JPS5933015B2 - Particulate matter mixing and discharging device - Google Patents
Particulate matter mixing and discharging deviceInfo
- Publication number
- JPS5933015B2 JPS5933015B2 JP54084916A JP8491679A JPS5933015B2 JP S5933015 B2 JPS5933015 B2 JP S5933015B2 JP 54084916 A JP54084916 A JP 54084916A JP 8491679 A JP8491679 A JP 8491679A JP S5933015 B2 JPS5933015 B2 JP S5933015B2
- Authority
- JP
- Japan
- Prior art keywords
- bellows
- hollow cylindrical
- cylindrical body
- diameter
- shaped
- 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
- 239000013618 particulate matter Substances 0.000 title claims description 12
- 238000007599 discharging Methods 0.000 title claims description 4
- 239000008187 granular material Substances 0.000 claims description 20
- 235000013339 cereals Nutrition 0.000 description 9
- 241000209094 Oryza Species 0.000 description 4
- 235000007164 Oryza sativa Nutrition 0.000 description 4
- 235000009566 rice Nutrition 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/80—Falling particle mixers, e.g. with repeated agitation along a vertical axis
- B01F25/82—Falling particle mixers, e.g. with repeated agitation along a vertical axis uniting flows of material taken from different parts of a receptacle or from a set of different receptacles
- B01F25/821—Falling particle mixers, e.g. with repeated agitation along a vertical axis uniting flows of material taken from different parts of a receptacle or from a set of different receptacles by means of conduits having inlet openings at different levels
- B01F25/8211—Falling particle mixers, e.g. with repeated agitation along a vertical axis uniting flows of material taken from different parts of a receptacle or from a set of different receptacles by means of conduits having inlet openings at different levels by means of a central conduit or central set of conduits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/116—Stirrers shaped as cylinders, balls or rollers
- B01F27/1161—Stirrers shaped as cylinders, balls or rollers having holes in the surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
- B01F31/44—Mixers with shaking, oscillating, or vibrating mechanisms with stirrers performing an oscillatory, vibratory or shaking movement
- B01F31/441—Mixers with shaking, oscillating, or vibrating mechanisms with stirrers performing an oscillatory, vibratory or shaking movement performing a rectilinear reciprocating movement
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
- Accessories For Mixers (AREA)
Description
【発明の詳細な説明】
この発明は、品質、粒径等にばらつきのある粒状物をホ
ッパー乃至は容器より吐出させるとき、吐出粒状物を一
様に混合させる混合排出装置に係るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a mixing and discharging device that uniformly mixes the discharged granules when they are discharged from a hopper or a container with variations in quality, particle size, etc.
従来、米、麦などの穀類を貯蔵若くは計量容器などから
他の容器に入れ替え乃至は包装袋などに充填する場合に
比重の軽いものや、粒径の大きいものはどうしてもホッ
パー内で上位に残る傾向にあり、受け容器や包装袋によ
つては著しく品質の分布が異なることが起る。Conventionally, when storing grains such as rice or wheat, transferring them from a measuring container to another container, or filling them into a packaging bag, grains with light specific gravity or grains with large grain sizes inevitably remain at the top in the hopper. There is a tendency for quality distribution to vary significantly depending on the receiving container or packaging bag.
また、家畜などの混合飼料のように、大きさの異なる穀
類や、顆粒物を混合する場合は、この傾向が更に顕著と
なる。Furthermore, this tendency becomes even more pronounced when grains or granules of different sizes are mixed, such as mixed feed for livestock.
この発明はこのような欠点を改善するためのもので、仮
令若干粒径の違いや、比重の差のある粒状物（混合飼料
、二種以上の米の混合物）であつても、吐出時の場所や
、時間的な前後において、混合粒状物の混合分布に著し
い斑が生じないようにするためのものである。This invention is intended to improve these drawbacks, and even if the particles have slightly different particle sizes or specific gravity (mixed feed, mixture of two or more types of rice), This is to prevent significant unevenness from occurring in the mixed distribution of mixed particulate matter depending on location or time.
