JPS58120603A - Neutralization of alkaline galactomannan - Google Patents

Neutralization of alkaline galactomannan

Info

Publication number
JPS58120603A
JPS58120603A JP333082A JP333082A JPS58120603A JP S58120603 A JPS58120603 A JP S58120603A JP 333082 A JP333082 A JP 333082A JP 333082 A JP333082 A JP 333082A JP S58120603 A JPS58120603 A JP S58120603A
Authority
JP
Japan
Prior art keywords
galactomannan
neutralization
water
carbon dioxide
alkaline
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.)
Granted
Application number
JP333082A
Other languages
Japanese (ja)
Other versions
JPH0140842B2 (en
Inventor
Naoki Mochida
望田 直規
Taku Tabuchi
田淵 卓
Masao Kobayashi
雅夫 小林
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 Acetate Co Ltd
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Acetate Co Ltd
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 Acetate Co Ltd, Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Acetate Co Ltd
Priority to JP333082A priority Critical patent/JPS58120603A/en
Publication of JPS58120603A publication Critical patent/JPS58120603A/en
Publication of JPH0140842B2 publication Critical patent/JPH0140842B2/ja
Granted legal-status Critical Current

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  • Polysaccharides And Polysaccharide Derivatives (AREA)

Abstract

PURPOSE:To neutralize alkaline galactomannan, uniformly and easily, by dispersing galactomannan in an alkaline aqueous solution of a hydrophilic organic solvent, and contacting the dispersion with carbon dioxide as a neutralizing agent. CONSTITUTION:Galactomannan is mixed with a hydrophilic organic solvent (a solvent miscible with water and containing >=30wt% water, e.g. methanol) and an alkaline aqueous solution (obtained by dissolving a basic substance such as sodium hydroxide in water), and stirred at room temperature for several hours to obtain a dispersion. Carbon dioxide gas is introduced into the reactor and bubbled at room temperature under atmospheric pressure to effect the neutralization of the dispersion and obtain galactomannan. USE:For food additive and various industrial fields such as paper manufacture industry, textile industry, etc.

Description

【発明の詳細な説明】 本発明はアルカリ性ガラクトマンナン類の中和方法に関
するものであり、更に詳しくはいわゆるスラリー法にお
けるアルカリ性ガラクトマンナン類の中和方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for neutralizing alkaline galactomannans, and more particularly to a method for neutralizing alkaline galactomannans in a so-called slurry method.

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
であっ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り、
これらの植物ガム質は植物粘質物であって水に沼解し−
(極めて高い粘性を示す性質がある。更にガラクトマン
ナン水溶液は非イオン性であり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
った特徴と併わせもつところから食品分野及び製紙、繊
維工業、化粧品。
Galactomannan is a neutral polysaccharide composed 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 whose main ingredient is galactomannan.
These plant gums are plant mucilages that dissolve in water.
(It has the property of exhibiting extremely high viscosity. Furthermore, galactomannan aqueous solution is nonionic and has a stable aqueous viscosity at a pH of 12 or less, and has a high aqueous viscosity even in the presence of high concentrations of various salts containing multivalent ions. Due to its ability to maintain viscosity, it is also used in the food industry, paper manufacturing, textile industry, and cosmetics.

塗料、土木建築1石油採掘、スジリー火薬初産業分野に
於て増粘剤として広く利用されている。
It is widely used as a thickener in the industrial fields of paint, civil engineering, construction, oil extraction, and gunpowder.

しかしながらこれらのガラクトマンナンは水溶液調整時
に「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
け易く経時的に腐敗し粘度低下を引起すという欠点をも
っている。
However, these galactomannans tend to cause agglomeration of powder particles called "mamako" when preparing an aqueous solution, and aqueous galactomannan solutions are easily attacked by bacteria, rotting over time, and causing a decrease in viscosity. There is.

