JPS5840049A - Preparation of feed from aquatic products - Google Patents
Preparation of feed from aquatic productsInfo
- Publication number
- JPS5840049A JPS5840049A JP56139090A JP13909081A JPS5840049A JP S5840049 A JPS5840049 A JP S5840049A JP 56139090 A JP56139090 A JP 56139090A JP 13909081 A JP13909081 A JP 13909081A JP S5840049 A JPS5840049 A JP S5840049A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- tank
- feed
- temperature
- added
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
- Y02A40/81—Aquaculture, e.g. of fish
- Y02A40/818—Alternative feeds for fish, e.g. in aquacultures
Abstract
Description
【発明の詳細な説明】 本発明は、水産飼料の製造方法に関する。[Detailed description of the invention] The present invention relates to a method for producing aquatic feed.
従来、斯種水産飼料の製法として、例えば魚体原料を蒸
煮釜に入れ、高温雰囲気中で激しく攪拌し、基質中の水
分にて自己を蒸し、熱分解、物理的分解を達せしめ、骨
片等の未溶解部分等、基質全体をデカンタフィルター・
プレスにかけて水分と411分を絞り、プレス中に残存
せる固形部分を再び高圧蒸煮釜に戻し、気密化した後、
真空乾燥する製法、或いは粉砕した魚体原料に通常培養
の醗酵菌を投入して原料基質の分解醗酵をなすと共に水
分率調整と涌分吸着を目的として米ぬか、ふすま及び維
繊質等の添加物を混合し同時に0/N 比を整えて好気
的醗酵せしめることにより飼料を製造する方法とがある
。Conventionally, the method for producing this kind of aquatic feed is to put fish raw materials in a steamer, stir vigorously in a high-temperature atmosphere, steam the fish itself in the moisture in the matrix, achieve thermal decomposition and physical decomposition, and produce bone fragments etc. Remove all undissolved portions of the substrate through a decanter filter.
After pressing to squeeze out water and 411 minutes, the solid portion remaining during pressing was returned to the high-pressure steamer and made airtight.
A manufacturing method of vacuum drying, or adding normally cultured fermentation bacteria to crushed fish raw material to decompose and ferment the raw material substrate, and add additives such as rice bran, bran, and fiber for the purpose of moisture content adjustment and water absorption. There is a method of producing feed by mixing, adjusting the 0/N ratio at the same time, and performing aerobic fermentation.
しかしながら、前者の製法では原料を100℃以−1−
の高i’i+?Lで加圧加熱する為に化石燃料消費が大
であると共に基質の結晶水が分離、脱水し、有用ミネラ
ルが飛散し目、つ蛋白質が変性して力口り−はあるが栄
養価に乏しく、しかも残存する不lid和脂肪分により
酸敗しゃ易い飼料となる詐りでなく、魚油を分離除去し
た際の原料中のSS(→J−スペンディングサブジェク
ト)を含む汚水を排出する水処理システム及びその作業
を必要とする等の不利がある。また後者の製法では、燃
料消費、水処理作業、及び栄養価の間層1は解消される
一方、魚体原料に対し100%以」−の繊維質等の添加
物を投入混合する為、生成品の量は大きくなるが蛋白含
量の比率か低下すると共に品質が一定しない♂「りてな
く、火(11処理の場合、該添加物の確保、備蓄手段等
、種々の不利がある。However, in the former method, the raw materials are heated at temperatures above 100℃.
High i'i+? Since it is heated under pressure, fossil fuel consumption is large, and the crystallized water in the substrate is separated and dehydrated, useful minerals are scattered, and proteins are denatured, making it strong but lacking in nutritional value. Moreover, the water treatment system discharges the wastewater containing SS (→J-spending subject) in the raw material when fish oil is separated and removed, rather than the feed that is prone to rancidity due to the residual non-lid fat content. There are disadvantages such as the need for such work. In addition, in the latter method, fuel consumption, water treatment work, and the nutritional value layer 1 are eliminated, but since additives such as fibers are added to the fish raw material at a rate of 100% or more, the resulting product is Although the amount of protein increases, the ratio of protein content decreases and the quality is not constant.In the case of heat treatment, there are various disadvantages such as the need to secure and stockpile the additives.
