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JPS6026506A - Device for distributing powdered material - Google Patents

Device for distributing powdered material

Info

Publication number
JPS6026506A
JPS6026506A JP13542683A JP13542683A JPS6026506A JP S6026506 A JPS6026506 A JP S6026506A JP 13542683 A JP13542683 A JP 13542683A JP 13542683 A JP13542683 A JP 13542683A JP S6026506 A JPS6026506 A JP S6026506A
Authority
JP
Japan
Prior art keywords
powder
supply pipe
powdered material
chute
powder supply
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
JP13542683A
Other languages
Japanese (ja)
Inventor
Akira Dewa
出羽 「あきら」
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
Kawasaki Motors Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Kawasaki Jukogyo KK
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, Kawasaki Jukogyo KK filed Critical Kawasaki Heavy Industries Ltd
Priority to JP13542683A priority Critical patent/JPS6026506A/en
Publication of JPS6026506A publication Critical patent/JPS6026506A/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
    • B65G69/00Auxiliary measures taken, or devices used, in connection with loading or unloading
    • B65G69/04Spreading out the materials conveyed over the whole surface to be loaded; Trimming heaps of loose materials
    • B65G69/0441Spreading out the materials conveyed over the whole surface to be loaded; Trimming heaps of loose materials with chutes, deflector means or channels

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chutes (AREA)
  • Air Transport Of Granular Materials (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Abstract

PURPOSE:To distribute a powdered or a particulate material in an arbitrary ratio, by installing a chute bottom plate which is connected to the top part of a powdered material feed pipe and has a slanted angle approximately equal to the angle of repose of the powdered material. CONSTITUTION:A powdered material, fed as shown by an arrow mark (a) from thr lower part of a powdered material feed pipe 1, is raised in a condition to fill the powdered material feed pipe 1 therewith. The powdered material so supplied is swollen in a cone at the top part of the powdered material feed pipe 1 depending upon the angle of repose inherent in the powdered material. When the supply of the powdered material is further continued starting with this state, the powdered material swollen in a cone is slipped down onto a chute bottom plate 2 along a slope inclined at the angle of repose. During such slip, the powdered material is divided by means of chute partitions 3, the slip of the powdered material onto each chute bottom plate 2 is distributed in a ratio proportioning a distance between the partitions 3.

Description

【発明の詳細な説明】 本発明は、粉体もし′くは粒状物を任意の比率に配分す
る為の粉体分配装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a powder dispensing device for distributing powder or granules in arbitrary proportions.

産業界の種々の技術分野において、粉体もしくは粒状物
(以下単に粉体とい5)を、一定の比率で正確に分割配
分し得るような設備の開発が要求されている。
In various technical fields of industry, there is a demand for the development of equipment that can accurately divide and distribute powder or granular materials (hereinafter simply referred to as powder 5) at a constant ratio.

例えば、流動床燃焼装置において、良好な燃焼を得る為
、あるいは窒素酸化物等の公害物質の排出を少なくする
為には、流動床内への燃料配分供給を、流動床内全体に
わたってできるだけ均等に行う必要がある。
For example, in a fluidized bed combustion device, in order to obtain good combustion or to reduce the emission of pollutants such as nitrogen oxides, the fuel must be distributed and supplied to the fluidized bed as evenly as possible throughout the entire fluidized bed. There is a need to do.

従って流動床燃焼装置にとっては、一定量の粒状燃料を
、多数の燃料供給ノズルに均等に分割配分する為の装置
が不可欠である。
Therefore, for a fluidized bed combustion apparatus, a device for evenly dividing and distributing a certain amount of granular fuel to a large number of fuel supply nozzles is essential.

従来の粉体供給装置を第1図に示し説明する。A conventional powder supply device is shown in FIG. 1 and will be described.

