JPS6133225A - Powdery granular body treating apparatus - Google Patents
Powdery granular body treating apparatusInfo
- Publication number
- JPS6133225A JPS6133225A JP15372884A JP15372884A JPS6133225A JP S6133225 A JPS6133225 A JP S6133225A JP 15372884 A JP15372884 A JP 15372884A JP 15372884 A JP15372884 A JP 15372884A JP S6133225 A JPS6133225 A JP S6133225A
- Authority
- JP
- Japan
- Prior art keywords
- vacuum
- drying
- jacket
- articles
- granulation
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/02—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
- F26B11/04—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
- F26B11/049—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis with provisions for working under increased or reduced pressure, with or without heating
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Crushing And Grinding (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Drying Of Solid Materials (AREA)
- Beans For Foods Or Fodder (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、粉粒体の処理装置、更に詳しくは、横型の二
重円錐の頂点と頂点を結び線を回転軸とし、これに投入
口、排出口、ジャケット、ロータリージヨイントを付し
て、粉粒体を真空乾燥、通気乾燥、乾式造粒、湿式造粒
、混合、粉砕、スラリー反応、加圧煮熟などの処理をす
る粉粒体処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a powder processing apparatus, more specifically, a horizontal double cone with a line connecting the apexes and the apex serving as a rotation axis, and an inlet, an outlet, a jacket, a rotary The present invention relates to a powder processing device equipped with a joint for processing powder and granular materials such as vacuum drying, ventilation drying, dry granulation, wet granulation, mixing, pulverization, slurry reaction, and pressure boiling.
従来、粉粒体の処理装置として、乾燥、造粒、煮熟、反
応、混合粉砕などの全ての処理操作を、最も好ましく行
なうことのできる装置機器は存在せず、不可能とされて
いた。すなわち、公知公用の粉粒体処理装置は、全て乾
燥用、造粒用、混合用、粉砕用など、それぞれの単一操
作もしくは、せいぜい例えば乾燥機として開発したもの
を混合に用いるとか、混合機として開発したものを乾燥
に用いるなどの応用はなされていても、そもそも乾燥機
として開発されたものは、他の操作を最も好ましい条件
で行なうことができず、結極、個々の操作に適する機種
を、各々そなえることが常識化されており、少量多品種
の生産では、特にその設備機器の数を多く必要とする等
の難点を有していたため、粉粒処理設備の装備は大がか
りなものとなり、機器の数が増すことにより、切替え工
数や、生産性などの他、沢山の解決しえない問題をかか
えて今日に至っている。BACKGROUND ART Conventionally, there has been no equipment that can perform all processing operations such as drying, granulation, boiling, reaction, mixing and pulverization in the most preferable manner as a processing apparatus for powder and granular materials, and it has been considered impossible to do so. In other words, all known and publicly used powder and granule processing equipment either performs a single operation for drying, granulation, mixing, or pulverization, or at best uses a device developed as a dryer for mixing, or a mixer. Even though products developed as dryers have been used for drying, the products originally developed as dryers cannot be used for other operations under the most favorable conditions. It has become common sense to have each type of powder processing equipment, but in the production of a wide variety of products in small quantities, there were difficulties such as the need for a large number of equipment, so the equipment for powder processing equipment became large-scale. As the number of devices increases, there are many unsolvable problems such as changeover man-hours and productivity.
本発明者は、これらの問題に着目し、粉粒体の全ての処
理操作を、最も好ましい条件と能力をもって処理するこ
とのできる万能の機器を開発すべく鋭意研究を重ねて来
た結果、横型二重円錐の頂点と頂点を結ぶ線を回転軸と
し、中心の最大円周上に、投入、排出口を設け、回転軸
の両端に、熱媒住人、出用ロータリージヨイントと、真
空又は加圧用、もしくは、薬液注入用のロータリージヨ
イントをもうけることにより、真空乾燥、通気乾燥、乾
式造粒、湿式造粒、混合、粉砕、スラリー反応、加圧煮
熟などの粉粒体もしくは、化学、食品、医薬品等の殆ん
どの操作を最も好ましい条件で行なうことのできる装置
を洲発し、本発明を完成するに至ったのである。The present inventor has focused on these problems and has conducted extensive research to develop a versatile device that can perform all processing operations for powder and granular materials under the most favorable conditions and capabilities. The axis of rotation is the line connecting the apexes of the double cone, and the inlet and outlet ports are provided on the maximum circumference of the center, and the heating medium housing, outlet rotary joint, and vacuum or By providing a rotary joint for pressure or chemical injection, it is possible to process powder and granular materials such as vacuum drying, ventilation drying, dry granulation, wet granulation, mixing, pulverization, slurry reaction, pressure boiling, etc., or chemical, They have developed an apparatus that can perform most operations on foods, medicines, etc. under the most favorable conditions, and have completed the present invention.
