JP2000236843A - Production of curcumins - Google Patents

Production of curcumins

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Publication number
JP2000236843A
JP2000236843A JP11043916A JP4391699A JP2000236843A JP 2000236843 A JP2000236843 A JP 2000236843A JP 11043916 A JP11043916 A JP 11043916A JP 4391699 A JP4391699 A JP 4391699A JP 2000236843 A JP2000236843 A JP 2000236843A
Authority
JP
Japan
Prior art keywords
curcumin
solvent
extraction
curcumins
extracting
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11043916A
Other languages
Japanese (ja)
Inventor
Keita Someya
慶太 染矢
Kenji Isobe
賢治 磯部
Masahiko Furue
雅彦 古江
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.)
Lion Corp
Original Assignee
Lion Corp
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 Lion Corp filed Critical Lion Corp
Priority to JP11043916A priority Critical patent/JP2000236843A/en
Publication of JP2000236843A publication Critical patent/JP2000236843A/en
Pending legal-status Critical Current

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  • Medicines Containing Plant Substances (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the deterioration of curcumin, reduce the amount of an extracting solvent and produce high-purity curcumins useful for medicines, foods, colorants, or the like, by dispersing a curcumin-containing extract solution in a solvent having a polarity different from that of the extracting solvent and then fractionating the curcumin. SOLUTION: For example, Curcuma longa L. is pulverized to 250-500 μm size to thereby provide a curcumin-containing extract solution according to a solid-liquid extracting method or a Soxhlet method, or the like, using an extracting solvent such as acetone. The resultant extract solution is then dispersed in a solvent having a polarity different from that of the extracting solvent and having high safety such as hydrous ethanol, hydrous denatured ethanol or water and the curcumin is subsequently fractionated to afford curcumins. For example, a deposition fractionating method by regulation of hydrogen ions of a solution, temperature regulation or polarity regulation is used as the method for fractionating the curcumins.

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、残留抽出溶媒を低
減化したクルクミン類の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing curcumins with reduced residual extraction solvent.

【0002】[0002]

【従来の技術】クルクミンは、ショウガ科多年性草であ
るターメリック(Curcuma longa L.)に代表される熱
帯、亜熱帯系の植物群に含まれている。ターメリック
は、食用のスパイス、食用、衣料用の着色剤として用い
られる他、特にアジア地域において薬用として用いられ
ており、その薬理作用としては胆汁分泌促進作用(利胆
作用)、内蔵(肝臓、膵臓)機能増強作用、抗炎症作
用、止血作用、健胃作用が知られている。
2. Description of the Related Art Curcumin is included in a group of tropical and subtropical plants represented by turmeric (Curcuma longa L.), which is a perennial ginger. Turmeric is used as a coloring agent for edible spices, food and clothing, and is also used as a medicinal product in the Asian region in particular. Its pharmacological actions include bile secretion promoting action (biliary action) and internal organs (liver, pancreas). ) Function-enhancing action, anti-inflammatory action, hemostatic action, and stomachic action are known.

【0003】また、最近クルクミンに関しては、抗酸化
作用、発癌抑制作用の他に脂質代謝改善作用の報告があ
り、着色料以外に生理作用の面で注目を集めている物質
である。
In addition, curcumin has recently been reported to have an effect of improving lipid metabolism in addition to an antioxidant effect and a carcinogenesis-suppressing effect.

【0004】クルクミンの製造に関しては、一般的にタ
ーメリックからの有機溶媒抽出により行われている。例
えば、タ−メリックを250〜500μmに粉砕した
後、有機溶媒、具体的にはエタノール、メタノール、イ
ソプロピルアルコール、プロピレングリコール、アセト
ン等の親水性溶媒又はこれらの溶媒とヘキサン、酢酸エ
チル等の疎水性溶媒との組み合わせ溶媒を用いて固液抽
出法若しくはソックスレー法等で抽出物を得、次いで、
本抽出物を減圧乾燥等の方法で脱溶媒し、その後必要に
応じてケイ酸カラムを用いて精製する方法等が用いられ
ている。
[0004] Curcumin is generally produced by extracting an organic solvent from turmeric. For example, after turmeric is crushed to 250-500 μm, an organic solvent, specifically, a hydrophilic solvent such as ethanol, methanol, isopropyl alcohol, propylene glycol, or acetone, or a hydrophobic solvent such as hexane or ethyl acetate, etc. An extract is obtained by a solid-liquid extraction method or a Soxhlet method using a combination solvent with a solvent,
The extract is desolvated by a method such as drying under reduced pressure, and then, if necessary, purified by using a silica column.

