JPS61207470A - Production of concentrated paprika pigment - Google Patents
Production of concentrated paprika pigmentInfo
- Publication number
- JPS61207470A JPS61207470A JP4744585A JP4744585A JPS61207470A JP S61207470 A JPS61207470 A JP S61207470A JP 4744585 A JP4744585 A JP 4744585A JP 4744585 A JP4744585 A JP 4744585A JP S61207470 A JPS61207470 A JP S61207470A
- Authority
- JP
- Japan
- Prior art keywords
- paprika
- pigment
- alcohol
- lipase
- layer
- 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
Links
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
/ぞシリカ色素は、パプリカ(Capsicum an
nuumL、 )の果実に含まれている赤色色素であっ
て。[Detailed description of the invention] [Industrial field of application] /zo silica pigment is
It is a red pigment contained in the fruits of nuumL, ).
赤色系天然色素としそ各種の分野で広く用いられている
。It is a red natural pigment and is widely used in various fields.
本発明は、このようなパプリカ色素であって、しかも発
色性に優れ、安定で且つ臭気のない品質のすぐれた濃厚
なパプリカ色素を、工業的に有利且つ容易に高い収率で
製造する新規な方法を提供するものである。The present invention is a novel paprika pigment, which is industrially advantageous and easy to produce in high yield, and is a rich paprika pigment with excellent coloring properties, stable and odorless. The present invention provides a method.
このようにして得られたノでシリカ色素は、高品質の濃
厚な天然着色料として、飲食品、嗜好物。The silica pigment obtained in this way is used as a high-quality, concentrated natural coloring agent in foods, beverages, and luxury foods.
医薬品、香粧品等の産業技−分野において広く且つ重用
されるものである。It is widely and importantly used in industrial technology fields such as pharmaceuticals and cosmetics.
従来パプリカ色素の製造方法として、パプリカ果実やそ
の乾燥粉末などを、大豆油、菜種油、ヤシ油、綿実油、
コーンオイル、魚油などの動植物性油で抽出して5.J
シリカ色素をこれら油中へ溶出する油溶法及びアルコー
ル類、ケトン類、やハロゲレ化炭化水素類などの有機溶
媒で抽出する溶剤法、その他の方法が知られている。Traditionally, paprika pigments have been produced using paprika fruit and its dried powder, etc., using soybean oil, rapeseed oil, coconut oil, cottonseed oil,
5. Extract with animal and vegetable oils such as corn oil and fish oil. J
Oil-dissolution methods in which silica pigments are eluted into these oils, solvent methods in which they are extracted with organic solvents such as alcohols, ketones, and halogenated hydrocarbons, and other methods are known.
しかしながらかかる方法では、濃厚な色素溶液を得るこ
とはむずかしく、且つ得られた色素はノξプリカ特有の
異臭を伴っている。However, with this method, it is difficult to obtain a concentrated dye solution, and the obtained dye is accompanied by an unusual odor peculiar to No.
これらの欠点を改善するための方法として、アルカリ水
溶液で加熱処理し、該色素を有機溶剤処理する方法も撓
案されている(4!公昭52−!1742号)。As a method for improving these drawbacks, a method has been proposed in which heat treatment is performed with an alkaline aqueous solution and the dye is treated with an organic solvent (4! Publication No. 52-1742).
しかし上記提案方法においてはアルカリ処理生成分は固
形物となるため、色素抽出効率も悪く且つ操作が著しく
煩雑で工業−製造に適さないという欠点を有している。However, in the above-mentioned proposed method, since the alkali-treated product becomes a solid substance, the dye extraction efficiency is poor and the operation is extremely complicated, making it unsuitable for industrial production.
そしてまた、アルカリ処理によって色素エステル自体が
加水分解されるために1色調が変化したυ退色したりす
るし、濃厚な色素を調製しようとしても色素が析出して
しまい、所期の目的を達成することができない。Furthermore, the dye ester itself is hydrolyzed by alkali treatment, resulting in a change in one color tone or fading, and even if you try to prepare a rich dye, the dye will precipitate, making it difficult to achieve the desired purpose. I can't.
以上のように、従来技術によったのでは、濃厚ノぞプリ
カ色素はもとよシ、通常のノぞプリカ色素でさえも、こ
れを有利に且つ満足できる程度に調製することはできな
かったのである。As described above, it has not been possible to advantageously and satisfactorily prepare concentrated Nozopurika pigments, or even ordinary Nozopurika pigments, using conventional techniques. It is.
