JPS63263064A - Preparation of raw material for feed or such - Google Patents

Preparation of raw material for feed or such

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Publication number
JPS63263064A
JPS63263064A JP62095239A JP9523987A JPS63263064A JP S63263064 A JPS63263064 A JP S63263064A JP 62095239 A JP62095239 A JP 62095239A JP 9523987 A JP9523987 A JP 9523987A JP S63263064 A JPS63263064 A JP S63263064A
Authority
JP
Japan
Prior art keywords
fish
liquid
raw material
digested
digestion
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
JP62095239A
Other languages
Japanese (ja)
Inventor
Mitsuo Iizuka
飯塚 光生
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.)
YAIZU MIILE KYOGYO KUMIAI
Original Assignee
YAIZU MIILE KYOGYO KUMIAI
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 YAIZU MIILE KYOGYO KUMIAI filed Critical YAIZU MIILE KYOGYO KUMIAI
Priority to JP62095239A priority Critical patent/JPS63263064A/en
Publication of JPS63263064A publication Critical patent/JPS63263064A/en
Pending legal-status Critical Current

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  • Meat, Egg Or Seafood Products (AREA)

Abstract

PURPOSE:To obtain the titled raw material in high efficiency, by digesting fish body or wastes, guts, etc., generated in the processing of fish in a digestion tan, separating the digested product into solid and liquid and subjecting the liquid to ultrafiltration. CONSTITUTION:The whole body of a fish, a part of the body or wastes, guts, boiled soup and/or stick water generated in the processing of fish is used as a raw material. The whole body, a part of the body, wastes or guts are optionally crushed and digested in a digestion tank. The boiled soup and the stick water are digested as it is in the tank. The digested product is separated into solid and liquid and the liquid is transferred to an ultrafiltration apparatus after removing the solid component and filtered to obtain the objective raw material.

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、魚体に含まれるアミノ酸、蛋白質等を取り
出して飼料、食品、医薬品等の原料を製造する方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for producing raw materials for feed, food, medicine, etc. by extracting amino acids, proteins, etc. contained in fish bodies.

(従来の技術) 従来、漁獲された魚の処理、加工は塩蔵、調味加工、缶
詰、瓶詰、鰹節などの食用加工か主に行なわれている。
(Prior Art) Conventionally, the main methods of processing and processing of caught fish include salting, seasoning, canning, bottling, and edible processing such as dried bonito flakes.

これに対して、魚体中には豊富に含まれているアミノ酸
、蛋白質等の有機成分を取り出して積極的に利用しよう
とするものとしては、フィッシュ・ソリュブルの飼料と
しての利用、タラ、マクロ、サメなどの肝臓から採取さ
れた肝油、ビタミン油、サメの膵臓から採取されたイン
シュリンを医薬品の原料として利用する程度てあり、そ
の数は極めて少ない。
On the other hand, methods that actively try to extract and utilize organic components such as amino acids and proteins that are abundantly contained in fish bodies include the use of fish solubles as feed, cod, macro, shark, etc. Cod liver oil and vitamin oil collected from the livers of sharks, and insulin collected from the pancreas of sharks are only used as raw materials for pharmaceuticals, and the number of such products is extremely small.

(発明が解決しようとする問題点) これは主に、魚体には頭部、骨等が含まれる割合か魚肉
、内臓等に比較して極めて多く、魚肉、内臓等にしても
これよりアミノ酸、蛋白質等を採取するには、不必要な
成分を取り除かねばならず、これらの作業か極めて困難
なことによるものである。
(Problem to be solved by the invention) This is mainly due to the fact that the proportion of the head, bones, etc. contained in the fish body is extremely large compared to the fish meat, internal organs, etc., and even in fish meat, internal organs, etc., amino acids are In order to collect proteins, etc., unnecessary components must be removed, and this process is extremely difficult.

そこで、この発明は魚体より効率良くアミノ酸、蛋白質
等を増り出して飼料5食品、医薬品等の原料とする方法
を提案することを目的とするものである。
Therefore, the object of this invention is to propose a method for efficiently increasing amino acids, proteins, etc. from fish bodies and using them as raw materials for feeds, foods, medicines, etc.

