JPH01311174A - Purification of yellow dyestuff of gardenia - Google Patents

Purification of yellow dyestuff of gardenia

Info

Publication number
JPH01311174A
JPH01311174A JP63140838A JP14083888A JPH01311174A JP H01311174 A JPH01311174 A JP H01311174A JP 63140838 A JP63140838 A JP 63140838A JP 14083888 A JP14083888 A JP 14083888A JP H01311174 A JPH01311174 A JP H01311174A
Authority
JP
Japan
Prior art keywords
clay
aqueous solution
crocin
alcohol
gardenia
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
JP63140838A
Other languages
Japanese (ja)
Other versions
JPH0415266B2 (en
Inventor
Hideaki Kashiwazaki
柏崎 秀明
Shinichi Saito
愼一 齊藤
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.)
Toyotama Koryo Co Ltd
Original Assignee
Toyotama Koryo 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 Toyotama Koryo Co Ltd filed Critical Toyotama Koryo Co Ltd
Priority to JP63140838A priority Critical patent/JPH01311174A/en
Publication of JPH01311174A publication Critical patent/JPH01311174A/en
Publication of JPH0415266B2 publication Critical patent/JPH0415266B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To simply purify the subject dyestuff free from causing color change to yellow-blue or brown in short process and high recovery by bringing an aqueous solution of yellow dyestuff extracted from Gardenia fruit into contact with an acid clay, then separating the clay, cleaning the clay with water and reacting the clay with an eluent. CONSTITUTION:An aqueous solution of yellow dyestuff extracted from Gardenia fruit is brought into contact with an acid clay and/or active clay and these clays are separated and cleaned with water or aqueous solution of alcohol. Yellow dyestuff of Gardenia fruit is desorbed from these clay by an eluent, recovered and purified. Furthermore, as the aqueous solution of alcohol for cleaning and the eluent, 5-15vol.% alcohol water solution and >=40vol.% concentrated alcohol water solution are each preferably used.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、緑ないし青変や褐変現象を起こさないクチナ
シ黄色色素を得るための精製法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a purification method for obtaining a gardenia yellow pigment that does not cause green to blue discoloration or browning phenomena.

[従来の技術] 従来、クチナシ果実から水あるいはアルコール水溶液で
黄色色素を抽出し、濾過後、濃縮又は粉末化したものが
クチナシ色素製剤として市販され、製菓、冷菓、麺類、
水産加工品、惣菜、漬物等に利用されている。そしてこ
の色素を特に麺類又は漬物等に使用した場1合、緑ない
し青色に変色したり、褐変化したりすることが知られて
おり、これらの原因物質はクチナシ色素抽出液中に含ま
れるイリドイド配糖体とポリフェノール類であるとされ
ている(特公昭52−13971、特開昭58−277
53)。
[Prior Art] Conventionally, yellow pigments are extracted from gardenia fruits with water or alcohol aqueous solution, filtered, and then concentrated or powdered and marketed as gardenia pigment preparations, which are used in confectionery, frozen desserts, noodles, etc.
It is used in processed seafood products, side dishes, pickles, etc. When this pigment is used especially in noodles or pickles, it is known that the color changes to green or blue or browns, and the causative agent is the iridoid compound contained in the gardenia pigment extract. They are said to be glycosides and polyphenols (Japanese Patent Publication No. 52-13971, Japanese Patent Publication No. 58-277)
53).

そこで、従来クチナシ色素の精製、即ち不純物であるイ
リドイド配糖体とポリフェノール類を除去するための吸
着剤として、スチレンとジビニルベンゼンの共重合体と
、ポリアミド樹脂との二種の物質を用いる第1の方法(
特開昭58−27753)と、半硬質ポリビニール系ゲ
ルを用いる第2の方法(特公昭6l−50981)とが
試みられた。
Therefore, in order to purify gardenia pigments, that is, to remove the impurities iridoid glycosides and polyphenols, the first method uses two types of materials: a copolymer of styrene and divinylbenzene and a polyamide resin. the method of(
Japanese Patent Publication No. 58-27753) and a second method using a semi-rigid polyvinyl gel (Japanese Patent Publication No. 61-50981) were attempted.

