JP2000026503A - Non-volatile organic solvent-containing xanthan gum and its production - Google Patents

Non-volatile organic solvent-containing xanthan gum and its production

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Publication number
JP2000026503A
JP2000026503A JP10190905A JP19090598A JP2000026503A JP 2000026503 A JP2000026503 A JP 2000026503A JP 10190905 A JP10190905 A JP 10190905A JP 19090598 A JP19090598 A JP 19090598A JP 2000026503 A JP2000026503 A JP 2000026503A
Authority
JP
Japan
Prior art keywords
xanthan gum
organic solvent
volatile organic
nonvolatile
gum containing
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
JP10190905A
Other languages
Japanese (ja)
Other versions
JP4462659B2 (en
Inventor
Junichi Inata
淳一 生稲
Yuko Terui
優子 照井
Makoto Arimoto
真 有本
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.)
Nisshin Oil Mills Ltd
Original Assignee
Nisshin Oil Mills Ltd
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Publication date
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Priority to JP19090598A priority Critical patent/JP4462659B2/en
Publication of JP2000026503A publication Critical patent/JP2000026503A/en
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Publication of JP4462659B2 publication Critical patent/JP4462659B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Polysaccharides And Polysaccharide Derivatives (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain xanthan gum having high viscosity characteristic, excellent resistance to salt when made into an aqueous solution and uniform dispersibility into water and useful as a thickener in a food filed, a cosmetic field and an agrochemical field, etc., a stabilizer or an additive. SOLUTION: The objective xanthan gum is obtained by heating xanthan gum containing >=0.01 wt.% of non-volatile organic solvent preferably having >=120 deg.C boiling point and <=90 deg.C melting point and preferably as a solvent (e.g. 1,3-butylene glycol) having more than one kind of substituting group selected from an ester group, hydroxy group and carboxy group at >=80 deg.C, preferably 120-150 deg.C for 15 min-4 hrs. Preferably, the heating treatment is performed after spraying the non-volatile organic solvent to the xanthan gum in the air.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は不揮発性有機溶媒含
有キサンタンガムおよびその製造方法に関する。かかる
改質キサンタンガムは、食品分野、化粧品分野、農薬分
野、医薬品分野または石油分野において増粘剤、安定化
剤、添加剤として用いられる。
The present invention relates to a xanthan gum containing a nonvolatile organic solvent and a method for producing the same. Such a modified xanthan gum is used as a thickener, a stabilizer, and an additive in the food field, cosmetics field, agrochemical field, pharmaceutical field, or petroleum field.

【0002】[0002]

【従来の技術】キサンタンガムは、微生物キサントモナ
ス・カンペストリス(Xanthomoas camp
estris)により、澱粉、グルコース、ショ糖等の
炭水化物からつくられる微生物多糖類の一種である。キ
サンタンガムの構造は、主としてD−グルコース、D−
マンノースおよびD−グルクロン酸のナトリウム、カリ
ウムおよびカルシウム塩からなり、主鎖はD−グルコー
スのβ−1,4結合からなる。キサンタンガムの製造方
法として、発酵工程の後、微生物を殺菌するために熱処
理され、そのアルコールを取り除き、乾燥、粉砕する方
法などが知られている。キサンタンガムは塩に対して安
定で、しかも、塩を添加することで水溶液が増粘するこ
とが知られている。また、特開平10−33125公報
には、キサンタンガムの粘度を向上させるために、キサ
ンタンガム粉末を加熱乾燥させる方法が開示されてい
る。
2. Description of the Related Art Xanthan gum is obtained from the microorganism Xanthomonas campestris.
estris) is a kind of microbial polysaccharide produced from carbohydrates such as starch, glucose, and sucrose. The structure of xanthan gum mainly consists of D-glucose and D-glucose.
It consists of the sodium, potassium and calcium salts of mannose and D-glucuronic acid, and the main chain consists of the β-1,4 linkage of D-glucose. As a method for producing xanthan gum, a method is known in which after a fermentation step, heat treatment is performed to sterilize microorganisms, the alcohol is removed, and drying and pulverization are performed. It is known that xanthan gum is stable against salts, and that addition of salts increases the viscosity of an aqueous solution. Japanese Patent Application Laid-Open No. 10-33125 discloses a method of drying xanthan gum powder by heating in order to improve the viscosity of xanthan gum.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、従来の
加熱乾燥法では、キサンタンガム水溶液の粘度は上昇す
るが、塩添加により沈澱するなど耐塩性が悪化すること
がわかった。また、水への分散性は「ままこ」ができに
くく、良好に見えるが、微視的には不均一となる。その
ため、加熱乾燥法で得られたキサンタンガムは未加熱乾
燥品に比べて局所的に濃度が濃い部分と薄い部分がで
き、粘度にむらができ、さらに白濁するなどの問題点が
あった。
However, it has been found that in the conventional heat drying method, although the viscosity of the aqueous xanthan gum solution increases, the salt resistance deteriorates, such as precipitation due to salt addition. In addition, the dispersibility in water is difficult to "makoko" and looks good, but becomes microscopically non-uniform. For this reason, the xanthan gum obtained by the heat drying method has a problem in that locally high and low density parts are formed as compared with the non-heat-dried product, the viscosity becomes uneven, and furthermore, it becomes cloudy.

