JPS5823299B2 - Airtight discharge device for powder and granular materials - Google Patents

Airtight discharge device for powder and granular materials

Info

Publication number
JPS5823299B2
JPS5823299B2 JP55065763A JP6576380A JPS5823299B2 JP S5823299 B2 JPS5823299 B2 JP S5823299B2 JP 55065763 A JP55065763 A JP 55065763A JP 6576380 A JP6576380 A JP 6576380A JP S5823299 B2 JPS5823299 B2 JP S5823299B2
Authority
JP
Japan
Prior art keywords
powder
supply pipe
granular material
weir plate
discharge
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
JP55065763A
Other languages
Japanese (ja)
Other versions
JPS56161223A (en
Inventor
高岸正春
合澤清志
村尾三樹雄
鈴木武司
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP55065763A priority Critical patent/JPS5823299B2/en
Publication of JPS56161223A publication Critical patent/JPS56161223A/en
Publication of JPS5823299B2 publication Critical patent/JPS5823299B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Air Transport Of Granular Materials (AREA)

Description

【発明の詳細な説明】 本発明は、粉粒体分離機たとえばサイクロンなどの下部
に設けられ、粉粒体を連続的、定量的かつ気密的に排出
する粉粒体の気密排出装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an airtight discharge device for powder and granular material that is installed at the lower part of a granular material separator, such as a cyclone, and discharges the powder and granular material continuously, quantitatively, and airtightly.

典型的な先行技術として第1図に示すような粉粒体の流
動化現象を応用した気密排出装置がある。
As a typical prior art, there is an airtight discharge device that utilizes the fluidization phenomenon of powder and granules as shown in FIG.

この装置では、上下に延びる供給管3と排出管4とを水
平面内でずらして配置し、両者間に上下方向で距離lを
有して相互に重なり合う制御壁5および堰6を設けて粉
粒体の貯留部分7を形成する。
In this device, a supply pipe 3 and a discharge pipe 4 that extend vertically are arranged offset in a horizontal plane, and a control wall 5 and a weir 6 that overlap each other with a distance l in the vertical direction are provided between them, and Forming a reservoir portion 7 of the body.

その貯留部分7の下部に設けられた多孔板8などを含む
流動化手段9から、ガスを貯留部分7に導入して粉粒体
を流動化させる。
Gas is introduced into the storage portion 7 from a fluidization means 9 including a perforated plate 8 provided at the lower part of the storage portion 7 to fluidize the powder.

それによって、粉粒体が堰6を越えて連続的に溢流され
、しかも供給管3と排出管4との間の気密性が保たれる
As a result, the powder and granules are continuously overflowed over the weir 6, and the airtightness between the supply pipe 3 and the discharge pipe 4 is maintained.

しかしこのような気密排出装置では、供給管3の上部の
図示しないサイクロンに付着したコーチングが塊状体と
なって貯留部分Iに落下すると、その塊状体は堰6を越
えることが困難であって排出されない。
However, in such an airtight discharge device, when the coating adhering to the cyclone (not shown) at the upper part of the supply pipe 3 becomes a lump and falls into the storage part I, the lump becomes difficult to cross the weir 6 and cannot be discharged. Not done.

この場合、粉粒体の流動化に大量のガスを使用すると、
そのガスが上方のサイクロンにまで及び、サイクロン内
部の気流渦が不安定となってサイクロンの分離機能が損
なわれる。
In this case, if a large amount of gas is used to fluidize the powder,
The gas reaches the cyclone above, and the airflow vortex inside the cyclone becomes unstable, impairing the separation function of the cyclone.

さらに、この気密排出装置がセメント原料焼成装置の予
熱装置に適用された場合には、流動化ガスとして常温空
気などの比較的低温のガスを用いると、予熱された粉粒
体原料を、却って冷却する結果となり、熱交換率が低下
する欠点がある。
Furthermore, when this airtight discharge device is applied to the preheating device of a cement raw material firing device, if a relatively low temperature gas such as room temperature air is used as the fluidizing gas, the preheated granular raw material will be cooled instead. This results in a disadvantage that the heat exchange rate decreases.

