JPS5938149B2 - Powder or liquid storage tank - Google Patents
Powder or liquid storage tankInfo
- Publication number
- JPS5938149B2 JPS5938149B2 JP52122605A JP12260577A JPS5938149B2 JP S5938149 B2 JPS5938149 B2 JP S5938149B2 JP 52122605 A JP52122605 A JP 52122605A JP 12260577 A JP12260577 A JP 12260577A JP S5938149 B2 JPS5938149 B2 JP S5938149B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- container
- storage tank
- discharge valve
- supply port
- 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
Links
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- Auxiliary Methods And Devices For Loading And Unloading (AREA)
Description
【発明の詳細な説明】
本発明は時系列に品質的な変化をもつて生産される粉粒
体または液体の物質を一時的に貯溜し、貯溜状態から再
びこれらの物質を取り出す際、上記の時系列的な品質の
バラツキをもつ物体を、バラツキのないように混合して
取り出し、これらの物質の品質変化を均一化するための
混合が促進されるようにした粉粒体または液体の貯溜槽
に関する。[Detailed Description of the Invention] The present invention temporarily stores powder, granular or liquid substances that are produced with quality changes over time, and when these substances are taken out from the storage state, the above-mentioned method is applied. A granular or liquid storage tank that mixes and extracts materials whose quality varies over time without any variation, and promotes mixing to equalize changes in quality of these materials. Regarding.
通常化学工業分野においては、粉粒体や高粘性液体の物
質を多く取り扱うが、これらの物質は種種の化学反応や
熱処理、分級などの操作を経て製造される場合が多い。The chemical industry usually handles many substances in the form of powder, granules, and highly viscous liquids, and these substances are often manufactured through various chemical reactions, heat treatments, classification, and other operations.
したがつてこれらの工程を経て得られる物質の特性は反
応時間、反応温度などの各種条件のバラツキのためその
品質的な特性が経時的に異なつている場合がある。たと
えば合成繊維の一種であるナイロン糸の製造においては
ナイロン樹脂からなる通常チップといわれる粒体を熱溶
融させて口金孔から糸状に押出し、更にこれを延伸して
ナイロン糸とするものである。Therefore, the quality characteristics of the substance obtained through these steps may vary over time due to variations in various conditions such as reaction time and reaction temperature. For example, in the production of nylon thread, which is a type of synthetic fiber, granules made of nylon resin, commonly called chips, are melted under heat and extruded into thread form through a spinneret hole, which is then drawn to form nylon thread.
しかし、同じロッドのチップから製造された糸が常に同
じ編物や織物にまとめて用いられるとは限らない。何故
ならばナイロン糸を使用して織物や編物を製造する場合
、同じロッドの糸が不足し他のロッドの糸を混ぜて使用
したり継ぎ足したりするとロッドのちがいによる品質差
に起因して色差や収縮差による欠陥を生ずることがある
。However, yarns produced from the tips of the same rod are not always used together in the same knitted or woven fabric. This is because when manufacturing woven or knitted fabrics using nylon thread, if there is a shortage of thread from the same rod and the thread from other rods is mixed or spliced, color differences may occur due to quality differences due to the different rods. Defects may occur due to differential shrinkage.
この糸のロッド間のバラツキはチップの品質バラツキに
起因することが多い。第1図は従来から知られている貯
溜槽の構造を示す断面図であり、供給される粉粒体は供
給口2より貯溜槽本体容器1内に投下されると投下地点
を中心として安息角をもつて円錐状に堆積し時系列的な
層が直列にtl、を2、を3、・・・・・・、tnの順
序に配列される。This variation between rods of thread is often caused by variation in the quality of the chips. FIG. 1 is a cross-sectional view showing the structure of a conventionally known storage tank. Time-series layers deposited in a conical shape are arranged in series in the order of tl, 2, 3, . . . , tn.
