JPS6327774Y2 - - Google Patents

Info

Publication number
JPS6327774Y2
JPS6327774Y2 JP1984126461U JP12646184U JPS6327774Y2 JP S6327774 Y2 JPS6327774 Y2 JP S6327774Y2 JP 1984126461 U JP1984126461 U JP 1984126461U JP 12646184 U JP12646184 U JP 12646184U JP S6327774 Y2 JPS6327774 Y2 JP S6327774Y2
Authority
JP
Japan
Prior art keywords
pipe
mixing
discharge port
powder
aerator
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
JP1984126461U
Other languages
Japanese (ja)
Other versions
JPS6144224U (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
Application filed filed Critical
Priority to JP1984126461U priority Critical patent/JPS6144224U/en
Publication of JPS6144224U publication Critical patent/JPS6144224U/en
Application granted granted Critical
Publication of JPS6327774Y2 publication Critical patent/JPS6327774Y2/ja
Granted legal-status Critical Current

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  • Accessories For Mixers (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【考案の詳細な説明】 この考案は、粉粒体を高精度で混入し、この均
一混合体を能率よく圧送できる混合圧送装置に関
するものである。
[Detailed Description of the Invention] This invention relates to a mixing and pumping device that can mix powder and granular materials with high precision and pump this uniform mixture efficiently.

粉粒体の混合装置として実開昭53−150969が提
案されているがこの装置は常圧混合であることは
勿論、排出は低圧排出しかできない上、多量の送
給空気を必要とするので動力経費がかかつて不経
済である。
Japanese Utility Model Application No. 53-150969 has been proposed as a mixing device for powder and granular materials, but this device not only mixes at normal pressure, but can only discharge at low pressure, and requires a large amount of air supply, so it is difficult to use power. It is expensive and uneconomical.

更に排出時においてタンク内での偏析を生じ易
い。また混合圧送装置として実公昭48−45153が
知られているが、この装置は構成が複雑でタンク
容量が大きくなると混合精度が悪くなり空気量も
多くなる他圧送時に偏析を生じ易くなる欠点があ
る。
Furthermore, segregation tends to occur within the tank during discharge. In addition, Utility Model Publication No. 48-45153 is known as a mixing pressure feeding device, but this device has a complicated structure, and as the tank capacity increases, the mixing accuracy deteriorates and the amount of air increases.In addition, it has the disadvantage that segregation is likely to occur during pressure feeding. .

本案は、高精度の混合ができると同時に圧送時
にタンク内偏析を生じないようにした混合圧送装
置を提供するものである。
The present invention provides a mixing and pumping device that is capable of high-precision mixing and at the same time prevents segregation within the tank during pumping.

本案装置は、タンクの中心排出口の上方に、上
部に絞り開口と側窓を有し下端部外周に案内コー
ンを固設した上昇混合管を垂設すると共に排出口
に混合時及び圧送時共に機能する送給器が連結さ
れて構成されている。
This device has an ascending mixing pipe vertically installed above the central discharge port of the tank, which has an aperture opening and a side window at the top and a guide cone fixed to the outer periphery of the bottom end. It is composed of functional feeders connected together.

本案の実施例装置を図について説明すると、1
は加圧タンク、2は投入弁、3は排気弁、4は排
出口、5は、タンク底部1aに設けられている漏
斗状エアレータ、5aはエアレータ室、6はこれ
に通ずる加圧空気を加減する弁である。
To explain the embodiment of the present invention with reference to the figures, 1
is a pressurized tank, 2 is an input valve, 3 is an exhaust valve, 4 is an outlet, 5 is a funnel-shaped aerator provided at the bottom of the tank 1a, 5a is an aerator chamber, and 6 is a regulator for controlling the pressurized air leading to this. It is a valve that does.