【0005】この中で特に脱溶媒の方法としては、単蒸
留、分留、精留、水蒸気蒸留、減圧蒸留、精密蒸留、分
子蒸留、加熱乾燥、減圧乾燥、通風乾燥といった各種の
方法が挙げられるが、いずれの方法でも残留溶媒量を低
減するためには加熱工程などの数種の工程と長い処理時
間が必要であるという課題を有する。また、上述の溶媒
低減工程においては、長い処理工程中にクルクミンが分
解、重合といった変性、劣化を受けてしまうという点に
課題を有する。
[0005] Among them, as a method of removing the solvent, various methods such as simple distillation, fractional distillation, rectification, steam distillation, reduced pressure distillation, precision distillation, molecular distillation, heat drying, reduced pressure drying, and ventilation drying are exemplified. However, any method has a problem that several steps such as a heating step and a long processing time are required to reduce the amount of the residual solvent. Further, in the above-mentioned solvent reduction step, there is a problem in that curcumin undergoes modification and deterioration such as decomposition and polymerization during a long treatment step.

【0006】一方、有機溶媒の中には、発ガン性や毒性
を有する物や刺激臭を有する物が数多く含まれ、水やエ
チルアルコールといった刺激性が少なく安全性が確認さ
れている物以外は極力除去されることが好ましいもので
ある。実際に、特開平3−65235号公報には、錠剤
の如き成形品からの残留溶剤の抽出法として、有機溶剤
の超臨界流体および臨界に近いガス抽出法が開示されて
おり、特開平2−292216号公報には、超臨界炭酸
ガス抽出によるグリチルリチン酸及びその塩類等医薬品
類の脱溶剤方法が開示されており、特開平3−6323
2号公報には、薬剤組成物を加圧気体と接触させること
で脱溶剤を図る溶剤抽出方法が開示されており、特開平
6−9479号公報には、ウコン粉末を超臨界炭酸ガス
に接触させることによりクルクミンを抽出する方法、及
び抽出したクルクミンをシクロデキストリンに吸着包接
させてクルクミン−シクロデキストリン複合体等を製造
する製造方法が開示されている。しかしながら、これら
の抽出方法等は、上述の如く、超臨界流体若しくはそれ
に近い加圧気体等を用いて残留溶剤等を除去するもので
あるが、非常に大規模な装置が必要であり、設備設置の
ために過大な初期投資が必要であるという点に課題を有
する。
[0006] On the other hand, organic solvents include many substances having carcinogenicity, toxicity, and irritating odor, and those having low irritating properties such as water and ethyl alcohol and whose safety has been confirmed. It is preferred that it be removed as much as possible. Actually, Japanese Patent Application Laid-Open No. 3-65235 discloses a method for extracting a supercritical fluid of an organic solvent and a gas near the criticality as a method for extracting a residual solvent from a molded product such as a tablet. JP-A-292216 discloses a method for desolvating pharmaceuticals such as glycyrrhizic acid and salts thereof by supercritical carbon dioxide extraction.
No. 2 discloses a solvent extraction method for removing a solvent by bringing a pharmaceutical composition into contact with a pressurized gas, and Japanese Patent Application Laid-Open No. 6-9479 discloses a method of contacting a turmeric powder with a supercritical carbon dioxide gas. There is disclosed a method of extracting curcumin by causing the curcumin to be extracted, and a method of producing a curcumin-cyclodextrin complex or the like by adsorbing and including the extracted curcumin with cyclodextrin. However, as described above, these extraction methods and the like remove residual solvents and the like using a supercritical fluid or a pressurized gas close thereto, but require a very large-scale apparatus, and require equipment installation. The problem is that excessive initial investment is required for the purpose.

