JP4045670B2 - Dust discharge chute - Google Patents

Dust discharge chute Download PDF

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Publication number
JP4045670B2
JP4045670B2 JP29465698A JP29465698A JP4045670B2 JP 4045670 B2 JP4045670 B2 JP 4045670B2 JP 29465698 A JP29465698 A JP 29465698A JP 29465698 A JP29465698 A JP 29465698A JP 4045670 B2 JP4045670 B2 JP 4045670B2
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Japan
Prior art keywords
granular material
discharge chute
pipe
inner tube
end opening
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Expired - Fee Related
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JP29465698A
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JP2000110970A (en
Inventor
里行 寺田
裕一 菊地
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Hitachi Plant Technologies Ltd
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Hitachi Plant Technologies Ltd
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  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Rigid Pipes And Flexible Pipes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は粉粒体の排出シュートに係り、特に連続式アンローダ等により高所に搬送した粉粒体を重力で落下させて後段の設備へ払出すための粉粒体の排出シュートに関する。
【0002】
【従来の技術】
連続式アンローダ等により高所に搬送した粉粒体を、排出シュートを介して重力で落下させて後段の設備に払い出す際、排出シュートに投入される粉粒体の流入量が変化する。従って、従来のように単に筒状の排出シュートの場合には流入量が流出量よりも多くなると、粉粒体が排出シュートに詰まってしまう。
【0003】
逆に、流入量が流出量よりも少なくなると、粉粒体が排出シュートの内壁や流出口に衝突するので、排出シュートが傷みやすいという問題がある。即ち、流入量が流出量よりも少ない場合、排出シュート内における粉粒体の流れは外力を加えない限り自由落下が最も速度が大きく、理論上は粒子の終末速度まで到達する。
【0004】
よって、従来この種のシュートでは粉粒体の落下速度を抑えるため、排出シュートを交互に曲げてつないで折曲部を設けたり、排出シュート内に緩衝板を設けたりして粉粒体の落下速度を抑えていた。
【0005】
【発明が解決しようとする課題】
しかしながら、従来の粉粒体の排出シュートでは、粉粒体を排出シュートの折曲部や緩衝板に当てて落下速度を抑える構造でないので、折曲部や緩衝板の損傷が著しく、根本的な解決とはならない。
また、接触部や緩衝板で粉粒体の流れが滞り易くなるので、排出シュート内で粉粒体が詰まる頻度が多くなるという欠点がある。
【0006】
本発明は、このような事情を鑑みてなされたもので、粉粒体の投入量が変動しても粉粒体の詰まりが発生しないと共に、粉粒体の落下衝突による損傷もしにくい粉粒体の排出シュートを提供することを目的とする。
【0007】
【課題を解決するための手段】
本発明は、前記目的を達成するために、下端開口が絞られた内管と外管とで二重管構造に形成され、前記内管の上端開口から粉粒体を投入する排出シュートであって、前記内管と前記外管との間を縦方向に仕切って複数の管路を形成する分割板と、前記形成された複数の管路ごとに高さを変えて前記内管に形成され、前記内管内と前記各管路とを連通する連通口と、を備えたことを特徴とする。
【0008】
本発明によれば、内管の上端開口から投入された粉粒体は、内管の下端が絞られているので内管内に粉粒体の層を形成しながら、内管の下端から排出される。そして、投入される粉粒体の量が増加すると、高さの一番低い位置に形成された連通口から管路内に越流して管路の下端から排出される。この時も、管路の下端が絞られているので粉粒体は管路内に層を形成した状態で排出される。更に、投入される粉粒体が増加すると、次の高さの連通口から管路に越流する。従って、投入された粉粒体は、内管、最初に越流した管路、次に越流した管路の3つから排出され、全て層を形成しながら排出される。これにより、粉粒体の投入量が変動しても粉粒体の詰まりが発生しないと共に、粉粒体の落下衝突による損傷もしにくい。
【0009】
【発明の実施の形態】
以下添付図面に従って、本発明に係わる粉粒体の排出シュートの好ましい実施の形態について詳説する。
図1は、本発明に係る粉粒体の排出シュートの1実施の形態を示す縦断面図である。この粉粒体の排出シュート10は、主として内管12とそれを内包する外管14から二重管構造に形成される。
【0010】
内管12はその上端部には粉粒体を投入する開口16Aを有する上側フランジ16が設けられ、その下端部には粉粒体が排出される開口18Aを有するホッパ部18が設けられる。この内管12の下端開口18Aの開口面積は、内管12の胴体部の径方向の断面積の約1/2になるように絞りこまれている。これにより、下端開口18Aから排出される粉粒体の排出量が規制されるので、内管12の上端開口16Aから投入された粉粒体は、内管12内において層を形成し、この層を維持した状態で下端開口18Aから排出される。
【0011】
内管12と外管14との間には、ドーナッツ状の空間部20が形成されると共に、外管14の上端が内管12側に直角に折曲されて空間部20の上端が閉塞される。また、外管14の下端が内管12側に傾斜して形成されており、空間部20の下端に形成されるリング状の開口20Aの面積が、胴体部における径方向の断面積よりも小さくなるように形成される。そして、排出シュート10の下端には、内管12の下端開口18Aと管路24の下端開口20Aが合流する開口25Aを備えた下側フランジ25が設けられる。
【0012】
内管12と外管14との間に形成された前記空間部20には、縦方向に仕切る複数の分割板22、22が設けられ、空間部20が複数の管路24に分割される。例えば、図2は、空間部20を2つの管路24A、24Bに分割した場合であり、図3は空間部20を4つの管路24A、24B、24C、24Dに分割した場合であるが、以下の説明は、2つの管路24A、24Bの場合である。