【0004】[0004]

【発明が解決するための手段】本発明者らは、かかる問
題を達成するために、鋭意研究を重ねた結果、キサンタ
ンガムの耐塩性や均一分散が、キサンタンガムと不揮発
性有機溶媒を混合し、さらに加熱することで、優れた耐
塩性および均一水分散を有することを見いだし本発明を
完成した。即ち、かかる本発明は、キサンタンガムと不
揮発性有機溶媒の混合粒子を加熱処理したことを特徴と
する不揮発性有機溶媒含有キサンタンガムおよびその製
造方法である。なお、本発明の不揮発性有機溶媒含有キ
サンタンガムはキサンタンガム濃度として0.5重量%
の水溶液とした場合、2000〜30000mPa・s
(B型粘度計6rpm 25℃)の粘度を示すが、定量
が難しい耐塩性や水均一分散性も本発明により向上す
る。本発明の不揮発性有機溶媒含有キサンタンガムは、
一般に、キサンタンガムとキサンタンガムに対して0.
01重量%以上の不揮発性有機溶媒を混合し、さらに8
0℃以上で加熱することによって得ることができる。上
記加熱は、不揮発性有機溶媒中もしくは不揮発性有機溶
媒含有有機溶媒中もしくはキサンタンガムに不揮発性有
機溶媒を添加して行うことができる。高温で処理した方
が効果的であるが、着色しやすく、特に空気中等酸素の
存在下で行うと着色する恐れがあるので、不活性ガス中
で加熱処理を行うのが良い。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies in order to achieve such a problem. As a result, the salt resistance and uniform dispersion of xanthan gum have been improved by mixing xanthan gum and a nonvolatile organic solvent. By heating, they found that they had excellent salt resistance and uniform water dispersion, and completed the present invention. That is, the present invention relates to a xanthan gum containing a non-volatile organic solvent, which is obtained by heat-treating mixed particles of xanthan gum and a non-volatile organic solvent, and a method for producing the same. The xanthan gum containing a nonvolatile organic solvent of the present invention has a xanthan gum concentration of 0.5% by weight.
2000 to 30000 mPa · s
(B-type viscometer, 6 rpm, 25 ° C.), but salt resistance and water uniform dispersibility, which are difficult to quantify, are also improved by the present invention. The nonvolatile organic solvent-containing xanthan gum of the present invention,
Generally, xanthan gum and 0.1% for xanthan gum.
More than 8% by weight of a non-volatile organic solvent
It can be obtained by heating at 0 ° C. or higher. The heating can be performed in a nonvolatile organic solvent, in a nonvolatile organic solvent-containing organic solvent, or by adding a nonvolatile organic solvent to xanthan gum. Although it is more effective to perform the treatment at a high temperature, it is easy to color, and particularly when subjected to the presence of oxygen such as in air, the coloring may occur. Therefore, the heat treatment is preferably performed in an inert gas.

【0005】[0005]

