JPH0453908B2 - - Google Patents

Info

Publication number
JPH0453908B2
JPH0453908B2 JP60106581A JP10658185A JPH0453908B2 JP H0453908 B2 JPH0453908 B2 JP H0453908B2 JP 60106581 A JP60106581 A JP 60106581A JP 10658185 A JP10658185 A JP 10658185A JP H0453908 B2 JPH0453908 B2 JP H0453908B2
Authority
JP
Japan
Prior art keywords
paprika
acetone
pigment
paprika pigment
extract
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 - Lifetime
Application number
JP60106581A
Other languages
Japanese (ja)
Other versions
JPS61264061A (en
Inventor
Hitoshi Toyoda
Kazutaka Ikeda
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 Seifun Group Inc
Original Assignee
Nisshin Seifun Group Inc
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 Nisshin Seifun Group Inc filed Critical Nisshin Seifun Group Inc
Priority to JP10658185A priority Critical patent/JPS61264061A/en
Publication of JPS61264061A publication Critical patent/JPS61264061A/en
Publication of JPH0453908B2 publication Critical patent/JPH0453908B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Coloring Foods And Improving Nutritive Qualities (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、パプリカ色素の製造法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for producing paprika pigment.

〔従来の技術及び発明が触決しようとする問題点〕[Problems that the prior art and invention attempt to resolve]

パプリカ色素は、ナス科の植物Capsicum
annuum L.の果皮の抽出物で、主な色素はカプ
サンチンと云われる。そして、果皮を水処理後、
石油エーテルと90%エタノールとで抽出し、色素
液を濃縮したものは、通常パプリカオレオレジン
と云われているものである。
Paprika pigment is produced by Capsicum, a plant in the Solanaceae family.
An extract of the pericarp of L. annuum, the main pigment is said to be capsanthin. After treating the peel with water,
The product obtained by extracting with petroleum ether and 90% ethanol and concentrating the pigment liquid is usually called paprika oleoresin.

これらパプリカ色素は、橙黄〜橙赤色の油溶性
の色素であつて、天然物由来の点などから、食
品、飼料、化粧品などの着色料として賞用され、
例えばサラダドレツシング、米菓用のたれ、蜜豆
用寒天、練うに、佃煮、魚のもろみ漬、ゼリー、
かば焼のたれ、パン粉、餅菓子などに添加使用さ
れている。
These paprika pigments are orange-yellow to orange-red oil-soluble pigments, and because they are derived from natural products, they are used as coloring agents for foods, feed, cosmetics, etc.
For example, salad dressing, sauce for rice crackers, agar for honey beans, sea urchin kneaded, tsukudani, moromi pickled fish, jelly,
It is used as an additive in Kabayaki sauce, bread crumbs, mochi sweets, etc.

従来パプリカから色素を採取するには、パプリ
カ色素含有物をアルカリ水溶液で処理し次に有機
溶媒又は植物油で抽出し後処理を行つてパプリカ
色素を得ている(特公昭52−3742号、同52−3809
号、同52−8741号、特開昭57−190051号、同59−
33259号など参照)。又前記方法と本質的には同一
であるが、パプリカ色素含有物をアルカリでけん
化した後、脂肪酸を不溶性の塩としてから色素を
抽出する方法がある(特開昭56−11960号参照)。
これら従来法では、それぞれけん化工程及び抽出
工程を分けているため、工程数が例えば4工程と
長く、けん化、後処理、遠心分離、減圧乾燥、有
機溶剤抽出等の操作が必要となる。それ故、操作
が煩雑となりその上処理時間が長いため、パプリ
カ色素の酸化など品質が劣化する恐れすらある。
Conventionally, to extract pigments from paprika, paprika pigments are obtained by treating paprika pigment-containing substances with an aqueous alkali solution, then extracting with an organic solvent or vegetable oil, and post-processing (Japanese Patent Publication No. 52-3742, 52 −3809
No. 52-8741, JP-A-57-190051, No. 59-
33259 etc.). Another method, which is essentially the same as the above method, is to saponify the paprika pigment-containing material with an alkali and then convert the fatty acid into an insoluble salt before extracting the pigment (see JP-A-56-11960).
In these conventional methods, since the saponification step and the extraction step are separated, the number of steps is long, for example, four steps, and operations such as saponification, post-treatment, centrifugation, vacuum drying, and organic solvent extraction are required. Therefore, the operation is complicated and the processing time is long, so there is a risk that the quality may deteriorate due to oxidation of the paprika pigment.