【0013】
図1に示すように、内管12には、内管12内と各管路24A、24Bとを連通する連通口26A、26Bがそれぞれ形成される。そして、管路24Aに連通する連通口26Aは内管12の高い位置に形成され、管路24Bに連通する連通口26Bは内管12の低い位置に形成される。また、図1及び図4に示すように、各管路24A、24B内には、前記連通口26A、26Bから各管路24A、24Bの下端開口20Aに至る傾斜板28A、28Bが設けられる。この傾斜板28A、28Bにより、連通口26A、26Bから越流した粉粒体は、傾斜板28A、28B上を滑るように案内されて下端開口20Aに導かれる。
【0014】
また、図5に示すように、内管12に形成された各連通口26A、26Bの下端には、内管12側から管路24A、24Bへ粉粒体を流れ易くするために、斜め上向きの突起板30が突起される。
そして、内管12の下端開口18Aからの粉粒体の排出能力、管路24Aの下端開口20Aからの粉粒体の排出能力、管路24Bの下端開口20Aからの粉粒体の排出能力の合計が、内管12の上端開口16Aから投入される最大投入量よりも大きくなるように設定しておく。
【0015】
次に、上記の如く構成された本発明の粉粒体の排出シュートの作用について説明する。
内管12の上端開口16Aから投入される粉粒体は、内管12の下端開口18Aから排出されるが、内管12の下端開口18Aが絞られているので、内管12内に少しずつ溜まって層を形成する。従って、内管12の上端開口16Aから投入された粉粒体は、粉粒体の層の上に落下した後、この層が移動して下端開口18Aから開口25Aを介して排出する。これにより、内管12の下端開口18Aに粉粒体が衝突しなくなると共に、内管12内に粉粒体の層を形成した状態で下端開口18Aから排出される。この時、下端開口18Aからの排出される粉粒体の排出速度は、粉粒体が自由落下する場合の排出速度の1/3以下にすることができる。従って、排出シュート10の損傷、特に下端開口18Aの損傷が殆どないようにできる。
【0016】
次に、粉粒体の投入量が増加すると、内管12内の粉粒体の層の高さが次第に高くなり、低い位置に形成された連通口26Bから管路24Bに越流する。管路24Bの下端開口20Aは狭く絞られていると共に、管路24B内には傾斜板28Bが設けられているので、排出量が規制される。従って、管路24Bに越流した粉粒体も内管12と同様に管路24B内に層を形成し、この層が移動しながら下端開口20Aから開口25Aを介して排出される。従って、内管12の場合と同様に排出シュートの管路24Bが損傷されにくい。
【0017】
更に、投入する粉粒体が多くなると、内管12の高い位置に形成された連通口26Aからも粉粒体が管路24Aに越流する。この場合にも、前記したと同様に粉粒体が管路24A内に層を形成し、層が移動しながら下端開口20Aから開口25Aを介して排出される。従って、前記したと同様に排出シュート10の管路24Aが損傷しにくい。
【0018】
このように、内管12や管路24A、24B内を粉粒体が層を成して移動しながら排出されるようにしたので、排出シュート10を損傷しにくくできる。また、投入される粉粒体の投入量が少ない場合には内管12だけから排出され、投入量が多くなるに従って、増加した粉粒体の分が連通口26を通って管路24に越流し、内管12と管路24の両方から排出される。従って、投入量の変動があっても排出シュート10が詰まることがない。
【0019】
この場合、投入される粉粒体の投入量の変動の頻度や大きさに応じて、内管12と外管14との間に形成する管路24の数や連通口26の高さを変えるとよい。また、図5に示すように、連通口の下端に設けた突起板30により、内管12側から管路24へ粉粒体が確実に流れやすくなる。
【0020】
【発明の効果】
以上説明したように、本発明の粉粒体の排出シュートによれば、排出シュートを損傷しにくくできる。また、投入量の変動があっても排出シュートが詰まることがない。
【図面の簡単な説明】
【図1】本発明に係る粉粒体の排出シュートの全体を示す縦断面図
【図2】図1におけるA−A線に沿った断面図で、内管と外管との間の空間部を2分割した横断面図
【図3】内管と外管との間の空間部を4分割した場合の横断面図
【図4】案内板を説明する説明図
【図5】本発明に係る粉粒体の排出シュートの連通口に設けた突起板を説明する説明図
【符号の説明】
10…排出シュート
12…内管
14…外管
16A…内管の上端開口(粉粒体の投入口)
18A…内管の下端開口(粉粒体の排出口)
20…空間部
20A…空間部の下端開口(粉粒体の排出口)
22…分割板
24…管路
26…連通口
28…傾斜板
30…突起板
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a discharge chute for a granular material, and more particularly to a discharge chute for a granular material for dropping a granular material conveyed to a high place by a continuous unloader or the like and discharging it to a subsequent facility.
[0002]
[Prior art]
When the granular material conveyed to a high place by a continuous unloader or the like is dropped by gravity through the discharge chute and is discharged to the subsequent equipment, the inflow amount of the granular material charged into the discharge chute changes. Therefore, in the case of a cylindrical discharge chute as in the prior art, if the inflow amount is larger than the outflow amount, the granular material is clogged with the discharge chute.
[0003]
On the contrary, when the inflow amount is smaller than the outflow amount, the powder particles collide with the inner wall or the outlet of the discharge chute, which causes a problem that the discharge chute is easily damaged. That is, when the amount of inflow is smaller than the amount of outflow, the flow rate of the granular material in the discharge chute is the fastest in the free fall unless an external force is applied, and theoretically reaches the end velocity of the particles.
