JPH0454971Y2 - - Google Patents

Info

Publication number
JPH0454971Y2
JPH0454971Y2 JP1987155772U JP15577287U JPH0454971Y2 JP H0454971 Y2 JPH0454971 Y2 JP H0454971Y2 JP 1987155772 U JP1987155772 U JP 1987155772U JP 15577287 U JP15577287 U JP 15577287U JP H0454971 Y2 JPH0454971 Y2 JP H0454971Y2
Authority
JP
Japan
Prior art keywords
pressure
valve
tank
piping
powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1987155772U
Other languages
Japanese (ja)
Other versions
JPH0162221U (en
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 filed Critical
Priority to JP1987155772U priority Critical patent/JPH0454971Y2/ja
Publication of JPH0162221U publication Critical patent/JPH0162221U/ja
Application granted granted Critical
Publication of JPH0454971Y2 publication Critical patent/JPH0454971Y2/ja
Expired legal-status Critical Current

Links

Landscapes

  • Air Transport Of Granular Materials (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は空気輸送装置用加圧タンクに係り、特
に加圧タンクを上下二段に重ねて、粉粒体を連続
的に空気輸送するのに好適な空気輸送装置用加圧
タンクに関する。
[Detailed description of the invention] [Industrial application field] The present invention relates to a pressurized tank for a pneumatic transport device, and in particular, it is a method for continuously pneumatically transporting powder and granular materials by stacking pressure tanks in two layers (upper and lower). The present invention relates to a pressurized tank for a pneumatic transportation device suitable for use in a pressurized tank.

〔従来の技術〕 粉粒体が入つたタンクを圧縮空気で加圧して圧
送する空気輸送装置は種々ある。しかし連続的に
粉粒体を受入れて輸送するのには、加圧タンクを
上、下二段に重ね、上部加圧タンクが粉粒体受入
中でも、下部加圧タンクにより輸送を継続する必
要がある。
[Prior Art] There are various pneumatic transport devices that pressurize a tank containing powder with compressed air and forcefully transport the powder. However, in order to continuously receive and transport powder and granules, it is necessary to stack pressurized tanks in two layers, upper and lower, so that even if the upper pressurized tank is receiving powder and granules, the lower pressurized tank can continue transporting the particles. be.

低速高濃度の空気輸送装置では一般の圧送式空
気輸送装置に比較して使用空気圧力が2〜3倍高
い。従がつて上部加圧タンク内の粉粒体を下部加
圧タンク内に供給する再、下部加圧タンク内の圧
力が高いため上部加圧タンク内に向つて空気の吹
き上がり現象が発生する。同様にホツパー内から
上部加圧タンク内に粉粒体を受け入れる際にも上
部加圧タンク内の圧力が高いためホツパー内に向
つて空気の吹き上がり現象が発生する。従がつて
これら空気の吹き上がり現象により粉粒体の供給
又は受け入れが円滑にできないことがある。
In low-speed, high-concentration pneumatic transportation devices, the air pressure used is two to three times higher than in general pressure-feeding pneumatic transportation devices. Therefore, when the powder in the upper pressurized tank is supplied to the lower pressurized tank, air blows up toward the upper pressurized tank because the pressure in the lower pressurized tank is high. Similarly, when receiving powder from the hopper into the upper pressurized tank, air blows up into the hopper due to the high pressure in the upper pressurized tank. Therefore, due to this phenomenon of air blowing up, it may not be possible to smoothly supply or receive the powder or granular material.