図において、燃料供給ノズルと同数の燃料定量供給機1
02を設け、燃料ホッパ101よシ上記燃料定量供給機
102を介して、各燃料供給ノズル毎に燃料を切シ出し
、これを空気ノズル104に供給して、空気搬送路10
5によシ、各燃料供給ノズルに導くようにしていた。
In the figure, the same number of fuel supply nozzles as fuel supply nozzles 1
02 is provided, and the fuel is cut out for each fuel supply nozzle through the fuel hopper 101 and the above-mentioned fuel quantitative supply device 102, and is supplied to the air nozzle 104, and the fuel is supplied to the air conveyance path 10.
5, it was designed to lead to each fuel supply nozzle.

このようにすることによって、各燃料供給ノズルに、燃
料を均等分配するようにしてい九〇然しなから、多数の
燃料定量供給機と、これに付随する制御装置が必要とな
り、その為装置全体が複雑且つ高価となり、又多数の燃
料定量供給装置を個別に駆動する為の消費動力が大きく
なるという欠点があった。
By doing this, the fuel is distributed evenly to each fuel supply nozzle, but a large number of fuel constant supply machines and associated control devices are required, which makes the entire system complicated. This method is complicated and expensive, and has the drawback of increasing power consumption for individually driving a large number of fuel metering devices.

これに代るものとして、第2図及び第3図に示す供給分
配装置が提案されている。
As an alternative to this, the supply distribution device shown in FIGS. 2 and 3 has been proposed.

先ず第2図に示す装置は、導管106によって空気搬送
されてきた燃料を、一旦集合筒107に導き、集合筒1
07から分岐した多数の空気搬送路105に分流する空
気流に乗せて分配するようにしたものである。
First, the device shown in FIG.
The air is distributed along air streams that branch out from air flow path 07 into a large number of air conveyance paths 105.

然しなから、集合筒107がら空気搬送路105に分流
する空気の流れは、空気搬送路105の通気抵抗に大き
く左右され、空気流量位各空気搬送路105の夫々に対
し必ずしも均一ではなく、従って精度の高い燃料の均等
配分は゛できないという欠点があった。
However, the flow of air branching from the collection tube 107 to the air conveyance path 105 is largely influenced by the ventilation resistance of the air conveyance path 105, and the air flow rate is not necessarily uniform for each air conveyance path 105. The drawback was that highly accurate and even fuel distribution was not possible.

これの改良として、第3図に示す配分手段が提案されて
いる。図において、導管106を2本の導管107′に
分岐し、更にこの導管107’を2本の導管108に、
次いで導管108を2本の導管109に順次分岐し、空
気の流れをできるだけ正確に分流するようにしたもので
ある。
As an improvement on this, a distribution means shown in FIG. 3 has been proposed. In the figure, the conduit 106 is branched into two conduits 107', which are further divided into two conduits 108,
The conduit 108 is then sequentially branched into two conduits 109 to divide the air flow as accurately as possible.

然しなから、各分岐管に均等に空気を分流させる為には
、分岐管の前後に相当長さの直管部を設けて整流する必
要があり、その為に可成り広い配管占有空間を必要とす
る欠点があった。
However, in order to divide the air evenly into each branch pipe, it is necessary to install a considerable length of straight pipe section before and after the branch pipe to rectify the flow, which requires a considerably large space occupied by the piping. There was a drawback.

このように第2図及び第3図に示すように、搬送の過程
で配分するのは、高い精度の配分ができないこと、及び
広い占有空間を要するという欠点があり、又第1図に示
す装置のように予め配分したものを空気搬送する場合は
、装置全体が複雑化すると共に、消費動力が大きくなる
という技術的問題があった。
As shown in FIGS. 2 and 3, distributing during the transportation process has the drawbacks of not being able to perform highly accurate distribution and requiring a large space; In the case of pneumatically conveying pre-distributed materials, there are technical problems in that the entire device becomes complicated and power consumption increases.