7はタンクの中央に、排出口の開口中心に位置
して垂設した上昇混合管であり、上端に絞り開口
8とテーパ部9を有し、その直下の管壁に窓10
が設けられている。窓10は粉粒体レベル11の
近傍になるように設けられている。
Reference numeral 7 designates a rising mixing pipe vertically installed in the center of the tank, located at the center of the opening of the discharge port, and has an aperture opening 8 and a tapered part 9 at the upper end, and a window 10 in the pipe wall directly below it.
is provided. The window 10 is provided near the powder level 11.

上昇管の下端外周には円錐状の案内コーン12
が固設されている。12aは底部案内面である。
A conical guide cone 12 is provided on the outer periphery of the lower end of the rising pipe.
is permanently installed. 12a is a bottom guide surface.

7aは上昇管の取付アームである。 7a is a mounting arm of the riser pipe.

排出口4の下端には加圧気体送給器13が連結
され、該送給器は、案内管14と、その下端14
aに内周間〓17を介して同心的に配設された内
管15とを共通に囲繞する外筒16とによつて構
成されている。
A pressurized gas feeder 13 is connected to the lower end of the outlet 4, and the feeder includes a guide tube 14 and a lower end 14 thereof.
It is constituted by an inner tube 15 which is concentrically disposed with an inner circumference 17 in between, and an outer tube 16 that commonly surrounds the inner tube 15.

而して外筒16には旋回気流供給管18が接続
され、内管15には圧送管20が接続される。
A swirling airflow supply pipe 18 is connected to the outer cylinder 16, and a pressure feeding pipe 20 is connected to the inner pipe 15.

19は加減弁、19aは逆止弁、21は排出弁
である。
19 is a control valve, 19a is a check valve, and 21 is a discharge valve.

22は共通の加圧空気源である。 22 is a common source of pressurized air.

上記装置において、粉粒体(2種以上)を投入
するには弁2及び3を開放した状態で行う。
In the above-mentioned apparatus, the valves 2 and 3 are left open when introducing the powder or granular material (two or more types).

混合においては、投入弁2と排出弁21を閉
じ、弁3,6,19を開く。
During mixing, input valve 2 and discharge valve 21 are closed, and valves 3, 6, and 19 are opened.

粉粒体はエアレータ5によつて流動化されると
共に加圧気体送給器13を介して加圧気体が排出
口4から吹き上げ上昇管7内を上昇する。
The granular material is fluidized by the aerator 5, and pressurized gas is blown up from the discharge port 4 via the pressurized gas feeder 13 and rises in the riser pipe 7.

而して粉粒体は案内コーンの底部案内部面12
a(エアレータ面とほぼ並行)に沿つて上昇管の
下端に導入され気流と共に上昇管の窓10及び上
端開口8から放出される。
Therefore, the granular material is transferred to the bottom guide surface 12 of the guide cone.
a (approximately parallel to the aerator surface) at the lower end of the riser and is discharged from the window 10 and upper end opening 8 of the riser along with the airflow.

ここにおいて粉粒体経路の差及び時間差に基い
て異種の粉粒体が混合されタンク内循環を繰り返
すうちに均一に混合される。
Here, different types of powder and granules are mixed based on the difference in the powder and granule paths and the time difference, and as they are repeatedly circulated in the tank, they are uniformly mixed.

混合が終了した後、弁3,6,19を一旦閉止
し、次いで弁6を開きタンク1内の圧力を所定圧
(例えば2Kg/cm2)まで加圧する。
After the mixing is completed, valves 3, 6, and 19 are temporarily closed, and then valve 6 is opened to increase the pressure in tank 1 to a predetermined pressure (for example, 2 kg/cm 2 ).

この加圧によつてタンク内の混合粉体は再び流
動化される。
The mixed powder in the tank is fluidized again by this pressurization.

その後弁19と21を開くと、送給器13から
の加圧気体が間〓17を通つて内管15に流入
し、これによつて混合粉体は圧送管20中に圧送
される。
When the valves 19 and 21 are then opened, pressurized gas from the feeder 13 flows into the inner tube 15 through the gap 17, whereby the mixed powder is pumped into the pumping tube 20.

