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JPH0140842B2 - - Google Patents
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JPH0140842B2 - - Google Patents

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Publication number
JPH0140842B2
JPH0140842B2 JP333082A JP333082A JPH0140842B2 JP H0140842 B2 JPH0140842 B2 JP H0140842B2 JP 333082 A JP333082 A JP 333082A JP 333082 A JP333082 A JP 333082A JP H0140842 B2 JPH0140842 B2 JP H0140842B2
Authority
JP
Japan
Prior art keywords
galactomannan
neutralization
slurry
carbon dioxide
water
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
JP333082A
Other languages
Japanese (ja)
Other versions
JPS58120603A (en
Inventor
Naoki Mochida
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 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)

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つて水に溶解して
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つ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、塗
料、土木建築、石油採掘、火薬等の産業分野に於
て増粘剤として広く利用されている。
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 typical plant gums whose main component is galactomannan.These plant gums are plant mucilages that dissolve in water. It has the property of exhibiting extremely high viscosity. Furthermore, the galactomannan aqueous solution is nonionic, has a stable aqueous viscosity at a pH of 12 or less, and can maintain a high aqueous viscosity even in the presence of high concentrations of various salts containing multivalent ions. Because of these properties, it is widely used as a thickening agent in the food field and industrial fields such as paper manufacturing, textile industry, cosmetics, paints, civil engineering and construction, oil mining, and explosives.

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つている。
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. I have it too.

近年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3326890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4112220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
を行つ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いる。
In recent years, various modified forms of galactomannan have been proposed to correct the drawbacks of galactomannan. For example, U.S. Patent No. 3,326,890 describes hydroxyalkyl ethers of galactomannan, U.S. Pat. Various esterified modified products of galactomannan, including nitrate ester of galactomannan, have been disclosed in Japanese Patent Application Laid-open No. 1983-
No. 38039 exemplifies various viscosity-lowering galactomannan modified products obtained by performing operations to lower the molecular weight of galactomannan. Such modified galactomannans have various performances added to the inherent properties of galactomannan, and are 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つて
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
つた。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
溶液を反応媒体とするいわゆるスラリー法の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つ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
くといつた欠点があつた。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つて膨潤も
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撹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
浄といつ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 galactomannan products, it has generally been done to react the modifying agent with galactomannan in a basic atmosphere, and the following are the technical points in producing such modified galactomannan products. The problem was how to uniformly neutralize denatured alkaline galactomannan. Conventionally, methods for producing modified galactomannan can be roughly divided into two methods: the so-called aqueous method using water as the reaction medium, and the so-called slurry method using an aqueous organic solvent solution 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 that may cause unexpected acid hydrolysis, which may force a decrease in the viscosity of the product, or The drawback was that unneutralized portions were 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 proportion of 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 processes such as purification, filtration and washing after neutralization proceed in a liquid state containing swollen or dissolved modified galactomannan. The result is that the process becomes complicated and individual unit operations become 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、もつ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 acid-hydrated. This causes decomposition and makes it 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
散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 and dispersed in an alkaline aqueous solution of a hydrophilic organic solvent. be.

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、更には溶解といつた不都合な現象があつ
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
つ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 with conventional neutralization operations
Another disadvantageous phenomenon was increased swelling and even dissolution of galactomannans in the dispersion medium. The present inventors discovered that this problem was caused by water, which had conventionally been unavoidably added to the medium when neutralizing galactomannan, and developed a neutralization method that does not add water. They found out.

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経由することなく平
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 easy to use, without increasing the swelling property of galactomannan derived from water in the medium and deteriorating 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
剤の添加によつ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つ
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 the problem of poor product properties in a localized acid-rich atmosphere. It was a change.

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
分が係る中和の不均一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. When a neutralizing agent is added to the galactomannan, the locally high concentration of the neutralizing agent occurs in the non-uniformity of the neutralization, and furthermore, the deterioration of the galactomannan due to acid hydrolysis is caused.

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
度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
れた場合にあつても中和は適度に緩慢かつ気液界
面の転移によつ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
しくないような現性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 is It depends on the rate of dissolution of carbon dioxide into the concentrated 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 moderately slow and uniform due to transition at the gas-liquid interface, and furthermore, it does not exhibit undesirable effects as a product, such as acid hydrolysis caused by contact with strong acids. It can also prevent sex.