本発゛明の装置が、このように、全ゆる粉粒体の処理に
最も適する理由は、粉粒体の回転が円周方向に回転する
ことにより、脈動が生じず、ミクロ的には個々の粒子が
スムーズな円軌道を運動することにより、粒子の遅速に
よるしようとつ現象、摩擦現象が生じにくい為と、死角
への停滞や、フラッシング現象、部分的Ｗ’ｌ’）現象
、圧縮現象が起りにくいため、粉粒体処理に生ずる問題
点である付着、粉子同士の固着、発塵、摩砕による微粉
の発生、部分的滑り現象による熱効率の低下等を誘発す
ることなく、更に加えて回転円周軌道を一定速度、一定
方向に粒子が運動すると同時に、横二重円錐型であるた
め、円錐の頂点方向に持ち運ばれた粒子は回転面に直角
方向にだ円軌道の運動が同時に与えられ、粒子は常に自
転と公転、たて方向及び斜よこ方向の運動をくりかえす
為、均一な撹拌、均一な粒子のネットワーク運動を保つ
ことになり、乾燥、造粒、混合、熱処理（煮熟、反応）
に最も好ましい条件を提供することができるのである。The reason why the apparatus of the present invention is most suitable for processing all kinds of powder and granules is that the rotation of the powder and granules rotates in the circumferential direction, so that pulsation does not occur and microscopically Because the particles move in a smooth circular orbit, it is difficult for particles to cause stagnation and friction due to their slow speed, as well as stagnation in blind spots, flashing, partial W'l'), and compression phenomena. Because it is difficult to cause problems such as adhesion, sticking of powder to each other, dust generation, generation of fine powder due to grinding, and a decrease in thermal efficiency due to partial slippage, which are problems that occur in powder and granule processing, it is possible to At the same time, since the particle is in a horizontal double cone shape, the particle carried toward the apex of the cone moves in an elliptical orbit in a direction perpendicular to the rotating surface. The particles are fed at the same time, and the particles constantly repeat rotation and revolution, vertical and horizontal movements, so uniform stirring and uniform network movement of particles are maintained, resulting in drying, granulation, mixing, and heat treatment (boiling). ripeness, reaction)
This allows us to provide the most favorable conditions for
以下に本発明を一実施例の図面にしたがって具体的に説
明すると、第１図は、本発明の粉粒体処理機の斜視図で
あり、第２図は対照例としてあげた公知公用の機器一覧
図であり、第３図は粒子の運動図である。The present invention will be specifically explained below with reference to drawings of an embodiment. Fig. 1 is a perspective view of a powder/granular material processing machine of the present invention, and Fig. 2 is a comparative example of a known and publicly used device. This is a list diagram, and FIG. 3 is a motion diagram of particles.
本発明の装置を用いて真空乾燥を行なう場合は、・投入
口（１）より部品を投入し、密閉して回転を開始し、真
空ポンプ（３）をまわして系内を真空に保ちながらコン
デンサー（２）に通水し、ロータリージヨイント（４）
を経て熱媒体ｆ ；Ｉｎ Ｌ／、乾燥する。乾燥が終了
すると、回転を停止し、排出口（５）を開けて排出する
。例えば、６０％含水のみそを用いて、ジャケット温度
８０°Ｃ１真空度３０トールで乾燥を行なったところ、
表１に示したように、平方メートル当りの乾燥速度、付
着残存率などから見た評価点は、第１表の通り、本発明
の装置が最も優れていることが証明された。対照例とし
てダブルコーン００を用いて、同一の操作を行なったが
付着と固結が起り乾燥効率は大巾に低下した。When vacuum drying is performed using the device of the present invention, ・Insert the parts through the inlet (1), close the container, start rotating, and turn the vacuum pump (3) to keep the system vacuum while drying the condenser. (2) and rotary joint (4).