一方取り出すときもほぼ同じ様にtl、を2、を3、゜
゜゜゜’゜、tnの順序に従つて排出弁3から排出され
るので時系列的に配列したtl、を2、を3、・・・・
・・、trp)層からなる粉粒体の集合をこの層の順序
に関係なく分散させることはできない。これらの欠点を
改善する手段としてチップのロッド間の品質差がないよ
うに既に製造された数ロッドのチップを混合してチップ
のロッド間品質差を少なくすることが実施されていた。
たとえば上記のチップ等粉粒体の場合、この種の品質バ
ラツキを均一化するのに混合すべき粉粒体を一つの容器
に入れ全体を混合撹拌することが行なわれるが、この混
合技術は混合すべき粉粒体を巨大な容器に入れ、該容器
内において空気流や撹拌翼を用いるかあるいは容器自体
を回転または往復動させた状態を20時間以上持続させ
ることにより撹拌混合を促進させている。On the other hand, when taking it out, it is discharged from the discharge valve 3 in the same way as tl, 2, 3, ゜゜゜゜'゜, tn, so tl, arranged in chronological order, is 2, 3, etc.・・・
..., trp) layers cannot be dispersed regardless of the order of the layers. As a means to improve these drawbacks, it has been practiced to mix several rods of chips that have already been manufactured so as to reduce the quality difference between the rods.
For example, in the case of powder and granular materials such as chips mentioned above, in order to equalize this type of quality variation, the powder and granular materials to be mixed are placed in one container and mixed and stirred as a whole. The powder and granules to be mixed are placed in a huge container, and stirring and mixing is promoted by using an air flow or stirring blade in the container, or by rotating or reciprocating the container itself for 20 hours or more. .
しかし、この方法は大きな動力と長時間の運転を必要と
し、しかもこのような長時間の撹拌作用を粉粒体に与え
ると、粉粒体の損傷、粉末化、粉粒体表面の衝撃による
結晶化などを生じ品質土の問題を起すことが少なくない
。上記の如き従来技術の欠陥を補うため容器に貯溜され
ている粉粒体または液状の物質を容器に貯溜したのち取
り出す際、容器に物質を供給したときの時系列とは関係
なく該容器から取り出すようにしたものが特開昭50−
157955号公報に示されており、その特徴は容器中
に高さの異なる多数の管を配置した点にある。However, this method requires large amounts of power and long-time operation, and when such long-term stirring action is applied to the powder, the powder may be damaged, powdered, or crystallized due to impact on the surface of the powder. This often results in problems with the quality of the soil. In order to compensate for the deficiencies of the prior art as described above, when taking out a powder, granular or liquid substance stored in a container after storing it in the container, the substance is taken out from the container regardless of the chronological order in which the substance was supplied to the container. This was published in the 1970s by Japanese Unexamined Patent Publication No.
This is disclosed in Japanese Patent No. 157955, and its feature is that a large number of tubes of different heights are arranged in the container.
この装置は時系列に従つて貯えられた物質を高さのちが
う管口から取り出されるため、どうしても低い位置の管
口から多く排出することはさけられず、管の高さ、位置
の配列がなずかしいし、粉粒体を用いる場合には管と底
部の間にある空間に滞溜しやすいなどの欠陥がさけられ
ない。また粉粒体の場合には排出口の形状、管内の流れ
やすさなどを考慮するとかなり複雑な構造とならざるを
得ない。本発明の目的は上記の如き従来技術の欠陥を改
善し、時系列となして順次貯溜された物質を容器から排
出する際、貯溜時の供給時系列に関係なく内容物を取り
出し、取り出しの過程で混合効果を促進できる新規な粉
粒体もしくは液体の貯溜槽を提供せんとするものである
。Since this device extracts the stored substances from the pipe ports at different heights in chronological order, it is unavoidable to discharge a large amount from the pipe ports located at a lower position, and the height and position of the pipes must be arranged. It is difficult, and when powder or granules are used, defects such as easy accumulation in the space between the tube and the bottom cannot be avoided. In addition, in the case of powder or granules, the structure must be quite complicated considering the shape of the discharge port, ease of flow within the pipe, etc. The purpose of the present invention is to improve the above-mentioned deficiencies of the prior art, and to provide a process for taking out the contents, regardless of the supply time sequence during storage, when discharging substances stored in a time series from a container. It is an object of the present invention to provide a novel powder or liquid storage tank that can promote the mixing effect.
