JPH0223563B2 - - Google Patents

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Publication number
JPH0223563B2
JPH0223563B2 JP61145943A JP14594386A JPH0223563B2 JP H0223563 B2 JPH0223563 B2 JP H0223563B2 JP 61145943 A JP61145943 A JP 61145943A JP 14594386 A JP14594386 A JP 14594386A JP H0223563 B2 JPH0223563 B2 JP H0223563B2
Authority
JP
Japan
Prior art keywords
emulsifier
emulsion
group
present
emulsifiers
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
JP61145943A
Other languages
Japanese (ja)
Other versions
JPS6312334A (en
Inventor
Akinobu Ichihara
Hitoshi Niike
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.)
DKS Co Ltd
Original Assignee
Dai Ichi Kogyo 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 Dai Ichi Kogyo Seiyaku Co Ltd filed Critical Dai Ichi Kogyo Seiyaku Co Ltd
Priority to JP61145943A priority Critical patent/JPS6312334A/en
Publication of JPS6312334A publication Critical patent/JPS6312334A/en
Publication of JPH0223563B2 publication Critical patent/JPH0223563B2/ja
Granted legal-status Critical Current

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  • Polyethers (AREA)
  • Polymerisation Methods In General (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Detergent Compositions (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

本発明は乳化重合甚乳化剀に関し、特に゚チレ
ン性䞍飜和単量䜓の氎系乳化重合に甚いる新芏、
か぀有甚な乳化剀に関するものである。 埓来、乳化重合甚乳化剀ずしおは、アルキル硫
酞゚ステル塩、アルキルベンれンスルホン酞塩、
ゞアルキルスルホコハク酞゚ステル塩、ポリオキ
シアルキレンアルキルアリヌル゚ヌテル硫酞
゚ステル塩等のアニオン性界面掻性剀、ポリオキ
シアルキレンアルキルアリヌル゚ヌテル、ポ
リオキシ゚チレンポリオキシプロピレンブロツク
共重合䜓、ポリオキシ゚チレン゜ルビタン脂肪酞
゚ステル等の非むオン性界面掻性剀が、単独ある
いは䜵甚で䜿甚されおいるが、゚マルゞペンの安
定性、たた゚マルゞペンから補造されたフむルム
の性質等は、かならずしも充分に満足し埗るもの
でなく、倚くの解決すべき問題点が残されおい
る。 即ち、゚マルゞペンの重合安定性、埗られた゚
マルゞペンの機械安定性、化孊安定性、凍結融解
安定性、顔料混和性、貯蔵安定性等に問題があ
り、特に、機械安定性に぀いおは、改善すべき問
題点が残されおいる。 さらに、゚マルゞペンからポリマヌフむルムを
䜜成した際、䜿甚した乳化剀が遊離の状態でポリ
マヌフむルムに残るため、フむルムの耐氎性、接
着性が劣る等の問題を生じおいる。 たた、゚マルゞペンを塩析等の手段によ぀お砎
壊しポリマヌを取り出すずき、排氎䞭に倚くの乳
化剀が含有され、河川汚濁の原因ずなるため、乳
化剀の陀去凊理に倚倧の劎力が必芁ずなる。 このような芳点から、埓来の乳化剀の問題点を
解決するため数倚くの䞀般に反応性乳化剀ずいわ
れる新芏乳化剀に関する特蚱が提案されおいる。
䟋えば、アニオン性の反応性乳化剀ずしお、特公
昭46−12472号、特開昭54−144317号、特公昭46
−34894号、特公昭56−29657号、特開昭51−
30285号、特公昭49−46291号等であり、非むオン
性反応性乳化剀ずしお、特開昭56−28208号、特
開昭50−98484号等があり、各皮モノマヌに぀い
おの乳化重合甚乳化剀ずしお詊みられおいるが、
これらの反応性乳化剀は乳化剀ずしお単独䜿甚し
たずきには、゚マルゞペン重合時の安定性が䞍充
分な堎合が倚く、䜿甚に際しおは、埓来の乳化剀
ず䜵甚しなければ重合が円滑に進行しない等、本
来の性胜を充分に発揮できないずころの問題点を
有しおいる。 以䞊のように、皮々の詊みはなされおいるが、
未だ前述の問題点を充分に解決するたでには至぀
おいないのが珟状である。 本発明者は、これら問題点を解消すべく鋭意研
究の結果本発明に到達したものである。即ち、本
発明は、 䞀般匏、 䞀般匏 䜆し、䞊蚘匏䞭は炭玠数〜30のアルキル
基、アルケニル基、アルキルアリヌル基、もしく
はアラルキルアリヌル基、は炭玠数〜のア
ルキレン基、もしくは眮換アルキレン基、は
〜100の敎数であり、は〜200の敎数であり、
はアルカリ金属原子、NH4、アルカノヌルア
ミン残基、たたは氎玠原子である。 で衚わされる化合物の混合物を含有するこずを特
城ずする乳化重合甚乳化剀を提䟛するものであ
る。 前蚘䞀般匏䞭、は炭玠数〜30のアルキル
基、アルケニル基、アルキルアリヌル基、もしく
はアラルキルアリヌル基であり、アルキル基ずし
おは、䟋えば、オクチル、ノニル、デシル、りン
デシル、ドデシル、トリデシル、テトラデシル、
ペンタデシル、ヘキサデシル、ヘプタデシル、オ
クタデシル、ノナデシル、゚むコシル等が挙げら
れる。 アルケニル基ずしおは、䟋えば、オクテニル、
ノネニル、デセニル、りンデセニル、ドデセニ
ル、トリデセニル、テトラデセニル、ペンタデセ
ニル、ヘキサデセニル、ヘプタデセニル、オクタ
デセニル等が挙げられる。 アルキルアリヌル基ずしおは、モノブチルプ
ノヌル、ゞブチルプノヌル、sec.ブチルプノ
ヌル、ゞsec.ブチルプノヌル、tert.ブチルプ
ノヌル、オクチルプノヌル、ノニルプノヌ
ル、ゞノニルプノヌル等が挙げられる。 アラルキルプノヌルずしおは、スチリル化フ
゚ノヌル、ベンゞルプノヌル、クミルプノヌ
ル等のモノ、ゞ、トリの単独あるいは、これらの
混合物等が挙げられ、これらのアルキル基等の混
合物であ぀おもよい。 たた、は炭玠数〜のアルキレン基たたは
眮換アルキレン基であり、䟋えば、゚チレン、プ
ロピレン、ブチレン、む゜ブチレン等であり、そ
れらの単独たたはブロツクあるいはランダムの混
合物であ぀おも良い。 は〜100の敎数、は〜200の敎数であ
り、より奜たしくははたたは〜50、は
〜100の範囲である。 たた、は氎玠原子、もしくはナトリりム、カ
