JPS5996103A - Method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency - Google Patents
Method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparencyInfo
- Publication number
- JPS5996103A JPS5996103A JP20458782A JP20458782A JPS5996103A JP S5996103 A JPS5996103 A JP S5996103A JP 20458782 A JP20458782 A JP 20458782A JP 20458782 A JP20458782 A JP 20458782A JP S5996103 A JPS5996103 A JP S5996103A
- Authority
- JP
- Japan
- Prior art keywords
- galactomannan
- water
- reaction
- aqueous solution
- organic solvent
- 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
Links
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、その水溶液が透明性に優れたガラクトマンナ
ンのヒドロキシアルキルエーテルの製法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency.
ガラクトマンナンはマンノースを構成単位とする主鎖に
ガラクトース単位が側鎖として構成される中性多糖類で
あって、主として豆科植物の(IF子に多く含r1され
ており、特にグア豆を原料とするクツ′カ人及びローカ
ストビーンを原料とするローカストビーンガλが代表的
なガラクトマンナンを主成分とする植物ガム質である。Galactomannan is a neutral polysaccharide composed of a main chain consisting of mannose as a constituent unit and galactose units as side chains. Locust bean λ made from locust bean and locust bean are representative vegetable gums containing galactomannan as a main component.
これらの植物ガム質は植物粘質物であって、水に溶解し
て極めて高い粘性を示すことから、食品分野及び工業分
野に広く利用されている8しかしながら、ガラクトマン
ナンは水溶液にしようとするとき「ママコ」と呼ばれる
粉体粒子の団粒化を起こし易く、またガラクトマンナン
の水溶液はバクテリアの攻撃を受けやすく、経時的に腐
敗して粘度低下を起こし、かつ水溶液が白濁するという
欠点がある。These plant gums are plant mucilage substances that exhibit extremely high viscosity when dissolved in water, so they are widely used in the food and industrial fields8. However, when galactomannan is made into an aqueous solution, Galactomannan aqueous solutions are easily attacked by bacteria, deteriorate over time and cause a decrease in viscosity, and the aqueous solution becomes cloudy.
従来ガラクトマンナンのヒドロキシアルキルエーテルの
製造、法としては、ガラクトマンナンをアルカリの存在
下に水を媒体としてグリセリンモノハロヒドリンと反応
させる方法が知られている(米国特許2496670号
明細書参照)。Conventionally, as a method for producing a hydroxyalkyl ether of galactomannan, a method is known in which galactomannan is reacted with glycerin monohalohydrin in the presence of an alkali and using water as a medium (see US Pat. No. 2,496,670).
しかし本発明者らの追試によれば、この方法には下記の
欠点が存在することが認められた。まず第一に、得られ
た製品を水溶液にしたときにガラクトマンナンよりは若
干透明性が良好とフヨろものの、優良な透明性を得るこ
とができない。However, according to additional tests conducted by the present inventors, it was found that this method has the following drawbacks. First of all, when the resulting product is made into an aqueous solution, although it has slightly better transparency than galactomannan, excellent transparency cannot be obtained.
第二に反応は水を媒体としているからガラクトマンナン
及び反応生成物は水中に溶解し、極めじ、また攪拌、輸
送、乾燥等の工程管理かほめて困難で・ある。Second, since the reaction uses water as a medium, galactomannan and the reaction product are dissolved in water, making it extremely difficult to control the process, such as stirring, transportation, and drying.
また米国特許3 ’32689 [1号明細書には、ア
ルカリ試薬として有機アミンと第4級有機アンモニウム
ヒドロキシドを用い、il l蜀法によりガラクトマン
ナンのヒドロキシアルキルエーテルを製造する方法が記
載されている。しかしこの方法は、アルキレンオキサイ
ドと・/jラクトマンナンの反応速度が遅く、通常6〜
8時間程度の反応時間ではガラクトマンナンへのアルキ
レンオキサイドの有効利用率示40%以下と低く経済性
に問題−がある。また製品の変性度の目安となるMS(
アンヒドロ糖単位当り付加したアルキレンオキサイドの
モル数)も0.1i下と不充分であり製品として不満足
である。更に反応後、未反応エーテル化試薬が多量残留
すること等の欠点がある。Further, US Pat. No. 3'32689 [1] describes a method for producing a hydroxyalkyl ether of galactomannan by the IL-Shu method using an organic amine and a quaternary organic ammonium hydroxide as an alkaline reagent. . However, this method has a slow reaction rate between alkylene oxide and /j lactomannan, and usually
When the reaction time is about 8 hours, the effective utilization rate of alkylene oxide to galactomannan is as low as 40% or less, which poses a problem in terms of economic efficiency. In addition, MS (
The number of moles of alkylene oxide added per anhydrosaccharide unit was less than 0.1i, which was insufficient and the product was unsatisfactory. Furthermore, there is a drawback that a large amount of unreacted etherification reagent remains after the reaction.
