JPS6013744B2 - Powder processing equipment - Google Patents
Powder processing equipmentInfo
- Publication number
- JPS6013744B2 JPS6013744B2 JP57178751A JP17875182A JPS6013744B2 JP S6013744 B2 JPS6013744 B2 JP S6013744B2 JP 57178751 A JP57178751 A JP 57178751A JP 17875182 A JP17875182 A JP 17875182A JP S6013744 B2 JPS6013744 B2 JP S6013744B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- flow path
- cylinder
- processing
- gas
- 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
Landscapes
- Drying Of Solid Materials (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
【発明の詳細な説明】
本発明は粉体の処理装置、更に詳しくは筒体を振動させ
、該筒体内に形成されている複数個の粉体流路を粉体が
ある種の浮遊回転状態となって押し流ミれる際に、該粉
体流路へ粉体に直接する処理用気体を流週させることに
より、乾燥や冷却その他各種の反応等の処理を効率的に
行なう粉体の処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a powder processing apparatus, more specifically, vibrates a cylindrical body so that the powder can move through a plurality of powder channels formed in the cylindrical body in a kind of floating and rotating state. Powder processing that efficiently performs processes such as drying, cooling, and various reactions by flowing processing gas directly onto the powder into the powder flow path as it flows through the powder. Regarding equipment.
粉体状の医薬品や化学製品等を製造する工場では振動方
式による粉体の処理装置が広く利用されている。BACKGROUND OF THE INVENTION Powder processing equipment using a vibration method is widely used in factories that manufacture powdered pharmaceuticals, chemical products, and the like.
この種の処理装置は、スプリングの如き弾性体で支持さ
れている容器を例えば偏心錘の如き振動発生源で振動さ
せ、この振動によって該容器内の粉体をある種の浮遊回
転状態とし、かかる状態で該容器に周設されているジャ
ケットに熱媒体を循環して、乾燥や冷却その他各種の反
応等の処理を行うものであり、既に本発明者もその基本
装置を提供している(特許法第1046826号)。そ
ころが、かかる従来装置は、該装置に組込まれている前
述の容器内を粉体が一方向にのみいわゆるワンパス方式
で流れるものであって、容器内の粉体へ熱媒体が直接有
効に作用するのは粉体が接触する部分における容器周壁
面だけである。そして、通常振動により粉体に略円状の
回転運動を与えると、粉体の挙動は同D円を描く傾向に
あるが、処理量の増大に伴なつて容器の直経が大きくな
ると、容器内の粉体層の厚みが増し、これがある一定以
上に達すると、中心部分の粉体に対して容器周壁面から
の影響が少なくなり、結局、乾燥や冷却その他各種の反
応等の処理が非効率的になるという欠点がある。本発明
は、叙上の従来欠点を解消する改良された粉体の処理装
置を提供するもので、その目的は、振動発生源を具備す
る一つの筒体内に複数個の粉体流路を形成し、該粉体流
路において浮遊回転状態となる粉体へ直綾するように処
理用気体を稀適させて、該粉体に処理用気体からの直接
の影響を与えつつ、粉体流路における粉体の層高を相対
的に低くして、該粉体の処理効率を向上する点にある。This type of processing equipment vibrates a container supported by an elastic body such as a spring using a vibration source such as an eccentric weight, and the powder in the container is brought into a kind of floating rotation state by this vibration. In this system, a heat medium is circulated through a jacket surrounding the container to perform drying, cooling, and various other reactions, and the present inventor has already provided the basic device (patented). Law No. 1046826). However, in such conventional devices, the powder flows in one direction only in the so-called one-pass method in the aforementioned container built into the device, and the heat transfer medium is directly effective to the powder in the container. It only acts on the peripheral wall surface of the container in the area where the powder comes into contact. When a roughly circular rotational motion is applied to the powder by normal vibration, the behavior of the powder tends to draw the same D circle, but as the throughput increases, the diameter of the container increases. When the thickness of the powder layer inside increases and reaches a certain level, the influence of the peripheral wall of the container on the powder in the center decreases, and as a result, treatments such as drying, cooling, and various other reactions become ineffective. It has the disadvantage of being more efficient. The present invention provides an improved powder processing device that eliminates the above-mentioned conventional drawbacks, and its purpose is to form a plurality of powder flow paths within a single cylinder provided with a vibration generation source. Then, the processing gas is diluted so as to flow directly to the powder that is in a floating and rotating state in the powder flow path, and the powder flow path is controlled while the processing gas has a direct influence on the powder. The purpose of this invention is to make the layer height of the powder relatively low in order to improve the processing efficiency of the powder.