[発明が解決しようとする課題] しかしながら、第1の方法は各不純物ごとに異なる吸着
剤を使用せねばならず、その公平間を要し、工程も長く
なるという欠点があり、また第2の方法は吸着剤が比較
的高価であるという欠点があった。
[Problems to be Solved by the Invention] However, the first method has the disadvantage that a different adsorbent must be used for each impurity, which requires considerable time and lengthens the process. The method had the disadvantage that the adsorbent was relatively expensive.

本発明は、上記した事情に鑑みてなされたものであり、
その目的は安価な吸着剤を用いて、イリドイド配糖体と
ポリフェノール類を同時に除去することが可能なりチナ
シ黄色色素(クロシン)の精製法を提供するにある。
The present invention has been made in view of the above circumstances, and
The purpose is to provide a method for purifying Chinaseed yellow pigment (crocin), which makes it possible to simultaneously remove iridoid glycosides and polyphenols using an inexpensive adsorbent.

[課題を解決するための手段] 本発明者らは、上記目的を達成するため種々検討した結
果、安価な吸着剤である酸性白土及びこれを酸処理等に
より活性化して得られる活性白土が、クロシンの精製に
優れた特性を有することを見出し、本発明を完成するに
至った。
[Means for Solving the Problem] As a result of various studies to achieve the above object, the present inventors found that acid clay, which is an inexpensive adsorbent, and activated clay obtained by activating this by acid treatment, etc. It was discovered that crocin has excellent properties for purification, and the present invention was completed.

本発明は、クチナシ果実より抽出した黄色色素(クロシ
ン)水溶液と酸性白土および/又は活性白土とを接触さ
せた後、これら白土を分離して水又はアルコール水溶液
で洗浄し、その後、この白土から溶離液によりクチナシ
黄色色素を脱着、回収することを特徴としている。
The present invention involves contacting an aqueous solution of yellow pigment (crocin) extracted from gardenia fruit with acidic clay and/or activated clay, then separating these clays and washing them with water or an aqueous alcohol solution, and then eluating from this clay. It is characterized by the fact that it uses a liquid to desorb and recover gardenia yellow pigment.

上記洗浄用アルコール水溶液は5〜15vol.%の低
濃度のアルコール水溶液を用いてもよく、上記溶離液は
40vol.%以上の高濃度のアルコール水溶液であれ
ばよい。
The above alcohol aqueous solution for cleaning has a volume of 5 to 15 vol. % alcohol aqueous solution may be used, and the above eluent is 40 vol. An alcohol aqueous solution with a high concentration of % or more may be used.

[作 用] クチナシ果実より抽出した黄色色素水溶液と酸性白土お
よび/又は活性白土とを接触させることによって、白土
にクロシンが優先的に吸着されるとともにクチナシ果実
の抽出液中に存在するイリドイド配糖体とポリフェノー
ル類も同時に吸着される。その後、白土は上記色素水溶
液から分離され水またはアルコール水溶液で洗浄される
ことによってイリドイド配糖及びポリフェノール類が同
時に除去される。次いで、この洗浄後の白土から溶離液
によりクロシンを脱着し、高純度で回収することができ
る。
[Action] By bringing the aqueous yellow pigment extracted from gardenia fruit into contact with acid clay and/or activated clay, crocin is preferentially adsorbed to the clay and the iridoid glycosides present in the gardenia fruit extract are absorbed. body and polyphenols are also adsorbed at the same time. Thereafter, the clay is separated from the aqueous dye solution and washed with water or an aqueous alcohol solution to simultaneously remove iridoid glycosides and polyphenols. Crocin can then be desorbed from the washed clay using an eluent and recovered with high purity.

上記洗浄用液は水よりもアルコール水溶液を用いた方が
不純物中のポリフェノール類の除去率が高くなるが、ア
ルコール濃度が15vol.%を越えるとクロシンの回
収率が急激に低下するので洗浄用アルコール水溶液とし
ては5〜15vol.%の低濃度のアルコール水溶液が
好ましい。
The removal rate of polyphenols among impurities is higher when an alcohol aqueous solution is used as the cleaning liquid than water, but when the alcohol concentration is 15 vol. %, the recovery rate of crocin will drop sharply, so the cleaning alcohol aqueous solution should be 5 to 15 vol. % alcohol aqueous solution is preferred.