圧送中、タンク内の加圧気体は圧送用ブスター
気体として作用する。
During pumping, the pressurized gas in the tank acts as a pumping booster gas.

本案装置においては、排出口断面積と上昇管断
面積とを略等しくすることによつて吹き込み空気
の管外散逸を少なくできる。
In the device of the present invention, by making the cross-sectional area of the discharge port and the cross-sectional area of the riser substantially equal, it is possible to reduce the amount of blown air dissipated outside the pipe.

更に案内コーンのフレヤー部と案内面12aが
設けられているので高精度の混合ができ圧送時の
偏析も防止できる。
Furthermore, since the flared portion of the guide cone and the guide surface 12a are provided, highly accurate mixing is possible and segregation during pressure feeding can be prevented.

この他加圧送給器を混合時及び圧送時とも共用
するので装置の無駄がなくコンパクトにできる他
流動化用気体及び送給用気体も同一ラインから供
給することができるので設備を簡略化できる。
In addition, since the pressurized feeder is used for both mixing and pressure feeding, the equipment can be made compact without waste, and the fluidizing gas and feeding gas can also be supplied from the same line, simplifying the equipment.

なお、本案において、粉粒体圧送機能は、タン
ク内圧と送給器にかかる圧力との差圧によつて行
われるので弁19によつて制御できる。
In the present invention, the function of pumping the granular material is performed by the pressure difference between the internal pressure of the tank and the pressure applied to the feeder, and therefore can be controlled by the valve 19.

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

図は本案装置の要部断面図である。 5……エアレータ、7……混合用上昇管、8…
…絞り開口、10……窓、12……案内コーン、
13……送給器。
The figure is a sectional view of essential parts of the proposed device. 5...Aerator, 7...Rising pipe for mixing, 8...
...Aperture aperture, 10...Window, 12...Guide cone,
13...Feeder.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 加圧可能なタンクの底部に漏斗状エアレータと
その中心に排出口が設けられてなる粉粒体の混合
圧送装置において、上端に絞り開口と窓を有し、
下端部外周に円錐形案内コーンを固設された上昇
混合管が前記排出口中心上方に垂設支持されると
共に前記排出口には案内管とその下端内周に間〓
を介して配設された内管とを共通に囲繞する外筒
とから構成された送給器の前記案内管が連結さ
れ、前記外筒には前記エアレータ用加圧空気源か
らの加圧気体が供給され、前記内管には圧送管が
接続されてなる粉粒体の混合圧送装置。
A mixing and pumping device for powder and granular materials comprising a funnel-shaped aerator at the bottom of a pressurizable tank and a discharge port at its center, which has an aperture opening and a window at the upper end,
A rising mixing pipe having a conical guide cone fixed to the outer periphery of its lower end is vertically supported above the center of the discharge port, and at the discharge port there is a space between the guide pipe and the inner periphery of its lower end.
The guide pipe of the feeder is connected to an outer cylinder that commonly surrounds an inner pipe disposed through the inner pipe, and the outer cylinder receives pressurized gas from the pressurized air source for the aerator. A mixing and pumping device for powder and granular materials, wherein a pumping pipe is connected to the inner pipe.
JP1984126461U 1984-08-22 1984-08-22 Powder mixing device Granted JPS6144224U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1984126461U JPS6144224U (en) 1984-08-22 1984-08-22 Powder mixing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984126461U JPS6144224U (en) 1984-08-22 1984-08-22 Powder mixing device

Publications (2)

Publication Number Publication Date
JPS6144224U JPS6144224U (en) 1986-03-24
JPS6327774Y2 true JPS6327774Y2 (en) 1988-07-27

Family

ID=30685137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984126461U Granted JPS6144224U (en) 1984-08-22 1984-08-22 Powder mixing device

Country Status (1)

Country Link
JP (1) JPS6144224U (en)

Also Published As

Publication number Publication date
JPS6144224U (en) 1986-03-24

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