JPS6067597A - Manufacture of crude fish oil - Google Patents

Manufacture of crude fish oil

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Publication number
JPS6067597A
JPS6067597A JP17573483A JP17573483A JPS6067597A JP S6067597 A JPS6067597 A JP S6067597A JP 17573483 A JP17573483 A JP 17573483A JP 17573483 A JP17573483 A JP 17573483A JP S6067597 A JPS6067597 A JP S6067597A
Authority
JP
Japan
Prior art keywords
fish oil
fish
crude
plant seeds
crude fish
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
JP17573483A
Other languages
Japanese (ja)
Other versions
JPH058239B2 (en
Inventor
和幸 山嵜
登 鈴木
太幡 利一
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.)
Taisei Corp
Original Assignee
Taisei Corp
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 Taisei Corp filed Critical Taisei Corp
Priority to JP17573483A priority Critical patent/JPS6067597A/en
Publication of JPS6067597A publication Critical patent/JPS6067597A/en
Publication of JPH058239B2 publication Critical patent/JPH058239B2/ja
Granted legal-status Critical Current

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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】 本発明は粗魚油の製造方法に関するものである。[Detailed description of the invention] The present invention relates to a method for producing crude fish oil.

最近社会の高齢化や医療費の圧縮などから健康食品が注
目されているが、その中でもとりわけ新鮮な魚油に含有
されているEPA (エイコサペンタエン酸)とDHA
 (ドコサヘキサエン酸)が注目されている。しかしな
がらかかるKPAやDHAの様な多価不飽和脂肪酸は分
子式内に二重結合が多い為、非常に不安定で酸化され易
(、従ってこれらを含有した魚油を効率的に製造するこ
とは非常に難かしい。
Recently, health foods have been attracting attention due to the aging of society and the reduction in medical costs, but among these, EPA (eicosapentaenoic acid) and DHA, which are contained in fresh fish oil, are particularly important.
(docosahexaenoic acid) is attracting attention. However, because polyunsaturated fatty acids such as KPA and DHA have many double bonds in their molecular formulas, they are extremely unstable and easily oxidized (therefore, it is extremely difficult to efficiently produce fish oil containing them). It's difficult.

KPAやDHAは前述した通り非常に不安定で酸化され
易く、その酸化速度は高温になる程大きくなるので、従
来は魚体を破砕する前後に於いて抗酸化剤を添加し、そ
して温和な条件下で粗魚油を製造している。この際一旦
過酸化物が生成すると加速度的にその品質が劣化するの
で、製造工程上の取り扱いには大きな注意を要している
As mentioned above, KPA and DHA are extremely unstable and easily oxidized, and the oxidation rate increases as the temperature increases. Conventionally, antioxidants are added before and after crushing the fish body, and the oxidation rate is increased under mild conditions. produces crude fish oil. At this time, once peroxide is generated, its quality deteriorates at an accelerated rate, so great care is required when handling it during the manufacturing process.

従来方法はこのようにEiPAやDHAが酸化され難い
製造条件に於いて製造するものではあるものの、魚体は
そのまま使用するものであって、酸化を強く促進する血
色素(ヘモグロビン)や、魚肉中に約70〜80%含ま
れ、やはり酸化を促進する水分をそのまま含有させた状
態で製造するものであるので、根本的な酸化防止を行な
えないという欠点がある。
Although the conventional method is manufactured under conditions that prevent EiPA and DHA from being oxidized, the fish body is used as is, and the fish meat contains hemoglobin, which strongly promotes oxidation, and It contains 70 to 80% of water, which also promotes oxidation, and is manufactured in a state where it is still contained, so it has the disadvantage that it cannot fundamentally prevent oxidation.