本発明は上記の目的を達成するため、次の如き構成から
なるものである。In order to achieve the above object, the present invention has the following configuration.
静置された容器の内部を、上部を空間部とし、下部を垂
直な隔壁によつて分割することにより上端部が前記空間
部に開口する複数の独立の小室を形成し、該複数の小室
のうちの一個又は一部分のみの上端部に対向するように
該上端部と間隔をおいて供給口を配置し、また前記複数
の全ての小室の底部に、一斉に開放を可能とする排出弁
を設けた粉粒体または液体の貯溜槽を特徴とするもので
ある。The interior of the container that is left still is divided into a space at the top and a vertical partition wall at the bottom to form a plurality of independent small chambers whose top ends open into the space. A supply port is arranged at a distance from the upper end so as to face the upper end of only one or a portion of the chambers, and a discharge valve is provided at the bottom of all of the plurality of small chambers to enable them to be opened all at once. It is characterized by a storage tank for powder, granular material or liquid.
本発明を図面に示す実施態様により更に詳しく説明する
。The present invention will be explained in more detail with reference to embodiments shown in the drawings.
第2図は本発明に係る貯溜槽の構造を説明するための断
面図であり、第3図は第2図のX−X矢視図であり、第
4図は同じくZ−Z矢視図である。FIG. 2 is a sectional view for explaining the structure of the storage tank according to the present invention, FIG. 3 is a view taken along the line X-X in FIG. 2, and FIG. 4 is a view taken along the line Z-Z in FIG. It is.
第5図は第2図に示したA部の拡大図である。第2図に
おいて貯溜槽1は容器1、供給口2、小室排出弁3、漏
斗状排出筒4および一斉排出弁5をその要部としている
。容器1の内部は隔壁Wl,W27W3“゜゛゜゜W0
−1によつて複数の小室Cl,C2・・・・・・COに
分割されている。供給口2は第1番目に配列された小室
C1の上端部と対向し、該小室の断面積内に包含される
面積をもつて該小室の上端部からHの間隔をもつて配置
されており、供給口から供給される物質は先ず小室C1
を満たし順次隔壁Wl,W2を超えてC2,C3・・・
・−・・COを満たして行くが、同時に2つの小室にま
たがつて物質が供給されないように配慮されている。容
器1に満杯となつた粉粒体は小室排出弁3を開くことよ
り自重力落下し該排出弁3を介して容器1に連接された
漏斗状排出筒4内に貯溜された時系列Tl,t2・・・
・・・TOの順序に並列に配列された物質が同時に漏斗
状排出筒内に移動する。漏斗状排出筒4には一斉排出弁
5が設けてあり、これを開くとTl,t2,・・・・・
・,TOの時系列における各粉粒体が一斉に排出される
結果、各時系列の粉粒体がほぼ均等に排出され、貯溜槽
への供給時の時系列とは関係なく貯溜槽内の物質を排出
できる。これらの具体的な手段について更に詳しく述べ
る。FIG. 5 is an enlarged view of section A shown in FIG. 2. In FIG. 2, the storage tank 1 has a container 1, a supply port 2, a small chamber discharge valve 3, a funnel-shaped discharge tube 4, and a simultaneous discharge valve 5 as its main parts. The inside of the container 1 has partition walls Wl, W27W3"゜゛゜゜W0
-1 into a plurality of small chambers Cl, C2...CO. The supply port 2 faces the upper end of the first arranged small chamber C1, and is arranged at a distance of H from the upper end of the small chamber with an area included within the cross-sectional area of the small chamber. , the substance supplied from the supply port first enters the small chamber C1.
C2, C3...
Although the chamber is filled with CO, care is taken not to supply the substance across two chambers at the same time. When the container 1 is full, the powder and granules fall under their own gravity by opening the small chamber discharge valve 3, and are stored in the funnel-shaped discharge tube 4 connected to the container 1 via the discharge valve 3, and the time series Tl, t2...
...The substances arranged in parallel in the order of TO move into the funnel-shaped discharge tube at the same time. The funnel-shaped discharge pipe 4 is provided with a simultaneous discharge valve 5, and when it is opened, Tl, t2,...