本発明は、上記従来の欠点乃至は技術的な問題を解決し
、配分精度が高く且つ簡単な構造にして占有空間の少な
い粉体分配装置を提供せんとするものである。
The present invention aims to solve the above-mentioned conventional drawbacks or technical problems and to provide a powder dispensing device that has high dispensing accuracy, has a simple structure, and occupies less space.

即ち本発明は、粉体供給管を垂直に立設し、この粉体供
給管の頂部に接続され、粉体の安息角にほぼ近い角度に
傾斜し、上記粉体供給管の外周を任意の角度に分割して
菊花弁状に複数個のシュート底板を設け、この複数のシ
ュート底板の接合部に7−−ト隔壁を設け、粉体供給管
の下方より粉体を供給し、粉体の安息角にそって粉体を
自由滑動させて分配するようにした本のである。
That is, in the present invention, a powder supply pipe is vertically installed, connected to the top of the powder supply pipe, and inclined at an angle approximately close to the angle of repose of the powder, and the outer periphery of the powder supply pipe is set at an arbitrary angle. A plurality of chrysanthemum-petal-shaped chute bottom plates are divided into angles, and a seven-piece partition is provided at the joint of the plurality of chute bottom plates, and the powder is supplied from the bottom of the powder supply pipe. This is a book that distributes powder by sliding it freely along the angle of repose.

第2の発明は、上記粉体供給管の頂部に臨ませてスクレ
ーパを設け、粉体供給管によって移送されてきた粉体を
スクレーパによって払い落しながら各シュートに対し粉
体を配分するようにしたものである。
In the second invention, a scraper is provided facing the top of the powder supply pipe, and the powder transferred by the powder supply pipe is scraped off by the scraper, and the powder is distributed to each chute. It is something.

又第3の発明としては、上記シュート底板を蓋板にて密
閉し、これに搬送用空気ダクトを接続し、上記スクレー
パによって払い落され分配した粉体を、直接空気搬送す
るようにしたものである。
In a third invention, the chute bottom plate is sealed with a cover plate, and a conveying air duct is connected to this, so that the powder scraped off and distributed by the scraper is directly conveyed by air. be.

以下本発明の一実施例について詳細に説明する。第4図
(平面図)及び第5図(縦断面図)において、1は垂直
に立設した粉体供給管である。2はシュート底板であり
、粉体の安息角に近い角度で傾斜するように、その一端
は粉体供給管1の頂部に接続されている。又このシュー
ト底板2は粉体供給管1の外周を任意の角度に分割し、
菊花弁状に複数個設けられている。第4図の場合は一例
として8等分角に分割する場合を外している。3ti上
記複数のシュート底板2の接合部に立設して設けたシュ
ート隔壁であシ、シュート底板2の分割された入口部を
形成する。4はシュート底板3に連続して接合され、シ
ュート底板2の傾斜面に沿って立設されたシュート側壁
である。5はシュート底板2の最終端に設けた排出管で
ある。
An embodiment of the present invention will be described in detail below. In FIG. 4 (plan view) and FIG. 5 (longitudinal cross-sectional view), reference numeral 1 denotes a powder supply pipe that stands vertically. Reference numeral 2 denotes a chute bottom plate, one end of which is connected to the top of the powder supply pipe 1 so as to be inclined at an angle close to the angle of repose of the powder. In addition, this chute bottom plate 2 divides the outer circumference of the powder supply pipe 1 into arbitrary angles,
Multiple pieces are arranged in the shape of chrysanthemum petals. In the case of FIG. 4, as an example, the case where the angle is divided into eight equal parts is excluded. 3ti The chute partition walls are provided upright at the joints of the plurality of chute bottom plates 2 to form divided entrance portions of the chute bottom plates 2. A chute side wall 4 is continuously joined to the chute bottom plate 3 and is erected along the inclined surface of the chute bottom plate 2. 5 is a discharge pipe provided at the final end of the chute bottom plate 2.