(問題点を解決するための手段) この発明は上記実情に鑑み、鋭意研究の結果、魚の全魚
体又はその一部或いは魚の処理工程で得られる残滓、内
臓、煮汁、ステックウォーターの1種又は2種以上を原
料とし、このうち魚の全魚体又はその一部或いは魚の処
理工程で得られる残滓、内臓は必要に応じて粉砕して、
また煮汁、ステックウォーターはそのまま、消化槽に送
り込み、ここで消化し、更に消化物を固液分離して限外
濾過機に移送して神過する飼料、食品、医薬品等の原料
を製造する方法を提案するものである。
(Means for Solving the Problems) In view of the above-mentioned circumstances, the present invention has been developed as a result of intensive research, and has been developed based on one or two of the following: the whole fish body or a part thereof, or the residue, internal organs, broth, and stick water obtained in the fish processing process. Seeds and above are used as raw materials, of which the whole body or part of the fish, or the residue and internal organs obtained in the fish processing process are crushed as necessary.
In addition, the broth and stick water are sent as they are to a digestion tank, where they are digested, and the digested matter is further separated into solid and liquid, and then transferred to an ultrafiltration machine to be filtered to produce raw materials for feed, food, medicine, etc. This is what we propose.

ここで、原料として使用する魚としては鰹、まぐろ、い
わし等を挙げることかできる。
Here, examples of fish used as raw materials include bonito, tuna, and sardines.

また、原料は頭部、骨等を含む生の全魚体又は缶詰、鰹
節加工、食品加工等に加工された新鮮な残滓、或いは内
臓、フィツシュミールを製造する工程から製造される煮
汁、またこの煮汁から油分を取り除いて得られたステッ
クウォーター等を使用することができる。
In addition, the raw materials include raw whole fish including the head, bones, etc. or canned fish, fresh residues or internal organs from processed bonito flakes, food processing, etc., the broth produced from the process of producing fishmeal, and Stick water etc. obtained by removing oil from the broth can be used.

これらの原料はその種類によって粗砕、粉砕等の粉砕を
行なうが、煮汁、ステックウォーター等を原料とした場
合には粉砕工程を省略することかできる。また1頭部、
骨等を含む魚体等を原料とする場合には原料の大きさに
より粗砕、粉砕何れも行なう必要があるが、内臓のみを
原料とする場合には粗砕のみでよいこともある。
These raw materials are subjected to pulverization such as coarse crushing or pulverization depending on the type of raw materials, but the pulverizing step can be omitted when broth, stick water, etc. are used as raw materials. Another head,
When the raw material is a fish body containing bones, etc., it is necessary to perform either coarse crushing or crushing depending on the size of the raw material, but when using only internal organs as the raw material, only coarse crushing may be sufficient.

また、消化工程においては消化槽中に、蛋白質分解酵素
、脂肪分解酵素等の1種又は2種以上を添加して消化を
行なう。ここで使用する消化酵素としては例えば商品名
ネオビタラーゼ スーパー(乗和酵素社製)等の細菌性
蛋白質分解酵素を挙げることができる。この酵素によれ
ば、魚肉中にゼラチン質、蛋白質か急速に分解液化し、
限外濾過機における分離操作を容易に行なうことかでき
る。
In addition, in the digestion step, one or more types of proteolytic enzymes, lipolytic enzymes, etc. are added to the digestion tank to perform digestion. Examples of the digestive enzyme used here include bacterial proteolytic enzymes such as Neovitalase Super (trade name, manufactured by Noriwa Koso Co., Ltd.). According to this enzyme, gelatin and proteins in fish meat are rapidly decomposed and liquefied.
Separation operation in an ultrafilter can be easily performed.

なお、多量の消化酵素か含まれているような原料、例え
ば魚の内臓を原料とするような場合には特に外部より消
化酵素を添加する必要がない。
Note that when the raw material contains a large amount of digestive enzymes, for example, fish internal organs, there is no need to add digestive enzymes from the outside.

消化槽内での消化は、例えば原料を概略50〜60°C
に昇温し、30分〜3時間、好ましくは1時間〜−2時
間保持することにより行なわれ、消化後は70〜95°
C迄昇温し、消化を止め、消化物質を失活させる。
Digestion in a digestion tank is carried out, for example, at approximately 50 to 60°C.
Digestion is carried out by raising the temperature to 30 minutes to 3 hours, preferably 1 hour to -2 hours, and after digestion, the temperature
The temperature is raised to C to stop digestion and deactivate the digested substances.

