JP3360003B2 - Powder inlet for powder flow tank - Google Patents

Powder inlet for powder flow tank

Info

Publication number
JP3360003B2
JP3360003B2 JP06194597A JP6194597A JP3360003B2 JP 3360003 B2 JP3360003 B2 JP 3360003B2 JP 06194597 A JP06194597 A JP 06194597A JP 6194597 A JP6194597 A JP 6194597A JP 3360003 B2 JP3360003 B2 JP 3360003B2
Authority
JP
Japan
Prior art keywords
powder
tank
dust
inlet
closed tank
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 - Fee Related
Application number
JP06194597A
Other languages
Japanese (ja)
Other versions
JPH10236582A (en
Inventor
一仁 花野
隆亮 出口
吉貞 道浦
勇治 橋本
公也 稼農
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.)
Kurimoto Ltd
Original Assignee
Kurimoto 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 Kurimoto Ltd filed Critical Kurimoto Ltd
Priority to JP06194597A priority Critical patent/JP3360003B2/en
Publication of JPH10236582A publication Critical patent/JPH10236582A/en
Application granted granted Critical
Publication of JP3360003B2 publication Critical patent/JP3360003B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Air Transport Of Granular Materials (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は粉体材料を貯蔵し、
かつ、必要のある部門へ的確に供給するために密閉状態
で流動化する粉体流動用タンク、特に該タンク内へ材料
である粉体を補充供給するときに開口する粉体投入口に
係る。
The present invention relates to a method for storing powder material,
Further, the present invention relates to a powder flow tank which is fluidized in a closed state in order to supply the powder to a necessary department accurately, and particularly to a powder inlet which is opened when refilling and supplying powder as a material into the tank.

【0002】[0002]

【従来の技術】粉体の輸送に空気力を利用する方法やそ
の方法を実施するための装置は既に多数の型式が提案さ
れ実用に供されている。粉体の使用範囲が研究の成果と
共に飛躍的に拡大し、その粉体の性格や品質に最も適応
した輸送手段が採られるのは当然であるが、従来からの
粉体輸送の思想としては、粉体貯蔵タンクの適正な位置
に装着した粉体搬送エゼクター等に高圧空気を噴き込ん
で粉体を大量に搬送する方式と、密閉タンク内で高圧空
気をほぼ全面に亘って均等に噴き上げ、粉体と空気とを
流動状態として必要時に排出供給する方式とが主要な分
類と解され、それぞれその長所を伸し短所を矯める多数
の従来技術が提示されている。
2. Description of the Related Art Numerous types of methods for utilizing pneumatic force for transporting powder and apparatuses for implementing the method have already been proposed and put to practical use. It is natural that the range of use of powder will expand dramatically with the results of research, and the most appropriate means of transport for the nature and quality of the powder will be adopted, but as a conventional concept of powder transport, A method of injecting high-pressure air into a powder transport ejector mounted at an appropriate position in the powder storage tank to transport a large amount of powder, and a method of blowing high-pressure air evenly over almost the entire surface in a closed tank, The method of discharging the body and air in a flowing state when necessary is understood as a main classification, and a number of conventional techniques have been proposed which extend their advantages and correct their disadvantages, respectively.