近来かかるガラクトマンナンの欠点を是正すべく各種の
変性体が提案されている。例えば米国特許第33268
90号にはガラクトマンナンのヒドロキシアルキルエー
テルが、米国特許第2477544号にはガラクトマン
ナンのカルボキシアルキルエーテルを始めとする各種の
ガラクトマンナンのエーテル化変性体が米国特許第41
12220号にはガラクトマンナンの硝酸エステルを始
めとする各種のガラクトマンナンのエステル化変性体が
特開昭52−38039号にはガラクトマンナンの低分
子量化操作を行った各種の低粘度化ガラクトマンナン変
性体等が例示される。かかるガラクトマンナン変性体は
ガラクトマンナンが本来具備している性質に更に各種の
性能を賦与せしめたものであり各種の産業用途の目的に
応じて使い分けられて℃・る。
Recently, various modified forms of galactomannan have been proposed to correct the drawbacks of galactomannan. For example, U.S. Patent No. 33268
No. 90 discloses hydroxyalkyl ethers of galactomannan, and U.S. Pat. No. 2,477,544 discloses various etherified modified products of galactomannan including carboxyalkyl ethers of galactomannan.
No. 12220 discloses various esterified modified products of galactomannan including nitrate ester of galactomannan, and JP-A No. 52-38039 discloses various modified galactomannan to reduce viscosity by performing an operation to lower the molecular weight of galactomannan. Examples include the body. These modified galactomannans have various properties added to the inherent properties of galactomannan, and can be used depending on the purpose of various industrial applications.

従来各種のガラクトマンナン変性体を製造するにあたり
変性化剤は塩基性雰囲気下でガラクトマンナンと反応さ
せることが一般的にとられ、かかるガラクトマンナン変
性体を製造するにあたっての技術上の要点は変性化した
アルカリ性ガラクトマンナンをいかに均一に中和するか
という点にあった。従来変性ガラクトマンナンを製造す
るには水を反応媒体とするいわゆる水媒法と有機溶剤水
6・1液を反応媒体とするいわ9るスラリー法の2つの
方法に大別することができる。水媒法はガラクトマンナ
ンを塩基性下に水に溶解した状態で反応せしめるもので
あり極めて高粘度の状態で反応を進行せしめなければな
らず反応も不均一になりがちであり、更に得られた反応
生成物の中和においては高粘度物への均一な酸の添加が
極めて難しく局部的に強酸性雰囲気になって予期せぬ酸
加水分解を生じて製品の粘度低下を余儀なくされたりま
た部分的に未中和部分を生じ製品の不均一性を招くとい
った欠点があった。一方スラリー法は反応系の低粘度化
を図ることができるが、従来法に於ては反応後のスラリ
ーに酸を添加し中和を行うのであるがこの際酸として希
酸を用いた場合にはスラリー媒体中の親水性有機溶剤の
比率が中和の過程で減少する結果中和されたガラクトマ
ンナン変性物はスラリー媒体中の過剰の水によって膨潤
もしくは溶解し可動性の乏しいスラリーとなる。かかる
事実はスラリーの攪拌を困難ならしめひいては中和の不
均一化′を誘起し中和以後の精製濾過洗浄といった工程
が膨潤もしくは溶解した変性ガラクトマンナンを含む液
の状態で進行するため工程が繁雑となり、かつ、個々の
単位操作が極めて困難となる結果を招く。
Conventionally, in producing various modified galactomannans, it has generally been done to react the modifying agent with galactomannan in a basic atmosphere, and the key technical point in producing such modified galactomannans is the modification. The problem was how to uniformly neutralize the alkaline galactomannan. Conventional methods for producing modified galactomannan can be roughly divided into two methods: the so-called water medium method using water as the reaction medium and the so-called slurry method using organic solvent water 6.1 as the reaction medium. In the aqueous method, galactomannan is reacted in a state dissolved in water under basic conditions, and the reaction must proceed in an extremely highly viscous state, and the reaction tends to be non-uniform. When neutralizing a reaction product, it is extremely difficult to uniformly add acid to a highly viscous material, resulting in a locally strong acidic atmosphere, resulting in unexpected acid hydrolysis and a reduction in the viscosity of the product. However, there are disadvantages in that unneutralized portions are produced, leading to non-uniformity of the product. On the other hand, the slurry method can reduce the viscosity of the reaction system, but in the conventional method, acid is added to the slurry after the reaction to neutralize it. As a result of the ratio of the hydrophilic organic solvent in the slurry medium decreasing during the neutralization process, the neutralized galactomannan modified product swells or dissolves due to excess water in the slurry medium, resulting in a slurry with poor mobility. This fact makes it difficult to stir the slurry, which in turn causes non-uniform neutralization, and the steps after neutralization, such as purification, filtration and washing, proceed in a liquid state containing swollen or dissolved modified galactomannan, making the process complicated. This results in the individual unit operations being extremely difficult.

