JPS5887105A - Production of synthetic resin emulsion - Google Patents

Production of synthetic resin emulsion

Info

Publication number
JPS5887105A
JPS5887105A JP18643881A JP18643881A JPS5887105A JP S5887105 A JPS5887105 A JP S5887105A JP 18643881 A JP18643881 A JP 18643881A JP 18643881 A JP18643881 A JP 18643881A JP S5887105 A JPS5887105 A JP S5887105A
Authority
JP
Japan
Prior art keywords
emulsion
starch
unsaturated monomer
water
ethylenically unsaturated
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.)
Pending
Application number
JP18643881A
Other languages
Japanese (ja)
Inventor
Masaki Bito
尾藤 昌己
Masahiro Tokuda
徳田 正弘
Kunihiko Kondo
邦彦 近藤
Tadakazu Yamada
忠和 山田
Yasuo Tamura
靖夫 田村
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.)
SUGIYAMA SANGYO KAGAKU KENKYUSHO
Original Assignee
SUGIYAMA SANGYO KAGAKU KENKYUSHO
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 SUGIYAMA SANGYO KAGAKU KENKYUSHO filed Critical SUGIYAMA SANGYO KAGAKU KENKYUSHO
Priority to JP18643881A priority Critical patent/JPS5887105A/en
Publication of JPS5887105A publication Critical patent/JPS5887105A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To produce a soapless soap synthetic resin emulsion excellent in chemical stability, by emulsion-polymerizing a difficultly water-soluble unsaturated monomer in the production of a MW-lowered starch and an ethylenically unsaturated monomer graft-polymerizable therewith. CONSTITUTION:A difficultly water-soluble monomer (e.g., styrene) is emulsion- polymerized in an aqueous medium containing 10-50wt%, based on the total solids of emulsion produced, MW-lowered starch and 0.5-5wt% ethylenically unsaturated monomer graft-copolymerizable with the starch, e.g., (meth)acrylate ester. EFFECT:This emulsion can be maintained at a stable emulsion state in both the strong acid and strong alkaline ranges and form films excellent in waterproofness. USE:Adhesives, sizes, biodegradable films, etc.

Description

【発明の詳細な説明】 本発明V′i新規な合成樹脂エマルジョンの製造法に関
するもので、その目的とするところけ、界面活性剤や石
けん類を全く使用せず、特に化学安定性に優れた工フル
ジョンを安価に提供することにある。
DETAILED DESCRIPTION OF THE INVENTION The present invention V′i relates to a method for producing a novel synthetic resin emulsion, which does not use any surfactants or soaps and has particularly excellent chemical stability. Our aim is to provide engineering fusion products at low prices.

元来、合成樹脂エマルジョンはロジン石けん等のごとき
石けん類や界面活性剤を乳化剤として使用し、さらに必
II’ Ic 応じてポリビニルアルコールやカルボキ
ンメチルセルロース、メチルセルロース等のごとき保護
コロイドを加え、乳化重合を行っている。
Originally, synthetic resin emulsions used soaps such as rosin soap and surfactants as emulsifiers, and if necessary, protective colloids such as polyvinyl alcohol, carboquine methylcellulose, methylcellulose, etc. were added to carry out emulsion polymerization. Is going.

しかるに、近年、エマルジョンの成膜後の物性が重を視
されるようになり、石けん類やが面粘性削等の低分子物
質が存在すると、それらがイミグレー/ヨンを生じ、膜
としての性能を低下させたり、また、吸水性の増加、耐
水性能の低下婚を引き起こす原因となることが問題睨さ
れている。
However, in recent years, emphasis has been placed on the physical properties of emulsions after they are formed, and the presence of low-molecular substances such as soaps and surface viscosity particles can cause immigration and impair the performance of the film. There are concerns that it may cause a decrease in water absorption, an increase in water absorption, and a decrease in water resistance.

擾だ、これらの乳化剤は排水中に混入すると泡立ちの原
因となり、排水処理操作上の障害となる等、aI々の問
題を引き起こす原因にもなっている7、 従来、これらのdK問題を解決する丸めの方法として、
ノープレス本しくはンープフリーエフルジ日ンのH造り
が開発され、安定したエマルジョンを得る研究が行われ
ている。
Unfortunately, when these emulsifiers are mixed into wastewater, they cause foaming, which impedes wastewater treatment operations and causes various other problems.7 Conventionally, these dK problems have been solved. As a rounding method,
The H structure of No-Press, or Nump-Free Efluji, has been developed, and research is being conducted to obtain a stable emulsion.

