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JPS6256883B2 - - Google Patents
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JPS6256883B2 - - Google Patents

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Publication number
JPS6256883B2
JPS6256883B2 JP20688481A JP20688481A JPS6256883B2 JP S6256883 B2 JPS6256883 B2 JP S6256883B2 JP 20688481 A JP20688481 A JP 20688481A JP 20688481 A JP20688481 A JP 20688481A JP S6256883 B2 JPS6256883 B2 JP S6256883B2
Authority
JP
Japan
Prior art keywords
galactomannan
reaction
product
water
present
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
JP20688481A
Other languages
Japanese (ja)
Other versions
JPS58109502A (en
Inventor
Naoki Mochizuki
Taku Tabuchi
Masao Kobayashi
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Mitsubishi Rayon 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 Mitsubishi Chemical Corp, Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Chemical Corp
Priority to JP20688481A priority Critical patent/JPS58109502A/en
Publication of JPS58109502A publication Critical patent/JPS58109502A/en
Publication of JPS6256883B2 publication Critical patent/JPS6256883B2/ja
Granted legal-status Critical Current

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  • Polysaccharides And Polysaccharide Derivatives (AREA)

Description

【発明の詳細な説明】 本発明はガラクトマンナンのヒドロキシアルキ
ルエーテルの製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a hydroxyalkyl ether of galactomannan.

ガラクトマンナンと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つて自然界には主として豆科
植物の種子に多く含有されている。特にグア豆を
原料とするグアガム、ローカストビーンを原料と
するローカストビーンガムはその代表的なガラク
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 consisting of a main chain consisting of mannose as a constituent unit and galactose units as side chains, and is mainly contained in large amounts in the seeds of leguminous plants in nature. In particular, guar gum made from guar beans and locust bean gum made from locust beans are representative vegetable gums containing galactomannan as a main component.

特に本発明においてはグアガム、ローカストビ
ーンガムを始めとするガラクトマンナンを主成分
とする物質を総称し、ガラクトマンナンと指称す
る。これらの植物ガム質は植物粘質物であつて水
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。しかし
ながらこれらのガラクトマンナンは水溶液にする
とき「ママコ」と呼ばれる粉体粒子の団粒化を引
起し易くまたガラクトマンナンの水溶液はバクテ
リアの攻撃をうけやすく経時的に腐敗しその粘度
低下を起こすという欠点をもつている。
In particular, in the present invention, substances whose main component is galactomannan, including guar gum and locust bean gum, are collectively referred to as galactomannan. These plant gums are plant mucilage substances that dissolve in water and exhibit extremely high viscosity, and are therefore widely used in the food and industrial fields. However, when these galactomannans are made into an aqueous solution, they tend to cause agglomeration of powder particles called "mamako", and aqueous solutions of galactomannans are susceptible to attack by bacteria and deteriorate over time, causing a decrease in their viscosity. It has

本発明者等はガラクトマンナン水溶液の特徴で
ある極めて高い粘度を維持しつつ上記欠点が改良
された変性ガラクトマンナンを得ることを目的と
して検討し本発明に到達したものである。
The present inventors conducted research and arrived at the present invention with the aim of obtaining a modified galactomannan that has the above-mentioned drawbacks improved while maintaining the extremely high viscosity that is characteristic of galactomannan aqueous solutions.

本発明によつて得られる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せし
め、PH12以下の液性で水溶液粘度が安定なものと
することができ、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保持でき
るという特性も合わせもつものである。かかる特
性から本発明によつて得られるガラクトマンナン
のヒドロキシアルキルエーテルは主として製紙、
化粧品、塗料、土木、建築、石油、火薬等の産業
分野に使用されるものである。
The hydroxyalkyl ether of galactomannan 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, and can reduce the viscosity of an aqueous solution with a pH of 12 or less. It also has the property of being stable and maintaining a high aqueous solution viscosity even in the presence of high concentrations of various salts containing multivalent ions. Due to these characteristics, the hydroxyalkyl ether of galactomannan obtained by the present invention is mainly used in paper manufacturing,
It is used in industrial fields such as cosmetics, paints, civil engineering, architecture, petroleum, and explosives.