【0003】本発明はそのうちの流動化の方式に係る粉
体流動用タンクの粉体投入口に関する改善を目的とし、
具体的には図2にその典型的な構造の概略を示した粉体
流動用タンクが対象となる。すなわち、密閉タンク10
1は水平な多孔板106によって上下に隔離され、上方
が粉体流動室105、下方が流動化用空気室107であ
る。粉体流動室105の下方、多孔板106の直上近く
に粉体の排出口108があり、排出弁109の開閉によ
って所望のタイミングで密閉タンク内の粉体をタンク外
へ排出する。一方、多孔板下の流動化用空気室107に
は流動用圧縮空気を供給する空気配管110が開閉弁1
11を介して接続し、流動化に必要な高圧空気を流動化
用空気室に供給し、多孔板106に多数規則的に穿孔し
た噴射孔112からほぼ全面的に均等な空気圧で上方の
流動化用空気室に噴き上げるから、流動化用空気室内で
は一様に流動層が形成され、多くの粉体は空気と共に恰
も液体が沸騰するような流動運動を誘発する。
An object of the present invention is to improve the powder inlet of a powder flowing tank according to the fluidizing method.
Specifically, the target is a powder flowing tank whose typical structure is schematically shown in FIG. That is, the closed tank 10
Numeral 1 is vertically separated by a horizontal perforated plate 106, an upper part is a powder flowing chamber 105, and a lower part is a fluidizing air chamber 107. A powder discharge port 108 is provided below the powder flow chamber 105 and immediately above the perforated plate 106, and discharges the powder in the closed tank at a desired timing by opening and closing the discharge valve 109. On the other hand, in the fluidizing air chamber 107 below the perforated plate, an air pipe 110 for supplying compressed air for fluidizing is provided with the on-off valve 1.
11 to supply high-pressure air necessary for fluidization to the fluidizing air chamber, and upwardly fluidize with substantially uniform air pressure almost entirely from the injection holes 112 that are regularly drilled in the perforated plate 106. Since the fluid is blown up into the fluidizing air chamber, a fluidized bed is uniformly formed in the fluidizing air chamber, and many powders induce a fluidizing motion such that the liquid boils together with the air.

【0004】通常はこの態様で順調に作用が進行し、均
等な流動化と所望の時機に粉体の排出とが行なわれるの
であるが、次第に密閉タンク内の粉体残量が減少するに
つれて流動化の状態にも変化が起こるし、定常状態の流
動化を持続しなければならないから、流動化運動を継続
中の密閉タンク101へ消費した粉体を補充する必要が
ある。図2のように通常の粉体流動用タンクの形態は密
閉タンクの上面に粉体投入口102を設け、作業中は上
蓋123を載置して密閉状態を保ち、粉体供給時には取
り外した開口部から粉体を装入して粉体流動室の粉体を
補充して定常状態に回帰させるのである。
Normally, the operation proceeds smoothly in this manner, and uniform fluidization and powder discharge are performed at a desired time. However, as the amount of powder remaining in the closed tank gradually decreases, the fluidization proceeds. Since the state of the fluidization changes and the steady-state fluidization must be maintained, it is necessary to replenish the consumed tank powder to the closed tank 101 during the fluidization movement. As shown in FIG. 2, in the form of a normal powder flowing tank, the powder inlet 102 is provided on the upper surface of the closed tank, and the upper lid 123 is placed during the operation to keep the sealed state. The powder is charged from the section and the powder in the powder flow chamber is replenished to return to a steady state.

【0005】[0005]

【発明が解決しようとする課題】上蓋を取り外した粉体
投入口102から粉体を密閉タンク101内へ装入する
ときは、垂直に大量の粉体が加速度を伴ってフリーに落
下するわけであるから、蒙々たる粉塵が立ち籠めて密封
空間の唯一の開口部である粉体投入口からその粉塵が集
中的に吹き出そうとするから、そのままでは到底作業で
きるような環境ではない。そのために通常は粉体投入口
102とは別に密閉タンクの頂面に吸粉ダクト104を
取り付けて端部が図示しない集塵機に繋がる配管を施
し、密閉タンク内の流動層上部の空間に浮遊する大量の
粉塵を吸引して排出することによって一応は作業可能な
職場環境の確保を図っている。
When powder is charged into the closed tank 101 from the powder inlet 102 with the upper lid removed, a large amount of powder vertically falls freely with acceleration. Therefore, it is not an environment in which the work can be performed as it is because the dust is gathered and the dust is intensively blown out from the powder inlet, which is the only opening of the sealed space. For this purpose, a dust-absorbing duct 104 is usually attached to the top surface of the closed tank separately from the powder inlet 102, and a pipe is connected to the dust collector whose end is not shown. By sucking and discharging the dust, we are working to ensure a work environment where we can work.

