JPH0334634Y2 - - Google Patents

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Publication number
JPH0334634Y2
JPH0334634Y2 JP1982148099U JP14809982U JPH0334634Y2 JP H0334634 Y2 JPH0334634 Y2 JP H0334634Y2 JP 1982148099 U JP1982148099 U JP 1982148099U JP 14809982 U JP14809982 U JP 14809982U JP H0334634 Y2 JPH0334634 Y2 JP H0334634Y2
Authority
JP
Japan
Prior art keywords
screw
main body
rotating shaft
dried
device main
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
JP1982148099U
Other languages
Japanese (ja)
Other versions
JPS5952392U (en
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
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Priority to JP14809982U priority Critical patent/JPS5952392U/en
Publication of JPS5952392U publication Critical patent/JPS5952392U/en
Application granted granted Critical
Publication of JPH0334634Y2 publication Critical patent/JPH0334634Y2/ja
Granted legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Description

【考案の詳細な説明】[Detailed explanation of the idea] 【産業上の利用分野】[Industrial application field]

本考案は、滞留時間を自由に調節できるスクリ
ユー内蔵形の乾燥等の連続処理装置に関するもの
である。
The present invention relates to a continuous processing device for drying, etc., which has a built-in screw and can freely adjust the residence time.

【従来の技術】[Conventional technology]

従来、各種の連続乾燥機が開発市販されてい
る。これらのうち機械的撹拌または気流撹拌を行
うものは、微粉末の粒子飛散が避けられず、気密
性を保持することが困難であり、薄膜式のもの
は、滞留時間の調節ができない等それぞれ欠点を
有している。 ところで、放射性物質等の有害物質を含む含水
物を乾燥する連続乾燥装置は、有害粉塵が排ガス
に伴われて、大気中に飛散するのを防止するた
め、気密性がよく、かつ装置内での粉塵発生がな
いことが要求される。また、同一装置によつて
色々な物性の有害物質含有物を乾燥することが多
く、滞留時間は、被乾燥物の物性に対して自由に
調節できることが望まれている。
Conventionally, various continuous dryers have been developed and commercially available. Among these, those that use mechanical stirring or air current stirring cannot avoid scattering of fine powder particles, making it difficult to maintain airtightness, while thin film types have drawbacks such as the inability to adjust residence time. have. By the way, continuous drying equipment that dries water-containing materials containing harmful substances such as radioactive materials has good airtightness and is designed to prevent harmful dust from scattering into the atmosphere along with the exhaust gas. No dust generation is required. In addition, substances containing harmful substances having various physical properties are often dried using the same apparatus, and it is desired that the residence time can be freely adjusted depending on the physical properties of the material to be dried.

【考案が解決しようとする問題点】[Problem that the invention attempts to solve]

これらの問題を一部解決するものとして、縦型
円筒形の炉体に、この炉体の縦軸まわりに直交す
る金属製螺旋体(水平形スクリユー)の炉床を設
置し、その螺旋体の回転速度を制御することによ
り滞留時間を調節して被乾燥物を炉床の上を順次
降下させつつ乾燥させる装置がある。この装置
は、気密性を有し粉塵の飛散が少ないという長所
がある。しかし、被乾燥物が汚泥等の湿潤物のよ
うな滑りの悪い物を対象とした装置の場合は、炉
床に付着して移動しないのを防止するために上記
螺旋体のピツチを大きくしなければならないが、
この装置で滑りの良い物を処理するとすぐに滑動
し滞留時間の制御ができない。逆に、上記螺旋体
のピツチを小さくしたものは、上記のような滑り
の悪い物が移動せず、結局上述した同一装置によ
つて被処理物の物性に応じて滞留時間を調節でき
ないという問題点があつた。このため、上記従来
のいずれの連続乾燥装置も、有害物質を含む含水
物の連続乾燥装置に対して要求される条件のすべ
てを同時に満たすことはできず、上記目的の連続
乾燥装置としてはいずれも不適当であつた。 本考案は上記の事情に鑑み、滞留時間が自由に
調節できるスクリユー内蔵形の乾燥等の連続処理
装置を提供することを目的とする。
To partially solve these problems, a hearth made of a metal spiral (horizontal screw) is installed in a vertical cylindrical furnace body, and the hearth is made of a metal spiral (horizontal screw) that is perpendicular to the vertical axis of the furnace body. There is a device that dries the material to be dried while lowering it sequentially over the hearth by controlling the residence time. This device has the advantage of being airtight and causing little dust to scatter. However, in the case of a device that targets drying materials that are not slippery, such as wet materials such as sludge, the pitch of the spiral body must be increased to prevent the material from adhering to the hearth and not moving. It won't be, but
When this device is used to process slippery materials, it immediately slides and the residence time cannot be controlled. On the other hand, when the pitch of the spiral body is made smaller, the problem is that the non-slippery substances described above cannot be moved, and the residence time cannot be adjusted according to the physical properties of the object to be treated using the same device as described above. It was hot. For this reason, none of the conventional continuous drying devices mentioned above can simultaneously satisfy all of the conditions required for continuous drying devices for water-containing materials containing harmful substances, and none of them can be used as continuous drying devices for the above purpose. It was inappropriate. In view of the above circumstances, it is an object of the present invention to provide a continuous processing apparatus for drying, etc. with a built-in screw, in which the residence time can be freely adjusted.