本発明者は、これら従来法の欠点である煩雑な
パプリカ色素含有物のけん化、抽出工程を1工程
で行い、高純度のパプリカ色素を得る方法につい
て検討した結果、本発明を見い出した。
The present inventors investigated a method for obtaining highly pure paprika pigment by carrying out the complicated saponification and extraction steps of paprika pigment-containing materials in one step, which are the disadvantages of these conventional methods, and as a result, they discovered the present invention.

〔問題点を解決するための手段〕[Means for solving problems]

即ち、本発明はパプリカ色素抽出物をアセトン
又はメチルエチルケトンの存在下苛性アルカリ水
溶液により処理し、不溶物を別し、得られた
液を濃縮して高純度パプリカ色素を得るパプリカ
色素の製造法に関する。
That is, the present invention relates to a method for producing paprika pigment in which a paprika pigment extract is treated with an aqueous caustic alkali solution in the presence of acetone or methyl ethyl ketone, insoluble materials are separated, and the resulting liquid is concentrated to obtain a highly pure paprika pigment.

本発明では、アセトン又はメチルエチルケトン
中で苛性アルカリによりけん化、脱塩を同時に行
うことによつて、パプリカ色素含有物中のトリグ
リセライド等の脂肪酸誘導体を除去し、不けん化
物である色素を濃縮することが出来る。
In the present invention, by simultaneously saponifying and desalting with a caustic alkali in acetone or methyl ethyl ketone, it is possible to remove fatty acid derivatives such as triglycerides in the paprika pigment-containing material and concentrate the unsaponifiable pigment. I can do it.

本発明に用いられるパプリカ色素抽出物は、パ
プリカ色素含有植物を有機溶媒(例えば、アセト
ン、ヘキサン、クロロホルム、エーテル等)処理
して得られたものなら何でもよい。
The paprika pigment extract used in the present invention may be any extract obtained by treating a paprika pigment-containing plant with an organic solvent (eg, acetone, hexane, chloroform, ether, etc.).

このパプリカ色素抽出物をアセトン又はメチル
エチルケトンの存在下苛性アルカリ水溶液により
処理する。この際アセトン及びメチルエチルケト
ン以外のケトンを用いると、色素の濃縮が不充分
であつたり色素がやや変質して吸光比が低下した
りする。又アルコール類では色素の分解が生じ全
く濃縮が出来ない。エーテル及び炭化水素類で
は、色素の濃縮が不充分であつて、後処理例えば
過が困難となる。アセトン又はメチルエチルケ
トンの使用量はパプリカ色素含有物に対して約5
〜10倍(v/w)又はそれ以上が好ましい。これ
より少いと反応が困難になり易い。パプリカ色素
抽出物を含むアセトン又はメチルエチルケトンに
苛性アルカリ水溶液を加える。苛性アルカリとし
ては例えば水酸化ナトリウム、水酸化カリウムな
どが挙げられる。そして濃度としては、約20〜50
重量%である。使用量は、パプリカ色素抽出物に
対して約1〜1.5倍(v/w)である。アセトン
又はメチルエチルケトンに対する苛性アルカリ水
溶液の量比は、約0.3以下好ましくは約0.2以下で
あつて、これより多いと反応に悪影響を及ぼすこ
とが多い。処理は、好ましくは撹拌下室温から沸
騰温度迄の温度で行われるが特に制限はない。処
理温度が低いと反応時間は長くなるが、約1時間
ないし数時間である。反応終了後、不溶性となつ
た脂肪酸塩を別し、液を濃縮することにより
目的を達成することが出来る。
This paprika pigment extract is treated with an aqueous caustic solution in the presence of acetone or methyl ethyl ketone. If a ketone other than acetone or methyl ethyl ketone is used in this case, the concentration of the dye may be insufficient, or the dye may be slightly altered, resulting in a decrease in the absorption ratio. In addition, alcohols cause decomposition of the pigment and cannot be concentrated at all. With ethers and hydrocarbons, the concentration of the dye is insufficient and post-treatments such as filtration are difficult. The amount of acetone or methyl ethyl ketone used is approximately 5
~10 times (v/w) or more is preferred. If the amount is less than this, the reaction tends to be difficult. Add an aqueous caustic solution to acetone or methyl ethyl ketone containing the paprika pigment extract. Examples of the caustic alkali include sodium hydroxide and potassium hydroxide. And the concentration is about 20 to 50
Weight%. The amount used is about 1-1.5 times (v/w) for paprika pigment extract. The ratio of the aqueous caustic alkali solution to acetone or methyl ethyl ketone is about 0.3 or less, preferably about 0.2 or less; if it is more than this, the reaction is often adversely affected. The treatment is preferably carried out under stirring at a temperature from room temperature to boiling temperature, but is not particularly limited. If the treatment temperature is low, the reaction time will be long, but it will be about 1 hour to several hours. After the reaction is completed, the objective can be achieved by separating the insoluble fatty acid salt and concentrating the liquid.

