JPS62280296A - Extraction of salmon oil - Google Patents

Extraction of salmon oil

Info

Publication number
JPS62280296A
JPS62280296A JP12317686A JP12317686A JPS62280296A JP S62280296 A JPS62280296 A JP S62280296A JP 12317686 A JP12317686 A JP 12317686A JP 12317686 A JP12317686 A JP 12317686A JP S62280296 A JPS62280296 A JP S62280296A
Authority
JP
Japan
Prior art keywords
salmon
trout
fish
meat
parts
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
JP12317686A
Other languages
Japanese (ja)
Inventor
稲多 昭七郎
小笠原 譲二
椿本 義一
均 内山
野内 黎吉
楢崎 宣夫
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.)
Sumitomo Seika Chemicals Co Ltd
Original Assignee
Seitetsu Kagaku 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 Seitetsu Kagaku Co Ltd filed Critical Seitetsu Kagaku Co Ltd
Priority to JP12317686A priority Critical patent/JPS62280296A/en
Publication of JPS62280296A publication Critical patent/JPS62280296A/en
Pending legal-status Critical Current

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  • Extraction Or Liquid Replacement (AREA)
  • Fats And Perfumes (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 3、発明の詳細な説明 (産業上の利用分野) 本発明は超pn界抽出法を用いてサケ・マス類よりサー
モンオイルを抽出分離する方法に関する。さらに詳しく
は、亜臨界または超臨界状態の二酸化炭素を抽剤として
、サケ・マス類、特にパーシャルフリージンク貯蔵され
たシロザケの頭部、就中、カマと称するエラの部分を原
料として新鮮な風味・香味の良いいわゆるサーモンピン
クのきれいな色相の良質のサーモンオイルを抽出分離す
る方法に関するものである。
Detailed Description of the Invention 3. Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a method for extracting and separating salmon oil from salmon and trout using a trans-pn field extraction method. More specifically, using subcritical or supercritical carbon dioxide as an extraction agent, salmon and trout, especially the head of chum salmon stored in partial free zinc, and especially the gill part called the kama, are used as raw materials to create a fresh flavor. - This relates to a method for extracting and separating high-quality salmon oil with a beautiful salmon pink color and a good flavor.

得られたサーモンオイルは、[J品、サケ缶詰、人エイ
クラ、ドレッシングソース類など種々の加工食品に風味
・香味を、また場合によってはサーモンピンクのきれい
な色相を併せ与えるために使用する。また養魚用飼料等
の高度不飽和脂肪酸(EPA等)補給用として添加する
と、タラ肝油等の様な不快臭もなく取板い易い飼料とす
ることができる。
The obtained salmon oil is used to add flavor and flavor to various processed foods such as J-products, canned salmon, human eikura, and dressing sauces, and in some cases, to add a beautiful salmon pink hue. Furthermore, when added as a supplement for highly unsaturated fatty acids (EPA, etc.) to feed for fish farming, etc., the feed can be made into feed that is easy to handle without the unpleasant odor of cod liver oil and the like.

(従来の技術ならびに発明が解決しようとする問題点) シロザケは、北海道・網走を中心としたサケ・マス全漁
獲量の80%に達するものである。
(Prior art and problems to be solved by the invention) Chum salmon accounts for 80% of the total catch of salmon and trout, mainly in Abashiri, Hokkaido.

毎年、9月からX2月にかけて、北海道のソロサケは、
各河川を産卯のため遡上するが、それは通称プナザケま
たはブナヶと呼ばれている。
Every year, from September to February, Hokkaido's solo salmon is
They go upstream in each river to produce eggs, which are commonly called Punazake or Bunaga.

之等ブナヶで斑紋の出たものは、既に脂質が減少してお
り、サケとしての食用には不向きで、せいぜいすり身と
しての活用がはかられているにすぎない、サケの魚体は
、その加工工程において、3枚におろし、肉部以外の頭
部・尾部等は廃棄されるか、または、フィンシュミール
原料として利用されているにすぎない。
Salmon with spots on it has already lost its fat content, making it unsuitable for consumption as salmon, and is only intended to be used as surimi. In the process, the fish is cut into three pieces, and the parts other than the meat, such as the head and tail, are either discarded or used as raw materials for finschmeal.