・As a result of each powder and granular material in the time series of TO being discharged at the same time, the powder and granules in each time series are discharged almost equally, and the amount of powder in the storage tank is Substances can be discharged. These specific means will be described in more detail.
粉粒体を各小室へ順次分配する具体的な仕方は、第5図
の如く小室C,に供給された粉粒体が満杯になり、さら
に供給を続けると粉粒体の安息角θで生ずる山の傾斜角
αが安息角θより大きくなつたとき次に小室C2へ粉粒
体が入る。同様にC3,・・・・・・,COまで満杯に
なり、複数の小室Cl,C2,C3,・・・・・・,C
nに時系列に従つて粉粒体がTl,t2,t3,・・・
・・・,TOの順に一時的に分配して貯溜される、各小
室の底部には小室排出弁が設けられている。この弁は各
小室が一斉に関くように構成してある。この作動は機械
的、電気的に作動させることができる。本実施例におい
ては長いバタフライバルブのようなもので排出すると漏
斗状排出筒4中に前記した通りに配列する。漏斗状排出
筒にある物質は一斉排出弁5から排出される。本実施例
においては一斉排出弁5をロータリーバルブにしている
が、この弁は排出量を規制する上で使用するのが好まし
いが必ずしも必要ではなく、前記小室排出弁3のみで操
作することもできる。第5図において隔壁W1′W27
W3“0゜゛8゜′Wn−1のピツチPおよび小室Cl
,C2,C3,・・・・・・,Cnの容量は貯溜された
粉粒体がスムーズに流れる間隔であり、貯溜槽の大きさ
と原料の種類、特性に適合するように予め定められた分
割数による。容器の形状および隔壁の形状は第4図の如
く本体容器1の壁に平行にすることもできる。そのとき
供給口2は容器1の中央附近で小室C1上に設ける。隔
壁W1?W2ツW32゛1゜10″?Wn−1の高さは
水平でも良いが、さらに物質の性状によつて流れ方が異
なるので後述するごとくその性状に応じて変えると良い
。粉粒体の場合は第5図の如く小室C2に入るべき粉粒
体が飛散して次の小室C3に入らないよう隔壁W1より
もW2を高くし同じ様にW3からWn−1まで順次高く
するのが好ましい。The specific method of sequentially distributing the powder and granules to each chamber is as shown in Figure 5, when the powder supplied to chamber C becomes full and the supply continues, the repose angle θ of the granules occurs. When the angle of inclination α of the mountain becomes larger than the angle of repose θ, the granular material then enters the small chamber C2. Similarly, C3,...,CO becomes full, and multiple small chambers Cl, C2, C3,...,C
The powder and granules are Tl, t2, t3,... in chronological order in n.
..., TO are temporarily distributed and stored in the order of the cells. A cell discharge valve is provided at the bottom of each cell. This valve is constructed so that each chamber is connected at the same time. This operation can be performed mechanically or electrically. In this embodiment, when the liquid is discharged using something like a long butterfly valve, it is arranged in the funnel-shaped discharge pipe 4 as described above. The substances in the funnel-shaped discharge tube are discharged all at once through the discharge valve 5. In this embodiment, the simultaneous discharge valve 5 is a rotary valve, and although it is preferable to use this valve to regulate the discharge amount, it is not always necessary, and it can also be operated by the small chamber discharge valve 3 alone. . In Fig. 5, partition wall W1'W27
W3 "0゜゛8゜'Wn-1 pitch P and small room Cl
, C2, C3, ......, Cn is the interval at which the stored powder and granules flow smoothly, and is divided in advance to suit the size of the storage tank, the type of raw material, and the characteristics. Depends on the number. The shape of the container and the shape of the partition wall can be made parallel to the wall of the main container 1 as shown in FIG. At this time, the supply port 2 is provided near the center of the container 1 above the small chamber C1. Bulkhead W1? The height of W2゛1゜10''?Wn-1 may be horizontal, but since the flow direction differs depending on the properties of the substance, it is better to change it according to the properties as described later.In the case of powder and granular materials As shown in FIG. 5, it is preferable that W2 is made higher than the partition wall W1, and in the same way, W3 to Wn-1 are made higher in order to prevent the powder and granular material that should enter the small chamber C2 from scattering and entering the next small chamber C3.
