JPS5863797A - Fish oil high yield collection by digestion process - Google Patents

Fish oil high yield collection by digestion process

Info

Publication number
JPS5863797A
JPS5863797A JP16106681A JP16106681A JPS5863797A JP S5863797 A JPS5863797 A JP S5863797A JP 16106681 A JP16106681 A JP 16106681A JP 16106681 A JP16106681 A JP 16106681A JP S5863797 A JPS5863797 A JP S5863797A
Authority
JP
Japan
Prior art keywords
oil
fish
weight
fish oil
yield
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
JP16106681A
Other languages
Japanese (ja)
Inventor
富山 哲夫
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.)
PURANDO KENKYUSHO KK
Original Assignee
PURANDO KENKYUSHO KK
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 PURANDO KENKYUSHO KK filed Critical PURANDO KENKYUSHO KK
Priority to JP16106681A priority Critical patent/JPS5863797A/en
Publication of JPS5863797A publication Critical patent/JPS5863797A/en
Pending 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】 本発明は魚体あるいは魚滓を酸性として加温自己消化し
、該自己消化液の含油量が概ね20重量%になるように
魚油を添加してエマルジョン中の油分を抽出することよ
りなる魚油の高率採取方法lこ関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention involves heating and autolyzing fish bodies or fish dregs to make them acidic, and adding fish oil so that the oil content of the autolysed liquid is approximately 20% by weight to extract the oil content in the emulsion. This relates to a high-efficiency method for harvesting fish oil.

さらに詳しくは、魚体あるいは魚滓に塩酸、硫酸または
リン酸などの無機酸またはリン酸などの有機酸の1種ま
たは2種以上を加えてpHを3.5〜5.5、好ましく
は4〜5に調整して45〜65℃、好ましくは50〜6
0’Cに加温[7て自己消化せしめ、該自己消化液の含
油量が概ね20重量%になるように魚油を混和攪はんし
、エマルジョン中の油分を抽出することよりなる魚油の
採取方法Cある。
More specifically, one or more inorganic acids such as hydrochloric acid, sulfuric acid, or phosphoric acid, or organic acids such as phosphoric acid are added to the fish body or fish dregs to adjust the pH to 3.5 to 5.5, preferably 4 to 5. 5 to 45-65°C, preferably 50-6
Collection of fish oil by heating to 0'C [7] for autolysis, mixing and stirring fish oil so that the oil content of the autolysate becomes approximately 20% by weight, and extracting the oil content in the emulsion. There is method C.

魚体あるいは魚滓は高度不飽和脂肪障含有油の給源であ
るが、加熱によるだん白凝固法(魚粉製造法)では原料
含油量が1.3重量%以下の場合企業的に全く採油でき
ないものとされている。また本発明者は酵素消化法では
原料含油量が4重量%以下の場合実験的に採油できない
ことを確認している。特に酵素消化法による収率が劣っ
ているのは、魚油が不消化だん白部とエマルジョンをつ
くって抽出がさまたげられるためである。
Fish bodies or fish dregs are a source of highly unsaturated fatty acid-containing oil, but if the oil content of the raw material is less than 1.3% by weight using the Danpaku coagulation method (fishmeal production method) by heating, it will not be possible to extract the oil at all for commercial purposes. has been done. Furthermore, the present inventor has experimentally confirmed that oil cannot be extracted using the enzymatic digestion method when the raw material oil content is 4% by weight or less. In particular, the yield obtained by enzymatic digestion is poor because the fish oil forms an emulsion with indigestible protein, which hinders extraction.

凡そ消化法においては、胆汁などの表面活性力が消化中
に原料油のエマルジョン形成を助け、このエマルジョン
が皮、内臓の不消化結蹄組織たん白と強く結合するため
に、固−液一油の3相分離を困難にする。
In general, in the digestion method, surface active forces such as bile help form an emulsion of the raw material oil during digestion, and this emulsion strongly binds to the indigestible clove tissue protein of the skin and internal organs, so that the solid-liquid oil is mixed. makes three-phase separation difficult.