以下、図面に基づいて本発明の構成を詳細に説明する。Hereinafter, the configuration of the present invention will be explained in detail based on the drawings.
第1図は従来の処理装置を例示する側面(一部断面)図
、第2図は第1図の処理装置における円筒容器内部を示
す縦断面拡大略視図である。処理装置11は、両側のフ
ランジにカバー21a,21bがネジ止め等で固定され
ている略水平設贋の胴長の円筒容器31に粉体の入口4
1a及び出口41b並びに粉体から発生する蒸気を検出
する排出口41cが穿設されるとともに粉体を加熱又は
冷却するための熱媒体を流すジャケット31aが周設さ
れ、振動発生源31bを備える該円筒容器31が弾性体
であるスプリング51a,51bによって支持されてい
るもので、円筒容器31を振動発生源31bで振動させ
る一方、ジャケット31aに熱媒体を流し、入口41a
から連続投入される粉体A,を円筒容器31内である種
の浮遊回転状態として乾燥や冷却その他各種の反応等の
処理を行い、処理後の粉体を出口41bから得るもので
ある。しかし、このような従来装置には、前述の如き欠
点がある。FIG. 1 is a side (partially cross-sectional) view illustrating a conventional processing apparatus, and FIG. 2 is an enlarged vertical cross-sectional schematic view showing the inside of a cylindrical container in the processing apparatus of FIG. The processing device 11 includes a powder inlet 4 in a substantially horizontally installed long-body cylindrical container 31 with covers 21a and 21b fixed to flanges on both sides by screws or the like.
1a, an outlet 41b, and an exhaust port 41c for detecting steam generated from the powder, a jacket 31a for flowing a heat medium for heating or cooling the powder is provided around it, and a vibration generation source 31b is provided. The cylindrical container 31 is supported by springs 51a and 51b, which are elastic bodies, and while the cylindrical container 31 is vibrated by a vibration source 31b, a heat medium is caused to flow through the jacket 31a, and the inlet 41a
Powder A, which is continuously introduced from the cylindrical container 31, is placed in a kind of floating rotation state and subjected to processes such as drying, cooling, and various other reactions, and the processed powder is obtained from the outlet 41b. However, such conventional devices have the drawbacks mentioned above.
第3図は本発明の一実施例を示す側面(一部断面)図、
第4図は第3図の実施例における筒体内部を示す縦断面
拡大略視図である。FIG. 3 is a side (partially cross-sectional) view showing one embodiment of the present invention;
FIG. 4 is an enlarged schematic vertical cross-sectional view showing the inside of the cylinder in the embodiment of FIG. 3. FIG.