−Cにサケの脂質は、いわし・さば・さんま等信の高脂
質魚の魚油と異なり、その風味・香味の良さのため及び
、いわゆるサーモンピンクのきれいな色相を有するため
に一部、圧搾法、蒸煮法等の方法で分離取得され、いわ
ゆるサーモンオイルとして重用されているが、通常、良
質な魚体中に6%程度含まれているものの、従来の圧搾
法では分離効率が悪く、蒸煮法では加勢のための変質の
懸念があり、しかも原料として良質のサケを使用する必
要があり、品質、コストの両面からその利用についても
種々制約がある。
-C: Salmon lipids differ from fish oils from high-fat fish such as sardines, mackerel, and saury Tonobu because of their good flavor and aroma, and because they have a beautiful so-called salmon pink hue. Salmon oil is separated and obtained using methods such as methane and other methods, and is heavily used as so-called salmon oil.Although it is normally contained in about 6% in high-quality fish bodies, the separation efficiency of conventional pressing methods is low, and the steaming method requires There are concerns about deterioration of the quality of salmon, and in addition, it is necessary to use high-quality salmon as a raw material, and there are various restrictions on its use from both quality and cost considerations.

サケ缶詰工場では通常肉部以外の頭部、内臓等より茎煮
法により、サーモンオイルを分離取得し、サケ缶詰に充
填還元しているが、その原料、および処理工程からみて
良質なサーモンオイルであることは朋待し得ない現状で
ある。
At salmon canning factories, salmon oil is usually separated from the head, internal organs, etc. other than the meat parts by a boiling method, and then filled and reduced into canned salmon. The current situation is one that we cannot wait for.

魚油中には、エイコサペンタエン酸(EPA)ドコサヘ
キサエン酸(DHA)等の高度不飽和脂肪酸が多く含ま
れており、之等は摂取した場合、生体内で一部は工フル
ギー源として分解酸化され、一部はそのまま生体を構成
するリン脂質その他の構成成分となるが、他の一部はプ
ロスタグランジンなどのホルモン物質の材料となり、抗
血栓症予防作用が朋待されることから成人病予防の健康
食品、更には医薬品としての用途が注目されている。し
かし之等高変不飽和脂肪酸は、非常に酸化され易く、そ
の扱いをあやまると逆に、人体に有害な過酸化脂質への
変成が懸念される。
Fish oil contains many highly unsaturated fatty acids such as eicosapentaenoic acid (EPA) and docosahexaenoic acid (DHA). Some of it becomes phospholipids and other constituents that make up living organisms, but the other part becomes a material for hormonal substances such as prostaglandins, and is expected to have an antithrombotic preventive effect, so it can be used to prevent adult diseases. It is attracting attention for its use as a health food and even as a medicine. However, these highly modified unsaturated fatty acids are highly susceptible to oxidation, and if they are mishandled, there is a concern that they may turn into peroxidized lipids that are harmful to the human body.

C問題点を解決するための手段) 一般に魚の鮮度、即ちイキの良さは、その流通消費の過
程で重要な問題である。また近年、魚の腐敗とイキの良
さは別の問題であり、無菌状態でも死後鮮度は低下する
ことが知られている。
Means for solving problem C) In general, the freshness of fish, that is, the quality of its freshness, is an important issue in the process of distribution and consumption. Furthermore, in recent years, it has become known that the decomposition of fish and the quality of its freshness are separate issues, and that the freshness of fish decreases after death even under sterile conditions.

生化学的鮮度を客観的に示すものとして業界ではに値が
使用されている。動物のエネルギー貯蔵物質であるアデ
ノシンニリン酸(ATP)は、動物が死ぬと酵素の働き
で、アデノシンニリン酸(ADP)、アデノシン−リン
酸(AMP)イノシン酸(IMP)、イノシン(HXR
)ヒボキサンチン(H,)と経時変化して行く。
The value is used in the industry as an objective indicator of biochemical freshness. Adenosine diphosphate (ATP), which is an energy storage substance in animals, is converted into adenosine diphosphate (ADP), adenosine-phosphate (AMP), inosinic acid (IMP), and inosine (HXR) by the action of enzymes when the animal dies.
) Hyboxanthin (H, ) changes over time.