そこで上部加圧タンクと下部加圧タンクに粉粒
体の供給、受け入れ口とは別の接続口を設け、こ
れら両接続口間を均圧配管で連絡して、上部加圧
タンク内から下部加圧タンク内へ粉粒体を供給す
る時には、均圧弁を開として上下部加圧タンク内
を同一圧力とする。又上部加圧タンクには排気配
管を設け、ホツパー内から上部加圧タンク内へ粉
粒体を受け入れる時には、排気弁を開として上部
加圧タンク内を大気圧とする。しかし、特に排気
配管を利用して上部加圧タンク内を大気圧にする
時には上部加圧タンク内の粉粒体を含んだ空気が
排気弁を通過する際排気弁の弁座等に詰まつて動
作不良を惹起し、安定した長時間連続運転をする
のに支障があつた。また、粉粒体が充填された上
部加圧タンクを再度下部加圧タンクと同一圧力に
する場合に、下部加圧タンクから均圧配管を介し
て排気弁に向つて空気が吹き上がり、含有された
粉粒体が同様に排気弁を詰らせるおそれもあつ
た。したがつて、排気弁の直前にフイルターを取
り付ければよいが、粉粒体の回収が極めて困難で
あり、頻繁にメンテナンスを行わなければならな
いという煩雑さがあつたものである。
Therefore, a connection port separate from the powder supply and reception port is provided in the upper pressurized tank and the lower pressurized tank, and a pressure equalization piping is used to connect these two connection ports. When supplying powder into the pressure tank, the pressure equalization valve is opened to maintain the same pressure in the upper and lower pressure tanks. Further, the upper pressurized tank is provided with an exhaust pipe, and when receiving powder from the hopper into the upper pressurized tank, the exhaust valve is opened to bring the inside of the upper pressurized tank to atmospheric pressure. However, especially when using the exhaust piping to bring the inside of the upper pressurized tank to atmospheric pressure, the air containing powder inside the upper pressurized tank may clog the valve seat of the exhaust valve as it passes through the exhaust valve. This caused malfunctions and hindered stable, long-term continuous operation. In addition, when the upper pressurized tank filled with powder and granules is brought to the same pressure as the lower pressurized tank again, air blows up from the lower pressurized tank toward the exhaust valve via the pressure equalization piping, causing the air to be removed. There was also a risk that the powder and granules could clog the exhaust valve. Therefore, although a filter may be installed just before the exhaust valve, it is extremely difficult to collect the powder and requires frequent maintenance, which is complicated.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

本考案は従来技術の欠点を解消して、排気配管
途中に設けた排気弁に粉粒体が詰まることのない
ような空気輸送装置用加圧タンクを提供するにあ
る。
The present invention eliminates the drawbacks of the prior art and provides a pressurized tank for a pneumatic transport device that prevents powder from clogging an exhaust valve provided in the middle of an exhaust pipe.

〔問題点を解決するための手段〕[Means for solving problems]

本考案に係る空気輸送装置用加圧タンクは、上
部の粉粒体受入口に受入弁を設けた加圧タンクを
上下二段に重ね、上下部加圧タンク間を連絡する
均圧配管と、均圧配管途中に設けた均圧弁と、均
圧弁と上部加圧タンク接続口間の均圧配管途中か
ら分岐して排気弁を有する排気配管と、均圧弁と
上部加圧タンク接続口間の均圧配管途中から分岐
して排気弁を有する排気配管と、均圧弁と下部加
圧タンク接続口間の均圧配管途中に接続して給気
弁を有する前記給気配管より成る空気輸送装置用
加圧タンクにおいて、前記上部および下部加圧タ
ンクに対する前記均圧配管の両接続口にフイルタ
ーを設けるとともに、当該フイルターはフイルタ
ーエレメントより下位のタンク側のケーシング内
面形状が逆円錐ホツパーとされ、粉粒体の自重落
下によるタンク内への回収を可能としていること
を特徴とするものである。
The pressurized tank for a pneumatic transportation device according to the present invention has two stacked pressurized tanks each having a reception valve at the upper part of the powder receiving port, and includes pressure equalization piping that connects the upper and lower pressurized tanks. A pressure equalizing valve installed in the middle of the pressure equalizing pipe, an exhaust pipe branching from the middle of the pressure equalizing pipe between the pressure equalizing valve and the upper pressurizing tank connection port and having an exhaust valve, and an equalizing valve installed between the pressure equalizing valve and the upper pressurizing tank connecting port. A pressurizer for a pneumatic transport device comprising an exhaust pipe branching from the middle of the pressure pipe and having an exhaust valve, and the air supply pipe having an air supply valve connected to the pressure equalizing pipe midway between the pressure equalizing valve and the lower pressurizing tank connection port. In the pressure tank, filters are provided at both connection ports of the pressure equalization piping to the upper and lower pressure tanks, and the inner surface of the casing on the tank side below the filter element is an inverted conical hopper. It is characterized by being able to be recovered into the tank by falling under its own weight.