それらの研宜の多く目、エマルジーン粒子に親水性の官
能基、主としてカルボキシル基を導入し、その塩を形成
させて安定化する方法をとっている。
In many of these studies, hydrophilic functional groups, mainly carboxyl groups, are introduced into Emulgene particles, and a salt thereof is formed to stabilize the particles.

しかしながら、この方法は、化学安定性に欠けるという
欠点を有し、その面での改良が必要とされている。
However, this method has the drawback of lacking chemical stability, and improvements in this respect are needed.

本発明省らは、特に化学安定性に優れたソープレスエマ
ルジョンを得るべく種々研宜′ft朧ねた結果、低分子
化処理Lfc澱粉と、該澱粉とグラフドロ■能な少属の
エチレン性不飽和モノマーとの存在下で、水に難溶な不
飽和モノマーを乳化重合させることにより、極めて化学
安定性に優れたンープレス合成樹脂エマル′)!iンが
生成することを見出し、その知見を基に本発明を光成し
た。
As a result of various efforts to obtain a soapless emulsion with particularly excellent chemical stability, the Ministry of the Invention and others have developed low-molecular LFC starch and a small group of ethylenic impurities that are capable of graphing with the starch. By emulsion polymerizing unsaturated monomers that are poorly soluble in water in the presence of saturated monomers, we have created a no-press synthetic resin emul with extremely excellent chemical stability! It was discovered that i-in is produced, and the present invention was completed based on this knowledge.

すなわち、本発明は、低分子化処理澱粉と、UN扮とグ
ラフト可能なエチレン性不飽和モノマーとの共存下にお
いて、水に*mな不飽和モノマーを乳化重合させるに当
九り、低分子化処理澱粉をエマルジョン中の固形分全量
の10〜50*jt%、澱粉とグラフト6(能なエチレ
ン性不飽和モノマーをエマルジョン中の固形分全量の0
,5〜5重量%含有させることを%徴とするノープレス
合成樹脂エマルジョンの製造法であり、この方法によっ
て親水性の澱粉低分子分解物が乳化剤の役割りを果たす
結果、石けん類や界面活性剤の存在なしに安定したエマ
ルジョンが得られるものでおる。
That is, the present invention emulsion polymerizes an unsaturated monomer in water in the coexistence of a low-molecular-weight treated starch and an ethylenically unsaturated monomer that can be grafted with a UN starch. The treated starch was added in an amount of 10 to 50*jt% of the total solid content in the emulsion, and the starch and the ethylenically unsaturated monomer capable of grafting 6 were added in an amount of 0% to the total solid content in the emulsion.
This is a method for producing a no-press synthetic resin emulsion in which the content is 5 to 5% by weight, and as a result of this method, the hydrophilic starch low-molecular decomposition product plays the role of an emulsifier, and as a result, soaps and surfactants A stable emulsion can be obtained without the presence of.

本発明において使用する低分子化処理澱粉とは、グルコ
ース単位群を有する冷水もしくは熱水に可溶なポリツー
ツカフィト、例えば、馬鈴薯、甘藷、トウモロコシ、小
麦、米、サゴ、タピオカ、ンルガム等のごとき植物源か
ら得られた澱粉(この#粉はその構成するアミロースと
アミルペクチンの1iI11合の如何にかかわらず使用
でさる)を塩酸、硫酸、ギ酸、シュウ酸等のどと?!酸
類や過ヨウ素酸、過硫酸アンモニウム、過塩素はンーダ
、過ホウ酸ソーダ、過酸化水素等のごとき酸化剤δらv
CLα−アミラーゼ吟のごとき酵素等で処理して低分子
化した澱粉を意味する。
The low-molecular-weight treated starch used in the present invention refers to a cold-water or hot-water soluble polysaccharide having a glucose unit group, such as potato, sweet potato, corn, wheat, rice, sago, tapioca, or gum, etc. Starch obtained from plant sources such as (this powder can be used regardless of the ratio of its constituent amylose and amyl pectin) to hydrochloric acid, sulfuric acid, formic acid, oxalic acid, etc. ! Oxidizing agents such as acids, periodic acid, ammonium persulfate, perchlorine, sodium perborate, hydrogen peroxide, etc.
It refers to starch that has been reduced in molecular weight by being treated with an enzyme such as CLα-amylase Gin.