【問題点を解決するための手段】[Means to solve the problem]

このため、この本考案の乾燥等の連続処理装置
は、竪型円筒形の装置本体と、この装置本体の円
筒軸線に沿つて設けられて回転軸と、この回転軸
に内縁が取り付けられ、外縁が上記円筒形の装置
本体の内周面に近接または接触するスクリユー
と、上記回転軸を上記スクリユーの上端から下端
に向かうねじり方向と逆の方向に回転駆動する駆
動機構と、上記円筒形の装置本体の外周面に設け
た加熱手段とを備え、上記スクリユーと上記回転
軸の軸線を含む平面とが交差する仮想線を内縁か
ら外縁に行くに従い下方に向かうように傾斜させ
た(すなわち、装置本体の半径方向における上記
スクリユーの螺旋面を、回転軸に対して下方に傾
斜させた)構成とする。 なお、以下の説明においては、上記スクリユー
を傾斜形スクリユーと称す。
Therefore, the continuous processing device for drying, etc. of the present invention has a vertical cylindrical device body, a rotating shaft provided along the cylindrical axis of the device body, an inner edge attached to the rotating shaft, and an outer edge attached to the rotating shaft. a screw that is close to or in contact with the inner circumferential surface of the cylindrical device main body; a drive mechanism that rotates the rotating shaft in a direction opposite to the twisting direction of the screw from the upper end to the lower end; and the cylindrical device a heating means provided on the outer circumferential surface of the main body, and an imaginary line where the screw intersects with a plane including the axis of the rotating shaft is inclined downward as it goes from the inner edge to the outer edge (i.e., The helical surface of the screw in the radial direction is inclined downward with respect to the rotation axis. In the following description, the screw described above will be referred to as an inclined screw.

【作用】[Effect]

傾斜形スクリユーの螺旋面に乗せられた被乾燥
物等の物体は、傾斜形スクリユーの螺旋面の半径
方向の傾斜形状と回転によつて、装置本体の円筒
壁内周面(以下単に内周面と記す)に寄り、内周
面に接しながら、傾斜形スクリユーの螺旋面に乗
つて回動する。 すなわち、スクリユーの螺旋面が半径方向に傾
斜していることから、スクリユー面上の物体は該
スクリユーの外周部(装置本体の円筒壁内周面)
に厚く分布し、従来の前記水平形スクリユーに比
べ、円筒壁内周面の物体との接触面積は極めて大
きくなり、スクリユーが回転したときに、スクリ
ユー面上の物体を内周壁との摩擦力によつて現在
位置に止めるように作用し、スクリユーの抜け
(すなわち物体の滑り)が良くなるので、水平ス
クリユーでは大きなピツチにしないと落下しない
湿潤物のような滑りの悪い物でも、スクリユーの
ピツチを大きくせずに移動させることができるよ
うになる。 このスクリユーの回転によつて発生する内周面
との摩擦力と、物体の重力によつて、内周面に接
しながら、物体は傾斜形スクリユーの上面に沿つ
て次第に下方に降下する。この降下過程におい
て、物体は内周面より熱を受け、連続的に下方に
移動する。 この場合、螺旋面上の物体の降下速度は、傾斜
形スクリユーの回転速度に対して、比例的に変化
する。したがつて物体の装置本体内における滞留
時間は、傾斜形スクリユーの回転速度を調節する
ことによつて、自由に調節出来るとともに、傾斜
形スクリユーの螺旋面が半径方向に傾斜している
ので、水平スクリユーでは大きなピツチにしない
と落下しないものでも、小さなピツチで落下でき
る。また、滑りの良い物もスクリユーのピツチ
(スクリユーの進み角)を大きくせずに済むので、
かつてに移動することがなく、滑りの悪い物も滑
りの良い物もスクリユーの回転数を変えることに
よつて滞留時間を容易かつ自由に調節できる。 さらに物体は、傾斜形スクリユーの螺旋面を転
動滑り降りるので自由表面積が大きいとともに、
螺旋面が半径方向に傾斜しているので伝熱面とし
ての内周面と物体との接触面積が大きくなり、有
効に熱が伝えられる。 また、水平形スクリユーにおける半径方向の位
置による物体の降下速度の差異(螺旋スクリユー
は進み角が内周部では大きく、外周部になるほど
小さくなることによる)によつて生じる物体の滞
留時間の不均一を、スクリユーの螺旋面が半径方
向に傾斜していることによつて、大部分の物体が
スクリユーの外周部(装置本体の円筒壁内周面)
にあるので、少なくなる。
The object to be dried, such as the material to be dried, placed on the helical surface of the inclined screw is transported to the inner circumferential surface of the cylindrical wall (hereinafter simply referred to as the inner circumferential surface) of the apparatus main body due to the radial inclined shape and rotation of the helical surface of the inclined screw. ) and rotates on the spiral surface of the inclined screw while contacting the inner peripheral surface. That is, since the helical surface of the screw is inclined in the radial direction, objects on the screw surface are located at the outer circumference of the screw (inner circumferential surface of the cylindrical wall of the main body of the device).
The area of contact with the inner peripheral surface of the cylindrical wall is extremely large compared to the conventional horizontal screw, and when the screw rotates, the object on the screw surface is subjected to frictional force with the inner peripheral wall. This acts to stop the screw at the current position, and improves the screw's slippage (that is, the object's slippage), so it is possible to hold the screw at its pitch even if it is a wet object or other non-slippery object that would not fall with a horizontal screw unless it is made at a large pitch. You will be able to move it without making it bigger. Due to the frictional force with the inner circumferential surface generated by the rotation of the screw and the gravity of the object, the object gradually descends downward along the upper surface of the inclined screw while contacting the inner circumferential surface. During this descending process, the object receives heat from the inner circumferential surface and continuously moves downward. In this case, the descending speed of the object on the spiral surface changes proportionally to the rotational speed of the inclined screw. Therefore, the residence time of the object within the device main body can be freely adjusted by adjusting the rotation speed of the inclined screw, and since the spiral surface of the inclined screw is inclined in the radial direction, With Screw, even objects that cannot fall unless they are made in a large pitch can be dropped in a small pitch. In addition, since there is no need to increase the screw pitch (advance angle of the screw) if the material is slippery,
The retention time of objects that have never moved, whether they are slippery or slippery, can be easily and freely adjusted by changing the rotational speed of the screw. Furthermore, since the object rolls and slides down the spiral surface of the inclined screw, the free surface area is large and
Since the spiral surface is inclined in the radial direction, the contact area between the inner circumferential surface as a heat transfer surface and the object is increased, and heat is effectively transferred. In addition, the object's residence time is uneven due to the difference in the descending speed of the object depending on the radial position in the horizontal screw (this is because the advance angle of the spiral screw is large at the inner periphery and becomes smaller toward the outer periphery). Because the spiral surface of the screw is inclined in the radial direction, most of the objects are located on the outer periphery of the screw (inner periphery of the cylindrical wall of the main body of the device).
, so it will be less.