一方上記の弊害を避けるために中和操作を行なうに際し
濃厚な酸を用いて行う方法があるが、かかる方法は極め
て可動性に乏しい変性ガラクトマンナンの濃厚スラリー
に濃厚な酸を添加することとなるので完全に均一な中和
を行うことが難しく局部的に過剰な酸が添加される傾向
が強く変性ガラクトマンナンは局部的に強度の酸性雰囲
気にさらされ、もって生成した変性ガラクトマンナンは
酸加水分解を引起し所望とする特性を有する変性ガラク
トマンナンを得ることが難しい。
On the other hand, in order to avoid the above-mentioned disadvantages, there is a method in which a concentrated acid is used in the neutralization operation, but such a method involves adding a concentrated acid to a concentrated slurry of modified galactomannan, which has extremely poor mobility. Therefore, it is difficult to perform completely uniform neutralization, and there is a strong tendency for excessive acid to be added locally. Modified galactomannan is locally exposed to a strong acidic atmosphere, and the resulting modified galactomannan is subject to acid hydrolysis. It is difficult to obtain a modified galactomannan with desired properties.

本発明者らはかかる実情に鑑みアルカリ性ガラクトマン
ナン類を均一かつ容易に中和せしめる方法を見出すべく
鋭意研究を重ねた結果本発明を完成した。
In view of these circumstances, the present inventors have completed the present invention as a result of intensive research to find a method for uniformly and easily neutralizing alkaline galactomannans.

本発明の要旨とするところはガラクトマンナンを親水性
有機溶剤のアルカリ性水溶液中に懸濁分11ンした媒体
と二酸化炭素とを接触させることを特徴とするアルカリ
性ガラクトマンナン類の中和方法を提供することにある
The gist of the present invention is to provide a method for neutralizing alkaline galactomannans, which comprises contacting carbon dioxide with a medium in which galactomannan is suspended in an alkaline aqueous solution of a hydrophilic organic solvent. There is a particular thing.

本発明の骨子とするところは、中和剤として弱酸性かつ
常温で気体状態の物質であるところの二酸化炭素を中和
剤として用いることにある。従来中和操作で技術上の問
題点とされていたものの1つにガラクトマンナン類の分
散媒に対する膨潤性の増大、更には溶解といった不都合
な現象があった。かかる問題点は、従来ガラクトマンナ
ンの中和に伴い必然的に媒体に添加を余儀なくされてい
た水分が原因であることを本発明者らは見出しもって水
分を添加しない中和方法を本発明者らは見出したのであ
る。
The gist of the present invention is to use carbon dioxide, which is a weakly acidic substance and is in a gaseous state at room temperature, as a neutralizing agent. One of the technical problems in conventional neutralization operations has been the disadvantageous phenomenon of increased swelling and even dissolution of galactomannans in dispersion media. The present inventors discovered that this problem was caused by water, which had conventionally been unavoidably added to the medium when neutralizing galactomannan.The present inventors developed a neutralization method that does not add water. was discovered.

本発明の方法は中和剤として二酸化炭素を用いるので水
分に由来するガラクトマンナンの中和工程に於ける媒体
に対する膨潤性の増大ひいては溶解に至る工程通過性の
悪化を軽重することなく平易かつ良好な中和操作が行え
るのである。
Since the method of the present invention uses carbon dioxide as a neutralizing agent, it is simple and effective without considering the increase in swelling property of galactomannan derived from water in the medium and the deterioration of process passability leading to dissolution. Neutralization operations can be performed.

従来法の問題点の第二は可動性に乏しい高濃度スラリー
状態のガラクトマンナン類への液状中和剤の添加によっ
て生ずる中和の不均一性及び局部的な酸過剰雰囲気にお
ける製品特性の変化にあった。
The second problem with the conventional method is the non-uniformity of neutralization caused by the addition of a liquid neutralizing agent to highly concentrated slurry galactomannans with poor mobility and changes in product properties in localized acid-rich atmospheres. there were.