〔作用〕[Effect]

上記構成によれば、上下加圧タンクを接続する
均圧配管の各接続口にフイルターが設けられてい
るので、粉粒体補充のために上部加圧タンクを圧
力を抜く排気操作時に粉粒体がフイルターに補足
され、排気管内への侵入を防止できる。また、補
充後に再加圧のために均圧弁を開放して給気配管
から給気を行うことにより両タンク内圧を均等に
するが、下部加圧タンクと上部加圧タンクの圧力
差がなくなるまでの間に、均圧配管を通じて圧力
空気が上部加圧タンクに逆流する可能性がある。
しかし均圧配管と下部加圧タンクの接続口にはフ
イルターが設けられているので、粉粒体が逆流す
ることは有効に防止される。そして、上下加圧タ
ンクに対する均圧管の接続口に設けられた各フイ
ルターは、フイルターエレメントより下位のケー
シングが逆円錐ホツパーとされているので、エレ
メントにより阻止された粉粒体は自重により各タ
ンク内に自動的に回収されるものとなり、回収効
果が高いものとなり、輸送する粉粒体を他所に逃
すことなく輸送できるのである。特に、再加圧空
気の供給によるフイルター逆洗機能と相俟つてフ
イルター部分への粉粒体の残留がなく、したがつ
てメンテナンスも容易となつている。
According to the above configuration, a filter is provided at each connection port of the pressure equalization piping that connects the upper and lower pressurized tanks, so when the upper pressurized tank is depressurized in order to replenish the powder and granules, the powder and granules are removed. is captured by the filter to prevent it from entering the exhaust pipe. In addition, after refilling, the pressure equalization valve is opened for repressurization and air is supplied from the air supply piping to equalize the internal pressure of both tanks, but until the pressure difference between the lower pressurized tank and the upper pressurized tank disappears. During this time, pressurized air may flow back into the upper pressurized tank through the pressure equalization piping.
However, since a filter is provided at the connection port between the pressure equalization pipe and the lower pressure tank, backflow of powder and granules is effectively prevented. Each filter installed at the connection port of the pressure equalizing pipe to the upper and lower pressurized tanks has an inverted conical hopper in its casing below the filter element, so the powder and granules blocked by the element are transported inside each tank by their own weight. This means that the powder and granules can be transported automatically without being lost to other locations. In particular, in combination with the filter backwashing function by supplying re-pressurized air, there is no residual powder on the filter, and therefore maintenance is easy.

〔実施例〕〔Example〕

以下図面を参照して本考案の一実施例の説明を
する。第1図は本考案の一実施例を示す全体構成
図である。本実施例による空気輸送装置の構成
は、頂部に粉粒体10の供給ホツパー13があ
り、この下部に一次受入弁14を有して粉粒体1
0を受入れる上部加圧タンク12と、さらにこの
下部に二次受入弁15を有して粉粒体10を圧送
する下部加圧タンク11がある。下部加圧タンク
11の下部は輸送管22に接続され粉粒体10は
貯槽23へ輸送される。均圧配管28は上部加圧
タンク12の接続口31と下部加圧タンク11の
接続口30の間を連絡して途中に均圧弁18を有
する。排気配管29は上記均圧配管28の途中よ
り分岐して途中に排気弁19を有する。給気配管
27はコンプレツサー24により圧縮空気を発生
し、エアーレシーバー25、エアーフイルター2
6を経て、加給弁17を経由して上記下部加圧タ
ンク11下部の輸送管22に、および給気弁16
を経由して上記均圧配管28途中にそれぞれ接続
してある。
An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is an overall configuration diagram showing an embodiment of the present invention. The configuration of the pneumatic transport device according to this embodiment is that there is a supply hopper 13 for the powder and granular material 10 at the top, and a primary receiving valve 14 at the lower part of the supply hopper for the powder and granular material 10.
There is an upper pressurized tank 12 that receives 0, and a lower pressurized tank 11 that has a secondary receiving valve 15 below the tank 12 and pumps the powder 10. The lower part of the lower pressurized tank 11 is connected to a transport pipe 22 and the granular material 10 is transported to a storage tank 23. The pressure equalization pipe 28 communicates between the connection port 31 of the upper pressure tank 12 and the connection port 30 of the lower pressure tank 11, and has a pressure equalization valve 18 in the middle. The exhaust pipe 29 branches from the middle of the pressure equalizing pipe 28 and has an exhaust valve 19 in the middle. The air supply pipe 27 generates compressed air by a compressor 24, and is connected to an air receiver 25 and an air filter 2.
6, to the transport pipe 22 at the bottom of the lower pressurized tank 11 via the booster valve 17, and to the air supply valve 16.
The pressure equalizing pipes 28 are connected to each other midway through the pressure equalizing pipes 28.

本考案のポイントであるフイルター20は上記
の上部加圧タンク12の均圧配管28の接続口3
1に取り付けてある。
The filter 20, which is the key point of the present invention, is the connection port 3 of the pressure equalization pipe 28 of the upper pressurized tank 12.
It is attached to 1.

以上の構成による本装置の運転手順を次に説明
する。
The operating procedure of this device with the above configuration will be explained next.