本発明に係る処理装置12は、略水平設置の筒体32の
両側にフード付きのフレキシブルジョイント22a,2
2bを介して処理用気体の入口32a及び出口32bが
接続されるとともに該筒体32内には4個の粉体流路6
2a〜62dが形成され、これらの各粉体流路には粉体
A2の入口42a〜42d及び出口43a〜43dが懐
続されてし、て、振動発生源32cの具備されている筒
体32が弾性体であるスプリング52a,52bによっ
て支持されているもので、筒体32を振動発生源32c
で振動させる一方、入口32aから出口32b方向へ各
粉体流路に処理用気体を流適させて、入口42a〜42
dから連続投入される粉体A2が各粉体流路をある種の
浮遊回転状態となってその投入量に応じ押し流される間
に、該粉体んに乾燥や冷却その他各種の反応等の処理を
行い、処理後の粉体を出口43a〜43dから得るもの
である。第5図は本発明の他の一実施例を示す側面(一
部断面)図、第6図は第5図の実施例における筒体内部
を示す縦断面拡大略視図、第7図は第5図の実施例にお
ける粉体流路を示す部分拡大斜視図である。第3図に示
した実施例は各粉体流路が相互に連絡されることなく単
純に並列形成されている場合であるが、第5図〜第7図
に示す実施例は4個の粉体流路が端部で連絡されていて
、粉体が各粉体流路を順次反対方向へ連続して流れるよ
うに構成されているものである。すなわち、本発明に係
る処理装置13は、筒体33の両側にフード付きのフレ
キシブルジョイント23a,23bを介して処理用気体
の入口33a及び出口33bが接続されるとともに筒体
33内には粉体A3が順次反対方向へ連続して流れる4
個の粉体流路63a〜63dが形成され、粉体流路63
aには粉体の入口44aが、また粉体流路63dには粉
体の出口44bが各々接続されていて、振動発生源33
cの具備されている筒体33が弾性体であるスプリング
53a,53bによって支持されているもので、筒体3
3を振動発生源33cで振動させる一方、入口33aか
ら出口33bへ各粉体流路に処理用気体を流遇させて、
入口44aから連続投入される粉体A3が各粉体流路を
ある種の浮遊回転状態となって順次反対方向へその投入
量に応じ押し流される間に、該粉体A3に乾燥や冷却そ
の他各種の反応等の処理を行い、処理後の粉体を出口4
4bから得るものである。連絡路や堰板等の一部を除き
第3図に示した実施例もほぼ同様であるが、第5図〜第
7図に示した実施例の場合、粉体流路63a,63b,
63cは筒体33の内周面に固定されている断面半円形
の樋状体73a,73b,73cから形成され、粉体流
路63dは筒体33の内周面それ自体から形成されてい
て、これらの各粉体流路の両端には粉体A3が溢流防止
壁83a〜83hが取付けられ且つ各粉体流路における
粉体A3の流れ方向側端部には堰板93a〜93dが突
設されており、各粉体流路間には粉体A3が順次反対方
向へ連続して流れるように、堰板93aと溢流防止壁8
3b、堰板93bと溢流防止壁83d、堰板93cと溢
流防止壁83fとで各々区画される部分から次の粉体流
路へと連絡路103a〜103cが開設されている。The processing device 12 according to the present invention includes flexible joints 22a, 2 with hoods on both sides of a cylinder 32 installed substantially horizontally.
An inlet 32a and an outlet 32b of the processing gas are connected through the cylinder 32, and four powder channels 6 are provided in the cylinder 32.
2a to 62d are formed, and inlets 42a to 42d and outlets 43a to 43d of powder A2 are connected to each of these powder flow paths, and a cylinder 32 equipped with a vibration generation source 32c are supported by springs 52a and 52b which are elastic bodies, and the cylindrical body 32 is connected to the vibration generating source 32c.
While vibrating with
Powder A2, which is continuously introduced from d, is in a kind of floating rotation state through each powder flow path and is swept away according to the amount of input, while the powder is subjected to drying, cooling, and various other reactions. The processed powder is obtained from the outlets 43a to 43d. FIG. 5 is a side (partially sectional) view showing another embodiment of the present invention, FIG. 6 is an enlarged vertical cross-sectional schematic view showing the inside of the cylinder in the embodiment of FIG. 5, and FIG. FIG. 6 is a partially enlarged perspective view showing the powder flow path in the embodiment of FIG. 5; The embodiment shown in Fig. 3 is a case where the powder channels are simply formed in parallel without being connected to each other, but the embodiments shown in Figs. The powder flow paths are connected at their ends, and the powder is configured to flow sequentially through each powder flow path in opposite directions. That is, in the processing apparatus 13 according to the present invention, an inlet 33a and an outlet 33b of the processing gas are connected to both sides of the cylinder 33 via hooded flexible joints 23a, 23b, and powder is contained in the cylinder 33. A3 flows continuously in opposite directions 4
Powder flow paths 63a to 63d are formed, and powder flow paths 63a to 63d are formed.