【0006】しかし、このような構成は有効な粉塵の排
出と回収が難しく、効果的に排塵を強化するためには、
必要以上に集塵機の能力を増大して臨まなければなら
ず、また、蓋面を被冠した定常状態では密閉タンクの内
圧と外圧との差が大きくなり過ぎて上蓋が開け難くな
り、ときには密閉タンク自体の変形や粉体の排出作用が
不安定となるなどの悪条件を誘発する虞れがある。
However, such a configuration makes it difficult to effectively discharge and collect dust, and in order to effectively enhance dust removal,
It is necessary to increase the capacity of the dust collector more than necessary, and in the steady state with the cover surface covered, the difference between the internal pressure and the external pressure of the closed tank becomes too large to make the upper lid difficult to open, and sometimes the closed tank There is a possibility that bad conditions such as deformation of the powder itself and instability of the powder discharging operation may be induced.

【0007】図3(A)(B)(C)は粉体流動用タン
クから別の粉体流動用タンクへ粉体を転送するとき飛散
する問題を解決するために提示された従来技術(実公昭
58−11785号公報)を引用したものである。図
(A)は全体の構成を例示し、図(B)が本従来技術に
おける課題を示したさらに以前の従来技術であり、図
(C)が本引用例の実施例である。この技術の内容は、
一つの粉体流動用タンク201から粉体を取り出して緩
傾斜の圧力シュート202を流動化しつつ転送して端部
に至り、垂直管203から別の粉体流動用タンク204
へ転落して移し替える基本構成において、従来は図
(B)で示すように垂直管内での落下速度が大きいため
粉体と一緒に大量の随伴エアーが降下し粉体流動用タン
ク204内に一緒に持ち込まれるから、タンク上面が開
放しておれば粉塵の飛散が凄じく、また上面を閉塞した
定常の流動化状態ではタンクの内圧が過大となって集塵
機206のフィルタの負担が著しく、タンクの隙間など
から漏出することを課題と捉えている。
FIGS. 3 (A), 3 (B) and 3 (C) show a prior art (actual) proposed to solve the problem of scattering when transferring powder from a powder flowing tank to another powder flowing tank. No. 58-11785). FIG. 1A illustrates the entire configuration, FIG. 1B shows a prior art prior to showing the problems in the present prior art, and FIG. 1C shows an embodiment of the cited example. The content of this technology is
The powder is taken out from one powder flow tank 201 and transferred while fluidizing a gentle-slope pressure chute 202 to reach the end, from the vertical tube 203 to another powder flow tank 204.
In the basic configuration in which the powder is dropped and transferred, a large amount of accompanying air drops together with the powder due to the high falling speed in the vertical pipe as shown in FIG. When the top surface of the tank is open, the scattering of dust is enormous, and in a steady fluidized state with the top surface closed, the internal pressure of the tank becomes excessive and the load on the filter of the dust collector 206 becomes remarkable. Leakage from gaps in the area is considered an issue.

【0008】この従来技術ではこの課題を解決するため
に図(C)のように垂直管203と平行に上下で連通す
る環流管205を併設し、粉体に随伴してきたエアーを
粉体流動用タンク内から導き戻し、再度、随伴エアーと
なるように環流させてタンクの内圧上昇と粉塵飛散の防
止の効果を得たと謳っている。しかしながら、この図
(C)のような機能が完全に発揮できるか疑問も残り、
粉体の供給に伴って浮遊粉体を濃厚に含む流体(空気)
がすべて環流できればよいのであるが、部分的には粉体
投入口の方向へ向って逆流し搬送作用を低下させる原因
となるのではないかとも懸念される。
In this prior art, in order to solve this problem, as shown in FIG. 1C, a reflux pipe 205 communicating vertically with the vertical pipe 203 is provided in parallel, and air accompanying powder is used for powder flow. It is said that the tank was returned from the tank and circulated again so as to become the accompanying air, and the effects of increasing the internal pressure of the tank and preventing dust scattering were obtained. However, there remains a question whether the function shown in FIG.
Fluid (air) that contains suspended powder in a rich state as the powder is supplied
However, there is a concern that this may partially cause the powder to flow backward in the direction of the powder inlet and reduce the conveying action.