従来開発されてきたガラクトマンナンのヒドロ
キシアルキルエーテル化法としては水を反応媒体
とする水媒法、水と有機溶媒との混合物にガラク
トマンナンを懸濁せしめた状態で実施する懸濁法
が知られ水媒法に較べ懸濁法が有利とされてい
る。懸濁法のかかる有利性は殊にガラクトマンナ
ンのヒドロキシアルキル化工程に於ける反応系が
極めて粘度の低い懸濁分散状で行われること、ヒ
ドロキシアルキル化反応終了後の中和、精製等の
後処理工程が水媒法に較べ容易であること等の理
由に依つたものである。従つてかかる理由のうち
後処理工程が不必要であり、かつ高粘度下でガラ
クトマンナンのヒドロキシル化反応が可能であれ
ば、高価な親水性有機溶剤を用いずにその実施を
することができ親水性有機溶剤の回収設備の不要
となるなど懸濁法に対しても有利な水媒法による
ガラクトマンナンのヒドロキシアルキル化が可能
となる。従つて水を媒体として高粘度アルカリ溶
液でのヒドロキシアルキル化の良好な反応性及び
後処理を不要とする方法の確立が業界からも強く
望まれる現状にある。ガラクトマンナンは水もし
くは温水に溶解し極めて高い粘度を発現するもの
であるから、ガラクトマンナンの団粒化を生ぜし
めないよう高濃度かつ均一な溶液を作製すること
は難しい技術であるが本発明者らはガラクトマン
ナンの水への溶解性が水の水素イオン濃度によつ
て変化し殊に高アルカリ性水溶液に対しては大量
のガラクトマンナンが容易に溶解すること、とく
にニーダー等の強制撹拌混合機を用いることによ
り、更に大量のガラクトマンナンが「ママコ」を
作ることなく均一に溶解することを見出した。か
かる溶解方法を見出すことにより、本発明者等は
ガラクトマンナンのヒドロキシアルキルエーテル
化反応必要な水媒の量を減少せしめても当該エー
テル化反応の効率に何等低減を伴うことなくその
後の製品の乾燥に伴う乾燥負荷の減少を可能とし
た本発明を完成した。
Conventionally developed methods for hydroxyalkyl etherification of galactomannan include an aqueous medium method using water as a reaction medium and a suspension method in which galactomannan is suspended in a mixture of water and an organic solvent. The suspension method is said to be more advantageous than the aqueous method. This advantage of the suspension method is particularly due to the fact that the reaction system in the hydroxyalkylation process of galactomannan is carried out in the form of suspension and dispersion with extremely low viscosity, and that the process of neutralization and purification after the completion of the hydroxyalkylation reaction is This is due to the fact that the treatment process is easier than the aqueous method. Therefore, among these reasons, if a post-treatment step is unnecessary and the hydroxylation reaction of galactomannan can be carried out under high viscosity, it can be carried out without using an expensive hydrophilic organic solvent. This makes it possible to hydroxyalkylate galactomannan using an aqueous method, which is advantageous over suspension methods, such as eliminating the need for recovery equipment for organic solvents. Therefore, there is a strong desire in the industry to establish a method for hydroxyalkylation that has good reactivity in a highly viscous alkaline solution using water as a medium and does not require post-treatment. Since galactomannan dissolves in water or hot water and exhibits an extremely high viscosity, it is a difficult technique to prepare a highly concentrated and uniform solution without causing galactomannan agglomeration. They found that the solubility of galactomannan in water changes depending on the hydrogen ion concentration of the water, and that a large amount of galactomannan is easily dissolved in a highly alkaline aqueous solution, especially when using a forced stirring mixer such as a kneader. It has been found that by using this method, even larger amounts of galactomannan can be uniformly dissolved without forming "mako". By discovering such a dissolution method, the present inventors have been able to reduce the amount of aqueous medium necessary for the hydroxyalkyl etherification of galactomannan without any reduction in the efficiency of the etherification reaction, and the subsequent drying of the product. The present invention has been completed, which makes it possible to reduce the drying load associated with drying.

本発明の要旨とするところはガラクトマンナ
ン、塩基性物質及び水との混合物を高速撹拌下に
アルキレンオキサイドと反応せしめ、乾燥するこ
とを特徴とする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方法にある。
The gist of the present invention is a method for producing a hydroxyalkyl ether of galactomannan, which comprises reacting a mixture of galactomannan, a basic substance and water with alkylene oxide under high-speed stirring and drying.