リりム等のアルカリ金属原子、NH4、もしくは、
モノ゚タノヌルアミン、トリ゚タノヌルアミン、
等のアルカノヌルアミン残基であり、これらの混
合物であ぀おも良い。 さらに、本発明の乳化剀は工業的に容易に補造
できるものであり、䟋えば次のようにしお補造す
るこずができる。即ち、ノニルプノヌルたたは
ラりリルアルコヌルを原料ずし、芁すればアルキ
レンオキサむドを付加し、アリルグリシゞル゚ヌ
テルを觊媒存圚䞋のもずで加熱反応し、埗られた
反応組成物に、曎に、アルキレンオキサむドを垞
法にお、付加させる。次に無氎リン酞、オキシ塩
化リン等のリン酞化剀を甚いおリン酞゚ステル化
し、芁すれば塩基性物質で䞭和するこずにより本
発明の乳化剀を埗るこずができる。 本発明の乳化剀を適甚する乳化重合甚のモノマ
ヌずしおは、各皮のものを挙げるこずができる。
䟋えば、アクリル酞、アクリル酞メチル、アクリ
ル酞ブチル、アクリル酞―゚チルヘキシル、メ
タアクリル酞メチル、アクリロニトリル、アクリ
ルアミド、アクリル酞ヒドロキシ゚チル゚ステル
等のアクリル系モノマヌ、スチレン、ゞビニルベ
ンれン等の芳銙族モノマヌ、酢酞ビニル等のビニ
ル゚ステルモノマヌ、塩化ビニル、塩化ビニリデ
ン等のハロゲン含有モノマヌ、ブタゞ゚ン、む゜
プレン、クロロプレン等の共圹ゞオレフむンモノ
マヌ、その他゚チレン、無氎マレむン酞、マレむ
ン酞メチル等がある。本発明の乳化剀はこれらの
モノマヌの皮たたは皮以䞊の乳化重合に䜿甚
できる。 重合開始剀ずしおは、埓来公知のものでよく、
䟋えば、過酞化氎玠、過硫酞カリりム、アゟビス
む゜ブチルニトリル、ベンゞルパヌオキサむド等
が挙げられる。たた、重合促進剀ずしおは亜硫酞
氎玠ナトリりム、硫酞第鉄アンモニりム等が挙
げられる。 本発明の乳化剀は通垞、党モノマヌに察しお
0.1〜20重量、さらに奜たしくは、0.2〜5.0重量
である。 たた、本発明の乳化剀は単独でも良奜な乳化重
合゚マルゞペンが埗られるが、必芁により、他の
乳化剀あるいは保護コロむド剀を䜵甚しおもよ
い。本発明の乳化剀を適甚しお埗られる乳化重合
゚マルゞペンは、䟋えば、接着剀、被芆剀、含浞
補匷剀等ずしお、朚材、金属、玙、垃、その他コ
ンクリヌト等に適甚するこずができる。 以䞋本発明を実斜䟋により、具䜓的に説明す
る。、郚ずあるは重量基準を瀺す。 補造䟋  撹拌機、枩床蚈、還流管を備えた反応容噚にノ
ニルプノヌル220、觊媒ずしおトリ゚チルア
ミン1.5を仕蟌み、぀ぎにアリルグリシゞル゚
ヌテル120を滎䞋し80℃にお時間撹拌反応し
た埌に120℃に加枩し、枛圧にお過剰のアリルグ
リシゞル゚ヌテルを陀去した。 次に、埗られた反応組成物をオヌトクレヌブに
移し、苛性カリりムを觊媒ずしお、圧力1.5Kg
cm2、枩床130℃の条件にお゚チレンオキサむドを
反応組成物に察しおモル、および10モル付加し
た。 次に撹拌機、枩床蚈、還流管を備えた反応容噚
に、䞊蚘の゚チレンオキサむドモル付加䜓を
211、無氎リン酞23を仕蟌み80℃にお時間
リン酞゚ステル化反応を行ない埗られた組成物を
本発明乳化剀ずした。本発明乳化剀
のモノ゚ステル、ゞ゚ステルの混合モル比は55
45であ぀た。 同様の操䜜にお埗られた゚チレンオキサむド10
モル付加䜓のリン酞゚ステル化物を本発明乳化剀
ずした。本発明乳化剀のモノ゚ステ
ル、ゞ゚ステルの混合モル比は6040であ぀た。 補造䟋  撹拌機、枩床蚈、還流管を備えた反応容噚にラ
りリルアルコヌル186、觊媒ずしお䞉フツ化ホ
り玠゚ヌテル錯䜓0.5を仕蟌み、぀ぎにアリル
グリシゞル゚ヌテル130を滎䞋し80℃にお時
間撹拌反応した埌に120℃に加枩し、枛圧にお過
剰のアリルグリシゞル゚ヌテルを陀去した。 次に、埗られた反応組成物をオヌトクレヌブに
移し、苛性カリりムを觊媒ずしお、圧力1.5Kg
cm2、枩床130℃の条件におプロピレンオキサむド
を反応組成物に察しおモル付加した。 次に撹拌機、枩床蚈、還流管を備えた反応容噚
に、䞊蚘のプロピレンオキサむドモル付加䜓を
295、無氎リン酞23を仕蟌み80℃にお時間
リン酞゚ステル化反応を行ない、埗られた組成物
を本発明乳化剀ずした。このモノ゚ステ
ル、ゞ゚ステルの混合モル比は6238であ぀た。 補造䟋  撹拌機、枩床蚈、還流管を備えた反応容噚にゞ
スチレン化プノヌルプロピレンオキサむドモ
ル、゚チレンオキサむドモルブロツク付加䜓
636、觊媒ずしお䞉フツ化ホり玠゚ヌテル錯䜓
を仕蟌み、぀ぎにアリルグリシゞル゚ヌテル
130を適䞋し80℃にお時間撹拌反応した埌に
120℃に加枩し、枛圧にお過剰のアリルグリシゞ
ル゚ヌテルを陀去した。 次に、埗られた反応組成物をオヌトクレヌブに
移し、苛性カリりムを觊媒ずしお、圧力1.5Kg
cm2、枩床130℃の条件にお゚チレンオキサむドを
反応組成物に察しお30モル、および10モル付加し
た。 次に撹拌機、枩床蚈、還流管を備えた反応容噚
に、䞊蚘の゚チレンオキサむド30モル付加䜓を
1035、無氎リン酞30を仕蟌み80℃にお時間
リン酞゚ステル化反応を行ない、埗られた組成物
を本発明乳化剀ずした。このモノ゚ステ
ル、ゞ゚ステルの混合モル比は7525であ぀た。
同様の操䜜にお埗られた゚チレンオキサむド100
モル付加䜓のリン酞゚ステル化物を本発明乳化剀
ずした。このモノ゚ステル、ゞ゚ステルの
混合モル比は8020であ぀た。 補造䟋  撹拌機、枩床蚈、還流管を備えた反応容噚にオ
レむルアルコヌル゚チレンオキサむド50モル付加
䜓2468、觊媒ずしお䞉フツ化ホり玠゚ヌテル錯
䜓を仕蟌み、぀ぎにアリルグリシゞル゚ヌテ
ル130を滎䞋し80℃にお時間撹拌反応した埌
に120℃に加枩し、枛圧にお過剰のアリルグリシ
ゞル゚ヌテルを陀去した。 次に、埗られた反応組成物をオヌトクレヌブに
移し、苛性カリりムを觊媒ずしお、圧力1.5Kg
cm2、枩床130℃の条件にお゚チレンオキサむド40
モル、プロピレンオキサむド40モルを反応組成物
に察しおランダムに付加した。 次に撹拌機、枩床蚈、還流管を備えた反応容噚
に、䞊蚘の゚チレンオキサむド40モル、プロピレ
ンオキサむド40モルランダム付加䜓を655、無
氎リン酞を仕蟌み80℃にお時間リン酞゚ス
テル化反応を行ない、48苛性゜ヌダにお䞭
和し、埗られた組成物を本発明乳化剀ずし
た。このモノ゚ステル、ゞ゚ステルの混合モル比
は5842であ぀た。 補造䟋  撹拌機、枩床蚈、還流管を備えた反応容噚にゞ
sec.ブチルプノヌルプロピレンオキサむド10モ
ル付加䜓786、觊媒ずしお䞉フツ化ホり玠゚ヌ
テル錯䜓を仕蟌み、぀ぎにアリルグリシゞル
゚ヌテル130を滎䞋し80℃にお時間撹拌反応
した埌に120℃に加枩し、枛圧にお過剰のアリル
グリシゞル゚ヌテルを陀去した。次に、埗られた
反応組成物をオヌトクレヌブに移し、苛性カリり
ムを觊媒ずしお、圧力1.5Kgcm2、枩床130℃の条
件にお゚チレンオキサむドを反応組成物に察しお
20モル付加した。 次に撹拌機、枩床蚈、還流管を備えた反応容噚
に、䞊蚘の゚チレンオキサむド20モル付加䜓を
890、無氎リン酞23を仕蟌み80℃にお時間
リン酞゚ステル化反応を行ない、ゞ゚タレヌルア
ミン50にお䞭和しお埗られた組成物を本発明乳
化剀ずした。このモノ゚ステル、ゞ゚ステ
ルの混合モル比は5050であ぀た。 実斜䟋  䞋蚘の乳化重合凊方により、本発明乳化剀
〜を甚いお乳化重合を行ない、埗ら
れた゚マルゞペンおよび、その゚マルゞペンから
埗られたポリマヌフむルムの物性を詊隓した。な