【発明の実施の形態】以下に、本発明を詳細に説明す
る。上述のごとく、本発明の不揮発性有機溶媒含有キサ
ンタンガムは、一般に、キサンタンガムとキサンタンガ
ムに対して0.01重量%以上の不揮発性有機溶媒を混
合し、さらに80℃以上で加熱することによって得るこ
とができる。本発明の不揮発性有機溶媒含有キサンタン
ガムを製造するのに使用する原料キサンタンガムとして
は、まず市販の粉末状、顆粒状等のキサンタンガムを用
いることができる。かかる原料キサンタンガムとしては
また、トウモロコシ澱粉やグルコース等を炭素源とし
て、キサントモナス・カンペストリスを液体培養して得
られる培養液から低級アルカノールで分別沈殿させるキ
サンタンガムの製造法において、分別沈殿後の濃縮した
キサンタンガムおよび乾燥工程中のキサンタンガムを用
いることができる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. As described above, the non-volatile organic solvent-containing xanthan gum of the present invention can be generally obtained by mixing xanthan gum and a non-volatile organic solvent in an amount of 0.01% by weight or more with respect to xanthan gum, and further heating the mixture at 80 ° C. or more. it can. As the raw material xanthan gum used for producing the xanthan gum containing a nonvolatile organic solvent of the present invention, first, commercially available powdery or granular xanthan gum can be used. As such a raw material xanthan gum, in a method for producing xanthan gum that is separated from a culture obtained by liquid culturing Xanthomonas campestris with a lower alkanol using corn starch, glucose or the like as a carbon source, concentrated xanthan gum after fractional precipitation, Xanthan gum during the drying step can be used.

【0006】原料の不揮発性有機溶媒としては、沸点が
100℃以上の有機溶媒が望ましい、さらに望ましくは
沸点が120℃以上で融点が90℃以下の有機溶媒であ
る。これらの不揮発性有機溶媒は加熱処理を80℃から
150℃の範囲で行うために、高沸点で低融点のものが
望ましい。不揮発性有機溶媒は前述の条件を満たすもの
であれば特に制限はないが、その中でも極性が高い不揮
発性有機溶媒を用いると、水均一分散性が良好で望まし
い。以下に不揮発性有機溶媒の例を挙げるが、これに限
定するものではない。塩基性有機溶媒類としては、ピリ
ジンおよびTMED等がある。置換基としてエステル
基、水酸基、カルボキシル基を持つものとしてグリセリ
ン、グリセリン重合物、ソルビトール、炭素数1〜4の
アルカンジオール等の多価アルコール類、炭素数6〜2
2の飽和脂肪酸および不飽和脂肪酸および分岐状脂肪酸
等の脂肪酸類、多価アルコールと脂肪酸の完全エステル
化物および部分エステル化物などの合成エステル類、植
物油脂および動物油脂等の各種油脂類を挙げることがで
きる。不揮発性有機溶媒の配合量は、キサンタンガムに
対して0.01重量%が望ましく、不揮発性有機溶媒の
1種もしくは2種以上を配合することができる。配合量
が0.01重量%以下であると効果が十分でなく、5重
量%で十分な耐塩性および水均一分散性が得られるが、
5重量%以上の不揮発性溶媒が存在していても効果は同
じである。
As the non-volatile organic solvent as a raw material, an organic solvent having a boiling point of 100 ° C. or higher is desirable, and more preferably an organic solvent having a boiling point of 120 ° C. or higher and a melting point of 90 ° C. or lower. These non-volatile organic solvents preferably have a high boiling point and a low melting point in order to perform the heat treatment in the range of 80 ° C. to 150 ° C. The non-volatile organic solvent is not particularly limited as long as it satisfies the above-mentioned conditions. Among them, the use of a non-volatile organic solvent having a high polarity is preferable because water uniform dispersibility is good. Examples of the non-volatile organic solvent will be described below, but it should not be construed that the invention is limited thereto. Basic organic solvents include pyridine and TMED. Glycerin, glycerin polymer, sorbitol, polyhydric alcohols such as alkanediols having 1 to 4 carbon atoms, those having 6 to 2 carbon atoms having an ester group, a hydroxyl group and a carboxyl group as substituents
2, fatty acids such as saturated fatty acids, unsaturated fatty acids, and branched fatty acids; synthetic esters such as fully esterified and partially esterified polyhydric alcohols and fatty acids; and various fats and oils such as vegetable fats and animal fats. it can. The amount of the nonvolatile organic solvent is preferably 0.01% by weight with respect to xanthan gum, and one or more nonvolatile organic solvents can be blended. When the amount is 0.01% by weight or less, the effect is not sufficient, and when 5% by weight, sufficient salt resistance and water uniform dispersibility can be obtained.
The effect is the same even when 5% by weight or more of the nonvolatile solvent is present.

