JPS60197524A - Rotary valve for feeding powdery material - Google Patents

Rotary valve for feeding powdery material

Info

Publication number
JPS60197524A
JPS60197524A JP5052284A JP5052284A JPS60197524A JP S60197524 A JPS60197524 A JP S60197524A JP 5052284 A JP5052284 A JP 5052284A JP 5052284 A JP5052284 A JP 5052284A JP S60197524 A JPS60197524 A JP S60197524A
Authority
JP
Japan
Prior art keywords
powder
gas
powdery material
case
rotor
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.)
Pending
Application number
JP5052284A
Other languages
Japanese (ja)
Inventor
Shiro Otaka
大高 士郎
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.)
Hitachi Plant Construction Co Ltd
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Construction Co Ltd
Hitachi Plant Technologies 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 Hitachi Plant Construction Co Ltd, Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Construction Co Ltd
Priority to JP5052284A priority Critical patent/JPS60197524A/en
Publication of JPS60197524A publication Critical patent/JPS60197524A/en
Pending 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
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/40Feeding or discharging devices
    • B65G53/46Gates or sluices, e.g. rotary wheels
    • B65G53/4608Turnable elements, e.g. rotary wheels with pockets or passages for material
    • B65G53/4625Turnable elements, e.g. rotary wheels with pockets or passages for material with axis of turning perpendicular to flow
    • B65G53/4633Turnable elements, e.g. rotary wheels with pockets or passages for material with axis of turning perpendicular to flow the element having pockets, rotated from charging position to discharging position, i.e. discrete flow

Abstract

PURPOSE:To prevent an influence from being exercised on powdery material feeding action by discharged gas and to enable smooth feed of quantities of powder materials, by a method wherein a passage for introduction of a powdery material is formed separately from a passage for discharge of gas. CONSTITUTION:A powdery material 80 is fed through a hopper 72 in the direction of an arrow mark T as a rotor 52 is rotated. The powdery material 80 is dropped in a case 50 under gravity, and is contained in chambers, divided by vanes 54, once. Since the vanes 54 are rotated togetherwith the rotor 52, the powdry material 80 is dropped, as shown by an arrow mark U, in a pressure tank 76 with the rotation of the rotor. Pressure gas, of which a chamber on the tank 76 side is full, is forced into contact with a gas discharge room 62 with the rotation of the rotor 52, and is discharged through a discharge hole 64. In which case, the powdery material 80 is dropped in a spot about right below an introduction 58. Even in case the powdery material is temporarily accumulated in a chamber formed with the vane plates 54, the shape of such accumulation maintains an angle of repose, and thereby the powdery material 80 is prevented from enterance and accumulation in the gas discharge room 62. This causes discharge gas to be discharged to the outside through the discharge room 62 and a discharge hole 64.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、粉体を圧力タンクまたけ圧力配管等に供給す
る際に用いられる粉体供給用ロータリーパルプに関する
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a rotary pulp for supplying powder, which is used when supplying powder to pressure piping, etc. across a pressure tank.

〔背景技術〕[Background technology]

従来のこの種のロータリーバルブを第1図に示す。この
図に2いて、中空円筒状のケース10内の中心軸線上に
はローター12が回転自在に設置されておp、このロー
ター12には、前記ケース10内を複数の部屋に分割し
該ローター12と一体にケース10内を回転する羽根板
14.・・・、14が取シ付けられている。また、前記
ケース10の上部には、外周部からケース10内に貫通
する開口部よシなる粉体導入口16が設けられ、下部に
は同様の粉体排出口18が設けられている。
A conventional rotary valve of this type is shown in FIG. In this figure, a rotor 12 is rotatably installed on the central axis of a hollow cylindrical case 10. A vane plate 14 that rotates inside the case 10 together with the vane plate 12. ..., 14 are attached. Further, a powder inlet 16, which is an opening penetrating into the case 10 from the outer periphery, is provided in the upper part of the case 10, and a similar powder outlet 18 is provided in the lower part.