【0009】本発明は以上の課題を解決するために粉体
の補充供給のために上蓋を開放したときでも、装入時に
密閉タンク内へ落下する粉体が舞上がって大量の粉塵が
吹き出す現象を阻止し、円滑な材料供給が容易に、かつ
職場環境を悪化させずに実施できる新規な粉体流動用タ
ンクの粉体投入口の提供を目的とする。
According to the present invention, in order to solve the above-mentioned problems, even when the upper lid is opened for replenishing and supplying powder, the powder falling into the closed tank at the time of charging rises and a large amount of dust is blown out. It is an object of the present invention to provide a new powder inlet for a powder flowing tank which can prevent the occurrence of a problem and facilitate the smooth material supply without deteriorating the work environment.

【0010】[0010]

【課題を解決するための手段】本発明に係る粉体流動用
タンクの粉体投入口2は、密閉タンク1の頂面11より
突出して上蓋23を着脱自在に装着する蓋面21と、密
閉タンク1の内部まで突出する底面22よりなる円筒体
で形成し、前記蓋面21より低位置に頂点31を固定
し、該粉体投入口2の内周面24との間に下窄みの傾斜
空間Eを形成する円錐面32を具え、前記底面22より
低く位置付けた円錐底面33よりなるコーン3を粉体投
入口2の円筒軸と同心に内設し、さらに前記密閉タンク
1の蓋面21上で粉体投入口2の外周を囲繞して密閉タ
ンク1内と連通する一端41を具え、他端42が前記傾
斜空間E内の流速を増加しつつ粉体Pを該タンク内へ流
入させると共に、舞い上がった粉塵を吸引する集塵機6
と開閉自在に繋がる吸粉ダクト4を設けたことを構成上
の特徴とする。
According to the present invention, a powder inlet 2 of a powder flowing tank according to the present invention has a lid surface 21 which protrudes from the top surface 11 of the closed tank 1 and on which an upper lid 23 is detachably mounted. It is formed of a cylindrical body having a bottom surface 22 protruding to the inside of the tank 1, and a vertex 31 is fixed at a position lower than the lid surface 21. A cone 3 having a conical surface 32 forming an inclined space E and having a conical bottom surface 33 positioned lower than the bottom surface 22 is provided concentrically with the cylindrical axis of the powder inlet 2, and a lid surface of the closed tank 1. 21 to seal the outer periphery of the powder inlet 2
And the other end 42 is connected to the inside of
The powder P flows into the tank while increasing the flow velocity in the oblique space E.
Dust collector 6
The configuration is characterized in that a dust-absorbing duct 4 is provided so as to open and close freely .

