JPS6219326B2 - - Google Patents

Info

Publication number
JPS6219326B2
JPS6219326B2 JP56038688A JP3868881A JPS6219326B2 JP S6219326 B2 JPS6219326 B2 JP S6219326B2 JP 56038688 A JP56038688 A JP 56038688A JP 3868881 A JP3868881 A JP 3868881A JP S6219326 B2 JPS6219326 B2 JP S6219326B2
Authority
JP
Japan
Prior art keywords
stirring
hollow
plate
plates
heat transfer
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
Application number
JP56038688A
Other languages
Japanese (ja)
Other versions
JPS57156913A (en
Inventor
Tatsuyuki Kasai
Hitoshi Asakura
Giichi Ueda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tsukishima Kikai Co Ltd
Original Assignee
Tsukishima Kikai Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tsukishima Kikai Co Ltd filed Critical Tsukishima Kikai Co Ltd
Priority to JP3868881A priority Critical patent/JPS57156913A/en
Publication of JPS57156913A publication Critical patent/JPS57156913A/en
Publication of JPS6219326B2 publication Critical patent/JPS6219326B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G33/00Screw or rotary spiral conveyors
    • B65G33/08Screw or rotary spiral conveyors for fluent solid materials
    • B65G33/14Screw or rotary spiral conveyors for fluent solid materials comprising a screw or screws enclosed in a tubular housing
    • B65G33/18Screw or rotary spiral conveyors for fluent solid materials comprising a screw or screws enclosed in a tubular housing with multiple screws in parallel arrangements, e.g. concentric

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Drying Of Solid Materials (AREA)
  • Screw Conveyors (AREA)

Description

【発明の詳細な説明】 本発明は粉粒体や粘着性の高い汚泥などの物質
を撹拌混合しながら加熱又は冷却するのに適した
撹拌伝熱装置の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a stirring heat transfer device suitable for heating or cooling substances such as powder or highly sticky sludge while stirring and mixing them.

従来、ほぼ水平のケーシング内に平行に隔置さ
れた回転軸とこれらの回転軸上に設置された撹拌
板とを含む撹拌移送装置が知られている。また、
このような回転および撹拌板を中空としかつ互に
連通させ、それらの内部に熱交換媒体を通過させ
ることによつて、汚泥や、粉粒体等を撹拌、移送
しながら加熱または冷却を行う装置も公知であ
る。このような熱交換装置は、移送しながら熱交
換を行うことができること、熱効率が高いこと、
単位容積当りの伝熱面積が大きく取れること、一
様な撹拌作用を与えるため物質を均一に加熱また
は冷却することができること、低速回転のため所
要動力が少なく回転翼の摩耗もきわめて少ないこ
と、加熱乾燥装置として用いたときの排気量が少
ないことなど多くの利点を有するため、撹拌型間
接式熱交換装置として広い分野で用いられてい
る。
BACKGROUND OF THE INVENTION Conventionally, stirring and transfer devices are known that include rotating shafts spaced parallel to each other within a substantially horizontal casing and stirring plates installed on these rotating shafts. Also,
A device that heats or cools sludge, powder, etc. while stirring and transporting such rotating and stirring plates, which are hollow and communicate with each other, and a heat exchange medium is passed through them. is also publicly known. Such a heat exchange device can perform heat exchange while transferring, has high thermal efficiency,
It has a large heat transfer area per unit volume, it provides a uniform stirring effect so it can heat or cool the substance uniformly, it rotates at a low speed, so it requires less power and has very little wear on the rotor blades. Since it has many advantages such as a small amount of exhaust gas when used as a drying device, it is used in a wide range of fields as an agitation type indirect heat exchange device.