この際、澱粉の代わりにアラビアガム、トラガカントガ
人、グアガム、−一カストビーンガム等のごとき天然よ
り産出するガム員、アルギン、イヌリン尋を使用しても
同様な効果が得られるが、これらの物質は価格が高いの
で経済的に不利となり好ましくない。
In this case, the same effect can be obtained by using naturally occurring gums such as gum arabic, tragacantoga, guar gum, and cast bean gum, algin, and inulin fat instead of starch, but these substances Since the price is high, it is economically disadvantageous and undesirable.

また、低分子化処理した澱粉とグラフト[if能なエチ
レン性不飽和モノマーとしては、低分子化処理澱粉と容
易にグラフトするエチレン性不飽和モノ1−1例えば、
(メタ)アクリル酸、アクリμニトリル、(メタ)アク
リルアミド、(メタ)アクリル酸エステル等があり、こ
れらのうちの1′8iもしくは2′s以上が用いられる
Examples of ethylenically unsaturated monomers that can be grafted onto low-molecular-weight starch include ethylenically unsaturated monomers 1-1 that easily graft with low-molecular-weight starch;
Examples include (meth)acrylic acid, acrinitrile, (meth)acrylamide, and (meth)acrylic acid ester, among which 1'8i or 2's or more is used.

さらに、エマルジョンの主体をなす水に難溶な不飽和モ
ノマーとしては、例えば、スチレン、スチレン誘導体、
ブタジェン、クロロプレン、イソプレン、インブテン、
エチレン、塩化ビニル、塩化ビニリデン、酢酸ビニル等
が多り。これらのうちの1橿もしくは共虚合可能な2種
以上の不飽和モノマーの混合物が使用で色る。
Furthermore, examples of the poorly water-soluble unsaturated monomer that forms the main body of the emulsion include styrene, styrene derivatives,
butadiene, chloroprene, isoprene, imbutene,
Ethylene, vinyl chloride, vinylidene chloride, vinyl acetate, etc. are common. Either one of these or a mixture of two or more unsaturated monomers that can be covalently combined can be used.

また、この水に難溶な不飽和モノマーの1部に(メタ)
アクリル酸、マレイン酸、クロトン酸、イタコン酸、(
メタ)アクリルアぐド、N−メチロールアクリルアミド
、ビニルスルホン酸、エチレンイミン、グリシジルメタ
クリレート等のごとき水に易溶な不飽和上ツマ−を共重
合させたものでも差支えない。
In addition, some of the unsaturated monomers that are poorly soluble in water (meth)
Acrylic acid, maleic acid, crotonic acid, itaconic acid, (
A copolymer of an unsaturated polymer easily soluble in water such as meth)acrylamide, N-methylolacrylamide, vinylsulfonic acid, ethyleneimine, glycidyl methacrylate, etc. may also be used.

本発明方法によって安定したエマルジヨンを得るために
は、低分子化処理した澱粉の添加量と、セれに容易にグ
ラフトスるエチレン性不飽和モノマーの添加量が重要な
意味を有し、Ph定の添加量範囲以下fたは以上ではエ
マルジョンが生成しないか、あるいは粒子が急速に沈澱
してしまい安定なエマルジヨンが得られない。
In order to obtain a stable emulsion by the method of the present invention, the amount of low-molecular starch added and the amount of ethylenically unsaturated monomer that is easily grafted onto the cellulose are important, and the pH constant If the amount added is below or above the range f, no emulsion will be formed, or the particles will rapidly settle, making it impossible to obtain a stable emulsion.

すなわち、これらの好ましい添加鮭範囲は、低分子化処
理した澱粉がエマルジョン中の固形分全量の10〜50
重蓋%となるように、一方、該澱粉とグラフト可能なエ
チレン性不飽和モノマーがエマルジョン中の固形分全量
の0.5〜5重1tXとなるように添加する。
That is, the preferable range of added salmon is such that the low-molecular-weight starch accounts for 10 to 50% of the total solid content in the emulsion.
On the other hand, the amount of the ethylenically unsaturated monomer capable of grafting with the starch is added in an amount of 0.5 to 5 tX of the total solid content in the emulsion.