お、比范ずしお、埓来の乳化剀の䟋も䜵せお詊隓
した。その結果を第衚に瀺した。 乳化重合凊方 æ°Ž295、乳化剀郚を溶解し、70℃たで昇枩
する。぀ぎに、モノマヌ20郚ず過硫酞アンモニり
ム0.5郚を加え、先行重合させ、さらに重合が開
始しおから10分埌より時間を芁しお180郚を適
䞋しお重合を行な぀た。その埌、重合枩床にお
時間熟成した埌、冷华し、゚マルゞペンを取り出
し、䟛詊サンプルずした。 ぀ぎに、この䟛詊サンプルをガラス板に塗垃し
お垞枩で24時間也燥、ならびにその也燥塗膜を
110℃、分間熱キナアヌしポリマヌフむルムを
䜜成した。 実斜䟋  æ°Ž295郚、乳化剀ずしお第衚に瀺す各皮䜵甚
乳化剀郚を溶解し、80℃たで昇枩し、モノマヌ
ずしおアクリル酞―ブチルスチレン
の混合モノマヌ20郚ず、過硫酞アンモニりム0.3
郚を加え、先行重合し、重合が開始しおから10分
埌から玄時間を芁しお䞊蚘の混合モノマヌ180
郚を滎䞋しお、その埌時間80℃にお熟成を行぀
た埌、冷华し、゚マルゞペンを取り出し䟛詊サン
プルずした。 さらに、この䟛詊サンプルをガラス板に塗垃し
お、垞枩で24時間也燥、ならびに、その也燥塗膜
を110℃、分間熱キナアヌしお、ポリマヌフむ
ルムを䜜成した。 以䞊のようにしお埗られた゚マルゞペンおよ
び、その゚マルゞペンから埗られたポリマヌフむ
ルムの物性を第衚に瀺した。なお、比范品ずし
お埓来の乳化剀の䟋も䜵せお第衚に瀺した。 実斜䟋  本発明乳化剀、、を、実斜䟋
の乳化重合凊方にお、乳化重合を実斜しお、埗ら
れた゚マルゞペンおよび、その゚マルゞペンから
埗られたポリマヌフむルムの物性を詊隓した。そ
の結果を第衚に瀺した。
The present invention relates to an emulsifier for emulsion polymerization, and in particular to a novel emulsifier for use in aqueous emulsion polymerization of ethylenically unsaturated monomers.
and useful emulsifiers. Conventionally, as emulsifiers for emulsion polymerization, alkyl sulfate salts, alkylbenzene sulfonate salts,
Anionic surfactants such as dialkyl sulfosuccinate salts, polyoxyalkylene alkyl (aryl) ether sulfate salts, polyoxyalkylene alkyl (aryl) ethers, polyoxyethylene polyoxypropylene block copolymers, polyoxyethylene sorbitan fatty acids Nonionic surfactants such as esters are used alone or in combination, but the stability of emulsions and the properties of films produced from emulsions are not always fully satisfactory, and many There are still issues to be resolved. That is, there are problems with the polymerization stability of the emulsion, the mechanical stability, chemical stability, freeze-thaw stability, pigment miscibility, storage stability, etc. of the obtained emulsion, and in particular, the mechanical stability should be improved. Problems remain. Furthermore, when a polymer film is made from an emulsion, the emulsifier used remains in the polymer film in a free state, resulting in problems such as poor water resistance and adhesive properties of the film. Furthermore, when the emulsion is destroyed by means such as salting out to extract the polymer, a large amount of emulsifier is contained in the wastewater, which causes river pollution, and therefore a great deal of effort is required to remove the emulsifier. From this point of view, a number of patents relating to new emulsifiers, generally referred to as reactive emulsifiers, have been proposed in order to solve the problems of conventional emulsifiers.
For example, as an anionic reactive emulsifier,
−34894, JP 56-29657, JP 51-
30285, Japanese Patent Publication No. 49-46291, etc., and as nonionic reactive emulsifiers, there are JP-A No. 56-28208, JP-A No. 50-98484, etc., which were tried as emulsifiers for emulsion polymerization of various monomers. Although it is
When these reactive emulsifiers are used alone as emulsifiers, they often have insufficient stability during emulsion polymerization, and when used in combination with conventional emulsifiers, polymerization may not proceed smoothly, resulting in poor performance. The problem is that it cannot fully demonstrate its capabilities. As mentioned above, various attempts have been made, but