また、溶離液はアルコール濃度が高くなるにつれて白土
からのクロシンの脱着率が向上するが、40vol.%
以上であれば上記脱着率はあまり変化しない。
Furthermore, as the alcohol concentration of the eluent increases, the desorption rate of crocin from clay improves; %
If it is above, the desorption rate does not change much.

[実施例] 以下、本発明は実施例に基づいてより詳細に説明する。[Example] Hereinafter, the present invention will be explained in more detail based on examples.

実施例1 クチナシ果実から抽出、濾過、濃縮して得られた、以下
の特性値を有する黄色色素(クロシン)抽出水溶液に対
し精製処理を行った。
Example 1 A purification treatment was performed on a yellow pigment (crocin) extracted aqueous solution having the following characteristic values, which was obtained by extraction, filtration, and concentration from gardenia fruit.

E’l?@ =39.7 (440nm)イリドイド配
糖体の吸収極大である波長238nmにおける吸光度(
Az3a)とクロシンの吸収極大である波長440 n
mにおける吸光度(A44゜)との比 A isa / A 44G  = 1 、 66ポリ
フエノール類の吸収極大である波長325nmにおける
吸光度(Aszs)とクロシンの吸収極大である波長4
40nmにける吸光度(A44゜)との比 A 32B / A aaa = 01482クロシン
抽出水溶液5g、酸性白土(ミズ力エース#400 水
沢化学工業■製)20g、水50m1をビーカーに入れ
10分間攪拌し、クロシンを選択的に吸着させた後、濾
布を敷いた内径9cmのブフナー漏斗にて常法により吸
引濾過した。次いで水200m1を流し漏斗中の白土層
を洗浄した。洗浄後口土石に吸着しているクロシンを5
゜vol、%エタノール水溶液60m1を流し脱着させ
た。脱着液は減圧蒸留により、エタノールの除去と共に
濃縮を行いクロシン液4gを得た。得られた精製クロシ
ン液の特性値は以下の通りであった。
E'l? @ = 39.7 (440 nm) Absorbance at a wavelength of 238 nm, which is the maximum absorption of iridoid glycosides (
Az3a) and crocin have a maximum absorption wavelength of 440 n.
Ratio to absorbance at m (A44°) A isa / A 44G = 1, 66 Absorbance at wavelength 325 nm, which is the maximum absorption of polyphenols (Aszs), and wavelength 4, which is maximum absorption of crocin
Ratio to absorbance at 40 nm (A44°) A 32B / A aaa = 01482 5 g of crocin extraction aqueous solution, 20 g of acid clay (Mizuriki Ace #400 manufactured by Mizusawa Chemical Industry ■), and 50 ml of water were placed in a beaker and stirred for 10 minutes. After selectively adsorbing crocin, the mixture was suction-filtered using a Buchner funnel with an inner diameter of 9 cm lined with a filter cloth using a conventional method. Next, 200 ml of water was poured to wash the clay layer in the funnel. After washing, remove crocin adsorbed to the mouth soil.
Desorption was carried out by pouring 60 ml of a % ethanol aqueous solution. The desorption solution was distilled under reduced pressure to remove ethanol and concentrate to obtain 4 g of crocin solution. The characteristic values of the obtained purified crocin liquid were as follows.

E:e’+s =46.3 (440nm)A i、a
 / A 44゜=Q、259A321 / A440
  = 0 、 291従って、吸光度を基準としたク
ロシンの回収率、イリドイド配糖体の除去率、ポリフェ
ノール類の除去率は次のようになる。
E: e'+s = 46.3 (440 nm) A i,a
/ A 44° = Q, 259A321 / A440
= 0, 291 Therefore, the recovery rate of crocin, the removal rate of iridoid glycosides, and the removal rate of polyphenols based on absorbance are as follows.

クロシン回収率     93.3% イリドイド配糖体除去率 84.4% ポリフェノール類除去率 39.6% 未精製のクロシン抽出水溶液と精製クロシン液の吸収ス
ペクトルを第1図、第2図に示す。両図の比較により2
38amに吸収極大をもつイリドイド配糖体のピークが
ほぼ完全に消失しており、アルコールを含まない水だけ
の洗浄によってもイリドイド配糖体が除去できることが
わかる。また325amに吸収極大をもつポリフェノー
ル類のピークが大幅に減少していることがわかる。
Crocin recovery rate: 93.3% Iridoid glycoside removal rate: 84.4% Polyphenol removal rate: 39.6% The absorption spectra of the unpurified crocin extract aqueous solution and the purified crocin solution are shown in FIGS. 1 and 2. By comparing both figures, 2
The peak of iridoid glycosides having an absorption maximum at 38 am has almost completely disappeared, indicating that iridoid glycosides can be removed even by washing with only water without alcohol. It can also be seen that the peak of polyphenols having an absorption maximum at 325 am has been significantly reduced.