この分解過程のATPの経時変化を数値化したものかに
値であり、K値の内容は次式のごとくに示される。
The K value is a numerical representation of the change in ATP over time during this decomposition process, and the content of the K value is expressed as in the following equation.

ATP+^叶+AMP+[MP+1lxR+l1gすな
わち、K値はATP分解生成物全量に対する1lXR+
l+、量の百分率であり、その値の小さいほど生鮮度良
好なことを示す。最近、このに値を低く維持する即ち、
魚の鮮度維持の方法として、マイナス3℃で保持するパ
ーシャルフリージンク貯蔵法が提案、実施されている。
ATP+^Ko+AMP+[MP+1lxR+l1g, that is, the K value is 1lXR+ for the total amount of ATP decomposition products
l+ is a percentage of the amount, and the smaller the value, the better the freshness. Recently, keeping this value low i.e.
As a method to maintain the freshness of fish, a partial-free zinc storage method has been proposed and implemented, in which fish is kept at -3°C.

パーシャルフリージンク法により魚を貯蔵した場合、上
記に値の上昇が抑制される他に、品質劣化の要因である
タンパク変成の変成率も、氷蔵法に比して顕著に少なく
、コスト高の冷凍法と差が無いことが認められている。
When storing fish using the partial-free zinc method, in addition to suppressing the increase in value mentioned above, the rate of protein denaturation, which is a factor in quality deterioration, is significantly lower than with the ice storage method, which eliminates the need for high-cost freezing. It is recognized that there is no difference from the law.

また、酸化による過酸化脂質値(POV)の上昇、いわ
ゆる、油焼けも+IT+制される他、生菌数も減少させ
て、腐敗防止の点からも有効であることが知られている
0通常に値20以下が刺身で食べられるイキの良さと云
われている。
In addition to controlling the increase in lipid peroxide value (POV) due to oxidation, so-called oil burn, it also reduces the number of viable bacteria and is known to be effective in preventing spoilage. It is said that a value of 20 or less is good enough to eat as sashimi.

また、サケの南中にはカロチノイド系色素の一種アスク
キサンチンが含まれ、ピンク色を呈しているが、脂質中
にもこの色素が含まれるため、新鮮な脂質はいわゆるサ
ーモンピンクのきれいな色相を呈している。
In addition, salmon nanchu contains askuxanthin, a type of carotenoid pigment, which gives it a pink color, and since this pigment is also contained in the lipids, fresh lipids have a beautiful salmon pink hue. ing.

このアスクキサンチン色素は、酸化され易く、直ちに赤
色のアスクシンの塩に変質するが、不飽和脂肪酸の酸化
分解生成物、及び光、温度によっても比較的容易に分解
し、色相、明度、彩度が変化し、色価の低下をもたらす
性質のものである。
This ascuxanthin pigment is easily oxidized and immediately transforms into a red ascucin salt, but it is also relatively easily decomposed by oxidative decomposition products of unsaturated fatty acids, light, and temperature, and its hue, brightness, and saturation change. It has the property of changing and causing a decrease in color value.

パーシャルフリージンク法を利用すれば、こうしたアス
タキサンチン色素の変πを抑制することも周知である。
It is also well known that such π changes in astaxanthin pigment can be suppressed by using the partial free zinc method.

本発明者らは、風味・香味の良い良質な、いわゆるサー
モンピンクのきれいな色相のサーモンオイルを得る方法
について鋭意検討した結果超臨界抽出法を用いれば、上
記問題点を克服して、工業的に有利に目的とするサーモ
ンオイルを得ることを知り本発明に到達した。
The inventors of the present invention have conducted intensive studies on how to obtain salmon oil of good quality with good flavor and aroma, and have a beautiful so-called salmon pink hue. As a result, the inventors have found that by using supercritical extraction, the above problems can be overcome and it can be used industrially. The present invention was achieved by finding out that the desired salmon oil can be advantageously obtained.