本発明の特徴の一つは従来技術で行われていた
ガラクトマンナンのヒドロキシアルキル化エーテ
ル化反応終了後の中和、精製工程を消略しヒドロ
キシアルキルエーテル反応終了後、直接乾燥する
方式を採用した点である。従来後処理はガラクト
マンナンのヒドロキシアルキルエーテル化反応時
に必要な強アルカリが製品中に混入することは好
しくないため、まず、この強アルカリを中和する
必要があつたのであるが、この中和工程を生じた
塩は灰分となつて製品中に残存する傾向があり、
粘性物質として使用されるガラクトマンナンのヒ
ドロキシアルキルエーテル中に灰分が多量に残る
ことは好しくない。従来かかるアルカリ性物質の
中和は無機酸及び有機酸が用いられているが特に
無機酸を用いた場合には製品中の灰分が増大する
という欠点がありそれ故有機酸が多用されている
が、アルカリ物質に対応する化学量論量の有機酸
による中和では十分な製品の中和はなされ得ず得
られる製品がアルカリ性となつており、その取扱
い性が低かつたのである。
One of the features of the present invention is that the neutralization and purification steps after the completion of the hydroxyalkylation etherification reaction of galactomannan, which were performed in the conventional technology, are omitted, and a method is adopted in which drying is performed directly after the completion of the hydroxyalkyl ether reaction. It is. Conventionally, in post-treatment, it was necessary to first neutralize the strong alkali necessary for the hydroxyalkyl etherification reaction of galactomannan, as it was undesirable for this strong alkali to be mixed into the product. The salt produced during the process tends to remain in the product as ash.
It is undesirable for a large amount of ash to remain in the hydroxyalkyl ether of galactomannan used as the viscous substance. Conventionally, inorganic acids and organic acids have been used to neutralize alkaline substances, but in particular, when inorganic acids are used, the ash content in the product increases, which is why organic acids are often used. Neutralization with a stoichiometric amount of organic acid corresponding to the alkaline substance did not sufficiently neutralize the product, resulting in an alkaline product that was difficult to handle.

本発明者らはかかる現状に鑑み検討しガラクト
マンナンのヒドロキシアルキルエーテル化反応は
弱アルカリ性下に於ても十分に進行することを見
出した点に本発明の他の特徴を有している。かか
る弱アルカリ下でのヒドロキシアルキルエーテル
化反応を採用することによつて、従来法にて不可
決と考えられていた反応終了後の中和工程を消略
し得、反応工程そのものの簡略化をなし得たと共
に、製品中へ混入することが好しくない灰分の原
因となる塩の生成を防止し得たのである。
Another feature of the present invention is that the present inventors conducted studies in view of the current situation and found that the hydroxyalkyl etherification reaction of galactomannan proceeds satisfactorily even under weak alkalinity. By employing such a hydroxyalkyl etherification reaction under a weak alkali, it is possible to eliminate the neutralization step after the completion of the reaction, which was considered to be impossible in conventional methods, and the reaction process itself can be simplified. At the same time, it was possible to prevent the formation of salts, which would cause undesirable ash content to be mixed into the product.

本発明を実施するに際して用いるガラクトマン
ナンの形態としては豆類を粗砕したいわゆるスプ
リツトの状態であつてもよく、また細かく粉砕し
た粉状の状態であつてもよい。更には粉状のガラ
クトマンナンをエーテル、アルコール、ベンゼン
等にて精製したものであつてもよい。また熱分
解、酸化分解、酵素分解、酸加水分解等の操作を
加えて分子量を低下せしめたガラクトマンナンも
使用することができる。
The form of galactomannan used in carrying out the present invention may be in the form of so-called splits obtained by coarsely pulverizing beans, or may be in the form of finely pulverized powder. Furthermore, powdered galactomannan purified with ether, alcohol, benzene, etc. may also be used. Furthermore, galactomannan whose molecular weight has been reduced by undergoing operations such as thermal decomposition, oxidative decomposition, enzymatic decomposition, and acid hydrolysis can also be used.