実施例2 洗浄液として水の代わりに15vol.%エタノール水
溶液200m1を用いて、実施例1と同様に処理を行い
、以下の特性値を有する精製クロシン液4gを得た。
Example 2 15 vol. was used instead of water as the cleaning liquid. The same treatment as in Example 1 was carried out using 200 ml of % ethanol aqueous solution to obtain 4 g of purified crocin liquid having the following characteristic values.

E+cs =41 、 0  (44,0am)Asz
a /A44゜=0. 183 A sag / A”。=0.213 クロシンの回収率、不純物の除去率は次のようになる。
E+cs =41, 0 (44,0am)Asz
a/A44°=0. 183 A sag / A”.=0.213 The recovery rate of crocin and the removal rate of impurities are as follows.

クロシン回収率      82.6%イリドイド配糖
体除去率  89.O%ポリフェノール類除去率  5
5.8%本精製クロシン液の吸収スペクトルを第3図に
示す。イリドイド配糖体のピークは完全に消失しており
、ポリフェノール類のピークも著しく減少していること
が分る。
Crocin recovery rate 82.6% Iridoid glycoside removal rate 89. O% polyphenol removal rate 5
The absorption spectrum of the 5.8% purified crocin solution is shown in FIG. It can be seen that the iridoid glycoside peak has completely disappeared, and the polyphenol peak has also decreased significantly.

実施例3 実施例1で用いたクロシン抽出液4g、酸性白土(ミズ
力エース#300 水沢化学工業■製)20g1水50
m1をビーカーに入れ10分間攪拌し、クロシンを選択
的に吸着させた後、濾布を敷いた内径9cmのブフナー
漏斗にて吸引濾過した。
Example 3 4 g of the crocin extract used in Example 1, 20 g of acid clay (Mizuriki Ace #300 manufactured by Mizusawa Chemical Industry ■) 1 50 g of water
ml was placed in a beaker and stirred for 10 minutes to selectively adsorb crocin, followed by suction filtration using a Buchner funnel with an inner diameter of 9 cm lined with a filter cloth.

次いで10vol.%エタノール水溶液100m1を流
し白土層を洗浄した。洗浄後、白土層に吸着しているク
ロシンを50vol.%エタノール水溶液60m1を流
し脱着させた。脱着液は減圧濃縮を行い、以下の特性値
を有する精製クロシン液3gを得た。
Then 10vol. % ethanol aqueous solution was poured to wash the clay layer. After washing, 50 vol. of crocin adsorbed on the clay layer. % ethanol aqueous solution was poured to allow desorption. The desorption solution was concentrated under reduced pressure to obtain 3 g of purified crocin solution having the following characteristic values.

E’1′:m =44.6 (440am)A23a 
/ A440 = 0 、 236A s2s / A
 4ao = 0 、249クロシンの回収率、不純物
の除去率は次のようになる。
E'1': m = 44.6 (440am) A23a
/ A440 = 0, 236A s2s / A
4ao = 0, the recovery rate of 249 crocin and the removal rate of impurities are as follows.

クロシン回収率      84.3%イリドイド配糖
体除去率  85.8%ポリフェノール類除去率  4
8.3%実施例4 実施例1で用いたクロシン抽出水溶液8g、活性白土(
ガレオンアースNS  水沢化学工業■製)40g、水
80m1をビーカーに入れ10分間攪拌し、クロシンを
選択的に吸着させた後、濾布を敷いた内径9cmのブフ
ナー漏斗にて吸引濾過した。次いで5 vol、%エタ
ノール水溶液400m1を流して白土層を洗浄した。洗
浄後白土だに吸着しているクロシンを40vol.%エ
タノール水溶液100m1を流し脱着させた。脱着液は
減圧濃縮を行い、以下の特性値を有する精製クロシン液
6gを得た。
Crocin recovery rate 84.3% Iridoid glycoside removal rate 85.8% Polyphenol removal rate 4
8.3% Example 4 8 g of the aqueous crocin extract solution used in Example 1, activated clay (
40 g of Galleon Earth NS (manufactured by Mizusawa Chemical Industry ■) and 80 ml of water were placed in a beaker and stirred for 10 minutes to selectively adsorb crocin, followed by suction filtration using a Buchner funnel with an inner diameter of 9 cm lined with a filter cloth. Next, 400 ml of a 5 vol, % ethanol aqueous solution was poured to wash the clay layer. After washing, 40 vol. 100 ml of % ethanol aqueous solution was poured for desorption. The desorption solution was concentrated under reduced pressure to obtain 6 g of purified crocin solution having the following characteristic values.