即ち、本発明においては風味・香味の良い、いわゆるサ
ーモンピンクのきれいな色相の良質のサーモンオイルを
得る原料として、サケ・マス類の魚体をそのまま利用す
るばかりでなく、前記、種々の画期的な利点を存するパ
ーシャルフリージンク法を活用し、この方法で貯蔵され
たンロサケの、通常は経費をかけて廃棄されるか、せい
ぜいフィンシュミール用としてしか活用されない頭部・
尾部、就中、カマと称するエラの部分を原料とし、亜臨
界または超臨界状態の二酸化炭素を抽剤として脂質を抽
出したところ、非常に風味・香味の良い、いわゆるサー
モンピンクのきれいな色相の、低P○■の良質なサーモ
ンオイルを得ることができた。
That is, in the present invention, as a raw material for obtaining high-quality salmon oil with good flavor and aroma and a beautiful so-called salmon pink hue, we not only use the fish bodies of salmon and trout as they are, but also use the various innovative methods mentioned above. We take advantage of the advantageous partial-free zinc process to eliminate the heads of salmon stored in this way, which are usually disposed of at great expense or are only used for finschmeal.
When we extract the lipids from the tail, especially the gill part called the kama, using subcritical or supercritical carbon dioxide as an extraction agent, we produce a product with a beautiful salmon pink color that has a very good flavor and aroma. We were able to obtain high-quality salmon oil with low P○■.

このサーモンオイルは、その風味・香味を生かして、サ
ケ香味のあるカマボコ等の練製品、サケ缶詰、人エイク
ラ、ドレツシングその他、種々の加工食品に広範囲に利
用しうるちのである。この場合これ等製品製造の適当な
段階で、適当量を単に添加するだけで如上の効果が得ら
れる。また、本発明者等は、原料よりサーモンオイルを
抽出した後の抽残は変成が少ないため、蛋白質、カルシ
ウム等を食品用原料として利用するのに、非常に適した
素材となり得ることを知った。例えば、之をそのまま乾
燥、粉砕等の処理をして食品に添加使用することも出来
るし、また、特公昭53−7508に見られる如く、酵
素分解処理することによりベプタイド化して魚肉エキス
、およびカルシウムミールとして調味料、健康食品等へ
の活用が可能である等その利用範囲は広い。
Taking advantage of its flavor and aroma, this salmon oil can be used in a wide range of processed foods, including salmon-flavored paste products such as kamaboko, canned salmon, human eikura, dressings, and more. In this case, the above effect can be obtained simply by adding an appropriate amount at an appropriate stage of manufacturing these products. In addition, the present inventors have learned that the raffinate after extracting salmon oil from raw materials has little denaturation, so it can be an extremely suitable material for using protein, calcium, etc. as food raw materials. . For example, it can be used as it is by drying, pulverizing, etc. and added to food, or it can be converted into peptides by enzymatic decomposition treatment to produce fish meat extract and calcium, as shown in Japanese Patent Publication No. 53-7508. Its range of uses is wide, as it can be used as a meal, as a seasoning, and as a health food.

さらに本発明者らはサーモンオイルを抽出分離するため
の詳細な条件、得られたサーモンオイルや、抽残の利用
法などについて検討を続は本発明を完成することに至っ
た。
Further, the present inventors continued to study the detailed conditions for extracting and separating salmon oil, the method of using the obtained salmon oil, the raffinate, etc., and finally completed the present invention.

(作 用) 亜臨界または超臨界a′態の流体を用いて有機化合物を
、それを含有する混合物から分離する方法は例えば、特
公昭54−10539号公報に記載のとおり公知である
が、サケ・マス類よりサーモンオイルを得る方法につい
ては未だ全く知られていない。亜臨界または超臨界状態
の流体とは臨界温度および臨界圧力付近あるいはそれを
超える状態にある流体である。例えばエチレン(9,9
℃、5QaLm)二酸化炭素(31,0℃、72.9a
Lm )のごとく臨界状態付近またはそれ以上の状態に
ある流体であって、液体に近い密度とガス体に近い大き
な拡散係数を有する流体である。この特性の故に種々の
化合物を速やかにかつ大量に効率よく抽出でき、しかも
抽剤の分離が容易であるという特徴を存する。また圧力
や温度をわずかに変化させるだけで種々の化合物にたい
する溶解能力が大きく変化するため、選択的な抽出も行
えるという特徴もある。
(Function) A method of separating an organic compound from a mixture containing it using a fluid in subcritical or supercritical a' state is known, for example, as described in Japanese Patent Publication No. 10539/1983,・Nothing is known yet about how to obtain salmon oil from trout. A fluid in a subcritical or supercritical state is a fluid that is near or above its critical temperature and pressure. For example, ethylene (9,9
℃, 5QaLm) Carbon dioxide (31.0℃, 72.9a
It is a fluid that is in a state near or above the critical state, such as Lm), and has a density close to that of a liquid and a large diffusion coefficient close to that of a gas. Because of this characteristic, various compounds can be extracted quickly and efficiently in large quantities, and the extractant can be easily separated. It also has the advantage of being able to perform selective extraction, since the ability to dissolve various compounds changes greatly with just a slight change in pressure or temperature.