然るに本発明者はこの際過化液の含油量を増加して親密
に混和すればエマルジョンは油層と衝突して油層に融合
されてエマルジョンが抽出されるので、3相分離が容易
に行われること、したがって消化液の含油量を一定量以
上に増大する場合にはエマルジョンから抽出されて3相
分離し易くなり魚油の収率を増大しうろことを明らかに
した。
However, the present inventor believes that if the oil content of the peroxidized liquid is increased and the mixture is intimately mixed, the emulsion collides with the oil layer and is fused with the oil layer, and the emulsion is extracted, thereby facilitating three-phase separation. Therefore, it was clarified that when the oil content of the digestive fluid is increased beyond a certain level, it becomes easier to extract the fish oil from the emulsion and separate the three phases, increasing the yield of fish oil.

本発明の方法を消化液に魚油を無添加/添加の場合にお
ける試料の含油率と魚油の収率との関係について例示し
た第1図について説明すれば、消化法で線Aは魚油を添
加しない場合における油の収率、また線Bは原料の油に
魚油を添加した場合におりる油の収率を示した線で、原
料の含油量が増加するほど油の収率が増加することを示
している。例えば原料の含油量が12重量%であれば油
の収率は原料の6重量%、すなわち含油量の収率―〕5
0重量%となる。この数値を外延し2て、含油量を20
重量%に増加すれば100重量−の収率がえられること
になる。
To explain the method of the present invention with reference to Figure 1, which illustrates the relationship between the oil content of the sample and the yield of fish oil when fish oil is not added/added to the digestive fluid, in the digestion method, line A indicates no addition of fish oil. Line B is a line showing the oil yield when fish oil is added to the raw material oil, and shows that the oil yield increases as the oil content of the raw material increases. It shows. For example, if the oil content of the raw material is 12% by weight, the oil yield is 6% by weight of the raw material, that is, the yield of the oil content -]5
It becomes 0% by weight. Extend this number by 2 to get the oil content by 20
% by weight, a yield of 100% by weight will be obtained.

したがって、含油量の低い原料魚の場合に、消化液の含
油量を概ね20重量%に増加すれば線Bの油を含む原料
魚1005’を消化して遠心分離しても、油の大部分は
エマルジョンをつくり、o2J2.す(含油量の4重量
%)しか分離できない。しかしこの原料の消化液100
pに約isyの魚油を加えて新型に約1時間混用後、遠
心分離すれ一:、約17.5 LJ−の油がえられ、添
加油量を除外して、251の採油となり、含油量の50
重量%かえられてV・る。
Therefore, in the case of raw material fish with low oil content, if the oil content of the digestive fluid is increased to approximately 20% by weight, even if raw material fish 1005' containing oil in line B is digested and centrifuged, most of the oil will be removed. Make an emulsion and o2J2. (4% by weight of oil content) can be separated. However, this raw material has 100% digestive juice.
After adding about isy of fish oil to P and mixing it with the new type for about 1 hour, it was centrifuged and about 17.5 LJ- of oil was obtained.Excluding the amount of added oil, the oil yield was 251, and the oil content was 50 of
The weight percentage was changed to V.ru.

これを要するに、本発明においては消化液中の魚油の採
取率は消化液の魚油の含油率の増加と共に増加するもの
であり、その採取率は消化液中の魚油の含油率が20重
量%以上で、10000重量%率に達しうるものである
ことを示している。
In short, in the present invention, the collection rate of fish oil in the digestive juice increases as the oil content of the fish oil in the digestive juice increases, and the collection rate increases when the oil content of the fish oil in the digestive juice is 20% by weight or more. This shows that the content can reach 10,000% by weight.

しかしながら、この事実t、1本発明方法c′こおける
消化液中の魚油の含油率を20重量%以上に限定するも
のではない。
However, this fact does not limit the oil content of fish oil in the digestive juices to 20% by weight or more in the method c' of the present invention.