本発明者らはこのような実情に鑑み、その水溶液が優良
な透明性を具備したガラクトマンナンのヒドロへンアル
キルエーテルを得るため鋭Q、 fiJf究を重、!、
1/こ結果、本発明に到達した。In view of these circumstances, the present inventors have conducted extensive research to obtain a hydrohen alkyl ether of galactomannan whose aqueous solution has excellent transparency! ,
1/ As a result, the present invention has been achieved.
本発明は、ガラクトマンナンを、ガラクトマンナンのア
ンヒドロ糖単位当たり0.−4モル以上のアルカリ金(
、i:水酸化物の存在下に、親水性有機溶剤及び水を媒
体として、アルキレンオキサイドと反応させる゛ことを
特徴とする、水溶液が透明性に優れたガラクトマンナン
のヒドロキシアルキルエーテルの製法である。The present invention provides galactomannan with 0.0% per anhydrosaccharide unit of galactomannan. -4 moles or more of alkali gold (
, i: A method for producing a hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency, which is characterized by reacting it with an alkylene oxide in the presence of a hydroxide in a hydrophilic organic solvent and water as a medium. .
本発明は全ての反応をガラクトマンナンが媒体中に懸濁
分散した状態で進行させる点に、大きな特色を有する。The present invention has a major feature in that all reactions proceed with galactomannan being suspended and dispersed in the medium.
このため反応終了後の中相、洗浄、精製等の操作を容易
にし、かつ運転保守等を容易にすることができる。Therefore, operations such as intermediate phase, washing, and purification after completion of the reaction can be facilitated, and operation and maintenance can be facilitated.
本発明によって得られる水溶液の透明性に優れたガラク
トマンナンのヒドロキシアルキルエーテルは、ガラクト
マンナンが本来具備している非イオン性を損なうことな
くバクテリアによる水溶液の経時粘度変化を減少させ、
pH12以下の液性で水溶液粘度が安定であり、かつ多
価イオンを含む各種塩類の高濃度の存在下でも高い水溶
液粘度を維持できるという特性を有する。The hydroxyalkyl ether of galactomannan, which has excellent transparency in an aqueous solution obtained by the present invention, reduces the viscosity change over time of an aqueous solution caused by bacteria without impairing the nonionic properties inherent in galactomannan.
The viscosity of the aqueous solution is stable at a pH of 12 or less, and the viscosity of the aqueous solution can be maintained at a high level even in the presence of high concentrations of various salts containing multivalent ions.
ガラクトマンナンとしては、グアガム、ローカストビー
ンガム等のガラクトマンナンを主成分とする物質及びこ
れらの原料であるグア豆、ローカストビーン等を用いる
こともで・きる。As the galactomannan, substances containing galactomannan as a main component such as guar gum and locust bean gum, and their raw materials such as guar beans and locust beans can also be used.
ガラクトマンナン今彩≠とじては、豆類を粗砕したいわ
ゆるスプリット状のもの、ある(・は細か(粉砕した粉
状のものを用いることができる。また粉状のガラクトマ
ンナンをエーテル、アルコール、ベンゼン等で精製した
ものも用いられる。更に熱分解、酸化分解、酵素分解、
酸加水分解等の操作を行って分子量を低下させたガラク
トマンナンも使用できる。Galactomannan Imaya ≠ Toji is a so-called split type made by coarsely crushing legumes, and finely crushed (pulverized powder) can also be used. Also used are products purified by methods such as thermal decomposition, oxidative decomposition, enzymatic decomposition,
Galactomannan whose molecular weight has been lowered by performing operations such as acid hydrolysis can also be used.