このため最近、当業界に於いて、低燃費で投入添加物が
少なく、しかも製造工程簡易で製造効率の高い飼料製造
方法の出現が永年要望されていたが、現在そのようなも
のは存在しない。For this reason, there has been a long-standing demand in the industry for a feed manufacturing method that is low in fuel consumption, requires few input additives, has a simple manufacturing process, and has high manufacturing efficiency, but currently no such method exists.
本発明は、粉砕原料にミネラル水及び高温酵素を投入し
て基質を消化処理した後、更に原料に醗酵細菌及び酵素
を添加して熟酊させ、菌体の厖大な増殖を図ると共にグ
リセリン等を菌体蛋白となす巨大数機生物生棲の濃溶液
を急速乾燥することにより、」−記要望をjJ4足し、
製造1−程の簡易合理化と製造効率の向−11を達成す
る新規な水産飼料の製造方法を提供するものである。In the present invention, mineral water and high-temperature enzymes are added to the pulverized raw material to digest the substrate, and then fermentation bacteria and enzymes are added to the raw material to make it ripen, and at the same time, glycerin, etc. By rapidly drying a concentrated solution of bacterial cell proteins and a large number of living creatures,
The present invention provides a new method for producing aquatic feed that achieves the simple rationalization of the production process and the improvements in production efficiency.
以下、図面に示す装置に)、(つき本発明を具体的に説
明する。The present invention will be specifically described below with reference to the apparatus shown in the drawings.
本発明は、水1f(e加工の際に得られる魚頭、内臓等
の魚体廃棄部や全魚体を原料とし、これら(幻入村を粉
砕)幾(1)にかむづて+’ili潰し、次に粉砕化し
た原料を溶解J:Hll菖2)に投入し攪拌、放置する
。攪1゛1′する際、多元素共存ミネラル水及び微量の
植物性高7!iA fIl素を66℃乃至73℃に保つ
槽内に約8時間投入して原料に付着するザルモネラ菌、
ブドウ状球菌等の病隙菌を殺菌すると共に原料の)k
’eIを消化分解させ粉砕原料を溶液化する。The present invention uses water 1f (fish head, viscera, etc. discarded parts obtained during e-processing) and whole fish bodies as raw materials, chews them (1) and crushes them to +'ili, Next, the pulverized raw material is put into a melting vessel 2), stirred, and left to stand. When stirring 1゛1', add multi-element coexisting mineral water and a trace amount of vegetable high 7! Salmonella bacteria that adhere to the raw material by putting the iA flI element into a tank maintained at 66°C to 73°C for about 8 hours,
In addition to sterilizing pathogenic bacteria such as staphylococcus, the raw material )k
'eI is digested and decomposed and the pulverized raw material is made into a solution.
ここに於いて多元素共存ミネラル水は、生化学反応にお
ける量子化学的なレベルでの触媒作用を営む一方、助触
媒・活性原子囚として脱臭作用を捕5)↓すると共に、
次の第3工程で投入する細菌の1t11全活性化に寄与
する。更(こ、この溶液化した原料をηYり出して養生
室(3)に装填する際、微111の中7+17L D:
C正分製細菌例えはバチルス属等の好気性菌及び嫌気性
菌を投入すると共に、プロテア−セ、セルラーゼ、アミ
ラーゼ、リパーゼ等の各神加水分1’lli′r++素
を微量添加し、槽内温度43℃乃至45°C1湿度35
96の下で3〜50間養生し熟酵させる。このとき、4
1”f f31内には原料10 Klに対し3 rre
/ min を送風し、原料を送風作用と微生物活性
とにより徐々に部分脱水させ濃溶液状原料とする。ここ
に於いて、細菌及び酵素群は飽和脂肪酸、アルコール、
又はグリセリンを微生物活性のうちに彼らの代謝経路に
乗せて菌体組織の一部として」1yり入れ、全体として
は菌体蛋白となすのである。尚、各種細菌は純水培養細
菌を使用すると共に好気性菌及び嫌気性菌の配合割合は
2:]とするのか好51&である。斯くして得た濃溶液
状原料を養生室(3)から取り出し、ドラムドライヤー
(4)に入れて乾燥し粉末状飼料となすの□である。Here, multi-element coexisting mineral water performs a catalytic action at the quantum chemical level in biochemical reactions, and at the same time captures the deodorizing action as a co-catalyst and active atom prisoner5).