本発明における最大の特鑓は、低分子化処理澱粉と、該
jI粉とグラフト可能な少量のエチレン性不飽和モノマ
ーが共存する条件下で、水に難溶な不飽和上ツマ−を乳
化重合することであって、これにより澱粉に容易にグラ
フトする少量のエチレン性不飽和モノマーを介して水に
難溶な不飽和上ツマ−が間接的に低分子化処理澱粉に接
収され、それが乳化剤としての作用を果たすことである
The greatest feature of the present invention is the emulsion polymerization of unsaturated monomers that are sparingly soluble in water under conditions in which low-molecular-weight treated starch and a small amount of ethylenically unsaturated monomer that can be grafted with the JI powder coexist. As a result, the unsaturated monomer, which is poorly soluble in water, is indirectly acquired by the low-molecular-weight treated starch through a small amount of ethylenically unsaturated monomer that is easily grafted onto the starch, and it becomes an emulsifier. It is to fulfill the function of

従って、水に難溶な不飽和上ツマ−はその種類の如何を
問わず使用することができる。
Therefore, any type of unsaturated powder that is sparingly soluble in water can be used.

また、低分子化処理澱粉にグラフト可能なエチレン性不
飽和モノマーが第三成分として少菫存在しないと均一で
安定ナエマルジョンeユ寿られナイO このような条件下における水に離溶な不飽和モノマーの
乳化重合法は、従来から公知の方法、例えd1過酸化物
系触媒を用いたラジカル重合、レドックス系触媒による
レドックス反応、光嵐合等が通用でき、これにより安定
ナエマルジ目ンを得ることができる。
In addition, if an ethylenically unsaturated monomer that can be grafted onto low-molecular-weight starch is not present as a third component, the emulsion will remain uniform and stable. Emulsion polymerization of monomers can be carried out by conventionally known methods, such as radical polymerization using a d1 peroxide catalyst, redox reaction using a redox catalyst, and photostorm polymerization, whereby a stable naemulsion can be obtained. Can be done.

本発明によって得られたエマルジョンは水溶性の#粉像
分子分解物に水に離溶なポリマーがグラフト1−でいる
ため、成膜した時に耐水性のおる膜が得られることなら
びに強酸あるいは強アルカリ性でも安定した乳化状態を
保つこと等の特徴があり、乳化剤′5r使用した公知の
方法で得られたエマルジョンに比べて格段の化学安定性
を有する。
Since the emulsion obtained by the present invention has a water-soluble polymer grafted onto the water-soluble # powder image molecule decomposition product, it is possible to obtain a water-resistant film when it is formed, and also to be able to withstand strong acid or strong alkalinity. However, it has the characteristic of maintaining a stable emulsified state, and has much greater chemical stability than emulsions obtained by known methods using emulsifier '5r.

また、使用する低分子化処理澱粉の分解度合をコントロ
ールすることによって任意の粘度のエマルジョンが得ら
れ、それぞれの用途に適したエマルジ17を容易に製造
することができる。
Furthermore, by controlling the degree of decomposition of the low-molecular-weight starch used, an emulsion of any viscosity can be obtained, and emulsions 17 suitable for each use can be easily produced.

さらに、安価な澱粉を1I31雑な誘導体として使用す
ることがないので、ブスト的にも極めて有利なエマルジ
ョンを得ることができる。
Furthermore, since cheap starch is not used as a crude derivative of 1I31, an emulsion that is extremely advantageous in terms of bust can be obtained.

本発明方法により得られたエマルジIa/l′i塗料用
ビヒクルとして、ま喪、紙、木材、無機質材等の接着剤
として、さらに、コート紙、不織布、植毛加工、モール
ディング等におけるバインダーとして使用できるばかり
でなく、サイズ剤、モルタル添加剤、微生物分解性フィ
ルムへの利用等、多方面に使用することができる。
The emulsion Ia/l'i obtained by the method of the present invention can be used as a paint vehicle, as an adhesive for adhesives, paper, wood, inorganic materials, etc., and as a binder for coated paper, nonwoven fabrics, flocking, molding, etc. In addition, it can be used in a variety of ways, including as a sizing agent, mortar additive, and microbially degradable film.

