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JPH0433838B2 - - Google Patents

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Publication number
JPH0433838B2
JPH0433838B2 JP57123007A JP12300782A JPH0433838B2 JP H0433838 B2 JPH0433838 B2 JP H0433838B2 JP 57123007 A JP57123007 A JP 57123007A JP 12300782 A JP12300782 A JP 12300782A JP H0433838 B2 JPH0433838 B2 JP H0433838B2
Authority
JP
Japan
Prior art keywords
fatty acid
hufa
lower alcohol
lipase
acid
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
JP57123007A
Other languages
Japanese (ja)
Other versions
JPS5914793A (en
Inventor
Yasuhisa Noguchi
Hidehiko Hibino
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.)
NOF Corp
Original Assignee
Nippon Oil and Fats 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 Nippon Oil and Fats Co Ltd filed Critical Nippon Oil and Fats Co Ltd
Priority to JP12300782A priority Critical patent/JPS5914793A/en
Publication of JPS5914793A publication Critical patent/JPS5914793A/en
Publication of JPH0433838B2 publication Critical patent/JPH0433838B2/ja
Granted legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Fats And Perfumes (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は脂肪酸低級アルコールエステルからそ
の中に含まれる高度不飽和脂肪酸低級アルコール
エステル(以下これをHUFAという)を濃縮分
離する方法に関する。 従来、動植物油、とりわけ魚油に含まれる高度
不飽和脂肪酸は主として魚類に対する必須脂質と
して配合飼料などの形で添加用いられてきたが、
最近では人間に対する生理活性とそれに基づく薬
理効果が解明されて、その有用性が確認されてい
る。しかしながらHUFAの濃縮分離に関して、
魚油あるいは海産生物よりの油脂をエステル化
し、それを原料として工業的規模で濃縮分離する
方法はまだ確立されていない。 従来からの脂肪酸エステルでの分別技術として
(1)自然分別法、(2)分子蒸留法、(3)溶剤分別法、(4)
尿素付加法などが見られる。 しかし(1)の方法はコストがかからないという利
点はあるが、HUFAのごとき低融点の油脂に対
しては使用しにくく、しかも結晶化に長時間を要
し、収率は高くない。(2)の方法はHUFAのよう
な二重結合の多いものの場合、重合や異性化が生
じやすく使用しにくい。(3)の方法は(1)の方法と比
較して結晶化が容易で、液の粘度も低いためろ過
効率も良く、収率も高い。しかし高濃度で
HUFAを得るためには低温を必要とし、ランニ
ングコストが高くなる。(4)の方法は(1)、(2)、(3)の
方法と比較して、高濃度でHUFAが得られ、す
ぐれた方法である。しかし多量の尿素やメタノー
ルなどの溶剤を必要とし、反応液中からHUFA
を回収するのは容易でない。 本発明者らはこれらの欠点を改良するために研
究した結果、特定のリパーゼを利用してHUFA
を簡便に得るための工業的に有利な方法を発明し
た。 本発明は、脂肪酸低級アルコールエステルをリ
ゾープス属、エスペルギルス属、ムコール属のい
ずれかから得られたリパーゼの基質特異性を利用
して選択的に加水分解させ、ついで分解させた脂
肪酸を除去することを特徴とするHUFAの濃縮
分離方法を提供するものである。 本発明におけるHUFAの高度不飽和脂肪酸は、
1分子当り炭素数が20以上、二重結合数3個以上
を有する長鎖脂肪酸の内で、生理活性を有するω
−3酸(オメガ−3酸、ω−3は脂肪酸の二重結
合が末端メチル基側から3番目に位置する)とω
−6酸(オメガ−6酸、ω−6は脂肪酸の二重結
合が末端メチル基側から6番目に位置する)を主
に対象とするものであり、このいずれもが生体内
で大きな意義を持つ高い生理活性を有している。 このような脂肪酸としてはC20:3ω−3(エイ
コサトリエン酸)、C20:4ω−3(エイコサテトラ
エン酸)、C20:5ω−3(エイコサペンタエン酸)、
C22:5ω−3(ドコサペンタエン酸)、C22:6ω−
3(ドコサヘキサエン酸)のごときω−3酸、
C20:3ω−6(エイコサトリエン酸)、C20:4ω−
6(エイコサテトラエン酸又はアラキドン酸)、
C22:3ω−6(ドコサトリエン酸)、C22:4ω−6
(ドコサテトラエン酸)、C22:5ω−6(ドコサペ
ンタエン酸)、C22:4ω−6(テトラコサテトラエ
ン酸)のごときω−6酸があげられ、二重結合は
シス位置で示されるものである。 本発明の方法で使用される脂肪酸低級アルコー
ルエステルは高度不飽和脂肪酸を含む油脂又は脂
肪酸とメタノール、エタノール、プロパノール、
ブタノールなどの低級アルコールとで合成された
エステルで、好ましくはメタノール、エタノール
とのエステルである。具体例を示せば魚油、肝油
などの海産動物油をはじめとする各種動植物油類
とエタノールを触媒の存在下エステル交換して得
られる脂肪酸エチルエステルなどである。 本発明において、リパーゼの基質特異性とは、
通常の脂肪酸低級アルコールエステルはリパーゼ
により分解されるが、HUFAはリパーゼにより
分解されにくいという性質を指している。 本発明に用いるリパーゼは微生物起源のリパー
ゼであり、リゾープス属起源のもの、アスペルギ
ルス属起源のもの、ムコール属起源のものであ
る。 本発明において、脂肪酸低級アルコールエステ
ルの加水分解時の温度やPHはそのリパーゼに適し
たものを用いればよく、緩衝液や乳化剤は用いて
も用いなくてもよいが、乳化剤を用いる場合は加
水分解物とリパーゼ溶液との分離が容易でない。
リパーゼ量はその活性に応じ適当量用いればよ
く、リパーゼ溶液は再使用できる。リパーゼ溶液
量は脂肪酸低級アルコールエステルと同量程度あ
ればよく、均一な乳化ができればよい。 加水分解後のHUFAの回収は一般的な油脂の
脱酸方法に準じることができる。すなわち、加水
分解液を遠心分離によりリパーゼ溶液と油分にわ
け、HUFAと脂肪酸の混合物である油分にアル
カリ水溶液を加えて中和し、脂肪酸を石ケンと
し、遠心分離によりHUFAと石ケン水とに分離
することができる。 本発明の方法によれば、従来の方法と異なり、
溶剤を使用する必要がなく、反応温度も40℃前後
であり、重合や異性化は生じない。しかも簡単な
操作でHUFAを濃縮分離することができる。 次に本発明の実施例について説明する。 実施例 1 イワシ、サバなどの雑魚油をナトリウムメチラ
ートを触媒としてエタノールと反応させ脂肪酸エ
チルエステルを得た。脂肪酸組成は表−1に示す
通りであつた。 この脂肪酸エチルエステル100gを反応器に入
れ、窒素気流下30000ユニツトのリゾープス属起
源のリパーゼ(田辺製薬(株)、製品)を含むイオン