次に本発明実施の例を示す。Next, an example of implementing the present invention will be shown.

実施例 l。Example l.

イワシ10Ky(含油率8.1重量%)を播砕し、水5
−eと10重量%塩酸0.6矛とを加えてpHを46と
し、ついで60℃に加温し、ときどき攪はんしつつ8時
間消化した後、・1.2−13の魚油を加えて30分ゆ
るやかに攪はんし、油層を遠心分離した。魚油の収量0
.67−e、収率83チであった。
10Ky of sardines (oil content 8.1% by weight) were crushed,
-e and 0.6 tablespoons of 10% by weight hydrochloric acid were added to adjust the pH to 46, then heated to 60°C and digested for 8 hours with occasional stirring, followed by the addition of 1.2-13 fish oil. The mixture was gently stirred for 30 minutes, and the oil layer was centrifuged. Fish oil yield 0
.. 67-e, yield was 83.

1.21の添加油を加えなかった場合、魚油の収量0.
16.、e(計算値の20重量To)Cあったから、0
.15A(計算値の63重量%)の収量増であった。
If no added oil of 1.21 was added, the yield of fish oil would be 0.
16. , e (calculated value of 20 weight To) Since there was C, 0
.. The yield was increased by 15A (63% by weight of the calculated value).

実施例 2゜ 魚津10Ky(含油率9.2重量係)を揺砕し、10重
量%塩酸0.9ノを加えてpH4,2とし、ついで60
℃に加温し、ときどき攪はんしつつ3時間消化し、これ
に1.5pの魚油を加えて30分間ゆるやかに攪はんし
た後、遠心分離機で油層を分離した。魚油の収量0.8
3−g、収量90%、添加油を加えなかった場合、魚油
の収量0.2’l(計算値の31重量%)であったから
、0.54[(計算値の59チ)の収量増であった。
Example 2゜Uozu 10Ky (oil content 9.2% by weight) was shaken and crushed, 10% by weight hydrochloric acid 0.9% was added to adjust the pH to 4.2, and then the pH was adjusted to 60% by weight.
℃ and digested for 3 hours with occasional stirring, 1.5p of fish oil was added thereto, gently stirred for 30 minutes, and the oil layer was separated using a centrifuge. Fish oil yield 0.8
3-g, yield 90%, if no added oil was added, the yield of fish oil was 0.2'l (31% by weight of the calculated value), so the yield increased by 0.54 [(59% of the calculated value)] Met.

実施例 3゜ 小アジ5に2(含油率42重量%)を拙砕し、水3pと
10重量係塩酸0.35−eを加えてpH4,2として
55℃に加温し、ときどき攪はんしつつ、15時間消化
した後、800 mlO魚油を添加してゆるやかに1時
間批はんしてから遠心分離機で油層を分離した0魚油の
収量95m1、収率48;6、添加油を加えなかった場
合、魚油はほとんど分離しなかったので95m1の収量
増であった。
Example 3 Crushed 2 (oil content 42% by weight) with 5 small horse mackerel, added 3 parts of water and 0.35 e of hydrochloric acid per 10 parts by weight to adjust the pH to 4.2, and heated to 55°C, stirring occasionally. After digesting for 15 hours, 800 mlO fish oil was added, stirred gently for 1 hour, and the oil layer was separated using a centrifuge.The yield of 0 fish oil was 95ml, yield 48;6, and the added oil was When it was not added, almost no fish oil was separated, resulting in an increase in yield of 95 ml.