本発明は優れた気密性を有し、粉粒体を連続的に排出で
きるとともにコーチングなどの大塊を排出することがで
き、しかも堆積した粉粒体の排出量を調整することが容
易であって高温の粉粒体にも利用できる気密排出装置を
提供することを目的とする。
The present invention has excellent airtightness, can continuously discharge powder and granules, and can also discharge large lumps such as coatings, and can easily adjust the amount of accumulated powder and granules to be discharged. The purpose of the present invention is to provide an airtight discharge device that can be used even for high-temperature powder and granular materials.

以下、図面によって本発明の詳細な説明する。Hereinafter, the present invention will be explained in detail with reference to the drawings.

第2図は本発明の一実施例の正面図であり、第3図はそ
の縦断面図である。
FIG. 2 is a front view of one embodiment of the present invention, and FIG. 3 is a longitudinal sectional view thereof.

この気密排出装置は、セメント原料焼成装置のサスペン
ションプレヒーターに含まれるサイクロンの下部に設け
られる。
This airtight discharge device is installed at the bottom of a cyclone included in a suspension preheater of a cement raw material firing device.

サイクロンの下部に連通し底部10aが閉塞されかつ上
下に延びる角状あるいは円筒状の供給管10と、上下に
延びる角状あるいは円筒状の排出管11とは、水平面内
でずれた位置に配設される。
An angular or cylindrical supply pipe 10 that communicates with the lower part of the cyclone and whose bottom part 10a is closed and extends vertically and an angular or cylindrical discharge pipe 11 that extends up and down are arranged at shifted positions in a horizontal plane. be done.

供給管10の下部には流動化手段12が設けられる。A fluidizing means 12 is provided at the bottom of the supply pipe 10 .

供給管10の排出管11側の側壁に沿って流動化手段1
2の上方には、制御壁13が設けられる。
Fluidization means 1 is provided along the side wall of the supply pipe 10 on the discharge pipe 11 side.
A control wall 13 is provided above 2.

一方、排出管11の上部において、制御壁13に対峙し
て上下に延びる堰板14が、回動軸18のまわりに回動
自在に設けられる。
On the other hand, in the upper part of the discharge pipe 11, a weir plate 14 that faces the control wall 13 and extends up and down is rotatably provided around a rotation shaft 18.

堰板14の下端部は底部10aの排出管11側の端部に
当接可能である。
The lower end of the weir plate 14 can come into contact with the end of the bottom portion 10a on the discharge pipe 11 side.

このようにして、供給管10と排出管11との間に粉粒
体原料の貯留部分15が形成される。
In this way, a storage portion 15 for the powder raw material is formed between the supply pipe 10 and the discharge pipe 11.

第4図を参照して、流動化手段12は貯留部分15の下
部で相互に平行にほぼ水平に設けられた複数(図示3つ
)の管体16と、それらの管体16が共通に接続され、
ガスを導入するガス供給管17とを含む。
Referring to FIG. 4, the fluidizing means 12 includes a plurality of tube bodies 16 (three in the figure) provided substantially horizontally in parallel with each other at the lower part of the storage portion 15, and these tube bodies 16 are commonly connected. is,
and a gas supply pipe 17 for introducing gas.

各管体16には多数の噴出口19が穿設させる。A large number of jet ports 19 are provided in each tube 16 .

堰板14は回動手段24によって駆動される。The weir plate 14 is driven by a rotation means 24.

回動手段24は排出管11の側壁で回転自在に軸支され
た回動軸18と、排出管11の外方で回動軸18の一端
部18aに固定されたアーム20と、アーム20にその
軸線方向の位置を調節自在にして取付けられた重錘21
とを含む。
The rotating means 24 includes a rotating shaft 18 rotatably supported on the side wall of the discharge pipe 11, an arm 20 fixed to one end 18a of the rotating shaft 18 outside the discharge pipe 11, and A weight 21 attached with its axial position adjustable
including.