【0007】不揮発性有機溶媒含有キサンタンガムを製
造するために、かかる原料のキサンタンガムと原料の不
揮発性有機溶媒と混合し、さらに加熱するが、加熱は8
0℃以上、好ましくは80〜150℃で15分〜50時
間、さらに好ましくは100〜150℃で15分〜6時
間、さらに一層好ましくは120〜150℃で15分〜
4時間である。これらの条件において高温側で短時間が
望ましい。加熱温度が低いと不揮発性有機溶媒含有が十
分でなく、また長時間加熱では着色する可能性が大きく
なる。上述の加熱は、加熱方法、加熱媒体については特
に限定するものではないが、以下の方法が挙げられる。
例えば、十分な不揮発性溶媒を用い、キサンタンガム粉
末を分散させ、加熱後、不必要な不揮発性溶媒をろ過も
しくは揮発性有機溶媒で軽く洗浄して除く方法がある。
または、沸点が低い揮発性溶媒中で常圧もしくは加圧条
件下で加熱し、ろ過もしくは蒸留で不必要な揮発性溶媒
を除去する方法がある。さらに、キサンタンガムに不揮
発性有機溶媒を添加し、気体中で加熱する方法もある。
いずれの方法も、酸素が存在する系では加熱着色がみら
れるために、空気を除去するか、もしくは空気をキサン
タンガムと反応しない不活性な気体と置換するのが望ま
しい。気体の例としては空気、窒素、酸素、二酸化炭
素、ヘリウム、アルゴン等を挙げることができる。上述
したキサンタンガムの処理方法は、市販の粉末状、顆粒
状等のキサンタンガムを直接用いるだけでなく、キサン
タンガムを発酵により製造する製造工程中で用いること
もできる。
To produce xanthan gum containing a non-volatile organic solvent, the starting material xanthan gum and the starting material non-volatile organic solvent are mixed and further heated.
0 ° C or higher, preferably 80 to 150 ° C for 15 minutes to 50 hours, more preferably 100 to 150 ° C for 15 minutes to 6 hours, even more preferably 120 to 150 ° C for 15 minutes to
4 hours. Under these conditions, a short time on the high temperature side is desirable. If the heating temperature is low, the content of the non-volatile organic solvent is not sufficient, and if heated for a long time, the possibility of coloring increases. The above-mentioned heating is not particularly limited with respect to the heating method and the heating medium, but includes the following methods.
For example, there is a method in which xanthan gum powder is dispersed using a sufficient nonvolatile solvent, and after heating, unnecessary nonvolatile solvents are removed by filtration or lightly washed with a volatile organic solvent.
Alternatively, there is a method of heating under a normal pressure or a pressurized condition in a volatile solvent having a low boiling point to remove unnecessary volatile solvent by filtration or distillation. Furthermore, there is a method of adding a non-volatile organic solvent to xanthan gum and heating in a gas.
In any of the methods, it is desirable to remove air or replace the air with an inert gas which does not react with xanthan gum, because heating and coloring are observed in a system in which oxygen is present. Examples of the gas include air, nitrogen, oxygen, carbon dioxide, helium, argon and the like. The method for treating xanthan gum described above can be used not only in the direct use of commercially available powdery or granular xanthan gum, but also in the production process of producing xanthan gum by fermentation.

【0008】上記方法によって製造される不揮発性有機
溶媒含有キサンタンガムは、その高い粘度特性において
従来のキサンタンガムと異なる。すなわち、本発明の不
揮発性有機溶媒含有キサンタンガムは、キサンタンガム
濃度として0.5重量%となるように水へ添加し、25
℃で1時間攪拌した場合、2000〜30000mPa
・s(B型粘度計6rpm 25℃)の粘度を示す。均
一分散性を調べるために、分散条件を厳しく比較した。
即ち、本発明品をキサンタンガム濃度として0.5重量
%となるように水へ添加し、25℃ないし80℃で1時
間攪拌し、分散させ、25℃に冷却した後に粘度を比較
すると、両者の粘度の差は、0〜50%の範囲に収まっ
た。一方、従来のキサンタンガムの乾燥品(90℃、6
時間加熱)の0.5重量%25℃分散水溶液は1980
mPa・sであるが、0.5重量%80℃分散水溶液の
25℃における粘度が1100mPa・sで60%以上
低下していることから、本発明の不揮発性有機溶媒含有
キサンタンガムは、分散温度が異なっても高い粘度を維
持し、かつ高い分散性を有するので驚異的である。な
お、不揮発性有機溶媒を添加し加熱しない場合は、物性
面に差がみられないことから本特許の必須条件は、キサ
ンタンガムと第2成分である不揮発性有機溶媒を混合
し、加熱することである。
[0008] Xanthan gum containing a non-volatile organic solvent produced by the above method differs from conventional xanthan gum in its high viscosity characteristics. That is, the xanthan gum containing the non-volatile organic solvent of the present invention is added to water so that the xanthan gum concentration becomes 0.5% by weight,
When stirred at ℃ for 1 hour, 2000 to 30000 mPa
-Indicates the viscosity of s (B-type viscometer 6 rpm 25 ° C). Dispersion conditions were rigorously compared to determine uniform dispersibility.
That is, the product of the present invention was added to water so as to have a xanthan gum concentration of 0.5% by weight, stirred at 25 ° C. to 80 ° C. for 1 hour, dispersed and cooled to 25 ° C., and the viscosity was compared. The difference in viscosity was in the range of 0-50%. On the other hand, a dried product of conventional xanthan gum (90 ° C., 6
0.5 h% aqueous dispersion at 25 ° C for 1980)
Although the viscosity at 25 ° C. of the 0.5% by weight dispersion aqueous solution at 80 ° C. is reduced by 60% or more at 1100 mPa · s, the dispersion temperature of the non-volatile organic solvent-containing xanthan gum of the present invention is It is surprising because it maintains a high viscosity even if it is different and has a high dispersibility. In addition, when the non-volatile organic solvent is added and not heated, there is no difference in physical properties, so the essential condition of the present patent is that xanthan gum and the non-volatile organic solvent as the second component are mixed and heated. is there.

