつたのち、冷却して30℃とし、塩酸を加えて
PH4.0に調整した。得られた製品は固形分40.3%
であつて、50℃に貯蔵しても3ケ月以上ゲル化し
なかつた。
比較例 1
実施例1において、塩酸の添加量を少くして、
PH5.6に調整した。得られた製品は固形分は33.0
%であつたが、このものは50℃で貯蔵すると43日
でゲル化した。
比較例 2
実施例2で得られたポリアミドポリアミン水溶
液(固形分49.8%),粘度519CPS)180g(二級
アミノ基0.41モル)と水231gを仕込み、30℃で
エピクロルヒドリン68.5g(0.74モル)を添加し
たのち、65℃に昇温して、この温度で反応液の粘
度が120CPSになるまで反応をおこなつて、30℃
に冷却して塩酸を添加しPHを4.0に調整した。こ
の製品は固形分31.9%であつたが、このものを50
℃に貯蔵すると、30日でゲル化した。
比較例 3
実施例3で得たポリアミドポリアミン水溶液
(固形分49.8%,粘度438CPS)150g(二級アミ
ノ基0.33モル)と水175gとを仕込み、30℃でエ
ピクロルヒドリン48.9g(0.53モル)を添加した
のち、昇温して、40℃で100分保持したのち、65
℃に昇温して、この温度で反応物の粘度が
142CPSになるまで反応をおこなつたのち、30℃
に冷却して、塩酸を添加してPH4.2に調整した。
得られた製品は固形分32.7%であつて、このもの
を50℃に貯蔵したところ、30日でゲル化した。
比較例 4
実施例4と同じ反応をおこなつたが、ポリアミ
ドポリアミン水溶液とエピクロルヒドリンとの反
応において、65℃で反応物の粘度が30CPSになつ
たところで反応を中止してPHを4.0に調整した。
得られた製品は固形分32.4%であり、このものを
50℃で貯蔵したところ、3ケ月以上ゲル化しなか
つた。
比較例 5
実施例4で得られたポリアミドポリアミン水溶
液(固形分50.2%,粘度806CPS)150g(二級ア
ミノ基0.32モル)と水270gとを仕込み、30℃で
エピクロルヒドリン94.8g(1.02モル)を添加し
たのち、昇温して40℃で100分保持し、次いで65
℃に昇温し、反応物の粘度が129CPSになるまで
反応をおこなつて、30℃に冷却し、塩酸を加えて
PH4.0に調整した。得られた製品は固形分30.9%
であつて、このものを50℃に貯蔵したが3ケ月以
上ゲル化しなかつた。
比較例 6
実施例1と同様の装置に、ジエチレントリアミ
ン491g(4.76モル),水90g,アジピン酸683g
(4.67g)を仕込み、撹拌下に外部より加熱して、
水を除きながら昇温して、180℃で4時間反応さ
せたのち、水980gを加えてポリアミドポリアミ
ン水溶液を得た。このポリアミドポリアミン水溶
液は固形分50.2%,粘度250CPS(25℃)であつ
た。別のフラスコに、このポリアミドポリアミン
水溶液150g(二級アミノ基,0.35モル)と水197
gを仕込み、30℃でエピクロルヒドリン58.3g
(0.63モル)を添加したのち、40℃に昇温して100
分保持し、次いで65℃に昇温して、この温度で反
応液の粘度が126CPSに到達するまで反応を行な
つたのち、30℃に冷却して塩酸を添加してPH4.3
に調整した。得られた製品は固形分32.4%であつ
たが、このものは50℃で貯蔵したところ、3ケ月
以上ゲル化しなかつた。
参考例 1
実施例1〜5および比較例4〜6で得たそれぞ
れの樹脂の紙力増強効果を調べた。抄紙および紙
力測定条件は次のとおりである。
(1) 試料パルプ NBKP,フリーネス370ml
(2) 樹脂添加率 0.3%/パルプ
(3) 硫酸バンド添加率 0.01%/パルプ
(4) 平均メートル坪量 120g/m2
(5) 抄紙機 角型シートマシン(紙葉寸法25cm×
25cm)
(6) 前処理条件 (20℃,湿度65%)×24時間
(7) 熱処理条件 105℃×10分
The present invention relates to a method for producing an aqueous cationic thermosetting resin solution with good storage stability. Conventionally, polyamide polyamine-epichlorohydrin resins useful as wet paper strength agents have been disclosed, for example, in Japanese Patent Publication No. 3547-3547 and Japanese Patent Application Laid-open No. 1983-3547.
