JPS5834101B2 - Feed manufacturing method - Google Patents
Feed manufacturing methodInfo
- Publication number
- JPS5834101B2 JPS5834101B2 JP57150790A JP15079082A JPS5834101B2 JP S5834101 B2 JPS5834101 B2 JP S5834101B2 JP 57150790 A JP57150790 A JP 57150790A JP 15079082 A JP15079082 A JP 15079082A JP S5834101 B2 JPS5834101 B2 JP S5834101B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- fatty acids
- feed
- present
- rice bran
- 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
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Fodder In General (AREA)
Description
【発明の詳細な説明】 本発明は、家畜の成長に好適な飼料の製造法に関する。[Detailed description of the invention] The present invention relates to a method for producing feed suitable for the growth of livestock.
従来、糠原料、殊に米糠原料は、米を精白する際に大量
に副生され、飼料原料用、担子菌類培地原料用、漬物用
等広範に利用されている。BACKGROUND ART Conventionally, bran raw materials, especially rice bran raw materials, have been produced in large quantities as a by-product when rice is polished, and have been widely used as feed raw materials, basidiomycete culture medium raw materials, pickles, etc.
そして、上記した米糠原料には、多量に油脂が含有され
ており、該米糠保存の際に、米糠原料中のリパーゼ等の
油脂分解酵素により酵素作用を受けて油脂より遊離脂肪
酸が生成し、さらに該遊離脂肪酸は、空気中の酸素によ
り酸化を受けて該脂肪酸の酸化物(例えば、ケトン、ア
ルデヒド等)等を生成する。The above-mentioned rice bran raw material contains a large amount of fat and oil, and when the rice bran is stored, free fatty acids are generated from the fat and oil through the enzymatic action of fat-degrading enzymes such as lipase in the rice bran raw material. The free fatty acid is oxidized by oxygen in the air to produce oxides of the fatty acid (eg, ketones, aldehydes, etc.).
したがって、上述のような遊離脂肪酸、該脂肪酸の酸化
物等を含有する米糠原料を、そのま工もしくは配合飼料
用原料に配合し、これを飼料に供した場合、当然家畜は
、下痢症状を呈するため、家畜の成長が著しく低下し、
さらには該脂肪酸の酸化物等のため、嗜好性が著しく低
下し、そのため飼料としての価値が著しく低下したもの
となる等の欠点があった。Therefore, when rice bran raw materials containing free fatty acids, oxides of fatty acids, etc. as mentioned above are added to raw or mixed feed raw materials and fed, livestock naturally exhibit diarrheal symptoms. As a result, the growth of livestock is significantly reduced,
Furthermore, due to the presence of oxides of the fatty acids, palatability is significantly lowered, resulting in a disadvantage that the value as feed is significantly lowered.
そこで本発明者等は、上記欠点を解消するため、鋭意検
討した結果、糠原料に、温度120〜300℃の過熱水
蒸気を直接接触させて、加熱加圧膨化処理すれば、糠原
料中の遊離脂肪酸および該脂肪酸の酸化物等がほとんど
飛散除去されること、また上記加熱処理後の糠を原材料
とする飼料を、家畜に供給すると、家畜を極めて効率良
く短期間に成長させることが出来ること等の知見を得て
本発明を完成した。Therefore, in order to eliminate the above-mentioned drawbacks, the present inventors have made extensive studies and found that if the bran raw material is brought into direct contact with superheated steam at a temperature of 120 to 300°C and subjected to heating and pressure swelling treatment, the free release in the bran raw material can be reduced. Most of the fatty acids and oxides of the fatty acids are removed by scattering, and feeding livestock with feed made from the bran after the heat treatment allows the livestock to grow extremely efficiently in a short period of time. The present invention was completed based on this knowledge.