【0009】本発明の不揮発性有機溶媒含有キサンタン
ガムは従来のキサンタンガムと同様な用途に用いること
ができるが、その際に従来品よりも少ない用量で同様の
増粘効果を発揮することができる。その際に水溶液の耐
塩性および水均一分散性が損なわれることなく増粘効果
を発揮することができる。かかる本発明の不揮発性有機
溶媒含有キサンタンガムは単独でまたは他の水溶液ゲル
化剤、水溶液増粘剤、塩類、酸類、乳化剤等と組み合わ
せることで、安定なゲル、増粘剤、および乳化物を得る
ことができる。したがって、本発明の不揮発性有機溶媒
含有キサンタンガムは、食品分野、化粧品分野、農薬分
野、医薬品分野を始め、石油分野や塗料分野を含む一般
工業分野において増粘剤、安定化剤、添加剤として用い
られる。本発明を以下実施例、比較例および参考例によ
って具体的に説明するが、これらは本発明を例証するた
めのものであって、本発明を何等限定するものではな
い。
The xanthan gum containing a non-volatile organic solvent of the present invention can be used for the same applications as conventional xanthan gum, but in that case, the same thickening effect can be exhibited with a smaller dose than the conventional product. At that time, the thickening effect can be exhibited without impairing the salt resistance and the water uniform dispersibility of the aqueous solution. Such a nonvolatile organic solvent-containing xanthan gum of the present invention can be used alone or in combination with other aqueous gelling agents, aqueous thickeners, salts, acids, emulsifiers, etc. to obtain stable gels, thickeners, and emulsions. be able to. Therefore, the non-volatile organic solvent-containing xanthan gum of the present invention is used as a thickener, a stabilizer, and an additive in general industrial fields including the fields of food, cosmetics, agrochemicals, pharmaceuticals, petroleum and paints. Can be EXAMPLES Hereinafter, the present invention will be described specifically with reference to Examples, Comparative Examples, and Reference Examples, which are intended to exemplify the present invention and do not limit the present invention in any way.

【0010】[0010]

【実施例】以下本発明の実施例および比較例を説明す
る。 <従来のキサンタンガムの比較製造例1>キサンタンガ
ム粉末を空気中で90℃、105℃、125℃で乾燥し
た。乾燥工程中でサンプルを取り出し、物性を比較し
た。キサンタンガム濃度として0.5重量%となるよう
に水へ添加し、25℃で1時間攪拌し、もしくは80℃
で1時間攪拌して25℃に冷却し粘度を測定した(B型
粘度計:6rpm、25℃、ローターNo.2もしくは
No.3)。両者の水溶液を比較して、水均一分散性を
比較した。さらに、25℃分散溶液を等量の1重量%塩
化ナトリウム溶液と混合させ、その分散性を比較するこ
とで耐塩性を調べた。結果を表1〜3に示す。
EXAMPLES Examples and comparative examples of the present invention will be described below. <Comparative Production Example 1 of Conventional Xanthan Gum> Xanthan gum powder was dried at 90 ° C, 105 ° C, and 125 ° C in the air. A sample was taken out during the drying process and the physical properties were compared. Xanthan gum is added to water so as to have a concentration of 0.5% by weight and stirred at 25 ° C. for 1 hour, or 80 ° C.
For 1 hour, cooled to 25 ° C., and measured for viscosity (B-type viscometer: 6 rpm, 25 ° C., rotor No. 2 or No. 3). The two aqueous solutions were compared to compare the water uniform dispersibility. Further, the 25 ° C. dispersion solution was mixed with an equal amount of a 1% by weight sodium chloride solution, and the dispersibility was compared to examine salt resistance. The results are shown in Tables 1 to 3.

