JPH0215449B2 - - Google Patents
Info
- Publication number
- JPH0215449B2 JPH0215449B2 JP57051050A JP5105082A JPH0215449B2 JP H0215449 B2 JPH0215449 B2 JP H0215449B2 JP 57051050 A JP57051050 A JP 57051050A JP 5105082 A JP5105082 A JP 5105082A JP H0215449 B2 JPH0215449 B2 JP H0215449B2
- Authority
- JP
- Japan
- Prior art keywords
- hopper
- powder
- service
- valve
- pipe
- 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 - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/16—Gas pressure systems operating with fluidisation of the materials
- B65G53/18—Gas pressure systems operating with fluidisation of the materials through a porous wall
- B65G53/22—Gas pressure systems operating with fluidisation of the materials through a porous wall the systems comprising a reservoir, e.g. a bunker
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Mechanical Optical Scanning Systems (AREA)
- Air Transport Of Granular Materials (AREA)
Description
この発明は、微粉炭、セメント、水処理剤など
の粉体をホツパーから他のホツパーなどに補給す
る粉体供給方法に関するものである。
内部が加圧状態となるホツパーから粉体を補給
する粉体補給装置が考えられるが、この場合に、
圧力気体源と連通する送気パイプをホツパーの上
部に開口させると、ホツパー内の加圧に際し、ホ
ツパー内の粉体面上に圧力が加わり、粉体を圧縮
して密着させてしまい、ホツパーの下端部に設け
た粉体排出口から重力によつて粉体を落下させる
際に排出状態が悪くなるという問題がある。
この発明は、気送パイプをホツパーの粉体排出
口にできるだけ近接させることにより、前述した
問題を解決して、ホツパー内の圧力を高めるため
に圧力気体を導入する際に粉体を圧縮して密着さ
せることを防止し、粉体のスムーズな排出ができ
る粉体供給方法を提供することを目的としてい
る。
即ち本発明は気密構造となるサービスホツパー
と、該サービスホツパーの下部の粉体排出口と開
閉弁を有する継手を介して連結された受粉ホツパ
ーとを備え、該両ホツパーの内圧をほぼ均等に維
持しつつ前記ホツパー内の粉体を該受粉ホツパー
へ供給する粉体供給方法において、該両ホツパー
の上部空間を開閉弁を介して調圧パイプで連結す
ると共に圧力気体源と開閉弁を介して連通した先
端開口の送気パイプを、この先端からサービスホ
ツパーの粉体排出口までの距離をHとしこの粉体
排出口の直径をdとするときH≦3dとなるよう
にサービスホツパー内に配設し、調圧パイプの開
閉弁及び両ホツパー間の開閉弁を閉じた状態で且
つ上部空間が大気開放下に該サービスホツパーに
粉体を供給し、その後該サービスホツパーを気密
状態とし、送気パイプから圧力気体を送気してサ
ービスホツパーと受粉ホツパーとの内圧を均圧下
し、次いで送気パイプの開閉弁を閉じ且つ調圧パ
イプの開閉弁及び両ホツパー間の開閉弁を開き、
サービスホツパー内の粉体を受粉ホツパーへ供給
することを特徴とする粉体供給方法である。
以下、この発明の一実施例につき図面を参照し
て説明する。
図において、1はサービスホツパーであり、こ
のホツパー1の上端部に設けた粉体供給口2はフ
レキシブルパイプ3の上、下に開閉弁4,5をそ
れぞれ設けた継手6で送入手段である貯蔵ホツパ
ー7と接続されている。この貯蔵ホツパー7は図
示しない装置枠に固定されている。前記サービス
ホツパー1の下端部に設けた粉体排出口8は、サ
ービスホツパー1の下方に配置された受粉ホツパ
ー(以下の実施例では計量ホツパー9と表示して
いる)の上端部に設けた粉体導入口10と継手1
1を介して接続されている。この継手11はフレ
キシブルパイプ12の上、下に開閉弁13,14
がそれぞれ設けられたものである。前記計量ホツ
パー9の下部には粉体気送用のロータリー式定量
粉体供給装置15が一体に結合され、この粉体供
給装置15の下端部には粉体送出口16が設けら
れている。この粉体送出口16はフレキシブルパ
イプ17を適所にもつ粉体送出パイプ18によつ
て粉体供給装置15の下方に設置したエゼクター
方式の気送用混合器19に接続され、この混合器
19の吐出側には粉体気送パイプ20が連通され
ている。また、サービスホツパー1および計量ホ
ツパー9は図示しない装置枠に固定されたロード
セルのような秤量装置21および22にそれぞれ
支持されている。
前記サービスホツパー1、計量ホツパー9およ
び粉体供給装置15の圧力気体入口23,24お
よび25がそれぞれ開閉弁26,27,28を有
する送気パイプ29,30,31の先端開口で形
成され、これらの送気パイプ29,30,31は
開閉弁26,27,28と前記両ホツパー1,
9,粉体供給装置15の間にフレキシブルパイプ
32,33,34が設けられ、前記送気パイプ2
9,30,31は前記混合器19への送気パイプ
35と共に図示しない同一のブロワのような圧力
気体源と連通されている。また、計量ホツパー9
の上部に設けた圧力気体出口36には開閉弁3
7,38を有する圧抜パイプ39が連通され、こ