しかしながら、この種の装置においては、被処
理物質によつては付着現象が著しく、性能の低下
を招いたり、種々のトラブルをひきおこすという
ことが最大の欠点である。この付着現象は回転す
る撹拌板の背面から特に発達して激しくなる。付
着が生じると、熱交換の場合には伝熱速度が低下
するし、撹拌、移送効果も低下する。はなはだし
い場合には、回転軸と撹拌板とが被処理物質で包
まれて丸棒状となり、操作不能になることさえあ
る。従来、このような問題の対策としては次のよ
うな2つの方式があつた。その一つは、軸中心線
に対して垂直に配置した撹拌板間に固定式の掻取
アームを設けることである。一般に、アームはケ
ーシング内壁面あるいは上部カバーに取付けられ
る。しかしながら、この方式では、掻取られた被
処理物質がアームの上に堆積するにつれてアーム
付近での物質の動きがにぶくなり、空間部を生じ
やすいこと、撹拌板間の物質とアームとの当り部
分がいつも同じであるため掻取り効果が部分的で
あり、アームと接触しない部分の物質は掻取り作
用を受けないこと、アームが被処理物質の後方へ
の流れに対する抵抗となること、撹拌板が軸心に
対して垂直であるため移送能力が劣ることなどま
だ多くの問題点がある。もう一つの方式は、軸中
心線に対して垂直に特殊な楔形の翼を取付けるも
のである。一方の軸の翼間に他方の軸の楔形翼の
向きと他方の軸のそれとが向き合うような状態に
取付けてある。しかしながら、この方式において
も、一方の軸の翼間の物質と他方の軸の翼の当り
部分が同じであるため撹拌作用が劣り、装置自体
の伝熱能力が劣るという問題点がある。
However, the biggest drawback of this type of apparatus is that depending on the substance to be treated, the adhesion phenomenon is significant, leading to a decrease in performance and various troubles. This adhesion phenomenon especially develops and becomes more severe from the back side of the rotating stirring plate. If adhesion occurs, the heat transfer rate will be reduced in the case of heat exchange, and the stirring and transfer effects will also be reduced. In extreme cases, the rotating shaft and the stirring plate may become wrapped in the substance to be treated and become round rod-shaped, making them inoperable. Conventionally, there have been two methods to deal with such problems: One of them is to provide a fixed scraping arm between stirring plates arranged perpendicular to the axis centerline. Generally, the arm is attached to the inner wall surface of the casing or the upper cover. However, with this method, as the scraped material to be treated accumulates on the arm, the movement of the material near the arm slows down, which tends to create a space, and the contact area between the material between the stirring plates and the arm. is always the same, so the scraping effect is partial, and the material in the area that does not come into contact with the arm is not affected by the scraping action, the arm acts as a resistance to the backward flow of the material to be processed, and the stirring plate There are still many problems such as poor transfer ability because it is perpendicular to the axis. Another method is to install special wedge-shaped wings perpendicular to the axis centerline. The blades of one shaft are installed in such a manner that the wedge-shaped blades of the other shaft face each other. However, even in this method, there are problems in that the material between the blades on one shaft and the contact area between the blades on the other shaft are the same, resulting in poor stirring action and poor heat transfer ability of the device itself.

そこで、上記点に鑑み、被処理物質がケーシン
グ内壁面および撹拌板間に付着するのを有効に防
止することができると共に、熱交換も行うことの
できる構造簡単な上記形式の撹拌移送装置が提供
されたが、該撹拌移送装置において大型加熱装置
とするときには第8図に示す如く軸6に隔置され
た傾斜撹拌板11が傾斜角を一定とするとき、一
枚の撹拌板11の長さが長くなり、単位体積当り
の板表面積は板の長径に反比例して少なくなると
いう不具合な点があつた。
Therefore, in view of the above points, there is provided a stirring transfer device of the above type with a simple structure, which can effectively prevent the substance to be treated from adhering to the inner wall surface of the casing and between the stirring plates, and can also perform heat exchange. However, when the stirring and transfer device is used as a large heating device, the length of one stirring plate 11 is determined when the inclined stirring plates 11 spaced apart from the shaft 6 have a constant angle of inclination as shown in FIG. The problem was that the surface area of the plate per unit volume decreased in inverse proportion to the major axis of the plate.