[0004]
Therefore, in this type of chute, in order to suppress the dropping speed of the granular material, the falling chute is dropped by alternately bending and connecting the discharge chute or providing a buffer plate in the discharge chute. I was slowing down.
[0005]
[Problems to be solved by the invention]
However, the conventional discharge chutes of granular material are not structured to suppress the falling speed by applying the granular material to the bent portions of the discharge chute or the buffer plate. It is not a solution.
In addition, since the flow of the powder particles is likely to stagnate at the contact portion or the buffer plate, there is a disadvantage that the frequency of the powder particles being clogged in the discharge chute increases.
[0006]
The present invention has been made in view of such circumstances, and even when the amount of the powder is changed, the powder is not clogged, and is not easily damaged by the drop collision of the powder. The purpose is to provide a discharge chute.
[0007]
[Means for Solving the Problems]
In order to achieve the above object, the present invention is a discharge chute that is formed in a double-pipe structure with an inner tube and an outer tube having a narrowed lower end opening, and in which a granular material is introduced from the upper end opening of the inner tube. The inner pipe and the outer pipe are partitioned in the vertical direction to form a plurality of pipes, and the inner pipes are formed at different heights for each of the formed pipes. And a communication port that communicates the inside of the inner pipe with the pipes.
[0008]
According to the present invention, the granular material introduced from the upper end opening of the inner tube is discharged from the lower end of the inner tube while forming a layer of granular material in the inner tube because the lower end of the inner tube is narrowed. The And if the quantity of the granular material thrown in increases, it will overflow in the pipe line from the communicating port formed in the position with the lowest height, and will be discharged | emitted from the lower end of a pipe line. Also at this time, since the lower end of the pipe is squeezed, the granular material is discharged in a state where a layer is formed in the pipe. Furthermore, when the granular material to be added increases, it overflows from the communication port of the next height to the pipe line. Accordingly, the charged granular material is discharged from the inner pipe, the first overflowed pipeline, and the next overflowed pipeline, and all are discharged while forming a layer. Thereby, even if the input amount of the granular material varies, clogging of the granular material does not occur, and damage due to the falling collision of the granular material is difficult.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of a granular material discharge chute according to the present invention will be described below in detail with reference to the accompanying drawings.
