JPH0255019B2 - - Google Patents
Info
- Publication number
- JPH0255019B2 JPH0255019B2 JP58088832A JP8883283A JPH0255019B2 JP H0255019 B2 JPH0255019 B2 JP H0255019B2 JP 58088832 A JP58088832 A JP 58088832A JP 8883283 A JP8883283 A JP 8883283A JP H0255019 B2 JPH0255019 B2 JP H0255019B2
- Authority
- JP
- Japan
- Prior art keywords
- okara
- feed
- dehydrated
- raw
- raw okara
- 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.)
- Expired - Lifetime
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- Fodder In General (AREA)
Description
この発明は、生おからを主成分とする発酵飼料
を製造する方法に関するものである。
従来生おからの用途の一つに飼料があるが、生
おからは、水分含量が高くて保存性に乏しく、為
に、1〜3日で変敗を来し、日配的に供給し且つ
短時間のうちに消費しなければならない不都合が
あつた。一方、水分の多い飼料原料は、嫌気的に
発酵させて、所謂サイレージとすることが行われ
ているが、通常のおからを単に嫌気状態においた
だけでは、乳酸発酵がおこりがたく、おからを主
原料にした安価な飼料原料を、保存下に嗜好性の
高い飼料に変換することは未だ行われていない。
通常のおからは豆腐粕とも称され、次表の組成
を有する(「日本標準飼料成分表」農林省農林水
産術会事務局編、中央蓄産会発行)が、本発明者
は、大豆又は脱脂大豆を水性溶媒で抽出する際、
高温に可及的さらさないないようになどすると、
副生するおからの成分について、粗蛋白質含量及
び可溶無窒素物の割合のおからとはかなり相違さ
せることができることに着目し、これを利用すれ
ば良好な発酵飼料がえられるのではないか、との
着想から、種々研究を行つた結果、粗蛋白質に対
する可溶無窒素物の重量比が1.5以上、PH5以下
の脱水性おからを調製すれば、これを主成分とし
た飼料原料を嫌気的に発酵して嗜好性の高い飼料
に変換させることができることを見いだし、この
発明を完成した。
The present invention relates to a method for producing fermented feed containing raw okara as a main component. Traditionally, raw okara has been used as feed, but raw okara has a high moisture content and has poor storage stability.As a result, it deteriorates within 1 to 3 days, so it cannot be supplied on a daily basis. In addition, there was an inconvenience that the product had to be consumed within a short period of time. On the other hand, feed materials with a high moisture content are fermented anaerobically to produce so-called silage, but if ordinary okara is simply left in an anaerobic state, lactic acid fermentation is difficult to occur. It has not yet been possible to convert inexpensive feed raw materials, which are mainly made from , into highly palatable feeds during storage. Ordinary okara is also called tofu meal and has the composition shown in the following table ("Japan Standard Feed Composition Table" edited by the Agriculture, Forestry and Fisheries Association Secretariat of the Ministry of Agriculture, Forestry and Forestry, published by the Chuo Food Products Association). When extracting with an aqueous solvent,
Avoid exposing it to high temperatures as much as possible.
We focused on the fact that the components of by-product okara can be made quite different from those of okara in terms of crude protein content and soluble nitrogen-free content, and if we use this, we can produce good fermented feed. Based on this idea, we conducted various studies and found that if we prepare dehydrated okara with a weight ratio of soluble nitrogen-free substances to crude protein of 1.5 or more and a pH of 5 or less, we can use it as a feed material as the main ingredient. They discovered that it could be fermented anaerobically and converted into highly palatable feed, and completed this invention.