It is known that it can be produced by the method of No. 159496. However, the polyamide polyamine/epichlorohydrin resins obtained by these conventionally known methods are not necessarily satisfactory in terms of storage stability, wet paper strength enhancing effect, and freeness improving effect. The inventors of the present invention have made intensive studies in view of the drawbacks of the resins produced by the above-mentioned known methods, and have found that by specifying the reaction conditions for producing polyamide polyamine/epichlorohydrin resin, it has an excellent wet paper strength enhancing effect. We succeeded in obtaining a resin with high storage stability. That is, the present invention synthesizes a polyamide polyamine by heating and condensing an aliphatic saturated dibasic acid and a polyalkylene polyamine, and then reacts this polyamide polyamine with epichlorohydrin in an aqueous solution to form a cationic thermosetting resin aqueous solution. In the manufacturing method, (1) aliphatic saturated dibasic acid and polyalkylene polyamine are reacted in a molar ratio of 1:1.0 to 1.2 such that a 50% aqueous solution of polyamide polyamine at 25°C has a viscosity of 300 to 1000 CPS. (2) Next, the above polyamide polyamine and 1.8 to 3.0 equivalents of epichlorohydrin based on its secondary amino group were reacted at 30 to 45°C for 30 to 120 minutes, and then the viscosity of a 30% aqueous solution of the product at 25°C was
A cation with a solid content concentration of 30 to 40%, which is characterized by reacting at 50 to 90°C to give 50 to 200 CPS, and (3) adjusting the PH of the reaction product at 25°C to 3 to 5. This is a method for producing a thermosetting resin aqueous solution. Examples of the aliphatic saturated dibasic acids used in the present invention include malonic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, and industrially preferred is adipic acid. Examples of polyalkylene polyamines include diethylenetriamine, triethylenetetramine, tetraethylenepentamine, and iminobispropylamine. The molar ratio of aliphatic saturated dibasic acid and polyalkylene polyamine is 1:
Can be reacted at 1.0 to 1.2. If there is too much polyalkylene polyamine, it is difficult to increase the degree of polymerization of the polyamide polyamine, and the performance of the final product may be insufficient or it may take a long time to reach a predetermined degree of polymerization. On the other hand, if the amount of polyalkylene polyamine is too small, the polyamide polyamine will have a highly branched structure, resulting in gelation of the polyamide polyamine and a tendency for the stability of the final product to deteriorate. The reaction between the polyalkylene polyamine and the aliphatic saturated dibasic acid is preferably carried out in the presence of water in order to control the reaction heat generated during charging of the raw materials. The reaction is carried out by raising the temperature while removing the water produced. Reaction temperature is 110-250℃, preferably 160℃
~200℃. In this reaction, the viscosity of a 50% aqueous solution of the polyamide polyamine produced at 25℃ is
You can continue until you reach 300 CPS or more. The viscosity of a 50% aqueous solution of polyamide polyamine at 25℃ is
If it is less than 300 CPS, the wet paper strength enhancement effect of the final product may be insufficient, and when used in the papermaking process, strong foaming may occur, which is disadvantageous in terms of work.
Generally speaking, the higher the viscosity is, the greater the wet paper strength enhancement effect of the final product, and the greater its usefulness as a freeness improver.