【実施例】【Example】

以下本考案を図面を参照して説明する。 第1図は、本考案の装置を乾燥装置に使用した
場合の一実施例を示すもので、図中符号1は、円
筒状の装置本体である。装置本体1の上部には、
密閉蓋2が設けられ、下方はコーン状部3となつ
ている。このコーン状部3の下端には、乾燥物を
排出する排出バルブ3aが設けられている。また
装置本体1の円筒部の中心には、上記密閉蓋2を
貫通して回転軸4が設けられている。この回転軸
4は、装置本体1内に設けられ回転軸4の下端を
支持する下部軸受4aと、密閉蓋2に設けられた
上部軸受4bによつて回動自在に保持されてい
る。 また、上記回転軸4にはスクリユー5が取付け
られている。このスクリユー5は、内縁5aが上
記回転軸4の外周に固定され、外縁5bは上記装
置本体1の内周面が沿つて近接して位置してい
る。また、上記回転軸4の軸線を含む平面と、ス
クリユー5の螺旋面と交わる仮想線、すなわち、
装置本体1の半径方向における螺旋面は、回転軸
4に対して下方に傾斜している(傾斜形スクリユ
ー)。 また、装置本体1の円筒状部の側面上部には、
水蒸気の排出管6が取付けられている。この排出
管6の先端には、水蒸気凝縮器7が設けられてい
る。また、上記回転軸4には、傾斜形スクリユー
5の上端から下方に向うねじれ方向と逆の方向に
回転軸4を回転駆動させる可変回転駆動機構8が
設けられている。また、上記密閉蓋2の上部に
は、被乾燥物を装置本体1内に供給する供給口9
が設けられている。この供給口9には、スクリユ
ーフイーダ10の一端が連結され、スクリユーフ
イーダ10の他端には、被乾燥物ホツパ11が設
けられている。また装置本体1の外周にはジヤケ
ツト12が設けられている。このジヤケツト12
には、熱媒タンク12aにおいて加熱された熱媒
流体(温水、カネクロール[商品名]、ダウサム
[商品名]等)が、熱媒循環ポンプ12bによつ
て循環されるようになつている。 次に上記のように構成された乾燥機の操作方法
を説明する。 操作は、次の手順によつて行なわれる。 1)先ず回転軸4を駆動し傾斜形スクリユー5を
回転せしめる。2)ジヤケツト12に熱媒流体を
循環させ、装置本体1の内部を加熱する。3)ス
クリユーフイーダ10を駆動して、ホツパ11に
貯留されている被乾燥物を供給口9より傾斜形ス
クリユー5の上端面に供給する。以上の操作によ
り、被乾燥物は連続乾燥される。 上記操作により傾斜形スクリユー5の螺旋面に
乗せられた被乾燥物は、傾斜形スクリユー5の螺
旋面の半径方向の傾斜形状と回転によつて、装置
本体1の内周面に寄り、内周面に接しながら、傾
斜形スクリユー5の螺旋面に乗つて回動する。こ
の回動によつて発生する内周面との摩擦力と、被
乾燥物の重力とによつて、内周面に接しながら、
傾斜形スクリユー5の上面に沿つて次第に下方に
降下する。この降下過程において、被乾燥物は熱
媒流体によつて加熱されている内周面および熱交
換片の役割をしている傾斜形スクリユー5より熱
を受けて水分が蒸発し、被乾燥物は乾燥する。 上記傾斜形スクリユー5の回転速度が遅い場合
には、上記のような状態で乾燥される。回転速度
が早くなると、被乾燥物は内周面に押しつけられ
て一部が付着し、回動する傾斜形スクリユー5の
外縁5bに掻き落とされるようになる。通常傾斜
形スクリユー5の回転速度は、毎時数回転程度の
遅い速度が用いられる。この場合、被乾燥物の降
下速度は、傾斜形スクリユー5の回転速度に対し
て、比例的に変化する。したがつて被乾燥物の装
置本体1内における滞留時間は、傾斜形スクリユ
ー5の回転速度を調節することによつて、自由に
調節出来るとともに、傾斜形スクリユーの螺旋面
が半径方向に傾斜しているので、水平スクリユー
では大きなピツチにしないと落下しないもので
も、小さなピツチで落下出来、装置を小型化する
ことができる。 また装置本体1は、簡単な構造を有しているの
で容易に気密性を保持することができる。さらに
被乾燥物は、傾斜形スクリユー5の螺旋面を転動
滑り降りるので自由表面積が大きい。また螺旋面
が半径方向に傾斜しているので伝熱面としての内
周面と被乾燥物との接触面積が大きくなり、有効
に伝熱面を利用できる。さらに、撹拌が行なわれ
ず、間接加熱によつて受熱するので、微粉末の粒
子が飛散することも少ない。なお、発生した水蒸
気は、排出管6により水蒸気凝縮器7に導かれて
冷却され凝縮分離される。また、乾燥物は、排出
バルブ3aにより外部に取出される。 上記加熱手段は、装置本体1の外周面に設けら
れたジヤケツト12にスチームや温水等の熱媒流
体を循環させるものであるが、この加熱手段の代
わりに、外周面に電気的加熱器、例えば抵抗加
熱、低周波誘導加熱、高周波誘導加熱、遠赤外線
加熱等の加熱手段を設けて加熱してもよい。ま
た、上記ジヤケツト12に循環する熱媒流体によ
る加熱とともに、回転軸4および傾斜形スクリユ
ー5を中空として、適宜熱媒経路を設け、熱媒流
体を流して被乾燥物からの水分蒸発を促進せしめ
ることも出来る。さらに、熱風を装置本体下部か
ら吹込んで乾燥せしめてもよい。この際熱風のみ
による加熱によつて十分乾燥できるが、上記間接
加熱手段と併用すれば、水蒸気分圧が低下して水
分蒸発が促進され少量の風量で乾燥効果が高ま
り、粉塵の発生も少なく有利である。また装置本
体1内を凝縮器7を介して減圧状態に保持するこ
とも乾燥が速まり有効である。 また、上記説明においては、単一の傾斜形スク
リユーについて述べた。しかし、取扱う被乾燥物
によつて物性は種々変化し、また乾燥される過程
においても含水量が減少するのに従つて物性が変
化する。傾斜形スクリユー5はこれ等に対応する
ため種々の形状のものが用いられる。 第2図は、傾斜形スクリユー5の下方のピツチ
13を小さくしたものである。この場合、含水し
て流れの悪い被乾燥物が乗る傾斜形スクリユー5
の上部はピツチ13を大きくしてもよいが、水分
が減少して流れ易くなると降下速度が早くなる。
これを防止するため、ピツチ13を下方に行くに
従つて小さくしたものである。同様な目的で、第
3図に示すようにスクリユー14の上段部を傾斜
形スクリユー5とし、これに連続して下方を回転
軸4の軸線を含む平面とスクリユーの螺旋面とが
交わる仮想線が水平となつている水平形スクリユ
ー15としてもよい。 第4図は、回転軸4の全長にわたつて連続した
傾斜形スクリユー5を設けず、複数の傾斜形スク
リユー5をスペーサ16を介在させて不連続に回
転軸4に取付けた傾斜形スクリユー5の例であ
る。この場合、被乾燥物の物性および乾燥過程に
おける物性の変化によつて、前記水平形スクリユ
ー15と組合せたり、ピツチ、長さを適宜選んで
回転軸4に取付ける。このようにすると、被乾燥
物はスクリユー14上では内周面とスクリユー1
4の回転による摩擦力と、被乾燥物の重力による
スクリユー14の螺旋面の流れによつて下方に転
動降下するが、スペーサ16が介在する不連続部
分でさらに落下撹拌され乾燥効率がよくなる。 第5図a,bは傾斜形スクリユー5の内周面に
当接する外縁5bを、傾斜形スクリユー5の半径
方向に設けた長孔17aを有するピース17によ
つて形成したものである。ピース17は、装置本
体1の半径より小さい小スクリユー18の外縁に
ボルト、ナツト18aによつて長孔を通して係止
されている。このためピース17は、装置本体1
の半径方向の移動が自在となり、ピース17は重
力によつて降下し、その外縁5bは内周面に当接
して回動し、被乾燥物が外縁5bと内周面との間
より落下することがなく、被乾燥物の装置本体1
内のシヨートパスが防止されるとともにこのピー
ス17を付けることにより傾斜形スクリユー5の
外径は自動的に装置本体1内に一致するように調
節されるため、該傾斜形スクリユー5の外周を精
密に加工する必要がなく製作が極めて容易とな
る。なお、ボルト、ナツト18aによつてピース
17を適当な位置に固定し、内周面とスクリユー
外縁との間隔を調節してもよい。 また、傾斜形スクリユー5のスクリユー羽根を
多孔板とすることにより、気流の流路を傾斜形ス
クリユー5の螺旋面に乗せられた被乾燥物の層表
面のみでなく、層内部も通るようにして乾燥効果
を増すことも出来る。この孔板スクリユーは、特
に熱風を併用した場合に効果を発揮する。 なお、上記スクリユー5は、第4図および第5
図に示すように筒状部材19に取付け、この筒状
部材19を回転軸4に纒着することによつて着脱
自在とすることができる。また以上の装置は、こ
れを耐熱鋼等によつて構成することにより乾留、
焼却、触媒再生等の燃焼装置として使うことがで
き、さらに被乾燥物の代りに触媒を用い装置本体
1内に被反応流体を流通するようにして、移動層
触媒反応装置としても使用できる。この場合に、
反応が発熱反応である場合には、ジヤケツト12