親水性有機溶剤とは、少なくとも水を60重量%含有し
た状態で水と分離しな(・有機溶剤を意味し、ガラクト
マンナン、アルカリ金属水酸化物及びアルキレンオキサ
イドのいずれとも反応しにくい・1.の゛(パあること
が好ましい。代表的な親水(41fl i(、Q Yi
’;剤としては、メタノール、エタノール、プ「コバノ
ール、ブタノール等のアルコール類、アセトン、メチル
エチルケトン等のケトン類及びそれらの混合物、好まし
くは2−プロパ/−ル、ターシャリ−ブタノール、アセ
トン、メチルエチルケトン等が挙げられる。Hydrophilic organic solvent refers to an organic solvent that contains at least 60% by weight of water and does not separate from water (-means an organic solvent that does not easily react with galactomannan, alkali metal hydroxides, or alkylene oxides).1. It is preferable that there is a typical hydrophilicity (41fl i(, Q Yi
Examples of the agent include alcohols such as methanol, ethanol, propanol and butanol, ketones such as acetone and methyl ethyl ketone, and mixtures thereof, preferably 2-propanol, tert-butanol, acetone, methyl ethyl ketone, etc. Can be mentioned.
反応媒体としての親水性有機溶剤と水との比率は、重量
比で30 ニア0ないし95:5の範囲が好ましい。。The ratio of the hydrophilic organic solvent as the reaction medium to water is preferably in the range of 30:0 to 95:5 by weight. .
反応媒体中の水の比率が5重量%よりも減少すると、ガ
ラクトマンナンのヒドロキシアル遵ル化の反応速度が顕
著に低下し、はとんど反応は進行しなくなる。また反応
後に反応液中に残存するアルキレンオキサイド量が極め
て多量となり好ましくない。水の比率が上昇するにつ、
11反反応度が増大し、良好な反応条件を得ることがで
きるようになり、反応後の反応液中に残存するアルキレ
ンオキサイド溺も減少する。更にアルキレンオキサイド
の有効利用率も増加し、80%の高率を達成することが
できる。When the proportion of water in the reaction medium decreases below 5% by weight, the reaction rate of hydroxyalylization of galactomannan decreases markedly and the reaction hardly proceeds. Further, the amount of alkylene oxide remaining in the reaction solution after the reaction becomes extremely large, which is not preferable. As the proportion of water increases,
11 reaction degree increases, it becomes possible to obtain good reaction conditions, and alkylene oxide residue remaining in the reaction solution after the reaction is also reduced. Furthermore, the effective utilization rate of alkylene oxide is increased, and a high rate of 80% can be achieved.
反応媒体中の水の比率が70重量%より増加すると、生
成したガラクトマンナンのヒドロキシアルキルエーテル
は媒体中に懸濁状態を保たずに溶解し、反応系全体が増
粘する。このためスラリー状態を保って反応を継続する
ことが不能となる結果、反応生成物の分離、精製等の後
処理工程を効率よく行うことが困難となり、後処理工程
での操作性が極めて悪化する。When the proportion of water in the reaction medium increases beyond 70% by weight, the hydroxyalkyl ether of galactomannan produced does not remain suspended in the medium but dissolves, resulting in thickening of the entire reaction system. As a result, it becomes impossible to maintain the slurry state and continue the reaction, which makes it difficult to efficiently perform post-processing steps such as separation and purification of reaction products, resulting in extremely poor operability in post-processing steps. .
一般に親水性有機溶剤9水に対する比率が増加するに従
って、反応生成物の水溶液の透明性が増大し、また反応
を安定な懸濁状態で進行することができる。Generally, as the ratio of hydrophilic organic solvent 9 to water increases, the transparency of the aqueous solution of the reaction product increases, and the reaction can proceed in a stable suspension state.
アルカリ金属水酸化物としては、水酸化ナトリウム、水
酸化カリウム等が用いられろ。アルカリ金属水酸化物の
添加量は、ガラクトマンラーンのアンヒドロ糖単位当り
0.4モル以上である。As the alkali metal hydroxide, sodium hydroxide, potassium hydroxide, etc. may be used. The amount of alkali metal hydroxide added is 0.4 mol or more per anhydrosaccharide unit of galactomanlaan.