本発明は上記不具合な点を解消するために、熱
交換媒体を通過させるために中空にした扇形の撹
拌板を複数枚有し、一方の伝熱板をその対応した
軸、または中空軸の長手方向軸線に直角の平面に
対して傾斜させて配置し、他方の撹拌板をほぼ同
じ傾斜角度で一方の撹拌板のほぼ間に配置し、一
方の軸上の各撹拌板を他方の軸上の隣合つた撹拌
板の間に互に部分的に入り込むように隔置し、前
記2軸が協働して回転するとき、前記2軸間に前
記入り込むように隔置した撹拌板とが周期的に増
減する空間を形成するようにしたので、単位容積
当りの板の伝熱表面積をほぼ2倍にすることがで
きて、加熱乾燥装置に使用するときには軸の長さ
をほぼ半分にすることにより装置の製作費用が非
常に低減できる撹拌伝熱装置を提供することを目
的とするものである。
In order to solve the above-mentioned problems, the present invention has a plurality of hollow fan-shaped stirring plates for passing the heat exchange medium, and one heat transfer plate is attached to the corresponding shaft or the longitudinal axis of the hollow shaft. The stirring plates on one axis are arranged at an angle with respect to a plane perpendicular to the direction axis, and the other stirring plate is arranged at approximately the same angle of inclination and approximately between one stirring plate, and each stirring plate on one axis Adjacent stirring plates are spaced so that they partially fit into each other, and when the two shafts rotate together, the stirring plates spaced so that they fit between the two shafts periodically increase and decrease. As a result, the heat transfer surface area of the plate per unit volume can be almost doubled, and when used in a heating dryer, the length of the shaft can be roughly halved, making it possible to reduce the heat transfer surface area of the plate per unit volume. It is an object of the present invention to provide a stirring heat transfer device whose manufacturing cost can be significantly reduced.

以下本発明を図に示す実施例について説明す
る。まず、第1図から第3図を参照すると、熱交
換式撹拌伝熱装置はほぼ水平に設置したケーシン
グ1を有し、該ケーシング1は底側部にジヤケツ
トを有し、比較的長い二軸スクリユーコンベヤ型
のトラフ状容器であつて、傾斜角度調製器2を備
えた支持台3に固定されている。ケーシング1の
両側面および底面と一部の側面をほぼ全面にわた
つて覆つて熱交換用ジヤケツト4が設けてあり、
底面ジヤケツト中央部には補強を兼ねた仕切板5
が長手方向に設けてある。ケーシング1の内部に
は、その長手方向に2本の中空回転軸6,6′が
互に平行に隔置してあり、これらの回転軸はケー
シング1の前後部にある軸受け7,7′によつて
回転自在に支持されている。また、両回転軸6,
6′の前部にはギヤ8,8′が固定してあり、これ
らのギヤ8,8′は互に噛み合つて互に反対方向
に回転するようになつている。回転軸6′にはス
プロケツト9が設けてあり、このスプロケツト9
はチエーン(図示せず)を介して原動機(図示せ
ず)に連結されている。
The present invention will be described below with reference to embodiments shown in the drawings. First, referring to FIGS. 1 to 3, the heat exchange type stirring heat transfer device has a casing 1 installed approximately horizontally, the casing 1 having a jacket on the bottom side, and a relatively long biaxial It is a trough-shaped container of the screw conveyor type, and is fixed to a support base 3 equipped with an inclination angle adjuster 2. A heat exchange jacket 4 is provided to almost entirely cover both sides, the bottom surface, and some side surfaces of the casing 1,
There is a partition plate 5 in the center of the bottom jacket that also serves as reinforcement.
are provided in the longitudinal direction. Inside the casing 1, two hollow rotating shafts 6, 6' are spaced parallel to each other in the longitudinal direction, and these rotating shafts are mounted in bearings 7, 7' at the front and rear of the casing 1. Therefore, it is rotatably supported. In addition, both rotating shafts 6,
Gears 8, 8' are fixed to the front part of 6', and these gears 8, 8' mesh with each other to rotate in opposite directions. A sprocket 9 is provided on the rotating shaft 6', and this sprocket 9
is connected to a prime mover (not shown) via a chain (not shown).