この種のロータリーバルブを用いて圧力タンク20等に
粉体30を供給するには、排出口18ケ圧力タンク20
の粉体供給口22に接続するとともに、導入口16をホ
ッパ24に接続する。この場合に用いられるホッパ24
は、接続部付近が2重構造に形成されておシ、粉体30
は内筒26からロータリーバルブのケース10内に導入
され、加圧されたガスは外筒28から外部に放出される
ようになっている。すなわち、ローター12を図の矢印
P方向に回転しつつ粉体30を図の矢印Qの方向に供給
すると、粉体30は羽根板14で分割された各部屋に一
旦収容され、ローター12の回転につれて順次矢印几で
示すように圧力タンク20内に落下して供給される。こ
の際圧力タンク20内の圧力と外気の圧力との圧力差は
羽根板14゜・・・、14によって維持される。しかし
、圧力タンク20と接した部屋には加圧気体が充満され
、これが回転するにつれて導入口16に至シ、外気と接
するとその圧力差によって気体が膨張して余分な気体は
放出される。この場合、内筒26内は粉体30によって
充満されているから外筒28?]l−通じて外部に排出
されるものである。
In order to supply the powder 30 to the pressure tank 20 etc. using this type of rotary valve, there are 18 discharge ports in the pressure tank 20, etc.
The inlet 16 is connected to the powder supply port 22 of the hopper 24 . Hopper 24 used in this case
The vicinity of the connection part is formed in a double structure, and the powder 30
is introduced into the case 10 of the rotary valve from the inner cylinder 26, and the pressurized gas is discharged to the outside from the outer cylinder 28. That is, when the powder 30 is supplied in the direction of the arrow Q in the figure while rotating the rotor 12 in the direction of the arrow P in the figure, the powder 30 is temporarily accommodated in each chamber divided by the vanes 14, and the rotation of the rotor 12 As time passes, the liquid drops and is supplied into the pressure tank 20 as shown by the arrows. At this time, the pressure difference between the pressure inside the pressure tank 20 and the pressure of the outside air is maintained by the vanes 14°..., 14. However, the room in contact with the pressure tank 20 is filled with pressurized gas, and as it rotates, it reaches the inlet 16, and when it comes into contact with outside air, the gas expands due to the pressure difference and excess gas is released. In this case, since the inner cylinder 26 is filled with powder 30, the outer cylinder 28? ]l- is discharged to the outside through.

このような従来のロータリーパルプにおいては、外筒2
8を通じて外部に放出される気体が増大するにつれて粉
体30が上部に吹き上げられ供給効率が減少するととも
に、放出気体が一定値以上になると粉体30が内筒26
と外筒28との間に充満して供給不能となることがある
。したがって、放出気体を所定の値以下におさえておが
なけれはな゛らない。一方、放出気体の量は、圧力タン
ク2゜の圧力値及びローター12の回転数に依存するの
で、圧力タンク20の圧力とローター12の回転数とは
一定の値以下にしなければならない。例えば、圧力タン
ク20の圧力が大きいときは回転数を減少しなければな
らず、逆に供給量を増大しようとすると圧力タンク20
の圧力を減少させなければならない。ローター12の回
転数減少は粉体供給量の減少を意味し、圧力タンク20
における圧力減少の要請はこの種のロータリーパルプの
応用範囲を著しくせばめることとなる。それ故、従来の
この種のロータリーパルプは結局において粉体の供給量
を一定値以上にすることができず、また、圧力変動その
他の要因によって供給不能となる危険を有するものであ
った。
In such conventional rotary pulp, the outer cylinder 2
As the amount of gas released to the outside through the tube 8 increases, the powder 30 is blown up to the top and the supply efficiency decreases.
The space between the container and the outer cylinder 28 may become full, making it impossible to supply the liquid. Therefore, it is necessary to keep the released gas below a predetermined value. On the other hand, since the amount of released gas depends on the pressure value of the pressure tank 2° and the rotation speed of the rotor 12, the pressure of the pressure tank 20 and the rotation speed of the rotor 12 must be kept below a certain value. For example, when the pressure in the pressure tank 20 is high, the rotation speed must be reduced, and conversely, when trying to increase the supply amount, the pressure tank 20
pressure must be reduced. A decrease in the rotation speed of the rotor 12 means a decrease in the amount of powder supplied, and the pressure tank 20
The requirement for pressure reduction in this type of rotary pulp significantly narrows the range of applications for this type of rotary pulp. Therefore, in the conventional rotary pulp of this type, it was not possible to increase the amount of powder supplied above a certain value, and there was a risk that supply could not be achieved due to pressure fluctuations or other factors.