【0011】[0011]

【表1】 [Table 1]

【0012】[0012]

【表2】 [Table 2]

【0013】[0013]

【表3】 [Table 3]

【0014】表1〜3から、乾燥が進んだキサンタンガ
ムは、粘度が上昇するが、同時に耐塩性が低下し、さら
に25℃分散と80℃分散の粘度の差が大きくなること
から水均一分散性が悪化していることがわかる。
From Tables 1 to 3, it can be seen that the dried xanthan gum has an increased viscosity, but at the same time, a reduced salt resistance, and the difference in viscosity between the dispersion at 25 ° C. and the dispersion at 80 ° C. increases. Is worse.

【0015】<不揮発性有機溶媒含有キサンタンガムの
製造例1>キサンタンガム粉末を5重量倍量の1,3―
ブチレングリコールに添加し、90℃で加熱した。加熱
工程中でサンプルを取り出し、エタノールで軽く洗浄し
た。エタノールを減圧乾燥にて留去した。比較製造例1
と同様の方法で物性を比較した。結果を表4に示す。
<Production Example 1 of xanthan gum containing nonvolatile organic solvent>
Added to butylene glycol and heated at 90 ° C. The sample was removed during the heating step and washed lightly with ethanol. Ethanol was distilled off under reduced pressure. Comparative Production Example 1
Physical properties were compared in the same manner as in. Table 4 shows the results.

【0016】[0016]

【表4】 [Table 4]

【0017】表4から、不揮発性有機溶媒含有キサンタ
ンガムは、従来品に比べ、粘度が高く、しかも良好な耐
塩性と水均一分散性を有していることがわかる。
From Table 4, it can be seen that the xanthan gum containing the non-volatile organic solvent has a higher viscosity than conventional products, and has good salt resistance and uniform water dispersibility.

【0018】<不揮発性有機溶媒含有キサンタンガムの
製造例2>キサンタンガム粉末を5重量倍量のステアリ
ン酸モノグリセリドを混合し、105℃で加熱した。加
熱工程中でサンプルを取り出し、熱時ろ過にてステアリ
ン酸モノグリセリドを除去した。比較製造例1と同様の
方法で物性を比較した。結果を表5に示す。
<Production Example 2 of Xanthan Gum Containing Non-Volatile Organic Solvent> Xanthan gum powder was mixed with 5 weight times the amount of stearic acid monoglyceride and heated at 105 ° C. The sample was taken out during the heating step, and the stearic acid monoglyceride was removed by hot filtration. The physical properties were compared in the same manner as in Comparative Production Example 1. Table 5 shows the results.

【0019】[0019]

【表5】 [Table 5]

【0020】表5から、不揮発性有機溶媒含有キサンタ
ンガムは、従来品に比べ、粘度が高く、しかも良好な耐
塩性と水均一分散性を有していることがわかる。
From Table 5, it can be seen that the xanthan gum containing the non-volatile organic solvent has a higher viscosity than the conventional product, and has good salt resistance and uniform water dispersibility.

【0021】<不揮発性有機溶媒含有キサンタンガムの
製造例3>キサンタンガム粉末を3重量倍量のトリメチ
ルエチレンジアミン(TMED)を混合し、105℃で
加熱した。加熱工程中でサンプルを取り出し、ろ過にて
TMEDを除去した。比較製造例1と同様の方法で物性
を比較した。結果を表6に示す。
<Production Example 3 of Xanthan Gum Containing Nonvolatile Organic Solvent> Xanthan gum powder was mixed with trimethylethylenediamine (TMED) in an amount of 3 times by weight and heated at 105 ° C. The sample was taken out during the heating step, and TMED was removed by filtration. The physical properties were compared in the same manner as in Comparative Production Example 1. Table 6 shows the results.

【0022】[0022]

【表6】 [Table 6]

【0023】表6から、不揮発性有機溶媒含有キサンタ
ンガムは、従来品に比べ、粘度が高く、しかも良好な耐
塩性と水均一分散性を有していることがわかる。
From Table 6, it can be seen that the xanthan gum containing the non-volatile organic solvent has a higher viscosity than the conventional product, and has good salt resistance and uniform water dispersibility.