At present, the above-mentioned problems have not yet been fully solved. The present inventor has arrived at the present invention as a result of intensive research to solve these problems. That is, the present invention has the following general formula: general formula [However, in the above formula, R is an alkyl group, alkenyl group, alkylaryl group, or aralkylaryl group having 8 to 30 carbon atoms, A is an alkylene group having 2 to 4 carbon atoms, or a substituted alkylene group, and n is 0
is an integer of ~100, m is an integer of 1 to 200,
M is an alkali metal atom, NH 4 , an alkanolamine residue, or a hydrogen atom. ] It provides an emulsifier for emulsion polymerization characterized by containing a mixture of compounds represented by the following. In the general formula, R is an alkyl group, alkenyl group, alkylaryl group, or aralkylaryl group having 8 to 30 carbon atoms, and examples of the alkyl group include octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, and tetradecyl. ,
Examples include pentadecyl, hexadecyl, heptadecyl, octadecyl, nonadecyl, eicosyl, and the like. Examples of alkenyl groups include octenyl,
Examples include nonenyl, decenyl, undecenyl, dodecenyl, tridecenyl, tetradecenyl, pentadecenyl, hexadecenyl, heptadecenyl, octadecenyl, and the like. Examples of the alkylaryl group include monobutylphenol, dibutylphenol, sec.butylphenol, disec.butylphenol, tert.butylphenol, octylphenol, nonylphenol, dinonylphenol, and the like. Examples of the aralkyl phenol include mono-, di-, and tri-styrylated phenols, benzylphenols, cumylphenols, and the like, or mixtures thereof, and may be mixtures of these alkyl groups. Further, A is an alkylene group or substituted alkylene group having 2 to 4 carbon atoms, such as ethylene, propylene, butylene, isobutylene, etc., and may be a single group or a block or random mixture thereof. n is an integer of 0 to 100, m is an integer of 1 to 200, more preferably n is 0 or 1 to 50, m is 2
~100 range. In addition, M is a hydrogen atom, an alkali metal atom such as sodium or potassium, NH 4 , or
monoethanolamine, triethanolamine,
It is an alkanolamine residue such as, and a mixture thereof may be used. Furthermore, the emulsifier of the present invention can be easily produced industrially, and can be produced, for example, as follows. That is, nonylphenol or lauryl alcohol is used as a raw material, alkylene oxide is added if necessary, allyl glycidyl ether is heated and reacted in the presence of a catalyst, and alkylene oxide is further added to the resulting reaction composition by a conventional method. Add it at . Next, the emulsifier of the present invention can be obtained by phosphoric acid esterification using a phosphorylating agent such as phosphoric anhydride or phosphorus oxychloride, and neutralization with a basic substance if necessary. Various monomers can be mentioned as monomers for emulsion polymerization to which the emulsifier of the present invention is applied.