に反応開始温度まで熱媒体を循環し、その後は冷
水等の冷却媒体を循環させればよい。
The present invention will be explained below with reference to the drawings. FIG. 1 shows an embodiment in which the device of the present invention is used as a drying device, and reference numeral 1 in the figure indicates a cylindrical device main body. At the top of the device main body 1,
A sealing lid 2 is provided, and a cone-shaped portion 3 is provided below. A discharge valve 3a for discharging dry matter is provided at the lower end of this cone-shaped portion 3. Further, a rotating shaft 4 is provided at the center of the cylindrical portion of the device main body 1, passing through the sealing lid 2. The rotating shaft 4 is rotatably held by a lower bearing 4a provided in the device main body 1 and supporting the lower end of the rotating shaft 4, and an upper bearing 4b provided in the sealing lid 2. Further, a screw 5 is attached to the rotating shaft 4. The screw 5 has an inner edge 5a fixed to the outer periphery of the rotating shaft 4, and an outer edge 5b located close to the inner circumferential surface of the apparatus main body 1. Further, a virtual line intersecting a plane including the axis of the rotating shaft 4 and the helical surface of the screw 5, that is,
The spiral surface in the radial direction of the device main body 1 is inclined downward with respect to the rotating shaft 4 (inclined screw). In addition, on the upper side of the cylindrical part of the device main body 1,
A water vapor discharge pipe 6 is attached. A water vapor condenser 7 is provided at the tip of the discharge pipe 6. Further, the rotary shaft 4 is provided with a variable rotation drive mechanism 8 that rotates the rotary shaft 4 in a direction opposite to the twisting direction downward from the upper end of the inclined screw 5. Further, a supply port 9 for supplying the material to be dried into the apparatus main body 1 is provided at the upper part of the airtight lid 2.
is provided. One end of a screw feeder 10 is connected to the supply port 9, and a drying material hopper 11 is provided at the other end of the screw feeder 10. Further, a jacket 12 is provided around the outer periphery of the main body 1 of the apparatus. This jacket 12
The heat medium fluid (hot water, Kaneklor [trade name], Dowsome [trade name], etc.) heated in the heat medium tank 12a is circulated by the heat medium circulation pump 12b. Next, a method of operating the dryer configured as described above will be explained. The operation is performed according to the following steps. 1) First, drive the rotating shaft 4 to rotate the inclined screw 5. 2) Circulating heat medium fluid through the jacket 12 to heat the inside of the device body 1. 3) Drive the screw feeder 10 to feed the material to be dried stored in the hopper 11 from the supply port 9 to the upper end surface of the inclined screw 5. Through the above operations, the material to be dried is continuously dried. Due to the radial inclination shape and rotation of the helical surface of the inclined screw 5, the material to be dried that has been placed on the helical surface of the inclined screw 5 due to the above operation approaches the inner circumferential surface of the apparatus main body 1, and It rotates on the spiral surface of the inclined screw 5 while contacting the surface. Due to the frictional force with the inner circumferential surface generated by this rotation and the gravity of the material to be dried, while in contact with the inner circumferential surface,