【0024】<不揮発性有機溶媒含有キサンタンガムの
製造例4>キサンタンガム粉末を5重量倍量の大豆油を
混合し、125℃で加熱した。加熱工程中でサンプルを
取り出し、熱時ろ過にて大豆油を除去した。比較製造例
1と同様の方法で物性を比較した。結果を表7に示す。
<Production Example 4 of Xanthan Gum Containing Nonvolatile Organic Solvent> Xanthan gum powder was mixed with soybean oil in an amount of 5 times by weight and heated at 125 ° C. A sample was taken out during the heating step, and soybean oil was removed by hot filtration. The physical properties were compared in the same manner as in Comparative Production Example 1. Table 7 shows the results.

【0025】[0025]

【表7】 [Table 7]

【0026】表7から、不揮発性有機溶媒含有キサンタ
ンガムは、従来品に比べ、粘度が高く、しかも良好な耐
塩性と水均一分散性を有していることがわかる。
From Table 7, it can be seen that the xanthan gum containing the non-volatile organic solvent has a higher viscosity than conventional products, and has good salt resistance and uniform water dispersibility.

【0027】<不揮発性有機溶媒含有キサンタンガムの
製造例5>キサンタンガム粉末に大豆油のヘキサン溶液
を大豆油がキサンタンガムに対して3重量%となるよう
に添加し、室温にてヘキサンを減圧留去した。得られた
キサンタンガム粉末を空気中で125℃で乾燥した。乾
燥工程中でサンプルを取り出し、比較製造例1と同様の
方法で物性を比較した。結果を表8に示す。
<Production Example 5 of Xanthan Gum Containing Non-Volatile Organic Solvent> A hexane solution of soybean oil was added to xanthan gum powder so that the soybean oil was 3% by weight with respect to xanthan gum, and hexane was distilled off under reduced pressure at room temperature. . The obtained xanthan gum powder was dried at 125 ° C. in air. The sample was taken out during the drying step, and the physical properties were compared in the same manner as in Comparative Production Example 1. Table 8 shows the results.

【0028】[0028]

【表8】 [Table 8]

【0029】表8から、不揮発性有機溶媒含有キサンタ
ンガムは、従来品に比べ、粘度が高く、しかも良好な耐
塩性と水均一分散性を有していることがわかる。
From Table 8, it can be seen that the xanthan gum containing the non-volatile organic solvent has a higher viscosity than conventional products, and has good salt resistance and uniform water dispersibility.

【0030】<従来のキサンタンガムの比較製造例2>
比較製造例1の表3のサンプルに、大豆油のヘキサン溶
液を大豆油がキサンタンガムに対して3重量%となるよ
うに添加し、室温にてヘキサンを減圧留去した。比較製
造例1と同様の方法で物性を比較した。結果を表9に示
す。
<Comparative Production Example 2 of Conventional Xanthan Gum>
A hexane solution of soybean oil was added to the samples in Table 3 of Comparative Production Example 1 so that the soybean oil was 3% by weight based on xanthan gum, and hexane was distilled off under reduced pressure at room temperature. The physical properties were compared in the same manner as in Comparative Production Example 1. Table 9 shows the results.

【0031】[0031]

【表9】 [Table 9]

【0032】表3および表9を比較すると、キサンタン
ガムに大豆油を添加した後に加熱しない場合は、物性に
差がないことがわかった。
Comparing Tables 3 and 9, it was found that there was no difference in physical properties when heating was not performed after adding soybean oil to xanthan gum.

【0033】[0033]

【発明の効果】本発明の不揮発性有機溶媒含有キサンタ
ンガムは、高い粘度特性を有する水溶性増粘剤であり、
水溶液にしたときの耐塩性および水への均一分散性に優
れている。
The non-volatile organic solvent-containing xanthan gum of the present invention is a water-soluble thickener having high viscosity characteristics,
It has excellent salt resistance and uniform dispersion in water when made into an aqueous solution.