この発明はホッパー乃至容器の下部を蛇腹形状とし、下
端の開ロロ径は、前記蛇腹形状部の細径部の径よりも更
に径が細くしてあり、この開口には上端が閉塞してあり
、下端が開放されて吐出口となつている中空円筒体が移
動自在に嵌挿してあり、かつこの中空円筒体は移動駆動
源と連動機構を介して連設してあり、該中空円筒体の上
端は前記蛇腹形状の上部にまで達しており、前記中空円
筒体の円筒壁及び前記蛇腹形状部のうち下位ほど径の細
くなつているホッパー状テーパ部には粒状物吐出孔がそ
れぞれ多数分布して穿設してあり、蛇腹形状部の外側に
はこの蛇腹形状部の太径部よりも内径の大きい外部吐出
案内筒が設けてあることを特徴とする粒状物混合排出装
置である。In this invention, the lower part of the hopper or container is shaped like a bellows, and the opening diameter of the lower end is smaller than the diameter of the small diameter part of the bellows-shaped part, and this opening is closed at the top end. , a hollow cylindrical body whose lower end is open and serves as a discharge port is movably inserted into the hollow cylindrical body, and this hollow cylindrical body is connected to a moving drive source via an interlocking mechanism, and the hollow cylindrical body is The upper end reaches the top of the bellows shape, and a large number of particulate discharge holes are distributed in the cylindrical wall of the hollow cylindrical body and in the hopper-like tapered portion of the bellows shape portion, the diameter of which becomes narrower toward the bottom. This particulate mixing and discharging device is characterized in that an external discharge guide cylinder is provided on the outside of the bellows-shaped portion and has an inner diameter larger than the large diameter portion of the bellows-shaped portion.
今この発明を図示の代表的な実施態様に基づいて説明す
る。第１実施態様
第１図に示すものであつて、１０はホッパー乃至容器（
以下単に容器と言う）の下部であつて、垂直軸線をもつ
蛇腹形をなした蛇腹形状部１１が連設してあり、この最
下端の開口１２の径は、前記蛇腹形状部１１の最細径部
１３よりも更に細径にしてある。The invention will now be described on the basis of exemplary embodiments shown in the drawings. The first embodiment is shown in FIG. 1, and 10 is a hopper or a container (
At the bottom of the bellows-shaped portion (hereinafter simply referred to as a container), a bellows-shaped portion 11 having a vertical axis is arranged in series, and the diameter of the opening 12 at the lowest end is the narrowest of the bellows-shaped portion 11. It has a smaller diameter than the diameter portion 13.
この開口１２には上端が閉塞され、下端が開放されて主
吐出口１４としてある中空円筒体１５が回転自在に嵌挿
してあり、この上端部には、この中空円筒体１５を軸線
の周りに自転させる為の伝動手段たる軸１６が軸線上に
結合して、軸１６の上端は容器１０の土部外にまで伸び
、この部分に駆動用モータ１７が直結又は適宜の減速装
置を介して連結してある。A hollow cylindrical body 15 whose upper end is closed and whose lower end is open as the main discharge port 14 is rotatably fitted into this opening 12. A shaft 16 serving as a transmission means for rotation is connected on the axis, and the upper end of the shaft 16 extends to the outside of the soil of the container 10, and a drive motor 17 is connected to this part directly or through an appropriate speed reduction device. It has been done.
前述の中空円筒体１５の周壁には、粒状物吐出孔１８が
多数分布して穿設してある。A large number of granule discharge holes 18 are formed in a distributed manner in the peripheral wall of the hollow cylindrical body 15 described above.
これら粒状物吐出孔１８の径は、これに使用する粒状物
の径の少なくとも５倍程の大きさがよい。１９は前述の
蛇腹形状部１１のうち、下部ほど径が細くなつているホ
ツパ一状テーパー部でありこの部分には、これまた前述
の粒状物吐出孔１８と同様の粒状物吐出孔２０が多数分
布して設けてある。The diameter of these particulate matter discharge holes 18 is preferably at least five times the diameter of the particulate matter used therein. Reference numeral 19 denotes a hopper-like tapered portion of the bellows-shaped portion 11 whose diameter becomes narrower toward the bottom, and this portion also has a large number of granule discharge holes 20 similar to the granule discharge holes 18 described above. They are distributed and provided.
２１は蛇腹形状部１１の外側には、この蛇腹形状部１１
の太径部よりも内径の大きい外部吐出案内筒２１が設け
てあり、この外部吐出案内筒２１は、蛇腹形状部１１の
粒状物吐出孔２０より吐出した粒状物が飛散しないよう
にする為のものでこの吐出案内筒２１のドーナツ型の下
端は開放されて副吐出口２４となつている。21 is a bellows-shaped portion 11 on the outside of the bellows-shaped portion 11.
An external discharge guide cylinder 21 having an inner diameter larger than the large diameter part of the bellows-shaped part 11 is provided. The lower end of the donut-shaped discharge guide tube 21 is opened to form a sub-discharge port 24.