〔発明の目的〕[Purpose of the invention]

本発明は上記事実を考慮し、放出気体の流路と粉体の通
路とが別個になるようにすることによって上記欠点を除
去し、多量の粉体の供給を可能にするとともに供給不能
となる危険のない粉体供給用ロータリーパルプを提供す
ることを目的とする。
The present invention takes the above facts into account and eliminates the above disadvantages by making the flow path for the discharged gas and the powder path separate, thereby making it possible to supply a large amount of powder and at the same time making it impossible to supply the powder. The purpose is to provide rotary pulp for powder feeding without any danger.

〔発明の構成〕[Structure of the invention]

本発明に係る粉体供給用ロータリーパルプでは中空円筒
状のケースと、このケース内の中心軸線上に回転自在に
設置されたローターと、このローターに取シ付けられて
おシ前記ケース内を複数の部屋に分割゛するとともに該
ケース内を回転可能に形成された羽根板と、前記ケース
上部に設けられておシ該ケース外周から内周へ貫通する
粉体導入口と、前記ケース下部に設けられておシ該ケー
ス外周から内周へ貫通する粉体排出口と、前記粉体導入
口の近傍に該導入口とは別個に設けられておシ前記ケー
ス外周から内周へ貫通するガス放出口とからなるもので
、ガス放出の流路と粉体供給の通路とを別個にすること
によって多量の粉体の供給を可能にするとともに供給不
能となる危険のないものとしたものである。
The rotary pulp for powder supply according to the present invention includes a hollow cylindrical case, a rotor rotatably installed on the central axis within the case, and a plurality of rotary rotors attached to the rotor. A vane plate divided into two chambers and rotatable within the case, a powder inlet provided at the top of the case and penetrating from the outer circumference to the inner circumference of the case, and a powder inlet provided at the bottom of the case. A powder discharge port penetrating from the outer periphery to the inner periphery of the case, and a gas discharge port penetrating from the outer periphery to the inner periphery of the case, and a By separating the gas discharge passage and the powder supply passage, it is possible to supply a large amount of powder and there is no danger of supply failure.

〔発明の実施例〕[Embodiments of the invention]

第2図には、本発明に係る粉体供給用ロータリーパルプ
の実施例が示されている。この実施例では、中空円筒状
のケース50内の中心軸線上にローター52が回転自在
に設置され、とのローター52の半径方向には前記ケー
ス50内を複数の部屋に分割するとともに該ケース50
内を回転する4枚の羽根板54.・・・、54が取シ付
けられている。
FIG. 2 shows an embodiment of the rotary pulp for supplying powder according to the present invention. In this embodiment, a rotor 52 is rotatably installed on the central axis inside a hollow cylindrical case 50, and the inside of the case 50 is divided into a plurality of chambers in the radial direction of the rotor 52.
Four blade plates 54 rotating inside. ..., 54 are attached.