本発明は、このような欠点を解決するため罠なされたも
のであって1発色性に優れ、濃厚、安定で臭気の表い良
好なパプリカ色素を工業的に有利且、容易に好収率で製
造することを目的とするものである。The present invention has been made to solve these drawbacks, and is to produce a paprika pigment that has excellent color development, is rich, stable, and exhibits no odor, and is industrially advantageous and easy to produce in good yield. The purpose is to manufacture.
本発明は上記目的を達成するためKなされたものであっ
て、物理的、化学的方法のみに依存したのでは所期の目
的を達成することができないとの観点にたち、従来から
の発想を根本的に転換して生物学的方法に着目するに至
った。The present invention has been made to achieve the above object, and based on the viewpoint that the desired object cannot be achieved by relying only on physical and chemical methods, the present invention is based on the conventional idea. This led to a fundamental shift and focus on biological methods.
そして生物学的方法について各方面から検討した結果、
酵素を利用する方法が有効であるとの知見を得、この新
知見を基礎として酵素について広範なスクリーニングを
行い、リパーゼ処理が極めて有効であることをつきとめ
た。As a result of examining biological methods from various angles,
They found that a method using enzymes is effective, and based on this new knowledge, they conducted extensive screening for enzymes and found that lipase treatment is extremely effective.
しかしながら、リノで−ゼ処理のみでは目的とする高品
位の濃厚ノセプリカ色素は得ることができず。However, it is not possible to obtain the desired high-grade, concentrated noseplica pigment only by the Lino-de-ze treatment.
更に後処理をする必要がある。そこで後処理として、有
機溶媒による分配抽出処理をリパーゼ処理に有機的に結
合する着想を得、ことに本発明の完成をみたのである。Further post-processing is required. Therefore, as a post-treatment, they came up with the idea of organically combining a partition extraction process using an organic solvent with a lipase treatment, and particularly completed the present invention.
すなわち本発明は、パプリカ及び/又はその処理物をリ
パーゼ処理して、ノブリカ色素エステルは変化させるこ
となく、悪臭成分であるところの脂肪分のみを選択的に
ケン化せしめた後、副生ずる脂肪酸、臭気成分を有機溶
媒を利用して洗滌除去することを重要なポイントとする
濃厚パプリカ色素の製法に係るものである。That is, the present invention subjects paprika and/or its processed product to lipase treatment to selectively saponify only the fat component, which is a malodorous component, without changing the Noblica pigment ester, and then to process the by-produced fatty acids, The present invention relates to a method for producing a concentrated paprika pigment, in which the important point is to wash and remove odor components using an organic solvent.
処理原料としては、/ツブリカそれ自体及び/又はその
処理物を使用する。パプリカ処理物としては、パプリカ
・オレオレジン、/J!デリカの(粗)抽出物、パプリ
カ磨砕物、パプリカ搾汁液、その濃縮液、その凍結乾燥
粉末、及びパプリカの乾燥粉末等が自由に使用できる。As the raw material for treatment, the turmeric itself and/or its treated product are used. Paprika processed products include paprika oleoresin, /J! Delica (crude) extract, ground paprika, paprika juice, concentrated liquid thereof, freeze-dried powder thereof, dried powder of paprika, etc. can be freely used.
これら処理原料のリパーゼ処理生成物は石けん様固形物
になることがなく、臭気の主因である脂肪分のみが選択
的にケン化されている。そこでこのリパーゼ処理生成物
を有機溶媒に溶解する。有機溶媒としては、はンタン、
ヘキサン、ヘプタン。The lipase-treated products of these treated raw materials do not become soap-like solids, and only the fat content, which is the main cause of odor, is selectively saponified. The lipase-treated product is then dissolved in an organic solvent. As an organic solvent, hantan,
Hexane, heptane.
オクタン、ノナン、デカン等のパラフィン系炭化水素、
ベンゼン、キシレン等の芳香族炭化水素。Paraffin hydrocarbons such as octane, nonane, decane,
Aromatic hydrocarbons such as benzene and xylene.
Jl’/−ル、エタノール、ブタノール、プロパツール
等のアルコール類、ケトン類、ハロゲン化炭化水素等が
広く使用される。Alcohols, ketones, halogenated hydrocarbons, and the like are widely used.
これらの有機溶媒に溶解した後、含水苛性アルカリ−ア
ルコール溶液、含水アルコール溶液を用いて洗滌して、
脂肪酸及び悪臭成分を除去すれば。After dissolving in these organic solvents, washing with a hydrous caustic alkaline-alcohol solution and a hydrous alcohol solution,
If fatty acids and malodorous components are removed.