For example, acrylic monomers such as acrylic acid, methyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, methyl methacrylate, acrylonitrile, acrylamide, acrylic acid hydroxyethyl ester, aromatic monomers such as styrene, divinylbenzene, and acetic acid. Examples include vinyl ester monomers such as vinyl, halogen-containing monomers such as vinyl chloride and vinylidene chloride, conjugated diolefin monomers such as butadiene, isoprene, and chloroprene, and others such as ethylene, maleic anhydride, and methyl maleate. The emulsifier of the present invention can be used for emulsion polymerization of one or more of these monomers. As the polymerization initiator, conventionally known ones may be used.
Examples include hydrogen peroxide, potassium persulfate, azobisisobutylnitrile, and benzyl peroxide. Examples of the polymerization accelerator include sodium hydrogen sulfite and ferrous ammonium sulfate. The emulsifier of the present invention typically has a
It is 0.1 to 20% by weight, more preferably 0.2 to 5.0% by weight. Although a good emulsion polymerization emulsion can be obtained using the emulsifier of the present invention alone, other emulsifiers or protective colloids may be used in combination, if necessary. The emulsion polymerization emulsion obtained by applying the emulsifier of the present invention can be applied to wood, metal, paper, cloth, concrete, etc., as an adhesive, a coating agent, an impregnation reinforcing agent, etc., for example. The present invention will be specifically explained below using examples. [% and parts indicate weight basis. ] Production Example 1 220 g of nonylphenol and 1.5 g of triethylamine as a catalyst were placed in a reaction vessel equipped with a stirrer, a thermometer, and a reflux tube. Next, 120 g of allyl glycidyl ether was added dropwise, and the mixture was reacted with stirring at 80°C for 5 hours. The mixture was heated to 0.degree. C. and excess allyl glycidyl ether was removed under reduced pressure. Next, the obtained reaction composition was transferred to an autoclave, and caustic potassium was used as a catalyst to
2 moles and 10 moles of ethylene oxide were added to the reaction composition under conditions of cm 2 and temperature of 130°C. Next, add 2 moles of the above ethylene oxide adduct to a reaction vessel equipped with a stirrer, thermometer, and reflux tube.
211 g of phosphoric anhydride and 23 g of phosphoric anhydride were charged, and a phosphoric acid esterification reaction was carried out at 80° C. for 5 hours. The resulting composition was designated as the emulsifier [A] of the present invention. Emulsifier of the present invention [A]
The mixing molar ratio of monoester and diester is 55/
It was 45. Ethylene oxide 10 obtained by similar operation
The phosphoric acid esterified product of the molar adduct was used as the emulsifier [B] of the present invention. The mixing molar ratio of monoester and diester in the emulsifier [B] of the present invention was 60/40. Production Example 2 186 g of lauryl alcohol and 0.5 g of boron trifluoride ether complex as a catalyst were placed in a reaction vessel equipped with a stirrer, a thermometer, and a reflux tube, and then 130 g of allyl glycidyl ether was added dropwise and stirred at 80°C for 5 hours. After the reaction, the mixture was heated to 120°C and excess allyl glycidyl ether was removed under reduced pressure. Next, the obtained reaction composition was transferred to an autoclave, and caustic potassium was used as a catalyst to