The heat medium f;In L/ is dried through the heating medium f;In L/. When drying is completed, the rotation is stopped and the discharge port (5) is opened to discharge. For example, when miso containing 60% water was dried at a jacket temperature of 80°C and a vacuum level of 30 Torr,
As shown in Table 1, the apparatus of the present invention was proven to be the most excellent in terms of evaluation points in terms of drying rate per square meter, adhesion residual rate, etc. As a control example, Double Cone 00 was used and the same operation was carried out, but adhesion and caking occurred and the drying efficiency was greatly reduced.
次に、本発明の装置を用いて、乾式造粒を行なう場合は
、投入口（１）より原料粉体を入れ、コーティング剤を
同時に投入するか、又は、分割して投入する時は系内を
減圧に保ちつつ回転させながら、供給用ロータリージヨ
イント（６）を経て、供給槽（７）より供給しながら、
除々に昇温して、融点をもつバインダーが、融点に達す
るまで昇温し、造粒が終了するまでその温度に保ち、ジ
ャケットを冷却して、造粒品を排出口（５）より排出す
る。例えば、８０〜１５０メツシユの魚粉を用いて、融
点６０°Ｃのシュガーエステルを５％同時投入し、回転
させながらジャケットの温度を除々に昇温させ、７０°
Ｃに５分間保ち、次にジャケットに通水して冷却をする
と、１〜３叩φの球状造粒物がえられ、系内には付着や
粒子同士の付着による塊状物もなく、優れた粒子径の、
巾のせまい粒度分布をもつ造粒物をえた。このものの粒
度分布１コ、付着率などより、対照例と比較した評価点
は第１表の通りであり、本発明の装置は、最も侵れた結
果をえた。Next, when performing dry granulation using the apparatus of the present invention, the raw material powder is introduced from the inlet (1), and the coating agent is introduced at the same time, or when it is introduced in parts, it is inside the system. While rotating while keeping the pressure reduced, while supplying from the supply tank (7) through the supply rotary joint (6),
The temperature is gradually increased until the binder with a melting point reaches its melting point, the temperature is maintained until granulation is completed, the jacket is cooled, and the granulated product is discharged from the discharge port (5). . For example, using 80 to 150 mesh of fishmeal, add 5% sugar ester with a melting point of 60°C at the same time, gradually raise the temperature of the jacket while rotating, and raise the temperature to 70°C.
C for 5 minutes, and then cooled by passing water through the jacket, a spherical granulate with a diameter of 1 to 3 was obtained. of particle size,
Granules with a narrow particle size distribution were obtained. Based on the particle size distribution, adhesion rate, etc. of this product, the evaluation points compared with the control example are as shown in Table 1, and the device of the present invention obtained the most aggressive results.
次に又、本発明の装置を用いて、湿式造粒を行なう場合
は、投入口（１）より、原料粉を入れ、回転させながら
、真空ポンプ（３）により系内を少減圧に保ちつつ、溶
媒に溶かしたバインダー又はノＸ１ノグーとなる溶剤を
供給槽（７）より、除々に供給すると、ノズル（８）の
先端より霧状にバインダーが吹き出され、造粒がなされ
る。造粒が完了するとノくルブ（９）は閉じられ、系内
は真空になり、ジャケットにロータリージヨイント（４
）より熱Ｗ“抹を通ずると、添加された溶媒は蒸発し、
次にジャケットを冷却して造粒品を冷却し、真空を切り
、排出口（５）より排出する。この間造粒品の停滞がな
いため、粒子同士の付着による塊状化や壁面付着は起ら
ないのである。このような操作条件でフェノール樹脂成
形材料の粉床を用いて粉床に対しメタノールを１０％用
いて造粒を行ない、ジャケット温度４０°Ｃで３０分乾
燥をしたところ、０．５〜３ｍｍφの揃った球状粒子が
形成された。対照例として、円盤型造粒機Ｏａを用いて
、造粒を行なったが、真空乾燥を別の装置で行なわなけ
ればならず、取出して乾燥根に移行する時、粒子の再付
着を生じる欠点を見出し、他の装置では、造粒が均一に
できても、乾燥根に移す段階で同様の問題を有するもの
であった。Next, when performing wet granulation using the apparatus of the present invention, feed the raw material powder through the inlet (1), and while rotating the system, maintain a slight vacuum in the system using the vacuum pump (3). When the binder dissolved in the solvent or the solvent used to form Nox1 Nogoo is gradually supplied from the supply tank (7), the binder is blown out in a mist form from the tip of the nozzle (8) and granulated. When granulation is completed, the knob (9) is closed, the system is evacuated, and the rotary joint (4) is attached to the jacket.