【表】
すなわちこの発明は、PH4〜5で水分77%以下
に脱水した粗蛋白質に対する可溶無窒素物の重量
比が1.5以上の生おからを得、これを主成分とす
る水分60%以上の飼料原料を、嫌気的に発酵させ
ることを特徴とする飼料の製造法であり、安価
に、嗜好性の高い飼料を製造することを目的とす
る。
上記表の様に、通常のおから(豆腐粕)では、
粗蛋白質に対する可溶無窒素物の重量比が1.2程
であるが、この比を高めるためのおからの調製に
は、大豆又は脱脂大豆を水性溶媒で抽出する際蛋
白質の熱変性が可及的少なくなる温度を用いるこ
とが最も有効であり、80℃を越える温度帯に長時
間曝さないのがよい。副次的には、大豆又は脱脂
大豆を水性溶媒で抽出した残渣をさらに水性溶媒
で抽出する多段階抽出を行うと、蛋白質が抽出さ
れる率が可溶無窒素物より相対的に高まるので、
前記重量比を高めるのに有効である。
脱水生おから中の粗蛋白質に対する可溶無窒素
物の重量比が1.5よりも低いと、これを主成分と
する飼料原料を嫌気的条件に置いても、殆ど乳酸
発酵がおこらず、良好な芳香や高い嗜好性の発酵
飼料を得難いのである。上記重量比は2.0以上に
するのがより好ましい。
この発明で使用するおからは、また、PH5以下
の脱水したものである。PHがこれより高いと、良
好な芳香を有する高い嗜好性の発酵飼料となり難
く、また脱水効率を高め難い。ただしPHが低すぎ
ると付酸処理するための設備にコストを要した
り、さらにPHが低くなると脱水効率が悪くなるの
で、通常PHを4より低くする利益は少ない。脱水
の程度は通常77%以下にするのがよく、このよう
な水分は、PHが4〜5の範囲であることにより、
通常の脱水機を用いて容易に達成できる。脱水し
て低水分にすることは、保存性の向上に役立つ
が、生おからの調製から、嫌気的発酵の過程に置
くまで4日程度以上を要する場合には加熱処理を
施してあるのが好ましい。この加熱処理は、脱水
前、湿おから基準で2.5〜4.5倍の加水をし、80℃
以上の温度において10分以上加熱するのがよく、
上記脱水処理とあいまつて、生おからの保在性を
著しく向上させる効果がある。
このようにして得られた脱水生おからは、これ
を主成分にした飼料原料にして、嫌気的に発酵さ
せることにより、良好な芳香や高い嗜好性を付与
された飼料にすることができる。
この発明では、脱水生おから以外に公知のどの
ような原料も補助的に用いるのをさまたげるもの
ではない。特に少量の糖質原料や乳酸菌を添加す
ると、卓越的且つ安定的に乳酸発酵させるのに役
立つ。安価な糖質原料としては、米糖、麸、玉蜀
黍等が例示されるが、これらでも、脱水生おから
より一般に高価であるから少量の使用にとどめる
のが経済的である。これら糖質原料は、また、飼
料原料の水分調整料としても機能させることが出
来る。
嫌気的発酵に供すべき飼料原料として好ましい
水分は概ね60%以上であり、これ以下では、乳酸
発酵の速度が遅くなつたり、踏圧による脱気がや
や困難で酪酸発酵などの異常発酵も起こる場合が
ある。脱水生おからの水分にもよるが、脱水生お
からの水分が70〜77%程度の範囲にあるとき、上
記水分調整料として用いる糖質原料は、全原料中
精々20%程をも必要としない。即ち米糖等の糖質
原料を多く用いたとき家畜の脂肪が所謂軟脂にな
り易い傾向を回避できる利点がある。
発酵は、所謂サイレージ調製の常法、即ちサイ
ロまたは適当な容器中に飼料原料を詰め込み、踏
圧または他の適当な手段により可及的脱気し、嫌
気的状態下で保存する。給餌するのに適当な期間
は、秀節、気温、水分等により相違するが、発酵
開始後、夏場で概ね15〜30日、冬場で概ね30〜60
日程度が適当である。
本発明によつて製造された飼料は、乳牛、肉
牛、豚等に好んで食される良好なものである。
以下この発明の実施例を挙げる。
実施例 1
低変性脱脂大豆フレーク1部に水道水7部を加
え、PH7.0において40℃50分間撹拌して抽出を行
ない、分離した抽出残渣に水道水5部を加え、同
じく40℃10分間撹拌抽出を行ない、再び分離した
抽出残渣(水分84%)に、2.5部の水を加えてPH
4.5とし、容器中に導入して蒸気を吹き込み85℃
で10分間加熱処理した後、スクリユープレスで脱
水しておからを得た。比較として常法による豆腐
製造工程で副生した製造直後のおから(水分84
%)を、同様に加水、酸性化、加熱、脱水したも
のを用いた。これらの成分は次の表の通りであつ
た。[Table] That is, the present invention obtains raw okara having a weight ratio of soluble nitrogen-free substances to crude protein that is dehydrated to a moisture content of 77% or less at pH 4 to 5 and is 1.5 or more, and produces raw okara having a moisture content of 60% or more as a main component. This method of producing feed is characterized by anaerobically fermenting feed materials, and its purpose is to produce feed with high palatability at low cost. As shown in the table above, regular okara (tofu lees)
The weight ratio of soluble nitrogen-free substances to crude protein is about 1.2, but in order to increase this ratio, it is possible to prepare okara by thermally denaturing the protein when extracting soybeans or defatted soybeans with an aqueous solvent. It is most effective to use a lower temperature, and it is best not to expose the product to temperatures above 80°C for long periods of time. Secondaryly, if a multi-step extraction is performed in which the residue obtained by extracting soybeans or defatted soybeans with an aqueous solvent is further extracted with an aqueous solvent, the extraction rate of protein will be relatively higher than that of soluble nitrogen-free substances.