本発明方法には、その他の公知の処理法例えば
脱臭、香味成分の除去などを必要に応じて付加し
て、その効果を増大させることも出来る。
Other known treatment methods such as deodorization, removal of flavor components, etc. can be added to the method of the present invention as needed to increase its effectiveness.

〔実施例〕〔Example〕

次に、実施例及び参考例を示す。参考例1〜3
は、本発明に用いられるパプリカ色素抽出物の製
造の例を示し、参考例4〜5は、本発明で得られ
た生成物の辛味の除去の例を示す。
Next, examples and reference examples will be shown. Reference examples 1 to 3
shows an example of producing a paprika pigment extract used in the present invention, and Reference Examples 4 and 5 show examples of removing pungency from the product obtained in the present invention.

参考例 1 粉砕したパプリカ(ポーランド産)1Kgにアセ
トン1.5を加え、55℃で1時間加温した後室温
になるまで放冷した。抽出物を過し、残渣は新
しいアセトン1.0で洗滌し、液、洗液を合せ
て減圧下に濃縮し、油状のパプリカ色素抽出物35
gを得た。
Reference Example 1 1.5 kg of acetone was added to 1 kg of ground paprika (produced in Poland), heated at 55°C for 1 hour, and then allowed to cool to room temperature. The extract was filtered, the residue was washed with fresh acetone 1.0, and the liquid and washings were combined and concentrated under reduced pressure to obtain an oily paprika pigment extract.
I got g.

参考例 2 粉砕したパプリカ(インド産)100gにメタノ
ール150mlを加え、55℃で30分加温後、室温にな
るまで放冷した。つぎに抽出物を過し、残渣を
新しいアセトン100mlで洗滌した。残渣は、新し
いアセトン150mlと共に55℃で1時間加温し、同
様にして過し、新しいアセトン100mlで洗滌し
た。総ての液、洗液を合せて減圧下で濃縮し、
パプリカ色素抽出物7.7gを得た。
Reference Example 2 150 ml of methanol was added to 100 g of crushed paprika (produced in India), heated at 55° C. for 30 minutes, and then allowed to cool to room temperature. The extract was then filtered and the residue was washed with 100 ml of fresh acetone. The residue was heated for 1 hour at 55° C. with 150 ml of fresh acetone, filtered in the same manner and washed with 100 ml of fresh acetone. Combine all liquids and washing liquid and concentrate under reduced pressure.
7.7 g of paprika pigment extract was obtained.

参考例 3 粉砕したパプリカ(インド産)500gにアセト
ン750mlを加え55℃に加温した。ときどきかきま
ぜながら30分加温した後、加温を止め室温になる
まで放冷し、パプリカを取した。
Reference Example 3 750 ml of acetone was added to 500 g of crushed paprika (produced in India) and heated to 55°C. After heating for 30 minutes while stirring occasionally, heating was stopped and the mixture was allowed to cool to room temperature, and the paprika was removed.

この粉砕パプリカをさらに2回アセトン500ml
で同様に抽出し、液を合せた後減圧でアセトン
を留去して、パプリカ色素抽出物37.6g〔E1% 1cm
32.3(460nmクロロホルム中)、吸光比(470nmの
吸光度/454nmの吸光度)0.9659〕を得た。
Add this crushed paprika twice more to 500ml of acetone.
After extracting in the same manner, the liquids were combined and the acetone was distilled off under reduced pressure to obtain 37.6 g of paprika pigment extract [E1% 1 cm
32.3 (460 nm in chloroform), absorbance ratio (absorbance at 470 nm/absorbance at 454 nm) 0.9659].