また、前記ケース50の上部にはクー250内周から外
部に開口する粉体導入口56が穿設され、該導入口56
には上方に向かって粉体導入管58が立設され、その上
端部にはフランジ部6oが形成されている。また、前記
導入管58の両側には、ケース50内に開口部を接する
ガス放出ルーム62゜62が設けられ、該放出ルーム6
2には外部に通ずるガス放出孔64.64力長設けられ
ている。さらに、前記ケース50の下部には該ケース5
0内 □周から外部に開口する粉体排出口66が穿設さ
れ、排出口66には下方に向かって粉体排出管68が立
設されているとともに、その先端部には7ランク部70
が形成されている。この7ランク部60は、粉体80を
供給するためのホッパ72の7ランク部74に接続され
、また排出導管68の7ランク部70は粉体が供給され
る圧力タンク76の7272部78に接合されるもので
ある。
Further, a powder introduction port 56 that opens from the inner circumference of the cooler 250 to the outside is bored in the upper part of the case 50.
A powder introduction pipe 58 is erected upward, and a flange portion 6o is formed at its upper end. Further, on both sides of the introduction pipe 58, gas release rooms 62°62 are provided, the openings of which are in contact with the inside of the case 50.
2 is provided with gas discharge holes 64 and 64 that communicate with the outside. Further, the lower part of the case 50 is provided with the case 50.
0 inside □ A powder discharge port 66 that opens from the periphery to the outside is drilled, and a powder discharge pipe 68 is erected downward from the discharge port 66, and a 7-rank part 70 is provided at the tip of the powder discharge port 66.
is formed. This 7-rank section 60 is connected to a 7-rank section 74 of a hopper 72 for supplying the powder 80, and the 7-rank section 70 of the discharge conduit 68 is connected to a 7272 section 78 of a pressure tank 76 to which the powder is supplied. It is something that is joined.

次に本実施例の作用を説明する。ローター52を第3図
の矢印S方向に回転しつつ粉体80を矢印Tのようにホ
ッパ72から供給する。粉体80は重力によってケース
50内に落下し、前記羽根板54で分割された各部屋に
一旦収容される。該羽根板54はローター52とともに
回転しているから、粉体80はその回転に従って順次図
の矢印Uで示すように圧力タンク76内に落下する。こ
の場合、圧力タンク76内の圧力と外気の圧力との圧力
差は、羽根板54.・・・、54によって維持される。
Next, the operation of this embodiment will be explained. Powder 80 is supplied from the hopper 72 in the direction of arrow T while the rotor 52 is rotated in the direction of arrow S in FIG. The powder 80 falls into the case 50 due to gravity, and is temporarily accommodated in each chamber divided by the wing plate 54. Since the vane plate 54 rotates together with the rotor 52, the powder 80 sequentially falls into the pressure tank 76 as shown by arrow U in the figure as the vane plate 54 rotates. In this case, the pressure difference between the pressure inside the pressure tank 76 and the pressure of the outside air is determined by the pressure difference between the pressure inside the pressure tank 76 and the pressure of the outside air. ..., maintained by 54.

また、圧力タンク76@の部屋に充満した加圧気体はロ
ーター52の回転に伴なってガス放出ルーム62に接し
、放出孔64から外部に放出される。その際、粉体80
は導入管58のほぼ真下に落下し、羽根板54.・・・
、54で形成される部屋に一時堆積する場合においても
、その堆積の形状は安息角を維持するから前記ガス放出
ルーム62内に粉体80が侵入堆積するおそれはない。
Further, the pressurized gas filling the chamber of the pressure tank 76@ comes into contact with the gas release room 62 as the rotor 52 rotates, and is released to the outside from the release hole 64. At that time, powder 80
falls almost directly below the introduction pipe 58, and the blade plate 54. ...
, 54, the shape of the deposit maintains the angle of repose, so there is no risk of the powder 80 entering and depositing in the gas release room 62.

したがって、放出ガスは放出ルーム62及び放出孔64
を通じてスムーズに外部に放出され、粉体80を吹き上
げてその供給効率を減少したシ、供給不能とすることは
ない。
Therefore, the released gas is transferred to the release room 62 and the release hole 64.
The powder 80 is smoothly discharged to the outside through the pump, and the powder 80 is not blown up to reduce its supply efficiency or become unable to be supplied.