発色性に優れた。安定で且つ臭気のない高品質の濃厚な
/ζシリカ色素を工業的に有利に好収率で製造すること
ができる。含水苛性アルカリ−アルコール溶液、含水ア
ルコール溶液処理の順序は適宜でよいし、必要ある場合
は片方の溶液による処理でも充分に洗滌の効果が得られ
る。また必要ある場合には、苛性アルカリ及び/又はア
ルコールの濃度を変化させ又は変化させることなく、こ
れらの洗滌処理をくシ返してもよい。苛性アルカリとし
ては、苛性ソーダ、苛性カリが使用され、アルコールと
しては、メタノール、エタノール、プロパツール、ブタ
ノールその他のアルコール類が自由に使用できる。Excellent color development. A stable, odorless, high-quality, concentrated /ζ silica dye can be industrially advantageously produced in a good yield. The order of treatment with the hydrated caustic alkaline-alcohol solution and the hydrated alcohol solution may be arbitrary, and if necessary, a sufficient cleaning effect can be obtained by treatment with one of the solutions. If necessary, these washing treatments may be repeated with or without changing the concentration of caustic alkali and/or alcohol. As the caustic alkali, caustic soda and caustic potash are used, and as the alcohol, methanol, ethanol, propatool, butanol, and other alcohols can be freely used.
リパーゼとしては、各種起源の9、−J−ゼが広く使用
されるが、例えば、97J−ゼMY、リパーゼAP、リ
パーゼ(サイクン)等微生物起源の市販の酵素が有利に
使用できる。リパーゼ処理を行うに当っては、リパーゼ
0.1〜5.好ましくは0.5〜1重量に対し、水50
〜500. 好ましくは150〜250重量を加えて
溶解した後、ノRプリカ又はその処理物50〜500.
好ましくは150〜250重量を加え、15〜40’C
1好ましくは20〜30℃にて1〜20時間、好ましく
は5〜10時間、撹拌してケン化反応を行えばよい。な
お、とのケン化反応中に、前以ってn−ヘキサンといっ
た有機溶媒を加えておいてもよい。As the lipase, 9,-J-ases of various origins are widely used, and commercially available enzymes of microbial origin, such as 97J-se MY, Lipase AP, and Lipase (Cykun), can be advantageously used. When performing lipase treatment, lipase 0.1 to 5. Preferably 0.5 to 1 weight to 50% water
~500. Preferably, after adding and dissolving 150 to 250 weight, 50 to 500.
Preferably add 150 to 250 weight and heat at 15 to 40'C.
1. The saponification reaction may be carried out by stirring preferably at 20 to 30°C for 1 to 20 hours, preferably 5 to 10 hours. Note that an organic solvent such as n-hexane may be added in advance during the saponification reaction.
クン化終了後、n−ヘキサン等有機溶媒を加えて撹拌し
た後、下層を分液し、パプリカ色素含有有機溶媒層を含
水苛性カリ−アルコール溶液を用いて洗滌する。苛性カ
リ−アルコール溶液の濃度は、それぞれ、1〜l0ts
、50〜90チ程度とするのがよく、特に好適な値は3
〜5チ、70〜80チである。次いで% 50〜95%
、好ましくは80チアルコール溶液で洗滌して、脂肪酸
、臭気成分を完全に除去する。洗滌処理の順序はこの逆
でもよいし、どちらか一方でもよいし、tた。After completion of curing, an organic solvent such as n-hexane is added and stirred, the lower layer is separated, and the paprika pigment-containing organic solvent layer is washed with a hydrous caustic potassium alcohol solution. The concentration of the caustic potash alcohol solution is 1 to 10ts, respectively.
, it is good to set it to about 50 to 90 inches, and a particularly suitable value is 3
-5 inches, 70-80 inches. Then% 50-95%
, preferably with an 80% alcohol solution to completely remove fatty acids and odor components. The order of the cleaning treatment may be the reverse of this order, or either one or the other.
処理をくシ返してもよい。洗滌処理終了後、n −ヘキ
サンといった有機溶媒を留去して、高品質の濃厚ノぐプ
リカ色素を得る。You may also repeat the process. After the washing process is completed, the organic solvent such as n-hexane is distilled off to obtain a high quality, concentrated Nogpurika dye.
本発明の方法で得られるパプリカ色素は、天然着色料と
して次の様な著効を持っている。The paprika pigment obtained by the method of the present invention has the following remarkable effects as a natural coloring agent.
■ 発色性に優れ1色相が経時的に安定である。■ Excellent color development and one hue is stable over time.
■ 製造操作が安全かつ容易である。■ Manufacturing operations are safe and easy.
■ 色調がオレオレジンのそれと殆んど同一である。■The color tone is almost the same as that of oleoresin.