重錘21は、たとえばアーム20に螺着されており、ア
ーム20に沿って螺進および螺退することによってその
位置が調節される。
The weight 21 is screwed onto the arm 20, for example, and its position is adjusted by screwing forward and backward along the arm 20.

アーム20は、回動軸18を含む鉛直面に関して堰板1
4と反対側に延びており、したがって堰体14には矢符
で示すごとく重錘21によるモーメントM(第2図参照
)が作用して、堰板14の下端部は右方向に付勢される
The arm 20 is connected to the weir plate 1 with respect to a vertical plane including the rotation axis 18.
Therefore, the moment M (see Fig. 2) by the weight 21 acts on the weir body 14 as shown by the arrow, and the lower end of the weir plate 14 is biased to the right. Ru.

サイクロンで捕集された粉粒体22が貯留部分15に堆
積すると、サイクロンに通ずる供給管10と排出管11
とは、堆積した粉粒体22によって遮断され、サイクロ
ンの気密性が保たれる。
When the powder 22 collected by the cyclone is deposited in the storage part 15, the supply pipe 10 and the discharge pipe 11 leading to the cyclone are
This is blocked by the accumulated powder 22, and the airtightness of the cyclone is maintained.

ガス供給管17には図示しない気体源例えば常温空気を
圧送するブロアが接続されており、このブロアから供給
されるガスが管体16の噴出口19から噴出されること
により、粉粒体22が粉気混合状態となって流動化され
る。
The gas supply pipe 17 is connected to a gas source (not shown), such as a blower that pumps air at room temperature, and the gas supplied from the blower is ejected from the spout 19 of the pipe body 16, thereby causing the powder and granular material 22 to be The powder becomes a mixed state and becomes fluidized.

この粉粒体22の流動化現象によって粉粒体22は貯留
部分15から堰板14を越えて排出管11に連続的、定
量的かつ気密的に溢流される。
Due to this fluidization phenomenon of the granular material 22, the granular material 22 is continuously, quantitatively, and airtightly overflowed from the storage portion 15 over the weir plate 14 into the discharge pipe 11.

貯留部分15にサイクロンから落下してきたコーチング
などの大塊が堆積すると、貯留部分15における流動化
現象が阻害され、粉粒体22の排出管11への排出能力
が低下する。
When large lumps such as coatings that have fallen from the cyclone accumulate in the storage portion 15, the fluidization phenomenon in the storage portion 15 is inhibited, and the ability to discharge the powder and granular material 22 to the discharge pipe 11 is reduced.

そのため貯留部分15に粉粒体22が次々に堆積して堰
板14に作用する粉体圧が増大し、重錘21によるモー
メンl−Mとのバランスがくずれて、堰板14が第3図
の鎖線で示すように開いて、貯留部分15の底部が開口
する。
Therefore, the powder 22 accumulates in the storage part 15 one after another, the powder pressure acting on the weir plate 14 increases, and the balance with the moment l-M caused by the weight 21 is lost, causing the weir plate 14 to The storage portion 15 is opened as shown by the chain line, and the bottom of the storage portion 15 is opened.

それによって、貯留部分15に堆積していたコーチング
などの大塊が粉粒体22とともに排出管11に排出され
る。
As a result, large lumps such as coating deposited in the storage portion 15 are discharged to the discharge pipe 11 together with the powder and granular material 22.

貯留部分15における粉粒体22の堆積量が減少すると
、重錘21のモーメントMによって、堰板14が実線で
示すごとく復元し、貯留部分15に粉粒体22が堆積さ
れ始める。
When the amount of granular material 22 deposited in the storage portion 15 decreases, the weir plate 14 is restored as shown by the solid line due to the moment M of the weight 21, and the granular material 22 begins to be deposited in the storage portion 15.

始動時などにおし・て、粉粒体の堆積量が極めて少ない
ときには、流動化手段12が有効に作用しないので、粉
粒体22が混気状態とならず、その;結果粉粒体22が
堰板14を越えて溢流できなくなる。
When the amount of accumulated powder and granular material is extremely small, such as during startup, the fluidizing means 12 does not work effectively, so that the powder and granular material 22 does not become in an aerated state. The water cannot overflow beyond the weir plate 14.