Exceeding 1000 CPS is not preferable because the stability of the final product deteriorates. Therefore, the viscosity of the 50% aqueous solution at 25° C. can be arbitrarily selected from the range of 300 to 1000 CPS depending on the desired use and performance of the product. When the viscosity of the polyamide polyamine reaches a predetermined value, the reaction is terminated and the polyamide polyamine is diluted with water to prepare a 50% aqueous solution. The polyamide polyamine thus prepared is then reacted with epichlorohydrin in an aqueous solution. The amount of epichlorohydrin used in this reaction is 1.8 to 3.0 equivalents, preferably 1.8 to 2.4 equivalents, based on the secondary amino groups in the polyamide polyamine. If the molar ratio of epichlorohydrin is smaller than 1.8, the storage stability of the final product will be poor, and if the molar ratio of epichlorohydrin is larger than 3.0, it may take a long time to complete the reaction or the performance of the final product may deteriorate. . The reaction between polyamide polyamine and epichlorohydrin is usually carried out in an aqueous solution with a solid content concentration of 30-50%. In this case, after adding epichlorohydrin to a polyamide polyamine aqueous solution at 30℃,
After carrying out the reaction at 45℃ for 30 to 120 minutes,
The reaction is continued at a relatively high reaction temperature, i.e. 50-90°C. and 30 at 25℃ of the product
The reaction is carried out until the viscosity of the aqueous solution reaches 50-200 CPS. If the viscosity of the 30% aqueous solution of the reaction product is less than 50 CPS, the final product may not have sufficient performance as a wet paper strength enhancer, and if it exceeds 200 CPS, the stability of the final product may deteriorate. Once the viscosity of the reaction product reaches a predetermined range, the reaction product is cooled to below 45°C, preferably below 40°C, and if necessary diluted with water to a solid moisture concentration of 30-40%. . Then add acid to adjust the pH to 305. During this period, the temperature of the reaction product is preferably maintained at 30-40°C. Examples of acids used to adjust pH include hydrochloric acid, sulfuric acid, phosphoric acid, and acetic acid, with hydrochloric acid being preferred. The cationic thermosetting resin obtained by the method of the present invention has an excellent effect of increasing wet paper strength and improving water freeness. Furthermore, since the present resin aqueous solution has excellent storage stability, even an aqueous solution with a high solid content concentration of 30 to 40% can be stably maintained for a long period of time. The cationic thermosetting resin obtained by the method of the present invention is useful as a wet paper strength enhancer, as well as a freeness improver and a retention aid used in the paper manufacturing process, and is also useful for cellulose materials. It can also be used as a waterproofing agent, fiber treatment agent, binder, and flocculant. EXAMPLES The present invention will be described in more detail with reference to Examples below. Example 1 487 g (4.74 mol) of diethylenetriamine, 90 g of water, and adipic acid were placed in a 2-4 neck round bottom flask equipped with a thermometer, condenser, stirrer, and nitrogen inlet tube.
683 g (4.67 mol) was charged, heated externally with stirring, heated while removing water, and reacted at 180° C. for 4 hours. Then, 965 g of water was gradually added to obtain an aqueous polyamide polyamine solution. This polyamide polyamine aqueous solution has a solid content of 50.1% and a viscosity of 455CPS.
(25℃). In another flask, put 150 g of this polyamide polyamine aqueous solution (secondary amino group: 0.33
mol) and 201 g of water, and at 30°C add 60.5 g (0.65 mol) of epichlorohydrin. Raise the temperature,
Hold at 40℃ for 100 minutes, then raise the temperature to 65℃, perform the reaction at this temperature, and the viscosity of the reaction liquid is 140CPS.
When the temperature reached (25°C), it was cooled, and at 30°C, hydrochloric acid was added to adjust the pH to 4.2. The obtained product had a solid content of 32.1% and did not gel even when stored at 50°C for more than 3 months. Example 2 In a reactor similar to Example 1, 487 g (4.74 mol) of diethylenetriamine, 90 g of water, and 683 g of adipic acid were added.
g (4.67 mol), heated externally while stirring, heated to 180℃ while removing water, and heated at 180℃ for 4 hours.
After reacting for several minutes, 970 g of water was gradually added to obtain a polyamide polyamine aqueous solution. This polyamide polyamine aqueous solution has a solid content of 49.8% and a viscosity of 519CPS.
