JPS5886044A - Preparation of feed - Google Patents
Preparation of feedInfo
- Publication number
- JPS5886044A JPS5886044A JP18314081A JP18314081A JPS5886044A JP S5886044 A JPS5886044 A JP S5886044A JP 18314081 A JP18314081 A JP 18314081A JP 18314081 A JP18314081 A JP 18314081A JP S5886044 A JPS5886044 A JP S5886044A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- liquid
- joint
- solid raw
- solid
- 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
Abstract
Description
【発明の詳細な説明】
液体原料を添加する飼料の従来の製造方法は、数多くの
異種原料を製品の成分割合になるように計量機で５１葉
し、これをバッチミキサーで混合し、その後連続ミキサ
ーにて液体を添加していた。この方法では、例えば圧扁
飼料のようにこわれ易い原料と混合すると、下記のフレ
ークメーズ破砕率表から分かる通り、原料中の粉の量が
１７６％であったものが２７・１％となり、１１．９％
の粉化率となる。同質の原粒につき本発明方法を適応し
た場合は２３１％しかならず、粉化率は６．７％となり
、粉化の少ない製品が得られる。DETAILED DESCRIPTION OF THE INVENTION The conventional method for producing feed by adding liquid raw materials is to weigh a large number of different raw materials using a weighing machine to match the proportions of the product, mix them using a batch mixer, and then continuously Liquid was added using a mixer. In this method, when mixed with a fragile raw material such as compressed feed, the amount of powder in the raw material goes from 176% to 27.1%, as seen from the flake maize crushing rate table below, and 11%. .9%
The powderization rate will be . When the method of the present invention is applied to homogeneous raw grains, the powdering rate is only 231%, and the powdering rate is 6.7%, and a product with less powdering can be obtained.
フレークノーズ破砕率実験値 ※タテ型混合機は回転数２０Ｏｒｐｍでテストした。Flake nose crushing rate experimental value *The vertical mixer was tested at a rotation speed of 20 rpm.
篩仕様
５メツンユＳＷＧす１８
目開き ３８８ｍｍ
即ち本発明はホッパーの扁平開口を揺動又は回転させな
がら固体原料をこの扁平開口から下方へ流下させ、該流
下通路の外側にあってこの開口と共に移動する液体添加
用のノズルにより液体原料をこの固体原料に添加し同一
機械にて混合することを特徴とする飼料の製造方法にが
がる。Sieve specifications: 5 mesh SWG 18 mesh opening: 388 mm In other words, in the present invention, the flat opening of the hopper is swung or rotated, and the solid raw material is allowed to flow downward from this flat opening, and is located outside of the flow passage and moves with this opening. The present invention relates to a method for producing feed, which is characterized in that a liquid raw material is added to the solid raw material using a liquid addition nozzle and mixed in the same machine.
以下に本発明実施の態様を図面につき詳述すれば次の通
シである。DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be explained in detail below with reference to the drawings.
１に内管固定で外管回転型の二浣体用スイベルジヨイン
ト、２はこのジヨイントＬの内管、３は外管で回転軸４
に固定される。この回転軸は動力＃５より伝導装置６を
介して回転し、連結棒７を通じホッパ−８全回転させる
。このホッパーに下端に扁平開口９會有する。又回転軸
４ｖｃ内管回転型の二流体用スイベルジヨイント１０を
付けて、ジヨイントｌより供給された二流体會回転ホッ
パー８と同−運動會させながら取り出すことができるよ
うにしである。１１は扁平開口９のまわりにこれと一緒
に移動できるようＶＣ配置された二流体用自！１１ｈ添
加ノズルで、春ｉ曇恭≠第４図では説明の都合で水平に
配置しであるが、実際は第１図のように傾けておく。こ
のノズル１ｔｖｃ対しては、供給口Ａより添加用ｙｒｔ
体を供給し、供給口Ｂへ添加用空気全供給し、供給ロａ
ＶＣコントロール用空気を入社る。供給口ＣにＬｌ二？
かけると図示してないがパルプ類が作動し、供和口Ａか
ら送られた液体全開口９から帯状に浣下する原料ｖｃ添
加し、供給口Ｃの子方ｔさげると供給口Ａからの液体金
製１０と同一能力を持つジヨイントで、運動する液体全
外部に取出すと共にコントロール用空気全供給する。１
４はジョイン）１３Ｖｃ連結さｎた液体の出口、１５Ｈ
コントロール用空気の入り口である。Ｌ 、６ Ｈ回転
ホッパー８の原料を送る供給部である。１７はこの混合
機のケーシングで、内部に４室に仕切られ、それぞれに
排出口１８がらる。1 is a swivel joint for two rods with a fixed inner tube and a rotating outer tube, 2 is an inner tube of this joint L, and 3 is an outer tube with a rotating shaft 4.
Fixed. This rotating shaft is rotated by power #5 via a transmission device 6, and the hopper 8 is rotated completely through a connecting rod 7. This hopper has 9 flat openings at its lower end. In addition, a two-fluid swivel joint 10 with a rotary shaft 4vc and an inner tube rotating type is attached so that the two-fluid rotary hopper 8 supplied from the joint 1 can be taken out while moving in the same manner. 11 is a two-fluid valve with a VC arranged around the flat opening 9 so that it can move with it! The 11h addition nozzle is arranged horizontally in Figure 4 for convenience of explanation, but in reality it is tilted as shown in Figure 1. For this nozzle 1tvc, add yrt from supply port A.
supply the body, supply all the air for addition to the supply port B, and then
Joined VC Control Air. Ll2 in supply port C?