消化物は、固液分離して限外濾過機に移送する。固液分
離は振動篩、遠心分離機、油分m機等を使用して行なわ
れるか、消化状況によつてはこれらの固液分離を全て行
なう必要もなく、これらの1種又は2種以上を組合せて
行なえばよい場合もある。なお、限外濾過機の前段階又
は後段階に最終製品の塩分濃度を調整するために、塩分
除去工程を挿入してもよい。
The digested material is separated into solid and liquid and transferred to an ultrafilter. Solid-liquid separation may be carried out using a vibrating sieve, centrifuge, oil separator, etc.Depending on the digestion situation, it may not be necessary to perform all of these solid-liquid separations, and one or more of these may be used. In some cases, a combination may be sufficient. Note that a salt removal step may be inserted before or after the ultrafilter in order to adjust the salt concentration of the final product.

限外濾過機では消化物は、限外濾過膜を通過させられる
ことによって内部に含まれる油分等が取り除かれる。
In the ultrafilter, the digested material is passed through an ultrafiltration membrane to remove oil and the like contained therein.

限外濾過機から取り出された痘過液はそのままで飼料、
食品、医薬品等の原料として使用することができるが、
更に濃縮工程に移送して得られた濃縮エキス、濃縮・乾
燥工程に移送して得られた乾燥製品をこれらの原料とし
て使用してもよい。
The smallpox filtrate taken out from the ultrafilter can be used as feed,
It can be used as a raw material for foods, medicines, etc.
Further, a concentrated extract obtained by transferring to the concentration step and a dry product obtained by transferring to the concentration/drying step may be used as these raw materials.

なお、限外濾過機から取り出す工程て吐過液か与しく発
泡する場合には消泡剤を濾過液中に添加することもある
In addition, if the discharged liquid foams considerably during the step of taking it out from the ultrafilter, an antifoaming agent may be added to the filtrate.

(実施例) 以下、この発明の実施例を示す。(Example) Examples of this invention will be shown below.

魚類の全体又は缶詰、am加工、食品加工等に加工され
た新鮮な残滓或いはこれらの内臓等を原料とする。
Raw materials include whole fish, canned fish, fresh residues processed through AM processing, food processing, etc., or their internal organs.

粉砕工程には、粗砕機1とポンプ2を介して粉砕機3か
設けられており、上記原料は必要により粗砕機1で先ず
粗砕する0次に、粗砕された原料は水を添加してポンプ
2で粉砕機3に送り込み、更に粉砕して原料の持つ有効
成分が七分液側に移行するように加工する。
In the crushing process, a crusher 3 is provided via a crusher 1 and a pump 2, and the raw material is first crushed by the crusher 1 if necessary.Next, water is added to the crushed raw material. The raw material is sent to a crusher 3 using a pump 2, and is further crushed so that the active ingredients of the raw material are transferred to the liquid.

粉砕413で粉砕された原料は、必要に応じて水を添加
してポンプ4で消化槽5に送入されて消化が行なわれる
。消化槽5では原料により、必要により水分を20%か
ら20oz加水して消化酵素を添加して消化したり、或
いは原料自体に依る自己消化を行なうことにより、ゼラ
チン分等を分解し、後工程の有効成分の分離を効果的に
進めることができる。
The raw material pulverized in the pulverization 413 is fed to the digestion tank 5 by the pump 4 with water added thereto as required, and is digested. In the digestion tank 5, depending on the raw material, if necessary, 20% to 20 oz of water is added and digestive enzymes are added for digestion, or the raw material itself undergoes self-digestion to decompose gelatin, etc., and prepare it for subsequent processing. The separation of active ingredients can be effectively promoted.

なお、フィ・ンシュミールを製造する工程から製造され
る煮汁、又は煮汁から油分を取り除いたステックウォー
ターについても同様に酵素分解することにより原液とし
て使用てきる。
Incidentally, the broth produced in the process of producing fish meal or the stick water obtained by removing the oil from the broth can also be used as a stock solution by enzymatically decomposing it in the same way.

また、消化槽5ての消化は、例えば原料を概略50〜5
00Cに昇温し730分〜3時間、好ましくは1時間〜
2時間保持することにより消化される。
In addition, the digestion in the digestion tank 5 is carried out, for example, by approximately 50 to 50% of the raw material.
Raise the temperature to 00C for 730 minutes to 3 hours, preferably 1 hour to
Digested by holding for 2 hours.

消化後は70〜95°C迄昇温し、消化酵素を失活させ
て消化を止める。
After digestion, the temperature is raised to 70-95°C to deactivate the digestive enzymes and stop the digestion.