(25℃). Another flask was charged with 180 g of this polyamide polyamine aqueous solution (0.41 mol of secondary amino groups) and 231 g of water, and 68.5 g (0.74 mol) of epichlorohydrin was added at 30°C. Raise the temperature,
After being held at 40°C for 100 minutes, the temperature was raised to 65°C and the reaction was carried out at this temperature. When the viscosity of the reaction liquid reached 120 CPS, it was cooled and the pH was adjusted to 4.0 by adding hydrochloric acid. The resulting product had a solid content of 32.3% and did not gel for more than 3 months even when stored at 50°C. Example 3 In a reactor similar to Example 1, 487 g (4.74 mol) of diethylenetriamine, 90 g of water, and adipic acid were added.
683 g (4.67 mol) was charged, heated externally with stirring, heated while removing water, and heated to 200°C for 2 hours.
After reacting for a period of time, 970 g of water was gradually added to obtain a polyamide polyamine aqueous solution. This polyamide polyamine aqueous solution has a solid content of 49.8% and a viscosity of
It was 438CPS (25℃). In another flask, 150 g of this polyamide polyamine aqueous solution (secondary amino group
0.33 mol) and 188 g of water were charged, and 55.0 g (0.60 mol) of epichlorohydrin was added at 30°C. After raising the temperature and holding it at 40℃ for 100 minutes, the temperature was raised to 65℃,
The reaction is carried out at this temperature, and the viscosity of the reaction liquid is
When it reached 144 CPS, it was cooled and hydrochloric acid was added at 30°C to adjust the pH to 4.2. The resulting product had a solid content of 32.6% and did not gel for more than 3 months even when stored at 50°C. Example 4 In a reactor similar to Example 1, 482 g (4.67 mol) of diethylenetriamine, 92 g of water, and 683 g of adipic acid were added.
(4.67 mol) was charged, heated externally under stirring, and raised the temperature while removing water. After reacting at 180° C. for 5 hours, 975 g of water was added to obtain an aqueous polyamide polyamine solution. This polyamide polyamine aqueous solution had a solid content of 50.2% and a viscosity of 806 CPS (25°C). In another flask, add 150 g of this polyamide polyamine aqueous solution (0.32 mol of secondary amino groups) and 222 g of water.
g, add epichlorohydrin at 30°C while stirring.
71 g (0.77 mol) was added. Raise the temperature to 40℃
After holding for 100 minutes, the temperature was raised to 70°C, and the reaction was carried out at this temperature until the viscosity of the reaction solution reached 131 CPS, then cooled to 30°C, and hydrochloric acid was added to PH.
Adjusted to 4.0. The resulting product has a solids content of 32.1%
This product did not gel for more than 3 months even when stored at 50°C. Example 5 In a reactor similar to Example 1, 491 g (4.76 mol) of diethylenetriamine, 111 g of water, and 683 g of adipic acid were added.
(4.67 mol) was charged, heated externally under stirring, and raised the temperature while removing water. After reacting at 180° C. for 1 hour, 990 g of water was added to obtain an aqueous polyamide polyamine solution. This polyamide polyamine aqueous solution had a solid content of 50.0% and a viscosity of 350 CPS (25°C). In another flask, add 150 g of this polyamide polyamine aqueous solution (0.35 mol of secondary amino groups) and 109 g of water.
and epichlorohydrin at 30℃ under stirring.
58.3g (0.63mol) was added. Raise the temperature to 40℃
After holding for 60 minutes, the temperature was raised to 65°C, and the reaction was carried out at this temperature until the viscosity of the reaction liquid reached 238 CPS, then cooled to 30°C, and hydrochloric acid was added.
Adjusted to PH4.0. The resulting product has a solids content of 40.3%
Even when stored at 50°C, it did not gel for more than 3 months. Comparative Example 1 In Example 1, the amount of hydrochloric acid added was reduced,
Adjusted to PH5.6. The resulting product has a solid content of 33.0
%, but this product gelled in 43 days when stored at 50°C. Comparative Example 2 180 g (secondary amino group 0.41 mol) of the polyamide polyamine aqueous solution obtained in Example 2 (solid content 49.8%, viscosity 519 CPS) and 231 g of water were charged, and 68.5 g (0.74 mol) of epichlorohydrin was added at 30°C. After that, the temperature was raised to 65℃, the reaction was carried out at this temperature until the viscosity of the reaction liquid reached 120CPS, and then the temperature was raised to 30℃.