本発明を実施するに際して用いるアルキレンオ
キサイドは低級アルキレンオキサイドであつて、
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、フタジエンモノ
オキサイド、グリシド等があり反応にあたつては
ガス状、液状に限らず用いることができ、その反
応系への添加は予め反応前に全量を仕込んでも逐
次反応系に添加することも可能である。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
の要求程度に応じて任意に変えることができる
が、好ましくは、ガラクトマンナンのアンヒドロ
糖単位当り0.01モルから6モルの間とくに0.1モ
ルから2モルの間である。反応は通常30℃乃至
100℃の間で行われ反応時間は所定の変性度が達
成されるに充分な時間、好ましくは2〜24時間と
するのがよい。
The alkylene oxide used in carrying out the present invention is a lower alkylene oxide, and
For example, ethylene oxide, propylene oxide, 1,2-butylene oxide, phtadiene monooxide, glycide, etc. can be used in the reaction regardless of whether they are in gaseous or liquid form, and they must be added to the reaction system in advance before the reaction. It is also possible to add the entire amount to the reaction system sequentially. The amount of alkylene oxide used can be arbitrarily changed depending on the required degree of modification of galactomannan, but it is preferably between 0.01 mol and 6 mol, particularly between 0.1 mol and 2 mol, per anhydrosaccharide unit of galactomannan. be. The reaction is usually carried out at 30°C to
The reaction time is preferably 2 to 24 hours, preferably 2 to 24 hours, which is sufficient to achieve the desired degree of modification.

本発明を実施するに際して用いる塩基性物質と
してはアルカリ金属水酸化物、アルカリ土類金属
水酸化物、アンモニア、有機アミン類、第4級ア
ンモニウム化合物及び強塩基と弱酸とからなる水
溶性の無機塩類等を用いることができる。上記塩
基性物質のうち強塩基し弱酸とからなる水溶性の
無機塩類を用いて作成したグラクトマンナンのヒ
ドロキシアルキルエーテル中に当該無機塩類が多
量に混入すると灰分として作用するのでその使用
量はできるだけ少なくすることが必要である。ア
ルカリ金属水酸化物、アルカリ土類金属水酸化物
はそれ自体強い塩基性を示すものが多く、他の塩
基性物質に較べ使用量が少量で満足な製品が得ら
れるが過剰量の使用量になると、本発明は反応系
の中和、精製を行わないプロセスとなつているた
め生成物がアルカリ性を示しその水溶液の粘度が
急激に低下する現象を呈するので、その使用量に
気を使うことが必要となる。アンモニア、有機ア
ミン類、第4級アンモニウム塩類は反応を良好に
進行せしめうると共に、反応終了後の生成物を直
ちに乾燥する工程に於て生品中から揮散するの
で、これらの有機アミン類は回収再利用しうる利
点もある。更にこれらの物質は例え得られた製品
中に混入しても灰分の原因とはならず、その水溶
液粘度が大幅に低下しないという特徴を有するも
のであり、とくに好ましいものである。
Basic substances used in carrying out the present invention include alkali metal hydroxides, alkaline earth metal hydroxides, ammonia, organic amines, quaternary ammonium compounds, and water-soluble inorganic salts consisting of strong bases and weak acids. etc. can be used. If large amounts of inorganic salts are mixed into the hydroxyalkyl ether of glactomannan, which is prepared using water-soluble inorganic salts consisting of a strong base and a weak acid among the above basic substances, they will act as ash, so the amount used should be minimized. It is necessary to reduce it. Many alkali metal hydroxides and alkaline earth metal hydroxides themselves exhibit strong basicity, and compared to other basic substances, a satisfactory product can be obtained with a small amount of use; however, if an excessive amount is used, In this case, since the process of the present invention does not involve neutralization or purification of the reaction system, the product becomes alkaline and the viscosity of the aqueous solution rapidly decreases, so it is important to be careful about the amount used. It becomes necessary. Ammonia, organic amines, and quaternary ammonium salts allow the reaction to proceed well, and they volatilize from the raw product in the process of immediately drying the product after the reaction is completed, so these organic amines must be recovered. It also has the advantage of being reusable. Furthermore, even if these substances are mixed into the obtained product, they do not cause ash content and do not significantly reduce the viscosity of the aqueous solution, so they are particularly preferred.

本発明はガラクトマンナンと水との混合液中で
アルキレンオキサイドを反応せしめる方式を取る
ため、通常の方法にては反応の不均一化が起るの
であるが、本発明に於てはこの混合液を高速撹拌
下に実施するため、上述したような不均一反応が
起ることはない。用い得る反応装置としては常圧
リフラツクス型容器、加圧撹拌釜、加圧ニーダ
ー、加圧ブレンダー等があるが、反応系の強制撹
拌が可能な加圧ニーダー、加圧ブレンダーを用い
た場合特に良好な結果が得られる。
The present invention uses a method in which alkylene oxide is reacted in a mixed solution of galactomannan and water, which causes non-uniformity of the reaction in normal methods, but in the present invention, this mixed solution Since this is carried out under high-speed stirring, the above-mentioned heterogeneous reaction does not occur. Usable reaction devices include atmospheric reflux type containers, pressure stirring vessels, pressure kneaders, pressure blenders, etc., but the use of pressure kneaders and pressure blenders that can forcefully stir the reaction system is particularly effective. results.