実施例 1 参考例で得られたパプリカ色素抽出物〔E1% 1cm
32.1(460nmクロロホルム中)〕5.01gをアセトン
34mlに溶解させ、窒素雰囲気下50℃に加温し撹拌
した。これに26%苛性ソーダ水5.7mlを徐々に滴
下し、さらに同温度で2時間撹拌を続けると固形
物が析出してきた。撹拌、加温を止め、室温まで
放冷させた後、固形物を別した。少量のアセト
ンで固形物を洗い、洗液と液とを合し、減圧下
でアセトンを留去しパプリカ臭の少ないパプリカ
色素0.72g〔E1% 1cm222.3(460nmクロロホルム)〕
を得た。またこのパプリカ色素をアセトンで稀釈
し、分光光度計を用いて、吸光比(470nmの吸光
度/454nmの吸光度)を求めたところ、原料パプ
リカ色素抽出物の吸光比1.0008に対し0.9980であ
つた。
Example 1 Paprika pigment extract obtained in Reference Example [E1% 1cm
32.1 (460nm in chloroform) 5.01g in acetone
The solution was dissolved in 34 ml, heated to 50°C under nitrogen atmosphere, and stirred. 5.7 ml of 26% caustic soda water was gradually added dropwise to the mixture, and stirring was continued for 2 hours at the same temperature, resulting in the precipitation of solid matter. Stirring and heating were stopped, and the mixture was allowed to cool to room temperature, and then the solid matter was separated. Wash the solid matter with a small amount of acetone, combine the washing liquid and the liquid, and distill off the acetone under reduced pressure to obtain 0.72 g of paprika pigment with little paprika odor [E1% 1 cm222.3 (460 nm chloroform)]
I got it. In addition, this paprika pigment was diluted with acetone and the absorbance ratio (absorbance at 470 nm/absorbance at 454 nm) was determined using a spectrophotometer, and it was found to be 0.9980 compared to 1.0008 of the raw paprika pigment extract.

実施例 2 参考例2で得られたパプリカ色素抽出物〔E1% 1cm28.9(454nmアセトン中)4.99gをメチルエチル
ケトン50mlに溶解させ窒素雰囲気下40℃に加温し
撹拌した。これに25%苛性ソーダ水6mlを徐々に
滴下し、40℃で3時間撹拌を続けると固形物が析
出してきた。撹拌、加温を止め、室温まで放冷さ
せた後、固形物を別した。つぎに固形物を少量
のメチルエチルケトンで洗滌し、洗液と液とを
合し、減圧下でメチルエチルケトンを留去し、パ
プリカ臭の少ないパプリカ色素1.18g〔E1% 1cm
115.8(454nm、アセトン中)〕を得た。このパプ
リカ色素の吸光比(470nmの吸光度/454nmの吸
光度)は原料パプリカ色素抽出物の1.0008に対し
0.9874であつた。
Example 2 4.99 g of the paprika pigment extract [E1% 1 cm28.9 (in 454 nm acetone) obtained in Reference Example 2] was dissolved in 50 ml of methyl ethyl ketone, heated to 40° C. under nitrogen atmosphere, and stirred. To this, 6 ml of 25% caustic soda water was gradually added dropwise, and stirring was continued at 40°C for 3 hours, and solid matter began to precipitate. Stirring and heating were stopped, and the mixture was allowed to cool to room temperature, and then the solid matter was separated. Next, the solid matter was washed with a small amount of methyl ethyl ketone, the washing liquid and the liquid were combined, and the methyl ethyl ketone was distilled off under reduced pressure. 1.18 g of paprika pigment with little paprika odor [E1% 1 cm
115.8 (454 nm, in acetone)]. The absorbance ratio of this paprika pigment (absorbance at 470 nm/absorbance at 454 nm) is 1.0008 for the raw paprika pigment extract.
It was 0.9874.

実施例 3 実施例1において、反応を加熱還流させて行な
うほかは実施例1と同様の操作を行ない、パプリ
カ色素0.69gを得た。〔E1% 1cm220.6(460nm、クロ
ロホルム中)〕、吸収比0.9955。
Example 3 The same operations as in Example 1 were carried out except that the reaction was carried out under heating to reflux, to obtain 0.69 g of paprika pigment. [E1% 1cm220.6 (460nm, in chloroform)], absorption ratio 0.9955.

実施例 4 実施例1において、反応温度を16℃〜18℃と
し、反応時間を20時間とするほかは、実施例1と
同様に行なつてパプリカ色素0.75gを得た。〔E
1% 1cm215.4(460nm、クロロホルム中)〕、吸光比
0.9982。
Example 4 The same procedure as in Example 1 was carried out except that the reaction temperature was 16°C to 18°C and the reaction time was 20 hours to obtain 0.75 g of paprika pigment. [E
1% 1cm215.4 (460nm, in chloroform)], extinction ratio
0.9982.