一方、魚肉からの粗魚油の分離方法として、例えばヘキ
サン等の有機溶媒による抽出法が一般的に行なわれてい
るが、この方法では粗魚油抽出後の有機溶媒の処理問題
と、粗魚油に於ける残留有機溶媒が人体に対して有害で
あるという、食品衛生上の問題がある。かかる問題を解
決する一般的な油の分離方法として物理的な圧搾方法が
あるが、魚肉中には前述した通り水分が多いことに加え
て、粗繊維が少ないのでこの方法で粗魚油を分離するこ
とは不可能である。
On the other hand, as a method for separating crude fish oil from fish meat, extraction using an organic solvent such as hexane is generally performed, but this method has problems in processing the organic solvent after crude fish oil extraction and There is a food sanitation problem in that residual organic solvents in raw materials are harmful to the human body. Physical compression is a common oil separation method that solves this problem, but as mentioned above, fish meat contains a lot of water and has little crude fiber, so this method is used to separate crude fish oil. That is impossible.

本発明は魚体を合理的に加工すると共に、これに、やは
り合理的に加工した植物種子を混合攪拌薄情して中間加
工物を生成し、かかる中間加工物から粗魚油を分離する
ようにしたことにより、製造時に於ける前記KPAやD
HAの酸化を効果的に防止し得ると共に粗魚油の分離に
物理的な圧搾方法を適用可能とし、こうして従来方法の
数々の欠点を全く解消したものである。
The present invention processes fish bodies rationally, mixes and stirs them with plant seeds that have also been rationally processed to produce an intermediate product, and separates crude fish oil from the intermediate product. Accordingly, the above KPA and D during manufacturing
The oxidation of HA can be effectively prevented and the physical pressing method can be applied to the separation of crude fish oil, thus completely eliminating the numerous drawbacks of the conventional methods.

即ち、本発明は血液を除去した魚体の全体または一部を
微細化溶液状にした後、凍結乾燥して得られる加工物と
、植物種子を微細化並びに加熱乾燥して得られる加工物
とを混合攪拌薄情し、その加工物を圧搾して粗魚油を得
ることを要旨とするものであって、以下実施例を示す図
面に基づいて詳細に説明すると次の通りである。
That is, the present invention uses a processed product obtained by making the entire or part of a fish body from which blood has been removed into a micronized solution and then freeze-drying it, and a processed product obtained by micronizing and heat-drying plant seeds. The gist is to obtain crude fish oil by mixing, stirring, and pressing the processed product, and will be described in detail below based on drawings showing examples.

符号1は粗魚油を製造するための原材料となる魚体を示
すもので、かかる魚体1は活魚又は鮮魚が好まし−。2
は該魚体1から血液を除去するための血液除去装置で、
かかる血液除去装置2は特願昭58年第113817号
に開示される自動採血装置を適用し得る他、適宜の構成
で良(、また人手で行なっても良い。本発明はこのよう
にまず血液を除去することにより、EPAやDHAの酸
化を強(促進する作用がある、血液中のヘモグロビン等
の金属を含んだ化合物を魚体1から除去する。
Reference numeral 1 indicates a fish body that is a raw material for producing crude fish oil, and the fish body 1 is preferably a live fish or a fresh fish. 2
is a blood removal device for removing blood from the fish body 1,
The blood removing device 2 may be an automatic blood collecting device disclosed in Japanese Patent Application No. 113,817 of 1980, or may have an appropriate configuration (or may be manually performed. By removing , compounds containing metals such as hemoglobin in the blood, which have the effect of strongly (promoting) the oxidation of EPA and DHA, are removed from the fish body 1.

符号3はカッターミキサーやホモゾナイず−あるいはプ
レンダー等の微細化装置であり、前工程に於いて血液を
除去された魚体1はこの装置3で微細化溶液状とされる
。符号4は凍結乾燥機であり、微細化溶液状とされた魚
肉はここで低温状態に於いて例えば水分約1%以下にま
で凍結乾燥される。
Reference numeral 3 denotes a micronization device such as a cutter mixer, homozonizer, or blender, and the fish body 1 from which blood has been removed in the previous step is made into a micronization solution by this device 3. Reference numeral 4 denotes a freeze dryer, in which the fish meat, which has been made into a micronized solution, is freeze-dried at a low temperature to, for example, a moisture content of about 1% or less.