本発明においては一般に前記亜臨界または超臨界状態に
ある流体のいずれも使用可能であるが、サケ・マス類よ
りサーモンオイルの分離能が優れていることや、比較的
低温での処理が可能で取扱いおよび操作が簡華かつ経済
的に有利である等、数々の利点を享受することができる
ので、通常抽剤としては二酸化炭素を用いる。
Generally, in the present invention, any of the above-mentioned fluids in a subcritical or supercritical state can be used, but the separation ability of salmon oil is superior to that of salmon and trout, and it is possible to process it at a relatively low temperature. Carbon dioxide is usually used as the extraction agent because it offers many advantages, such as being easy to handle and operate and being economically advantageous.

以下本発明の実施態様をフローンートに基づいて説明す
る。
Embodiments of the present invention will be described below based on a flow route.

第1図においてCO□シリンダー1より圧縮機2を用い
て所定の圧力まで圧縮したCO□をさ交換機3を通して
所定の抽出温度にし、亜臨界または超臨界状態にして抽
出塔4へと導入する。
In FIG. 1, CO□ is compressed from a CO□ cylinder 1 to a predetermined pressure using a compressor 2, and is brought to a predetermined extraction temperature through an exchanger 3 and brought into a subcritical or supercritical state and introduced into an extraction column 4.

抽出塔4には原料のサケ・マス類の魚体あるいはこれを
解体した肉部以外の部分、好ましくはこれを細片状にし
たものを仕込んでおき、ここで002による抽出を行っ
た後、抽出対象物を含んだCO□2相を減圧弁5を通し
て減圧し、セパレーター6に導き抽出物をCO□から分
離する。抽出物と分離されたCO2はコンデンサー7で
冷却液化されれ圧ゐ機2を経てリサイクルする。
The extraction tower 4 is charged with fish bodies of raw materials such as salmon and trout, or parts other than the meat parts that have been dissected, preferably in pieces, and after extraction with 002 is carried out here, the extraction The pressure of the CO□2 phase containing the target substance is reduced through the pressure reducing valve 5, and the extract is separated from the CO□ by passing into the separator 6. The CO2 separated from the extract is cooled and liquefied in a condenser 7, and recycled via a compressor 2.

上記プロセスにおいて抽出塔内のCOzの圧力は、50
〜50Gkg/cj、好ましくは、60〜300 kg
/ci、温度は25〜lOO℃、好ましくは、25〜6
0℃の範囲に保って抽出することが必要である。低すぎ
ると液化COtとなるため抽剤と抽出物との分離にもエ
ネルギーを要する。逆に高すぎると装置費がかさみ経済
性に問題の出る他、熱劣化等の悪影響の現れる場合もあ
る。セパレーター6において抽出相より抽出物を分離す
る際の条件は圧力が1−150 kg/cれ温度30〜
60℃の範囲で定めると好ましい結果が得られる。
In the above process, the pressure of COz in the extraction column is 50
~50Gkg/cj, preferably 60-300 kg
/ci, temperature is 25-100°C, preferably 25-6
It is necessary to maintain the temperature in the range of 0°C for extraction. If it is too low, it becomes liquefied COt, which requires energy to separate the extractant from the extract. On the other hand, if it is too expensive, the cost of the equipment will increase, causing problems in terms of economic efficiency, and may also cause adverse effects such as thermal deterioration. The conditions for separating the extract from the extraction phase in separator 6 are a pressure of 1-150 kg/c and a temperature of 30-
Preferable results can be obtained by setting the temperature within the range of 60°C.

