JPS6032018Y2 - Device for transferring powder and granular materials between two chambers with a pressure difference - Google Patents

Device for transferring powder and granular materials between two chambers with a pressure difference

Info

Publication number
JPS6032018Y2
JPS6032018Y2 JP3759579U JP3759579U JPS6032018Y2 JP S6032018 Y2 JPS6032018 Y2 JP S6032018Y2 JP 3759579 U JP3759579 U JP 3759579U JP 3759579 U JP3759579 U JP 3759579U JP S6032018 Y2 JPS6032018 Y2 JP S6032018Y2
Authority
JP
Japan
Prior art keywords
powder
cylindrical tube
screw
tube
pressure difference
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
JP3759579U
Other languages
Japanese (ja)
Other versions
JPS55136728U (en
Inventor
及也 安田
昌三 和田
一馬 峰
Original Assignee
株式会社協和エンヂニアリング
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 株式会社協和エンヂニアリング filed Critical 株式会社協和エンヂニアリング
Priority to JP3759579U priority Critical patent/JPS6032018Y2/en
Publication of JPS55136728U publication Critical patent/JPS55136728U/ja
Application granted granted Critical
Publication of JPS6032018Y2 publication Critical patent/JPS6032018Y2/en
Expired legal-status Critical Current

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  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Description

【考案の詳細な説明】 この考案は、気体又は液体に圧力差がある二基間におけ
る粉粒体の移送装置に関するものである。
[Detailed Description of the Invention] This invention relates to a device for transferring powder or granular material between two units in which there is a pressure difference between gas or liquid.

圧力差がある二基間において、両室間をシールされた状
態に保って、粉粒体を移動させる装置としては、例えば
ロータリーバルブとかキニョンポンプ等が知られている
For example, a rotary valve or a Kinyon pump is known as a device for moving powder or granular material between two chambers where there is a pressure difference while maintaining a sealed state between the two chambers.

しかし、ロータリーバルブはその構造上シール性が悪い
といった欠点があり、キニョンポンプには次のような欠
点があった。
However, rotary valves have the disadvantage of poor sealing properties due to their structure, and Kinyon pumps have the following disadvantages.

すなわち、キニョンポンプは、直円筒管内にオーバーハ
ングして内装されたスクリュー羽根のピッチを、排出口
側程狭くしておいて、このスクリュー羽根が高速回転す
ることにより、スクリュー羽根間で粉粒体を圧密して、
円筒管内を、このようにして圧密された粉粒体でもって
シールせしめつつ、粉粒体を円筒管の排出口方向へと押
し出すものであるから、完全なシール効果を得るために
は、スクリュー羽根ノ高速回転のために大馬力を必要と
する他、常に一定量の粉粒体を一定の速度で送り続けな
ければならないので、移送量の調節ができない等の欠点
があった。
In other words, in the Kinyon pump, the pitch of the screw blades overhanging inside the right cylindrical pipe is made narrower toward the discharge port, and when the screw blades rotate at high speed, powder and granules are transferred between the screw blades. By consolidating
The inside of the cylindrical tube is sealed with the powder and granules compacted in this way, and the granules are pushed out toward the discharge port of the cylindrical tube, so in order to obtain a complete sealing effect, the screw blades must be In addition to requiring a large amount of horsepower due to the high speed rotation, it also had the disadvantage that the amount of powder transported cannot be adjusted because a certain amount of powder and granules must be continuously fed at a certain speed.

そこで、この考案は上記のような欠点をもたない粉粒体
の移送装置を提供しようとするものであって、その要旨
とするところは、円筒管と該円筒管内に横架させるスク
リュー軸とからなり円筒管の適所にあけられた投入口へ
と投入された粉粒体が円筒管の管端から排出されるよう
に構成されたスクリューフィーダを、圧力差のある二基
間の仕切壁を貫いて横架すると共に、このスクリューフ
ィーダの排出口に、常時該排出口を閉塞する向きに弾性
的に附勢されたダンパーを配設してなる、圧力差のある
二基間における粉粒体の移送装置であって、前記スクリ
ュー軸の排出側が、先細り形状に形成されると共に、こ
のスクリュー軸の先端部近傍と排出口との間の円筒管の
部分が逆テーパーの末広管に形成されていること、を特
徴としてなる粉粒体の移送装置にある。
Therefore, this invention aims to provide a device for transferring powder and granular materials that does not have the above-mentioned drawbacks. A screw feeder is constructed in such a way that powder and granules introduced into an inlet opened at an appropriate position in a cylindrical tube are discharged from the end of the cylindrical tube, and a partition wall between the two bases with a pressure difference is used. The powder and granular material between the two screw feeders with a pressure difference is installed horizontally through the screw feeder, and a damper is provided at the discharge port of the screw feeder, which is elastically energized in a direction that always closes the discharge port. In the transfer device, the discharge side of the screw shaft is formed into a tapered shape, and the portion of the cylindrical tube between the vicinity of the tip of the screw shaft and the discharge port is formed into a reversely tapered diverging tube. The apparatus for transferring powder and granular materials is characterized by:

実施例を図について説明すると、この実施例は、槽外の
雰囲気(大気圧)よりも高圧に保たれた貯槽1内へと、
例えば木粉のような粉粒体を移送する装置として、つま
り高圧の該貯槽1内へと粉粒体をシール状態下に投入供
給する装置として実施した場合に関し、図において、2
はこの貯槽1の上部に連設された排出箱、3はこの排出
箱2の壁を貫いて横架されたスクリューフィーダで、ス
クリューフィーダ3は、排出箱2の壁を貫いて設けられ
た円筒管4と該円筒管4内にオーバーハング式に横架さ
れたスクリュー軸5とからなりこのスクリューフィーダ
3は、槽1外において円筒管4の適所にあけられた投入
口6へと投入された粉粒体が前記排出箱2内へと開口さ
れた円筒管4の管端の排出ロアから排出されるように構
成されており、排出箱2内に開口された円筒管4端には
スイングダンパー8が配設されている。
To explain the embodiment with reference to the figures, in this embodiment, the inside of the storage tank 1 is kept at a higher pressure than the atmosphere outside the tank (atmospheric pressure),
For example, when implemented as a device for transferring powder or granular material such as wood flour, that is, as a device for supplying the powder or granular material into the high-pressure storage tank 1 under a sealed condition, in the figure, 2
is a discharge box connected to the upper part of the storage tank 1; 3 is a screw feeder horizontally suspended through the wall of the discharge box 2; This screw feeder 3, which consists of a tube 4 and a screw shaft 5 horizontally suspended in the cylindrical tube 4 in an overhanging manner, is fed into an input port 6 made at an appropriate position in the cylindrical tube 4 outside the tank 1. The granular material is configured to be discharged from a discharge lower at the end of the cylindrical pipe 4 opened into the discharge box 2, and a swing damper is installed at the end of the cylindrical pipe 4 opened into the discharge box 2. 8 are arranged.

このスイングダンパー8は、それが固着された軸9を排
出箱2に軸受されて揺動自在に枢支されており、軸9が
排出箱2外へと突出された部分には、腕10が固着され
ていて、このスイングダンパー8は上記腕10の先端と
排出箱2に固定されたブラケット11との間に張設せる
ばね12でもって、常時円筒管4端を閉塞する向きに附
勢されている。
This swing damper 8 has a shaft 9 to which it is fixed, which is rotatably supported by the discharge box 2, and an arm 10 is attached to the portion where the shaft 9 protrudes outside the discharge box 2. The swing damper 8 is always urged in a direction to close the 4 ends of the cylindrical pipe by a spring 12 stretched between the tip of the arm 10 and the bracket 11 fixed to the discharge box 2. ing.

13はこの附勢圧力の調節ねじである。13 is a screw for adjusting this biasing pressure.

なお図において14は前記投入口6に連結せるホッパー
15.16はスクリュー軸5の軸受で、スクリュー軸5
はその軸端に嵌着せる駆動ホイール17へとその駆動力
を入力されるようになっているのであるが、この考案に
したがった粉粒体の移送装置にあっては、上記スクリュ
ーフィーダ3が特に次のように構成されているのである
In the figure, 14 is a hopper 15 connected to the input port 6, and 16 is a bearing for the screw shaft 5.
The driving force is inputted to a drive wheel 17 fitted on the shaft end of the screw feeder 3. It is structured as follows.

すなわち、スクリューフィーダ3はそのスクリュー軸5
を、附属軸部分5aと円錐軸部分5bとでもって構成さ
れていて、円錐軸部分5bでもってその排出側を先細り
形状に形成されており、スクリュー羽根18も附属軸部
分5aでは同一径であるが、円錐軸部分5bでは、羽根
18の径を次第に減少しである。
That is, the screw feeder 3 has its screw shaft 5
is composed of an attached shaft portion 5a and a conical shaft portion 5b, and the discharge side of the conical shaft portion 5b is formed into a tapered shape, and the screw blade 18 also has the same diameter in the attached shaft portion 5a. However, in the conical shaft portion 5b, the diameter of the blade 18 is gradually reduced.