実施例 5 参考例3のパプリカ色素抽出物21.70gを実施
例1と同様に処理し、パプリカ色素3.12g〔E1% 1cm215.4(460nm、クロロホルム中)、吸光比
0.9660〕とした。
Example 5 21.70 g of the paprika pigment extract of Reference Example 3 was treated in the same manner as in Example 1, and 3.12 g of paprika pigment [E1% 1 cm215.4 (460 nm, in chloroform), extinction ratio
0.9660].

実施例 6 パプリカ色素抽出物〔E1% 1cm32.1(460nm、ク
ロロホルム中)〕10.23gに20%苛性ソーダ水溶液
を18ml加え、100℃で3時間加熱撹拌した。冷却
後、反応物にアセトン150mlを加え、15分撹拌後
過し、固形物は少量のアセトンで洗滌した。
液、洗液を合せて、減圧下でアセトンを留去し、
パプリカ臭の少ないパプリカ色素1.54g〔E1% 1cm
208.8(460nm、クロロホルム中)〕を得た。
Example 6 18 ml of 20% caustic soda aqueous solution was added to 10.23 g of paprika pigment extract [E1% 1 cm32.1 (460 nm, in chloroform)], and the mixture was heated and stirred at 100°C for 3 hours. After cooling, 150 ml of acetone was added to the reaction mixture, stirred for 15 minutes, and then filtered, and the solid matter was washed with a small amount of acetone.
Combine the liquid and washing liquid and distill off the acetone under reduced pressure.
Paprika pigment with little paprika smell 1.54g [E1% 1cm
208.8 (460 nm, in chloroform)] was obtained.

実施例 7 パプリカ色素抽出物〔E1% 1cm28.9(460nm、ク
ロロホルム中)〕10.04gをイソプロピルエーテ20
mlに溶解し、26%苛性ソーダ水溶液15mlを加え、
50℃で2時間撹拌した。冷却後反応液にアセトン
130mlを加え析出した固形物を過し、固形物は
少量のアセトンで洗滌した。
Example 7 10.04g of paprika pigment extract [E1% 1cm28.9 (460nm, in chloroform)] was added to isopropyl ether20
ml, add 15 ml of 26% caustic soda aqueous solution,
Stirred at 50°C for 2 hours. Add acetone to the reaction solution after cooling.
130 ml was added and the precipitated solid matter was filtered, and the solid matter was washed with a small amount of acetone.

液、洗液を合せて減圧下で溶媒を留去し、パプ
リカ色素1.30g〔E1% 1cm220.5(460nm、クロロホ
ルム中)〕を得た。
The solution and washing solution were combined and the solvent was distilled off under reduced pressure to obtain 1.30 g of paprika pigment [E1% 1 cm220.5 (460 nm, in chloroform)].

参考例 4 実施例5で得られたパプリカ色素2.05gを50ml
のn−ヘキサンに溶解させ、95%メタノール5ml
を加え振とうした後放置し分離した下層を除去し
た。さらにこの操作を1回くり返した後n−ヘキ
サン層を分離し、n−ヘキサンを減圧で留去する
ことにより、E1% 1cm224.0(460nm、クロロホルム
中)、吸光比0.9651の香味成分が除去されたほぼ
無臭のパプリカ色素1.65gを得た。
Reference example 4 50ml of 2.05g of paprika pigment obtained in Example 5
of n-hexane and 5 ml of 95% methanol.
was added, shaken, left to stand, and the separated lower layer was removed. After repeating this operation once, the n-hexane layer was separated and the n-hexane was distilled off under reduced pressure to remove the flavor component with an E1% of 1 cm224.0 (460 nm, in chloroform) and an absorption ratio of 0.9651. 1.65 g of almost odorless paprika pigment was obtained.

〔効果〕〔effect〕

本発明によれば、パプリカ色素の濃縮が一工程
で行われるため、操作が簡単であり、コストも低
い。しかもその効果は、例えばCV10万の原料を
吸光比を全く変えることなく、CV50〜70万の生
成物へと飛躍的に精製させることが出来るもので
ある。そして、そのけん化条件が温和で、色素の
変質(パプリカ色素エステルの分解)が生じな
い。又、短時間、一工程による処理のため、空気
酸化による色素劣化が少い。
According to the present invention, since the concentration of paprika pigment is performed in one step, the operation is simple and the cost is low. Moreover, the effect is that, for example, a raw material with a CV of 100,000 can be dramatically purified into a product with a CV of 500,000 to 700,000 without changing the absorption ratio at all. Furthermore, the saponification conditions are mild, and no alteration of the pigment (decomposition of paprika pigment ester) occurs. In addition, because the process is short and one step, there is little deterioration of the dye due to air oxidation.