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】不揮発性有機溶媒を0.01重量%以上含
有したキサンタンガムを80℃以上で加熱して生成され
るものであることを特徴とする不揮発性有機溶媒含有キ
サンタンガム。
1. A xanthan gum containing a non-volatile organic solvent, which is produced by heating xanthan gum containing not less than 0.01% by weight of a non-volatile organic solvent at 80 ° C. or more.
【請求項2】不揮発性有機溶媒を0.01重量%以上含
有したキサンタンガムを80℃以上で加熱することを特
徴とする不揮発性有機溶媒含有キサンタンガムの製造方
法。
2. A method for producing xanthan gum containing a nonvolatile organic solvent, comprising heating xanthan gum containing not less than 0.01% by weight of a nonvolatile organic solvent at 80 ° C. or more.
【請求項3】不揮発性有機溶媒が沸点100℃以上であ
ることを特徴とする請求項1または2記載の不揮発性有
機溶媒含有キサンタンガムの製造法。
3. The method for producing xanthan gum containing a nonvolatile organic solvent according to claim 1, wherein the nonvolatile organic solvent has a boiling point of 100 ° C. or higher.
【請求項4】不揮発性有機溶媒が沸点120℃以上で、
融点90℃以下であることを特徴とする請求項1〜3の
いずれか1項記載の不揮発性有機溶媒含有キサンタンガ
ムの製造法。
4. A non-volatile organic solvent having a boiling point of 120 ° C. or higher,
The method for producing xanthan gum containing a nonvolatile organic solvent according to any one of claims 1 to 3, wherein the melting point is 90 ° C or less.
【請求項5】不揮発性有機溶媒が、エステル基、水酸
基、カルボキシル基から選ばれる1種または2種以上の
置換基を有することを特徴とする請求項1〜4のいずれ
か1項記載の不揮発性有機溶媒含有キサンタンガムの製
造法。
5. The non-volatile organic solvent according to claim 1, wherein the non-volatile organic solvent has one or more substituents selected from an ester group, a hydroxyl group and a carboxyl group. For producing xanthan gum containing a neutral organic solvent.
【請求項6】不揮発性溶媒が塩基性有機溶媒であること
を特徴とする請求項1〜5のいずれか1項記載の不揮発
性有機溶媒含有キサンタンガムの製造法。
6. The method for producing xanthan gum containing a nonvolatile organic solvent according to claim 1, wherein the nonvolatile solvent is a basic organic solvent.
【請求項7】加熱処理が、80〜150℃で15分〜5
0時間であることを特徴とする請求項1〜6のいずれか
1項記載の不揮発性有機溶媒含有キサンタンガムの製造
方法。
7. The heat treatment is performed at 80 to 150 ° C. for 15 minutes to 5 hours.
The method for producing xanthan gum containing a nonvolatile organic solvent according to any one of claims 1 to 6, wherein the time is 0 hour.
【請求項8】加熱処理が、100〜150℃で15分〜
6時間であることを特徴とする請求項1〜6のいずれか
1項記載の不揮発性有機溶媒含有キサンタンガムの製造
方法。
8. The heat treatment is performed at 100 to 150 ° C. for 15 minutes or more.
The method for producing xanthan gum containing a non-volatile organic solvent according to any one of claims 1 to 6, wherein the time is 6 hours.
【請求項9】加熱処理が、120〜150℃で15分〜
4時間であることを特徴とする請求項1〜6のいずれか
1項記載の不揮発性有機溶媒含有キサンタンガムの製造
方法。
9. The heat treatment is performed at 120 to 150 ° C. for 15 minutes or more.
The method for producing xanthan gum containing a nonvolatile organic solvent according to any one of claims 1 to 6, wherein the treatment is performed for 4 hours.
【請求項10】加熱処理が、不揮発性有機溶媒を濃度と
して0.1重量%以上含有する有機溶媒中で行うことを
特徴とする請求項1〜9のいずれか1項記載の不揮発性
有機溶媒含有キサンタンガムの製造方法。
10. The nonvolatile organic solvent according to claim 1, wherein the heat treatment is performed in an organic solvent containing the nonvolatile organic solvent in a concentration of 0.1% by weight or more. A method for producing xanthan gum.
【請求項11】加熱処理が、不揮発性有機溶媒をキサン
タンガムに散布した後に気体中で行われる請求項1〜1
0のいずれか1項記載の不揮発性有機溶媒含有キサンタ
ンガムの製造方法。
11. The heat treatment is performed in a gas after spraying a nonvolatile organic solvent on xanthan gum.
0. The method for producing a xanthan gum containing a nonvolatile organic solvent according to any one of 0.
JP19090598A 1998-07-07 1998-07-07 Nonvolatile organic solvent-containing xanthan gum and method for producing the same Expired - Fee Related JP4462659B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005526886A (en) * 2002-05-21 2005-09-08 エー、イー、ステーリー、マニュファクチュアリング、カンパニー Polysaccharide gum and method for producing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005526886A (en) * 2002-05-21 2005-09-08 エー、イー、ステーリー、マニュファクチュアリング、カンパニー Polysaccharide gum and method for producing the same

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