【0007】また、特開昭57−8739号公報には、
大豆や菜種からの油脂抽出残渣蛋白質中の有機溶剤の低
減方法として、抽出温度を35℃以下でなるべく短時間
での溶媒接触を行う方法が開示されているが、クルクミ
ンのような溶媒抽出物を対象とした場合は、低温、短時
間の抽出処理では抽出効率が低下してしまうという点に
課題を生じる。更に、特開平5−255241号公報に
は、カロチンを対象物とした脱溶剤方法としてカロチン
結晶を溶解後不活性ガスを通気する方法が開示されてい
るが、クルクミン結晶の場合、溶解のためには高温で加
熱する必要が生じ、その結果クルクミンが分解、重合と
いった変性、劣化を受けてしまうという点に課題を有す
る。更にまた、実際のクルクミン製造を考慮する際にタ
ーメリック抽出乾燥物を調製した後に、新たに残留溶媒
低減工程を付加することは製造コストの高騰を引き起こ
すことが予想され、抽出工程中に並行して残留溶媒低減
化工程が実施されることが望まれている。
Further, Japanese Patent Application Laid-Open No. 57-8739 discloses that
As a method for reducing the organic solvent in the protein extracted from fats and oils from soybeans and rapeseed, a method in which the solvent is brought into contact with the solvent at an extraction temperature of 35 ° C. or lower in as short a time as possible is disclosed. In the case of the target, a problem arises in that the extraction efficiency is reduced in low-temperature, short-time extraction processing. Furthermore, Japanese Patent Application Laid-Open No. 5-255241 discloses a method of removing carotene as a target solvent, in which a carotene crystal is dissolved and then an inert gas is ventilated. Has a problem in that it requires heating at a high temperature, and as a result, curcumin is subject to denaturation and degradation such as decomposition and polymerization. Furthermore, adding a new residual solvent reduction step after preparing the turmeric extract dry matter when considering the actual curcumin production is expected to cause an increase in the production cost, and during the extraction step, It is desired that a residual solvent reduction step is performed.

【0008】[0008]

【発明が解決しようとする課題】本発明は、上記従来の
課題等に鑑み、これを解消しようとするものであり、ク
ルクミンの劣化を抑制して、残留抽出溶媒を低減化した
クルクミン類の製造方法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned conventional problems and the like, and is intended to solve the problem. The present invention provides a method for producing curcumins, which suppresses curcumin deterioration and reduces a residual extraction solvent. The aim is to provide a method.

【0009】[0009]

【課題を解決するための手段】本発明者らは、上記従来
の課題について検討した結果、クルクミン含有抽出液を
抽出溶媒とは異なる特定の溶媒に分散後、クルクミンを
分別することにより、上記目的のクルクミン類の製造方
法が得られることを見い出し、本発明を完成するに至っ
たのである。すなわち、本発明のクルクミン類の製造方
法は、クルクミン含有抽出液を抽出溶媒とは極性の異な
る溶媒に分散後、クルクミンを分別することを特徴とす
る。
Means for Solving the Problems As a result of studying the above conventional problems, the present inventors disperse a curcumin-containing extract in a specific solvent different from the extraction solvent and then separate the curcumin to obtain the above object. It has been found that a method for producing curcumins can be obtained, and the present invention has been completed. That is, the method for producing curcumin of the present invention is characterized in that curcumin-containing extract is dispersed in a solvent having a different polarity from the extraction solvent, and then curcumin is separated.

【0010】[0010]

【発明の実施の形態】以下に、本発明の実施の形態を詳
しく説明する。本発明のクルクミン類の製造方法は、ク
ルクミン含有抽出液を抽出溶媒とは極性の異なる溶媒に
分散後、クルクミンを分別することを特徴とするもので
ある。
Embodiments of the present invention will be described below in detail. The method for producing curcumins of the present invention is characterized in that a curcumin-containing extract is dispersed in a solvent having a different polarity from the extraction solvent, and then curcumin is fractionated.