それぞれの回転軸6,6′には、第5図に示す
如くその長手方向に複数の撹拌板が隔置してあ
り、一方の回転軸の撹拌板が他方の回転軸の隣合
つた撹拌板の間に互に隔置されて部分的に入り込
むような回転軸間距離となつている。各撹拌板
は、第3図に示す実施例のように、分割された1
対の平板扇状の中空切欠撹拌板11または11′
からなり、各対の中空撹拌板11,11′は第5
図に示す如く、その一方の撹拌板をその対応した
軸の長手方向軸線に直角の平面に対して傾斜させ
て配置し、他方の撹拌板を一方の撹拌板とほぼ同
じ傾斜方向角で平行移動して、一方の撹拌板のほ
ぼ下に配置されている。このように撹拌板11,
11′を中空軸6,6′に取り付けても、第3図に
示す如く全くはなれているので取り付けに問題は
ない。撹拌板11,11″は第4A図に示すよう
にすべて同一の方向に傾斜していてもよいし、第
4B図に示すように隣合つたものが互に逆の方向
に傾斜していてもよい。また、撹拌板は、図示の
扇形以外の形状をしていてもよいし、断面が図示
のように矩形でなくて、三角形、菱形であつても
よい。図示実施例においては、撹拌板11,1
1′の後縁には、後述するように作用する小さな
楔上げ羽根10が設置してある。
Each rotating shaft 6, 6' has a plurality of stirring plates spaced apart in its longitudinal direction, as shown in FIG. The distance between the rotating axes is such that they are spaced apart from each other and partially penetrate into each other. Each stirring plate is divided into 1 parts as in the embodiment shown in FIG.
A pair of flat fan-shaped hollow notched stirring plates 11 or 11'
Each pair of hollow stirring plates 11, 11' has a fifth
As shown in the figure, one of the stirring plates is arranged inclined with respect to a plane perpendicular to the longitudinal axis of its corresponding shaft, and the other stirring plate is moved in parallel at approximately the same angle of inclination as one of the stirring plates. It is located almost under one of the stirring plates. In this way, the stirring plate 11,
Even if 11' is attached to the hollow shafts 6, 6', there is no problem with the attachment since they are completely separated as shown in FIG. The stirring plates 11, 11'' may all be inclined in the same direction as shown in FIG. 4A, or adjacent ones may be inclined in opposite directions as shown in FIG. 4B. In addition, the stirring plate may have a shape other than the fan shape shown in the figure, and the cross section may not be rectangular as shown in the figure, but may be triangular or diamond-shaped.In the illustrated embodiment, the stirring plate 11,1
At the trailing edge of 1' there is a small wedge-up vane 10 which operates as described below.