のパイプ39の先端は大気に開放されている。圧
抜パイプ39の開閉弁37,38間が連通パイプ
40でサービスホツパー1の上端部に連通され
て、サービスホツパー1と計量ホツパー9との上
部空間を結ぶ調圧パイプを構成している。前記両
ホツパー1,9間に設けた継手11の開閉弁1
3,14間のフレキシブルパイプ12以外の部分
には開閉弁42をもつパージパイプ41の一端が
連通され、このパイプ38の他端が大気に開放さ
れている。そして、サービスホツパー1の圧力気
体入口23は粉体排出口8にできるだけ近接させ
てある。すなわち、送気パイプ23が少なくとも
サービスホツパー1内では水平面に対し60゜〜90゜
傾斜して粉体排出口8の真上に先端開口すなわち
圧力気体入口23が配置され、この入口23から
粉体排出口8までの距離をH、この粉体排出口8
の直径をdとして、H≦3dとなるようにされて
いる。
次に、前述のように構成された粉体計量装置の
動作について説明する。
計量ホツパー9に上限まで粉体が投入されてい
る状態で、粉体供給装置15を駆動させると、圧
力気体源から所要圧力に調整されている空気のよ
うな気体が送気パイプ30,31,35から計量
ホツパー9、粉体供給装置15および気送用混合
器19に供給される。これによつて計量ホツパー
9内の粉体は重力と圧力気体との作用で粉体供給
装置15のロータの回転により、所定量ずつ切出
されて粉体送出パイプ18を通り、気送用混合器
19に送られ、これにも圧力気体が送られている
ため、この気体と混合して粉体気送パイプ20で
所要の機器、装置へ供給される。この場合に、サ
ービスホツパー1内の圧力が計量ホツパー9内の
圧力より低い状態では圧抜パイプ39の開閉弁3
7、両ホツパー1,9間の継手11の開閉弁1
3,14、サービスホツパー1の送気パイプ29
の開閉弁26は閉じており、計量ホツパー9、粉
体供給装置15、気送用混合器19内の圧力が低
下することを防止する。
そして、サービスホツパー1内は空になつてい
るので、計量ホツパー9内の粉体が少し減少した
時点で貯蔵ホツパー7からサービスホツパー1内
に粉体を入れる。すなわち、開閉弁37,13,
14,26は閉じたままで開閉弁38、サービス
ホツパー1と貯蔵ホツパー7との間の継手6の開
閉弁4,5を開き、貯蔵ホツパー7から重力によ
つて粉体をサービスホツパー1内に落下させる。
なお、この場合に、サービスホツパー1内に落下
する粉体と置換してこのホツパー1内の気体を連
通パイプ40、圧抜パイプ39の開閉弁38より
大気側部分を経て大気へ放出する。このサービス
ホツパー1への粉体の送入は計量ホツパー9内の
粉体が下限まで達しないうちに完了し、サービス
ホツパー1内の粉体が上限に達する。
サービスホツパー1内の粉体が上限に達する
と、これを図示しないレベル計などで検出して、
開閉弁38,4,5を閉じ、開閉弁26を開く。
これによつて、送気パイプ29からサービスホツ
パー1内に圧力気体が導入される。なお、この場
合に開閉弁37,13,14は閉じたままであ
る。サービスホツパー1内の圧力が計量ホツパー
9内の圧力と均等になるまで高くなるとこれをサ
ービスホツパー1、計量ホツパー9の秤量装置2
1,22で検出して開閉弁26を閉じ、この状態
を計量ホツパー9内の粉体が下限に達するまで維
持する。
計量ホツパー9から気送用混合器19への粉体
の供給は、前述したサービスホツパー1への粉体
の送入およびサービスホツパー1と計量ホツパー
9との均圧動作中も続けられる。計量ホツパー9
内の粉体が下限に達すると、これの適宜の手段で
検出して開閉弁37,13,14を開く。これに
よつてサービスホツパー1から粉体が重力で計量
ホツパー9に短時間内に補給される。この場合
に、計量ホツパー9に補給される粉体と置換して
このホツパー9内の空気が圧抜パイプ39の一部
と連通パイプ40を経てサービスホツパー1へ導
かれるので、両ホツパー1,9内の圧力は均等に
保たれる。サービスホツパー1内の粉体の全部が
計量ホツパー9に補給されてこのホツパー9内の
粉体が上限に達すると、これを検出して開閉弁3
7,13,14を閉じ、以下前述した動作を繰返
す。
そして、開閉弁26を開いて送気パイプ29か
らサービスホツパー1内に圧力気体を導入する際
に、送気パイプ29はサービスホツパー1下端部
の粉体排出口8の近くに圧力気体入口23を設け
てあるので、圧力気体による圧力が粉体の下部か
ら上部に向かつてかかり、粉体を圧縮して密着さ
せることがない。したがつて、サービスホツパー
1と計量ホツパー9との内圧を均等に維持しつつ
開閉弁13,14を開いて、サービスホツパー1
から計量ホツパー9に粉体を補給する際に粉体が
重力によつてスムーズにサービスホツパー1から
落下排出される。ここで、送気パイプ29の先端
即ち圧力気体入口23の粉体排出口8からの距離
Hの変化によつてサービスホツパー1内の粉体排
出状態を調べてみると第1表の如き結果を得た。
この実験では粉体排出口8の直径dを250mmとし、
Hを100,200,400,600,700,800mmとした場合
についてその排出状況を調べたものである。
The present invention relates to a powder supply method for supplying powder such as pulverized coal, cement, water treatment agent, etc. from one hopper to another hopper. A powder replenishment device that replenishes powder from a hopper whose interior is pressurized can be considered, but in this case,