【0011】本発明で製造対象とするクルクミン類は、
クルクミン及びその誘導体、例えば、クルクミン、デメ
トキシクルクミン、ビスデメトキシクルクミン等である
が、その純度において医薬品、食品として不適当な不純
物を含有しない限り、半精製、または粗製のクルクミン
も対象となり、なお且つ必要に応じて他の化合物との混
合組成物も対象となりうるものである。
The curcumins to be produced in the present invention include:
Curcumin and its derivatives, for example, curcumin, demethoxycurcumin, bisdemethoxycurcumin and the like, but also semi-purified or crude curcumin as long as they do not contain impurities that are unsuitable for pharmaceuticals and foods in their purity. In addition, if necessary, a mixed composition with another compound can be a target.

【0012】本発明の対象物であるクルクミンの抽出原
料は、いずれの由来のものでも使用できる。例えば、タ
ーメリック(Curcuma longa L.)のほか、マンゴージシ
ジャー、インド産アロールート、ガジュツ、黄色ガジュ
ツ、黒色ガジュツ、ガランガール等の植物から抽出する
ことができる。
The curcumin extraction raw material of the present invention can be of any origin. For example, in addition to turmeric (Curcuma longa L.), it can be extracted from plants such as mangoshjija, Indian arrow root, gajutsu, yellow gejutsu, black gejutsu, and galangard.

【0013】本発明に用いるクルクミン含有抽出液(以
下、「抽出溶液」という)としては、上記原料等から有
機溶媒抽出されたクルクミン含有抽出液であれば、特に
限定されず、例えば、タ−メリックを250〜500μ
mに粉砕した後、抽出溶媒、具体的にはエタノール、メ
タノール、イソプロピルアルコール、プロピレングリコ
ール、アセトン、エチレンジクロライド等を用いて固液
抽出法若しくはソックスレー法等から得られるクルクミ
ン含有抽出液が挙げられる。
The curcumin-containing extract used in the present invention (hereinafter referred to as "extraction solution") is not particularly limited as long as it is a curcumin-containing extract obtained by extracting an organic solvent from the above raw materials and the like. 250-500μ
After being pulverized to m, a curcumin-containing extract obtained by a solid-liquid extraction method or a Soxhlet method using an extraction solvent, specifically, ethanol, methanol, isopropyl alcohol, propylene glycol, acetone, ethylene dichloride or the like can be used.

【0014】本発明における抽出溶液の分散用の溶媒
は、抽出溶媒とは異なる極性の溶媒であれば、いずれの
溶媒でも使用できるが、好ましくは、含水エタノール、
含水変性エタノール、水、グリセリン、中鎖脂肪酸トリ
グリセリド、食用油といった安全性の高い溶媒が使用さ
れる。
As the solvent for dispersing the extraction solution in the present invention, any solvent can be used as long as it has a polarity different from that of the extraction solvent.
A highly safe solvent such as hydrous denatured ethanol, water, glycerin, medium-chain fatty acid triglyceride, and edible oil is used.

【0015】抽出溶液の分散方法は、特に限定されるも
のではないが、沈殿物をすばやく生成させるために滴下
する方法が好ましい。また、本発明において分散時の温
度は、使用する溶媒に応じ、いずれの温度でも実施可能
であり、含水エタノール、含水変性エタノール、水など
の溶媒では−20℃〜100℃、好ましくは、5℃〜7
5℃の温度で実施可能であり、更に、使用する溶媒量は
クルクミン等の処理量並びに目標とする残留抽出溶媒量
に応じていずれの量でも使用可能である。
The method of dispersing the extraction solution is not particularly limited, but is preferably a method of dropping in order to quickly generate a precipitate. Further, in the present invention, the temperature at the time of dispersion can be carried out at any temperature according to the solvent to be used. For a solvent such as hydrated ethanol, hydrated denatured ethanol, and water, the temperature is -20C to 100C, preferably 5C. ~ 7
It can be carried out at a temperature of 5 ° C., and any amount of solvent can be used depending on the amount of curcumin or the like to be treated and the target amount of residual extraction solvent.