A powder inlet 44a is connected to the powder flow path 63d, and a powder outlet 44b is connected to the powder flow path 63d.
The cylinder 33 equipped with c is supported by springs 53a and 53b which are elastic bodies.
3 is vibrated by a vibration source 33c, while flowing processing gas into each powder flow path from the inlet 33a to the outlet 33b,
Powder A3, which is continuously introduced from the inlet 44a, enters each powder flow path in a kind of floating rotation state and is sequentially swept away in opposite directions according to the amount of input, while the powder A3 undergoes drying, cooling, and other various processes. After the treatment, the powder is sent to outlet 4.
4b. The embodiment shown in FIG. 3 is almost the same except for some parts such as communication channels and weir plates, but in the case of the embodiment shown in FIGS. 5 to 7, the powder flow channels 63a, 63b,
63c is formed from gutter-like bodies 73a, 73b, and 73c with semicircular cross sections fixed to the inner peripheral surface of the cylinder 33, and the powder flow path 63d is formed from the inner peripheral surface of the cylinder 33 itself. , Powder A3 overflow prevention walls 83a to 83h are attached to both ends of each of these powder channels, and weir plates 93a to 93d are installed at the end of each powder channel in the flow direction of powder A3. A weir plate 93a and an overflow prevention wall 8 are provided between each powder flow path so that the powder A3 continuously flows in opposite directions.
3b, communication paths 103a to 103c are established from the parts defined by the weir plate 93b and the overflow prevention wall 83d, and the areas partitioned by the weir plate 93c and the overflow prevention wall 83f to the next powder flow path.
したがって、第5図〜第7図に示した実施例の粉体A3
の押し流れは、入口44a→粉体流路63a→堰板93
a→連絡路103a→粉体流路63b→堰板93b→連
絡路103b→粉体流路63c→堰板93c→連絡路1
03c→粉体流路63d→堰板93d→出口44b、の
順序となっている。第8図と第9図とは、第4図や第6
図に対応して、本発明の更に他の各別の実施例における
筒体内部を示す縦断面拡大略視図である。Therefore, the powder A3 of the example shown in FIGS. 5 to 7
The push flow is from the inlet 44a to the powder flow path 63a to the weir plate 93.
a → communication path 103a → powder flow path 63b → weir plate 93b → communication path 103b → powder flow path 63c → weir plate 93c → communication path 1
The order is 03c→powder flow path 63d→dam plate 93d→outlet 44b. Figures 8 and 9 refer to Figures 4 and 6.
Corresponding to the figure, it is a vertical cross-sectional enlarged schematic view showing the inside of a cylinder in still other embodiments of the present invention.
いずれも、略々断面V字形の粉体流路が、第8図の場合
は7個、また第9図の場合は9個形成されている。これ
らの他の実施例においても、粉体A4,A5の流れは、
前述の第3図又は第5図に示した実施例の場合と同様に
することができる。本発明は、筒体の形状や該筒体に形
成される粉体流路の形状、また該粉体流路を形成する例
えば樋状体の固定手段、更には処理用気体の流過手段等
、図示した実施例の場合に限定されるものではなく、例
えば粉体流路は断面U字形にゥェッジワィャや金網等で
形成してもよく、また要すれば各粉体流路を二重構造と
してその内部に外部の粉体を間接加熱する熱媒体を循環
させたり、筒体外周に熱媒体の循環可能なジャケットを
付設併用したりすることもできるが、粉体流路の形状は
粉体の浮遊回転に無理とならない湾曲状又は煩斜状にす
るのが好ましい。In each case, seven powder channels each having a substantially V-shaped cross section are formed in the case of FIG. 8, and nine in the case of FIG. 9. In these other examples as well, the flow of powders A4 and A5 is as follows:
This can be done in the same way as in the embodiment shown in FIG. 3 or FIG. 5 described above. The present invention relates to the shape of the cylindrical body, the shape of the powder flow path formed in the cylindrical body, the means for fixing the gutter-like body forming the powder flow path, and furthermore, the flow means for processing gas, etc. However, the present invention is not limited to the illustrated embodiment; for example, the powder flow path may be formed into a U-shaped cross section using wedge wires, wire mesh, etc., and if necessary, each powder flow path may be formed into a double structure. It is also possible to circulate a heat medium that indirectly heats the external powder inside the cylinder, or to attach a jacket around the outer circumference of the cylinder that allows the circulation of the heat medium, but the shape of the powder flow path is different from that of the powder. It is preferable to have a curved or oblique shape that does not make floating rotation difficult.