It gradually descends downward along the upper surface of the inclined screw 5. In this descending process, the material to be dried receives heat from the inner circumferential surface heated by the heat transfer fluid and the inclined screw 5 acting as a heat exchange piece, and moisture evaporates, and the material to be dried evaporates. dry. When the rotational speed of the inclined screw 5 is slow, drying is performed in the above-mentioned state. As the rotational speed increases, the material to be dried is pressed against the inner circumferential surface, a portion of which adheres, and is scraped off by the outer edge 5b of the rotating inclined screw 5. Normally, the rotational speed of the inclined screw 5 is as slow as several revolutions per hour. In this case, the rate of descent of the material to be dried changes proportionally to the rotational speed of the inclined screw 5. Therefore, the residence time of the material to be dried in the main body 1 of the apparatus can be freely adjusted by adjusting the rotational speed of the inclined screw 5, and the helical surface of the inclined screw is inclined in the radial direction. Therefore, even if a horizontal screw requires a large pitch to fall, it can be dropped in a small pitch, allowing the device to be made more compact. Further, since the device main body 1 has a simple structure, airtightness can be easily maintained. Furthermore, since the material to be dried rolls and slides down the spiral surface of the inclined screw 5, the free surface area is large. Furthermore, since the spiral surface is inclined in the radial direction, the contact area between the inner circumferential surface as a heat transfer surface and the material to be dried is increased, and the heat transfer surface can be used effectively. Furthermore, since no stirring is performed and heat is received through indirect heating, there is little chance of fine powder particles being scattered. Note that the generated water vapor is led to a water vapor condenser 7 through a discharge pipe 6, cooled, and condensed and separated. Further, the dried material is taken out to the outside by a discharge valve 3a. The above-mentioned heating means circulates a heat medium fluid such as steam or hot water through the jacket 12 provided on the outer peripheral surface of the device main body 1, but instead of this heating means, an electric heater, for example, is installed on the outer peripheral surface. Heating may be performed by providing a heating means such as resistance heating, low frequency induction heating, high frequency induction heating, and far infrared heating. In addition to heating by the heating medium fluid circulating in the jacket 12, the rotary shaft 4 and the inclined screw 5 are made hollow to provide appropriate heating medium paths to flow the heating medium fluid to promote moisture evaporation from the material to be dried. You can also do that. Furthermore, hot air may be blown from the bottom of the device main body to dry it. At this time, sufficient drying can be achieved by heating only with hot air, but if used in combination with the indirect heating method described above, the water vapor partial pressure will be reduced and water evaporation will be promoted, the drying effect will be enhanced with a small air volume, and it will be advantageous to generate less dust. It is. It is also effective to maintain the inside of the apparatus main body 1 in a reduced pressure state via the condenser 7, as this speeds up the drying process. Also, in the above description, a single inclined screw has been described. However, the physical properties vary depending on the material to be dried, and the physical properties also change as the water content decreases during the drying process. The inclined screw 5 has various shapes to accommodate these requirements. In FIG. 2, the lower pitch 13 of the inclined screw 5 is made smaller. In this case, the inclined screw 5 on which the material to be dried containing water and having poor flow is placed.
The pitch 13 may be made larger in the upper part, but if the moisture decreases and becomes easier to flow, the rate of descent will become faster.