【0016】また、本発明は、抽出溶液の分散時に抽出
溶媒留去条件下で行うこともできる。本抽出溶媒留去条
件としては、具体的には加熱蒸留条件、通気条件、減圧
条件などの条件が用いられる。上記抽出溶媒留去条件下
での実施により、残留抽出溶媒の除去量の向上が期待さ
れると共に、抽出溶液滴下用の溶媒量の減少が図られ装
置全体の縮小が可能となる。更に、抽出溶媒の回収も同
時に可能となり工程全体の経済性を向上することができ
る。
The present invention can also be carried out under the conditions of distilling off the extraction solvent when dispersing the extraction solution. As the extraction solvent distillation conditions, specifically, conditions such as heating distillation conditions, aeration conditions, and reduced pressure conditions are used. By performing the process under the above-mentioned extraction solvent distillation conditions, the removal amount of the residual extraction solvent is expected to be improved, and the amount of the solvent for dropping the extraction solution is reduced, so that the entire apparatus can be reduced in size. Furthermore, the extraction solvent can be recovered at the same time, and the economics of the entire process can be improved.

【0017】本発明において、抽出溶液の分散後のクル
クミンの分別法としては、例えば、溶液の水素イオン濃
度調整、温度調整、極性調整による析出分別法、単蒸
留、分留、精留、水蒸気蒸留、減圧蒸留、精密蒸留、分
子蒸留、加熱乾燥、減圧乾燥といった溶媒留去法、イオ
ン交換樹脂等による吸脱着、ケイ酸カラム、ODSカラ
ム、イオン交換クロマト、ゲル濾過クロマト等によるク
ロマトグラフィーなどが挙げられる。
In the present invention, as a method for separating curcumin after dispersion of the extraction solution, for example, a separation separation method by adjusting the hydrogen ion concentration of the solution, adjusting the temperature, adjusting the polarity, simple distillation, fractionation, rectification, steam distillation Solvent distillation methods such as vacuum distillation, precision distillation, molecular distillation, heat drying, and vacuum drying, adsorption and desorption with an ion exchange resin, etc., chromatography using a silica column, an ODS column, ion exchange chromatography, gel filtration chromatography, and the like. Can be

【0018】このように構成される本発明では、クルク
ミン含有抽出溶液を抽出溶媒とは極性が異なる溶媒、特
に、含水エタノール、含水変性エタノール、水といった
安全性の高い溶媒に分散後、クルクミンを分別すること
により、残留が問題となる抽出溶媒の低減化が図られ、
且つ、抽出工程と並行した簡便な工程で行うことができ
るので、更にクルクミンの劣化を抑制しつつ実施するこ
とができるものである。
In the present invention thus constituted, the curcumin-containing extraction solution is dispersed in a solvent having a polarity different from that of the extraction solvent, particularly a highly safe solvent such as aqueous ethanol, aqueous denatured ethanol, and water, and then curcumin is separated. By doing so, it is possible to reduce the amount of the extraction solvent in which the residue becomes a problem,
And since it can be performed in a simple step in parallel with the extraction step, it can be performed while further suppressing the deterioration of curcumin.

【0019】[0019]

【実施例】次に、実施例及び比較例により本発明を更に
説明するが、本発明は下記の実施例に限定されるもので
はない。
Next, the present invention will be further described with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples.

【0020】〔実施例1〕40gのターメリック末に1
20mLのアセトンを加え、40℃で30分攪拌し、濾
過を行いターメリック抽出液を得た。得られた抽出液を
20℃の水15L中に攪拌しながらゆっくりと滴下し、
30分攪拌継続後、得られた沈殿物を濾別し、80℃の
恒温槽で一晩乾燥し粗製クルクミン1.0gを得た。本
粗製クルクミン中の残留アセトン量は下記表1に記した
ように81ppmであった。
Example 1 1 g of turmeric powder of 40 g
20 mL of acetone was added, the mixture was stirred at 40 ° C. for 30 minutes, and filtered to obtain a turmeric extract. The obtained extract was slowly dropped into 15 L of water at 20 ° C. while stirring,
After continuing stirring for 30 minutes, the obtained precipitate was separated by filtration and dried overnight in a constant temperature bath at 80 ° C. to obtain 1.0 g of crude curcumin. The amount of residual acetone in the crude curcumin was 81 ppm as shown in Table 1 below.