If the air supply pipe that communicates with the pressure gas source is opened at the top of the hopper, pressure will be applied to the powder surface in the hopper when the hopper is pressurized, compressing the powder and making it adhere tightly. There is a problem in that when the powder is dropped by gravity from the powder discharge port provided at the lower end, the discharge condition becomes poor. This invention solves the aforementioned problems by placing the pneumatic pipe as close as possible to the powder outlet of the hopper, thereby compressing the powder when introducing pressurized gas to increase the pressure inside the hopper. The object of the present invention is to provide a powder supply method that prevents the powder from coming into close contact and allows smooth discharge of the powder. That is, the present invention includes a service hopper having an airtight structure, and a pollination hopper that is connected to a powder discharge port at the lower part of the service hopper via a joint having an on-off valve, so that the internal pressure of both hoppers is approximately equalized. In the powder supply method, the powder in the hopper is supplied to the pollination hopper while maintaining the powder in the pollination hopper. Connect the air supply pipe with the opening at the tip to the service hopper so that H≦3d, where the distance from the tip to the powder discharge port of the service hopper is H, and the diameter of this powder discharge port is d. Powder is supplied to the service hopper with the on-off valve of the pressure regulating pipe and the on-off valve between both hoppers closed and with the upper space open to the atmosphere, and then the service hopper is airtight. Then, the internal pressure of the service hopper and the pollination hopper is equalized by supplying pressurized gas from the air supply pipe, and then the on-off valve of the air supply pipe is closed, and the on-off valve of the pressure regulating pipe and the opening and closing between the two hoppers are open the valve,
This is a powder supply method characterized by supplying powder in a service hopper to a pollination hopper. Hereinafter, one embodiment of the present invention will be described with reference to the drawings. In the figure, 1 is a service hopper, and a powder supply port 2 provided at the upper end of this hopper 1 is connected to a joint 6 with on-off valves 4 and 5 provided above and below a flexible pipe 3 as a feeding means. It is connected to a certain storage hopper 7. This storage hopper 7 is fixed to a device frame (not shown). The powder discharge port 8 provided at the lower end of the service hopper 1 is provided at the upper end of a pollination hopper (indicated as a weighing hopper 9 in the following examples) located below the service hopper 1. Powder inlet 10 and joint 1