ガラクトマンナンのヒドロキシアルキル応過程で、アル
カリ金属水酸化物の果す役割は触媒であって、その添加
量も僅かで反応が進行する。しかしガラクトマンナンの
アンヒドロ糖単位当り0.4モル以下のアルカリ金属水
酸化物の添加量では、得られたガラクトマンナンのヒド
ロキシアルキルエーテルの水溶液は、ガラクトマンナン
そのもの噴水溶液よりも白濁の程度は少ないが、まだ透
明とはいえない。In the hydroxyalkyl reaction process of galactomannan, the role of the alkali metal hydroxide is as a catalyst, and the reaction proceeds even if the amount added is small. However, when the amount of alkali metal hydroxide added is less than 0.4 mol per anhydrosaccharide unit of galactomannan, the resulting aqueous solution of hydroxyalkyl ether of galactomannan is less cloudy than the fountain solution of galactomannan itself. , it is still not transparent.
一方、アルカリ金属水酸化物の添加量はアンヒドロ糖単
(Q、当り6モル以下が好まし℃・。添加量がこれより
増加すると、反応中にガラクトマンナンスラリーが団粒
化するおそれがある。On the other hand, the amount of alkali metal hydroxide added is preferably 6 mol or less per anhydrosaccharide (Q). If the amount added is greater than this, there is a risk that the galactomannan slurry will aggregate during the reaction.
例えば、反応媒体としてインプロ・くノール45 0
’fJ量部及び水220容量部を用いた場合には、グア
ガム100重量部に対し、水酸化ナトリウム20重量部
を添加すると団粒化が生じて好ましくない。しかし水酸
化ナトリウム15重量部を添加した場合は、よ(攪拌す
ることにより団粒化を防止することができる。また親水
性有機溶剤の比率を増加させることによって団粒化を防
止することもできる。For example, Impro Kunor 450 as reaction medium
When parts of 'fJ and 220 parts by volume of water are used, if 20 parts by weight of sodium hydroxide is added to 100 parts by weight of guar gum, agglomeration will occur, which is not preferable. However, when 15 parts by weight of sodium hydroxide is added, agglomeration can be prevented by stirring.Agglomeration can also be prevented by increasing the proportion of the hydrophilic organic solvent. .
アルキレンオキサイドとしては、低級アルキレンオキサ
イド例えばエチレンオキサイド、プロピレンオキサイド
、1,2−ブチレンオキサイド、ブクジエンモノオキサ
イド、グリシド等が挙げられる。アルキレンオキサイド
はガス状、液状のいずれも用いることができ、また反応
前に全量を仕込んでもよく、逐次反応系に添加してもよ
い。Examples of the alkylene oxide include lower alkylene oxides such as ethylene oxide, propylene oxide, 1,2-butylene oxide, butdiene monooxide, and glycide. The alkylene oxide can be used in either gaseous or liquid form, and the entire amount may be charged before the reaction, or it may be added to the reaction system sequentially.
アルキレンオキサイドの使用量はガラクトマンナンの変
性の程度に応じて任意に変えることができるか、ガラク
トマンナンのアンヒドロ糖単位当り0.01〜6モル、
特に0.1〜4モルが好ましい。The amount of alkylene oxide used can be arbitrarily changed depending on the degree of modification of galactomannan;
Particularly preferred is 0.1 to 4 mol.
本発明を実施ずろに際しては、ガラクトマンナンにアル
カリ金属水酸化物、水及び親水性有機溶r’+llも’
+111え、混合して)ひ振分散液を調製する。When carrying out the present invention, an alkali metal hydroxide, water and a hydrophilic organic solvent r'+ll are also added to the galactomannan.
+111 and mix) to prepare a dispersion liquid.
アル、IJ IJ金1.・11水酸化物は水溶液として
加えることが好ましい。このためには所定量の水の全部
又は一部をアルカリ金属水酸化物溶液の調製に用い、ガ
ラクトマンナンを親水性有機溶剤又はこれと水との混液
に懸濁分散液したのち、アルカリ金属水酸化物溶液を加
えることが好ましい。Al, IJ IJ Gold 1. - It is preferable to add 11-hydroxide as an aqueous solution. For this purpose, all or part of a predetermined amount of water is used to prepare an alkali metal hydroxide solution, and after suspending and dispersing galactomannan in a hydrophilic organic solvent or a mixture of this and water, Preferably, an oxide solution is added.