5 mol of propylene oxide was added to the reaction composition under conditions of cm 2 and temperature of 130°C. Next, add 5 moles of the above propylene oxide adduct to a reaction vessel equipped with a stirrer, thermometer, and reflux tube.
295 g and 23 g of phosphoric anhydride were charged and a phosphoric acid esterification reaction was carried out at 80° C. for 5 hours, and the obtained composition was designated as the emulsifier [C] of the present invention. The mixing molar ratio of monoester and diester was 62/38. Production Example 3 In a reaction vessel equipped with a stirrer, a thermometer, and a reflux tube, 2 moles of distyrenated phenol propylene oxide and 5 moles of ethylene oxide block adduct were added.
636g, 2g of boron trifluoride ether complex as a catalyst, then allyl glycidyl ether
After dropping 130g and reacting with stirring at 80℃ for 5 hours,
The mixture was heated to 120°C and excess allyl glycidyl ether was removed under reduced pressure. Next, the obtained reaction composition was transferred to an autoclave, and caustic potassium was used as a catalyst to
30 moles and 10 moles of ethylene oxide were added to the reaction composition under conditions of cm 2 and temperature of 130°C. Next, add 30 moles of the above ethylene oxide adduct to a reaction vessel equipped with a stirrer, thermometer, and reflux tube.
1,035 g of phosphoric acid anhydride and 30 g of phosphoric anhydride were charged, and a phosphoric acid esterification reaction was carried out at 80° C. for 5 hours, and the obtained composition was designated as the emulsifier [D] of the present invention. The mixing molar ratio of monoester and diester was 75/25.
Ethylene oxide 100 obtained by similar operation
The phosphoric acid esterified product of the molar adduct was designated as the emulsifier [E] of the present invention. The mixing molar ratio of monoester and diester was 80/20. Production Example 4 Into a reaction vessel equipped with a stirrer, a thermometer, and a reflux tube, 2468 g of oleyl alcohol ethylene oxide 50 mole adduct and 5 g of boron trifluoride ether complex as a catalyst were charged, and then 130 g of allyl glycidyl ether was added dropwise at 80°C. After stirring for 5 hours, the mixture was heated to 120°C, and excess allyl glycidyl ether was removed under reduced pressure. Next, the obtained reaction composition was transferred to an autoclave, and caustic potassium was used as a catalyst to
cm 2 and ethylene oxide 40 at a temperature of 130°C.
40 moles of propylene oxide were randomly added to the reaction composition. Next, in a reaction vessel equipped with a stirrer, a thermometer, and a reflux tube, 40 moles of ethylene oxide, 655 g of the random adduct of 40 moles of propylene oxide, and 5 g of phosphoric anhydride were charged, and phosphoric acid esterification was carried out at 80°C for 5 hours. The reaction was carried out and neutralized with 8 g of 48% caustic soda, and the resulting composition was designated as the emulsifier [F] of the present invention. The mixing molar ratio of the monoester and diester was 58/42. Production Example 5 A reaction vessel equipped with a stirrer, a thermometer, and a reflux tube was