叙上のように構成しているこの考案のものにおいて、例
えば産地の異なる穀類、或は等級の異なる穀類二種以上
を容器など１０の中に投入し、その滞積量が、中空円筒
体１５の上端よりも上位になるまで入れる。In this device constructed as described above, for example, two or more types of grains from different production areas or different grades are put into a container 10, and the accumulated amount is Insert until it is above the top of the .
このように粒状物たる穀類の一部は穀類吐出孔１８及び
２０より一部はこぼれるが、通常は、粒状物の圧力によ
つて吐出孔１８，２０の径の大きさが粒状物の最大径の
３倍乃至１０倍程度までの大きさにおいては殆んど吐出
孔１８，２０から粒状物はこぼれることがない。次にモ
ータ１７によつて軸１６及び中空円筒体１５をその軸線
の周りに回転させると、中空円筒体１５の周面と接する
粒状物の摩擦が切れ、粒状物は、各々の吐出孔１８，２
０から、中空円筒体１５及び外部吐出案内筒２１中へ落
下し、主吐出口１４及び副吐出口２４より下方に吐出さ
れる。またこれに伴つて、蛇腹形状部１１中の穀類全体
が下方に移動し、この移動及び振動によつて各吐出孔２
０からも粒状物が吐出される。この中空円筒体１５の回
転速度は、その周速度が３乃至５０（７１Ｌ／Ｓｅｃ程
度に調整できるようにしてあり、この速度の範囲内にお
いては回転速度が速い程粒状物の吐出量は増加する。In this way, some of the grains as granules spill out from the grain discharge holes 18 and 20, but normally the diameters of the discharge holes 18 and 20 are adjusted to the maximum diameter of the granules due to the pressure of the granules. Particulate matter hardly spills out from the discharge holes 18 and 20 when the size is about 3 to 10 times that of the above. Next, when the shaft 16 and the hollow cylindrical body 15 are rotated around their axes by the motor 17, the friction of the granules in contact with the circumferential surface of the hollow cylindrical body 15 is broken, and the granules are transferred to the respective discharge holes 18, 2
0, it falls into the hollow cylindrical body 15 and the external discharge guide cylinder 21, and is discharged downward from the main discharge port 14 and the sub-discharge port 24. Along with this, the entire grain in the bellows-shaped portion 11 moves downward, and this movement and vibration causes each discharge hole 2
Particulate matter is also discharged from 0. The rotational speed of the hollow cylinder 15 is adjustable from 3 to 50 (about 71L/Sec), and within this speed range, the faster the rotational speed, the greater the amount of granular material discharged. .
粒状物が米である場合は中空円筒体１５の回転が余りに
速いと肌づれを起し、米の品質を低下させることもある
ので、肌づれを起さない程度の回転速度とする。When the granules are rice, if the rotation of the hollow cylindrical body 15 is too fast, it may cause chafing and reduce the quality of the rice, so the rotation speed is set to a level that does not cause chafing.
前述のように中空円筒体１５を回転させて、各孔１８，
２０から吐出する粒状物の流出量は、容器など１０の流
入量と釣り合うようにし、おｋむね粒状物が中空円筒体
１５の上端よりも更に上部にまで滞積するようにして運
転するのがよい。By rotating the hollow cylindrical body 15 as described above, each hole 18,
The amount of particulate matter discharged from the container 20 is balanced with the amount of inflow from the container 10, and the operation is performed so that the particulate matter generally accumulates above the upper end of the hollow cylindrical body 15. good.
第２実施態様第２図に示すものであつて、第１実施態様
と同一符号のところは之と同一の構成部分であつて、同
一の作用及び効果を奏する。The second embodiment is shown in FIG. 2, and the same reference numerals as in the first embodiment represent the same constituent parts and have the same functions and effects.