次いでこの懸濁分散液にヒドロキシアルキルエーテルを
加えて反応させる。反応は通常60〜100°Cの間で
行われる。反応時間は所定の変性度(MS)が達成され
るに充分な時間であり、好ましくは2〜24時間である
。反応容器の形態は常圧リフラックス型容器、加圧攪拌
釜、加圧ニーダ−1加圧ブレンダー等いずれでもよい。Next, a hydroxyalkyl ether is added to this suspension dispersion and reacted. The reaction is usually carried out between 60 and 100°C. The reaction time is sufficient to achieve a predetermined degree of modification (MS), and is preferably 2 to 24 hours. The form of the reaction vessel may be any one such as a normal pressure reflux type vessel, a pressurized stirring vessel, a pressurized kneader-1 pressurized blender, etc.
反応終了後、反応生成物を中和して濾過し、水溶性有機
溶剤の水溶液で洗浄したのち乾燥粉砕して製品を得るこ
とができる。After the reaction is completed, the reaction product is neutralized, filtered, washed with an aqueous solution of a water-soluble organic solvent, and then dried and ground to obtain a product.
本発明方法によれば、ガラクトマンナン及びその反応物
が、水及び水溶性有機溶剤に懸濁した形で反応が進行す
るため、反応終了後の操作も懸濁の状態で進めることが
できる。このため工程管理が容易となり、優良な品質の
製品を効率よく製造することができる。また米国特許2
496670号明細書に記載の方法に比べて、同一容積
の反応釜を用いてより多量のガラクトマンナンを処理す
ることができる。According to the method of the present invention, since the reaction proceeds while the galactomannan and its reactants are suspended in water and a water-soluble organic solvent, operations after the completion of the reaction can also proceed in the suspended state. Therefore, process control becomes easy and products of excellent quality can be manufactured efficiently. Also, US Patent 2
Compared to the method described in No. 496,670, a larger amount of galactomannan can be processed using the same volume of reaction vessel.
本発明方法によって製造されたガラクトマンナンのヒド
ロキシアルキルエーテルは、殊に塗料、絵具、繊維、ゴ
ム、化粧品、製紙等の分野で有用である。The hydroxyalkyl ether of galactomannan produced by the method of the present invention is particularly useful in the fields of coatings, paints, fibers, rubber, cosmetics, paper manufacturing, and the like.
以下実施例において更に詳しく説明を加えるが、実施例
及び比較例中に示す透明度は下記の方法で測定した。A more detailed explanation will be given in the Examples below, but the transparency shown in the Examples and Comparative Examples was measured by the following method.
ホモジナイザーで蒸留水を激しく攪拌しながら試料を加
え、試料の絶乾換算1重量%水溶液を調製し、これを真
空デシケータ中で脱泡し、1昼夜放置する。一方、日立
製作所製可視光分光光度計モデル101を改造し、プリ
ズム分光器部分に凹面反射鏡を設置した自作の白色光透
明度測定器を用い、光路長10圏のガラス製セル中に試
料水溶液を入れ、同一セルの蒸留水透過光を対照として
透過率を%表示したものを透明度とした。A sample is added to the distilled water while vigorously stirring it with a homogenizer to prepare a 1% by weight aqueous solution of the sample on an absolute dry basis, which is defoamed in a vacuum desiccator and left overnight. On the other hand, using a self-made white light transparency measuring device that was a modification of the Hitachi visible light spectrophotometer model 101 and a concave reflector installed in the prism spectrometer section, a sample aqueous solution was poured into a glass cell with an optical path length of 10 zones. The transparency was expressed as a percentage of transmittance with reference to the light transmitted through distilled water from the same cell.
実施例1
攪拌器、冷却器、滴下ロート及び温度計を装備した内容
積1eの4つロフラスコに、2−プロパツール400
ml、水6(3ml及び水分率12%のグアガム粉末6
0gを仕込み、攪拌して均一な懸濁分散液とする。この
分散液に滴下ロートより徐々に水酸化ナトリウム3.!
9を水50mt′に溶解した水酸化ナトリウム溶液を常
温で滴下し、次いで常温で1時間攪拌したのち、プロピ
レンオキサイド55&を滴下ロートより滴下しフラスコ
全体な湯浴により80℃に昇温し、7時間反応を続ける
。Example 1 2-Propatool 400 was placed in a four-loaf flask with an internal volume of 1e equipped with a stirrer, a condenser, a dropping funnel and a thermometer.
ml, 6 ml of water (3 ml and 6 ml of guar gum powder with a moisture content of 12%)
0 g was added and stirred to form a uniform suspension and dispersion. 3. Sodium hydroxide is gradually added to this dispersion through a dropping funnel. !