以上のように構成した本実施例において、粉体供給管1
の下方よシ矢印イのように供給されてきた粉体は、粉体
供給管1に充満された状態で上昇する。このようにして
供給されてきた粉体は、粉体供給管1の頂部において、
粉体個有の安息角に応じて円錐状に盛り上る。この状態
から更に供給を続けると、円錐状に盛り上った粉体は、
安息角の傾斜面に沿って、シュート底板2上に滑落する
。この過程において、粉体はシュート隔壁3によって分
割され、各シュート底板2上への粉体の滑落は隔壁3の
間隔に応じた比率に配分される。このようにして所望の
比率に配分されて、シュート底板2上に滑落した粉体は
、続いてシュート底板2の斜面に沿って滑シ落ち、排出
管5よシ所定の所へと分配される。
In this embodiment configured as above, the powder supply pipe 1
The powder that has been supplied downward as shown by arrow A rises while the powder supply pipe 1 is filled with it. The powder thus supplied is placed at the top of the powder supply pipe 1.
It rises in a conical shape according to the powder's unique angle of repose. If the supply continues from this state, the powder that has risen into a conical shape will become
It slides down onto the chute bottom plate 2 along the slope of the angle of repose. In this process, the powder is divided by the chute partition walls 3, and the amount of powder falling onto each chute bottom plate 2 is distributed at a ratio according to the spacing between the partition walls 3. The powder, which is distributed in a desired ratio in this manner and slides down onto the chute bottom plate 2, then slides down along the slope of the chute bottom plate 2 and is distributed to a predetermined location through the discharge pipe 5. .

次に第6図(平面図)及び第7図(縦断面図)に示した
第2の実施例について説明する。
Next, a second embodiment shown in FIG. 6 (plan view) and FIG. 7 (longitudinal sectional view) will be described.

図において、第4図及び第5図に示しだ第1の実施例と
異る点は、粉体供給管1の頂部に臨ませて、スクレーパ
を設けたことである。
In the figure, the difference from the first embodiment shown in FIGS. 4 and 5 is that a scraper is provided facing the top of the powder supply pipe 1.

図において、6はスクレーパの回転軸であυ、図示省略
の駆動装置により回転させられる。7は回転軸6に取付
けられた複数枚の羽根であり、この羽根7の形状は、矢
印方向に回転することによシ、粉体を外方に押し出すよ
うに形成されている。
In the figure, 6 is a rotating shaft of the scraper, which is rotated by a drive device (not shown). Reference numeral 7 denotes a plurality of blades attached to the rotating shaft 6, and the blades 7 are shaped so as to push the powder outward when rotated in the direction of the arrow.

この第2実施例において、粉体供給管1内を充満して押
し上げられてきた粉体は、順次スクレーパの羽根7によ
って外方に更に押し出される。このようにして押し出さ
れた粉体は、シュート隔壁3によって任意の比率に配分
されて、シュート底板2上に滑落し、次いでシュート底
板2上を滑り落ち、排出管5(第5図参照)よシ排出さ
れる。
In this second embodiment, the powder that has filled the powder supply pipe 1 and been pushed up is successively further pushed outward by the blades 7 of the scraper. The powder thus pushed out is distributed in an arbitrary ratio by the chute bulkhead 3, slides down onto the chute bottom plate 2, then slides down on the chute bottom plate 2, and then passes through the discharge pipe 5 (see Fig. 5). is discharged.

この第2実施例の場合は、比較的微粉のもの又は水分の
含んでいるもの等、粉体の安息角が小なるものに適して
いる。
The second embodiment is suitable for powders with a small angle of repose, such as relatively fine powders or those containing moisture.

次に第8図(平面図)及び第9図(縦断面図)に示す第
3の実施例について説明する。
Next, a third embodiment shown in FIG. 8 (plan view) and FIG. 9 (longitudinal sectional view) will be described.