), the added solvent evaporates,
Next, the jacket is cooled to cool the granulated product, the vacuum is turned off, and the product is discharged from the discharge port (5). During this time, there is no stagnation of the granulated product, so no clumping or adhesion to the wall due to particles adhering to each other occurs. Under these operating conditions, using a powder bed of phenolic resin molding material, granulation was carried out using 10% methanol in the powder bed and drying for 30 minutes at a jacket temperature of 40°C resulted in particles of 0.5 to 3 mmφ. Uniform spherical particles were formed. As a control example, granulation was carried out using a disk-type granulator Oa, but vacuum drying had to be performed in a separate device, and the drawback was that particles re-attached when taken out and transferred to dry roots. However, even if other devices were able to produce uniform granules, they had similar problems at the stage of transfer to dry roots.
更に又、本発明の装置を用いて、煮熟を行なう場合は、
投入口（１）より、煮熟用原料を投入し、密閉して、ジ
ャケットに熱媒を通すと系内は加圧になり、短時間で煮
熟が完了する。最初より調味料を加えない場合は、系内
を常圧又は少減圧にして、供給槽（７）より、調味料を
供給することができる。Furthermore, when performing boiling using the apparatus of the present invention,
When the raw material for boiling is input through the input port (1), the jacket is sealed, and a heating medium is passed through the jacket, the inside of the system is pressurized and boiling is completed in a short time. If no seasoning is added from the beginning, the seasoning can be supplied from the supply tank (7) with the system inside at normal pressure or slightly reduced pressure.
このようにして短時間に、とくに、豆類などは、水に一
夜浸漬することなしに、１〜３時間洗浄をかねて浸漬す
る程度で、中心部まで完全に均一に煮熟されるので、調
味料が均一に浸透され、まろやかな煮豆ができると共に
つくだに類の場合、他の攪拌式の煮熟装置では、コンブ
類やその他加えられるものが切断、損傷されるのに比べ
、本発明の装置を用いると、全く損傷、変形、切断、が
なく外観上も高品位の煮物をえることができることを発
見した。In this way, in a short time, especially beans, etc., without soaking them in water overnight, just soaking them in water for 1 to 3 hours is enough to boil them completely and evenly to the center, so you can add seasonings. The beans are evenly penetrated, producing mellow boiled beans, and in the case of tsukuni (chicken crab), compared to other stirring-type boiling devices that cut or damage kelp and other added ingredients, the device of the present invention It was discovered that by using this method, it is possible to obtain boiled foods that are of high quality in appearance and are completely free from damage, deformation, and cutting.
このような操作条件で、大豆とコンブのつくだにを製造
した例を以下に述べると、まず、洗浄を兼ねて１，５時
間水浸漬をした大豆を、本装置に投入し、密閉し、ジャ
ケット温度１０５°Ｃで３０分煮熟を行ない、次に乾燥
コンブを切断して投入し、同上条件で５分間煮熟し、調
味料を加えて、のち、ジャケットを加熱から冷却に切替
えると同時に、真空に保つと、水分の蒸発により、せん
熱がうばわれ系内は約１０分で３０°Ｃに冷却された。The following is an example of producing soybean and kelp tsukuda under these operating conditions. First, soybeans were soaked in water for 1.5 hours for washing, then put into this device, sealed, and Boil for 30 minutes at a jacket temperature of 105°C, then cut and add dried kelp, boil for 5 minutes under the same conditions as above, add seasonings, and then switch the jacket from heating to cooling at the same time. When the system was kept in a vacuum, the heat was absorbed by the evaporation of water, and the inside of the system was cooled to 30°C in about 10 minutes.