この場合には、貯留部分15の底部を必要に応じた開度
で開口しておくか、あるいは重錘21をアーム20に沿
って適宜移動させて堰板14をわずかな堆積時にも回動
できるようにして・おくと、排出作用に柔軟性をもたせ
ることができる。
In this case, the weir plate 14 can be rotated even when a small amount of accumulation occurs by leaving the bottom of the storage section 15 open at an opening degree that suits your needs, or by moving the weight 21 along the arm 20 as appropriate. By doing this, you can make the discharge action more flexible.

なお、貯留部分15の底部を形成する供給管10の底部
10aは平坦であっても良いが、図示のように傾斜面で
形成すると排出には都合が良い。
The bottom portion 10a of the supply pipe 10 forming the bottom portion of the storage portion 15 may be flat, but it is convenient for discharge if it is formed as an inclined surface as shown.

;さらに、堰板14は図示のように全体が回動するもの
であっても良いし、下部の一部分のみが回動するもので
あってもよい。
Furthermore, the weir plate 14 may be entirely rotatable as shown in the figure, or only a portion of the lower portion may be rotatable.

なお、貯留部分15の底部10aの傾斜角αを粉粒体2
20安息角以上にとることによって、排高時における粉
粒体22の残留を防止できることは言うまでもない。
Note that the inclination angle α of the bottom portion 10a of the storage portion 15 is
It goes without saying that by setting the angle of repose to 20 or more, it is possible to prevent the powder 22 from remaining during evacuation.

第5図は本発明の他の実施例の断面図であり、第2図〜
第4図の実施例に対応する部分には同一の参照符を付す
FIG. 5 is a sectional view of another embodiment of the present invention, and FIG.
Parts corresponding to the embodiment of FIG. 4 are given the same reference numerals.

この実施例では、ガス供給管17の途中に弁27を設け
、その弁27よりも上流側に、弁28を途中に備える枝
管25の一端部が接続される。
In this embodiment, a valve 27 is provided in the middle of the gas supply pipe 17, and one end of a branch pipe 25 having a valve 28 in the middle is connected to the upstream side of the valve 27.

この枝管25の他端部は、供給管10における粉粒体堆
積層26の上部に接続される。
The other end of this branch pipe 25 is connected to the upper part of the powder deposited layer 26 in the supply pipe 10 .

弁27.28の開凌は、貯留部分15における粉粒体2
2の堆積量が予め設定した値となるように設定されてい
る。
The opening of the valves 27 and 28 means that the powder and granular material 2 in the storage section 15
The amount of accumulation of No. 2 is set to a preset value.

この状態で貯留部分15における粉粒体22の堆積量が
異常に増大すると、枝管25の供給管10における開口
部25aから堆積層26の上面26aまでの距離に応じ
て開口部25aにおけるガスの流通抵抗が犬となる。
If the amount of deposited powder 22 in the storage portion 15 increases abnormally in this state, the amount of gas at the opening 25a increases depending on the distance from the opening 25a in the supply pipe 10 of the branch pipe 25 to the upper surface 26a of the deposited layer 26. Distribution resistance becomes a dog.

それに応じて枝管25からのガス噴出量が小となるとと
もに、管体16からのガス噴出量が犬となる。
Accordingly, the amount of gas ejected from the branch pipe 25 becomes small, and the amount of gas ejected from the tube body 16 becomes small.

したがって貯留部分15における粉粒体の流動化が促進
され、排出管11への排出量が犬となり、貯留部分15
における粉粒体の過剰堆積が防止される。
Therefore, fluidization of the powder and granular material in the storage portion 15 is promoted, the amount of discharge to the discharge pipe 11 becomes small, and the storage portion 15
Excessive accumulation of powder and granules in the process is prevented.