1. This joint 11 has on-off valves 13 and 14 located above and below the flexible pipe 12.
are provided for each. A rotary quantitative powder supply device 15 for pneumatically feeding powder is integrally connected to the lower part of the measuring hopper 9, and a powder delivery port 16 is provided at the lower end of the powder supply device 15. This powder delivery port 16 is connected to an ejector-type pneumatic mixer 19 installed below the powder supply device 15 by a powder delivery pipe 18 having a flexible pipe 17 in place. A powder pneumatic pipe 20 is connected to the discharge side. Further, the service hopper 1 and the weighing hopper 9 are respectively supported by weighing devices 21 and 22, such as load cells, which are fixed to a device frame (not shown). Pressure gas inlets 23, 24 and 25 of the service hopper 1, metering hopper 9 and powder supply device 15 are formed by openings at the ends of air supply pipes 29, 30 and 31 having on-off valves 26, 27 and 28, respectively, These air supply pipes 29, 30, 31 are connected to on-off valves 26, 27, 28 and both hoppers 1,
9. Flexible pipes 32, 33, and 34 are provided between the powder supply device 15, and the air supply pipe 2
9, 30, and 31 are in communication with the air supply pipe 35 to the mixer 19 and a pressure gas source such as the same blower (not shown). Also, weighing hopper 9
An on-off valve 3 is provided at the pressure gas outlet 36 provided at the top of the
A depressurizing pipe 39 having pipes 7 and 38 is connected, and the tip of this pipe 39 is open to the atmosphere. The opening/closing valves 37 and 38 of the pressure relief pipe 39 are connected to the upper end of the service hopper 1 through a communication pipe 40, forming a pressure regulating pipe that connects the upper spaces of the service hopper 1 and the weighing hopper 9. . Opening/closing valve 1 of the joint 11 provided between the two hoppers 1 and 9
One end of a purge pipe 41 having an on-off valve 42 is communicated with the portion other than the flexible pipe 12 between 3 and 14, and the other end of this pipe 38 is open to the atmosphere. The pressurized gas inlet 23 of the service hopper 1 is placed as close as possible to the powder outlet 8. That is, at least inside the service hopper 1, the air supply pipe 23 is inclined at an angle of 60° to 90° with respect to the horizontal plane, and a tip opening, that is, a pressurized gas inlet 23 is disposed directly above the powder discharge port 8. The distance to the powder discharge port 8 is H, and the distance to the powder discharge port 8 is
Letting the diameter of d be H≦3d. Next, the operation of the powder measuring device configured as described above will be explained. When the powder supply device 15 is driven with the powder being charged up to the upper limit in the metering hopper 9, gas such as air whose pressure has been adjusted to the required pressure is supplied from the pressure gas source to the air supply pipes 30, 31, 35 to the metering hopper 9, powder supply device 15 and pneumatic mixer 19. As a result, the powder in the weighing hopper 9 is cut out in predetermined amounts by the rotation of the rotor of the powder supply device 15 under the action of gravity and pressure gas, passes through the powder delivery pipe 18, and is mixed for pneumatic feeding. The powder is sent to the powder container 19, and since pressure gas is also sent thereto, the powder is mixed with this gas and supplied to the required equipment and devices through the powder pneumatic pipe 20. In this case, if the pressure in the service hopper 1 is lower than the pressure in the metering hopper 9, the on-off valve 3 of the pressure relief pipe 39
7. Opening/closing valve 1 of joint 11 between both hoppers 1 and 9
3, 14, Air supply pipe 29 of service hopper 1
The on-off valve 26 is closed to prevent the pressure in the metering hopper 9, the powder supply device 15, and the pneumatic mixer 19 from decreasing. Then, since the inside of the service hopper 1 is empty, powder is put into the service hopper 1 from the storage hopper 7 when the amount of powder in the weighing hopper 9 decreases a little. That is, the on-off valves 37, 13,
14 and 26 remain closed, and the on-off valves 38 and the on-off valves 4 and 5 of the joint 6 between the service hopper 1 and the storage hopper 7 are opened, and the powder is transferred from the storage hopper 7 into the service hopper 1 by gravity. let it fall.