すなわち本発明は、温度120〜300℃の過熱水蒸気
を糠原料に直接接触させて、加熱加圧膨化処理したもの
そのま\、またはこれに、各種増量剤、栄養剤、防腐剤
、各種微量成分等より選ばれた1種以上の飼料成分を添
加することを特徴とする飼料の製造法である。In other words, the present invention is directed to directly contacting superheated steam at a temperature of 120 to 300°C to bran raw material to heat and pressurize it, or to add various fillers, nutrients, preservatives, and various trace ingredients to this. This is a feed manufacturing method characterized by adding one or more feed ingredients selected from the following.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
先ず、本発明に使用される糠原料は、例えば米糠等が特
に好適なものとして挙げられる。First, rice bran and the like are particularly preferred as the bran raw material used in the present invention.
なお上記糠原料は、そのま〜でも良いが、必要によりこ
れを通常の粉砕機等を用いて粉砕したものに適宜な加水
を行っても良い。The above-mentioned bran raw material may be used as is, but if necessary, it may be pulverized using an ordinary pulverizer or the like and appropriate water may be added thereto.
次に、本発明における加熱加圧膨化処理を具体的に述べ
る。Next, the heating, pressurizing and swelling treatment in the present invention will be specifically described.
糠原料を、加熱加圧処理装置に投入し、圧力Okg/c
a(ゲージ圧力)を越える圧力以上、好ましくは3〜8
に9/cat(ゲージ圧力)の過熱水蒸気の存在下で、
温度120〜300°C1好ましくは120〜220℃
に5秒以上、好ましくは10〜180秒間直接接触させ
て加熱加圧したのち、加熱加圧処理装置内の圧力を、よ
り低圧下例えば、大気圧下に急激に放出して膨化核原料
を得る。The bran raw material is put into a heating and pressure treatment equipment, and the pressure is Okg/c.
Pressure exceeding a (gauge pressure) or higher, preferably 3 to 8
In the presence of superheated steam at 9/cat (gauge pressure),
Temperature: 120-300°C, preferably 120-220°C
After heating and pressurizing by directly contacting the material for 5 seconds or more, preferably 10 to 180 seconds, the pressure inside the heating and pressurizing treatment device is suddenly released to a lower pressure, for example, atmospheric pressure, to obtain a expanded core material. .
上記の如く、糖原料を加熱水蒸気の存在下で加熱加圧膨
化処理することにより、乾燥と同時に糖原料中の遊離脂
肪酸および該脂肪酸の酸化物等が飛散除去されるのであ
る。As described above, by subjecting the sugar raw material to heating, pressure and swelling treatment in the presence of heated steam, free fatty acids and oxides of the fatty acids, etc. in the sugar raw material are scattered and removed at the same time as drying.
この飛散除去は、先ず過熱水蒸気と糖原料との接触によ
って、過熱水蒸気の一部が糖原料の表面に凝縮し、その
際、凝縮潜熱を与えられた糖原料は高温となり、該糖原
料は周囲の水蒸気により、その付着凝縮水を再び蒸発し
、水蒸気蒸留が行われるようなかたちで水分と共に遊離
脂肪酸および該脂肪酸の酸化物等が飛散除去されるもの
と考えられる。In this scattering removal process, first, a portion of the superheated steam condenses on the surface of the sugar raw material due to contact between the superheated steam and the sugar raw material, and at this time, the sugar raw material that has been given latent heat of condensation becomes high temperature, and the sugar raw material is exposed to the surroundings. It is thought that the adhering condensed water is evaporated again by the water vapor, and the free fatty acids and oxides of the fatty acids are scattered and removed along with the water in a manner similar to steam distillation.
なお、本発明においては、家畜の成長に悪影響を及ぼす
成分、すなわち遊離脂肪酸もしくは該脂肪酸の酸化物等
を比較的多量に含有する糖原料を用いた場合でも、該遊
離脂肪酸もしくは該脂肪酸の酸化物含量の極めて少ない
糖原料を用いた場合と同程度に、家畜の成長に好適な飼
料を得ることが出来る。In addition, in the present invention, even when using a sugar raw material containing a relatively large amount of components that adversely affect the growth of livestock, that is, free fatty acids or oxides of the fatty acids, the free fatty acids or the oxides of the fatty acids Feed suitable for the growth of livestock can be obtained to the same extent as when using raw materials with extremely low sugar content.