この第3の実施例において、前記第1及び第2の実施例
と異る点は、シュート底板を密閉にし、直接空気搬送で
きるようにした点である。
The third embodiment differs from the first and second embodiments in that the chute bottom plate is sealed to allow direct pneumatic conveyance.

図において、11は張板であシ、シュート隔壁3、シュ
ート側板4の上面及びスクレーノくの羽根7の上面を覆
うように設けられ、シュート底板2を密閉にしている。
In the figure, reference numeral 11 is a clad plate, which is provided so as to cover the chute partition wall 3, the upper surface of the chute side plate 4, and the upper surface of the crane blade 7, thereby sealing the chute bottom plate 2.

14は円環状の搬送用空気ダクトでアシ、上記蓋板11
を開にして接続され、主空気ダクト12よシ送風されて
きた空気を、円錐ダクト13を介して円環ダクト14に
導き、シュート隔壁3によって任意の比率に分流(第8
図参照)し、シュート底板2の斜面に沿って流れるよう
に形成されている。
14 is an annular conveying air duct with reeds, and the lid plate 11
The air blown through the main air duct 12 is guided to the annular duct 14 via the conical duct 13, and is divided into arbitrary ratios by the chute bulkhead 3 (the eighth
(see figure) and is formed to flow along the slope of the chute bottom plate 2.

尚、図中8は駆動装置9とスクレーノ(の回転軸6とを
接続する為の接続部材、10は駆動装置9の支持部材で
ある。
In the figure, 8 is a connecting member for connecting the drive device 9 and the rotating shaft 6 of the screener, and 10 is a support member for the drive device 9.

以上のように構成した第3の実施例において、矢印イの
方向から供給され、粉体供給管1内を充満して押し上げ
られてきた粉体は、スクレーパの羽根7によって外方に
−押し出されながら、シュート隔壁3によって任意の比
率に配分され、シュート底板2上に滑落する。このよう
にしてシュート底板2上を滑り落ちてきた粉体は、環状
の搬送用ダクト14より送風され、シュート底板2の斜
面に沿って流れている空気流に乗って搬送され、排出管
5を介してそのまま所定の所まで搬送される。
In the third embodiment configured as described above, the powder that is supplied from the direction of arrow A, fills the powder supply pipe 1, and is pushed up is pushed outward by the blades 7 of the scraper. Meanwhile, it is distributed in an arbitrary ratio by the chute partition wall 3 and slides down onto the chute bottom plate 2. The powder that has slipped down on the chute bottom plate 2 in this way is blown from the annular conveying duct 14, carried by the air flow flowing along the slope of the chute bottom plate 2, and then passed through the discharge pipe 5. It is transported as it is to a predetermined location.

以上詳述した通シ、本発明の粉体分配装置によれば、粉
体供給管を垂直に立設し、粉体の安息角にほぼ等しい傾
斜角で、複数のシュート底板を粉体供給管の頂部に接続
し、シュート底板相互間の接合部にシュート隔壁を立設
したので、下方より粉体供給管内を通して供給されてく
る粉体は、粉体の安息角に応じて滑落しながら、シュー
ト隔壁によって任意の比率に分配することができた。
As described in detail above, according to the powder distribution device of the present invention, the powder supply pipe is vertically erected, and the plurality of chute bottom plates are connected to the powder supply pipe at an angle of inclination approximately equal to the angle of repose of the powder. Since the chute bulkhead is installed at the joint between the chute bottom plates, the powder supplied from below through the powder supply pipe will slide down the chute according to the angle of repose of the powder. It could be distributed in any ratio by means of partitions.

又上記粉体供給管の頂部開口に臨ませて、スクレーパを
設け、供給されてくる粉体な外方に向けて押し出すよう
にしたので、粉体の性状に拘わりなく、シュート隔壁を
介して強制的に配分することができた。
In addition, a scraper is provided facing the top opening of the powder supply pipe to push out the powder that is being supplied to the outside, so regardless of the properties of the powder, it is forced through the chute partition wall. It was possible to allocate it evenly.