かかる問題点は従来の中和操作が液状中和剤を用いてい
た点に由来している。すなわち、かかる中和操作におい
て液状中和剤を用いた場合には該スラリーに中和剤を添
加した瞬間に中和反応が極めて高速に進行し可動性に乏
しい高濃度スラリー状態のガラクトマンナン類スラリー
に中和剤を添加した時に発生する局部的に中和剤濃度の
高い部分が係る中和の不拘−性更には酸加水分解による
ガラクトマンナンの劣悪化を引起している。
This problem stems from the fact that conventional neutralization operations use liquid neutralizing agents. That is, when a liquid neutralizing agent is used in such a neutralization operation, the neutralization reaction proceeds at an extremely high speed the moment the neutralizing agent is added to the slurry, resulting in a galactomannan slurry in the form of a highly concentrated slurry with poor mobility. The locally high concentration of neutralizing agent that occurs when a neutralizing agent is added to the gel causes irresponsibility of neutralization, and also causes deterioration of galactomannan due to acid hydrolysis.

本発明の実施に際して用いる中和剤は常温で気体状態に
ありかつ水分に溶解し弱酸性を示す二酸化炭素であり、
中和はスラリーの気液界面より進行し、かつ実質的な中
和速度は二酸化炭素の高濃18スラリーへの溶解速度に
依存する。二酸化炭素は高濃度スラリーへ添加された場
合、高濃度スラリー中に含有する水分を反応して始めて
酸となり中和剤としての性能を発揮するものであるから
たとえ一度に大量の二酸化炭素がスラリーへ添加された
場合にあっても中和は適度に緩慢かつ気液界面の転移に
よって均一に行われ更には強度な酸との接触に由来する
酸加水分解等の製品として好ましくないような現象をも
防ぐことができるのである。
The neutralizing agent used in carrying out the present invention is carbon dioxide, which is in a gaseous state at room temperature, dissolves in water, and exhibits weak acidity.
Neutralization proceeds from the gas-liquid interface of the slurry, and the actual neutralization rate depends on the rate of dissolution of carbon dioxide into the highly concentrated 18 slurry. When carbon dioxide is added to a highly concentrated slurry, it becomes an acid only after it reacts with the water contained in the highly concentrated slurry and exhibits its performance as a neutralizing agent. Therefore, even if a large amount of carbon dioxide is added to the slurry at once, Even when it is added, neutralization is carried out moderately slowly and uniformly by transition at the gas-liquid interface, and it also does not cause undesirable phenomena as a product, such as acid hydrolysis caused by contact with strong acids. It can be prevented.

従って、本発明の中和方法を用いることにより、従来困
難とされていたアルカリ性ガラクトマンナンの中和工程
を極めて平易かつ円滑に通過せしめることができ更に中
和以後の固液分離、精製、洗浄、乾燥といった操作をも
極めて容易に進行せしめることができるのである。
Therefore, by using the neutralization method of the present invention, it is possible to pass through the neutralization process of alkaline galactomannan, which has been considered difficult in the past, very easily and smoothly. Operations such as drying can also proceed extremely easily.

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ットの状態で
あっても、細かく粉砕した粉状にした未精製のものであ
ってもよい。また、粉状のガラクトマンナンをエーテル
、ベンゼン、アルコール等にて精製したものであっても
よく更に熱分解、酸化分解、酵素分解、酸加水分解等の
操作を施し分子量を低下せしめたガラクトマンナンをも
使用することができまた、ガラクトマンナンな骨格とし
てもつ各種の変性体、例えばガラクトマンナンの各種の
エーテル化誘導体、エステル化誘導体、グラフト共重合
体等、更に架橋剤等で変性されたが如き高分子量化もし
くは高粘度化ガラクトマンナンをも含むものである。
The form of the galactomannan used in carrying out the present invention may be in the so-called split state obtained by coarsely pulverizing beans, or in the unrefined form obtained by finely pulverizing it into powder. It may also be a powdered galactomannan purified with ether, benzene, alcohol, etc., and a galactomannan whose molecular weight has been lowered by further operations such as thermal decomposition, oxidative decomposition, enzymatic decomposition, acid hydrolysis, etc. In addition, various modified products having a galactomannan skeleton, such as various etherified derivatives, esterified derivatives, and graft copolymers of galactomannan, as well as high It also includes galactomannan with increased molecular weight or increased viscosity.