排出されたつくだには、豆およびコンブの変形、破損、
切断もなく、高品位でまろやかな味をもつ製品をえるこ
とができた。本実施例に対して対照例として、撹拌型煮
熟機Ｑ］）を用いて同様の操作を行なったところ、豆及
びコンブとくにコンブの切断や、圧損が多く、粘性を有
するもので、煮熟時間等は同一であったが、品位的に劣
るものであった。同様に、ダブルコーン型ＱＯ，斜円筒
型αＱをテストしたが、内容物のブロッキング現象を住
じ、特性を更に増した品位の低いものかえられた。The discharged Tsukuda contains beans and kelp that are deformed, damaged,
Without cutting, we were able to obtain a product with high quality and a mellow taste. As a control example for this example, similar operations were carried out using a stirrer-type boiling machine Q). The time was the same, but the quality was inferior. Similarly, a double cone type QO and an oblique cylindrical type αQ were tested, but they suffered from the blocking phenomenon of the contents and were replaced with lower quality ones with further improved characteristics.
（以下余白）
第１表
以上に本発明の実施例の一部と、対照例の一部を対比し
て説明したが、本発明と公知公用の機器とのちがいをよ
り明確にする為本発明の装置と、他の公知公用の装置と
の、乾燥機能（乾燥速度、付着性、微粉発生、排出残存
率、操作性などから）、混合性能（混合速度、微粉発生
率、偏析性、排出残存率、操作性などから）、造粒性能
（乾式、湿式、真空乾燥共用性、粒度分布、粒子形状、
微粉発生、排出残存率、付着、操作性などから）、煮熟
性能（煮熟時間、均一煮熟、損傷、切断率、外観、味覚
、操作性などから）を第１表に総合点としてかかげ対比
した。(Left space below) Although some of the embodiments of the present invention and some of the comparative examples have been explained in comparison with Table 1 and above, in order to clarify the difference between the present invention and publicly known devices, the present invention The drying function (drying speed, adhesion, fine powder generation, discharge residual rate, operability, etc.) and mixing performance (mixing speed, fine powder generation rate, segregation, discharge residual rate, operability, etc.), granulation performance (compatibility with dry, wet, and vacuum drying methods, particle size distribution, particle shape,
Table 1 summarizes the overall scores based on fine powder generation, discharge residual rate, adhesion, operability, etc.), and boiling performance (in terms of boiling time, uniform boiling, damage, cutting rate, appearance, taste, operability, etc.) Contrasted.
本発明は、以上のような実施態様からなりたっており、
本発明の装置を用いることにより、第１表を見ても明ら
かであり、機器装置の操作目的とその効用から推定して
も明らかなように、本発明の装置は真空乾燥、混合、乾
式造粒、湿式造粒乾燥、煮熟の他、粉粒体又は、これに
類するものの殆んどの操作に最も好ましい条件で使用す
ることができ喝だけでな（、その構造と、操作機構が示
すように、円滑な回転による品位、操作上発生する諸問
題を解決し、密閉系での操作・クローズ化された投入排
出による自動化、無人化、無害化、衛生性の向上等が可
能とされ、多くの機器を用いて行なう操作を、本発明の
装置で、殆んど全て可能とすることにより、工程の簡略
化や設備投資の経済性等に於て著るしく侵位であり、今
までに、比類のない万能な装置であり、本発明が産業の
発展と、コストダウン、品位の向上などに役立つことは
、想像を絶するものであり、きわめて画期的かつ有効な
発明である。The present invention consists of the above embodiments,
By using the apparatus of the present invention, the apparatus of the present invention can perform vacuum drying, mixing, dry manufacturing, etc. It can be used under the most favorable conditions for most operations of granules, wet granulation, drying, boiling, powder, granules, and the like (as indicated by its structure and operating mechanism). In addition, smooth rotation improves quality, solves various problems that occur during operation, and enables automation, unmanned operation, detoxification, and improved hygiene through closed system operation and closed input and discharge. The device of the present invention makes it possible to perform almost all the operations that would be performed using the equipment of It is an unparalleled and versatile device, and it is unimaginable that the present invention will be useful for industrial development, cost reduction, and quality improvement, making it an extremely innovative and effective invention.