Elで、=46.2 (440r+m)A a3s /
 A 44゜=0.269A 5zII/ A 44゜
=0.278クロシンの回収率、不純物の除去率は次の
ようになる。
At El, =46.2 (440r+m)A a3s /
A 44° = 0.269 A 5zII / A 44° = 0.278 The recovery rate of crocin and the removal rate of impurities are as follows.

クロシン回収率      87.3%イリドイド配糖
体除去率  83.8%ポリフェノール類除去率  4
2.3%[試験例] 小麦粉1kgに、未精製のクロシン抽出水溶液及び実施
例1〜4で得られた精製クロシン液を水で希釈しE=’
rjm 0.04 (440am)に調整した液450
m1に食塩10g又は食塩10gと粉末がんすい5gを
溶解したものを加え、常法により中華生麺を作り、30
℃の恒温層に48時間保存し、色調の変化を観察した。
Crocin recovery rate 87.3% Iridoid glycoside removal rate 83.8% Polyphenol removal rate 4
2.3% [Test Example] To 1 kg of wheat flour, unpurified crocin extract aqueous solution and purified crocin liquid obtained in Examples 1 to 4 were diluted with water, and E='
Liquid 450 adjusted to rjm 0.04 (440am)
Add 10g of table salt or a solution of 10g of table salt and 5g of powdered Gansui to m1, make Chinese raw noodles by the usual method,
The sample was stored in a constant temperature bath at ℃ for 48 hours, and changes in color tone were observed.

その結果を第1表にまとめた。未精製のクロシン抽出液
の添加区はかんすい添加、無添加の両区とも変色したが
、実施例の精製クロシン液の添加区は、いずれも色調の
変化は認められなかった。
The results are summarized in Table 1. In the plots to which the unpurified crocin extract was added, there was a change in color in both the plots with and without the addition of kansui, but no change in color was observed in the plots in which the purified crocin extract of Example was added.

(以下余白) [発明の効果] 本発明のクチナシ黄色色素の精製法は上記のように措成
されており、吸着剤として安価な酸性白土及び/又は活
性白土を用いているにも拘らず、クチナシ黄色色素抽出
液中に含まれる不純物であるイリドイド配糖体とポリフ
ェノール類を同時に除去することができるので、本性に
よれば、短い工程で簡便に、しかも高回収率で精製度の
高いクチナシ黄色色素(クロシン)を得ることができる
(The following is a blank space) [Effects of the Invention] Although the method for purifying gardenia yellow pigment of the present invention is constructed as described above, and cheap acid clay and/or activated clay is used as an adsorbent, Since the iridoid glycosides and polyphenols, which are impurities contained in the gardenia yellow pigment extract, can be removed at the same time, it is possible to easily remove the iridoid glycosides and polyphenols contained in the gardenia yellow pigment extract. A pigment (crocin) can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図、2図、3図は実施例1.2における未精製のク
ロシン抽出水溶液及び精製クロシン液の吸収スペクトル
である。 特許出願人  豊玉香料株式会社 53図 1北例2の4貫1遵クロシ〉聾」っ暖収スヘリトlし手
続補正書 1.事件の表示 昭和63年特許願第140838号 2、発明の名称 クチナシ黄色色素の精製法 3、補正をする者 事件との関係 特許出願人 住所 名 称 豊玉香料株式会社 4、代理人 別紙の通り。 [補正の内容] (1)明細書第1O頁第19行の「恒温層」とあるのを
「恒温槽」と補正する。 (2)同書第11頁第1行の「抽出液」とあるのを「抽
出水溶液」と補正する。 (3)同書第12頁第1表を下記のように補正する。 (以下余白)
Figures 1, 2, and 3 are absorption spectra of the unpurified aqueous crocin extract solution and purified crocin liquid in Example 1.2. Patent Applicant Toyotama Fragrance Co., Ltd. 53 Figure 1 North Example 2 4 Kan 1 Compliance 1 Deaf” Warrant Suherit 1 Procedural Amendment 1. Description of the case 1986 Patent Application No. 140838 2 Title of the invention Method for purifying gardenia yellow pigment 3 Relationship to the case by the person making the amendment Patent applicant Address Title Toyotama Fragrance Co., Ltd. 4 Agent As per attached sheet. [Contents of amendment] (1) In the specification, page 1, line 19, "constant temperature layer" is corrected to "constant temperature bath." (2) In the first line of page 11 of the same book, "extract liquid" is corrected to "extract aqueous solution." (3) Table 1 on page 12 of the same book is amended as follows. (Margin below)