その上、パプリカ色素のもつ特異臭が極めて低減
する。
Moreover, the characteristic odor of paprika pigment is extremely reduced.

これらの優れた点から、本発明により天然の着
色剤としてのパプリカ色素の効用が増大される。
Because of these advantages, the utility of paprika pigment as a natural coloring agent is enhanced by the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 パプリカ色素抽出物をアセトン又はメチルエ
チルケトンの存在下苛性アルカリ水溶液により処
理し、不溶物を別し、得られた液を濃縮して
高純度パプリカ色素を得るパプリカ色素の製造
法。
1. A method for producing paprika pigment in which a paprika pigment extract is treated with an aqueous caustic alkali solution in the presence of acetone or methyl ethyl ketone, insoluble matter is separated, and the resulting liquid is concentrated to obtain a high-purity paprika pigment.
JP10658185A 1985-05-18 1985-05-18 Production of paprika dyestuff Granted JPS61264061A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10658185A JPS61264061A (en) 1985-05-18 1985-05-18 Production of paprika dyestuff

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10658185A JPS61264061A (en) 1985-05-18 1985-05-18 Production of paprika dyestuff

Publications (2)

Publication Number Publication Date
JPS61264061A JPS61264061A (en) 1986-11-21
JPH0453908B2 true JPH0453908B2 (en) 1992-08-27

Family

ID=14437177

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10658185A Granted JPS61264061A (en) 1985-05-18 1985-05-18 Production of paprika dyestuff

Country Status (1)

Country Link
JP (1) JPS61264061A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2267084B1 (en) * 2001-06-14 2016-10-19 San-Ei Gen F.F.I., Inc. Carotenoids color emulsion preparation
US7097867B2 (en) 2003-03-24 2006-08-29 Council Of Scientific And Industrial Research Process of extracting chili (capsicum) oleoresin
US7501141B2 (en) 2003-03-25 2009-03-10 Council Of Scientific And Industrial Research Process for the preparation of colorant from oleoresin
CN109370252B (en) * 2018-11-23 2020-02-21 晨光生物科技集团股份有限公司 Refining method of capsanthin pigment residue

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS523741A (en) * 1975-06-27 1977-01-12 Matsushita Electric Works Ltd Pipe for transmitting radiant heat
JPS523742A (en) * 1975-10-10 1977-01-12 Sony Corp Stand of a heating device for objects to be heated

Also Published As

Publication number Publication date
JPS61264061A (en) 1986-11-21

Similar Documents

Publication Publication Date Title
JP4029032B2 (en) Purification of xanthophyll from marigold extract containing high levels of chlorophyll
CN1332947C (en) Method for separating and purifying lutein crystal from vegetable oleoresin
JP5795572B2 (en) Method for separating carotenoid crystals from various plants
AU2005331246B2 (en) Isolation and purification of carotenoids from Marigold flowers
WO2002012159A1 (en) Process for producing oleanolic acid and/or maslinic acid
EP1963245B1 (en) Process for purification of free xanthophylls
JPWO2003029391A1 (en) Method for producing oil and fat composition containing oleanolic acid and / or maslinic acid
US8481769B2 (en) Isolation and purification of cartenoids from marigold flowers
JPH0453908B2 (en)
TWI357333B (en) Method for obtaining natural astaxanthin from eggs
US3274073A (en) Method for recovering chlorophylls from papaya plants
JPH07304977A (en) Production method of carotenoid pigment with excellent stability
JPH07304978A (en) Manufacturing method of carotenoid pigment
JPH0741687A (en) Method for producing concentrated natural red pigment oil for food and concentrated natural red pigment oil for food
JPH07304976A (en) Method for producing carotenoid pigment
JPH0799883A (en) Pickles containing concentrated Phaffia dye oil
JPS6330346B2 (en)
JPH07101827A (en) Cosmetics containing concentrated Phaffia dye oil
EP0137862A1 (en) Process for the preparation of fatty material
JPS5888353A (en) Extraction of astaxanthine from shell of crustaceas
JPH0799927A (en) Production of emulsion of concentrated and naturally occurring red coloring matter oil for food product and emulsion product therefrom
JP2001139543A (en) Crystallization of high purity carotene
JPWO2002012159A1 (en) Method for producing oleanolic acid and/or maslinic acid
JP2012070717A (en) Method for producing astaxanthin crystal