更にシェード底板を密閉にし、これに搬送用空気ダクト
を接続することによって、複雑な空気ダクトを必要とせ
ず、粉体を直接空気搬送することができる。
Furthermore, by sealing the shade bottom plate and connecting the conveying air duct to it, the powder can be directly conveyed by air without the need for a complicated air duct.

このようにして粉体を予め任意の比率に配分することに
よって空気搬送路の流路抵抗がそれぞれ異っても、搬送
される粉体の配分には何ら影響されず、粉体の配分が確
実に行われる。
By distributing the powder in advance in an arbitrary ratio in this way, even if the flow path resistance of the air conveyance path differs, the distribution of the powder to be conveyed is not affected in any way, and the distribution of the powder is ensured. It will be held on.

又粉体は、粉体供給管内を充満して移送されるので、粉
体供給量の調節は敏捷に行われ、粉体供給量の微量調節
及び応答性の高い制御が可能である。
Further, since the powder is transferred while filling the inside of the powder supply pipe, the amount of powder supplied can be quickly adjusted, and the amount of powder supplied can be finely adjusted and controlled with high responsiveness.

更には、構造が簡単であるので、装置の占有空間が少な
くて済み、又駆動部分が少ないので、これに要する消費
動力も大巾に軽減され、配分機能、制御性、占有空間及
び経済面等すべての点で優れた効果を有する。
Furthermore, since the structure is simple, the space occupied by the device is small, and since there are few moving parts, the power consumption required for this is greatly reduced, which improves distribution function, controllability, space occupancy, and economical aspects. It has excellent effects in all respects.

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

第1図乃至第3図は、従来の分配装置の概略を示す図で
ある。第4図乃至第9図は本発明の実施例である。第4
図は第1実施例の平面図、第5図は第4図のA−A線に
おける縦断面図である。第6図はスクレーパを設けた第
2実施例の要部平面図、第7図は第6図のA−A線にお
ける縦断面図である。第8図はシュート底板を1・・・
粉体供給管 2・−・シュート底板3・・・シュート隔
壁 4・・−シュート側壁5・・・排出管 6・・・回
転軸 7・・・スクレーパ羽根(スクレーパ) 11−
・・蓋板 °−1..1パ′■゛ ゛ 101 03 箪 21文 第5図 計・ 第6図
1 to 3 are diagrams schematically showing a conventional dispensing device. 4 to 9 show embodiments of the present invention. Fourth
The figure is a plan view of the first embodiment, and FIG. 5 is a longitudinal cross-sectional view taken along line A--A in FIG. 4. FIG. 6 is a plan view of a main part of the second embodiment in which a scraper is provided, and FIG. 7 is a longitudinal cross-sectional view taken along the line A--A in FIG. 6. Figure 8 shows the chute bottom plate 1...
Powder supply pipe 2... Chute bottom plate 3... Chute partition wall 4... - Chute side wall 5... Discharge pipe 6... Rotating shaft 7... Scraper blade (scraper) 11-
・・Lid plate °-1. .. 1st part'■゛ ゛ 101 03 箪 21 sentences 5th diagram/Figure 6

Claims (3)