【0021】〔比較例1〕上記実施例1と同様にして得
られた抽出液をロータリーエバポレーターにて40℃で
減圧濃縮し、続いて65℃で一晩減圧乾燥して粗製クル
クミンを得た。次いで、得られた粗製クルクミン1.1
g中の残留アセトン量を比較例として下記表1に記した
が、その残留アセトン量は850ppmであった。
Comparative Example 1 The extract obtained in the same manner as in Example 1 was concentrated under reduced pressure at 40 ° C. using a rotary evaporator, and then dried under reduced pressure at 65 ° C. overnight to obtain crude curcumin. Then, the obtained crude curcumin 1.1
The amount of residual acetone in g was shown in Table 1 below as a comparative example, and the amount of residual acetone was 850 ppm.

【0022】〔実施例2〕直径1cm、長さ40cmの
ガラス管にディクソンパッキンを充填した精留塔を装着
した容器に10%のエタノール溶液2Lを入れ、攪拌し
ながら85℃の蒸留条件下にて上記実施例1と同様にし
て得られた抽出液をゆっくりと滴下し、滴下終了後30
分間攪拌保持した。次いで、得られた沈殿物を濾別し、
80℃の恒温槽で一晩乾燥し粗製クルクミン1.0gを
得た。本粗製クルクミン中の残留アセトン量は、下記表
1に記したように190ppmであった。また、本条件
において水分6%を含むアセトンを60ml回収した。
Example 2 2 L of a 10% ethanol solution was placed in a vessel equipped with a rectification tower filled with Dixon packing in a glass tube having a diameter of 1 cm and a length of 40 cm. Then, the extract obtained in the same manner as in Example 1 was slowly dropped, and after the dropping was completed, 30 minutes.
It was kept stirring for minutes. Then, the obtained precipitate was filtered off,
It was dried in a constant temperature bath at 80 ° C. overnight to obtain 1.0 g of crude curcumin. The amount of residual acetone in the crude curcumin was 190 ppm as shown in Table 1 below. Further, 60 ml of acetone containing 6% of water was recovered under the above conditions.

【0023】〔実施例3〕上記実施例2の装置に水2L
を入れ、65℃で攪拌しながら減圧条件下にて上記実施
例1と同様にして得られた抽出液をゆっくりと滴下し、
滴下終了後30分間攪拌保持した。次いで、得られた沈
殿物を濾別し、80℃の恒温槽で一晩乾燥し粗製クルク
ミン1.1gを得た。本粗製クルクミン中の残留アセト
ン量は下記表1に記したように94ppmであった。ま
た、本条件において水分11%を含むアセトンを65m
l回収した。
[Embodiment 3] 2 L of water was added to the apparatus of Embodiment 2 above.
And the extract obtained in the same manner as in Example 1 above was slowly added dropwise under reduced pressure while stirring at 65 ° C.,
After completion of the dropping, the mixture was stirred and held for 30 minutes. Next, the obtained precipitate was separated by filtration and dried in a constant temperature bath at 80 ° C. overnight to obtain 1.1 g of crude curcumin. The amount of residual acetone in the crude curcumin was 94 ppm as shown in Table 1 below. Also, under these conditions, acetone containing 11% water was 65 m
1 was collected.

【0024】[0024]

【表1】 [Table 1]

【0025】上記表1の結果から明らかなように、本発
明方法となるクルクミン含有抽出液を抽出溶媒とは極性
の異なる溶媒に分散後、クルクミンを分別する実施例1
〜3は、本発明の範囲外となる比較例1に較べ、残留ア
セトン量がきわめて低減していることが判明した。
As is clear from the results shown in Table 1 above, the curcumin-containing extract used in the method of the present invention was dispersed in a solvent having a different polarity from the extraction solvent, and then curcumin was separated.
In Comparative Examples Nos. 1 to 3, it was found that the amount of residual acetone was extremely reduced as compared with Comparative Example 1 out of the range of the present invention.