次に本発明の実施例を示す。Next, examples of the present invention will be shown.

実施例1゜ 水190]を皿部に酸処理馬鈴薯澱粉10重に部を溶解
した溶液とアクリル酸エチル1fi部とを反応容器に入
れ、これにスチレンモノマー29重綾部および触媒とし
て30%過酸化水素水Q、6容1部、硫酸第1鉄アンモ
ニウム0.15重区部を加え、攪拌しながら50℃まで
加温し、同温度で6時間反応を続けて均一な乳I蜀液を
得た。
Example 1 A solution prepared by dissolving 10 parts of acid-treated potato starch in a dish of 190 parts of water and 1 part of ethyl acrylate was placed in a reaction vessel, and to this was added 29 parts of styrene monomer and 30% peroxide as a catalyst. Add 1 part of 6 volumes of hydrogen water Q and 0.15 parts of ferrous ammonium sulfate, heat to 50°C with stirring, and continue the reaction at the same temperature for 6 hours to obtain a uniform milk I-shu solution. Ta.

この乳濁液を密栓容器に入れ5℃および40℃の温度下
に半年間放置したが、粒子の沈澱もなく、外観上全く変
化が認められなかった。
This emulsion was placed in a sealed container and left at temperatures of 5° C. and 40° C. for half a year, but no particles were precipitated and no change in appearance was observed.

また、この乳濁液の1部を1規定の塩酸および1規定の
苛性ンーダ水溶液中に滴下したが、粒子の破壊や凝集も
なく、均一に分散した。
Further, when a part of this emulsion was dropped into 1N hydrochloric acid and 1N caustic soda aqueous solution, the particles were uniformly dispersed without breaking or agglomerating.

実施例2゜ 光重合装置(内部照射法)に水190重it部、ワキシ
ーコーンスターチの酵素分解デキストリフ10重1部を
入れ、15分間窒素置換を行い、攪拌しながら冷却装置
付きaoowの水銀ランプで5分間前照射した。
Example 2 190 parts by weight of water and 1 part by weight of 10 parts by weight of enzymatically decomposed waxy cornstarch dextrif were placed in a photopolymerization apparatus (internal irradiation method), and nitrogen substitution was performed for 15 minutes. Pre-irradiated for 5 minutes.

ゝ次いで、これにスチレンモノマーろo、1−itsと
アクリル酸モノマー 2重′s1sを加え、常温下で6
時間照射を続けて1合反応させfC8 このようにして得た乳濁液な密栓容器中に入れ、5℃お
よび40℃の温度下に半年開放[した。
Next, styrene monomer RO, 1-its and acrylic acid monomer 2's 1s were added to this, and the mixture was heated at room temperature.
The emulsion thus obtained was placed in a sealed container and left open for half a year at temperatures of 5°C and 40°C.

その間、外観変化を調べたが、粒子の沈澱や分離等の現
象は全く認められず、均一な乳濁状態を保持していた。
During this time, changes in appearance were examined, but no phenomena such as precipitation or separation of particles were observed, and a uniform emulsion state was maintained.

また、この乳濁液の1部を1規定の塩酸お↓び1規定の
苛性ンーダ水溶液中に滴下したが、粒子の破壊や凝集も
なく、均一に分散した。
Further, when a part of this emulsion was dropped into 1N hydrochloric acid and 1N caustic soda aqueous solution, the particles were uniformly dispersed without breaking or agglomerating.

実施ガム 水190重量部に市販のデキストリン(プラットマン社
製、tJoredux B−i 57 ) 10重書部
を溶解した浴液とアクリロニトリル1m1it部とを反
応容器に入れ、これにスチレンモノマ−29甫猷部およ
び触媒として硝酸總2セリウムアンモニウムI、M O
,4重一部、1規定の硝酸7容童部を加え攪拌12なが
ら30℃で6時間反応を続けて均一な乳濁液を得た。
EXAMPLE A bath solution prepared by dissolving 10 parts of commercially available dextrin (Joredux B-i 57, manufactured by Platman) in 190 parts by weight of gum water and 1 ml of acrylonitrile were placed in a reaction vessel, and 29 parts of styrene monomer was added to the reaction vessel. part and as a catalyst discerium ammonium nitrate I, MO
, 4 parts and 7 parts of 1N nitric acid were added, and the reaction was continued at 30° C. for 6 hours with stirring for 12 hours to obtain a uniform emulsion.