【0011】粉体を密閉タンク内へ供給するときには、
粉体投入口2の蓋面21上に被冠した上蓋23を取り外
して開放し、開口した蓋面から装入する。装入された粉
体は粉体投入口の円筒内周面とコーン3の円錐面32間
の傾斜空間E(ディフューザー)内を通過してタンク内
へ投入される。このとき当然大量の粉体が舞上がるが、
密閉タンク内は常に吸粉ダクト4を介して終端に接続す
る集塵機6の作用を受けて大気圧より減圧された状態と
なっているから、下窄みの傾斜空間形状によって空気は
流速を増加しながら粉体投入口2から密閉タンク内へ流
入し、舞上がる粉体が粉体投入口から外部へ流出するこ
とを阻止する作用が現われる。すなわち、吸粉ダクト4
の一端41は密閉タンク1の頂面11より上方で該タン
クと連通しているから、該タンク内の上方に舞い上がっ
た粉塵のみを効果的に捕捉して吸引する。しかも前記一
端41は、言うまでもなく粉体投入口2の底面22より
上位にあるから、この円筒体が隔壁となって傾斜空間E
内の粉体Pの流入を進行させ、連行した空気が増速して
効果的に粉体の供給を促進するという作用を両立させ
る。
When powder is supplied into a closed tank,
The upper lid 23 covered on the lid surface 21 of the powder inlet 2 is removed and opened, and the powder is charged from the opened lid surface. The charged powder passes through the inclined space E (diffuser) between the inner peripheral surface of the cylinder of the powder inlet and the conical surface 32 of the cone 3 and is charged into the tank. At this time, of course, a large amount of powder soars,
Since the inside of the closed tank is always reduced in pressure from the atmospheric pressure by the action of the dust collector 6 connected to the end via the dust absorbing duct 4, the air velocity increases due to the inclined space shape of the lower constriction. While flowing from the powder inlet 2 into the closed tank, the function of preventing the soaring powder from flowing out of the powder inlet to the outside appears. That is, the dust absorbing duct 4
One end 41 of the tank is above the top surface 11 of the closed tank 1.
So that it rises up in the tank
Effectively captures and sucks only dust. And the one
The end 41 is, of course, from the bottom surface 22 of the powder inlet 2.
Since it is on the upper level, this cylindrical body serves as a partition wall and the inclined space E
The inflow of the powder P in the inside proceeds, and the entrained air speeds up
Effectively promote powder supply
You.

【0012】密閉タンクから粉体を排出するときには、
吸粉ダクトの外部への連通を閉鎖するか絞り込んで一次
的に密閉タンクの内圧を高めてスムースに粉体が排出す
るようにする。また、蓋面を被冠している上蓋23を取
り外すときも吸粉ダクトの外部(集塵機)との連通を一
次遮断するか絞り込むと、内圧が高くなるために取り外
しが容易に行なえる。この場合、上蓋を外して蓋面21
を開口すると同時に吸粉ダクトを開き粉塵の舞上がりを
吸引して阻止することは、既述の通りである。
When discharging powder from a closed tank,
By closing or narrowing down the communication with the outside of the dust absorbing duct, the internal pressure of the closed tank is temporarily increased to smoothly discharge the powder. Also, when the upper lid 23 covering the lid surface is removed, if the communication with the outside (the dust collector) of the dust-absorbing duct is primarily cut off or narrowed down, the internal pressure increases, so that the removal can be easily performed. In this case, the upper lid is removed and the lid surface 21 is removed.
As described above, the dust suction duct is opened at the same time that the dust is opened to suck and prevent the dust from rising.

【0013】[0013]

【発明の実施の形態】図1(A)(B)は本発明の実施
形態の一つであり、特に粉体投入口と吸粉ダクト付近を
主に示した部分正面図である。その他の構造は図2の従
来技術の正面図と基本的に変らず、図1では図示しない
多孔板や流動用空気室、密閉タンク1内に貯蔵し流動し
ている粉体を適宜必要な時機に排出する排出口、高圧空
気を流動用空気室内へ供給する空気配管などは省略して
いる。
1 (A) and 1 (B) are one embodiment of the present invention, and are partial front views mainly showing the vicinity of a powder inlet and a dust absorbing duct. The other structures are basically the same as the front view of the prior art shown in FIG. 2, and the powder stored and flowing in the perforated plate, the flowing air chamber, and the closed tank 1 not shown in FIG. And an air pipe for supplying high-pressure air into the air chamber for flow are omitted.