It contributes to the total activation of 1t11 of the bacteria introduced in the next third step. Furthermore, when taking out this solutionized raw material and loading it into the curing chamber (3), 7+17L of micro 111 D:
For example, aerobic bacteria and anaerobic bacteria such as Bacillus are added, and a small amount of each hydrolyzing element such as protease, cellulase, amylase, and lipase is added to the tank. Internal temperature 43°C to 45°C1 Humidity 35
Cured for 3 to 50 minutes under 96°C and fermented. At this time, 4
1"f f31 contains 3 rre for 10 Kl of raw material
/min, and the raw material is gradually partially dehydrated by the blowing action and microbial activity to form a concentrated solution raw material. Here, the bacteria and enzyme group are saturated fatty acids, alcohol,
Alternatively, glycerin can be carried into the metabolic pathway of microorganisms and incorporated as part of the bacterial cell tissue, forming bacterial cell proteins as a whole. It is preferable to use pure water-cultured bacteria as the various bacteria, and to mix the aerobic bacteria and anaerobic bacteria at a ratio of 2:2. The concentrated solution raw material thus obtained is taken out of the curing chamber (3) and placed in a drum dryer (4) to be dried and made into powdered feed.
実施例
魚体原料1000 Kgを粉砕機でI’ji li、’
k L/た後、溶解槽に入れ、多元素共存ミネラル水5
501゜高温酵素1501を投入して66°C乃至73
℃の下で8時間攪拌、放置した。次に、この溶液原料に
微生物固体数5000億個及び加水分解rlイ素5oo
ooユニットを投入して養生室(3)に入れた。このと
き微生物の増殖倍率速度は22分乃至45分てあった。Example 1000 kg of fish body raw material was crushed in a crusher.
After k L/, put it in a dissolution tank and add multi-element coexistence mineral water 5
501° High temperature enzyme 1501 was added and the temperature was raised to 66°C to 73°C.
The mixture was stirred and left at ℃ for 8 hours. Next, 500 billion solid microorganisms and 500 billion hydrolyzed rl ions were added to this solution raw material.
The oo unit was put in the curing room (3). At this time, the growth rate of the microorganisms was between 22 and 45 minutes.
斯くして5日間養生した濃溶液状原料の重量は1050
Krで水分含量は約70%であった。次いて濃溶液状
原料をドラムドライヤー(4)にて乾燥させたとき29
0にりの粉末飼料を得た。The weight of the concentrated solution raw material cured in this way for 5 days was 1050
The water content was about 70% in Kr. Next, when the concentrated solution raw material was dried with a drum dryer (4), 29
A powdered feed containing 0 garlic was obtained.
斯くして得られた飼料の成分は以下のとおりである。The ingredients of the feed thus obtained are as follows.
本発明は、以−」−の如く、第1工程の原料抽潰から第
4工程の原料乾燥までを常圧下で連続して行なうように
したから、製造工程が簡易で作業の安全性と製造効率の
向上に効果を発揮する。In the present invention, as described below, the steps from raw material extraction in the first step to raw material drying in the fourth step are performed continuously under normal pressure, so the manufacturing process is simple and the work safety is improved. Effective in improving efficiency.