The mixture was cooled to 500 mL and hydrochloric acid was added to adjust the pH to 4.0. This product had a solid content of 31.9%;
When stored at °C, it gelled in 30 days. Comparative Example 3 150 g (secondary amino group 0.33 mol) of the polyamide polyamine aqueous solution obtained in Example 3 (solid content 49.8%, viscosity 438 CPS) and 175 g of water were charged, and 48.9 g (0.53 mol) of epichlorohydrin was added at 30°C. After that, the temperature was raised and held at 40℃ for 100 minutes, and then the temperature was increased to 65℃.
℃, and at this temperature the viscosity of the reactant decreases.
After carrying out the reaction until 142CPS was reached, the temperature was increased to 30°C.
The mixture was cooled to pH 4.2 and hydrochloric acid was added thereto to adjust the pH to 4.2.
The resulting product had a solid content of 32.7% and gelled in 30 days when stored at 50°C. Comparative Example 4 The same reaction as in Example 4 was carried out, but in the reaction between the polyamide polyamine aqueous solution and epichlorohydrin, the reaction was stopped when the viscosity of the reactant reached 30 CPS at 65° C., and the pH was adjusted to 4.0.
The obtained product has a solid content of 32.4%, and this
When stored at 50°C, it did not gel for more than 3 months. Comparative Example 5 150 g (secondary amino group 0.32 mol) of the polyamide polyamine aqueous solution obtained in Example 4 (solid content 50.2%, viscosity 806 CPS) and 270 g of water were charged, and 94.8 g (1.02 mol) of epichlorohydrin was added at 30°C. After that, the temperature was raised and held at 40℃ for 100 minutes, and then heated to 65℃.
The temperature was raised to ℃, the reaction was carried out until the viscosity of the reactant reached 129 CPS, the temperature was cooled to 30℃, and hydrochloric acid was added.
Adjusted to PH4.0. The resulting product has a solids content of 30.9%
Although this product was stored at 50°C, it did not gel for more than 3 months. Comparative Example 6 Into the same apparatus as in Example 1, 491 g (4.76 mol) of diethylenetriamine, 90 g of water, and 683 g of adipic acid were added.
(4.67g) and heated from the outside while stirring.
The temperature was raised while removing water, and the mixture was reacted at 180° C. for 4 hours, and then 980 g of water was added to obtain an aqueous polyamide polyamine solution. This polyamide polyamine aqueous solution had a solid content of 50.2% and a viscosity of 250 CPS (25°C). In another flask, add 150 g of this polyamide polyamine aqueous solution (secondary amino group, 0.35 mol) and 197 g of water.
Prepare 58.3g of epichlorohydrin at 30℃
After adding (0.63 mol), the temperature was raised to 40℃ and 100
The temperature was then raised to 65°C, and the reaction was carried out at this temperature until the viscosity of the reaction solution reached 126 CPS, and then cooled to 30°C and hydrochloric acid was added to make the pH 4.3.