In this case, the gas in the service hopper 1 is replaced by the powder falling into the service hopper 1 and released into the atmosphere through the communication pipe 40 and the on-off valve 38 of the depressurization pipe 39 through the atmosphere side portion. The feeding of the powder to the service hopper 1 is completed before the powder in the weighing hopper 9 reaches the lower limit, and the powder in the service hopper 1 reaches the upper limit. When the powder in the service hopper 1 reaches the upper limit, it is detected by a level meter (not shown), etc.
The on-off valves 38, 4, and 5 are closed, and the on-off valve 26 is opened.
As a result, pressurized gas is introduced into the service hopper 1 from the air supply pipe 29. In this case, the on-off valves 37, 13, and 14 remain closed. When the pressure in the service hopper 1 increases until it becomes equal to the pressure in the weighing hopper 9, the service hopper 1 and the weighing device 2 of the weighing hopper 9
1 and 22, the on-off valve 26 is closed, and this state is maintained until the powder in the weighing hopper 9 reaches the lower limit. The supply of powder from the metering hopper 9 to the pneumatic mixer 19 continues during the above-described feeding of the powder to the service hopper 1 and the pressure equalization operation between the service hopper 1 and the metering hopper 9. Weighing hopper 9
When the powder inside reaches the lower limit, it is detected by an appropriate means and the on-off valves 37, 13, 14 are opened. As a result, powder is replenished from the service hopper 1 to the weighing hopper 9 by gravity within a short time. In this case, the air in this hopper 9 is replaced with the powder supplied to the weighing hopper 9 and is led to the service hopper 1 via a part of the pressure relief pipe 39 and the communication pipe 40, so that both hoppers 1, The pressure inside 9 is kept equal. When all of the powder in the service hopper 1 is replenished to the weighing hopper 9 and the powder in this hopper 9 reaches its upper limit, this is detected and the on-off valve 3
7, 13, and 14, and repeat the above-described operation. When the on-off valve 26 is opened to introduce pressurized gas into the service hopper 1 from the air supply pipe 29, the air supply pipe 29 is placed near the powder discharge port 8 at the lower end of the service hopper 1. 23, the pressure of the pressurized gas is applied from the bottom to the top of the powder, and the powder is not compressed and brought into close contact with each other. Therefore, the on-off valves 13 and 14 are opened while maintaining the internal pressures of the service hopper 1 and the weighing hopper 9 evenly, and the service hopper 1 is opened.
When replenishing the powder from the service hopper 9 to the weighing hopper 9, the powder is smoothly dropped and discharged from the service hopper 1 by gravity. Here, when examining the powder discharge state in the service hopper 1 by changing the distance H from the tip of the air supply pipe 29, that is, the distance H from the pressure gas inlet 23 to the powder discharge port 8, the results shown in Table 1 are obtained. I got it.
In this experiment, the diameter d of the powder discharge port 8 was 250 mm.
The discharge status was investigated when H was set to 100, 200, 400, 600, 700, and 800 mm.