【0014】図1(A)において密閉タンク1は鋼製溶
接構造で製作された断面がほぼ長方形の箱体からなり、
図で表示する上部が粉体流動室5である。密閉タンク1
の頂面11のほぼ中央に円筒体からなる粉体投入口2が
立設され、蓋面21は頂面11よりも高位に固定され、
底面22は密閉タンク内に突出した低位にある。コーン
3はこの円筒体内に囲まれて内包した状態で固定し、頂
点31は頂面11よりは高いが蓋面21よりは若干低位
にある。コーンの円錐面32は下方へ向けて拡径し、粉
体投入口の内周面24との間隔は次第に狭くなるが、最
も狭隘となる粉体投入口の底面22のレベルにおいても
粉体の供給に充分有効な程度の空間を保持した傾斜空間
Eを形成している。
In FIG. 1A, a closed tank 1 is formed of a box having a substantially rectangular cross section made of a steel welded structure.
The upper part shown in the figure is the powder flow chamber 5. Closed tank 1
A powder input port 2 made of a cylindrical body is erected at substantially the center of the top surface 11 of the container, and the lid surface 21 is fixed at a higher position than the top surface 11.
The bottom surface 22 is at a low level protruding into the closed tank. The cone 3 is fixed in a state of being enclosed and enclosed by the cylindrical body, and the vertex 31 is higher than the top surface 11 but slightly lower than the lid surface 21. The diameter of the conical surface 32 of the cone is increased downward, and the distance between the conical surface 32 and the inner peripheral surface 24 of the powder inlet is gradually narrowed. An inclined space E that holds a space that is sufficiently effective for supply is formed.

【0015】密閉タンク1の頂面11上であって粉体投
入口2の外周面を取り囲む形態で環状の吸粉ダクト4が
巻き回され、吸粉ダクトの一端41は頂面11を貫通し
て密閉タンク内と連通すると共に、他端は絞り弁43を
介して集塵機6に接続している。したがって図1のよう
に上蓋23を取り外して粉体投入口2を開口した時点で
は、粉体と共に連行してきた空気は一旦、密閉タンク内
へ進入しても一端41からの負圧に誘導されて他端42
側へ進行し、粉体供給と共に舞上がった粉塵も一緒に開
放状態の絞り弁43を通過して集塵機6を目指して流動
する。これらの気流や粉体の流れの方向を示したのが図
(B)中の矢視である。
An annular dust-absorbing duct 4 is wound on the top surface 11 of the closed tank 1 so as to surround the outer peripheral surface of the powder inlet 2, and one end 41 of the dust-absorbing duct penetrates the top surface 11. And the other end is connected to the dust collector 6 via a throttle valve 43. Therefore, when the upper lid 23 is removed and the powder inlet 2 is opened as shown in FIG. 1, the air entrained with the powder once is guided by the negative pressure from one end 41 even if it enters the closed tank. Other end 42
The dust that has flown to the side and flows along with the powder supply also flows toward the dust collector 6 through the throttle valve 43 in the open state. The direction of the flow of the air or the powder is indicated by arrows in FIG.

【0016】粉体の用途にもよるが、粉体の使用範囲が
拡大され機能材として、または他の液体材料に替えて適
用する例が増加し、そのための品質管理、たとえば粒度
分布の管理が従来よりも一段と厳しく要求されるケース
も目立つ傾向にある。たとえば従来の液状の防食塗料に
代って粉体塗装が主体となっているなど、今後も粉体の
占める技術的価値は増強される一方である。その意味も
あって粉体流動用タンクは業界で注目を集め、従来の粉
体輸送が大量の粉体を取り混ぜて急速に気流と共に輸送
することを原則とするのに対し、粉体流動用タンクでは
一定の条件で粉体を流動化させ、規定に達しない粉体、
たとえば超微粉など品質に悪影響を及ぼす規定外の粉体
は、流動中の粉体から分離して吸粉ダクトを通じて排出
し集塵機に回収させるという品質向上のテクニックも考
えられ、このような利点も活用すれば、さらに本発明の
意義が活かされる。
Although it depends on the use of the powder, the range of use of the powder is expanded and the number of applications where the powder is used as a functional material or in place of another liquid material is increasing. There are cases where even more stringent requirements are required than before. For example, the technical value occupied by powders will continue to increase in the future, as powder coatings are mainly used in place of conventional liquid anticorrosive paints. For that reason, powder flow tanks have attracted attention in the industry.In contrast to conventional powder transport, which is based on the principle that a large amount of powder is mixed and transported quickly with airflow, the powder flow tank is Then, fluidize the powder under certain conditions,
For example, extra-fine powders that have an adverse effect on quality, such as ultrafine powders, can be separated from flowing powders, discharged through a dust-suction duct, and collected by a dust collector. Then, the significance of the present invention is further utilized.