なお抽出塔に抽剤を段階的に圧力を上げて導入し段階的
抽出を行うこともできる。さらに抽出塔を複数個並列に
設けて切換え、半連続的な操作を行うことも可能である
。また抽出物と抽剤との分離は通常上記減圧法によって
行なうが抽出i温度を上げると溶解度が下がるので温度
変化を与えて分離を行なってもよい。
Incidentally, stepwise extraction can also be carried out by introducing the extracting agent into the extraction column while increasing the pressure stepwise. Furthermore, it is also possible to perform semi-continuous operation by installing a plurality of extraction columns in parallel and switching between them. Separation of the extract and extractant is usually carried out by the above-mentioned reduced pressure method, but since increasing the extraction temperature lowers the solubility, the separation may be carried out by changing the temperature.

−C的に第1図に示したプロセスにおいてセパレーター
6より経時的に抽出物を分離するが、例えば段階的に圧
力を下げて行くとサーモンオイルの成分のあるものが一
部゛濃縮されて得られるように抽出物の成分が異なって
くるので適宜目的に応して分取の仕方を変えて回収する
ことができる。即ちセパレーターを複数個直列に設け、
段階的に圧力を下げて分別分離回収を行なうことなども
可能である。また、第1図に示したプロセスにおいて、
前記のごとくセパレーター6より経時的に抽出物を分離
するが、分取の仕方によって得られる抽出物成分が異な
ってくるので目的とする有効成分の分割抽出を行なうこ
ともできる。
-C In the process shown in Figure 1, the extract is separated over time by the separator 6, but for example, if the pressure is gradually lowered, some of the components of salmon oil will become concentrated. Since the components of the extract vary, it can be recovered by changing the method of fractionation depending on the purpose. That is, multiple separators are provided in series,
It is also possible to perform fractional separation and recovery by lowering the pressure in stages. Furthermore, in the process shown in Figure 1,
As described above, the extract is separated over time using the separator 6, but since the components of the extract obtained differ depending on the method of fractionation, it is also possible to extract the desired active ingredients in portions.

(実施例) 以下実施例を示して本発明をさらに詳細に説明するが本
発明はこれに限定されるものではない。
(Example) The present invention will be explained in more detail below with reference to Examples, but the present invention is not limited thereto.

実施例1 パーシャルフリージンク貯蔵されたソロザケの肉部分6
00gを原料とし、第1図に示すプロセスにて、圧力2
30kg/c+d、温度40℃の超臨界CO□を抽剤と
して抽出を行ない常温大気圧下で抽出物を分離して37
gのサーモンオイルを得た。
Example 1 Meat portion 6 of solo salmon stored in partially free zinc
Using 00g as raw material, the process shown in Figure 1 was carried out at a pressure of 2.
Extraction was carried out using supercritical CO□ at 30 kg/c+d and a temperature of 40°C, and the extract was separated at room temperature and atmospheric pressure.
g of salmon oil was obtained.

実施例2 パーシャルフリージンク貯蔵されたシロザケのエラおよ
びヒレ部分3kgを原料とし第1図に示すプロセスにて
圧力240 kg/cot、温度40℃の超臨界CO,
を抽剤として抽出を行ない、常温大気圧下で抽出物を分
離して340gの抽出物を得た。この抽出物は実施例1
で肉部分より得たサーモンオイルと同等の香味を有して
いた。
Example 2 Using 3 kg of chum salmon gills and fins stored in partial free zinc as raw materials, supercritical CO was used at a pressure of 240 kg/cot and a temperature of 40°C in the process shown in Figure 1.
Extraction was carried out using as an extractant, and the extract was separated at room temperature and atmospheric pressure to obtain 340 g of extract. This extract is Example 1
It had the same flavor as salmon oil obtained from the meat part.

実施例3 実施例2で得たサーモンオイルを白身魚のすり身に0.
1%添加し加工したところサケ香味のカマボコ練製品が
得られた。
Example 3 0.0% of the salmon oil obtained in Example 2 was added to ground white fish.
When 1% was added and processed, a salmon-flavored kamaboko paste product was obtained.

〔発明の効果〕〔Effect of the invention〕

本発明の方法により、工業的に有利にシロザケの、頭部
、就中、カマより風味・香味の良いいわゆるサーモンピ
ンクのきれいな色相の良質のサーモンオイルを得ること
が出来、下記の優れた効果が奏せられる。
By the method of the present invention, it is possible to industrially advantageously obtain high-quality salmon oil with a beautiful so-called salmon pink hue that has a better flavor and aroma than the head, especially the head, of chum salmon, and has the following excellent effects. It can be played.