異なるところは、中空円筒体１５がその軸線の周りに自
転するものではなく、上下方向に往復運動するものであ
つて、例えば偏心輪２２などで代表される往復運動機構
と連設してある。この往復の振幅は１０ｍｕ以内であつ
て、速度も３０乃至１２００！ＲＬ／Ｍｉｎ程度として
ある。往復運動手段としては、上述の外、電磁式なもの
、空気圧式のもの、その他、これらと機械的なものとを
組合せたものでもよく、特に限定はない。この第２実施
態様においては、中空円筒体１５を上下移動させて、こ
れと粒状物の摩擦を切り、中空円筒体１５の吐出孔１８
より粒状物を吐出させ、粒状物の降下移動に伴つて蛇腹
形状部１１の吐出孔２０よりも粒状物を吐出させる。The difference is that the hollow cylindrical body 15 does not rotate about its axis, but reciprocates in the vertical direction, and is connected to a reciprocating mechanism represented by, for example, an eccentric ring 22. The amplitude of this round trip is within 10 mu, and the speed is between 30 and 1200! It is approximately RL/Min. In addition to the above-mentioned reciprocating means, the reciprocating means may be an electromagnetic type, a pneumatic type, or a combination of these and mechanical types, and is not particularly limited. In this second embodiment, the hollow cylindrical body 15 is moved up and down to reduce friction between the hollow cylindrical body 15 and the granules, and the discharge hole 18 of the hollow cylindrical body 15 is
The granular material is discharged from the discharge hole 20 of the bellows-shaped portion 11 as the granular material moves downward.
このようにこの発明の装置においては前述のような構成
及び作用を為すから、蛇腹形状部１１及び中空円筒部１
５の上端部まで滞積した粒状物は、中空円筒体１５及び
蛇腹形状部１１の上下及び全円周に分布する多数の吐出
孔１８，２０より、落下吐出するから、この容器など１
０の中で粒状物の質が上下の何れか、若くは左又は右な
どに偏在していたとしても、吐出孔１８，２０は前述の
ように広く分布しているために、この装置より吐出する
粒状物は、吐出時に混合され、ぼＫ均一化される効果を
有する。Since the device of the present invention has the above-described structure and operation, the bellows-shaped portion 11 and the hollow cylindrical portion 1
The particulate matter that has accumulated up to the upper end of the container 1 falls and is discharged from a large number of discharge holes 18 and 20 distributed above and below and around the entire circumference of the hollow cylindrical body 15 and the bellows-shaped part 11.
Even if the quality of the particulate matter is unevenly distributed either above or below, or on the left or right, the discharge holes 18 and 20 are widely distributed as described above, so it is difficult to discharge from this device. The granules are mixed during discharge and have the effect of being almost uniform.
殊に蛇腹形状部１１を前述のような寸法に設けた事によ
つて蛇腹形状部１１の内周面及び中空円筒体１５外周面
に過圧力がかＸらず、各吐出孔１８，１９よりの粒状物
の吐出が容易であり、しかも吐出口１８，１９の総面積
が大きいから、単位時間当りの吐出量の最大値は相当に
大きくでき、多量の粒状物を短時間に混合吐出すること
ができる。その他構造が簡単で故障を起すおそれもない
。In particular, by providing the bellows-shaped portion 11 with the dimensions described above, no overpressure is generated on the inner circumferential surface of the bellows-shaped portion 11 and the outer circumferential surface of the hollow cylindrical body 15. Since it is easy to discharge granular materials and the total area of the discharge ports 18 and 19 is large, the maximum value of the discharge amount per unit time can be considerably large, and a large amount of granular materials can be mixed and discharged in a short time. Can be done. In addition, the structure is simple and there is no risk of failure.
尚図示の如く吐出案内筒２１の下端全面を開閉するゲー
ト２３を設けておくと、運転停止時に粒状物がこぼれる
のを防ぐことができる。この装置は、容器など１０であ
れば特に限定はなく、例えば秤量器に取付けた粒状物を
入れるための容器であつても、貯蔵タンク、混合器のホ
ツパ一であつてもこの発明としては同一である。その他
、吐出孔１８，２０の形状も円形、楕円形、長孔など、
特に限定はない。By providing a gate 23 that opens and closes the entire lower end of the discharge guide cylinder 21 as shown in the figure, it is possible to prevent particulate matter from spilling when the operation is stopped. This device is not particularly limited as long as it is a container or the like; for example, even if it is a container for storing granular materials attached to a weighing device, a storage tank, or a hopper of a mixer, the present invention is the same. It is. In addition, the shape of the discharge holes 18 and 20 may also be circular, oval, elongated, etc.
There are no particular limitations.
追加の関係
特許第１１９８０１５号（特公昭５８−３０２１４号公
報）の構成要件の主要部を含み、更に、これに新しい構
成要件を附加したものである。It includes the main components of the additional related patent No. 1198015 (Japanese Patent Publication No. 58-30214), and furthermore, new components are added thereto.