上述のように、堰板14は粉粒体の貯留部分15におけ
る粉粒体22の堆積量とのバランスがくずれたときに回
動するものであれば良(、堰板14の回動手段としては
上述の重錘21を用いる構成のほかに、ばねなどで堰板
14を弾発的に付勢する構造であっても良い。
As mentioned above, the weir plate 14 may be of any type as long as it rotates when the balance with the amount of granular material 22 deposited in the granular material storage portion 15 is lost. In addition to the structure using the above-mentioned weight 21, a structure in which the weir plate 14 is elastically biased by a spring or the like may be used.

上述の実施例ではセメント原料焼成装置の予熱装置に用
いられるザイクロンの気密排出装置について述べたが、
本発明は粉粒体を気密的に排出する他の技術分野の装置
に関連して広〈実施できることは言うまでもない。
In the above embodiment, a Zyclone airtight discharge device used in a preheating device of a cement raw material firing device was described.
It goes without saying that the present invention can be broadly implemented in connection with devices in other technical fields for airtightly discharging powder or granular materials.

上述のとと(、本発明によれば以下のような顕著な技術
的効果が得られる。
According to the present invention, the following remarkable technical effects can be obtained.

すなわち、塊状物が貯留部分に落下したときには、速や
かにそれを排出でき、また、粉粒体の供給量に応じて排
出量を増減させることができ、しかも貯留部分における
粉粒体の堆積によるマテリアルシールを確実に行なうこ
とができる。
In other words, when lumps fall into the storage section, they can be quickly discharged, and the amount of discharge can be increased or decreased depending on the amount of powder and granules supplied. Sealing can be performed reliably.

また粉粒体の堆積量が適切に保たれるので、必要最小量
のガスによって流動化を行なうことができる。
Furthermore, since the amount of powder particles deposited is maintained at an appropriate level, fluidization can be performed using the minimum necessary amount of gas.

したがって七メント原料の予熱装置などに用いる場合に
おいても熱交換性を阻害することはない。
Therefore, even when used in a preheating device for menthol raw materials, the heat exchange performance is not inhibited.

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

第1図は先行技術を示す縦断面図、第2図は本発明の一
実施例の正面図、第3図は第2図の縦断面図、第4図は
第1図および第2図の切断面線■−IVから見た断面図
、第5図は本発明の他の実施例の縦断面図である。 10・・・・・・供給室、10a・・・・・・底部、1
1・・・・・・排出管、12・・・・・・流動化手段、
14・・・・・・堰板、15・・・・−・貯留部分、1
8・−・・・・回動軸、20・・・・・・アーム、21
・・・・・・重錘、22・・・・・・粉粒体、24・・
・・・・回動手段。
Fig. 1 is a longitudinal sectional view showing the prior art, Fig. 2 is a front view of an embodiment of the present invention, Fig. 3 is a longitudinal sectional view of Fig. 2, and Fig. 4 is a longitudinal sectional view of Fig. 1 and Fig. 2. FIG. 5 is a cross-sectional view taken along the section line -IV, and a vertical cross-sectional view of another embodiment of the present invention. 10... Supply chamber, 10a... Bottom, 1
1...Discharge pipe, 12...Fluidization means,
14...Weir plate, 15...--Storage part, 1
8...Rotation axis, 20...Arm, 21
... Weight, 22 ... Powder, 24 ...
...Rotating means.

Claims (1)