以上は本発明に関する最も好ましい具体例について説明
したが、本発明の精神を逸脱しない範囲で、これに種々
の変形を加えることも可能であり、それらも本発明の範
囲に属するものである。Although the most preferred embodiment of the present invention has been described above, it is possible to make various modifications without departing from the spirit of the present invention, and these also fall within the scope of the present invention.
第１図は、本発明の粉粒体処理装置の斜視図、第２図は
対照例としてあげた公知公用の機器一覧斜視図、第３図
は粒子の運動図。
（１）・・・投入口、（２）・・・コンデンサー、（３
）・・・真空ポンプ、
（４）・・・ロータリージヨイント、
（５）・・・排出口、
（６）・・・供給用ロータリージヨイント、（７）・・
・供給槽、（８）・・・ノズル、（９）・・・ハルツ、
α０・・・ダブルコーン型、θυ・・・ロ
ータリードラム型、
αト・・円盤型、
０ト°°ロータリーキルン型、
α萄・・・回転箱型、 ＱＩＶ型、０時・・・斜
円筒型、 αη・・・自転公転型、（至）・・・
ディスク型、（１１・・・ミゾ型、Ｃ１−・・斜ディス
ク型、 ■）・・・攪拌型。
特許出願人 株式会社山北鉄工所
１２図FIG. 1 is a perspective view of a powder processing apparatus of the present invention, FIG. 2 is a perspective view of a list of known and publicly used equipment as a comparative example, and FIG. 3 is a particle movement diagram. (1)...Inlet, (2)...Condenser, (3
)...Vacuum pump, (4)...Rotary joint, (5)...Discharge port, (6)...Rotary joint for supply, (7)...
・Supply tank, (8)...nozzle, (9)...harz,
α0...double cone type, θυ...rotary drum type, αto...disc type, 0t°° rotary kiln type, α萄...rotating box type, QIV type, 0 o'clock...oblique cylindrical type , αη...Rotation-revolution type, (to)...
Disk type, (11...groove type, C1-...slanted disk type, ①)...agitation type. Patent applicant Yamakita Iron Works Co., Ltd. Figure 12
Claims (1)
の最大円周上に投入排出口をもうけ、二重円錐にジャケ
ットを付し回転軸の両端又はどちらかに、加熱、冷却の
媒体用と、真空、加圧の通気用もしくは、薬液注入用の
ロータリージョイントをそれぞれもうけ、真空乾燥、通
気乾燥、乾式造粒、湿式造粒、混合、粉砕、スラリー反
応、加圧煮熟などの処理をすることのできる、粉粒体処
理装置。The axis of rotation is the line connecting the vertices of the horizontal double cone, and an inlet and outlet is provided on the maximum circumference of the center.A jacket is attached to the double cone, and heating and cooling are installed at either or both ends of the rotation axis. It has rotary joints for media, vacuum, pressurized ventilation, and chemical injection, and is suitable for vacuum drying, ventilation drying, dry granulation, wet granulation, mixing, pulverization, slurry reaction, pressure boiling, etc. Powder processing equipment that can process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15372884A JPS6133225A (en) | 1984-07-23 | 1984-07-23 | Powdery granular body treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15372884A JPS6133225A (en) | 1984-07-23 | 1984-07-23 | Powdery granular body treating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6133225A true JPS6133225A (en) | 1986-02-17 |
Family
ID=15568797
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15372884A Pending JPS6133225A (en) | 1984-07-23 | 1984-07-23 | Powdery granular body treating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6133225A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63204092A (en) * | 1987-02-19 | 1988-08-23 | 株式会社 徳寿工作所 | Vacuum rotary drier |
| EP0315041A2 (en) * | 1987-11-02 | 1989-05-10 | Fujisawa Pharmaceutical Co., Ltd. | Vacuum rotary dryer |