【0017】[0017]

【発明の効果】本発明は以上に述べた通り近年注目を集
めている粉体流動用タンクの大きな課題を解決するもの
であり、粉体流動用タンク内で流動化した粉体が使用と
共に減量し、その消費分を補充するために新たな粉体を
供給するときに舞上がる猛烈な粉塵の外部への流出を防
止し、快適な職場環境を維持する効果がある。また、集
塵機に通じる吸粉ダクトの開閉も特に負担となるほどの
煩瑣な作業を必要とせず、適正な負圧を設定して定常的
に操業し、粉体補充時と定常運転時とを問わず、粉塵の
防止、さらに積極的には粉体の粒度管理などに一役果す
など、メンテナンスと品質向上を兼ねた機能も併せ得ら
れる利点もある。
As described above, the present invention solves a major problem of a powder flowing tank which has been receiving attention in recent years. In addition, there is an effect that the intense dust that rises when supplying new powder to replenish the consumption is prevented from flowing out to the outside, and a comfortable work environment is maintained. In addition, opening and closing of the dust suction duct leading to the dust collector does not require complicated work that is particularly burdensome, and operates at a proper negative pressure and operates steadily. In addition, there is an advantage that a function for both maintenance and quality improvement can be obtained, such as preventing dust and more positively controlling the particle size of the powder.

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

【図1】本発明の実施形態の要部の部分縦断正面図
(A)と、特に空気の流れを矢視によって明らかに示し
た部分縦断正面図(B)である。
FIG. 1 is a partial vertical front view (A) of a main part of an embodiment of the present invention, and a partial vertical front view (B) particularly showing the flow of air clearly by arrows.

【図2】従来技術の全体を示す縦断正面図である。FIG. 2 is a vertical sectional front view showing the entire prior art.

【図3】別の従来技術の全体図(A)、課題を示す部分
縦断正面図(B)、および課題解決手段を示す部分縦断
正面図(C)である。
FIG. 3 is an overall view (A) of another prior art, a partial longitudinal front view (B) showing a problem, and a partial vertical front view (C) showing a means for solving the problem.

【符号の説明】[Explanation of symbols]

1 密閉タンク 2 粉体投入口 3 コーン 4 吸粉ダクト 5 粉体流動室 6 集塵機 11 頂面 21 蓋面 22 底面 23 上蓋 24 内周面 25 外周面 31 頂点 32 円錐面 33 円錐底面 41 一端 42 他端 43 圧力調整弁 E 傾斜空間 DESCRIPTION OF SYMBOLS 1 Closed tank 2 Powder inlet 3 Cone 4 Suction duct 5 Powder flow chamber 6 Dust collector 11 Top surface 21 Cover surface 22 Bottom surface 23 Top cover 24 Inner peripheral surface 25 Outer peripheral surface 31 Apex 32 Conical surface 33 Conical bottom 41 One end 42 Others End 43 Pressure regulating valve E Inclined space

───────────────────────────────────────────────────── フロントページの続き (72)発明者 道浦 吉貞 大阪府大阪市西区北堀江1丁目12番19号 株式会社栗本鐵工所内 (72)発明者 橋本 勇治 大阪府池田市石橋3丁目4番27号 株式 会社コーテム内 (72)発明者 稼農 公也 大阪府池田市石橋3丁目4番27号 株式 会社コーテム内 (56)参考文献 特開 昭56−43130(JP,A) 特開 平8−113369(JP,A) 特開 平7−330080(JP,A) 実開 平5−54531(JP,U) 実開 昭54−18881(JP,U) (58)調査した分野(Int.Cl.7,DB名) B65D 90/00 B65G 53/36 B65G 69/18 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoshisada Michiura 1-12-19 Kitahorie, Nishi-ku, Osaka-shi, Osaka Inside Kurimoto Ironworks Co., Ltd. No. 27 In Cotem Co., Ltd. (72) Inventor Kunya Konomori 3-4-2, Ishibashi, Ikeda-shi, Osaka (56) Reference Co., Ltd. JP-A-56-43130 (JP, A) 113369 (JP, A) JP-A-7-330080 (JP, A) JP-A-5-54531 (JP, U) JP-A-54-18881 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B65D 90/00 B65G 53/36 B65G 69/18