1、従来、廃棄処分されるか、利用価値の低いシロザケ
の頭部、就中、カマの部分を原料として。
1. The head of chum salmon, especially the kama part, which has traditionally been discarded or has low utility value, is used as raw material.

パーシャルフリージンク貯蔵法の活用と亜臨界または超
臨界状態の二酸化炭素を抽剤とした低温度抽出により、
K値、povの上昇が抑えられ、静菌作用反型殺菌作用
も期待されるので、新鮮で衛生面でも安全な風味・香味
の良いいわゆるサーモンピンクのきれいな色相の良質の
サーモンオイルが得られる。
By utilizing the partial-free zinc storage method and low-temperature extraction using subcritical or supercritical carbon dioxide as an extractant,
Since the increase in K value and POV is suppressed, and bacteriostatic and anti-sterilizing effects are expected, high-quality salmon oil with a beautiful so-called salmon pink hue, which is fresh, hygienic and safe, and has good flavor and aroma can be obtained.

2、抽出に際しては、重金属は抽出されないため使用上
安全である。
2. During extraction, heavy metals are not extracted, so it is safe to use.

3、通常知られている脂質含量に対し、特にブナヶのカ
マの部分から予想を1廻る量の脂質が得られたことは、
原料としての有利性と抽出法の高効率を示すものである
3. Considering the normally known lipid content, the fact that we were able to obtain an amount of lipid that was much higher than expected from the part of the beetle
This shows its advantage as a raw material and the high efficiency of the extraction method.

4、抽出後の原料は、略々、完全に脱脂され、異臭発生
もなく、その取扱いが容易であり、しかも、蛋白質、カ
ルシウム等の有用成分は変質することなく豊富に含有さ
さているため、単に低脂肪フィツシュミール用としてで
なく、食品用原料として非常に適した素材となる。
4. The raw material after extraction is almost completely defatted, does not generate any off-odor, and is easy to handle. Moreover, it contains abundant useful components such as protein and calcium without deterioration. It is a very suitable material not only for low-fat fishmeal but also as a food ingredient.

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

第1図は本発明の実施態様を示すフローシートである。 FIG. 1 is a flow sheet showing an embodiment of the present invention.

Claims (12)