また先細形状に形成されたスクリュー軸5の先端部と、
円筒管4端の排出ロアとの間には、一定の間隔aを附与
してあって、円筒管4は、前記スクリュー軸5がその内
側へと位置して内装された部分を同一径の直管4aに形
成されているが、スクリュー軸5がその内側に位置して
いない排出ロア側の前記間隔a部分は、これを排出ロア
側に向って逆テーパーが附与された截頭円錐形の末広管
4bに形成されている。
Further, the tip of the screw shaft 5 is formed into a tapered shape,
A certain distance a is provided between the end of the cylindrical tube 4 and the discharge lower, and the cylindrical tube 4 has a portion with the same diameter where the screw shaft 5 is located inside. The above-mentioned interval a portion on the discharge lower side, which is formed in the straight pipe 4a but where the screw shaft 5 is not located inside, is shaped like a truncated cone with a reverse taper toward the discharge lower side. It is formed in the wide-divergent tube 4b.

この考案に係る粉粒体の移送装置は、上記のような構成
であるから、スクリューフィーダ3の投入口6へとホッ
パー14から粉粒体を投入すると投入口6へと投入され
た粉粒体は、円筒管4の直管4a部分に入り、管内を回
転しているスクリュー軸5の羽根18によって排出ロア
方向へと送られることになるのであるが、スクリュー軸
5は、それが、前記せる如き附属軸部分5aと円錐軸部
分5bとでもって構成されているので、附属軸部分5a
では、粉粒体は単に前方へと移送されるにすぎないが、
その先端の円錐軸部分5bでは排出ロアがスイングダン
パー8にて閉塞され軸が先細形状になるので、その先端
部まで達した粉粒体は、ここでは中空状になることなく
、管内の全断面に均一に分散して圧密され、この円錐軸
部分5bの先端部近傍と、排出ロア間の末広管4b内に
は、粉粒体の圧縮槽Aが形成される。
Since the granular material transfer device according to this invention has the above-described configuration, when the granular material is introduced from the hopper 14 into the inlet 6 of the screw feeder 3, the granular material introduced into the inlet 6 is transferred. enters the straight pipe 4a of the cylindrical pipe 4 and is sent toward the discharge lower direction by the blades 18 of the screw shaft 5 rotating inside the pipe. Since it is composed of the attached shaft portion 5a and the conical shaft portion 5b, the attached shaft portion 5a
In this case, the granular material is simply transported forward, but
At the conical shaft portion 5b at the tip, the discharge lower is closed by the swing damper 8 and the shaft becomes tapered, so that the powder and granules that have reached the tip do not form a hollow shape, but instead cover the entire cross section of the tube. The powder is uniformly dispersed and compacted, and a compressed tank A of the powder is formed in the vicinity of the tip of the conical shaft portion 5b and within the wide-spread pipe 4b between the discharge lower.

このようにして末広管4b内に圧密された粉粒体は、圧
密状態に保たれたま)、スクリュー軸5の羽根18に押
され、スイングダンパー8をばね12による附勢に抗し
て若干押し開き、排出ロアに隙間を形成して、そこから
、排出箱2内へと、スクリュー羽根18の送り量に相当
する量を排出される。
The powder compacted in the diverging tube 4b in this way is pushed by the blades 18 of the screw shaft 5 while being kept in a compacted state, and pushes the swing damper 8 slightly against the bias of the spring 12. It opens to form a gap in the discharge lower, from which an amount corresponding to the feed amount of the screw blade 18 is discharged into the discharge box 2.

したがってこの考案の装置によれば、前記末広管4bの
管内に圧密された粉粒体の圧縮層Aによって、スクリュ
ーフィーダ3の管内が閉塞されることになる結果、該圧
縮層Aでもって、圧力差のある二基間つまり貯槽1内と
貯槽1外との間が、シール状態に保たれたま)、粉粒体
が両室間において移送されることになるのであるが、こ
の考案の装置はスクリュー軸5が特に単なる移送の役目
をする附属軸部分5aと移送兼圧密の役目をする円錐軸
部分5bとでもって構成されているので、スクリュー軸
5を粉粒体の移送目的にあった低速でもって回転させて
も、末広管4b内に粉粒体の圧縮層Aからなるシール層
を形成せしめうるものであり、スクリュー軸5の摩耗が
少く、ダンパー8の附勢を強弱調節することによって、
従来のキニョンポンプに比し少い動力でもって所望量の
粉粒体を移送しうるものである。
Therefore, according to the device of this invention, the inside of the screw feeder 3 is obstructed by the compressed layer A of the powder compacted inside the diverging tube 4b, and as a result, the compressed layer A increases the pressure. The powder and granules are transferred between the two chambers (while maintaining a seal between the two chambers with a difference, that is, the inside of the storage tank 1 and the outside of the storage tank 1), and the device of this invention Since the screw shaft 5 is composed of an auxiliary shaft portion 5a that serves as a mere transport and a conical shaft portion 5b that serves as a transport and consolidation role, the screw shaft 5 can be moved at a low speed suitable for the purpose of transporting powder and granules. Even if it is rotated, a sealing layer consisting of the compressed layer A of powder and granules can be formed in the divergent tube 4b, and the wear of the screw shaft 5 is small, and by adjusting the force of the damper 8 ,
The desired amount of powder can be transferred with less power than conventional Kinyon pumps.