また糖原料を、加熱加圧膨化処理した糖原料に、水分を
補給して糖原料中の水分が10〜20%(W/W )程
度となるように調整したのち、これに過熱水蒸気を直接
接触させれば、糖原料中の遊離脂肪酸および該脂肪酸の
酸化物等を一層効率良く飛散除去させることが出来る。In addition, the sugar raw material is heated, pressure-expanded, and then water is replenished so that the water content in the sugar raw material is about 10 to 20% (W/W). When brought into contact, free fatty acids and oxides of the fatty acids in the sugar raw material can be more efficiently scattered and removed.
なお、上記糖原料を、温度120℃未満の過熱水蒸気に
直接接触させた場合には、糖原料中の遊離脂肪酸および
該脂肪酸の酸化物等は、除去され難く、一方過熱水蒸気
の温度が極端に高い場合、例えば300℃を越える場合
には、糖原料が炭化されるので好ましくない。In addition, when the above-mentioned sugar raw material is brought into direct contact with superheated steam at a temperature of less than 120°C, free fatty acids and oxides of the fatty acids in the sugar raw material are difficult to remove. If the temperature is high, for example exceeding 300°C, the sugar raw material will be carbonized, which is not preferable.
なおまた、本発明において前記糖原料に過熱水蒸気を直
接接触させることは、極めて重要であり、例えば、プラ
スチック袋等に、上記糖原料を充填し、加熱加圧した場
合には、糖原料より、遊離脂肪酸および該脂肪酸の酸化
物等を飛散除去させることはほとんど出来ないので好ま
しくない。Furthermore, in the present invention, it is extremely important to bring superheated steam into direct contact with the sugar raw material. For example, when a plastic bag or the like is filled with the sugar raw material and heated and pressurized, the sugar raw material This is not preferable because it is hardly possible to scatter and remove free fatty acids and oxides of the fatty acids.
本発明に用いられる加熱加圧処理装置としては、如何な
る形状、構造のものでも使用可能であり、その具体的な
装置例としては、例えば、特公昭46−34747号公
報記載の気流式連続加熱膨化装置等は、特に好適である
。The heating and pressurizing treatment apparatus used in the present invention can be of any shape or structure, and specific examples include, for example, the air flow continuous heating expansion device described in Japanese Patent Publication No. 46-34747. The apparatus and the like are particularly suitable.
次に、前記加熱加圧膨化処理後の糖原料そのまま、もし
くはこれに配合飼料原料、例えば、草類、乾草類、茎葉
類、木材飼料等の繊維質飼料、根菜類、葉菜類、果菜類
、草類、サイレージ等の多汁質飼料等の増量剤;犬豆粕
、油粕、乳、魚粕、サナギ等の蛋白質飼料、穀実類、イ
ネ類等の殿粉質飼料、油質種実、大豆、油の多い油粕等
の脂肪質飼料、カルシウム類、骨粉、石灰類、リン酸カ
ルシウム、食塩、塩類混合物等の無機質飼料、草類、緑
葉類、肝油、酵母、総合ビタミン剤、乾草緑葉粉末等の
ビタミン飼料等の栄養剤;デヒドロ酢酸ナトリウム、プ
ロピオン酸カルシウム、プロピオン酸ナトリウム等の防
腐剤;サイロプロティン(Thyroprotein
) (ヨードカゼインともいわれ、人工的につくった
甲状腺ホルモン製剤である。Next, the sugar raw material after the heating and pressure swelling treatment is used as it is, or it is mixed with feed raw materials, such as grasses, hays, stems and leaves, fibrous feeds such as wood feeds, root vegetables, leafy vegetables, fruit vegetables, grasses, etc. fillers for succulent feeds such as rice, silage, etc.; protein feeds such as dog bean meal, oil cake, milk, fish meal, pupae, starch feeds such as grains and rice, oily seeds, soybeans, and oils. Fatty feed such as oil cake with a high content, mineral feed such as calcium, bone meal, lime, calcium phosphate, salt, salt mixture, etc., vitamin feed such as grass, green leaves, cod liver oil, yeast, multivitamins, hay green leaf powder, etc. nutritional supplements; preservatives such as sodium dehydroacetate, calcium propionate, and sodium propionate;
) (Also called iodocasein, it is an artificially produced thyroid hormone preparation.