小室Cl,C2,C3,・・・・・・,Cnの分割の仕
方と供給口2の位置関係は上記の如く流体が供給される
流体の時系列を乱すことなく順次分配されるように選択
されるものであり、隔壁の間隔、形状および高さは物質
の性状、粘度とか安息角によつて大きく影響をうける。The method of dividing the small chambers Cl, C2, C3, . The spacing, shape, and height of the partition walls are greatly influenced by the properties, viscosity, and angle of repose of the substance.
また第2図において、たとえばナイロンチツプの如き粒
体を使用したとき、このチツプの安息角θは約45をで
ある。Further, in FIG. 2, when particles such as nylon chips are used, the angle of repose θ of the chips is about 45.
したがつて供給口2と隔壁WO−,の高さをHとし、供
給口と隔壁WO−,の水H平長さをLとしたとき、−す
なわちTanθを一定LにするためにはLが長くなつた
ときHを高くする必要がある。Therefore, when the height of the supply port 2 and the partition wall WO-, is H, and the horizontal length of the supply port and the partition wall WO-, is L, in order to make - that is, Tanθ constant L, L must be When the length increases, H must be increased.
また、安息角で生ずる円錐状の山の部分に、この粉体の
時系列Tl,t2,t3,・・・・・・,Tnが堆積し
ていて、これが排出される際、均一分散に多少変化が見
られるが隔壁で区切られた各小室に自重力落下し、ある
程度分散するので、この上部円錐状山の影響は少ない。
この関係で第3図の貯溜槽ストレート部高さをH′とし
たとき、第且2図のHとの割合を〒aで表わし、この比
を1/3以下にすることが好ましいが、1/5程度が最
もよい。In addition, the time series Tl, t2, t3, ......, Tn of this powder is deposited on the conical mountain part that occurs at the angle of repose, and when it is discharged, it is not uniformly dispersed to some extent. Although some changes can be seen, the influence of this upper conical mountain is small because it falls under its own gravity into each chamber separated by a partition wall and is dispersed to some extent.
In this relationship, when the height of the straight part of the storage tank in FIG. 3 is H', the ratio with H in FIG. /5 is best.
第6図は第2図とは異なる貯溜槽を示す断面図であり、
第7図は第6図の側面図である。FIG. 6 is a sectional view showing a storage tank different from FIG. 2,
FIG. 7 is a side view of FIG. 6.
第8図は第6図のB部の拡大図である。FIG. 8 is an enlarged view of section B in FIG. 6.
第6図の実施例は液体に適するように構成したもので容
器1には、供給口2、小室排出弁3,小室排出弁を1本
にまとめるための配管4′,一斉排出弁5が取りつけら
れてある。The embodiment shown in FIG. 6 is constructed to be suitable for liquids, and the container 1 is equipped with a supply port 2, a small chamber discharge valve 3, a pipe 4' for combining the small chamber discharge valves into one, and a simultaneous discharge valve 5. It has been.
貯溜槽本体容器内には隔壁W1ラW2?W3ア1102
Wn−1により小室Cl,C2,C3,・・・・・・,
Cnがある。上記の各小室へ液体を分配する仕方は粉粒
体の場合とほとんど同じで、液体が流れやすく、容易に
供給される時系列の順に分配するために、第8図の如く
隔壁をWlFW27W3CO″″″′?Wn−1の順序
で低くすれば、隔壁が水平のときよりもさらに好ましい
、隔壁を低くする割合は用いる液体の供給速度および粘
度などの特性条件により異なる。第9図,第10図,第
11図は本発明に係る貯溜槽の横断面を例示したもので
これらの実施例においては容器の形状および小室の仕切
り方と供給口の位置関係を表わしたものである。第9図
に示すものは四角形の断面を有する容器の角の位置に供
給口2を設けた態様であつて、隔壁は斜めに取り付ける
のが好ましい。There are partition walls W1 and W2 inside the storage tank main body container. W3a1102
Due to Wn-1, small chambers Cl, C2, C3,...