以上説明した本発明によれば、一つの筒体内に複数個の
粉体流路を形成して、該粉体流路における粉体に処理用
気体の影響を直接に及ぼすことができる。According to the present invention described above, it is possible to form a plurality of powder channels in one cylinder, and to directly exert the influence of the processing gas on the powder in the powder channels.
しかも、本発明における筒体の振動方向は、従来の振動
コンベヤ等において粉体の移動推進力となるような斜め
方向ではなく、その殆んどが略円形のラジアル方向だけ
であり、粉体流路における粉体がかかる振動によりある
種の浮遊回転状態となって流動化しているため、該粉体
の入口から出口方向への移動は入口からの粉体投入量に
よって容易に決定することができる。したがつて、処理
対象である粉体の性状や量に応じて、最も適切な粉体層
高となる粉体流路を必要な数だけ形成使用することによ
り、一つの大口径の容器を組み込んだ前述の如き従来装
置に比べて、はるかに効率良く粉体の乾燥や冷却その他
各種の反応等の処理をすることができるのである。Moreover, the direction of vibration of the cylinder in the present invention is not an oblique direction that provides a driving force for moving powder in conventional vibrating conveyors, etc., but is mostly only in a substantially circular radial direction, which prevents the powder from flowing. Since the powder in the channel is fluidized in a kind of floating rotation state due to the vibration, the movement of the powder from the inlet to the outlet can be easily determined by the amount of powder input from the inlet. . Therefore, by forming and using the necessary number of powder channels that provide the most appropriate powder layer height depending on the properties and amount of powder to be processed, it is possible to incorporate a single large-diameter container. However, compared to the conventional apparatus described above, it is possible to dry, cool, and perform various reactions on powder much more efficiently.
【図面の簡単な説明】
第1図は従来の処理装置を例示する側面(一部断面)図
、第2図は第1図の処理装置における円筒容器内部を示
す縦断面拡大略視図、第3図は本発明の一実施例を示す
側面(一部断面)図、第4図は第3図の実施例における
筒体内部を示す縦断面拡大略視図、第5図は本発明の他
の一実施例を示す側面(一部断面)図、第6図は第5図
の実施例における筒体内部を示す縦断面拡大略視図、第
7図は第5図の実施例における粉体流路を示す部分拡大
斜視図、第8図と第9図とは本発明の更に他の各別の実
施例における筒体内部を示す縦断面拡大略視図である。
11,12,13・・・・・・処理装置、21a,21
b……カバー、22a,220,23a,23b……フ
レキシブルジョイント、31……円筒容器、31a……
ジャケット、31b,32c,33c・・・・・・振動
発生源、32,33・・・・・・筒体、32a,33a
・・・・・・処理用気体の入口、32b,33b・・・
・・・処理用気体の出口、41a,42a〜42b,4
4a・・・・・・粉体の入口、41b,43a〜43d
,44b・・・・・・粉体の出口、51a,51b,6
2a,52b,53a,53b……スプリング、62a
〜62d,63a〜63d・・・・・・粉体流路、73
a〜73c・・・・・・樋状体、83a〜83h・・・
・・・溢流防止壁、93a〜93c・・・・・・堰板、
103a〜103c・・・・・・連絡路。第1図
第2図
第3図
第4図
第5図
第6図
第7図
第8図
第9図[Brief Description of the Drawings] Fig. 1 is a side (partially sectional) view illustrating a conventional processing device; 3 is a side (partially cross-sectional) view showing one embodiment of the present invention, FIG. 4 is an enlarged vertical cross-sectional schematic view showing the inside of the cylinder in the embodiment of FIG. 3, and FIG. A side view (partially cross-sectional) showing one embodiment, FIG. 6 is an enlarged vertical cross-sectional schematic view showing the inside of the cylinder in the embodiment of FIG. 5, and FIG. 7 is a view of the powder in the embodiment of FIG. A partially enlarged perspective view showing a flow path, and FIGS. 8 and 9 are enlarged vertical cross-sectional schematic views showing the inside of a cylinder in still other embodiments of the present invention. 11, 12, 13...processing device, 21a, 21
b... Cover, 22a, 220, 23a, 23b... Flexible joint, 31... Cylindrical container, 31a...