魚肉はこのように微細化溶液状で凍結乾燥されるので脱
水効率が非常に高く、また加熱をしないので酸化を効果
的に防止することができる。尚、かかる凍結乾燥工程に
於いて、凍結乾燥機4に窒素(3) ガス等の不活性ガスを封入して空気を追い出すようにす
れば更に酸化を防止することができる。
Since fish meat is freeze-dried in the form of a finely divided solution, the dehydration efficiency is very high, and since no heating is required, oxidation can be effectively prevented. In this freeze-drying step, oxidation can be further prevented by filling the freeze dryer 4 with an inert gas such as nitrogen (3) gas and expelling air.

次に符号5は大豆等の植物種子であり、かかる植物種子
5をウィレー粉砕機やミル等の微粉砕機6で微細化する
。植物種子5は大豆の他に、トコフェロール(ビタミン
E)を比較的多く含有しているものであれば、コムギ、
ゴマ、トウモロコシ、米等適宜に選定することができる
。符号1は恒温乾燥器であり、かかる乾燥器7によって
植物種子を加熱乾燥する。植物種子はこの工程に於いて
水分を例えば1%以下に脱水されると共に、例えば大豆
の場合にはトリジシンインヒビターやヘマグルチニン等
の生理的有害物質を加熱により不活性化され、また青臭
味を除去される。尚、加熱温度は前記作用を奏する温度
、例えば100℃以上とするが、植物種子中のトコフェ
ロールが分解され易くなる温度、約120℃以上にはし
ない。
Next, reference numeral 5 indicates plant seeds such as soybeans, and the plant seeds 5 are pulverized by a pulverizer 6 such as a Willey pulverizer or a mill. In addition to soybeans, the plant seeds 5 may include wheat, wheat, etc., as long as they contain a relatively large amount of tocopherol (vitamin E).
Sesame, corn, rice, etc. can be selected as appropriate. Reference numeral 1 denotes a constant temperature dryer, and this dryer 7 heats and dries plant seeds. In this process, plant seeds are dehydrated to, for example, 1% or less, and in the case of soybeans, physiologically harmful substances such as tridicin inhibitor and hemagglutinin are inactivated by heating, and the grassy smell is removed. removed. The heating temperature is set to a temperature that achieves the above-mentioned effect, for example, 100°C or higher, but is not set to a temperature of approximately 120°C or higher, which is a temperature at which tocopherols in plant seeds are easily decomposed.

本発明は以上の如(魚体1を加工した加工物と、植物種
子5を加工した加工物とを、自動乳鉢機等の混合攪拌薄
情装置8で混合攪拌薄情する。かか(4〕 る混合攪拌薄情により、魚肉からの油脂と、大豆等の植
物種子からの油脂が混合されるが、植物種子の油脂に含
まれるトコフェロールは、魚肉油脂のEPAやDHAの
抗酸化剤であるため、魚肉油脂の不安定性が改良されこ
れらの酸化を効果的に防止することができる。以上の如
(混合攪拌して得られる加工物を、次いでエキスペラ−
やスクリュープレス等の圧搾機9に導入し、かかる圧搾
機9に於ける物理的圧搾により粗魚油を得ることができ
る。圧搾機9に導入する前記加工物は、前述した通り十
分脱水されていることに加えて、植物種子の粗繊維が含
まれているため、効率的に粗魚油を分離して得ることが
できる。
In the present invention, as described above, a processed product obtained by processing the fish body 1 and a processed product obtained by processing the plant seeds 5 are mixed and stirred using a mixing and stirring device 8 such as an automatic mortar machine. Due to gentle stirring, oil from fish meat and oil from plant seeds such as soybeans are mixed, but since tocopherol contained in oil from plant seeds is an antioxidant for EPA and DHA in fish oil, fish oil and fat are mixed together. It is possible to improve the instability of these substances and effectively prevent their oxidation.
Crude fish oil can be obtained by introducing the raw fish oil into a pressing machine 9 such as a screw press or a screw press, and physically compressing it in the pressing machine 9. The processed product introduced into the press 9 has been sufficiently dehydrated as described above, and also contains crude fibers of plant seeds, so that crude fish oil can be efficiently separated and obtained.