ケーシング1の上面には交互にカバー12,1
2′が設置してあり、各カバー12,12′はパツ
キン(図示せず)を介してケーシング1と係合
し、それを密閉している。カバー12′は把手1
3を備えており、必要に応じて取外すことができ
るようになつている。最前部のカバー12には、
被処理物質供給口14が設けてあり、ケーシング
1の後底部には排出口15が設けてある。ケーシ
ング1内の排出口直前部には、高さ調節可能なせ
き16が設けてあり、ケーシング内の物質保持量
が調節できるようになつている。供給口、中央部
カバー12および排出口15には、それぞれ、搬
送ガスの送入、排出配管(図示せず)の接続口1
7,17′,17が設けてあり、被処理物質に
応じて並流式、向流式または並向流式の蒸気搬出
作業を行なえるようになつている。
Covers 12, 1 are arranged alternately on the upper surface of the casing 1.
2' are installed, and each cover 12, 12' engages with the casing 1 via a gasket (not shown) to seal it. Cover 12' is handle 1
3 and can be removed if necessary. The front cover 12 has
A material supply port 14 is provided, and a discharge port 15 is provided at the rear bottom of the casing 1. A height-adjustable weir 16 is provided in the casing 1 immediately in front of the discharge port, so that the amount of substance held in the casing can be adjusted. The supply port, the central cover 12, and the discharge port 15 each have a connection port 1 for supplying and discharging a carrier gas (not shown).
7, 17', and 17 are provided, so that a cocurrent type, countercurrent type, or cocurrent type of steam discharge operation can be performed depending on the substance to be treated.

ジヤケツト4には、熱媒体流入、流出配管(図
示せず)の連結口18,18′,18″が設けてあ
り、回転軸の最前、後部には、熱媒体流入、流出
配管(図示せず)の静止連結口19,19′が設
けてある。これらの連結口19,19′は、加熱
または冷却の操作や熱媒体の違いに応じて使い分
けられるようになつている。回転軸と静止連結口
との間には、圧力回転接手20,20′が設けて
ある。さらに、中空回転軸内部と中空撹拌板内部
とは連結管21,21′を通して連通しており、
熱媒体が流入流出できるようになつている。
The jacket 4 is provided with connecting ports 18, 18', 18'' for heat medium inflow and outflow pipes (not shown), and the heat medium inflow and outflow pipes (not shown) are provided at the front and rear of the rotating shaft. ) are provided with stationary connection ports 19, 19'.These connection ports 19, 19' can be used appropriately depending on the heating or cooling operation and the difference in heat medium. Pressure rotary joints 20 and 20' are provided between the opening and the hollow rotating shaft.Furthermore, the inside of the hollow rotating shaft and the inside of the hollow stirring plate are communicated through connecting pipes 21 and 21'.
The heat medium can flow in and out.

上記構成の装置において、被処理物質を温水に
よつて並向流式に加熱乾燥する場合について説明
する。まず、傾斜角度調製器にて最適な傾斜角度
に本体を設置し2つの回転軸6,6′をスプロケ
ツト9およびギヤ8,8′を介して原動機によつ
て静かに回転させる。各軸6,6′は、第3図に
示す如く矢印のように反対方向に回転している。
ジヤケツト4には所定温度の温水が連結口18か
ら送り込まれ、連結口18′から排出される。こ
の場合、連結口18″はブロー配管接続口として
用いられる。一方、回転軸6,6′および撹拌板
11,11′用の温水は、後方の静止連結口1
9′および圧力回転接手20′を通して送り込ま
れ、連絡管21,21′を経て各撹拌板11,1
1′内を通過しながら前方へ流れ、軸前部の圧力
回転接手20および静止連結口19を通して排出
される。
In the apparatus having the above configuration, a case will be described in which a substance to be treated is heated and dried using hot water in a parallel and countercurrent manner. First, the main body is set at an optimal inclination angle using an inclination angle adjuster, and the two rotating shafts 6, 6' are gently rotated by the prime mover via the sprocket 9 and gears 8, 8'. Each shaft 6, 6' rotates in opposite directions as indicated by the arrows, as shown in FIG.
Hot water at a predetermined temperature is fed into the jacket 4 through the connection port 18, and is discharged through the connection port 18'. In this case, the connection port 18'' is used as a blow pipe connection port.On the other hand, the hot water for the rotating shafts 6, 6' and the stirring plates 11, 11' is supplied to the stationary connection port 1 at the rear.
9' and pressure rotary joint 20', and is fed through connecting pipes 21, 21' to each stirring plate 11, 1.
It flows forward while passing through 1' and is discharged through the pressure rotary joint 20 and stationary connection port 19 at the front of the shaft.