A sodium hydroxide solution prepared by dissolving 9 in 50 mt of water was added dropwise at room temperature, and after stirring at room temperature for 1 hour, propylene oxide 55& was added dropwise from the dropping funnel and the entire flask was heated to 80°C in a hot water bath. Continue the time reaction.
反応終了後、フラスコ内部を65°C以下に冷却し、攪
拌下に氷酢酸を滴下ロートより徐々に滴下して中和する
。この反応全工程にわたって反応系は良好な懸濁状態が
保たれる。次いで反応生成物をf過し、更に80%2−
プロパツール水溶液200m1で洗浄したのち再びr過
し、更に2−プロパツール150m1で洗浄したのち反
応生成物を取り出し、70℃の真空乾燥機で一昼夜乾燥
する。次いで反応生成物をコーヒーミルによって粉砕し
、150メツシユを全量通過させるようにしてガラクト
マンナンのヒドロ比較例1
実施例1で原料として用いたグアガムの透明度を測定し
たところ25%であった。After the reaction is completed, the inside of the flask is cooled to 65° C. or below, and glacial acetic acid is gradually added dropwise from the dropping funnel while stirring to neutralize the flask. The reaction system is kept in a good suspended state throughout the entire reaction process. The reaction product was then filtered and further 80% 2-
After washing with 200 ml of propatool aqueous solution, it is filtered again and further washed with 150 ml of 2-propanol, and then the reaction product is taken out and dried in a vacuum dryer at 70° C. all day and night. The reaction product was then ground in a coffee mill, and the entire amount was passed through 150 meshes. Galactomannan Hydrogen Comparative Example 1 The transparency of the guar gum used as a raw material in Example 1 was measured and found to be 25%.
比較例2
実施例1と同一の反応容器を用い、同様な手段で、下記
の処方にしたがってガラクトマンナ2−)o ハ/ −
/l/ 150ml水
20m1グアガム粉末
100g水酸化ナトリウム 6
g水(水酸化ナトリウム溶解用) 5Qmlプロ
ピレンオキサイド 15g実施例2
内容積6eの加圧オートクレーブに水分率12%のグア
ガノ、粉末600g及び2−プロノ(ノール1200m
6を仕込み、攪拌して懸濁分散液となし、水酸化カリウ
ム50gを水200 mlに溶解した溶液を徐々に添加
する。オートクレーブ内を窒素置換し、1時間攪拌した
のちエチレンオキサイド100gを添加し、55℃で6
時間反応させる。反応終了後、オートクレーブ内を室温
まで冷却してから再び窒素置換を行い、生成物を取出す
。反応生成物を化学量論量の氷酢酸で中和し、濾過した
のち80%2−グロパノール溶液2000 mlで洗浄
し、再び濾過したのち2−プロパツール2000m1で
洗浄し、生成物を濾過して風乾する。これをコーヒーミ
ルによって粉砕し、ガラクトマンナンのヒドロキ出願人
三菱アセテート株式会社
外1名
代理人 弁理士 小 林 正 雄
19−Comparative Example 2 Using the same reaction vessel as in Example 1 and using the same method, galactomanna 2-)o ha/- was prepared according to the following recipe.
/l/ 150ml water
20ml guar gum powder
100g sodium hydroxide 6
g Water (for dissolving sodium hydroxide) 5Qml Propylene oxide 15g Example 2 In a pressurized autoclave with an internal volume of 6e, guagano with a moisture content of 12%, 600g of powder, and 2-prono (Nol 1200ml)
6 was prepared, stirred to form a suspension and dispersion, and a solution of 50 g of potassium hydroxide dissolved in 200 ml of water was gradually added. After purging the inside of the autoclave with nitrogen and stirring for 1 hour, 100 g of ethylene oxide was added and the mixture was heated at 55°C for 6 hours.