消化槽5て消化された原料は、固液分離工程に移送する
。固液分離工程は、この実施例では振動篩6、遠心分離
機7、油分離機8、ストレナ−9で構成され、消化槽5
て酵素分解又は自己消化した液は振動篩6、遠心分離機
7、油分分離機8、ストレーナ−9を経て、固形分の分
離除去か行なわれる。
The raw material digested in the digestion tank 5 is transferred to a solid-liquid separation process. In this embodiment, the solid-liquid separation step is composed of a vibrating sieve 6, a centrifuge 7, an oil separator 8, a strainer 9, and a digestion tank 5.
The enzymatically decomposed or self-digested liquid passes through a vibrating sieve 6, a centrifugal separator 7, an oil separator 8, and a strainer 9 to separate and remove solids.

固形分の除去された原液は、原液タンク10a。The stock solution from which the solid content has been removed is stored in the stock solution tank 10a.

10bのいずれか一方に貯留される。原液タンク10a
 、 10bに貯留された原液は、必要に応じて塩分除
去工程を経てから内部に限外濾過IQを備えた限外濾過
機11に導かれる。
10b. Raw solution tank 10a
, 10b is guided to an ultrafilter 11 equipped with an ultrafiltration IQ inside after undergoing a salt removal process as required.

限外濾過41311ては原液の°油分、高分子の蛋白質
等の高分子成分とアミノ酸、低分子の蛋白質等の低分子
成分との分離が行なわれる。更に、原液は限外濾過機1
1と原液タンク1.Oa、]Obの間を循環することに
よりアミノ醜、低分子の蛋白質等の成分を豊富に含む液
が得られる。
Ultrafiltration 41311 separates high-molecular components such as oil and high-molecular proteins of the stock solution from low-molecular components such as amino acids and low-molecular proteins. Furthermore, the stock solution is passed through ultrafilter 1.
1 and stock solution tank 1. By circulating between Oa and ]Ob, a liquid rich in components such as amino acids and low-molecular proteins can be obtained.

このようにして液はアミノ酸、低分子の蛋白質等が豊富
に含まれているため、そのまま飼料、医薬品1食品等の
原料として使用することかできるが、これらの濃縮液、
或いはこれらの液を低温真空濃縮して得られた濃縮エキ
ス、更には濃縮エキスを乾燥して得られた乾燥製品を飼
料、医薬品、食品等の原料として使用してもよい。
Since the liquid thus produced is rich in amino acids, low-molecular proteins, etc., it can be used as is as raw material for feed, pharmaceuticals, foods, etc.; however, these concentrated liquids,
Alternatively, concentrated extracts obtained by vacuum concentrating these liquids at low temperatures, or even dried products obtained by drying the concentrated extracts, may be used as raw materials for feeds, medicines, foods, and the like.

そこで、限外濾過機11を通過したアミノ酸、低分子蛋
白質を豊富に含む濾過液はポンプ12で吸引して濾液タ
ンク14に貯留し、濾液タンク14に貯留された液は、
ポンプ15で順次真空濃縮工程に移送され、ここで低温
真空濃縮される。
Therefore, the filtrate rich in amino acids and low-molecular proteins that has passed through the ultrafilter 11 is sucked by the pump 12 and stored in the filtrate tank 14, and the liquid stored in the filtrate tank 14 is
They are sequentially transferred to a vacuum concentration step by a pump 15, where they are vacuum concentrated at a low temperature.

真空濃縮工程は濃縮装置本体16とベーパーコンデンサ
ー17と真空装置18とから構成され、上記のようにポ
ンプ15で移送された液は1:を線装置本体16のヒー
タ一部16aで加熱されて濃縮部16bに送入される。
The vacuum concentration process consists of a concentrator main body 16, a vapor condenser 17, and a vacuum device 18, and the liquid transferred by the pump 15 as described above is heated by the heater part 16a of the line device main body 16 and concentrated. 16b.

BIIrfJ部16bの内部は真空装2118で真空状
態に保持されており、したかって濾過液は水分と分離し
、濃縮が行なわれる。
The inside of the BIIrfJ section 16b is maintained in a vacuum state by a vacuum device 2118, so that the filtrate is separated from water and concentrated.