被処理物質は供給口14からケーシング1内に
連続的に定量供給され、撹拌板11,11′の後
縁に設ける掻上げ羽根10の運動によつてケーシ
ング1内部に掻き込まれ、撹拌板11,11′の
回転によつて撹拌され、該板の送りピツチまたは
後述する物質供給の押出作用によつて後方へ移送
される。移送中、物質はジヤケツト4、中空軸
6,6′および中空撹拌板11,11′内を流れる
温水と熱交換を行なつて加熱され、物質中の水分
がケーシング内で蒸発する。乾燥した物質はせき
16からオーバーフローして排出口15を通して
排出される。搬送ガスは接続口17,17″から
送り込まれ、ケーシング1内の物質の上方を流
れ、物質から蒸発した蒸気を伴つて接続口17′
を通つて排出される。
The substance to be treated is continuously supplied in a fixed amount into the casing 1 from the supply port 14, and is scraped into the inside of the casing 1 by the movement of the scraping blades 10 provided at the rear edges of the stirring plates 11 and 11'. , 11', and is transported rearward by the feed pitch of the plate or the extrusion action of the material supply described later. During the transfer, the substance is heated through heat exchange with the hot water flowing through the jacket 4, the hollow shafts 6, 6' and the hollow stirring plates 11, 11', and the moisture in the substance evaporates within the casing. The dried material overflows from the weir 16 and is discharged through the outlet 15. The carrier gas is fed through the connections 17, 17'' and flows over the material in the casing 1, taking with it the vapor evaporated from the material into the connection 17'.
is discharged through.

本発明による撹拌板11,11′において付着
物質の自動清掃作用を説明する。回転軸上に撹拌
板が傾斜して設けてあるため、撹拌板11,1
1′は半回転するごとに変位して、周期的な首振
り運動を行ない、ケーシング1の内壁面に付着す
る物質を軸線方向に掻落し、自動的かつ周期的に
除去する。また、撹拌板間に付着する物質は次の
ようにして除去される。第6図および第7図を参
照して、軸6に対する軸6′の相対的な運動を考
えると、軸6′の撹拌板11′は軸6の撹拌板11
間で首振り運動を行ない、それにつれて撹拌板1
1と11′で区切られた空間部の容積が第6図の
Aから第7図のBのように周期的に縮小、拡大を
繰返す。第6図および第7図に示す如く、撹拌板
間に物質が捕捉されていれば、縮小時に圧縮作用
を受けて撹拌板11,11′の外周縁を越えて排
除され拡大時には圧縮後に生じた空間部に新して
被処理物質が落込んで伝熱撹拌作用を受ける。こ
のような作用は汚泥などには特に有効であつて、
本発明により回転軸には一方の撹拌と他方の撹拌
板とを軸周に沿つて平行に設置したので、単位容
積当りの板表面積が2倍にすることができ、伝熱
撹拌を有効に行うことができる。
The automatic cleaning action of adhering substances on the stirring plates 11, 11' according to the present invention will be explained. Since the stirring plate is inclined on the rotating shaft, the stirring plate 11,1
1' is displaced every half rotation to perform a periodic swinging motion to scrape off substances adhering to the inner wall surface of the casing 1 in the axial direction and automatically and periodically remove them. Further, substances adhering between the stirring plates are removed in the following manner. 6 and 7, considering the relative movement of the shaft 6' with respect to the shaft 6, the stirring plate 11' of the shaft 6' is
The stirring plate 1 performs an oscillating motion between the
The volume of the space divided by 1 and 11' is repeatedly reduced and expanded periodically from A in FIG. 6 to B in FIG. 7. As shown in Figures 6 and 7, if the substance is trapped between the stirring plates, it will be removed beyond the outer periphery of the stirring plates 11, 11' due to the compression action during contraction, and will be removed after compression during expansion. A new substance to be treated falls into the space and is subjected to heat transfer and stirring action. This effect is particularly effective against sludge, etc.
According to the present invention, one stirring plate and the other stirring plate are installed on the rotating shaft in parallel along the circumference of the shaft, so the surface area of the plate per unit volume can be doubled, and heat transfer stirring can be performed effectively. be able to.