次に本発明の実施例を示す。Next, examples of the present invention will be shown.

魚体重4〜6 kgのハマチの活魚を予め10°C以下
の蓄養槽に入れ、できる限り低温にして活ハマチの運動
性を押さえた後、自動採血装置に一部づつ投入し血液を
魚体1から除去した。そして血液が除去されたハマチを
二枚におろし、可食部と皮下脂肪部及び内臓部の三部に
分別した。次いでそれら可食部と皮下脂肪部及び内臓部
それぞれをカッターミキサーで微細化溶液状(換言する
とマヨネーズの状態)にして凍結乾燥機4に入れ凍結温
度−30℃乾燥温度最大20℃乾燥時間15時間の条件
で脱水した。その結果水分量1%以下のそれぞれの凍結
乾燥物が得られた。それぞれの凍結乾燥物のうち臭気が
比較的あったのは内臓の凍結乾燥物であり、他のものは
特に注意する程ではなかった。
Live yellowtail fish weighing 4 to 6 kg were placed in advance in a culture tank at a temperature of 10°C or less, and the temperature was kept as low as possible to suppress the motility of the live yellowtail. After that, a portion of the live yellowtail was placed into an automatic blood sampling device, and the blood was collected into one fish body. removed from. Then, the yellowtail from which the blood had been removed was cut into two pieces and divided into three parts: the edible part, the subcutaneous fat part, and the visceral part. Next, the edible parts, subcutaneous fat parts, and visceral parts are each made into a fine solution (in other words, mayonnaise state) using a cutter mixer and placed in a freeze dryer 4 at a freezing temperature of -30°C, a maximum drying temperature of 20°C, and a drying time of 15 hours. Dehydrated under the following conditions. As a result, each freeze-dried product with a moisture content of 1% or less was obtained. Among the freeze-dried products, the one that had a relatively strong odor was the freeze-dried internal organs, and the odor of the other products was not so strong that it was noteworthy.

一方植物種子の方は北海道十勝特産の大豆を微粉砕機6
にかけ微粉末化すると共に平均10%前後含まれる水分
を除去する目的で100℃±5°Cの範囲で恒温乾燥器
7で乾燥させた。
On the other hand, for plant seeds, soybeans from Tokachi, Hokkaido are pulverized using a pulverizer 6.
The powder was dried in a constant temperature dryer 7 at a temperature of 100° C.±5° C. for the purpose of pulverizing the powder and removing moisture contained on average at about 10%.

しかして前記それぞれの凍結乾燥物と、大豆のけ粗魚油
を製造した。
In this way, each of the above-mentioned lyophilized products and crude fish oil with soybean paste were produced.

そして得られた粗魚油のうち内臓からのものを選び、こ
れと大豆の乾燥微粉末の混合されていない、即ち原料が
ノ・マチ内臓だけの粗魚油の安定性を比較する為、30
℃で20日間放置した後のそれぞれの粗魚油の酸化、過
酸化物価を測定したところ両者に差が見られ、一本発明
方法より得た粗魚油の方が酸化及び過酸化物価共低い値
であった。
Of the obtained crude fish oil, one from internal organs was selected, and in order to compare the stability of this with the crude fish oil that was not mixed with dried fine soybean powder, that is, the raw material was only from internal organs.
When the oxidation and peroxide values of each crude fish oil were measured after being left for 20 days at there were.