【特許請求の範囲】 1 上下に延びて底部が閉塞された供給管、水平面内で
供給管からずれて配置され供給管に連結された上下に延
びる排出管、 下端部が前記供給管の底部における排出管側の端部に当
接可能であって、供給管および排出管相互間に粉粒体の
貯留部分を形成すべく上下に延びて設けられ、少なくと
も下部が水平軸のまわりに回動自在な堰板、 前記貯留部分の下部に設けられ粉粒体を流動化させる流
動化手段、ならびに 前記堰板の少なくとも下部を貯留部分の粉粒体堆積量に
応じて水平軸のまわりに回動する回動手段を含むことを
特徴とする粉粒体の気密排出装置。 2 前記回動手段は、前記堰板の少なくとも下部を軸支
する水平な回動軸と、前記貯留部分の外方における回動
軸の端部に固定され回動軸を含む鉛直面に関して前記堰
板の反対側に延びるアームと、アームにその軸線方向に
沿う位置を調節自在にして取付けられた重錘とを含むこ
とを特徴とする特許請求の範囲第1項記載の粉粒体の気
密排出装置。
[Scope of Claims] 1. A supply pipe that extends vertically and is closed at the bottom; a discharge pipe that extends vertically and is disposed offset from the supply pipe in a horizontal plane and is connected to the supply pipe; the lower end is at the bottom of the supply pipe; It is capable of coming into contact with the end of the discharge pipe, extends vertically to form a particulate material storage area between the supply pipe and the discharge pipe, and is rotatable at least at the lower part around a horizontal axis. a weir plate, a fluidizing means provided at a lower part of the storage section to fluidize the powder and granular material, and at least a lower part of the weir plate is rotated around a horizontal axis according to the amount of powder and granular material deposited in the storage section. An airtight discharge device for powder and granular material, characterized by including a rotating means. 2. The rotation means is fixed to a horizontal rotation shaft that pivotally supports at least a lower part of the weir plate, and an end of the rotation shaft outside the storage portion, and is fixed to the weir plate with respect to a vertical plane including the rotation shaft. The airtight discharge of powder and granular material according to claim 1, characterized by comprising an arm extending on the opposite side of the plate, and a weight attached to the arm so that its position along the axial direction can be freely adjusted. Device.
JP55065763A 1980-05-16 1980-05-16 Airtight discharge device for powder and granular materials Expired JPS5823299B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55065763A JPS5823299B2 (en) 1980-05-16 1980-05-16 Airtight discharge device for powder and granular materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55065763A JPS5823299B2 (en) 1980-05-16 1980-05-16 Airtight discharge device for powder and granular materials

Publications (2)

Publication Number Publication Date
JPS56161223A JPS56161223A (en) 1981-12-11
JPS5823299B2 true JPS5823299B2 (en) 1983-05-14

Family

ID=13296382

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55065763A Expired JPS5823299B2 (en) 1980-05-16 1980-05-16 Airtight discharge device for powder and granular materials

Country Status (1)

Country Link
JP (1) JPS5823299B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6470390A (en) * 1987-09-07 1989-03-15 Meiji Machine Fine particle flow regurator
JPH0385286A (en) * 1989-08-25 1991-04-10 Mitsui Eng & Shipbuild Co Ltd Prevention of occurrence of bridge of material in storage tank

Also Published As

Publication number Publication date
JPS56161223A (en) 1981-12-11

Similar Documents

Publication Publication Date Title
CN1153633C (en) Multi-chamber type fluidized bed-carrying classifier
KR100376560B1 (en) Fluidized bed-carrying drying classifier
WO1997024570A1 (en) Pulverized body drying method and apparatus
JPS5823299B2 (en) Airtight discharge device for powder and granular materials
JP3063163B2 (en) Ventilated tumble dryer
US3998583A (en) Apparatus for thermal treatment of moist raw material
US3599344A (en) Apparatus for drying pulverant materials
JP2000197854A (en) Multi-chamber type fluidized bed classification apparatus
GB2101980A (en) Metered discharge of material from fluidized bed
JP2840579B2 (en) Fluidized bed classifier
CN108286872A (en) A kind of sand drying device
JPS5832136B2 (en) Airtight discharge device for powder and granular materials
JPH06191615A (en) Powder dispersing device
US2841385A (en) Rotary kiln
KR101546382B1 (en) Discharging Type of Fine Particles Granules is Exclusive Drying Device for Energy Saving
JPH0464732B2 (en)
JPS5830842B2 (en) Classifier in air transport pipes
SU1242230A2 (en) Fluidized bed apparatus
JPS581756Y2 (en) improved rotary dryer
JP3370972B2 (en) Airtight discharge device in fluidized bed cement clinker firing device
JPH04330929A (en) Discharge mechanism in fluidized-bed treating device
JPH0223932Y2 (en)
JPS57160832A (en) Discharger in grain driers
JP2549812B2 (en) Cement clinker firing equipment
JPS5982226A (en) Powdery granule spraying device