また、撹拌板間隔、送りや戻しのピツチの有
無、撹拌板の傾斜角度等は本発明の範囲内で自由
に選定できることは明らかである。
Furthermore, it is clear that the spacing between the stirring plates, the presence or absence of feed and return pitches, the angle of inclination of the stirring plates, etc. can be freely selected within the scope of the present invention.

以上説明したように本発明の撹拌伝熱装置は、
回転軸に隔置された撹拌板を分割し、一方の撹拌
板を軸の長手方向軸線に対して傾斜させ、他方の
撹拌板を一方の撹拌板とほぼ同じ傾斜角度で平行
移動し、かつ一方の撹拌板の下に配置して、一方
の軸上の各撹拌板が他方の軸上の隣合つた撹拌板
間に互に部分的に入り込むように隔置したので、
単位容積当りの撹拌板の表面積をほぼ2倍にする
ことができ、撹拌作用も改良されて、加熱乾燥装
置に使用するときには軸の長さがほぼ半分になる
ので装置の製作費用が非常に低減できるという優
れた効果がある。
As explained above, the stirring heat transfer device of the present invention has the following features:
The stirring plates spaced apart on the rotating shaft are divided, one stirring plate is tilted with respect to the longitudinal axis of the shaft, the other stirring plate is moved in parallel at approximately the same angle of inclination as one stirring plate, and one stirring plate is The stirrer plates were placed under the stirrer plates and spaced apart so that each stirrer plate on one shaft was partially inserted between the adjacent stirrer plates on the other shaft.
The surface area of the stirring plate per unit volume can be almost doubled, the stirring action has been improved, and when used in a heating drying device, the length of the shaft can be roughly halved, greatly reducing the manufacturing cost of the device. There is an excellent effect that can be done.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の熱交換式撹拌装置の平面図、
第2図は第1図の側面図、第3図は第2図の−
線に沿つた拡大横断面図、第4A図は回転軸上
に取付けた撹拌板の傾斜状態の一例を示す概略断
面図、第4B図は第4A図と同様な撹拌板の傾斜
状態の別の例を示す図、第5図は撹拌板の概略側
面図、第6図および第7図は、撹拌板間の空間部
の容積が変化する状況を説明するための拡大図、
第8図は従来の撹拌板の概略側面図である。 1……ケーシング、4……ジヤケツト、6,
6′……中空軸、11,11′……撹拌板、12,
12′……カバー、14……供給口、15……排
出口。
FIG. 1 is a plan view of the heat exchange type stirring device of the present invention;
Figure 2 is a side view of Figure 1, and Figure 3 is a side view of Figure 2.
FIG. 4A is a schematic sectional view showing an example of an inclined state of the stirring plate mounted on the rotating shaft, and FIG. 4B is an enlarged cross-sectional view along the line, FIG. A diagram showing an example, FIG. 5 is a schematic side view of the stirring plate, FIGS. 6 and 7 are enlarged views for explaining the situation where the volume of the space between the stirring plates changes,
FIG. 8 is a schematic side view of a conventional stirring plate. 1... Casing, 4... Jacket, 6,
6'...Hollow shaft, 11, 11'...Stirring plate, 12,
12'...cover, 14...supply port, 15...discharge port.