When it is turned on, the pulp is activated (not shown), and the raw material vc is added to the liquid fed from the feed port A, which is drawn down in a strip from the full opening 9. When the lower side of the feed port C is lowered, the pulp is fed from the feed port A. This joint has the same ability as the liquid gold 10, and it takes out all of the moving liquid to the outside and also supplies all of the air for control. 1
4 is joint) 13Vc connected liquid outlet, 15H
This is the control air entrance. L, 6H This is a supply section for feeding raw materials to the rotating hopper 8. Reference numeral 17 denotes a casing of this mixer, which is internally partitioned into four chambers, each of which has a discharge port 18.
１９は液体出口１４に設けたパルプである。 ・粘
性の高い液体ｔ−添加する時、例えば屯°υ℃に加温さ
れた糖蜜等が配管等により冷却され粘性が変化するの全
防止するため、ジョイン）１Ｂよジ入ンクへもどし、装
置全体が一定温度を保つようにしておく。供給部１６よ
り原料を入れた時、パルプ１９を絢めることによジ液体
に圧力をかけ、同時にジヨイント１，１０を介し＃ｑ気
を、またジヨイント】０及び取出し部１２を介し吹付※
晰僚米用の空気をそれぞれ入れると、添加される。原料
は供給部１６、ホッパー８を介し扁平開口９より帯状を
なして流下しながら回転もし、しかもこの間液体を添加
されながら、ケーシング１７の底部より層状に堆積する
。これを排出口をある時間をおきランダムに排出すると
、層状に堆積した原料は竪方向に落下し、配合がなされ
る。19 is a pulp provided at the liquid outlet 14.・When adding a highly viscous liquid, for example, to completely prevent molasses, etc. that have been heated to 1°υ°C from being cooled by piping etc., the viscosity changes. Make sure to maintain a constant temperature throughout. When the raw material is introduced from the supply section 16, pressure is applied to the liquid by tightening the pulp 19, and at the same time, #q air is sprayed through the joints 1 and 10, and also through the joint 0 and the take-out section 12*
If you add air for each rice, it will be added. The raw material rotates while flowing down from the flat opening 9 in a belt shape through the supply section 16 and hopper 8, and is deposited in layers from the bottom of the casing 17 while being added with liquid during this time. When this is randomly discharged from the discharge port after a certain period of time, the raw materials deposited in layers fall vertically and are blended.
本発明によれば固体原料を帯状にしかも回転させながら
流下させ、その回転と共に移動するノズルにより液体原
料をこの固体原料に添加するようにし層状に堆積した後
竪方向に落下させて配合するようにしたので、固体原料
を攪拌しながら流体原料を添加するやり方に比べ固体原
料の粉化率を低く抑えるてとができる特徴がある。According to the present invention, a solid raw material is made to flow down in the form of a belt while rotating, and a liquid raw material is added to the solid raw material by a nozzle that moves with the rotation, so that the liquid raw material is deposited in a layer and then dropped in a vertical direction for blending. Therefore, compared to a method in which a fluid raw material is added while stirring a solid raw material, the pulverization rate of the solid raw material can be kept low.
第１図は本発明方法の実施に際し使用される装置の一例
を示す一部切断概略正面図、第２図は同側面図、第３図
は一部の部分切欠拡大正面図、第４図はノズル部分の説
明図である。
８・・−ホッパー、９・・・扁平開口、１１・・・ノズ
ル。
特許出願人 全国農業協同組合連合会同 株式
会社 尾上機械
第１図
第３図
２０９−
第４図
ＣFIG. 1 is a partially cutaway schematic front view showing an example of the apparatus used in carrying out the method of the present invention, FIG. 2 is a side view of the same, FIG. 3 is a partially cutaway enlarged front view, and FIG. It is an explanatory view of a nozzle part. 8...-hopper, 9... flat opening, 11... nozzle. Patent applicant: National Federation of Agricultural Cooperatives Co., Ltd. Onoe Kikai Co., Ltd. Figure 1 Figure 3 209- Figure 4 C
Claims (1)
させながら固体原料をこの扁平間［］から１丁へ流）−
させ、該流下通路の外側にあってこの開口と共に移動す
る液体添加用のノズルにより液体原料をこの固体原料に
添加し混合も同一機械で行うことを特徴とする飼料の製
造方法。While rocking or rotating the flat opening at the lower end of the raw material supply port inside the mixer, the solid raw material flows from this flat space [] to one pipe).
A method for producing feed, characterized in that the liquid raw material is added to the solid raw material by a liquid addition nozzle that is located outside the flow passage and moves together with the opening, and mixing is also performed in the same machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18314081A JPS5886044A (en) | 1981-11-17 | 1981-11-17 | Preparation of feed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18314081A JPS5886044A (en) | 1981-11-17 | 1981-11-17 | Preparation of feed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5886044A true JPS5886044A (en) | 1983-05-23 |
Family
ID=16130495
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18314081A Pending JPS5886044A (en) | 1981-11-17 | 1981-11-17 | Preparation of feed |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5886044A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100763764B1 (en) | 2007-06-18 | 2007-10-04 | 남기욱 | A liquid material accretive system for formula feed |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS507575B1 (en) * | 1969-08-04 | 1975-03-27 | ||
| JPS5244451A (en) * | 1975-10-04 | 1977-04-07 | Ig Tech Res Inc | Process and aparatus for mixing a fluid and a particulate |
-
1981
- 1981-11-17 JP JP18314081A patent/JPS5886044A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS507575B1 (en) * | 1969-08-04 | 1975-03-27 | ||
| JPS5244451A (en) * | 1975-10-04 | 1977-04-07 | Ig Tech Res Inc | Process and aparatus for mixing a fluid and a particulate |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100763764B1 (en) | 2007-06-18 | 2007-10-04 | 남기욱 | A liquid material accretive system for formula feed |
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