There is Cn. The method of distributing the liquid to each of the above-mentioned chambers is almost the same as in the case of powder and granules, and in order to distribute the liquid in a chronological order that is easy to flow and is easily supplied, the partition walls are arranged as shown in Figure 8. It is more preferable to lower the partition wall in the order of ``'?Wn-1'' than when the partition wall is horizontal.The rate at which the partition wall is lowered varies depending on the characteristic conditions such as the supply rate and viscosity of the liquid used. Figs. 9 and 10 , FIG. 11 shows a cross section of a storage tank according to the present invention, and in these embodiments, the shape of the container, the partitioning of the small chambers, and the positional relationship of the supply port are shown. What is shown is an embodiment in which the supply port 2 is provided at a corner of a container having a rectangular cross section, and the partition wall is preferably attached diagonally.
流体が矢印Rの方向に流れるよう隔壁の間隔、形状およ
び高さを流体の性質に応じて決定する。第10図に示す
ものは円形の断面を有する容器の中心に供給口2を設け
た態様であつて、隔壁は同心円で、液体が放射状に流れ
るよう隔壁、形状および高さを流体の性質に応じて決め
る。The spacing, shape, and height of the partition walls are determined according to the properties of the fluid so that the fluid flows in the direction of arrow R. The container shown in Fig. 10 has a supply port 2 in the center of a container with a circular cross section, and the partition walls are concentric circles, and the shape and height of the partition walls are adjusted according to the properties of the fluid so that the liquid flows radially. Decide.
第11図に示すものは円形の断面を有する容器を放射状
の隔壁Wl,W2,W3,・・・・・・,WOで区切り
供給口2は小室C1の上に位置するよう設け、流体が矢
印Rの方向に流れるよう隔壁の間隔、形状および高さと
流体の性質を考慮して決めるが、この態様のものは、小
室C1からCOに直接入らないように隔壁WOが高い構
造にする必要がある。In the case shown in FIG. 11, a container having a circular cross section is separated by radial partition walls Wl, W2, W3, ..., WO, and the supply port 2 is located above the small chamber C1, and the fluid is This is determined by considering the spacing, shape, and height of the partition walls and the properties of the fluid so that the flow flows in the direction R. However, in this embodiment, the partition wall WO needs to be structured to be high so that CO does not enter directly from the small chamber C1. .
この他にも容器が多角形のものや容器は円形で隔壁がス
パイラル状のもの等にすることもでき、これらの態様の
もの同一効果を示すこは明らかである。本発明に係る貯
溜槽の容量は流体の量によつて決まるが、通常小さいも
のは10kg程度から大きなものは20t0n程度のも
のにまで適用し得る。In addition, the container may be polygonal, or the container may be circular with spiral partition walls, and it is clear that these embodiments will have the same effect. The capacity of the storage tank according to the present invention is determined by the amount of fluid, but it is generally applicable from a small tank of about 10 kg to a large tank of about 20 tons.
この大きさは通常生産される流体の特性のバラツキを均
一化するに十分な時間内に生産された粉粒体を含む流体
の量を一度に貯溜可能とする大きさであれば良い。本発
明に係る貯溜槽は単に貯溜するだけで該槽に貯溜された
物質を取り出す際に混合がなされるというすぐれた作用
、効果を奏するものである。The size may be such that it is possible to store at one time an amount of fluid containing powder or granules produced within a sufficient period of time to equalize variations in the characteristics of normally produced fluids. The storage tank according to the present invention has an excellent function and effect in that the substances stored in the tank are mixed when taken out by simply storing the substances.
これらの混合作用は貯溜槽の内部を複数の独立の小室に
分割したこと、これらの小室から同時に取り出す構造と
したことに基(ものである。然もこれらのことは何ら余
分の動力も必要とせずに行なわれるものであるし、槽の
大きさも従来のものとほぼ同じ位のものであり特別に床
面積などを要しない。These mixing effects are based on the fact that the inside of the storage tank is divided into a plurality of independent small chambers, and that the liquid is taken out from these small chambers at the same time.However, these things do not require any extra power. The size of the tank is almost the same as the conventional one, so no special floor space is required.