Claims (1)

【特許請求の範囲】 1 入口と出口を有するほぼ水平方向のケーシン
グと、該ケーシングの外周にジヤケツトを有し、
かつその長手方向に回転自在に平行に隔置された
少なくとも2本の中空軸と、該各中空軸上にその
長手方向に隔置される前記中空軸の内部に連通し
た複数の中空の撹拌板と、前記中空軸および中空
の撹拌板の内部に熱の交換媒体を通過させる装置
とを含む撹拌伝熱装置において、前記中空の撹拌
板を分割し、一方の撹拌板をその対応した中空軸
の長手方向軸線に直角の平面に対して傾斜させて
配置し、他方の撹拌板をほぼ同じ傾斜角度で一方
の撹拌板の間に互に部分的に入り込むように隔置
し、さらの前記両軸を互に異つた向きで回転させ
る駆動装置を備えていることを特徴とする撹拌伝
熱装置。 2 特許請求の範囲第1項に記載の撹拌伝熱装置
において、1本の中空軸上の前記中空撹拌板が全
て同一方向に傾斜していることを特徴とする撹拌
伝熱装置。 3 特許請求の範囲第1項に記載の撹拌伝熱装置
において、前記中空撹拌伝熱装置の隣合つたもの
が互に逆の方向に傾斜していることを特徴とする
撹拌伝熱装置。
[Claims] 1. A substantially horizontal casing having an inlet and an outlet, and a jacket around the outer periphery of the casing,
and at least two hollow shafts spaced parallel to each other so as to be rotatable in the longitudinal direction thereof, and a plurality of hollow stirring plates communicating with the interiors of the hollow shafts spaced apart in the longitudinal direction on each of the hollow shafts. and a device for passing a heat exchange medium through the hollow shaft and the hollow stirring plate, wherein the hollow stirring plate is divided and one stirring plate is connected to the corresponding hollow shaft. one of the stirring plates is spaced apart from the other stirring plate at approximately the same angle of inclination so as to partially fit between the two stirring plates; A stirring heat transfer device characterized in that it is equipped with a drive device that rotates in different directions. 2. The stirring heat transfer device according to claim 1, wherein the hollow stirring plates on one hollow shaft are all inclined in the same direction. 3. The stirring heat transfer device according to claim 1, wherein adjacent hollow stirring heat transfer devices are inclined in opposite directions.
JP3868881A 1981-03-19 1981-03-19 Stirring conveyor Granted JPS57156913A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3868881A JPS57156913A (en) 1981-03-19 1981-03-19 Stirring conveyor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3868881A JPS57156913A (en) 1981-03-19 1981-03-19 Stirring conveyor

Publications (2)

Publication Number Publication Date
JPS57156913A JPS57156913A (en) 1982-09-28
JPS6219326B2 true JPS6219326B2 (en) 1987-04-28

Family

ID=12532228

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3868881A Granted JPS57156913A (en) 1981-03-19 1981-03-19 Stirring conveyor

Country Status (1)

Country Link
JP (1) JPS57156913A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01151539U (en) * 1988-03-31 1989-10-19

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62157113A (en) * 1985-12-28 1987-07-13 Nichinan Sangyo Kk Self-cleaning method and device for conveyance mixer
DE3721533C1 (en) * 1987-06-30 1988-10-06 Lothar Dipl-Ing Teske Device for conveying and mixing a bulk material, for example
JP2006090590A (en) * 2004-09-22 2006-04-06 Hitachi Zosen Corp Powder and granular material heating device
JP4585960B2 (en) * 2005-11-18 2010-11-24 メタウォーター株式会社 Oil bath sludge dryer
JP6121719B2 (en) * 2013-01-07 2017-04-26 水ing株式会社 Sludge drying equipment
CN117468299B (en) * 2023-10-31 2024-05-17 临沂市玉泉沥青有限公司 Automatic asphalt conveying equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50136856U (en) * 1974-04-26 1975-11-11
JPS6035440Y2 (en) * 1979-11-19 1985-10-21 株式会社東芝 small air purifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01151539U (en) * 1988-03-31 1989-10-19

Also Published As

Publication number Publication date
JPS57156913A (en) 1982-09-28

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