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

第1図は消化液に魚油を無添加/添加の場合における試
料含油率と魚油の収率との関係を示す。 特許出願人 株式会社 パう71・゛研究所出願代理人
  国 井 真 吾 iI  w 沈 鼎 め 右 呻 卆 〃 )寺1参1日R58−63797(3)手続補正書 昭和56年11月l乞 特許庁長官 島田春樹 殿 1、事件の表示 ll11和56年特許願第161066  号2・発明
の名称 消化法による魚油の高率採軸3、 補正をする
者 事件との関係  事大 !t > t’r 針+*ζ6
、  W正により増加す乏発明の数 7、補正の対象  明細書の詳細な発明の欄8、補正の
内容 明細書の詳細な説明の欄下記の誤記を訂正する。 1 第2頁s6行目、 [・・・・・・脂肪含有油の」とあるな[・−・−脂肪
酸含有・・・・・・」と訂正する。 ■ 第4頁第1行「・・・−5k)Jとあるな「・・・
=St」と訂正する。 −第5頁第8行目、 ro、tsJ・・・・・」とあるを「0.51J−・・
・・・」と訂正する。
FIG. 1 shows the relationship between sample oil content and fish oil yield in the cases where fish oil was not added/added to the digestive fluid. Patent Applicant: Pau 71 Institute Co., Ltd. Application Agent: Makoto Kunii (Shin Ding Me) R58-63797 (3) Procedural Amendment November 1980 Mr. Haruki Shimada, Commissioner of the Patent Office1, Indication of the case 11 Japanese Patent Application No. 161066 2 Title of the invention High rate extraction of fish oil by digestion method 3 Relationship with the amended person case Important! t >t'r needle + *ζ6
, The number of deficient inventions will increase due to the W amendment 7, Subject of amendment Detailed invention column 8 of the specification, Contents of amendment The following errors in the detailed explanation column of the specification will be corrected. 1 Page 2, line s 6, it says [...of fat-containing oil]. Correct it to read [...-fatty acid content...]. ■ Page 4, line 1 "...-5k) J"...
=St”. -Page 5, line 8, replace "ro, tsJ..." with "0.51J-...
"..." I corrected myself.

Claims (1)

【特許請求の範囲】[Claims] 魚体あるいは魚滓に酸を加えてpHを3.5〜5.5と
し−C45〜65℃に加温してなる自己消化液に該自己
消化液の含油量が概ね20重量%になるように魚油を混
和攪はんしたる後、静置または遠心分離等によりて分離
することを特徴とする消化法による魚油の高率採取方法
Add acid to fish bodies or fish dregs to adjust the pH to 3.5 to 5.5 and heat to -C45 to 65°C to produce an autolysing liquid such that the oil content of the autolysing liquid is approximately 20% by weight. A high-efficiency method for collecting fish oil using a digestion method, which is characterized by mixing and stirring fish oil and then separating it by standing or centrifuging.
JP16106681A 1981-10-12 1981-10-12 Fish oil high yield collection by digestion process Pending JPS5863797A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16106681A JPS5863797A (en) 1981-10-12 1981-10-12 Fish oil high yield collection by digestion process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16106681A JPS5863797A (en) 1981-10-12 1981-10-12 Fish oil high yield collection by digestion process

Publications (1)

Publication Number Publication Date
JPS5863797A true JPS5863797A (en) 1983-04-15

Family

ID=15727962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16106681A Pending JPS5863797A (en) 1981-10-12 1981-10-12 Fish oil high yield collection by digestion process

Country Status (1)

Country Link
JP (1) JPS5863797A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001088961A3 (en) * 2000-05-19 2002-02-28 Biozyme Systems Inc Process for recovering bone and oil from animal byproducts
JP2020534860A (en) * 2017-07-28 2020-12-03 ウニコ‐ファースト アーゲー Methods of using animal products to extract nutritionally beneficial or biologically active ingredients, and the extracts obtained thereby.

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001088961A3 (en) * 2000-05-19 2002-02-28 Biozyme Systems Inc Process for recovering bone and oil from animal byproducts
US6685975B2 (en) 2000-05-19 2004-02-03 Biozyme Systems Inc. Process for recovering bone and oil from animal byproducts
JP2020534860A (en) * 2017-07-28 2020-12-03 ウニコ‐ファースト アーゲー Methods of using animal products to extract nutritionally beneficial or biologically active ingredients, and the extracts obtained thereby.

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