Claims (2)

【特許請求の範囲】[Claims] (1)クチナシ果実より抽出した黄色色素水溶液と酸性
白土および/又は活性白土とを接触させた後、これら白
土を分離して水又はアルコール水溶液で洗浄し、その後
、この白土から溶離液によりクチナシ黄色色素を脱着、
回収することを特徴とするクチナシ黄色色素の精製法。
(1) After bringing the yellow pigment aqueous solution extracted from gardenia fruits into contact with acidic clay and/or activated clay, these clays are separated and washed with water or an aqueous alcohol solution, and then the gardenia yellow color is obtained from this clay using an eluent. Desorbs dye,
A method for purifying gardenia yellow pigment, the method comprising recovering gardenia yellow pigment.
(2)洗浄用アルコール水溶液は5〜15vol.%ア
ルコール水溶液であり、溶離液は40vol.%以上の
高濃度のアルコール水溶液である請求項第(1)項記載
のクチナシ黄色色素の精製法。
(2) The alcohol aqueous solution for cleaning is 5 to 15 vol. % alcohol aqueous solution, and the eluent was 40 vol. The method for purifying gardenia yellow pigment according to claim (1), which is an aqueous alcohol solution with a high concentration of % or more.
JP63140838A 1988-06-08 1988-06-08 Purification of yellow dyestuff of gardenia Granted JPH01311174A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63140838A JPH01311174A (en) 1988-06-08 1988-06-08 Purification of yellow dyestuff of gardenia

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63140838A JPH01311174A (en) 1988-06-08 1988-06-08 Purification of yellow dyestuff of gardenia

Publications (2)

Publication Number Publication Date
JPH01311174A true JPH01311174A (en) 1989-12-15
JPH0415266B2 JPH0415266B2 (en) 1992-03-17

Family

ID=15277891

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63140838A Granted JPH01311174A (en) 1988-06-08 1988-06-08 Purification of yellow dyestuff of gardenia

Country Status (1)

Country Link
JP (1) JPH01311174A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995010567A1 (en) * 1993-10-13 1995-04-20 Neria De Giovanni Process for extraction of natural colours by means of bentonite
FR2940656A1 (en) * 2008-12-31 2010-07-02 Lvmh Rech COLORING MATERIALS AND THEIR USE IN COMPOSITIONS, ESPECIALLY COSMETIC COMPOSITIONS

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57151657A (en) * 1981-03-13 1982-09-18 Riken Vitamin Co Ltd Preparation of yellow pigment resistant to green discoloration

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57151657A (en) * 1981-03-13 1982-09-18 Riken Vitamin Co Ltd Preparation of yellow pigment resistant to green discoloration

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995010567A1 (en) * 1993-10-13 1995-04-20 Neria De Giovanni Process for extraction of natural colours by means of bentonite
FR2940656A1 (en) * 2008-12-31 2010-07-02 Lvmh Rech COLORING MATERIALS AND THEIR USE IN COMPOSITIONS, ESPECIALLY COSMETIC COMPOSITIONS
WO2010076545A1 (en) * 2008-12-31 2010-07-08 Lvmh Recherche Dyes and the use thereof in compositions, in particular cosmetic compositions
JP2010155830A (en) * 2008-12-31 2010-07-15 Lvmh Recherche Coloring material and composition, and their use particularly in cosmetic compositions

Also Published As

Publication number Publication date
JPH0415266B2 (en) 1992-03-17

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