濃縮装置本体16では、例えば濃縮部16b内か真空度
fioOTorr 〜50Torr、温度約!](1〜
sa’c程度の有効成分が分解しないような条件にして
、水分60〜20%迄になるようにして低温真空濃縮が
行なわれる。
In the concentrator main body 16, for example, the inside of the concentrator 16b has a vacuum degree of fioOTorr ~50 Torr and a temperature of about 50 Torr! ] (1~
Low-temperature vacuum concentration is carried out under conditions such that the active ingredients on the sa'c level do not decompose, and the water content is reduced to 60 to 20%.

濃縮部16bで分離された水分に同伴されたミストはベ
ーパーコンデンサー17に送られる過程でミストセパレ
ータ19でミストを分離して濃縮装置本体16に戻す。
The mist entrained by the water separated in the concentration section 16b is sent to the vapor condenser 17, where it is separated by the mist separator 19 and returned to the concentration device main body 16.

更にベーパーコンデンサー17ては冷却して水分を凝縮
させ、その凝縮液を排水処理工程に移送するようにして
いる。
Furthermore, the vapor condenser 17 is cooled to condense water, and the condensed liquid is transferred to a wastewater treatment process.

また、濃縮装置本体16て得られたe縮エキスはポンプ
20で順次製品タンク21に送られ2製品タンク21で
は濃縮エキスは、必要に応じて取り出されて製品となる
が、ここで得られた′a縮エキスは低温真空で濃縮され
ているため、アミノ酸、低分子の蛋白質等が分解せず、
したがってより高濃度の飼料、食品、医薬品の原料を得
ることができる。
In addition, the e-condensed extract obtained from the concentrator body 16 is sequentially sent to a product tank 21 by a pump 20, and in the two-product tank 21, the concentrated extract is taken out as needed to become a product. 'a-condensed extract is concentrated in a low-temperature vacuum, so amino acids and low-molecular proteins do not decompose.
Therefore, it is possible to obtain feed, food, and pharmaceutical raw materials with higher concentrations.

更に、この実施例では濃縮エキスの一部を、ドラムドラ
イヤー、スプレードライヤー、真空乾燥機等の乾燥装置
22に移送し、ここでアミノ酸、蛋白質等の分解しない
ような条件下で乾燥し、得られた乾燥品は製品タンク2
3に貯留し、必要に応じて取り出し飼料、食品、医薬品
の原料として使用する。
Furthermore, in this example, a part of the concentrated extract is transferred to a drying device 22 such as a drum dryer, a spray dryer, or a vacuum dryer, where it is dried under conditions that do not decompose amino acids, proteins, etc. Dried products are stored in product tank 2.
3, and then taken out as needed and used as raw materials for feed, food, and medicine.

次に、この発明のように魚の煮汁を消化して分解した後
、該分解液(原液)を限外濾過機に通過させた場合の原
液、濾過液中の各アミノ酸含有量と各アミノ酸透過率並
びに未消化液、即ち未分解液(原液)を限外濾過機に通
過させた場合の原液、i!!過液中の各アミノ酸含有量
と各アミノ酸透過率を下記第1表に示す。
Next, after digesting and decomposing the fish broth as in this invention, the decomposition liquid (undiluted solution) is passed through an ultrafiltration machine, and the content of each amino acid in the undiluted solution and the filtrate and the permeability of each amino acid are determined. Also, the undigested liquid, i.e., the undecomposed liquid (undiluted solution), is the undiluted solution obtained by passing it through an ultrafilter, i! ! The content of each amino acid in the permeate and the permeability of each amino acid are shown in Table 1 below.

第1表     全アミノ酸A[l威(無水換算)これ
によれば、この発明のように消化した後、限外−過程を
通過させた場合には、各アミノ酸の透過率が未消化のま
ま限外濾過機を通過させた場合に比べて大きく、また処
理速度も未消化のまま限外濾過機を通過させた場合に比
べて3倍程度向上した。
Table 1 Total amino acids A This was larger than when the undigested product was passed through the ultrafilter, and the processing speed was about three times higher than when it was passed through the ultrafilter without being digested.

なお、以下に魚の内臓を消化した後、該消化液(原液)
を限外濾過機に通過させた場合の原液並びに濾過液中の
アミノ酸含有量を第2表に、前頭煮汁の酵素分解液、透
過液の試験結果を第3表に示すが、何れも上記同様の良
好な結果か得られた。
In addition, after digesting fish internal organs, the digestive juice (undiluted solution)
The amino acid content in the stock solution and filtrate when passed through an ultrafilter is shown in Table 2, and the test results for the enzymatically decomposed liquid and permeated liquid of the frontal broth are shown in Table 3, both of which are the same as above. Good results were obtained.