本発明は、上述した如く反応を行つた反応生成
物を中和、精製等の処理を施すことなく乾燥させ
る方法をとり得るので、その工程省略化は著るし
いものとなる。例えば反応生成物をキヤステイン
グしてフイルム状物となして乾燥ししかるのち粉
砕する方法やドラムドライヤーで乾燥する方法、
ダイスより薄層として押出し乾燥する方法等が採
用しうる。
In the present invention, a method can be employed in which the reaction product obtained by the reaction as described above is dried without being subjected to any treatment such as neutralization or purification, so that the process can be significantly simplified. For example, a method of casting the reaction product to form a film, drying it and then pulverizing it, or drying it with a drum dryer,
A method such as extrusion drying as a thin layer using a die may be adopted.

本発明の方法は強制撹拌下にガラクトマンナン
とアルキレンオキサイドとを反応せしめるという
方式をとることにより、反応系高濃化が可能であ
り反応生成物のフイルム状での乾燥を行い得、工
程が極めて簡略化されており、また、反応を弱ア
ルカリ下で行なうことによつて反応終了後の系の
中和工程を消略することにも成巧し、製品である
ガラクトマンナンのヒドロキシアルキルエーテル
化物中に製品の特性を低下せしめる灰分の混入を
低減し得たのである。
The method of the present invention uses a system in which galactomannan and alkylene oxide are reacted under forced stirring, so that the reaction system can be highly concentrated, the reaction product can be dried in the form of a film, and the process is extremely simple. The process is simple, and by conducting the reaction under a weak alkali, the process of neutralizing the system after the completion of the reaction can be omitted. This made it possible to reduce the amount of ash contamination that degrades the properties of the product.

以下実施例により本発明を更に詳細に説明す
る。
The present invention will be explained in more detail with reference to Examples below.

実施例 1 内容積3の加圧密閉型ニーダーに8gの水酸
化ナトリウムを400mlの水に溶解した水溶液と水
分率12%のグアガム粉末500gを添加し「ママ
コ」及び団粒物が確認できなくなるまで練合わせ
る。しかるのちニーダーを密閉し窒素でシール
し、ニーダーを80℃に加温し150gのプロピレン
オキサイドを徐々に加え4時間反応を行つたのち
ニーダーを常温まで冷却し再び窒素置換を行つて
から内容物を取出した。反応生成物を薄板状に成
形し、70℃の真空乾燥機で1昼夜乾燥させた。そ
の後粉砕して水分率11%灰分は3.0%なるグアガ
ムのヒドロキシプロピルエーテルを得た。
Example 1 An aqueous solution of 8 g of sodium hydroxide dissolved in 400 ml of water and 500 g of guar gum powder with a moisture content of 12% were added to a pressurized sealed kneader with an internal volume of 3 until "mamako" and aggregates were no longer observed. Practice. After that, the kneader was sealed and sealed with nitrogen, the kneader was heated to 80°C, 150g of propylene oxide was gradually added, and the reaction was carried out for 4 hours.The kneader was then cooled to room temperature, replaced with nitrogen again, and the contents were poured out. I took it out. The reaction product was formed into a thin plate and dried in a vacuum dryer at 70°C for one day and night. Thereafter, it was crushed to obtain guar gum hydroxypropyl ether with a moisture content of 11% and an ash content of 3.0%.

実施例 2 内容積3の加圧密閉型ニーダーに500mlの水
と、水分率12%のグアガム粉末500gを添加し反
応器を閉じたのち窒素でシール、ジエチルアミン
20gを添加し常温で2時間撹拌する。その後反応
器を60℃に加温し75gのエチレンオキサイドを
徐々に加えながら8時間反応を行つた。その後反
応器を常温まで冷却し窒素置換を行つたのち反応
生成物を取出した。この反応生成物を薄板状に成
形し70℃の真空乾燥機で1昼夜乾燥させた後粉砕
し水分率8%、灰分1.6%のグアガムのヒドロキ
シエチルエーテルを得た。
Example 2 Add 500 ml of water and 500 g of guar gum powder with a moisture content of 12% to a pressurized closed kneader with an internal volume of 3, close the reactor, seal with nitrogen, and add diethylamine.
Add 20g and stir at room temperature for 2 hours. Thereafter, the reactor was heated to 60° C., and 75 g of ethylene oxide was gradually added to carry out the reaction for 8 hours. Thereafter, the reactor was cooled to room temperature and replaced with nitrogen, and then the reaction product was taken out. This reaction product was formed into a thin plate, dried in a vacuum dryer at 70°C for one day and night, and then pulverized to obtain guar gum hydroxyethyl ether having a moisture content of 8% and an ash content of 1.6%.