)等の微量成分等より選ばれた1種以上の飼料成分を適
宜な量添加、配合して配合飼料を得る。) and other trace ingredients, etc., are added and blended in an appropriate amount to obtain a compounded feed.
本発明における家畜の具体例としては、ニワトリ、ウズ
ラ、牛、ブタ、ブリ、マダイ、コイ、ウナギ、ニジマス
、アユ等が挙げられる。Specific examples of livestock in the present invention include chicken, quail, cow, pig, yellowtail, red sea bream, carp, eel, rainbow trout, sweetfish, and the like.
本発明によれば、糖原料より家畜の成長に悪影響を及ぼ
す遊離脂肪酸、該脂肪酸の酸化物等が著しく除去された
、家畜の成長を著しく促進することの出来る飼料を得る
ことが出来る。According to the present invention, it is possible to obtain a feed that can significantly promote the growth of livestock, in which free fatty acids, oxidized products of the fatty acids, and the like that adversely affect the growth of livestock are significantly removed from sugar raw materials.
以下に、実施例を挙げて本発明をさらに具体的に説明す
る。The present invention will be explained in more detail below by giving examples.
実施例
米糠〔水分含量;10.2%(W/W ) 、13kg
を回分式多孔板取付型加熱処理装置に投入し、該装置に
装着された多孔板の底部より、温度165℃で3kg/
crrt(ゲージ圧力)の過熱水蒸気を導入し、3分間
該過熱水蒸気を米糠に直接接触させたのち、該装置に装
着された排出弁を瞬間的に開放して装置内の圧力を大気
圧送急激に低下させて膨化米糠を得た(本発明)。Example rice bran [moisture content: 10.2% (W/W), 13kg
was put into a batch-type perforated plate-mounted heat treatment device, and 3 kg/kg was added at a temperature of 165°C from the bottom of the perforated plate attached to the device.
After introducing superheated steam at crrt (gauge pressure) and allowing the superheated steam to come into direct contact with the rice bran for 3 minutes, the discharge valve attached to the device was opened momentarily and the pressure inside the device was rapidly pumped to atmospheric pressure. to obtain puffed rice bran (the present invention).
なお、対照は、上述した加熱処理を全く施さないもので
ある。Note that, as a control, the above-mentioned heat treatment was not performed at all.
上記操作により得た夫々の米糠の水分(実験農芸化学、
上巻、P、114、昭和46年2月5日発行、第15版
)、ニコチン酸〔小原他著、「食品分析ハンドブック」
、317〜318頁、建帛社、昭和44年9月1日発行
(初版)〕、ニコチン酸無水物基準値および酸価値(実
験農芸化学、下巻、P・458、昭和46年4月15日
発行、第11版)について夫々測定した結果を下表に示
す。The moisture content of each rice bran obtained by the above procedure (Experimental Agricultural Chemistry,
Volume 1, P. 114, February 5, 1970, 15th edition), Nicotinic acid [Ohara et al., "Food Analysis Handbook"
, pp. 317-318, Kenpakusha, published September 1, 1970 (first edition)], Nicotinic acid anhydride standard value and acid value (Jikken Agricultural Chemistry, Volume 2, P. 458, published April 15, 1970) , 11th edition) are shown in the table below.
なお、酸価値については、上記処理後の米糠をさらに夫
々ポリエチレン袋に充填して、温度25〜30℃に保持
した室内で30日間保存したものについて測定した結果
を下表に示す。The table below shows the acid value of the rice bran after the above treatment, which was further filled into a polyethylene bag and stored for 30 days indoors at a temperature of 25 to 30°C.