■ タンニン等フェノール性物質が完全に除去されてい
る。■ Phenolic substances such as tannins are completely removed.
■ 無臭で品質的に優れている。■ It is odorless and has excellent quality.
■ 高濃度においても色素が析出しない。■ Dye does not precipitate even at high concentrations.
本発明パプリカ色素は、天然着色料として飲食物、嗜好
物、医薬品、香粧品、その他の幅広い分野に利用可能で
ある。The paprika pigment of the present invention can be used as a natural coloring agent in a wide range of fields such as food and beverages, luxury foods, pharmaceuticals, cosmetics, and others.
パプリカ色素の製造に当ってリパーゼを使用する試みは
従来未知の新規な技術であって 9a!!−ゼ処理と有
機溶媒処理とを有機的に結合することによって、はじめ
て、極めて有利に高品位の濃厚パプリカ色素を得ること
ができる。The attempt to use lipase in the production of paprika pigment is a new and previously unknown technology, and 9a! ! Only by organically combining the -ze treatment and the organic solvent treatment can very advantageous high-grade concentrated paprika pigments be obtained.
実施例1゜
リパーゼMY1gを水200.9に溶解後、ノξプリカ
・オレオレジン(カラーバリユー82.500)200
gを加える。さらにn−ヘキサン200Iを加え、常温
にて4時間撹拌反応する。反応終了後n−ヘキナン60
0Iを加え、攪拌溶解後、静置し下層を分液する。Example 1 After dissolving 1 g of lipase MY in 200.9 g of water, 200 g of No.
Add g. Furthermore, 200 I of n-hexane was added, and the mixture was stirred and reacted at room temperature for 4 hours. After completion of the reaction, 60 n-hexane
Add 0I, stir and dissolve, then leave to stand and separate the lower layer.
ノ々シリカ含有n−ヘキサン層(上層)を90%エタノ
ール600gで洗浄し、さらに15N−75チエタノー
ル水溶液600J/にて洗浄する。The Nono silica-containing n-hexane layer (upper layer) is washed with 600 g of 90% ethanol, and further washed with 600 J/of a 15N-75 diethanol aqueous solution.
らいで80−エタノール溶液300gにて3回洗浄後、
n−ヘキサンを回収し、濃厚パプリカ48Jを得た。After washing three times with 300 g of leprosy 80-ethanol solution,
N-hexane was collected to obtain 48J of concentrated paprika.
カラーバリユーは355.100で無臭の品質の優れた
パプリカ色素であった。The color value was 355.100, and the paprika color was odorless and of excellent quality.
実施例2 リパーゼMY500pを水100#IC溶解し。Example 2 Dissolve lipase MY500p in 100 #IC of water.
パプリカ・オレオレジン(カラーバリユー97.280
)10 QIcg、 n−ヘキサン100ノを加え、常
温にて6時間ケン化反応を行った。Paprika Oleoresin (Color Value 97.280
) 10 QIcg and 100 g of n-hexane were added, and a saponification reaction was carried out at room temperature for 6 hours.
ケン化反応終了後、n−へキサン′500ノを加え、分
液後パプリカ含有n−ヘキサン層(上層)をエタノール
280峠−水15#にて洗浄し、さらにエタノール20
0#−水73#−カセイカリ9に9にて洗浄後、エタノ
ール170kg−水40IcIIにて2回洗浄した。After the saponification reaction, 500 g of n-hexane was added, and after separation, the paprika-containing n-hexane layer (upper layer) was washed with 280 ethanol and 15 # of water, and then 200 g of ethanol was added.
After washing with 170 kg of ethanol and 40 IcII of water, the sample was washed twice with 170 kg of ethanol and 40 IcII of water.
その後れ−へキサンを回収し、パプリカ23#を得た。Thereafter, hexane was recovered to obtain Paprika 23#.
カラーバリユーは822.620で無臭の優れた/ぞプ
リカ色素であった。The color value was 822.620, and it was an odorless and excellent pigment.