従って従来の如く、高温加圧加熱しないから燃料消費か
少なく目つ目■消化性純タンパクの豊富な高栄養価飼料
が得られる詐りでなく魚油を分前する際の諸設備及び水
処理作業が不1υである。Therefore, unlike conventional methods, fuel consumption is reduced because high-temperature and pressure heating is not performed. - Highly nutritious feed rich in digestible pure protein can be obtained instead of deception. Various equipment and water treatment work required when distributing fish oil. is not 1υ.
また、原料に対し繊維質等の大ffF添加物か不要であ
るから大量処理にも効果を発揮する等、発明目的を達成
した効果を有する。Furthermore, since large ffF additives such as fibers are not required for the raw material, it is effective in mass processing, and has the effect of achieving the purpose of the invention.
図面は本発明に係る飼料軸θモの−L稈を示す概略図で
ある。
(1)・・・・・・粉砕機 (2)・・・・・・
溶解槽(3)・・・・・・養生室 (4)・・
・・・・ 1・゛ラムドライヤー特許出願人 平 井
孝 志The drawing is a schematic diagram showing the -L culm of the feed axis θ mo according to the present invention. (1)・・・・・・Crusher (2)・・・・・・
Dissolving tank (3)...Curing room (4)...
... 1. Lamb dryer patent applicant Hirai
Takashi
Claims (1)
第1工稈と、溶解槽(2)に粉砕原料、ミネラル水及び
高温酵素を投入し、約60℃乃至76℃で加熱処理して
原料の殺菌及び基質を消化分解する第2工程と、槽内を
約35℃乃至/18℃に保持する養生槽(3)に溶液状
原料、中l晶真性細菌及び分解酵素を投入し熟酵させて
濃溶液状原料を得る第3工程と、養生槽から取り111
シた濃溶液状原料を乾燥機(4)にて乾燥し粉末飼料を
得る第4工程とを常圧下で一連に行なうことを特徴とす
る水産飼料の製造方法。The first culm is where the fish raw material is crushed to 1'1-V 1Fji in the crusher (1), and the crushed raw material, mineral water, and high-temperature enzyme are put into the dissolution tank (2), and heat-treated at about 60°C to 76°C. In the second step, the raw materials are sterilized and the substrate is digested and decomposed, and the solution raw materials, medium-sized eubacteria, and degrading enzymes are put into the curing tank (3), which maintains the inside of the tank at a temperature of about 35°C to 18°C. The third step of fermentation to obtain a concentrated solution raw material and the removal from the curing tank 111
A method for producing aquatic feed, characterized in that a fourth step of drying a concentrated liquid raw material in a dryer (4) to obtain a powdered feed is performed in series under normal pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56139090A JPS5840049A (en) | 1981-09-02 | 1981-09-02 | Preparation of feed from aquatic products |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56139090A JPS5840049A (en) | 1981-09-02 | 1981-09-02 | Preparation of feed from aquatic products |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5840049A true JPS5840049A (en) | 1983-03-08 |
Family
ID=15237251
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56139090A Pending JPS5840049A (en) | 1981-09-02 | 1981-09-02 | Preparation of feed from aquatic products |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5840049A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000053199A1 (en) * | 1999-03-10 | 2000-09-14 | Realisec Aktiebolag | Pharmaceutical and animal fodder comprising fermented fish |
CN108559697A (en) * | 2018-04-09 | 2018-09-21 | 淮北嘉吉农牧科技有限公司 | A kind of Preparation equipment of environment protection biological feed |
JP2020182403A (en) * | 2019-05-07 | 2020-11-12 | 株式会社しいの食品 | Bait and production method of bait |
-
1981
- 1981-09-02 JP JP56139090A patent/JPS5840049A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000053199A1 (en) * | 1999-03-10 | 2000-09-14 | Realisec Aktiebolag | Pharmaceutical and animal fodder comprising fermented fish |
CN108559697A (en) * | 2018-04-09 | 2018-09-21 | 淮北嘉吉农牧科技有限公司 | A kind of Preparation equipment of environment protection biological feed |
JP2020182403A (en) * | 2019-05-07 | 2020-11-12 | 株式会社しいの食品 | Bait and production method of bait |
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