sec. 786 g of a 10 mole adduct of butylphenol propylene oxide and 4 g of boron trifluoride ether complex as a catalyst were charged, and then 130 g of allyl glycidyl ether was added dropwise and reacted with stirring at 80°C for 5 hours, followed by heating to 120°C. Excess allyl glycidyl ether was removed under reduced pressure. Next, the obtained reaction composition was transferred to an autoclave, and ethylene oxide was applied to the reaction composition using caustic potassium as a catalyst at a pressure of 1.5 Kg/cm 2 and a temperature of 130°C.
Added 20 moles. Next, add 20 moles of the above ethylene oxide adduct to a reaction vessel equipped with a stirrer, thermometer, and reflux tube.
890 g and 23 g of phosphoric anhydride were charged, a phosphoric acid esterification reaction was carried out at 80° C. for 5 hours, and the resulting composition was neutralized with 50 g of dietaleramine, and the resulting composition was designated as the emulsifier [G] of the present invention. The mixing molar ratio of monoester and diester was 50/50. Example 1 Emulsion polymerization was carried out using the emulsifiers [A] to [E] of the present invention according to the following emulsion polymerization recipe, and the physical properties of the obtained emulsion and the polymer film obtained from the emulsion were tested. For comparison, examples of conventional emulsifiers were also tested. The results are shown in Table 1. [Emulsion polymerization recipe] Dissolve 295 g of water and 5 parts of emulsifier, and raise the temperature to 70°C. Next, 20 parts of monomer and 0.5 part of ammonium persulfate were added for preliminary polymerization, and 180 parts were added over a period of 3 hours starting 10 minutes after the start of polymerization to carry out polymerization. Then, at the polymerization temperature, 1
After aging for a time, it was cooled and the emulsion was taken out and used as a test sample. Next, this test sample was applied to a glass plate and dried for 24 hours at room temperature, and the dried coating film was
A polymer film was prepared by heat curing at 110°C for 3 minutes. Example 2 295 parts of water and 5 parts of various combination emulsifiers shown in Table 2 as emulsifiers were dissolved, heated to 80°C, and n-butyl acrylate/styrene = 7/3 as monomers.
20 parts of mixed monomers and 0.3 parts of ammonium persulfate
The above mixed monomer 180
After that, the emulsion was aged at 80° C. for 1 hour, cooled, and the emulsion was taken out and used as a test sample. Further, this test sample was applied to a glass plate, dried at room temperature for 24 hours, and the dried coating film was heat cured at 110° C. for 3 minutes to prepare a polymer film. Table 2 shows the physical properties of the emulsion obtained as described above and the polymer film obtained from the emulsion. In addition, examples of conventional emulsifiers are also shown in Table 2 as comparative products. Example 3 The emulsifiers [A], [F], and [G] of the present invention were prepared in Example 1.
Emulsion polymerization was carried out using the following emulsion polymerization formulation, and the physical properties of the resulting emulsion and the polymer film obtained from the emulsion were tested. The results are shown in Table 3.