Jacket, 31b, 32c, 33c... Vibration source, 32, 33... Cylindrical body, 32a, 33a
...Inlet of processing gas, 32b, 33b...
... Processing gas outlet, 41a, 42a to 42b, 4
4a...Powder inlet, 41b, 43a to 43d
, 44b...Powder outlet, 51a, 51b, 6
2a, 52b, 53a, 53b... Spring, 62a
~62d, 63a~63d...Powder flow path, 73
a~73c...Gutter-shaped body, 83a~83h...
...Overflow prevention wall, 93a-93c...Weir plate,
103a-103c...Connection route. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6 Figure 7 Figure 8 Figure 9
Claims (1)
振動発生源が具備された略水平設置の筒体の両側にフレ
キシブルジヨイントを介して処理用気体の入口と出口が
接続され、該筒体内には粉体の入口及び出口が適宜接続
された複数個の粉体流路が形成されていて、該粉体流路
に前記処理用気体が流過されるようにして成る粉体の処
理装置。 2 粉体流路が該粉体流路を粉体が順次反対方向へ連続
して流れるように連絡された特許請求の範囲第1項記載
の粉体の処理装置。 3 処理用気体が窒素ガスの如き不活性ガスである特許
請求の範囲第1項又は第2項記載の粉体の処理装置。 4 処理用気体が低温気体である特許請求の範囲第1項
〜第3項のいずれか一つの項記載の粉体の処理装置。[Claims] 1. An inlet and an outlet for processing gas via flexible joints on both sides of a substantially horizontally installed cylinder supported by an elastic body such as a spring and equipped with one to several vibration sources. is connected to the cylindrical body, and a plurality of powder channels are formed in the cylinder body, with powder inlets and outlets connected as appropriate, and the processing gas is allowed to flow through the powder channels. Powder processing equipment consisting of 2. The powder processing apparatus according to claim 1, wherein the powder flow paths are connected so that the powder sequentially flows in opposite directions through the powder flow paths. 3. The powder processing apparatus according to claim 1 or 2, wherein the processing gas is an inert gas such as nitrogen gas. 4. A powder processing apparatus according to any one of claims 1 to 3, wherein the processing gas is a low-temperature gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57178751A JPS6013744B2 (en) | 1982-10-12 | 1982-10-12 | Powder processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57178751A JPS6013744B2 (en) | 1982-10-12 | 1982-10-12 | Powder processing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5969137A JPS5969137A (en) | 1984-04-19 |
| JPS6013744B2 true JPS6013744B2 (en) | 1985-04-09 |
Family
ID=16053949
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57178751A Expired JPS6013744B2 (en) | 1982-10-12 | 1982-10-12 | Powder processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6013744B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000078441A1 (en) * | 1999-06-21 | 2000-12-28 | Sunroute Corporation | Mixing device |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2572731B2 (en) * | 1987-06-22 | 1997-01-16 | 中央化工機株式会社 | Drying equipment for fine powder |
| JP4891611B2 (en) * | 2005-12-27 | 2012-03-07 | 紀伊産業株式会社 | Cosmetic container |
-
1982
- 1982-10-12 JP JP57178751A patent/JPS6013744B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000078441A1 (en) * | 1999-06-21 | 2000-12-28 | Sunroute Corporation | Mixing device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5969137A (en) | 1984-04-19 |
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