Allow time to react. After the reaction is completed, the inside of the autoclave is cooled to room temperature, replaced with nitrogen again, and the product is taken out. The reaction product was neutralized with a stoichiometric amount of glacial acetic acid, filtered, washed with 2000 ml of 80% 2-gropanol solution, filtered again and washed with 2000 ml of 2-propanol, and the product was filtered. Air dry. This is ground in a coffee mill to produce galactomannan. Applicant: Mitsubishi Acetate Co., Ltd. and one other representative, patent attorney Masao Kobayashi 19-
Claims (1)
単位当たり0.4モル以上のアルカリ金属水酸化物の存
在下に、親水性有機溶剤及び水を媒体として、アルキレ
ンオキサイドと反応させることを特徴とする。水溶液が
透明性に優れたガラクトマンナンのヒドロキシアルキル
エーテルの製法。It is characterized in that galactomannan is reacted with alkylene oxide in the presence of 0.4 mol or more of alkali metal hydroxide per anhydrosaccharide unit of galactomannan, using a hydrophilic organic solvent and water as a medium. A method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20458782A JPS5996103A (en) | 1982-11-24 | 1982-11-24 | Method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20458782A JPS5996103A (en) | 1982-11-24 | 1982-11-24 | Method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5996103A true JPS5996103A (en) | 1984-06-02 |
Family
ID=16492928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20458782A Pending JPS5996103A (en) | 1982-11-24 | 1982-11-24 | Method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5996103A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0686643A1 (en) * | 1994-06-09 | 1995-12-13 | Rhone-Poulenc Inc. | Guar gum composition and process for making it |
| WO1998018828A1 (en) * | 1996-10-25 | 1998-05-07 | Rhodia Inc. | Derivatized guar gum composition including nonionic and cationic groups which demonstrate excellent solution clarity properties for detergent applications |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5730701A (en) * | 1980-07-30 | 1982-02-19 | Shikishima Boseki Kk | Preparation of hydroxyalkylated polysaccharide |
-
1982
- 1982-11-24 JP JP20458782A patent/JPS5996103A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5730701A (en) * | 1980-07-30 | 1982-02-19 | Shikishima Boseki Kk | Preparation of hydroxyalkylated polysaccharide |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0686643A1 (en) * | 1994-06-09 | 1995-12-13 | Rhone-Poulenc Inc. | Guar gum composition and process for making it |
| WO1998018828A1 (en) * | 1996-10-25 | 1998-05-07 | Rhodia Inc. | Derivatized guar gum composition including nonionic and cationic groups which demonstrate excellent solution clarity properties for detergent applications |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5298018B2 (en) | Process for producing silane-modified cationized cellulose | |
| NO157229B (en) | DRILLING TOOL FOR MANUFACTURING CRUDE PARTS IN DRILL. | |
| KR20140032391A (en) | Method for producing alkali cellulose | |
| JP2025060971A (en) | Process for producing crosslinked cellulose ethers | |
| JP4150186B2 (en) | Method for producing hydroxyalkyl cellulose | |
| JPH03146501A (en) | Production of cellulose ether having high polymerization degree | |
| JP2022530342A (en) | Process for Producing Crosslinked Cellulose Ether | |
| US5001232A (en) | Carboxymethylsulphoethyl celluloses and a process for their preparation | |
| ITVA20060069A1 (en) | PROCEDURE FOR THE PREPARATION OF PURIFIED CATIONIC GUAR | |
| FI100657B (en) | Water-soluble hydroxypropylsulfoethylcellulose derivatives (HPSEC) with low degree of substitution and process for their preparation | |
| EP2928925B1 (en) | Process for producing hydroxyalkyl celluloses | |
| JP5577331B2 (en) | Process for producing silane-modified cationized polymer compound | |
| JP3002916B2 (en) | Production method of cellulose mixed ether | |
| JPS5996103A (en) | Method for producing hydroxyalkyl ether of galactomannan whose aqueous solution has excellent transparency | |
| JPS59159801A (en) | Manufacture of cellulose ether from cellulose and etherifier | |
| JPS5975902A (en) | Production of hydroxyethylcellulose | |
| JPH08245701A (en) | Highly transparent hydroxyalkyl cellulose and its production | |
| Liu et al. | Effect of substituent distribution on water solubility of O-methylcellulose | |
| US4177345A (en) | Process for preparing a sulfate ester of a polyhydroxy polymer | |
| JP2000186101A (en) | Production of hydroxypropyl cellulose | |
| JP5489484B2 (en) | Method for producing silane-modified cationized polymer compound powder | |
| US7777026B2 (en) | Aminoalkyl-containing guar derivatives | |
| JP2005171089A (en) | Method for cationized hydroxyalkyl cellulose | |
| JPH09227601A (en) | Method for producing cellulose derivative containing sulfonic acid group | |
| JPH01123801A (en) | Production of cellulose ether |