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 粉体Pを貯蔵し流動化して供給する粉体
流動用タンクの頂面に開口し粉体Pを供給する粉体投入
口において、粉体投入口2は密閉タンク1の頂面11よ
り突出して上蓋23を着脱自在に装着する蓋面21と、
密閉タンク1の内部まで突出する底面22よりなる円筒
体で形成し、前記蓋面21より低位置に頂点31を固定
し、該粉体投入口2の内周面24との間に下窄みの傾斜
空間Eを形成する円錐面32を具え、前記底面22より
下方に位置する円錐底面33よりなるコーン3を粉体投
入口2の円筒軸と同心に内設し、さらに前記密閉タンク
1の頂面11上で粉体投入口2の外周面25を囲繞して
密閉タンク1内と連通する一端41を具え、他端42が
前記傾斜空間E内の流速を増加しつつ粉体Pを該タンク
内へ流入させると共に、舞い上がった粉塵を吸引する集
塵機6と開閉自在に繋がる吸粉ダクト4を設けたことを
特徴とする粉体流動用タンクの粉体投入口。
1. A powder supply port for supplying and supplying powder P, which is opened at the top surface of a powder flow tank for storing, fluidizing and supplying the powder P. A lid surface 21 protruding from the surface 11 and detachably mounting the upper lid 23,
It is formed of a cylindrical body having a bottom surface 22 protruding to the inside of the closed tank 1, a vertex 31 is fixed at a position lower than the lid surface 21, and a lower constriction is formed between the powder container 2 and the inner peripheral surface 24. And a cone 3 having a conical bottom surface 33 located below the bottom surface 22 is provided concentrically with the cylindrical axis of the powder inlet 2. It surrounds the outer peripheral surface 25 of the powder inlet 2 on the top surface 11
One end 41 communicating with the inside of the closed tank 1 is provided,
While increasing the flow velocity in the inclined space E, the powder P
A collection that draws the dust that has flown in
A powder inlet for a powder flowing tank, wherein a powder suction duct 4 is provided so as to be openable and closable with a dust machine 6 .
JP06194597A 1997-02-28 1997-02-28 Powder inlet for powder flow tank Expired - Fee Related JP3360003B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06194597A JP3360003B2 (en) 1997-02-28 1997-02-28 Powder inlet for powder flow tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06194597A JP3360003B2 (en) 1997-02-28 1997-02-28 Powder inlet for powder flow tank

Publications (2)

Publication Number Publication Date
JPH10236582A JPH10236582A (en) 1998-09-08
JP3360003B2 true JP3360003B2 (en) 2002-12-24

Family

ID=13185846

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06194597A Expired - Fee Related JP3360003B2 (en) 1997-02-28 1997-02-28 Powder inlet for powder flow tank

Country Status (1)

Country Link
JP (1) JP3360003B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007326352A (en) * 2006-06-09 2007-12-20 Ube Ind Ltd Appliance for preventing separation and truck for processing cement composition
KR101412105B1 (en) * 2012-06-28 2014-06-26 현대제철 주식회사 Appratus for preventing scattering of dust
JP7032200B2 (en) * 2018-03-29 2022-03-08 株式会社日立プラントサービス Local exhaust ventilation
CN108816684B (en) * 2018-06-21 2024-05-10 格力电器(芜湖)有限公司 Device for removing powder on surface of bolt
CN113405951A (en) * 2021-05-07 2021-09-17 安徽省金标准检测研究院有限公司 Sample conveying device applied to dust laser detection

Also Published As

Publication number Publication date
JPH10236582A (en) 1998-09-08

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