【表】
この結果から明らかなように距離Hが3dを越
えると送入される圧力空気によつて粉体の圧縮、
密着が生じてホツパー内に粉体のアーチが発生し
てしまうため粉体の排出が不可能となる。ところ
が、H≦3dであれば、送入される圧力空気が粉
体層の中を通つて上昇するため圧密した粉体は再
びほぐされ、流動化してホツパー内での粉体の圧
縮、密着が解消でき、特に、0.5d≦H≦2dの範囲
が粉体の補給に好ましい。
また、前述した動作は、制御盤に検出信号を送
り、この制御盤からの指令により電気的手段、あ
るいはこれと圧縮空気などを用いて自動制御で行
う。さらに、この実施例において、計量ホツパー
に粉体の異常下限を検出して全装置を停止させる
手段を設けたり、計量ホツパーの秤量装置で計量
ホツパー内の圧力に応じ、粉体供給装置の電動機
の回転数を制御し、粉体供給量を適切にすること
が好ましい。
さらに、この発明は、ホツパー内に圧力気体を
導入し、かつ気密構造となるホツパーからの粉体
補給装置に広く適用できるが、実施例のように、
粉体を補給するホツパーと粉体が補給されるホツ
パーとを連通させて圧力を均等に維持しつつ粉体
を補給させるものに適用して大きな利点がある。
以上説明したように、この発明の粉体補給装置
は、粉体供給口を上端部に、粉体排出口を下端部
にそれぞれ設け、この排出口の下部に開閉弁を設
け気密構造となるホツパー内に、圧力気体源と開
閉弁を介して連通する送気パイプの先端を開口さ
せ、この送気パイプの先端を、この先端からホツ
パーの粉体排出口までの距離をH、この粉体排出
口の直径をdとして、H≦3dとなるように配設
したので、送気パイプから圧力気体をホツパーに
導入して内圧を高くする際に粉体を圧縮、密着さ
せることがなく、したがつて、粉体の排出口から
排出をスムーズに行うことができるという効果が
ある。[Table] It is clear from this result that when the distance H exceeds 3d, the powder is compressed by the pressure air introduced.
Due to the close contact, an arch of powder is generated in the hopper, making it impossible to discharge the powder. However, if H≦3d, the compressed air passes through the powder bed and rises, loosening the compacted powder again and fluidizing it, which prevents the compaction and adhesion of the powder in the hopper. In particular, the range of 0.5d≦H≦2d is preferable for powder replenishment. Further, the above-mentioned operations are automatically controlled by sending a detection signal to a control panel, and using electrical means or compressed air in conjunction with the same based on commands from the control panel. Furthermore, in this embodiment, a means is provided in the weighing hopper to detect the abnormal lower limit of the powder and stop the entire device, and the weighing device of the weighing hopper adjusts the electric motor of the powder feeding device according to the pressure inside the weighing hopper. It is preferable to control the rotation speed and make the powder supply amount appropriate. Furthermore, the present invention can be widely applied to a powder replenishment device from a hopper that introduces pressurized gas into the hopper and has an airtight structure, but as in the embodiment,
There is a great advantage in applying this method to a device in which a hopper for replenishing powder and a hopper for replenishing powder are communicated with each other to replenish powder while maintaining an even pressure. As explained above, the powder replenishment device of the present invention has a powder supply port provided at the upper end and a powder discharge port provided at the lower end, and an on-off valve provided at the bottom of the discharge port to form an airtight hopper. The tip of the air pipe that communicates with the pressure gas source via the on-off valve is opened, and the distance from the tip of the air pipe to the powder discharge port of the hopper is H, and the powder discharge port is Since the diameter of the outlet is d, it is arranged so that H≦3d, so that when pressure gas is introduced from the air pipe into the hopper to increase the internal pressure, the powder is not compressed and brought into close contact. Therefore, there is an effect that the powder can be smoothly discharged from the discharge port.
図はこの発明の一実施例を示す構成説明図であ
る。
1…サービスホツパー、2…粉体導入口、5…
開閉弁、8…粉体排出口、13…開閉弁、23…
圧力気体入口、26…開閉弁、29…送気パイ
プ。
The figure is a configuration explanatory diagram showing an embodiment of the present invention. 1...Service hopper, 2...Powder inlet, 5...
On-off valve, 8... Powder discharge port, 13... On-off valve, 23...
Pressure gas inlet, 26...opening/closing valve, 29...air supply pipe.