【特許請求の範囲】[Claims] (1)サケ・マス類の魚体、あるいはこれを解体した肉
部以外の部分より、亜臨界または超臨界状態の二酸化炭
素を抽剤としてサーモンオイルを抽出分離する方法。
(1) A method of extracting and separating salmon oil from the bodies of salmon and trout, or from parts other than the meat parts of the fish, using subcritical or supercritical carbon dioxide as an extractant.
(2)サケ・マス類がシロザケである特許請求の範囲(
1)記載の方法。
(2) Claims in which the salmon and trout are chum salmon (
1) The method described.
(3)サケ・マス類を解体した肉部以外の部分がシロザ
ケの頭部、就中、カマと称するエラの部分である特許請
求の範囲(1)または(2)記載の方法。
(3) The method according to claim (1) or (2), wherein the part other than the meat part of the salmon/trout is the head of chum salmon, particularly the gill part called a kama.
(4)抽出の原料たるサケ・マス類の魚体、あるいはこ
れを解体した肉部以外の部分が、パーシャルフリージン
ク貯蔵されたものである特許請求の範囲(1)(2)ま
たは(3)記載の方法。
(4) Claim (1), (2) or (3) states that the fish bodies of salmon and trout, which are raw materials for extraction, or parts other than the meat parts of the fish that are butchered are stored in partially free zinc. the method of.
(5)サケ・マス類の魚体、あるいはこれを解体した肉
部以外の部分より、亜臨界または超臨界状態の二酸化炭
素を抽剤として抽出分離したサーモンオイルを、スケト
ウダラ等の白身の魚のすり身に添加することを特徴とす
る、サケ風味・香味にすぐれた食品を得る方法。
(5) Salmon oil extracted and separated from the bodies of salmon and trout, or from parts other than the flesh of dissected fish, using subcritical or supercritical carbon dioxide as an extractant, is added to the minced meat of white fish such as walleye pollack. A method for obtaining food with excellent salmon flavor and flavor, characterized by adding the following:
(6)サケ・マス類がシロザケである特許請求の範囲(
5)記載の方法。
(6) Claims in which the salmon and trout are chum salmon (
5) The method described.
(7)サケ・マス類を解体した肉部以外の部分がシロザ
ケの頭部、就中、カマと称するエラの部分である特許請
求の範囲(5)または(6)記載の方法。
(7) The method according to claim (5) or (6), wherein the part other than the meat part of the salmon/trout is the head of chum salmon, particularly the gill part called a kama.
(8)抽出の原料たるサケ・マス類の魚体、あるいはこ
れを解体した肉部以外の部分が、パーシャルフリージン
ク貯蔵されたものである特許請求の範囲(5)(6)ま
たは(7)記載の方法。
(8) Claim (5), (6) or (7) states that the fish bodies of salmon and trout, which are raw materials for extraction, or parts other than the meat parts of the fish that are butchered are stored in partially free zinc. the method of.
(9)サケ・マス類の魚体、あるいはこれを解体した肉
部以外の部分より、亜臨界または超臨界状態の二酸化炭
素を抽剤として、サーモンオイルを抽出分離した後の抽
残を加工食品向けの蛋白質、カルシュウム源として利用
する方法。
(9) Salmon oil is extracted and separated from the bodies of salmon and trout, or from the parts other than the meat after being dissected, using subcritical or supercritical carbon dioxide as an extractant, and the residue is used for processed foods. How to use it as a source of protein and calcium.
(10)サケ・マス類がシロザケである特許請求の範囲
(9)記載の方法。
(10) The method according to claim (9), wherein the salmon/trout is chum salmon.
(11)サケ・マス類を解体した肉部以外の部分がシロ
ザケの頭部、就中、カマと称するエラの部分である特許
請求の範囲(9)(10)または(11)記載の方法。
(11) The method according to claim (9), (10) or (11), wherein the part other than the meat part of the salmon/trout is the head of chum salmon, particularly the gill part called a kama.
(12)抽出の原料になる、サケ・マス類の魚体あるい
はこれを解体した肉部以外の部分が、パーシャルフリー
ジンク貯蔵されたものである特許請求の範囲(9)また
は(10)記載の方法。
(12) The method according to claim (9) or (10), wherein the salmon/trout fish body or the parts other than the meat part of the fish that are butchered and used as the raw material for extraction are stored in partially free zinc. .
JP12317686A 1986-05-27 1986-05-27 Extraction of salmon oil Pending JPS62280296A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12317686A JPS62280296A (en) 1986-05-27 1986-05-27 Extraction of salmon oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12317686A JPS62280296A (en) 1986-05-27 1986-05-27 Extraction of salmon oil

Publications (1)

Publication Number Publication Date
JPS62280296A true JPS62280296A (en) 1987-12-05

Family

ID=14854065

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12317686A Pending JPS62280296A (en) 1986-05-27 1986-05-27 Extraction of salmon oil

Country Status (1)

Country Link
JP (1) JPS62280296A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003512481A (en) * 1999-10-21 2003-04-02 ラボラトイレス ラヴィファーム エス.エー. Method for fractionating raw materials consisting of several components using supercritical solvent
WO2009038029A1 (en) * 2007-09-21 2009-03-26 Bizen Chemical Co., Ltd. METHOD OF PRODUCING Ω3-HIGHLY UNSATURATED FATTY ACID
JP2014005440A (en) * 2012-05-30 2014-01-16 Central Research Institute Of Electric Power Industry Fat extraction method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003512481A (en) * 1999-10-21 2003-04-02 ラボラトイレス ラヴィファーム エス.エー. Method for fractionating raw materials consisting of several components using supercritical solvent
WO2009038029A1 (en) * 2007-09-21 2009-03-26 Bizen Chemical Co., Ltd. METHOD OF PRODUCING Ω3-HIGHLY UNSATURATED FATTY ACID
JPWO2009038029A1 (en) * 2007-09-21 2011-01-06 備前化成株式会社 Method for producing ω3 series highly unsaturated fatty acid
JP2014005440A (en) * 2012-05-30 2014-01-16 Central Research Institute Of Electric Power Industry Fat extraction method

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