第2表 第3表 前頭煮汁の酵素分解液、透過液試験結果原液    透
過液 水分           96.79    97.
98アミノ酸及び蛋白質量   2.18     1
.36(発明の効果) 以上要するに、この発明によれば魚の全魚体又はその一
部或いは内臓等を必要に応じて粉砕した後、消化し、更
に消化物を固液分離して限外濾過機に移送して濾過する
ため、アミノ酸、蛋白質等飼料1食品、医薬品の原料と
しての有効成分か効率的に製造することができる。
Table 2 Table 3 Test results for enzymatic decomposition solution and permeate of frontal broth Stock solution Permeate moisture 96.79 97.
98 amino acids and protein amount 2.18 1
.. 36 (Effects of the Invention) In summary, according to the present invention, the whole body of a fish, a part thereof, internal organs, etc. are crushed and digested as necessary, and the digested product is further separated into solid and liquid and then passed through an ultrafilter. Because it is transported and filtered, it is possible to efficiently produce active ingredients such as amino acids and proteins that can be used as raw materials for feed, foods, and medicines.

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

図面は、この発明の一実施例を示すフローシートである
。 手続7市正書(方式) 昭和62年7月9日
The drawing is a flow sheet showing one embodiment of the present invention. Procedure 7 City official document (method) July 9, 1986

Claims (1)

【特許請求の範囲】[Claims] 魚の全魚体又はその一部或いは魚の処理工程で得られる
残滓、内臓、煮汁、ステックウォーターの1種又は2種
以上を原料とし、このうち魚の全魚体又はその一部或い
は魚の処理工程で得られる残滓、内臓は必要に応じて粉
砕して、また煮汁、ステックウォーターはそのまま、消
化槽に送り込み、ここで消化し、更に消化物を固液分離
して限外濾過機に移送して濾過することを特徴とする飼
料、食品、医薬品等の原料を製造する方法。
The whole body of a fish or a part thereof, or one or more of the following: the whole body of a fish, a part thereof, or the residue obtained in a fish processing process, internal organs, broth, stick water, and among these, the whole body of a fish, a part thereof, or a residue obtained in a fish processing process. The internal organs are crushed as necessary, and the broth and stick water are sent as they are to the digestion tank, where they are digested, and the digested material is separated into solid and liquid, and then transferred to an ultrafilter for filtration. A method for producing raw materials for feed, food, medicine, etc.
JP62095239A 1987-04-20 1987-04-20 Preparation of raw material for feed or such Pending JPS63263064A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62095239A JPS63263064A (en) 1987-04-20 1987-04-20 Preparation of raw material for feed or such

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62095239A JPS63263064A (en) 1987-04-20 1987-04-20 Preparation of raw material for feed or such

Publications (1)

Publication Number Publication Date
JPS63263064A true JPS63263064A (en) 1988-10-31

Family

ID=14132206

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62095239A Pending JPS63263064A (en) 1987-04-20 1987-04-20 Preparation of raw material for feed or such

Country Status (1)

Country Link
JP (1) JPS63263064A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52145556A (en) * 1976-05-31 1977-12-03 Nippon Suisan Kaisha Ltd Ultraafiltration method of water extract of fish meat
JPS5372855A (en) * 1976-12-08 1978-06-28 Toyo Jozo Kk Digestable protein food and feed
JPS55124458A (en) * 1979-03-09 1980-09-25 Nestle Sa Production of refined protein hydrolysate
JPS57183797A (en) * 1981-05-06 1982-11-12 Yamanouchi Pharmaceut Co Ltd Straight and purely short-chain peptide and its preparation
JPS6070037A (en) * 1983-06-14 1985-04-20 エデイネン・センタ−・ポ・シミア Biomass treating method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52145556A (en) * 1976-05-31 1977-12-03 Nippon Suisan Kaisha Ltd Ultraafiltration method of water extract of fish meat
JPS5372855A (en) * 1976-12-08 1978-06-28 Toyo Jozo Kk Digestable protein food and feed
JPS55124458A (en) * 1979-03-09 1980-09-25 Nestle Sa Production of refined protein hydrolysate
JPS57183797A (en) * 1981-05-06 1982-11-12 Yamanouchi Pharmaceut Co Ltd Straight and purely short-chain peptide and its preparation
JPS6070037A (en) * 1983-06-14 1985-04-20 エデイネン・センタ−・ポ・シミア Biomass treating method

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