【0026】[0026]

【発明の効果】本発明によれば、クルクミン含有抽出溶
液を抽出溶媒とは極性が異なる溶媒に分散後、クルクミ
ンを分別することにより残留が問題となる抽出溶媒の低
減化が図られ、且つ抽出工程と並行した簡便な工程でさ
らにクルクミンの劣化を抑制しつつ実施することができ
るクルクミン類の製造方法が提供される。
According to the present invention, after the curcumin-containing extraction solution is dispersed in a solvent having a polarity different from that of the extraction solvent, the curcumin is separated to reduce the amount of the extraction solvent in which the residue becomes a problem. Provided is a method for producing curcumin, which can be carried out in a simple step parallel to the step while further suppressing the deterioration of curcumin.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 古江 雅彦 東京都墨田区本所1丁目3番7号 ライオ ン株式会社内 Fターム(参考) 4B047 LB03 LG43 LP01 LP07 4C088 AB81 BA08 BA10 BA11 BA31 BA32 ZA53 ZA66 ZA69 ZA76 ZB11 ZB26 ZC21 ZC33  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Masahiko Furue 1-37, Honjo, Sumida-ku, Tokyo F-term in Lion Corporation (reference) 4B047 LB03 LG43 LP01 LP07 4C088 AB81 BA08 BA10 BA11 BA31 BA32 ZA53 ZA66 ZA69 ZA76 ZB11 ZB26 ZC21 ZC33

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 クルクミン含有抽出液を抽出溶媒とは極
性の異なる溶媒に分散後、クルクミンを分別することを
特徴とするクルクミン類の製造方法。
1. A method for producing curcumins, comprising: dispersing a curcumin-containing extract in a solvent having a polarity different from that of an extraction solvent, and then separating curcumin.
JP11043916A 1999-02-22 1999-02-22 Production of curcumins Pending JP2000236843A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JP2000236843A true JP2000236843A (en) 2000-09-05

Family

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Country Link
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US7723515B1 (en) 2009-01-26 2010-05-25 Codman & Shurtleff, Inc. Methylene blue—curcumin analog for the treatment of alzheimer's disease
US7745670B2 (en) 2008-06-27 2010-06-29 Codman & Shurtleff, Inc. Curcumin-Resveratrol hybrid molecule
US7985776B2 (en) 2008-06-27 2011-07-26 Codman & Shurtleff, Inc. Iontophoretic delivery of curcumin and curcumin analogs for the treatment of Alzheimer's Disease
EP2359820A1 (en) 2010-01-29 2011-08-24 Codman & Shurtleff, Inc. Shunt delivery of curcumin for the treatment Alzneimer
US8350093B2 (en) 2008-02-12 2013-01-08 Codman & Shurtleff, Inc. Methylated curcumin-resveratrol hybrid molecules for treating cancer
US8383865B2 (en) 2007-04-17 2013-02-26 Codman & Shurtleff, Inc. Curcumin derivatives

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8383865B2 (en) 2007-04-17 2013-02-26 Codman & Shurtleff, Inc. Curcumin derivatives
EP2749552A1 (en) 2007-04-17 2014-07-02 Codman & Shurtleff, Inc. Curcumin-resveratrol hybrids
US8350093B2 (en) 2008-02-12 2013-01-08 Codman & Shurtleff, Inc. Methylated curcumin-resveratrol hybrid molecules for treating cancer
US7745670B2 (en) 2008-06-27 2010-06-29 Codman & Shurtleff, Inc. Curcumin-Resveratrol hybrid molecule
US7985776B2 (en) 2008-06-27 2011-07-26 Codman & Shurtleff, Inc. Iontophoretic delivery of curcumin and curcumin analogs for the treatment of Alzheimer's Disease
US8288444B2 (en) 2008-06-27 2012-10-16 Codman & Shurtleff, Inc. Iontophoretic delivery of curcumin and curcumin analogs for the treatment of Alzheimer's disease
US7723515B1 (en) 2009-01-26 2010-05-25 Codman & Shurtleff, Inc. Methylene blue—curcumin analog for the treatment of alzheimer's disease
US7906643B2 (en) 2009-01-26 2011-03-15 Codman & Shurtleff, Inc. Methylene blue-curcumin analog for the treatment of Alzheimer's Disease
US8609652B2 (en) 2009-01-26 2013-12-17 DePuy Synthes Products, LLC Method of administering a methylene blue-curcumin analog for the treatment of alzheimer's disease
EP2359820A1 (en) 2010-01-29 2011-08-24 Codman & Shurtleff, Inc. Shunt delivery of curcumin for the treatment Alzneimer

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