なお、上記実施例においては、ガス放出口64を粉体導
入管58の両側に設けているが、これを例えば、粒体導
入管58の前方、すなわち、ローター52の回転方向に
向かって距離をおき、完全に別個に設けることも可能で
ある。この場合、上記実施例に比較して圧力タンク76
と外気との間に挿入される羽根板54の数が減少して圧
力差維持の観点からは不利となるが、粉体導入口56と
ガス放出口64とを完全に別個にしているからガス放出
による粉体供給用への影響を完全に遮断することが可能
であシ、きわめて多量の粉体供給を行なう際には有利と
なる。
In the above embodiment, the gas discharge ports 64 are provided on both sides of the powder introduction pipe 58, but they are provided, for example, in front of the particle introduction pipe 58, that is, at a distance toward the rotation direction of the rotor 52. It is also possible to provide them completely separately. In this case, compared to the above embodiment, the pressure tank 76
This reduces the number of vanes 54 inserted between the air and the outside air, which is disadvantageous from the viewpoint of maintaining pressure difference, but since the powder inlet 56 and the gas outlet 64 are completely separate, the gas It is possible to completely block out the influence of the discharge on the powder supply, which is advantageous when supplying a very large amount of powder.

〔発明の効果〕〔Effect of the invention〕

以上説明した如く本発明に係る粉体供給用ロータリーパ
ルプでは、粉体導入の通路とガス放出の流路とを別個に
することによって放出ガスによる粉体供給作用への影響
を除去し、粉体供給が不能となる危険がなく多量の粉体
をスムーズに供給することができるものである。
As explained above, in the rotary pulp for powder supply according to the present invention, by separating the powder introduction passage and the gas discharge passage, the influence of the discharged gas on the powder supply action is eliminated, and the powder It is possible to smoothly supply a large amount of powder without the risk of supply failure.

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

第1図は従来の粉体供給用ロータリーパルプを 7示す
断面図であシ、第2図は本発明−の好適な実施例を示す
縦断面一、第3図は第2図■−■線に沿う断面図である
。 50・・・ケース、52・・・ローター、54・・・羽
根板56・・・粉体導入口、66・・・粉体排出口、6
2・・・カス放出ルーム、64・・・ガス放出死出 願
 人 日立プランし建設株式会社第1図 3゜ 第2図 mw ! ■」 第3図
Fig. 1 is a cross-sectional view showing a conventional rotary pulp for supplying powder, Fig. 2 is a vertical cross-sectional view showing a preferred embodiment of the present invention, and Fig. 3 is a cross-sectional view taken along the line ■-■ in Fig. 2. FIG. 50... Case, 52... Rotor, 54... Vane plate 56... Powder introduction port, 66... Powder discharge port, 6
2...Gas release room, 64...Gas release application Hitachi Plan Shi Construction Co., Ltd. Figure 1 3゜Figure 2 mw! ■'' Figure 3

Claims (1)

【特許請求の範囲】[Claims] 中空円筒状のケースと、このケース内へ回転可ケース下
方へ開口する粉体排出口と、前記粉体導入口の近傍に設
げら2しこの導入口とは別個に形成されたガス放出口と
、′を具備する粉体供給用ロータリーパルプ。
A hollow cylindrical case, a powder discharge port rotatable into the case and opening downward from the case, and a gas discharge port provided near the powder introduction port and formed separately from the introduction port. A rotary pulp for supplying powder, comprising: and ′.
JP5052284A 1984-03-16 1984-03-16 Rotary valve for feeding powdery material Pending JPS60197524A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5052284A JPS60197524A (en) 1984-03-16 1984-03-16 Rotary valve for feeding powdery material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5052284A JPS60197524A (en) 1984-03-16 1984-03-16 Rotary valve for feeding powdery material

Publications (1)

Publication Number Publication Date
JPS60197524A true JPS60197524A (en) 1985-10-07

Family

ID=12861310

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5052284A Pending JPS60197524A (en) 1984-03-16 1984-03-16 Rotary valve for feeding powdery material

Country Status (1)

Country Link
JP (1) JPS60197524A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245022U (en) * 1975-09-26 1977-03-30

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245022U (en) * 1975-09-26 1977-03-30

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