交換水100gを加えて40℃で12時間撹拌しながら
加水分解させた。反応後遠心分離により油分を得
た。得られた油分の酸価は74.5であつた。この油
分をカセイソーダ水溶液で中和し、遠心分離によ
り石ケン水を除去し、52gのHUFAを得た。こ
のHUFAの脂肪酸組成は表−1に示す通りであ
つた。表−1の結果から特にC20:5ω−3と
C22:6ω−3成分の増加が著しいことがわかる。
(以下の実施例の効果についても同様である) 実施例 2 実施例−1の脂肪酸エチルエステルを実施例−
1と同様に50000ユニツトのアスペルギルス属起
源のリパーゼ(天野製薬(株)、製品)を用い40℃で
24時間加水分分解させた。そのときの酸価は50.7
であり、中和、遠心分離処理後の62gのHUFA
を得た。このHUFAの脂肪酸組成は表−1に示
す通りであつた。 実施例 3 実施例−1と同じ雑魚油から同様にして得た脂
肪酸メチルエステルを実施例−1と同様に50000
ユニツトのムコール属起源のリパーゼ(天野製薬
(株)、製品)を用い30℃で24時間加水分解させた。
そのときの酸価は98.8であり、中和、遠心分離処
理後44.5gのHUFAを得た。このHUFAの脂肪
酸組成は表−1に示す通りであつた。
The present invention relates to a method for concentrating and separating highly unsaturated fatty acid lower alcohol esters (hereinafter referred to as HUFA) contained therein from fatty acid lower alcohol esters. Conventionally, highly unsaturated fatty acids contained in animal and vegetable oils, especially fish oil, have been added to fish as essential lipids in the form of compounded feed, etc.
Recently, its physiological activity and pharmacological effects on humans have been elucidated, and its usefulness has been confirmed. However, regarding the concentration and separation of HUFA,
A method for esterifying fish oil or fats from marine organisms and concentrating and separating it as a raw material on an industrial scale has not yet been established. As a conventional fractionation technology using fatty acid esters
(1) Natural fractionation method, (2) Molecular distillation method, (3) Solvent fractionation method, (4)
Examples include urea addition method. However, although method (1) has the advantage of being low cost, it is difficult to use for oils and fats with low melting points such as HUFA, and furthermore, it takes a long time to crystallize, and the yield is not high. Method (2) is difficult to use for materials with many double bonds, such as HUFA, as polymerization and isomerization tend to occur. Compared to method (1), method (3) allows easier crystallization, has a lower liquid viscosity, has better filtration efficiency, and has a higher yield. But at high concentrations
Obtaining HUFA requires low temperatures, which increases running costs. Method (4) is superior to methods (1), (2), and (3), as it allows HUFA to be obtained at a higher concentration. However, it requires large amounts of solvents such as urea and methanol, and HUFA is removed from the reaction solution.
is not easy to recover. The present inventors conducted research to improve these shortcomings, and found that HUFA was produced using a specific lipase.
We have invented an industrially advantageous method for easily obtaining . The present invention involves selectively hydrolyzing fatty acid lower alcohol esters by utilizing the substrate specificity of lipase obtained from any of the genus Rhizopus, Espergillus, and Mucor, and then removing the decomposed fatty acids. The present invention provides a method for concentrating and separating characteristic HUFA. The highly unsaturated fatty acids of HUFA in the present invention are:
Among long-chain fatty acids with 20 or more carbon atoms and 3 or more double bonds per molecule, ω that has physiological activity.
-3 acid (omega-3 acid, ω-3 is a fatty acid whose double bond is located third from the terminal methyl group) and ω
It mainly targets -6 acids (omega-6 acids, where the fatty acid double bond is located at the 6th position from the terminal methyl group), and both of these have great significance in the body. It has high physiological activity. Such fatty acids include C20:3ω-3 (eicosatrienoic acid), C20:4ω-3 (eicosatetraenoic acid), C20:5ω-3 (eicosapentaenoic acid),