本発明を実施するに際して用いる親水性有機溶剤とは少
なくとも水を30重量係含有した状態で水と分離せずに
水と混合しうる有機溶剤であり、また、かかる有機溶剤
はガラクトマンナン、塩基性物質更に変性ガラクトマン
ナンの中和にあたっては変性化剤に対して反応しにくい
ものであることが好ましい。代表的な親水性有機溶剤と
してはメタノール、エタノール、プロノくノール、ブタ
ノールなどのアルコール類、アセトン、メチルエチルケ
トンなどのケトン類及びそれらの混合物を具体的に例示
することができる。
The hydrophilic organic solvent used in carrying out the present invention is an organic solvent that contains at least 30% water by weight and can be mixed with water without separating from the water, and such organic solvents include galactomannan, basic Furthermore, when neutralizing the modified galactomannan, it is preferable that the material is one that does not easily react with the modifying agent. Specific examples of typical hydrophilic organic solvents include alcohols such as methanol, ethanol, pronophenol and butanol, ketones such as acetone and methyl ethyl ketone, and mixtures thereof.

本発明を実施するに際して用いるアルカリ性水浴液とは
塩基性物質を水に溶解せしめたものであり、かかる塩基
性物質としてはアルカリ金属水酸化物、アルカリ土類水
酸化物、アンモニア、アミン類、第4級アンモニウム化
合物が例示される。
The alkaline bath liquid used in carrying out the present invention is one in which a basic substance is dissolved in water, and such basic substances include alkali metal hydroxides, alkaline earth hydroxides, ammonia, amines, and alkaline metal hydroxides. Quaternary ammonium compounds are exemplified.

本発明を実施するに際して用いる二酸化炭素としては、
ドライアイス二酸化炭素ガスの他に加熱もしくは分解に
よって容易に二酸化炭素を発生する物質より発生する二
酸化炭素をも含むものである。更には炭化水素類炭水化
物類など完全燃焼して二酸化炭素及び水を生ずる物質の
燃焼ガスをも含む。かかる二酸化炭素は一度にスラリー
系に添加することも可能であるが徐々に添加する方法を
採用するのが好ましい。二酸化炭素の添加方法としては
、スラリー媒体中へのノ(プリング加圧溶解等の方法を
とることができるが、スラリー系が充分攪拌されている
限り常圧における通常の液面接触の方式で充分にその目
的を達成することができる。また中和にあたってのスラ
リーの攪拌方式としては通常の回転攪拌翼方式、ブレン
ダ一方式。
Carbon dioxide used in carrying out the present invention includes:
In addition to dry ice carbon dioxide gas, it also contains carbon dioxide generated from substances that easily generate carbon dioxide when heated or decomposed. It also includes combustion gases of substances such as hydrocarbons and carbohydrates that can be completely combusted to produce carbon dioxide and water. Although it is possible to add carbon dioxide to the slurry system all at once, it is preferable to add it gradually. Carbon dioxide can be added to the slurry medium by pulling or dissolving under pressure, but as long as the slurry system is sufficiently stirred, the normal surface contact method at normal pressure is sufficient. This purpose can be achieved. Also, the slurry stirring method used for neutralization is the usual rotating stirring blade method or the blender one-way method.

ニーダ一方式等が例示されるがそのいずれも用(・るこ
とかできる。また中和は常圧下、加圧下(・ずれも可能
である。加圧下に二酸化炭素の添加を行った方が常圧で
行ったものに較べ中和がより良好に行われるが、通常の
場合常圧による添加によって充分に中和は行われる。
One-type kneaders are exemplified, but any of these can be used.Also, neutralization can be carried out under normal pressure or under pressure.It is usually better to add carbon dioxide under pressure. Neutralization is carried out better than when carried out under pressure, but neutralization is usually effected sufficiently by addition under normal pressure.

本発明にかかる中和方法はガラクトマンナンのみならず
ガラクトマンナンの各種変性体を製造する際に生ずる塩
基性物質の中和に用いることができ、しかもかかる場合
にきわめて自然な形で各種のアルカリ性ガラクトマンナ
ン類を中和せしめることができる。
The neutralization method according to the present invention can be used to neutralize basic substances generated when producing not only galactomannan but also various modified forms of galactomannan. It can neutralize mannans.