【衚】【table】

【衚】【table】

【衚】【table】

【衚】【table】

Claims (1)

【特蚱請求の範囲】  䞀般匏、 䞀般匏、 䜆し、䞊蚘匏䞭は炭玠数〜30のアルキル
基、アルケニル基、アルキルアリヌル基、もしく
はアラルキルアリヌル基、は炭玠数〜のア
ルキレン基、もしくは眮換アルキレン基、は
〜100の敎数であり、は〜200の敎数であり、
はアルカリ金属原子、NH4、アルカノヌルア
ミン残基、たたは氎玠原子である。 で衚わされる化合物の混合物を含有するこずを特
城ずする乳化重合甚乳化剀。
[Claims] 1 General formula, general formula, [However, in the above formula, R is an alkyl group, alkenyl group, alkylaryl group, or aralkylaryl group having 8 to 30 carbon atoms, A is an alkylene group having 2 to 4 carbon atoms, or a substituted alkylene group, and n is 0
is an integer of ~100, m is an integer of 1 to 200,
M is an alkali metal atom, NH 4 , an alkanolamine residue, or a hydrogen atom. ] An emulsifier for emulsion polymerization characterized by containing a mixture of compounds represented by the following.
JP61145943A 1986-06-20 1986-06-20 Emulsifying agent for aqueous resin dispersion Granted JPS6312334A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61145943A JPS6312334A (en) 1986-06-20 1986-06-20 Emulsifying agent for aqueous resin dispersion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61145943A JPS6312334A (en) 1986-06-20 1986-06-20 Emulsifying agent for aqueous resin dispersion

Publications (2)

Publication Number Publication Date
JPS6312334A JPS6312334A (en) 1988-01-19
JPH0223563B2 true JPH0223563B2 (en) 1990-05-24

Family

ID=15396629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61145943A Granted JPS6312334A (en) 1986-06-20 1986-06-20 Emulsifying agent for aqueous resin dispersion

Country Status (1)

Country Link
JP (1) JPS6312334A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022054640A1 (en) 2020-09-08 2022-03-17 凞版印刷株匏䌚瀟 Organic conductive film manufacturing method, organic conductive film, and laminate

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1330134C (en) * 1988-08-09 1994-06-07 Kenji Yamamoto Finely divided gelled polymer and process for producing the same
GB0101771D0 (en) 2001-01-24 2001-03-07 Ici Plc Anionic surfactants
CN104011088A (en) * 2011-12-20 2014-08-27 第䞀工䞚制药株匏䌚瀟 Emulsifying agent for emulsion polymerization, and emulsion polymerization method using same
JP7680868B2 (en) * 2020-04-10 2025-05-21 東邊化孊工業株匏䌚瀟 Emulsifier for emulsion polymerization and method for producing emulsion polymerization latex

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022054640A1 (en) 2020-09-08 2022-03-17 凞版印刷株匏䌚瀟 Organic conductive film manufacturing method, organic conductive film, and laminate

Also Published As

Publication number Publication date
JPS6312334A (en) 1988-01-19

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