従つて、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、乾燥といつ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 be carried out 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
リツトの状態であつても、細かく粉砕した粉状に
した未精製のものであつてもよい。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つてもよく更に熱分
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、ガラクトマンナンを骨
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 form of so-called splits obtained by coarsely pulverizing beans, or in the form of unrefined particles obtained by finely pulverizing beans. It may also be a powdered galactomannan purified with ether, benzene, alcohol, etc. Galactomannan may be further subjected to thermal decomposition, oxidative decomposition, enzymatic decomposition, acid hydrolysis, etc. to reduce its molecular weight. In addition, various modified products having galactomannan as a backbone, 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%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つて
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、プロパノール、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% by weight of water and can be mixed with water without separating from it, and such organic solvents include galactomannan, basic When neutralizing the modified galactomannan, it is preferable that the material be less reactive to the modifying agent. Specific examples of typical hydrophilic organic solvents include alcohols such as methanol, ethanol, propanol 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
溶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 aqueous solution 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, quaternary An example is a class ammonium compound.

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つ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バブリング加圧溶
解等の方法をとることができるが、スラリー系が
充分撹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。また中和にあたつてのスラリーの撹拌方式
としては通常の回転撹拌翼方式、ブレンダー方
式、ニーダー方式等が例示されるがそのいずれも
用いることができる。また中和は常圧下、加圧下
いずれも可能である。加圧下に二酸化炭素の添加
を行つた方が常圧で行つ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
よつて充分に中和は行われる。
In addition to dry ice and carbon dioxide gas, the carbon dioxide used in carrying out the present invention includes carbon dioxide generated from substances that easily generate carbon dioxide upon heating or decomposition. 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 by methods such as bubbling into the slurry medium and dissolving under pressure, but as long as the slurry system is sufficiently stirred, the usual liquid surface contact method at normal pressure is sufficient to add carbon dioxide. Able to achieve purpose. Examples of the slurry stirring method for neutralization include the usual rotating stirring blade method, blender method, kneader method, etc., and any of these methods can be used. Further, neutralization can be carried out either under normal pressure or under increased pressure. Neutralization is better carried out when carbon dioxide is added under pressure than when it is carried out at normal pressure, but neutralization is usually achieved sufficiently by addition at 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 撹拌機滴下ロート冷却器付の内容積1のフラ
スコにアセトン80mlと水50mlとグアガム粉末100
gを仕込み撹拌下にスラリーを形成した。しかる
のち3gの水酸化ナトリウムを水20mlとアセトン
20ml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時間撹拌を行つた。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ーに導き室温で1
分間に100c.c.の割合で常圧下にバブリングさせな
がら中和を行つた。かかる操作を20分にわたつて
行つた。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%
アセトン水溶液で洗浄し、再び濾過後アセトン
100mlで洗浄してから、濾過、乾燥、粉砕を行つ
た。かくして得られたグアガム粉末の絶乾換算1
%水溶液のPHは9.8であつた。
Example 1 80 ml of acetone, 50 ml of water, and 100 ml of guar gum powder are added to a flask with an internal volume of 1 and equipped with a stirrer, dropping funnel, and condenser.
A slurry was formed under stirring. Then, add 3g of sodium hydroxide to 20ml of water and acetone.
A sodium hydroxide solution dissolved in 20 ml of the mixed liquid was gradually added dropwise from the dropping funnel. Thereafter, the mixture was stirred at room temperature for 8 hours. After that, carbon dioxide gas was introduced from the cylinder into the slurry in the flask at room temperature.
Neutralization was carried out by bubbling under normal pressure at a rate of 100 c.c. per minute. This operation was carried out for 20 minutes. This neutralization operation was performed extremely easily and uniformly. Afterwards, remove the contents and filter 80%.
Wash with acetone aqueous solution, filter again and then add acetone
After washing with 100 ml, filtration, drying, and pulverization were performed. The absolute dryness of the guar gum powder thus obtained is 1
% aqueous solution was 9.8.