This is effective in increasing the weight ratio. If the weight ratio of soluble nitrogen-free substances to crude protein in dehydrated raw bean curd is lower than 1.5, lactic acid fermentation will hardly occur even if the feed material containing this as the main ingredient is placed under anaerobic conditions, resulting in a good result. It is difficult to obtain fermented feed with aroma and high palatability. It is more preferable that the weight ratio is 2.0 or more. The okara used in this invention is also dehydrated to a pH of 5 or less. If the pH is higher than this, it is difficult to obtain fermented feed with good aroma and high palatability, and it is difficult to increase dehydration efficiency. However, if the pH is too low, the cost of equipment for acid treatment will be required, and if the pH is further lowered, the dehydration efficiency will deteriorate, so there is usually little benefit in lowering the pH below 4. The degree of dehydration should normally be 77% or less, and such moisture can be reduced by having a pH in the range of 4 to 5.
This can be easily achieved using a normal dehydrator. Dehydration to reduce the moisture content helps to improve shelf life, but if it takes more than 4 days from preparing raw okara to putting it through the anaerobic fermentation process, heat treatment is recommended. preferable. In this heat treatment, water is added 2.5 to 4.5 times based on wet okara before dehydration, and the temperature is increased to 80°C.
It is best to heat for 10 minutes or more at the above temperature.
Combined with the above dehydration treatment, this has the effect of significantly improving the retention of raw okara. The dehydrated raw okara thus obtained can be made into a feed material having a good aroma and high palatability by fermenting it anaerobically. In this invention, there is no hindrance to the supplementary use of any known raw material other than dehydrated raw bean curd. In particular, adding a small amount of carbohydrate raw materials or lactic acid bacteria helps to achieve excellent and stable lactic acid fermentation. Examples of inexpensive carbohydrate raw materials include rice sugar, wheat flour, and maize, but even these are generally more expensive than dehydrated raw okara, so it is economical to use only a small amount. These carbohydrate raw materials can also function as moisture regulators for feed raw materials. The preferred moisture content for feed raw materials to be subjected to anaerobic fermentation is approximately 60% or more; if it is less than this, the rate of lactic acid fermentation may be slow, degassing due to treading may be somewhat difficult, and abnormal fermentation such as butyric acid fermentation may occur. be. It depends on the moisture content of dehydrated raw okara, but when the moisture content of dehydrated raw okara is in the range of 70 to 77%, the carbohydrate raw material used as the moisture adjustment agent needs to be at most 20% of the total raw materials. I don't. That is, it has the advantage of avoiding the tendency for livestock fat to become so-called soft fat when a large amount of carbohydrate raw materials such as rice sugar is used. Fermentation is carried out using the conventional method of so-called silage preparation, ie, the feed material is packed into a silo or a suitable container, deaerated as much as possible by treading or other suitable means, and stored under anaerobic conditions. The appropriate period for feeding varies depending on the season, temperature, moisture, etc., but after the start of fermentation, it is approximately 15 to 30 days in summer and 30 to 60 days in winter.