Adjusted to. The resulting product had a solids content of 32.4%, but did not gel for more than 3 months when stored at 50°C. Reference Example 1 The paper strength enhancing effect of each resin obtained in Examples 1 to 5 and Comparative Examples 4 to 6 was investigated. Paper making and paper strength measurement conditions are as follows. (1) Sample pulp NBKP, freeness 370ml (2) Resin addition rate 0.3%/pulp (3) Sulfuric acid band addition rate 0.01%/pulp (4) Average metric basis weight 120g/m 2 (5) Paper machine Square sheet machine (Paper size 25cm x
25cm) (6) Pretreatment conditions (20℃, humidity 65%) x 24 hours (7) Heat treatment conditions 105℃ x 10 minutes
【表】【table】
Claims (1)
ミンとを加熱縮合させてポリアミドポリアミンを
合成し、ついでこのポリアミドポリアミンを水溶
液中でエピクロルヒドリンと反応させて、陽イオ
ン性熱硬化性樹脂水溶液を製造する方法におい
て、 (1) 脂肪族飽和二塩基酸とポリアルキレンポリア
ミンとをモル比1:1.0〜1.2で生成するポリア
ミドポリアミンの25℃における50%水溶液の粘
度が300〜1000cpsになるように反応させ (2) ついで上記ポリアミドポリアミンとその二級
アミノ基に対して1.8〜3.0当量のエピクロルヒ
ドリンとを30〜45℃で30〜120分反応させ、つ
いで25℃における生成物の30%水溶液の粘度が
50〜200cpsになるように50〜90℃で反応させ、 (3) 反応生成物の25℃におけるPHを3〜5に調整
する ことを特徴とする固形分濃度が30〜40%である陽
イオン性熱硬化性樹脂水溶液の製造法。[Claims] 1 A polyamide polyamine is synthesized by heating and condensing an aliphatic saturated dibasic acid and a polyalkylene polyamine, and then this polyamide polyamine is reacted with epichlorohydrin in an aqueous solution to produce a cationic thermosetting resin. In the method for producing an aqueous solution, (1) the viscosity of a 50% aqueous solution at 25°C of a polyamide polyamine produced at a molar ratio of aliphatic saturated dibasic acid and polyalkylene polyamine of 1:1.0 to 1.2 is 300 to 1000 cps. (2) Then, the above polyamide polyamine and 1.8 to 3.0 equivalents of epichlorohydrin to its secondary amino group were reacted at 30 to 45°C for 30 to 120 minutes, and then a 30% aqueous solution of the product at 25°C was reacted. The viscosity
A cation having a solid content concentration of 30 to 40%, which is characterized by reacting at 50 to 90°C to give a reaction rate of 50 to 200 cps, and (3) adjusting the pH of the reaction product at 25°C to 3 to 5. A method for producing a thermosetting resin aqueous solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1436580A JPS56110727A (en) | 1980-02-07 | 1980-02-07 | Preparation of aqueous solution of cationic thermo-setting resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1436580A JPS56110727A (en) | 1980-02-07 | 1980-02-07 | Preparation of aqueous solution of cationic thermo-setting resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56110727A JPS56110727A (en) | 1981-09-02 |
JPS6346092B2 true JPS6346092B2 (en) | 1988-09-13 |
Family
ID=11859023
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1436580A Granted JPS56110727A (en) | 1980-02-07 | 1980-02-07 | Preparation of aqueous solution of cationic thermo-setting resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56110727A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5993728A (en) * | 1982-11-22 | 1984-05-30 | Dick Hercules Kk | Preparation of paper coating resin |
JPS61123633A (en) * | 1984-11-20 | 1986-06-11 | Toho Chem Ind Co Ltd | Production of polyamide polyamine epichlorohydrin resin, and water-resistance agent for coating of coated paper using same |
JPS61152900A (en) * | 1984-12-27 | 1986-07-11 | 荒川化学工業株式会社 | Wet paper strength enhancer |
JP2516748B2 (en) * | 1986-09-12 | 1996-07-24 | 日本ピー・エム・シー株式会社 | Method for producing polyamide polyamine epichlorohydrin resin aqueous solution |
US4853431A (en) * | 1987-12-07 | 1989-08-01 | Georgia-Pacific Resins, Inc. | Method for stabilizing aqueous solutions of cationic thermosetting polyamide-epichlorohydrin resins |
US20110114275A1 (en) * | 2008-07-01 | 2011-05-19 | Akzo Nobel N.V. | Resin precursor |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54159496A (en) * | 1978-06-07 | 1979-12-17 | Sumitomo Chem Co Ltd | Preparation of aqueous solution of cationic thermosetting resin |
-
1980
- 1980-02-07 JP JP1436580A patent/JPS56110727A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54159496A (en) * | 1978-06-07 | 1979-12-17 | Sumitomo Chem Co Ltd | Preparation of aqueous solution of cationic thermosetting resin |
Also Published As
Publication number | Publication date |
---|---|
JPS56110727A (en) | 1981-09-02 |
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