図はこの発明の代表的な実施態様を示すものでおつて、
第１図は第１実施態様の縦断正面図、第２図は第２実施
態様の縦断正面図である。
図中、符号、１０・・・・・・容器、１１・・・・・・
蛇腹形状部、１２・・・・・・開口、１３・・・・・・
最細径部、１４・・・・・・主吐出口、１５・・・・・
・中空円筒体、１６・・・・・・軸、１７・・・・・・
モータ、１８・・・・・・吐出孔、２１・・・・・・外
部吐出案内筒。The figure shows a typical embodiment of this invention.
FIG. 1 is a longitudinal sectional front view of the first embodiment, and FIG. 2 is a longitudinal sectional front view of the second embodiment. In the figure, code: 10...container, 11...
Bellows-shaped portion, 12...Opening, 13...
Smallest diameter part, 14... Main discharge port, 15...
・Hollow cylindrical body, 16...shaft, 17...
Motor, 18...Discharge hole, 21...External discharge guide tube.
Claims (1)
口口径は、前記蛇腹形状部の細径部の径よりも更に径が
細くしてあり、この開口には上端が閉塞してあり、下端
が開放されて吐出口となつている中空円筒体が移動自在
に嵌挿してあり、かつこの中空円筒体は移動駆動源と連
動機構を介して連設してあり、該中空円筒体の上端は前
記蛇腹形状の上部にまで達しており、前記中空円筒体の
円筒壁及び前記蛇腹形状部のうち下位ほど径の細くなつ
ているホッパー状テーパ部には粒状物吐出孔がそれぞれ
多数分布して穿設してあり、蛇腹形状部の外側には蛇腹
形状部の太径部よりも内径の大きい外部吐出案内筒が設
けてあることを特徴とする粒状物混合排出装置。1 The lower part of the hopper or container is bellows-shaped, and the diameter of the opening at the lower end is smaller than the diameter of the small diameter part of the bellows-shaped part, and this opening is closed at the upper end and closed at the lower end. A hollow cylindrical body which is open and serves as a discharge port is movably inserted into the hollow cylindrical body, and this hollow cylindrical body is connected to a moving drive source via an interlocking mechanism, and the upper end of the hollow cylindrical body is connected to the movable drive source through an interlocking mechanism. The cylindrical wall of the hollow cylindrical body and the hopper-like tapered portion of the bellows-shaped portion, which reaches the top of the bellows-shaped portion and has a diameter that becomes narrower toward the bottom, are each provided with a large number of granule discharge holes distributed therein. A particulate matter mixing and discharging device characterized in that an external discharge guide tube having an inner diameter larger than a large diameter part of the bellows-shaped part is provided on the outside of the bellows-shaped part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54084916A JPS5933015B2 (en) | 1979-07-06 | 1979-07-06 | Particulate matter mixing and discharging device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54084916A JPS5933015B2 (en) | 1979-07-06 | 1979-07-06 | Particulate matter mixing and discharging device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5610326A JPS5610326A (en) | 1981-02-02 |
| JPS5933015B2 true JPS5933015B2 (en) | 1984-08-13 |
Family
ID=13844035
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP54084916A Expired JPS5933015B2 (en) | 1979-07-06 | 1979-07-06 | Particulate matter mixing and discharging device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5933015B2 (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62258730A (en) * | 1986-05-01 | 1987-11-11 | Reika Kogyo Kk | Stationary type powdery mixer |
| RU2496565C2 (en) * | 2012-02-14 | 2013-10-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2496564C2 (en) * | 2012-02-14 | 2013-10-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2494802C1 (en) * | 2012-02-14 | 2013-10-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2494796C1 (en) * | 2012-02-14 | 2013-10-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2496566C2 (en) * | 2012-02-14 | 2013-10-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2494797C1 (en) * | 2012-02-14 | 2013-10-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2494800C1 (en) * | 2012-03-06 | 2013-10-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2496567C1 (en) * | 2012-03-06 | 2013-10-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2496568C1 (en) * | 2012-03-06 | 2013-10-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU2496569C1 (en) * | 2012-04-16 | 2013-10-27 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Братский государственный университет" | Vibration mixer |
| RU182465U1 (en) * | 2018-06-19 | 2018-08-20 | федеральное государственное бюджетное образовательное учреждение высшего образования "Национальный исследовательский университет "МЭИ" (ФГБОУ ВО "НИУ "МЭИ") | Rotary mixer with electromechanical vibration exciter |
-
1979
- 1979-07-06 JP JP54084916A patent/JPS5933015B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5610326A (en) | 1981-02-02 |
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