【特許請求の範囲】[Claims] (1) 垂直に立設した粉体供給管と、該粉体供給管の
頂部に接続し粉体の安息角にほぼ近い傾斜角を有し粉体
供給管の外周を任意の角度に分割して菊花弁状に設けた
複数個のシュート底板と、該複数個のシュート底板の接
合部に立設したシュート隔壁とから成る粉体分配装置。
(1) A powder supply pipe installed vertically, connected to the top of the powder supply pipe and having an inclination angle approximately close to the angle of repose of the powder, and dividing the outer circumference of the powder supply pipe into arbitrary angles. A powder distribution device comprising a plurality of chrysanthemum petal-shaped chute bottom plates and a chute partition wall erected at the joint of the plurality of chute bottom plates.
(2)垂直に立設した粉体供給管と、該粉体供給管の頂
部に接続し粉体の安息角にtlは近い傾斜角を有し粉体
供給管の外周を任意の角度に分割して菊花弁状に設けた
複数個のシュート底板と、該複数個のシュート底板と、
該複数個のシュート底板の接合部に立設したシュート隔
壁と、前記粉体供給管の頂部開口に臨ませて設けたスク
レーパとから成る粉体分配装置。
(2) A powder supply pipe installed vertically, connected to the top of the powder supply pipe, with an inclination angle tl close to the angle of repose of the powder, and the outer periphery of the powder supply pipe is divided into arbitrary angles. a plurality of shoot bottom plates provided in the shape of chrysanthemum petals, and the plurality of shoot bottom plates;
A powder distribution device comprising a chute partition wall installed upright at the joint of the plurality of chute bottom plates, and a scraper provided facing the top opening of the powder supply pipe.
(3)垂直に立設した粉体供給管と、該粉体供給管の頂
部に接続し粉体の安息角にほぼ近い傾斜角を有し粉体供
給管の外周を任意の角度に分割して菊花弁状に設けた複
数個のシュート底板と、該複数個のシュート底板の接合
部に立設したシュート隔壁と、前記粉体供給管の頂部開
口に臨ませて設けたスクレーパとから成り、上記シュー
ト底板に蓋板を設けて密閉し、該密閉にしたシュート底
板に搬送用空気ダクトを接続したことを特徴とする粉体
分配装置。
(3) A powder supply pipe installed vertically, connected to the top of the powder supply pipe and having an inclination angle approximately close to the angle of repose of the powder, and dividing the outer periphery of the powder supply pipe into arbitrary angles. It consists of a plurality of chrysanthemum petal-shaped chute bottom plates, a chute partition wall erected at the joint of the plurality of chute bottom plates, and a scraper provided facing the top opening of the powder supply pipe, A powder distribution device characterized in that the chute bottom plate is provided with a lid plate and sealed, and a conveying air duct is connected to the sealed chute bottom plate.
JP13542683A 1983-07-25 1983-07-25 Device for distributing powdered material Pending JPS6026506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13542683A JPS6026506A (en) 1983-07-25 1983-07-25 Device for distributing powdered material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13542683A JPS6026506A (en) 1983-07-25 1983-07-25 Device for distributing powdered material

Publications (1)

Publication Number Publication Date
JPS6026506A true JPS6026506A (en) 1985-02-09

Family

ID=15151448

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13542683A Pending JPS6026506A (en) 1983-07-25 1983-07-25 Device for distributing powdered material

Country Status (1)

Country Link
JP (1) JPS6026506A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS628227U (en) * 1985-06-28 1987-01-19
JPS63287541A (en) * 1987-04-30 1988-11-24 デグツサ・アクチエンゲゼルシヤフト Method and apparatus for continuously compounding powdery substance
CN112173589A (en) * 2020-10-12 2021-01-05 武汉轻工大学 Belt type grain flow dividing and conveying device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5393568A (en) * 1977-01-25 1978-08-16 Yoshiaki Nakamura Apparatus for exhausting water which is separated in constant volume

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5393568A (en) * 1977-01-25 1978-08-16 Yoshiaki Nakamura Apparatus for exhausting water which is separated in constant volume

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS628227U (en) * 1985-06-28 1987-01-19
JPH0215864Y2 (en) * 1985-06-28 1990-04-27
JPS63287541A (en) * 1987-04-30 1988-11-24 デグツサ・アクチエンゲゼルシヤフト Method and apparatus for continuously compounding powdery substance
JPH0448493B2 (en) * 1987-04-30 1992-08-06 Degussa
CN112173589A (en) * 2020-10-12 2021-01-05 武汉轻工大学 Belt type grain flow dividing and conveying device

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