Approximately one day is appropriate. The feed produced by the present invention is a good feed that is preferred by dairy cattle, beef cattle, pigs, and the like. Examples of this invention will be described below. Example 1 Add 7 parts of tap water to 1 part of low-denatured defatted soybean flakes, stir at pH 7.0 at 40°C for 50 minutes to perform extraction, add 5 parts of tap water to the separated extraction residue, and stir at 40°C for 10 minutes. Perform stirring extraction and add 2.5 parts of water to the extracted residue (84% water) separated again to adjust the pH.
4.5, then introduced into a container and blown steam to 85℃.
After heat treatment for 10 minutes, okara was obtained by dehydration using a screw press. For comparison, okara (moisture: 84
%) was similarly hydrated, acidified, heated, and dehydrated. These ingredients were as shown in the table below.
【表】
両脱水おからは、各々の9部に対し米糖1部を
加えて飼料原料とし、これを200容の罐中に入
れ、踏圧により150Kg充填後、非通気性シートで
密着カバーし、30℃の恒温室で15日間嫌気状態に
保つた。上記保存後、内容物を取り出して評価し
たところ次の結果を得た。
即ち本例のものは、PH3.7となり乳酸発酵に特
有の甘酸つぱい芳香が有り、色調も詰め込み時と
変化なく明るい色調を保つており、良質のサイレ
ージであると判定された。一方比較のものはPH
4.3で乳酸発酵の進行が遅く、やや酪酸臭感じら
れ、色調はやや暗褐色に変化しており不良と判定
された。
実施例 2
脱水生おからを調製後、直ちに使用するのでは
なく25℃で10日間開放状態で放置してから使用す
る他は実施例1と同様にして発酵飼料を調製した
が、開放状態の保存時に腐敗は生じず、且つ発酵
飼料も実施例1と同様に良好であつた。比較とし
て同じく脱脂大豆から調製した脱水生おからを用
いたが(但し、比較2のものは酸性化のPHが5.5
のため脱水後の水分は79%であり、比較3のもの
は脱水前の加熱を行わなかつたものである)、25
℃開放状態で放置する間、これら比較はいずれも
4日目で腐敗臭が感じられ、いずれも10日目には
到底発酵飼料の原料となりえないものであつた。
実施例 3
実施例1と同じ脱水生おから(調製後3日経
過)に対して米糖を、水分調整もしくは糖質補強
に種々の割合で加え、若しくは加えず、他は実施
例1と同様に発酵飼料を製造したところ、95:5
〜85〜15の配合のものが最も良質であつた。[Table] For both dehydrated okara, add 1 part of rice sugar to 9 parts of each to use as a feed ingredient, put this into a 200-volume can, fill it with 150 kg by treading, and then cover tightly with a non-breathable sheet. The cells were kept under anaerobic conditions for 15 days in a constant temperature room at 30°C. After the above storage, the contents were taken out and evaluated, and the following results were obtained. That is, the silage of this example had a pH of 3.7, a sweet and sour aroma characteristic of lactic acid fermentation, and the color tone remained bright, unchanged from when it was packed, and was judged to be a good quality silage. On the other hand, the comparison one is PH
At 4.3, the progress of lactic acid fermentation was slow, a slight butyric acid odor was felt, and the color changed to a slightly dark brown, so it was judged as poor. Example 2 Fermented feed was prepared in the same manner as in Example 1, except that after preparing dehydrated raw okara, it was not used immediately, but was left open for 10 days at 25°C before use. No spoilage occurred during storage, and the fermented feed was also good as in Example 1. For comparison, we used dehydrated raw okara prepared from defatted soybeans (however, in Comparison 2, the pH of acidification was 5.5).