FIG. 1 is a longitudinal sectional view showing an embodiment of a discharge chute for a granular material according to the present invention. The particulate discharge chute 10 is formed in a double tube structure mainly from an inner tube 12 and an outer tube 14 containing the inner tube 12.
[0010]
The inner tube 12 is provided with an upper flange 16 having an opening 16A through which powder particles are introduced at the upper end thereof, and a hopper 18 having an opening 18A through which the powder particles are discharged at the lower end thereof. The opening area of the lower end opening 18 </ b> A of the inner tube 12 is narrowed down to be about ½ of the radial cross-sectional area of the body portion of the inner tube 12. Thereby, since the discharge amount of the granular material discharged from the lower end opening 18A is regulated, the granular material charged from the upper end opening 16A of the inner tube 12 forms a layer in the inner tube 12, and this layer Is discharged from the lower end opening 18A.
[0011]
A donut-shaped space 20 is formed between the inner tube 12 and the outer tube 14, and the upper end of the outer tube 14 is bent at a right angle toward the inner tube 12 to close the upper end of the space 20. The Further, the lower end of the outer tube 14 is formed to be inclined toward the inner tube 12, and the area of the ring-shaped opening 20A formed at the lower end of the space 20 is smaller than the radial cross-sectional area of the body portion. Formed to be. And the lower flange 25 provided with the opening 25A where the lower end opening 18A of the inner pipe 12 and the lower end opening 20A of the pipe line 24 merge is provided at the lower end of the discharge chute 10.
[0012]
The space portion 20 formed between the inner tube 12 and the outer tube 14 is provided with a plurality of dividing plates 22, 22 that are partitioned in the vertical direction, and the space portion 20 is divided into a plurality of pipelines 24. For example, FIG. 2 shows a case where the space part 20 is divided into two pipe lines 24A and 24B, and FIG. 3 shows a case where the space part 20 is divided into four pipe lines 24A, 24B, 24C and 24D. The following description is for the two pipe lines 24A and 24B.
[0013]
As shown in FIG. 1, communication ports 26 </ b> A and 26 </ b> B that connect the inside of the inner tube 12 and the pipe lines 24 </ b> A and 24 </ b> B are formed in the inner tube 12. The communication port 26A communicating with the conduit 24A is formed at a high position of the inner tube 12, and the communication port 26B communicating with the conduit 24B is formed at a low position of the inner tube 12. As shown in FIGS. 1 and 4, inclined plates 28A and 28B extending from the communication ports 26A and 26B to the lower end openings 20A of the pipes 24A and 24B are provided in the pipes 24A and 24B. By the inclined plates 28A and 28B, the powder particles that have overflowed from the communication ports 26A and 26B are guided so as to slide on the inclined plates 28A and 28B and guided to the lower end opening 20A.
[0014]
Further, as shown in FIG. 5, the lower end of each communication port 26A, 26B formed in the inner pipe 12 is inclined upward in order to facilitate the flow of powder from the inner pipe 12 side to the ducts 24A, 24B. The protruding plate 30 is protruded.
And the discharge capacity of the granular material from the lower end opening 18A of the inner pipe 12, the discharge capacity of the granular material from the lower end opening 20A of the pipe line 24A, the discharge capacity of the granular material from the lower end opening 20A of the pipe line 24B. The total is set so as to be larger than the maximum input amount supplied from the upper end opening 16 </ b> A of the inner pipe 12.
[0015]
Next, the action of the discharge chute of the granular material of the present invention configured as described above will be described.
Although the granular material thrown in from the upper end opening 16A of the inner tube 12 is discharged from the lower end opening 18A of the inner tube 12, the lower end opening 18A of the inner tube 12 is narrowed. Accumulate to form a layer. Therefore, after the granular material introduced from the upper end opening 16A of the inner tube 12 falls on the granular material layer, this layer moves and is discharged from the lower end opening 18A through the opening 25A. As a result, the granular material does not collide with the lower end opening 18 </ b> A of the inner tube 12 and is discharged from the lower end opening 18 </ b> A in a state where a layer of granular material is formed in the inner tube 12. At this time, the discharge speed of the powder particles discharged from the lower end opening 18A can be set to 1/3 or less of the discharge speed when the powder particles freely fall. Accordingly, the discharge chute 10 can be hardly damaged, particularly the lower end opening 18A.