以下実施例により更に詳しく説明する。This will be explained in more detail below with reference to Examples.

実施例1 攪拌様滴下ロート冷却器付の内容積1tのフラスコにア
セトン801nlと水50tnlとグアガム粉末100
2を仕込み攪拌下にスラリーを形成した。
Example 1 801 nl of acetone, 50 tnl of water, and 100 g of guar gum powder were placed in a flask with an internal volume of 1 t equipped with a stirring-like dropping funnel condenser.
2 was added to form a slurry with stirring.

しかるのち32の水酸化ナトリウムを水20rnlとア
セトン20−の混合液に溶解した水酸化ナトリウム溶液
を滴下ロートより徐々に滴下した。しかるのち室温で8
時間攪拌を行った。その後二酸化炭素ガスをボンベより
該フラスコ内スラリ:に導き室温で1分+nlに100
ccの割合で常圧下にバブリングさせながら中和を行っ
た。かかる操作を20分にわたって行った。かかる中和
操作は極めて平易かつ均一に行われた。しかるのち内容
物を取出し濾過後80チアセトン水溶液で洗浄し、再び
濾過後アセトン100−で洗浄してから、濾過。
Thereafter, a sodium hydroxide solution prepared by dissolving No. 32 sodium hydroxide in a mixture of 20 rnl of water and 20 rnl of acetone was gradually added dropwise from the dropping funnel. After that, at room temperature 8
Stirring was performed for hours. After that, carbon dioxide gas was introduced from the cylinder into the slurry in the flask at room temperature for 1 minute + 100 nm to nl.
Neutralization was performed while bubbling under normal pressure at a rate of cc. This operation was carried out for 20 minutes. This neutralization operation was performed extremely easily and uniformly. Thereafter, the contents were taken out, filtered, washed with an aqueous solution of 80% thiacetone, filtered again, washed with 100% acetone, and then filtered.

乾燥、粉砕を行った。かくして得られたグアガム粉末の
絶乾換算1チ水溶液のpHは98であった。
Drying and pulverization were performed. The pH of the aqueous solution of guar gum powder obtained in this way was 98 on an absolute dry basis.

実施例2 内容積1tの加熱及び加圧が可能なニーダ−に2プロパ
ツール100−と水40−とローカストビーンガム粉末
100りを仕込み攪拌下にスラリーを形成した。しかる
のち32の水酸化ナトリウムを水207!2プロパツー
ル20m1の混合液に溶解した水酸化ナトリウム溶液を
徐々に滴下した。
Example 2 In a kneader having an internal volume of 1 ton and capable of heating and pressurizing, 100 g of 2proper tool, 40 g of water, and 100 g of locust bean gum powder were charged and stirred to form a slurry. Thereafter, a sodium hydroxide solution prepared by dissolving 32 parts of sodium hydroxide in a mixture of 20 parts of water and 20 parts of propatool was gradually added dropwise.

しかるのち室温で3時間攪拌を行った。その後20気圧
の二酸化炭素ガスをボyべよりニーダ−に導き中和を行
った。中和に消費された二酸化炭素量は2.0気圧の状
態でILであった。中和は極めて均一かつ容易に進行し
た。しかるのち濾過し、80%2プロパツール水溶液1
5〇−中で洗浄し再び濾過し更に2プロパツ一ル100
m7!で洗浄しテカら濾過、乾燥、粉砕を行いローカス
トビーンガム粉末を得た。かがるローカストビーンガム
粉末を絶乾換算で509とり500 ccの給水に分散
し80℃で溶解させた。かかる水溶液のpHは10.0
であった。
Thereafter, the mixture was stirred at room temperature for 3 hours. Thereafter, carbon dioxide gas at 20 atm was introduced from the boiler into the kneader for neutralization. The amount of carbon dioxide consumed for neutralization was IL at 2.0 atm. Neutralization proceeded extremely uniformly and easily. After that, filter and add 80% 2propatool aqueous solution 1
50 - Wash in a medium, filter again, and add 2 protons of 100
m7! Locust bean gum powder was obtained by washing, filtering, drying, and pulverizing. Kagaru locust bean gum powder was dispersed in 500 cc of water on an absolute dry basis and dissolved at 80°C. The pH of this aqueous solution is 10.0
Met.