またこの槽の本体部には機械的な可動部がないため保守
、点検に特別な労力を必要としないし、これまでの混合
装置に比べ貯溜槽の数を減らすこともでき、本発明に係
る槽を通過する粉粒体には何らの損傷も生じないという
すぐれた作用効果を奏するものである。In addition, the main body of this tank has no mechanically moving parts, so maintenance and inspection do not require special effort, and the number of storage tanks can be reduced compared to conventional mixing devices. This provides an excellent effect in that no damage is caused to the powder passing through the tank.
第1図は従来公知の貯溜槽を示す断面図である。
第2図は本発明に係る貯溜槽を説明するための断面図で
あり、第3図は第2図のX−X矢視図、第4図は同じく
Z−Z矢視図である。第5図は第2図に示すA部の拡大
図である。第6図は第2図とは異なる本発明の貯溜槽を
示す断面図であり、第7図は第6図の側面図である。第
8図は第6図のB部の拡大図である。第9,10,11
図は本発明に係る貯溜槽の横断面を夫々例示したもので
ある。1:貯溜槽本体容器、2:供給口、3:小室排出
弁、4:漏斗状排出筒、4′:排出配管、5:ー斉排出
弁SWl2W2′W3?11′Wn−1 :隔壁)Cl
,C2,C3,・・・・・・,CO:小室。FIG. 1 is a sectional view showing a conventionally known storage tank. FIG. 2 is a sectional view for explaining the storage tank according to the present invention, FIG. 3 is a view taken along the line X-X in FIG. 2, and FIG. 4 is a view taken along the line Z-Z in FIG. FIG. 5 is an enlarged view of section A shown in FIG. 2. FIG. 6 is a cross-sectional view showing the storage tank of the present invention, which is different from FIG. 2, and FIG. 7 is a side view of FIG. 6. FIG. 8 is an enlarged view of section B in FIG. 6. 9th, 10th, 11th
The figures each illustrate a cross section of a storage tank according to the present invention. 1: Storage tank main container, 2: Supply port, 3: Small chamber discharge valve, 4: Funnel-shaped discharge tube, 4': Discharge piping, 5: - Simultaneous discharge valve SWl2W2'W3?11'Wn-1: Partition wall) Cl
, C2, C3, ..., CO: Komuro.
Claims (1)
を垂直な隔壁によつて分割することにより上端部が前記
空間部に開口する複数の独立の小室を形成し、該複数の
小室のうちの一個又は一部分のみの上端部に対向するよ
うに該上端部と間隔をおいて供給口を配置し、また前記
複数の全ての小室の底部に、一斉に開放を可能とする排
出弁を設けたことを特徴とする粉粒体または液体の貯溜
槽。1 The interior of a container that is left still is divided into a space at the top and a vertical partition wall at the bottom to form a plurality of independent small chambers whose top ends open into the space, and the plurality of small chambers. A supply port is arranged at a distance from the upper end so as to face the upper end of only one or a portion of the chambers, and a discharge valve is provided at the bottom of all of the plurality of small chambers so as to be able to open them all at once. A storage tank for powder, granular material or liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52122605A JPS5938149B2 (en) | 1977-10-13 | 1977-10-13 | Powder or liquid storage tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52122605A JPS5938149B2 (en) | 1977-10-13 | 1977-10-13 | Powder or liquid storage tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5455964A JPS5455964A (en) | 1979-05-04 |
| JPS5938149B2 true JPS5938149B2 (en) | 1984-09-13 |
Family
ID=14840069
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52122605A Expired JPS5938149B2 (en) | 1977-10-13 | 1977-10-13 | Powder or liquid storage tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5938149B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5055183B2 (en) * | 2008-03-31 | 2012-10-24 | 旭有機材工業株式会社 | Method and apparatus for mixing powder particles |
-
1977
- 1977-10-13 JP JP52122605A patent/JPS5938149B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5455964A (en) | 1979-05-04 |
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