[0016]
Next, when the input amount of the granular material is increased, the height of the layer of the granular material in the inner pipe 12 is gradually increased and overflows from the communication port 26B formed at a low position to the pipe line 24B. Since the lower end opening 20A of the pipe line 24B is narrowed down and the inclined plate 28B is provided in the pipe line 24B, the discharge amount is regulated. Therefore, the granular material that has flowed over the conduit 24B also forms a layer in the conduit 24B in the same manner as the inner tube 12, and this layer is discharged from the lower end opening 20A through the opening 25A while moving. Therefore, as in the case of the inner tube 12, the discharge chute conduit 24B is not easily damaged.
[0017]
Further, when the amount of the granular material to be charged increases, the granular material also overflows from the communication port 26A formed at a high position of the inner tube 12 to the conduit 24A. Also in this case, the granular material forms a layer in the conduit 24A as described above, and the layer is discharged from the lower end opening 20A through the opening 25A while moving. Accordingly, the conduit 24A of the discharge chute 10 is not easily damaged as described above.
[0018]
As described above, since the powder particles are discharged while moving in layers in the inner pipe 12 and the pipe lines 24A and 24B, the discharge chute 10 can be hardly damaged. In addition, when the input amount of the granular material to be input is small, the powder is discharged only from the inner pipe 12, and as the input amount increases, the increased amount of the granular material passes through the communication port 26 to the conduit 24. And is discharged from both the inner tube 12 and the conduit 24. Therefore, the discharge chute 10 is not clogged even if the input amount varies.
[0019]
In this case, the number of conduits 24 formed between the inner tube 12 and the outer tube 14 and the height of the communication port 26 are changed in accordance with the frequency and magnitude of variation in the amount of the charged granular material. Good. Further, as shown in FIG. 5, the protruding plate 30 provided at the lower end of the communication port makes it easy for the granular material to easily flow from the inner tube 12 side to the conduit 24.
[0020]
【The invention's effect】
As described above, according to the discharge chute of the granular material of the present invention, the discharge chute can be hardly damaged. Further, the discharge chute is not clogged even if the input amount varies.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view showing an entire discharge chute of a granular material according to the present invention. FIG. 2 is a sectional view taken along line AA in FIG. 1, and a space portion between an inner tube and an outer tube. FIG. 3 is a cross-sectional view of the space between the inner tube and the outer tube divided into four. FIG. 4 is an explanatory view for explaining the guide plate. Explanatory drawing explaining the projection plate provided at the communication port of the discharge chute of powder
DESCRIPTION OF SYMBOLS 10 ... Discharge chute 12 ... Inner pipe | tube 14 ... Outer pipe | tube 16A ... Upper end opening of an inner pipe | tube (injection port of a granular material)
18A ... Lower end opening of inner pipe (powder outlet)
20 ... Space 20A ... Lower end opening of space (powder outlet)
22 ... Split plate 24 ... Pipe line 26 ... Communication port 28 ... Inclined plate 30 ... Projection plate

Claims (2)

下端開口が絞られた内管と外管とで二重管構造に形成され、前記内管の上端開口から粉粒体を投入する排出シュートであって、
前記内管と前記外管との間を縦方向に仕切って複数の管路を形成する分割板と、
前記形成された複数の管路ごとに高さを変えて前記内管に形成され、前記内管内と前記各管路とを連通する連通口と、を備えたことを特徴とする粉粒体の排出シュート。
A discharge chute that is formed into a double tube structure with an inner tube and an outer tube with a narrowed lower end opening, and that throws in powder from the upper end opening of the inner tube,
A dividing plate that vertically partitions between the inner pipe and the outer pipe to form a plurality of pipelines;
A granular material comprising: a communication port formed in the inner pipe by changing the height for each of the plurality of formed pipe lines, and communicating with the inside of the inner pipe and each of the pipe lines. Discharge chute.
前記管路内には、前記開口から前記管路の下端開口に至る傾斜板を設けたことを特徴とする請求項1の粉粒体の排出シュート。  The discharge chute for the granular material according to claim 1, wherein an inclined plate extending from the opening to the lower end opening of the pipe is provided in the pipe.
JP29465698A 1998-10-01 1998-10-01 Dust discharge chute Expired - Fee Related JP4045670B2 (en)

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JP4045670B2 true JP4045670B2 (en) 2008-02-13

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FR2872497B1 (en) * 2004-07-02 2007-11-30 Total France Sa DEVICE AND METHOD FOR LOADING AN ENCLOSURE WITH A DIVIDED SOLID COMPRISING A HOLLOW ROTATION TREE
FR3083527B1 (en) 2018-07-04 2022-09-02 Crealyst Group COMPENSATED FLOW FILLING SYSTEM

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