C22:5ω-3 (docosapentaenoic acid), C22:6ω-
omega-3 acids such as 3 (docosahexaenoic acid),
C20:3ω-6 (eicosatrienoic acid), C20:4ω-
6 (eicosatetraenoic acid or arachidonic acid),
C22:3ω-6 (docosatrienoic acid), C22:4ω-6
(docosatetraenoic acid), C22:5ω-6 (docosapentaenoic acid), and C22:4ω-6 (tetracosatetraenoic acid), where the double bond is shown in the cis position. It is something. The fatty acid lower alcohol ester used in the method of the present invention is a mixture of fats and oils containing highly unsaturated fatty acids or fatty acids, methanol, ethanol, propanol,
An ester synthesized with a lower alcohol such as butanol, preferably an ester with methanol or ethanol. Specific examples include fatty acid ethyl esters obtained by transesterifying various animal and vegetable oils, including marine animal oils such as fish oil and cod liver oil, with ethanol in the presence of a catalyst. In the present invention, the substrate specificity of lipase is
Normal fatty acid lower alcohol esters are decomposed by lipase, but HUFA refers to the property that it is difficult to be decomposed by lipase. The lipase used in the present invention is a lipase of microbial origin, such as one originating from the genus Rhizopus, one originating from the genus Aspergillus, and one originating from the genus Mucor. In the present invention, the temperature and PH during hydrolysis of fatty acid lower alcohol ester may be set to those suitable for the lipase, and buffers and emulsifiers may or may not be used, but if an emulsifier is used, hydrolysis It is not easy to separate the substance from the lipase solution.
An appropriate amount of lipase may be used depending on its activity, and the lipase solution can be reused. The amount of lipase solution should be about the same amount as the fatty acid lower alcohol ester, and it is sufficient if uniform emulsification can be achieved. Recovery of HUFA after hydrolysis can be performed in accordance with a general method for deoxidizing fats and oils. That is, the hydrolyzed solution is separated into a lipase solution and oil by centrifugation, the oil, which is a mixture of HUFA and fatty acids, is neutralized by adding an alkaline aqueous solution, the fatty acids are made into soap, and the HUFA and soap water are separated by centrifugation. Can be separated. According to the method of the present invention, unlike conventional methods,
There is no need to use a solvent, the reaction temperature is around 40°C, and no polymerization or isomerization occurs. Moreover, HUFA can be concentrated and separated with simple operations. Next, examples of the present invention will be described. Example 1 Fatty acid ethyl ester was obtained by reacting small fish oil such as sardine and mackerel with ethanol using sodium methylate as a catalyst. The fatty acid composition was as shown in Table-1. 100g of this fatty acid ethyl ester was placed in a reactor, 100g of ion-exchanged water containing 30,000 units of lipase originating from the genus Rhizopus (Tanabe Seiyaku Co., Ltd., product) was added under a nitrogen stream, and the mixture was hydrolyzed with stirring at 40°C for 12 hours. I let it happen. After the reaction, oil was obtained by centrifugation. The acid value of the obtained oil was 74.5. This oil was neutralized with an aqueous solution of caustic soda, and the soap water was removed by centrifugation to obtain 52 g of HUFA. The fatty acid composition of this HUFA was as shown in Table-1. From the results in Table 1, especially when C20:5ω-3