| JPH0642867A (en) * | 1992-07-23 | 1994-02-18 | Nippon Kansouki Kk | Tumbler type rotary dryer |
| JPH0659787U (en) * | 1993-11-04 | 1994-08-19 | 株式会社徳寿工作所 | Vacuum rotary dryer |
| JPH08311443A (en) * | 1995-05-15 | 1996-11-26 | Samsung Display Devices Co Ltd | Apparatus and method for drying phosphor |
| EP1079188A1 (en) * | 1999-08-25 | 2001-02-28 | Chuo Kakohki Co., LTD. | Apparatus for treatment by vibration |
| CN105371617A (en) * | 2015-11-13 | 2016-03-02 | 张海娟 | Continuous rotating type vacuum drier |
| CN105403010A (en) * | 2015-12-15 | 2016-03-16 | 张海娟 | Rotary vacuum drying cabin |
| CN107525368A (en) * | 2017-08-02 | 2017-12-29 | 温州市联和针纺科技有限公司 | A kind of vacuum drum drying machine and the method using its drying chemical fibre |
| CN108088194A (en) * | 2017-12-22 | 2018-05-29 | 宿州学院 | A kind of agricultural vacuum dewatering apparatus |
| CN113059165A (en) * | 2021-03-26 | 2021-07-02 | 成都虹波实业股份有限公司 | Efficient powder wet mixing and drying integrated equipment |
| CN115574563A (en) * | 2022-10-13 | 2023-01-06 | 江苏威拉里新材料科技有限公司 | Metal powder rotary drying device and using method thereof |
| KR102593812B1 (en) * | 2023-01-20 | 2023-10-24 | 제정숙 | tumbler for vacuum smoking |
-
1984
- 1984-07-23 JP JP15372884A patent/JPS6133225A/en active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63204092A (en) * | 1987-02-19 | 1988-08-23 | 株式会社 徳寿工作所 | Vacuum rotary drier |
| EP0315041A2 (en) * | 1987-11-02 | 1989-05-10 | Fujisawa Pharmaceutical Co., Ltd. | Vacuum rotary dryer |
| JPH0642867A (en) * | 1992-07-23 | 1994-02-18 | Nippon Kansouki Kk | Tumbler type rotary dryer |
| JPH0659787U (en) * | 1993-11-04 | 1994-08-19 | 株式会社徳寿工作所 | Vacuum rotary dryer |
| JPH08311443A (en) * | 1995-05-15 | 1996-11-26 | Samsung Display Devices Co Ltd | Apparatus and method for drying phosphor |
| EP1079188A1 (en) * | 1999-08-25 | 2001-02-28 | Chuo Kakohki Co., LTD. | Apparatus for treatment by vibration |
| CN105371617A (en) * | 2015-11-13 | 2016-03-02 | 张海娟 | Continuous rotating type vacuum drier |
| CN105403010A (en) * | 2015-12-15 | 2016-03-16 | 张海娟 | Rotary vacuum drying cabin |
| CN107525368A (en) * | 2017-08-02 | 2017-12-29 | 温州市联和针纺科技有限公司 | A kind of vacuum drum drying machine and the method using its drying chemical fibre |
| CN108088194A (en) * | 2017-12-22 | 2018-05-29 | 宿州学院 | A kind of agricultural vacuum dewatering apparatus |
| CN113059165A (en) * | 2021-03-26 | 2021-07-02 | 成都虹波实业股份有限公司 | Efficient powder wet mixing and drying integrated equipment |
| CN115574563A (en) * | 2022-10-13 | 2023-01-06 | 江苏威拉里新材料科技有限公司 | Metal powder rotary drying device and using method thereof |
| CN115574563B (en) * | 2022-10-13 | 2023-10-13 | 江苏威拉里新材料科技有限公司 | Metal powder rotary drying device and application method thereof |
| KR102593812B1 (en) * | 2023-01-20 | 2023-10-24 | 제정숙 | tumbler for vacuum smoking |
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