Therefore, the moisture content after dehydration was 79%, and the one in comparison 3 was not heated before dehydration), 25
While left in an open state at ℃, in all of these comparisons, a putrid odor was felt on the 4th day, and on the 10th day, all of them could not be used as raw materials for fermented feed. Example 3 Rice sugar was added or not added in various proportions to the same dehydrated raw okara (3 days after preparation) as in Example 1 for moisture adjustment or carbohydrate reinforcement, but otherwise the same as in Example 1. When we produced fermented feed, the ratio was 95:5.
The composition with a composition of ~85-15 was of the highest quality.
【表】
実施例 4
実施例1と同様に調製した脱水性おから約25ト
ンを麸500Kg、その他少量の食塩、乳酸菌と共に
地上型サイロ(2.5x2.5x4.0m3)中で嫌気的に発
酵させた(外気温約20℃前後)。30日時点のPHは
3.83で水分77%(下部取り出しの為やや水分の高
い部分)であり、良好な飼料であつた。30日経過
後6日間、乳牛1頭、1日当たり6Kg供与した
が、食い込みがよく良質であることが牧場スケー
ルで確認された。[Table] Example 4 Approximately 25 tons of dehydrated okara prepared in the same manner as in Example 1 was anaerobically fermented in an above-ground silo (2.5x2.5x4.0m 3 ) with 500kg of starch, a small amount of salt, and lactic acid bacteria. (outside temperature around 20℃). PH as of 30th is
3.83 and 77% moisture (slightly high moisture content due to removal from the bottom), making it a good feed. After 30 days, 6 kg per day was fed to one dairy cow for 6 days, and it was confirmed on a farm scale that the feed was well penetrated and of good quality.
Claims (1)
に対する可溶無窒素物の重量比が1.5以上の生お
からを得、これを主成分とする水分60%以上の飼
料原料を、嫌気的に発酵させることを特徴とする
飼料の製造法。 2 飼料原料中に占める脱水生おからの割合が80
%以上である特許請求の範囲第1項記載の製造
法。[Claims] 1. Raw okara with a weight ratio of soluble nitrogen-free substances to crude protein dehydrated to 77% or less at pH 4 to 5 is 1.5 or more, and raw okara with a water content of 60% or more containing this as a main component. A feed manufacturing method characterized by anaerobically fermenting feed ingredients. 2 The proportion of dehydrated raw okara in feed ingredients is 80%
% or more, the manufacturing method according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58088832A JPS59213366A (en) | 1983-05-19 | 1983-05-19 | Preparation of feed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58088832A JPS59213366A (en) | 1983-05-19 | 1983-05-19 | Preparation of feed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59213366A JPS59213366A (en) | 1984-12-03 |
| JPH0255019B2 true JPH0255019B2 (en) | 1990-11-26 |
Family
ID=13953913
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58088832A Granted JPS59213366A (en) | 1983-05-19 | 1983-05-19 | Preparation of feed |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59213366A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63317055A (en) * | 1987-06-18 | 1988-12-26 | Seinosuke Ueda | Production of food material |
| KR100336411B1 (en) * | 1999-12-03 | 2002-05-10 | 장철수 | The manufacturing process of high temperature unaerobic lactic acid fermentation mixed-feed |
| CN104161216A (en) * | 2013-12-14 | 2014-11-26 | 安徽牧仕达饲料科技有限公司 | Hog feed without soybean meal and preparation method thereof |
-
1983
- 1983-05-19 JP JP58088832A patent/JPS59213366A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59213366A (en) | 1984-12-03 |
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