実施例 2 内容積1の加熱及び加圧が可能なニーダーに
2プロパノール100mlと水40mlとローカストビー
ンガム粉末100gを仕込み撹拌下にスラリーを形
成した。しかるのち3gの水酸化ナトリウムを水
20ml2プロパノール20ml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。しかるのち
室温で3時間撹拌を行つた。その後2.0気圧の二
酸化炭素ガスをボンベよりニーダーに導き中和を
行つた。中和に消費された二酸化炭素量は2.0気
圧の状態で1であつた。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
パノール水溶液150ml中で洗浄し再び濾過し更に
2プロパノール100mlで洗浄してから濾過、乾燥、
粉砕を行いローカストビーンガム粉末を得た。か
かるローカストビーンガム粉末を絶乾換算で5.0
gとり500c.c.の絶水に分散し80℃で溶解させた。
かかる水溶液のPHは10.0であつた。
Example 2 100 ml of 2-propanol, 40 ml of water, and 100 g of locust bean gum powder were charged into a kneader having an internal volume of 1 and capable of heating and pressurizing, and a slurry was formed under stirring. Then, add 3g of sodium hydroxide to water.
A solution of sodium hydroxide dissolved in a mixture of 20 ml and 20 ml of 2-propanol was slowly added dropwise. Thereafter, the mixture was stirred at room temperature for 3 hours. Thereafter, carbon dioxide gas at 2.0 atm was introduced from the cylinder into the kneader for neutralization. The amount of carbon dioxide consumed for neutralization was 1 at 2.0 atm. Neutralization proceeded extremely uniformly and easily. After that, it was filtered, washed in 150 ml of an 80% aqueous 2-propanol solution, filtered again, further washed with 100 ml of 2-propanol, filtered, dried,
It was pulverized to obtain locust bean gum powder. This locust bean gum powder is 5.0% on an absolute dry basis.
It was dispersed in 500 c.c. of pure water and dissolved at 80°C.
The pH of this aqueous solution was 10.0.

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100mlの2プロパノールと20mlの水と
水分率12%のグアガム粉末を仕込み撹拌して均一
な懸濁分散液を作成した。その後水酸化ナトリウ
ム3gを30mlの水に溶解した水酸化ナトリウム水
溶液を徐々に添加撹拌した。その後ニーダー内を
窒素で置換し1時間撹拌後15g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、ニーダー
を80℃に昇温し3時間反応を続けた。その後ニー
ダー内部を35℃以下に冷却し撹拌下に再び窒素置
換を行つてから、常温常圧換算2.5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200mlの80%2プロパノール水溶液で洗浄し
濾過し更に100mlの2プロパノール水溶液で洗浄、
濾過した。その後乾燥、粉砕を行つてグアガムの
ヒドロキシプロピルエーテル化物を得た。かかる
グアガムのヒドロキシプロピルエーテル化物の絶
乾換算1%水溶液のPHは9.5であつた。
Example 3 In a pressurized and heatable kneader similar to that used in Example 2, 100 ml of 2-propanol, 20 ml of water, and guar gum powder with a moisture content of 12% were charged and stirred to create a uniform suspension dispersion. . Thereafter, a sodium hydroxide aqueous solution prepared by dissolving 3 g of sodium hydroxide in 30 ml of water was gradually added and stirred. Thereafter, the inside of the kneader was purged with nitrogen, and after stirring for 1 hour, 15 g of propylene oxide 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. Thereafter, the inside of the kneader was cooled to 35° C. or lower, nitrogen substitution was performed again with stirring, and then 2.5 carbon dioxide (calculated at room temperature and pressure) was added. After that, the contents were taken out, filtered, washed with 200 ml of 80% 2-propanol aqueous solution, filtered, and further washed with 100 ml of 2-propanol aqueous solution.
Filtered. Thereafter, it was dried and pulverized to obtain a hydroxypropyl etherified product of guar gum. The pH of a 1% aqueous solution of the hydroxypropyl etherified guar gum on bone dry basis was 9.5.

Claims (1)

【特許請求の範囲】[Claims] 1 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。
1. 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 Method for neutralizing alkaline galactomannans Granted JPS58120603A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP333082A JPS58120603A (en) 1982-01-14 1982-01-14 Method for neutralizing alkaline galactomannans

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP333082A JPS58120603A (en) 1982-01-14 1982-01-14 Method for neutralizing alkaline galactomannans

Publications (2)

Publication Number Publication Date
JPS58120603A JPS58120603A (en) 1983-07-18
JPH0140842B2 true 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 Method for neutralizing alkaline galactomannans

Country Status (1)

Country Link
JP (1) JPS58120603A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5771360B2 (en) * 2010-04-06 2015-08-26 花王株式会社 Method for producing powdered polysaccharide derivative

Also Published As

Publication number Publication date
JPS58120603A (en) 1983-07-18

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