しかもこのようにして末広管4b内に圧密された粉粒体
の圧縮層Aは、前記せる如く、中心部の圧密状態が管壁
近傍の部分に比して疎になった中空状圧密状態になるこ
となく、完全に中実にして管内の全断面が均一な圧密状
態に圧縮されているので完全なシール層が得られるので
あるが、この圧縮層Aが形成された末広管4bは、排出
ロア側が拡がった逆テーパーの抜は勾配であるから、こ
の末広管4b内に形成された圧縮層Aは、粉粒体の排出
方向においては管壁との間に大きい摩擦抵抗を生じない
し、また、管壁との間の摩擦抵抗を、附属管の場合のよ
うに、粉粒体の種類及び含水率又は気象条件等によって
大きく変動されない。
Moreover, the compacted layer A of the powder material compacted in the diverging tube 4b in this way is in a hollow compacted state in which the compacted state in the center is less dense than in the part near the pipe wall, as described above. Since the pipe is made completely solid and the entire cross section of the pipe is compressed to a uniformly compacted state, a perfect sealing layer can be obtained. Since the reverse taper with the lower side widened has a slope, the compressed layer A formed in the diverging tube 4b does not generate large frictional resistance with the tube wall in the direction of discharging the powder and granules. The frictional resistance between the pipe wall and the pipe wall does not vary greatly depending on the type of powder, moisture content, weather conditions, etc., as in the case of attached pipes.

すなわち、この考案の移送装置では、末広管4b内に形
成される圧縮層Aの比密度の強弱をスイングダンパー8
の附勢ばね12を調節することによって容易且つ正確に
コントロールできるので、スイングダンパー8の附勢ば
ね12により、充分上記摩擦抵抗の変動を吸収せしめ、
長期間に亘り、管壁面との間の摩擦抵抗の低下による圧
密状態の破壊とか、該摩擦抵抗の増加による過負荷停止
等のトラブルを生せしめることなく、粉粒体を円滑に連
続移送し続けるものである。
That is, in the transfer device of this invention, the strength of the specific density of the compressed layer A formed in the divergent tube 4b is controlled by the swing damper 8.
Since it can be easily and accurately controlled by adjusting the biasing spring 12 of the swing damper 8, the fluctuation of the frictional resistance can be sufficiently absorbed by the biasing spring 12 of the swing damper 8.
Powder and granular materials can be smoothly and continuously transferred over a long period of time without causing problems such as destruction of the compacted state due to a decrease in frictional resistance with the pipe wall surface, or overload stoppage due to an increase in frictional resistance. It is something.

また、円筒管4の排出ロア側を逆テーパーの末広管4b
としたことによっては、上記せる如く管壁と粉粒体間の
摩擦抵抗を少ならしめ、且つその変動の影響を小ならし
めて得ているばかりでなく、次のようなくさび効果も得
ている。
In addition, the discharge lower side of the cylindrical pipe 4 is a reversely tapered diverging pipe 4b.
By doing so, we not only reduce the frictional resistance between the tube wall and the granular material as described above, and also reduce the influence of its fluctuations, but also obtain the following wedge effect. .

すなわち、この末広管4bは、粉粒体の排出方向に対し
て抜は勾配であるが、反対向きには、圧縮層Aがくさび
状となるので、粉粒体は、それが戻される方向には移動
し難い。
In other words, the wide-spread pipe 4b has a vertical slope with respect to the direction in which the powder and granules are discharged, but in the opposite direction, the compressed layer A becomes wedge-shaped, so that the powder and granules are returned in the direction in which they are returned. is difficult to move.