実施例3 実施例2で用いたものと同様な加圧加熱可能なニーダー
に100−の2グロバノールと20−の水と水分率12
チのグアガム粉末を仕込み攪拌して均一な懸濁分散液を
作成した。その後水酸化ナトリウム3fを307!の水
に溶解した水酸化ナトリウム水溶液を徐々に添加攪拌し
た。その後ニーグー内を窒素で置換し1時間攪拌後15
9のプロピレンオキサイドを定量ポンプにより圧入添加
し、ニーダ−を80℃に昇温し3時間反応を続けた。
Example 3 In a pressurized and heated kneader similar to that used in Example 2, 100-2 globanol, 20-globanol, and water with a moisture content of 12 were added.
A uniform suspension and dispersion was prepared by adding guar gum powder and stirring. Then add 3f of sodium hydroxide to 307! An aqueous solution of sodium hydroxide dissolved in water was gradually added and stirred. After that, the inside of Nigu was replaced with nitrogen and stirred for 1 hour.
Propylene oxide No. 9 was added under pressure using a metering pump, the temperature of the kneader was raised to 80° C., and the reaction was continued for 3 hours.

その後ニーダ−内部を35℃以下に冷却し攪拌下に再び
窒素置換を行ってから、常温常圧換算2.5tの二酸化
炭素を添加した。しかるのち内容物を取出し濾過し更に
200 mの80チ2プロパツール水溶液で洗浄し濾過
し更に100mの2グロパメール水溶液で洗浄、濾過し
た。その後乾燥、粉砕を行ってグアガムのヒドロキシグ
ロビルエーテル化物を得た。かかるグアガムのヒドロキ
シグロビルエーテル化物の絶乾換算1%水溶液のpHは
9.5であった。
Thereafter, the inside of the kneader was cooled to 35° C. or below, nitrogen substitution was performed again while stirring, and then 2.5 t of carbon dioxide (calculated at room temperature and pressure) was added. Thereafter, the contents were taken out, filtered, washed with 200 m of 80 2-propamel aqueous solution, filtered, and further washed and filtered with 100 m of 2-gropamel aqueous solution. Thereafter, it was dried and pulverized to obtain a hydroxyglobyl etherified product of guar gum. The pH of a 1% aqueous solution of the hydroxyglobyl etherified product of guar gum was 9.5.

特 許 出 願 人 三菱アセテート株式会社(ほか1
名) 代理人 弁理士 1)村 武 敏
Patent applicant: Mitsubishi Acetate Co., Ltd. (and 1 others)
Name) Agent Patent Attorney 1) Takeshi Mura

Claims (1)

【特許請求の範囲】[Claims] ガラクトマンナンを親水性有機溶剤のアルカリ性水溶液
中に懸濁分散した媒体に二酸化炭素を接触させることを
特徴とするアルカリ性ガラクトマンナン類の中和方法。
A method for neutralizing alkaline galactomannans, which comprises bringing carbon dioxide into contact with a medium in which galactomannan is suspended and dispersed in an alkaline aqueous solution of a hydrophilic organic solvent.
JP333082A 1982-01-14 1982-01-14 Neutralization of alkaline galactomannan Granted JPS58120603A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP333082A JPS58120603A (en) 1982-01-14 1982-01-14 Neutralization of alkaline galactomannan

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP333082A JPS58120603A (en) 1982-01-14 1982-01-14 Neutralization of alkaline galactomannan

Publications (2)

Publication Number Publication Date
JPS58120603A true JPS58120603A (en) 1983-07-18
JPH0140842B2 JPH0140842B2 (en) 1989-08-31

Family

ID=11554337

Family Applications (1)

Application Number Title Priority Date Filing Date
JP333082A Granted JPS58120603A (en) 1982-01-14 1982-01-14 Neutralization of alkaline galactomannan

Country Status (1)

Country Link
JP (1) JPS58120603A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011219564A (en) * 2010-04-06 2011-11-04 Kao Corp Method for producing powdered polysaccharide derivative

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011219564A (en) * 2010-04-06 2011-11-04 Kao Corp Method for producing powdered polysaccharide derivative

Also Published As

Publication number Publication date
JPH0140842B2 (en) 1989-08-31

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