It can be seen that the C22:6ω-3 component increases significantly.
(The same applies to the effects of the following examples.) Example 2 The fatty acid ethyl ester of Example-1 was converted to Example-
As in step 1, 50,000 units of lipase originating from the Aspergillus genus (manufactured by Amano Pharmaceutical Co., Ltd.) was used at 40°C.
Hydrolyzed for 24 hours. The acid value at that time was 50.7
62g of HUFA after neutralization and centrifugation
I got it. The fatty acid composition of this HUFA was as shown in Table-1. Example 3 Fatty acid methyl ester obtained from the same small fish oil as in Example-1 was prepared in the same manner as in Example-1.
Unit's lipase of Mucor origin (Amano Pharmaceutical Co., Ltd.)
Co., Ltd., products) for 24 hours at 30°C.
The acid value at that time was 98.8, and 44.5 g of HUFA was obtained after neutralization and centrifugation. The fatty acid composition of this HUFA was as shown in Table-1.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 脂肪酸低級アルコールエステルを、リゾープ
ス属、アスペルギルス属、ムコール属のいずれか
から得られたリパーゼの基質特異性を利用して選
択的に加水分解させ、ついで分解された脂肪酸を
除去することを特徴とする高度不飽和脂肪酸低級
アルコールエステルの濃縮分離方法。 2 高度不飽和脂肪酸低級アルコールエステルの
高度不飽和脂肪酸が炭素数20以上であり、二重結
合数3個以上有するものである特許請求の範囲第
一項記載の方法。
[Scope of Claims] 1. A fatty acid lower alcohol ester is selectively hydrolyzed using the substrate specificity of lipase obtained from any of Rhizopus, Aspergillus, and Mucor, and then the decomposed fatty acid is A method for concentrating and separating highly unsaturated fatty acid lower alcohol esters, the method comprising: removing lower alcohol esters of highly unsaturated fatty acids; 2. The method according to claim 1, wherein the highly unsaturated fatty acid of the highly unsaturated fatty acid lower alcohol ester has 20 or more carbon atoms and 3 or more double bonds.
JP12300782A 1982-07-16 1982-07-16 Concentration and separation of lower alcohol ester of highly unsaturated fatty acid Granted JPS5914793A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12300782A JPS5914793A (en) 1982-07-16 1982-07-16 Concentration and separation of lower alcohol ester of highly unsaturated fatty acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12300782A JPS5914793A (en) 1982-07-16 1982-07-16 Concentration and separation of lower alcohol ester of highly unsaturated fatty acid

Publications (2)

Publication Number Publication Date
JPS5914793A JPS5914793A (en) 1984-01-25
JPH0433838B2 true JPH0433838B2 (en) 1992-06-04

Family

ID=14849939

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12300782A Granted JPS5914793A (en) 1982-07-16 1982-07-16 Concentration and separation of lower alcohol ester of highly unsaturated fatty acid

Country Status (1)

Country Link
JP (1) JPS5914793A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9404483D0 (en) * 1994-03-08 1994-04-20 Norsk Hydro As Refining marine oil compositions
JP5111363B2 (en) * 2006-04-13 2013-01-09 日本水産株式会社 Method for producing highly unsaturated fatty acid concentrated oil

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58165796A (en) * 1982-03-26 1983-09-30 Asahi Denka Kogyo Kk Concentration of long chain highly unsaturated fatty acid glyceride

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58165796A (en) * 1982-03-26 1983-09-30 Asahi Denka Kogyo Kk Concentration of long chain highly unsaturated fatty acid glyceride

Also Published As

Publication number Publication date
JPS5914793A (en) 1984-01-25

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