したがってこの考案の移送装置では、スクリュー軸の駆
動を停止しても、くさび状の圧縮層Aはスイングダンパ
ー8によって圧密状態に保たれ、シールご破壊されるこ
とがないものである。
Therefore, in the transfer device of this invention, even if the drive of the screw shaft is stopped, the wedge-shaped compressed layer A is kept in a compressed state by the swing damper 8, and the seal is not destroyed.

なお上記実施例においては、ダンパーを、一端が枢支さ
れたスイングダンパー8でもって構成せる例を示したが
、ダンパーはスイング式のものに限定されるものではな
く、他の実施例においては、これを排出ロア向きに摺動
自在に支持せしめて設けてもよく、また上記実施例は一
応貯槽1内が高圧である場合を想定して説明したが、こ
の考案に係る粉粒体の移送装置は、貯槽1側が低圧の場
合においても実施みうるものであることは言うまでもな
い。
In addition, in the above embodiment, an example was shown in which the damper is constituted by a swing damper 8 whose one end is pivotally supported, but the damper is not limited to a swing type damper, and in other embodiments, This may be provided so as to be slidably supported in the direction of the discharge lower, and although the above embodiment has been explained assuming that the inside of the storage tank 1 is under high pressure, the powder and granular material transfer device according to this invention It goes without saying that this can be carried out even when the pressure on the storage tank 1 side is low.

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

第1図はこの考案に係る粉粒体の移送装置の実施例を示
した縦断面図である。 1・・・・・・貯槽、3・・・・・・スクリューフィー
ダ、4・・・・・・円筒管、4a・・・・・・直管、4
b・・・・・・末広管、5・・・・・・スクリュー軸、
5a・・・・・・附属軸部分、5b・・・・・・円錐軸
部分、6・・・・・・投入口、7・・・・・・排出口、
8・・・・・・スイングダンパー、12・・・・・・ば
ね。
FIG. 1 is a longitudinal cross-sectional view showing an embodiment of a powder or granular material transfer device according to this invention. 1... Storage tank, 3... Screw feeder, 4... Cylindrical pipe, 4a... Straight pipe, 4
b... Wide diverging tube, 5... Screw shaft,
5a... Attached shaft part, 5b... Conical shaft part, 6... Input port, 7... Outlet port,
8... Swing damper, 12... Spring.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 円筒管と該円筒管内に横架せるスクリュー軸とからなり
円筒管の適所にあけられた投入口へと投入された粉粒体
が円筒管の管端から排出されるように構成されたスクリ
ューフィーダを、圧力差のある二基間の仕切壁を貫いて
横架すると共に、このスクリューフィーダの排出口に、
常時該排出口を閉塞する向きに弾性的に附勢されたダン
パーを配設してなる、圧力差のある二基間における粉粒
体の移送装置であって、前記スクリュー軸の排出側が、
先細り形状に形成されると共に、このスクリュー軸の先
端部近傍と排出口との間の円筒管の部分が逆テーパーの
末広管に形成されていること、を特徴としてなる粉粒体
の移送装置。
A screw feeder consisting of a cylindrical tube and a screw shaft disposed horizontally within the cylindrical tube, and configured so that powder and granules introduced into an inlet opened at an appropriate position in the cylindrical tube are discharged from the end of the cylindrical tube. is suspended horizontally through the partition wall between the two units where there is a pressure difference, and at the discharge port of this screw feeder,
A device for transferring powder or granular material between two units with a pressure difference, the device comprising a damper that is elastically biased in a direction that always closes the discharge port, wherein the discharge side of the screw shaft is
A device for transferring powder or granular material, characterized in that the cylindrical tube is formed into a tapered shape, and the portion of the cylindrical tube between the vicinity of the tip of the screw shaft and the discharge port is formed into a reversely tapered diverging tube.
JP3759579U 1979-03-22 1979-03-22 Device for transferring powder and granular materials between two chambers with a pressure difference Expired JPS6032018Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3759579U JPS6032018Y2 (en) 1979-03-22 1979-03-22 Device for transferring powder and granular materials between two chambers with a pressure difference

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3759579U JPS6032018Y2 (en) 1979-03-22 1979-03-22 Device for transferring powder and granular materials between two chambers with a pressure difference

Publications (2)

Publication Number Publication Date
JPS55136728U JPS55136728U (en) 1980-09-29
JPS6032018Y2 true JPS6032018Y2 (en) 1985-09-25

Family

ID=28900943

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3759579U Expired JPS6032018Y2 (en) 1979-03-22 1979-03-22 Device for transferring powder and granular materials between two chambers with a pressure difference

Country Status (1)

Country Link
JP (1) JPS6032018Y2 (en)

Also Published As

Publication number Publication date
JPS55136728U (en) 1980-09-29

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