本発明は以上の通り、魚肉を微細化溶液状とした後凍結
乾燥して合理的に脱水すると共に、魚肉の油脂中に少な
い物質、即ち魚肉の油脂中のBPAやDHAの抗酸化剤
として作用するトコフェロール並びに粗繊維を植物種子
から得るようにし、即ち、該植物種子を微細化すると共
に加熱乾燥して得られた加工物を前記魚肉の加工物と混
合攪拌捕潰して新たな中間加工物とし、かかる中間加工
物から粗魚油を分離するようにしたので、製造時に於け
る前記KPAやDHAの酸化を効果的に防止し得ると共
に、粗魚油の分離に物理的圧搾方法を使用し得るので、
有機溶媒を用いた抽出方法のように有機溶媒の処理問題
や食品衛生上の問題が一切生じず、しかも低コストであ
るという大きな特徴を有する。
As described above, the present invention is capable of rationally dehydrating fish meat by making it into a micronized solution and then freeze-drying it, and also acts as an antioxidant for substances that are rare in the fats and oils of fish meat, such as BPA and DHA in the fats and oils of fish meat. Tocopherol and crude fiber are obtained from plant seeds, that is, the plant seeds are made fine and dried by heating, and the resulting processed product is mixed with the processed fish meat, stirred and crushed to form a new intermediate processed product. Since the crude fish oil is separated from the intermediate processed product, it is possible to effectively prevent the oxidation of KPA and DHA during production, and a physical compression method can be used to separate the crude fish oil.
Unlike extraction methods using organic solvents, this method does not pose any problems in processing organic solvents or food hygiene, and it has the major characteristics of being low cost.

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

図は本発明方法を装置的に示した説明図である。 符号1・・・魚体、2・・・血液除去装置、3・・・微
細化装置、4・・・凍結乾燥機、5・・・植物種子、6
・・・微粉砕機、7・・・乾燥器、8・・・混合攪拌薄
情装置、9・・・圧搾機。 出願人 大成建設株式会社 岨憲漬 カス
The figure is an explanatory diagram showing the method of the present invention in terms of apparatus. Code 1... Fish body, 2... Blood removal device, 3... Micronization device, 4... Freeze dryer, 5... Plant seed, 6
. . . Fine grinder, 7. Dryer, 8. Mixing stirring device, 9. Pressing machine. Applicant: Taisei Construction Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 血液を除去した魚体の全体または一部を微細化溶液状に
した後、凍結乾燥して得られる加工物と、植物種子を微
細化並びに加熱乾燥して得られる加工物とを混合攪拌信
潰し、その加工物を圧搾して粗魚油を得ることを特徴と
する粗魚油の製造方法
The whole or part of the fish body from which blood has been removed is made into a micronized solution, and then the processed product obtained by freeze-drying and the processed product obtained by micronized and heat-dried plant seeds are mixed and crushed, A method for producing crude fish oil, which comprises compressing the processed product to obtain crude fish oil.
JP17573483A 1983-09-22 1983-09-22 Manufacture of crude fish oil Granted JPS6067597A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17573483A JPS6067597A (en) 1983-09-22 1983-09-22 Manufacture of crude fish oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17573483A JPS6067597A (en) 1983-09-22 1983-09-22 Manufacture of crude fish oil

Publications (2)

Publication Number Publication Date
JPS6067597A true JPS6067597A (en) 1985-04-17
JPH058239B2 JPH058239B2 (en) 1993-02-01

Family

ID=16001302

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17573483A Granted JPS6067597A (en) 1983-09-22 1983-09-22 Manufacture of crude fish oil

Country Status (1)

Country Link
JP (1) JPS6067597A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002527603A (en) * 1998-10-21 2002-08-27 デノフア・エイ・エス Methods for separating lipids and proteins from biological materials

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002527603A (en) * 1998-10-21 2002-08-27 デノフア・エイ・エス Methods for separating lipids and proteins from biological materials

Also Published As

Publication number Publication date
JPH058239B2 (en) 1993-02-01

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