上表より明らかなように、本発明は、対照に比し、遊離
脂肪酸、該脂肪酸の酸化物、水分等が著しく除去され、
しかも、保存性が著しく優れたものであり、さらに本発
明処理により、米糠中のニコチン酸は、何等減少せず、
安定であることがわかる。As is clear from the above table, the present invention significantly removes free fatty acids, oxides of fatty acids, water, etc. compared to the control.
In addition, the storage stability is extremely excellent, and the treatment of the present invention does not reduce nicotinic acid in rice bran at all.
It can be seen that it is stable.
このようにして得た本発明、対照および通常の脱脂米糠
を用いて、下表組成の養鶏用ブロイラー飼料および産卵
鶏飼料を夫々調製した。Using the thus obtained defatted rice bran of the present invention, the control, and the conventional defatted rice bran, broiler feed for poultry farming and feed for laying hens having the compositions shown below were prepared, respectively.
次いで、このようにして得た配合飼料を夫々温度25〜
30℃に保持した室内で90日間保存したのち、ブロイ
ラー飼育試験および産卵鶏飼育試験に供した。Next, the compounded feed obtained in this way was heated to a temperature of 25 to 25°C.
After being stored indoors at 30°C for 90 days, it was subjected to a broiler breeding test and an egg-laying chicken breeding test.
すなわち、ブロイラー飼育試験は、ブロイラーの初雛を
入荷したのち、3週間経過したものを、20羽単位で3
週間経時的に飼育比較給飼を行なったものであり、また
、産卵鶏飼育試験は、産卵鶏の中雛期のものを、20羽
単位で5週間経時的に飼育比較給飼を行なったものであ
る。In other words, in the broiler rearing test, the first broiler chicks were brought in, and 3 weeks after they arrived, broiler chicks were raised in groups of 20.
In addition, in the breeding test of laying hens, middle-chicken laying hens were reared and comparatively fed over a period of 5 weeks in units of 20 chickens. It is.
そして、得られた結果を、夫々下表に示す。The results obtained are shown in the table below.
上表より明らかな如く、本発明は、対照および脱脂米糠
を使用した配合飼料に比し、体重増加量の点で著しく優
れていることが判明した。As is clear from the above table, the present invention was found to be significantly superior in terms of weight gain compared to the control and the compound feed using defatted rice bran.
上表より明らかな如(、本発明は、対照および脱−脂米
糠を使用した配合飼料に比し、体重増加量の点で優れて
いることが判明した。As is clear from the above table, the present invention was found to be superior to the control and the compound feed using defatted rice bran in terms of weight gain.
Claims (1)
接接触させて、加熱加圧膨化処理したものそのまま、ま
たはこれに、各種増量剤、栄養剤、防腐剤、各種微量成
分等より選ばれた1種以上の飼料成分を添加することを
特徴とする飼料の製造法。1. Direct contact with superheated steam at a temperature of 120 to 300°C to the bran raw material to heat and pressurize it, as it is, or as it is, with various fillers, nutrients, preservatives, various trace ingredients, etc. selected. A method for producing feed, characterized by adding one or more feed ingredients.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57150790A JPS5834101B2 (en) | 1982-09-01 | 1982-09-01 | Feed manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57150790A JPS5834101B2 (en) | 1982-09-01 | 1982-09-01 | Feed manufacturing method |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP53122051A Division JPS5832951B2 (en) | 1978-10-05 | 1978-10-05 | Feed manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5847441A JPS5847441A (en) | 1983-03-19 |
JPS5834101B2 true JPS5834101B2 (en) | 1983-07-25 |
Family
ID=15504484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57150790A Expired JPS5834101B2 (en) | 1982-09-01 | 1982-09-01 | Feed manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5834101B2 (en) |
-
1982
- 1982-09-01 JP JP57150790A patent/JPS5834101B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5847441A (en) | 1983-03-19 |
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