In order to prevent this, the pitch 13 is made smaller as it goes downward. For the same purpose, as shown in FIG. 3, the upper part of the screw 14 is an inclined screw 5, and the imaginary line where the plane containing the axis of the rotating shaft 4 intersects the helical surface of the screw is continuously below the screw 5. It may be a horizontal screw 15 that is horizontal. FIG. 4 shows an inclined screw 5 in which a plurality of inclined screws 5 are discontinuously attached to the rotating shaft 4 with spacers 16 interposed between them, without providing a continuous inclined screw 5 over the entire length of the rotating shaft 4. This is an example. In this case, depending on the physical properties of the material to be dried and changes in physical properties during the drying process, it may be combined with the horizontal screw 15 or attached to the rotating shaft 4 by appropriately selecting the pitch and length. In this way, the material to be dried is separated from the inner circumferential surface and the screw 1 on the screw 14.
4 and the flow of the spiral surface of the screw 14 due to the gravity of the drying material, the drying material rolls downward, but further falls and is agitated at the discontinuous portion where the spacer 16 is interposed, improving drying efficiency. 5a and 5b, the outer edge 5b of the inclined screw 5 which comes into contact with the inner peripheral surface is formed by a piece 17 having a long hole 17a provided in the radial direction of the inclined screw 5. In FIGS. The piece 17 is secured to the outer edge of a small screw 18 whose radius is smaller than the radius of the main body 1 of the apparatus by means of a bolt or nut 18a through an elongated hole. Therefore, the piece 17 is
becomes free to move in the radial direction, the piece 17 descends due to gravity, its outer edge 5b contacts the inner circumferential surface and rotates, and the material to be dried falls from between the outer edge 5b and the inner circumferential surface. The main body 1 of the device for drying
By attaching this piece 17, the outer diameter of the inclined screw 5 is automatically adjusted to match the inside of the apparatus main body 1, so that the outer circumference of the inclined screw 5 can be precisely adjusted. There is no need for processing, making production extremely easy. Note that the piece 17 may be fixed in an appropriate position with bolts and nuts 18a, and the distance between the inner peripheral surface and the outer edge of the screw may be adjusted. Furthermore, by making the screw blades of the inclined screw 5 into perforated plates, the air flow path passes not only through the surface of the layer of the material to be dried placed on the spiral surface of the inclined screw 5, but also through the inside of the layer. It can also increase the drying effect. This perforated plate screw is particularly effective when used in combination with hot air. Note that the screw 5 is shown in FIGS. 4 and 5.
As shown in the figure, it can be attached to a cylindrical member 19, and by tightening this cylindrical member 19 to the rotating shaft 4, it can be made detachable. Furthermore, the above-mentioned equipment can be constructed from heat-resistant steel, etc.
It can be used as a combustion device for incineration, catalyst regeneration, etc. Furthermore, it can also be used as a moving bed catalytic reaction device by using a catalyst instead of the dried material and allowing the fluid to be reacted to flow through the device body 1. In this case,
If the reaction is exothermic, the jacket 12
The heat medium may be circulated until the reaction start temperature is reached, and then a cooling medium such as cold water may be circulated.