実施例 3 内容積3の加圧密閉型ニーダーに30gのトリ
エチルベンジルアンモニウムクロリド、水分率10
%のローカストビーンガム粉末500g及び水500ml
を仕込み「ママコ」及び団粒物が確認できなくな
るまで温度80℃で練合わせる。しかるのち反応器
内を窒素で置換し75gのプロピレンオキサイドを
徐々に加え8時間反応を行つた。その後ニーダー
を常温まで冷却してから反応生成物を取出した。
反応生成物を薄板状に成形し70℃の真空乾燥機に
て1昼夜乾燥させた後粉砕し水分率10%、灰分
1.9%のローカストビーンガムのヒドロキシプロ
ピルエーテルを得た。
Example 3 30 g of triethylbenzylammonium chloride, moisture content 10, in a pressurized closed kneader with an internal volume of 3.
% locust bean gum powder 500g and water 500ml
Prepare and knead at a temperature of 80℃ until "mamako" and aggregates are no longer visible. Thereafter, the inside of the reactor was purged with nitrogen, 75 g of propylene oxide was gradually added, and the reaction was carried out for 8 hours. Thereafter, the kneader was cooled to room temperature and the reaction product was taken out.
The reaction product was formed into a thin plate and dried in a vacuum dryer at 70℃ for one day and night, and then ground to a moisture content of 10% and an ash content.
1.9% locust bean gum hydroxypropyl ether was obtained.

Claims (1)

【特許請求の範囲】 1 ガラクトマンナンと塩基性物質と水との混合
物を高速撹拌下にアルキレンオキサイドと反応さ
せて得た反応生成物を直接乾燥することを特徴と
するガラクトマンナンのヒドロキシアルキルエー
テルの製造方法。 2 塩基性物質としてアンモニア有機アミン第4
級アンモニウム化合物より選ばれた物質を用いる
ことを特徴とする特許請求の範囲第1項記載のガ
ラクトマンナンのヒドロキシアルキルエーテルの
製造方法。 3 乾燥法として反応生成物を薄い成形物とした
状態で行なうことを特徴とする特許請求の範囲第
1項記載のガラクトマンナンのヒドロキシアルキ
ルエーテルの製造方法。
[Claims] 1. A hydroxyalkyl ether of galactomannan, which is characterized in that the reaction product obtained by reacting a mixture of galactomannan, a basic substance, and water with an alkylene oxide under high-speed stirring is directly dried. Production method. 2 Ammonia organic amine No. 4 as a basic substance
The method for producing a hydroxyalkyl ether of galactomannan according to claim 1, characterized in that a substance selected from class ammonium compounds is used. 3. The method for producing a hydroxyalkyl ether of galactomannan according to claim 1, characterized in that the drying method is carried out with the reaction product formed into a thin molded product.
JP20688481A 1981-12-23 1981-12-23 Production of hydroxyalkyl ether of galactomannan Granted JPS58109502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20688481A JPS58109502A (en) 1981-12-23 1981-12-23 Production of hydroxyalkyl ether of galactomannan

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20688481A JPS58109502A (en) 1981-12-23 1981-12-23 Production of hydroxyalkyl ether of galactomannan

Publications (2)

Publication Number Publication Date
JPS58109502A JPS58109502A (en) 1983-06-29
JPS6256883B2 true JPS6256883B2 (en) 1987-11-27

Family

ID=16530639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20688481A Granted JPS58109502A (en) 1981-12-23 1981-12-23 Production of hydroxyalkyl ether of galactomannan

Country Status (1)

Country Link
JP (1) JPS58109502A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4310088A1 (en) * 1993-03-27 1994-09-29 Hoechst Ag Process for the preparation and workup of aqueous medium-soluble N-hydroxyalkyl chitosans
JP5889669B2 (en) * 2012-02-21 2016-03-22 三菱化学フーズ株式会社 Method for producing galactomannan

Also Published As

Publication number Publication date
JPS58109502A (en) 1983-06-29

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