代理人 弁理士 戸 83 R男 手続補正書 昭和60年11月15日Agent: Patent attorney, Todo 83, R-man Procedural amendment November 15, 1985
Claims (1)
有機溶媒を用いて分配抽出処理することを特徴とする高
品質の濃厚パプリカ色素の製造方法。1. A method for producing a high-quality concentrated paprika pigment, which comprises treating paprika or a processed product thereof with lipase, and then subjecting it to partition extraction treatment using an organic solvent.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4744585A JPS61207470A (en) | 1985-03-12 | 1985-03-12 | Production of concentrated paprika pigment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4744585A JPS61207470A (en) | 1985-03-12 | 1985-03-12 | Production of concentrated paprika pigment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61207470A true JPS61207470A (en) | 1986-09-13 |
JPS6330346B2 JPS6330346B2 (en) | 1988-06-17 |
Family
ID=12775340
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4744585A Granted JPS61207470A (en) | 1985-03-12 | 1985-03-12 | Production of concentrated paprika pigment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61207470A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002059341A1 (en) * | 2001-01-26 | 2002-08-01 | Fuji Chemical Industry Co., Ltd. | Method of purifying crude xanthophylls |
CN106700642A (en) * | 2016-12-29 | 2017-05-24 | 河南中大恒源生物科技股份有限公司 | Purifying method of capsanthin |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5337253A (en) * | 1976-09-20 | 1978-04-06 | Hitachi Ltd | Detection method of eroded position of hydraulic machine by cavitation |
JPS57133160A (en) * | 1981-02-13 | 1982-08-17 | T Hasegawa Co Ltd | Preparation of paprica dyestuff |
JPS58173163A (en) * | 1982-04-05 | 1983-10-12 | San Ei Chem Ind Ltd | Production of carotenoid coloring matter |
JPS5934736A (en) * | 1982-08-23 | 1984-02-25 | Matsushita Electric Ind Co Ltd | State display system of radio device |
-
1985
- 1985-03-12 JP JP4744585A patent/JPS61207470A/en active Granted
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5337253A (en) * | 1976-09-20 | 1978-04-06 | Hitachi Ltd | Detection method of eroded position of hydraulic machine by cavitation |
JPS57133160A (en) * | 1981-02-13 | 1982-08-17 | T Hasegawa Co Ltd | Preparation of paprica dyestuff |
JPS58173163A (en) * | 1982-04-05 | 1983-10-12 | San Ei Chem Ind Ltd | Production of carotenoid coloring matter |
JPS5934736A (en) * | 1982-08-23 | 1984-02-25 | Matsushita Electric Ind Co Ltd | State display system of radio device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002059341A1 (en) * | 2001-01-26 | 2002-08-01 | Fuji Chemical Industry Co., Ltd. | Method of purifying crude xanthophylls |
CN106700642A (en) * | 2016-12-29 | 2017-05-24 | 河南中大恒源生物科技股份有限公司 | Purifying method of capsanthin |
Also Published As
Publication number | Publication date |
---|---|
JPS6330346B2 (en) | 1988-06-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101691520B (en) | Walnut oil refining method | |
FR2567149A1 (en) | PROCESS FOR THE EXTRACTION OF POLY-BETA-HYDROXYBUTYRATES USING A SOLVENT FROM AN AQUEOUS SUSPENSION OF MICROORGANISMS | |
CN108373953A (en) | A kind of soapberry ferment handmade soap and preparation method thereof | |
CN107858202A (en) | Selenium-rich tea oil and its processing technology | |
JPS6035057A (en) | Production of yellowish orange to reddish orange dye | |
JPS61207470A (en) | Production of concentrated paprika pigment | |
KR20020000660A (en) | Pigment extraction of chlorophyll and carotenoid from seaweed, crustacea and echinoderm using supercritical and subcritical CO2 with entrainer | |
JPS62115067A (en) | Production of concentrated paprika pigment | |
CN110256238A (en) | A kind of refining methd of long-chain mixed dibasic acid | |
CN104844441B (en) | A kind of method of purification of long-chain mixed dibasic acid | |
CN101210113A (en) | Preparation method of oil-soluble citrus yellow pigment | |
JP4125532B2 (en) | Quality improvement and bleaching method of crude rice bran wax and quality improved rice bran wax | |
JPH0119826B2 (en) | ||
JPS58173164A (en) | Production of paprika coloring matter | |
JPH07304977A (en) | Production of carotenoid dyestuff excellent in stability | |
CN1951929A (en) | Oil-soluble red rice red pigment and oil-soluble red rice yellow pigment and its preparation method | |
CN111393280A (en) | Decanedioic acid decoloring method | |
JP2004208504A (en) | Method for producing astaxanthin-containing yeast extract | |
JPS6390598A (en) | Production of lipid containing docosahexaenic acid | |
JPS5950704B2 (en) | Manufacturing method of paprika pigment | |
JPS61264061A (en) | Production of paprika dyestuff | |
US2717210A (en) | Method of obtaining concentrates of carotene | |
JPS6368511A (en) | Cosmetic | |
JPH083468A (en) | Production of colorant, production of colored seaweed extract, and production of seaweed food material | |
Norfaezah et al. | Comparative study between microwave assisted extraction and Soxhlet extraction techniques for bio-oil extraction from Jatropha curcas |