【考案の効果】[Effect of the idea]

以上述べた如く、本考案の装置は、被乾燥物等
の物体を傾斜形スクリユーの回転によつて下方に
移行せしめるので次のような特徴が発揮される。 1 スクリユーの面上を転動降下するので自由表
面が大きく、物体の有効表面面積が大きくとれ
る。 2 本考案においてはスクリユーの螺旋面が半径
方向に傾斜していることから、スクリユー面上
の物体は該スクリユーの外周部(装置本体の円
筒壁内周面)に厚く分布し、水平形スクリユー
に比べ、円筒壁内周面と物体との接触面積は極
めて大きくなり、スクリユーが回転したとき
に、スクリユー面上の物体を内周壁との摩擦力
によつて現在位置に止めるように作用し、スク
リユーの抜け(すなわち物体の滑り)が良くな
るので、水平スクリユーでは大きなピツチにし
ないと落下しない湿潤物のような滑りの悪い物
でも、スクリユーのピツチを大きくせずに移動
させることができる。また、滑りの良い物もス
クリユーのピツチ(スクリユーの進み角)を大
きくせずに済むので、かつてに移動することが
なく、滑りの悪い物も滑りの良い物もスクリユ
ーの回転数を変えることによつて滞留時間を容
易かつ自由に調節でき、物体の種類、性状の多
様性に対応できる。 3 水平形スクリユーにおける半径方向の位置に
よる物体の降下速度の差異(螺旋スクリユーは
進み角が内周部では大きく、外周部になるほど
小さくなることによる)によつて生じる物体の
滞留時間の不均一を、本考案においてはスクリ
ユーの螺旋面が半径方向に傾斜していることに
よつて、大部分の物体がスクリユーの外周部
(装置本体の円筒壁内周面)にあるので、少な
くすることができる。 4 滑りの悪い物に対しても、螺旋スクリユーの
ピツチを前述のように大きくせずに、降下を促
進することができ、装置の小型化を図ることが
できる。 5 水平形スクリユーでは、装置の内周面には物
体が充分に接触しないが、本考案においてはス
クリユーの螺旋面が半径方向に傾斜しているこ
とから、装置本体の円筒壁内周面に物体がよく
接するので内周面も有効に伝熱面として利用で
きる。 6 本考案においてはスクリユーの螺旋面が半径
方向に傾斜していることから、同一径の水平形
スクリユーよりもスクリユー表面積が広くな
り、必要によつて有効に伝熱面として利用でき
る。 7 外形、構造が簡単で密閉性を保持し易く、負
圧運転も容易で、有害物質または有臭物質等を
公害発生なく処理することも可能である。 等の数多くの長所を有するものである。
As described above, the apparatus of the present invention has the following characteristics because the object to be dried is moved downward by the rotation of the inclined screw. 1. Since the object rolls down on the surface of the screw, the free surface is large and the effective surface area of the object is large. 2 In the present invention, since the helical surface of the screw is inclined in the radial direction, objects on the screw surface are distributed thickly on the outer periphery of the screw (inner peripheral surface of the cylindrical wall of the device main body), and are In comparison, the contact area between the inner circumferential surface of the cylindrical wall and the object is extremely large, and when the screw rotates, the object on the screw surface is stopped at the current position by the frictional force with the inner circumferential wall, and the screw This improves the slippage of the screw (that is, the slippage of the object), so even objects with poor slippage, such as wet objects, which would not fall unless the pitch of the screw is made large with a horizontal screw, can be moved without increasing the pitch of the screw. In addition, objects with good sliding do not need to increase the screw pitch (advance angle of the screw), so they do not move as before, and the rotation speed of the screw can be changed for objects with poor slippage and objects with good slippage. Therefore, the residence time can be easily and freely adjusted, and it is possible to respond to a variety of object types and properties. 3. The uneven residence time of an object caused by the difference in the descending speed of the object depending on the radial position in a horizontal screw (for a spiral screw, the advance angle is large at the inner periphery and becomes smaller toward the outer periphery). In the present invention, since the spiral surface of the screw is inclined in the radial direction, most of the objects are located on the outer periphery of the screw (inner periphery of the cylindrical wall of the main body of the device), so that the number of objects can be reduced. . 4. Even on objects with poor slippage, it is possible to accelerate the descent of the helical screw without increasing the pitch as described above, and the device can be made more compact. 5 With horizontal screws, objects do not come into sufficient contact with the inner peripheral surface of the device, but in this invention, the spiral surface of the screw is inclined in the radial direction, so objects do not come into contact with the inner peripheral surface of the cylindrical wall of the device body. Since they are in good contact with each other, the inner peripheral surface can also be effectively used as a heat transfer surface. 6 In the present invention, since the helical surface of the screw is inclined in the radial direction, the screw surface area is larger than that of a horizontal screw of the same diameter, and can be effectively used as a heat transfer surface when necessary. 7. The external shape and structure are simple, it is easy to maintain airtightness, negative pressure operation is easy, and it is also possible to dispose of harmful or odorous substances without causing pollution. It has many advantages such as:

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

第1図は、本考案に係る装置の一実施例を示す
一部断面図、第2図ないし第5図a,bは本考案
の装置に使用する傾斜形スクリユーの図で、第2
図は下方のピツチを小さくした傾斜形スクリユー
の図、第3図は傾斜形スクリユーと水平形スクリ
ユーを連続して設けた傾斜形スクリユーの図、第
4図は、短いスクリユーをスペーサを挟んで不連
続に設けた傾斜形スクリユーの図、第5図aは外
縁が可動ピースとなつている傾斜形スクリユーの
縦断面図、第5図bは、外縁が可動ピースとなつ
た傾斜形スクリユーの平面図である。 1……装置本体、2……密閉蓋、3……コーン
状部、3a……排出バルブ、4……回転軸、4a
……下部軸受、4b……上部軸受、5……傾斜形
スクリユー、5a……内縁、5b……外縁、9…
…供給口、13……スクリユーピツチ、14……
スクリユー、15……水平形スクリユー、16…
…スペーサ、17……ピース、17a……長孔、
18……小スクリユー、18a……ボルト、ナツ
ト、19……筒状部材。
FIG. 1 is a partial sectional view showing one embodiment of the device according to the present invention, and FIGS. 2 to 5 a and b are views of an inclined screw used in the device of the present invention.
The figure shows an inclined screw with a smaller pitch at the bottom, Figure 3 shows an inclined screw with an inclined screw and a horizontal screw installed in succession, and Figure 4 shows a short screw with a spacer in between. Figure 5a is a longitudinal cross-sectional view of an inclined screw whose outer edge is a movable piece, and Fig. 5b is a plan view of an inclined screw whose outer edge is a movable piece. It is. DESCRIPTION OF SYMBOLS 1... Device main body, 2... Sealing lid, 3... Cone-shaped part, 3a... Discharge valve, 4... Rotating shaft, 4a
...lower bearing, 4b...upper bearing, 5...inclined screw, 5a...inner edge, 5b...outer edge, 9...
...Supply port, 13...Screw pitch, 14...
Screw, 15...Horizontal screw, 16...
...Spacer, 17... Piece, 17a... Long hole,
18... Small screw, 18a... Bolt, nut, 19... Cylindrical member.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 竪型円筒形の装置本体と、この装置本体の円筒
軸線に沿つて設けられた回転軸と、この回転軸に
内縁が取り付けられ、外縁が上記円筒形の装置本
体の内周面に近接または接触するスクリユーと、
上記回転軸を上記スクリユーの上端から下端に向
かうねじり方向と逆の方向に回転駆動する駆動機
構と、上記円筒形の装置本体の外周面に設けた加
熱手段とを備え、上記スクリユーと上記回転軸の
軸線を含む平面とが交差する仮想線は内縁から外
縁に行くに従い下方に向かうように傾斜している
ことを特徴とする乾燥等の連続処理装置。
A vertical cylindrical device main body, a rotating shaft provided along the cylindrical axis of the device main body, an inner edge attached to the rotating shaft, and an outer edge close to or in contact with the inner circumferential surface of the cylindrical device main body. Screw to do,
A driving mechanism for rotationally driving the rotating shaft in a direction opposite to the twisting direction of the screw from the upper end to the lower end, and a heating means provided on the outer peripheral surface of the cylindrical device main body, the screw and the rotating shaft A continuous processing device for drying, etc., characterized in that an imaginary line that intersects with a plane containing an axis line is inclined downwardly from the inner edge to the outer edge.
JP14809982U 1982-09-30 1982-09-30 Continuous processing equipment such as drying Granted JPS5952392U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14809982U JPS5952392U (en) 1982-09-30 1982-09-30 Continuous processing equipment such as drying

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14809982U JPS5952392U (en) 1982-09-30 1982-09-30 Continuous processing equipment such as drying

Publications (2)

Publication Number Publication Date
JPS5952392U JPS5952392U (en) 1984-04-06
JPH0334634Y2 true JPH0334634Y2 (en) 1991-07-23

Family

ID=30329143

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14809982U Granted JPS5952392U (en) 1982-09-30 1982-09-30 Continuous processing equipment such as drying

Country Status (1)

Country Link
JP (1) JPS5952392U (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5072887B2 (en) * 2009-03-12 2012-11-14 株式会社東芝 Nanocarbon generator

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5355673A (en) * 1976-10-30 1978-05-20 Shinko Pfaudler Vertical rotary bed furnace
JPS5521819A (en) * 1978-08-01 1980-02-16 Seiko Instr & Electronics Ltd Super-thin make silver oxide cell

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5355673A (en) * 1976-10-30 1978-05-20 Shinko Pfaudler Vertical rotary bed furnace
JPS5521819A (en) * 1978-08-01 1980-02-16 Seiko Instr & Electronics Ltd Super-thin make silver oxide cell

Also Published As

Publication number Publication date
JPS5952392U (en) 1984-04-06

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