Claims (1)
ビスホツパーの下部の粉体排出口と開閉弁を有す
る継手を介して連結された受粉ホツパーとを備
え、該両ホツパーの内圧をほぼ均等に維持しつつ
前記ホツパー内の粉体を該受粉ホツパーへ供給す
る粉体供給方法において、該両ホツパーの上部空
間を開閉弁を介して調圧パイプで連結すると共に
圧力気体源と開閉弁を介して連通した先端開口の
送気パイプを、この先端からサービスホツパーの
粉体排出口までの距離をHとしこの粉体排出口の
直径をdとするときH≦3dとなるようにサービ
スホツパー内に配設し、調圧パイプの開閉弁及び
両ホツパー間の開閉弁を閉じた状態で且つ上部空
間が大気開放下に該サービスホツパーに粉体を供
給し、その後該サービスホツパーを気密状態と
し、送気パイプから圧力気体を送気してサービス
ホツパーと受粉ホツパーとの内圧を均圧化し、次
いで送気パイプの開閉弁を閉じ且つ調圧パイプの
開閉弁及び両ホツパー間の開閉弁を開き、サービ
スホツパー内の粉体を受粉ホツパーへ供給するこ
とを特徴とする粉体供給方法。1. A service hopper with an airtight structure, and a pollination hopper connected to a powder discharge port at the lower part of the service hopper via a joint having an on-off valve, and maintains the internal pressure of both hoppers almost equally. In the powder supply method for supplying the powder in the hopper to the pollination hopper, the upper spaces of both hoppers are connected by a pressure regulating pipe via an on-off valve and communicated with a pressure gas source via an on-off valve. Arrange the air supply pipe with the opening at the tip in the service hopper so that H≦3d, where the distance from the tip to the powder discharge port of the service hopper is H, and the diameter of this powder discharge port is d. supplying the powder to the service hopper with the on-off valve of the pressure regulating pipe and the on-off valve between both hoppers closed and with the upper space open to the atmosphere, and then making the service hopper airtight, Pressure gas is sent from the air supply pipe to equalize the internal pressure between the service hopper and the pollination hopper, and then the on-off valve of the air supply pipe is closed, and the on-off valve of the pressure regulating pipe and the on-off valve between both hoppers are opened. , a powder supply method characterized by supplying powder in a service hopper to a pollination hopper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5105082A JPS58172115A (en) | 1982-03-31 | 1982-03-31 | Powder supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5105082A JPS58172115A (en) | 1982-03-31 | 1982-03-31 | Powder supply device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58172115A JPS58172115A (en) | 1983-10-08 |
| JPH0215449B2 true JPH0215449B2 (en) | 1990-04-12 |
Family
ID=12875968
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5105082A Granted JPS58172115A (en) | 1982-03-31 | 1982-03-31 | Powder supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58172115A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4933378A (en) * | 1972-08-07 | 1974-03-27 | ||
| JPS5742900Y2 (en) * | 1977-12-01 | 1982-09-21 |
-
1982
- 1982-03-31 JP JP5105082A patent/JPS58172115A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58172115A (en) | 1983-10-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5370951B2 (en) | Pneumatic transport method and apparatus for bulk material with poor flow | |
| JP2703690B2 (en) | Ultrafine powder quantitative batch feeder | |
| US4501518A (en) | Automatic pneumatic feeder | |
| US5503198A (en) | Method and apparatus for filling containers with dry ice pellets | |
| US3840155A (en) | Nuclear fuel handling powder container | |
| US3315824A (en) | Method and apparatus for continuous gravity feed of fluent materials | |
| CZ297609B6 (en) | Method of and apparatus for conveying particulate matter to equipment receiving the same | |
| CN218664275U (en) | Automatic coal conveying device | |
| JPH0215449B2 (en) | ||
| JPS58168919A (en) | Weighing apparatus of powdered body | |
| US2326276A (en) | Method and apparatus for feeding hygroscopic and reactive materials | |
| CA1291192C (en) | Material conveying apparatus | |
| JP2547228B2 (en) | Powder filling device | |
| JP7058406B2 (en) | Powder supply system | |
| JPH0449052B2 (en) | ||
| US3385634A (en) | Device for continuous hydropneumatic conveyance of powder-like material | |
| CN213107497U (en) | Powder additive feeding machine | |
| KR20130020163A (en) | Apparatus for pneumatically transporting powdered coal to a high pressure | |
| JPH085158Y2 (en) | Powder dispensing device | |
| CN216509214U (en) | Powder quantitative split charging equipment | |
| CN221419920U (en) | Pneumatic conveying system for powdery or granular materials | |
| CN223836621U (en) | A material conveying device | |
| KR100611237B1 (en) | Feeding Particle Dispersion Feeder | |
| CN219382857U (en) | Tea metering packaging machine | |
| JP4893993B2 (en) | Pressurized tank, apparatus for feeding powder into transport pipe, and method for feeding the same |