この乳濁液の粒子径を透過型電子崩微鏡で測定したとこ
ろ測定数100個で平均186mμであり、分散粒子の
小さい、なめらかな球゛状を呈していた。
The particle diameter of this emulsion was measured using a transmission electron disintegration microscope, and the average diameter was 186 mμ in 100 measurements, and the emulsion had a smooth spherical shape with small dispersed particles.

ま九、この乳濁液を密栓客器に入れ5℃および40℃の
温度下に半年間放置したが、粒子の沈澱もなく、外観上
全く変化が認められなかった。
(9) This emulsion was placed in a sealed container and left at temperatures of 5°C and 40°C for half a year, but no particles were precipitated and no change in appearance was observed.

さらに、この乳濁液の1部を1規定の塩酸および1規定
の苛性ソーダ水浴液中に滴下したが、粒子の破壊や凝集
もなく、均一に分散した。
Furthermore, when a portion of this emulsion was dropped into a 1N hydrochloric acid and 1N caustic soda water bath, the particles were uniformly dispersed without breaking or agglomerating.

Claims (1)

【特許請求の範囲】[Claims] (1)  低分子化処理澱粉と、該澱粉とグラフト可能
なエチレン性不飽和モノマー古の共をト−においで、水
に難溶な不飽和モノマーを乳化重合させるに当たり、低
分子化処理澱粉をエマルジョン中の同形分全蓋の10〜
50重l−%、/a粉とクラフト可能なエチレン性不飽
和モノマーをエマルジョン中の固形分全一の0.5〜5
市−%へ有させることを特徴とするソープレス合成樹脂
エマルジョンの製造法1゜
(1) When low-molecular-weight treated starch and an ethylenically unsaturated monomer that can be grafted with the starch are combined in a toner to emulsion polymerize an unsaturated monomer that is sparingly soluble in water, the low-molecular-weight treated starch is 10~ of the same shape in the emulsion
50 weight l-%, /a powder and kraftable ethylenically unsaturated monomer in an amount of 0.5 to 5% of the total solid content in the emulsion.
Method for producing a soapless synthetic resin emulsion characterized in that it contains 1%
JP18643881A 1981-11-20 1981-11-20 Production of synthetic resin emulsion Pending JPS5887105A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18643881A JPS5887105A (en) 1981-11-20 1981-11-20 Production of synthetic resin emulsion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18643881A JPS5887105A (en) 1981-11-20 1981-11-20 Production of synthetic resin emulsion

Publications (1)

Publication Number Publication Date
JPS5887105A true JPS5887105A (en) 1983-05-24

Family

ID=16188442

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18643881A Pending JPS5887105A (en) 1981-11-20 1981-11-20 Production of synthetic resin emulsion

Country Status (1)

Country Link
JP (1) JPS5887105A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5026746A (en) * 1989-06-26 1991-06-25 Sequa Chemicals, Inc. Starch based binder composition for non-woven fibers or fabrics
US5147907A (en) * 1989-07-11 1992-09-15 Synthomer Chemie Gmbh Process of producing aqueous polymer dispersions
US5536779A (en) * 1991-10-07 1996-07-16 Basf Aktiengesellschaft Aqueous polymer dispersions
US5705563A (en) * 1991-10-07 1998-01-06 Basf Aktiengesellschaft Aqueous polymer dispersions

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5026746A (en) * 1989-06-26 1991-06-25 Sequa Chemicals, Inc. Starch based binder composition for non-woven fibers or fabrics
US5147907A (en) * 1989-07-11 1992-09-15 Synthomer Chemie Gmbh Process of producing aqueous polymer dispersions
US5536779A (en) * 1991-10-07 1996-07-16 Basf Aktiengesellschaft Aqueous polymer dispersions
US5705563A (en) * 1991-10-07 1998-01-06 Basf Aktiengesellschaft Aqueous polymer dispersions

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