粉粒体10は供給ホツパー13に入つており、
まず一次受入弁14を開くと、上部加圧タンク1
2内に粉粒体10が入り、満杯になると一次受入
弁14を閉じる。このとき二次受入弁15は閉じ
ている。この段階で上部加圧タンク12内の圧力
は大気圧である。このまゝで二次受入弁15を開
くと下部加圧タンク11内の空気圧力による吹き
上がり現象が発生してしまうので、均圧弁18を
開いて給気配管27内の圧縮空気を上部加圧タン
ク12内に流入させて、下部加圧タンク11内と
同一圧力にする。この状態で二次受入弁15を開
くと、上部加圧タンク12内の粉粒体10は下部
加圧タンク11内へ吹き上ることなく落下流入す
る。このとき給気配管27内の圧縮空気は給気弁
16および加給弁17が常時開状態のため下部加
圧タンク11内と輸送管22内に供給され、下部
加圧タンク11内の粉粒体10は輸送管22内へ
押し出されて、貯槽23へ空気輸送される。上部
加圧タンク12内が空になれば二次受入弁15と
均圧弁18を閉じ、排気弁19を開く。そうする
と下部加圧タンク11内と同一な圧力を保持して
いた上部加圧タンク12内の空気は排気配管29
を経て、大気中に放出される。その結果上部加圧
タンク12内の圧力は大気圧となり、再び一次受
入弁14を開いて、供給ホツパー13から粉粒体
10を上部加圧タンク12内へ吹き上がることな
く落下流入することができる。
The granular material 10 is in the supply hopper 13,
First, when the primary receiving valve 14 is opened, the upper pressurized tank 1
Powder 10 enters the chamber 2, and when it is full, the primary receiving valve 14 is closed. At this time, the secondary receiving valve 15 is closed. At this stage, the pressure inside the upper pressurized tank 12 is atmospheric pressure. If the secondary intake valve 15 is opened in this state, a blow-up phenomenon will occur due to the air pressure in the lower pressure tank 11, so open the pressure equalization valve 18 to pressurize the compressed air in the air supply pipe 27 to the upper part. It is made to flow into the tank 12 to make it have the same pressure as the inside of the lower pressurized tank 11. When the secondary receiving valve 15 is opened in this state, the powder 10 in the upper pressurized tank 12 falls into the lower pressurized tank 11 without blowing up. At this time, the compressed air in the air supply pipe 27 is supplied to the lower pressure tank 11 and the transport pipe 22 because the air supply valve 16 and the booster valve 17 are always open, and the powder and granules in the lower pressure tank 11 are 10 is pushed into the transport pipe 22 and pneumatically transported to the storage tank 23. When the upper pressurized tank 12 is empty, the secondary intake valve 15 and pressure equalization valve 18 are closed, and the exhaust valve 19 is opened. Then, the air in the upper pressurized tank 12, which had maintained the same pressure as that in the lower pressurized tank 11, is removed from the exhaust pipe 29.
It is then released into the atmosphere. As a result, the pressure inside the upper pressurized tank 12 becomes atmospheric pressure, and the primary receiving valve 14 is opened again, allowing the powder and granular material 10 to fall into the upper pressurized tank 12 from the supply hopper 13 without being blown up. .

以上の操作手順をくり返すことで粉粒体10を
連続的に受入れ、輸送することができる。
By repeating the above operating procedure, the powder and granular material 10 can be continuously received and transported.

上記排気操作時に排気配管29内に上部加圧タ
ンク12内の粉粒体10が空気流に同伴して侵入
し排気弁19の弁座等に詰まつて排気弁19の開
閉動作不良を発生せぬよう上部加圧タンク12の
均圧配管28の接続口31にフイルター20が取
り付けてある。これにより粉粒体10はフイルタ
ー20に捕捉されて、排気弁19部まで流入しな
い。
During the above exhaust operation, the particulate matter 10 in the upper pressurized tank 12 enters the exhaust pipe 29 along with the air flow and clogs the valve seat of the exhaust valve 19, causing malfunction of opening and closing of the exhaust valve 19. A filter 20 is attached to the connection port 31 of the pressure equalization pipe 28 of the upper pressurized tank 12. As a result, the powder 10 is captured by the filter 20 and does not flow into the exhaust valve 19.

フイルター20に捕捉された粉粒体10は均圧
操作時の空気流aが排気操作時の空気流bと反対
方向のため逆洗され、フイルター20の過効率
が低下することはない。
The powder 10 captured by the filter 20 is backwashed because the air flow a during the pressure equalization operation is in the opposite direction to the air flow b during the exhaust operation, and the overefficiency of the filter 20 does not decrease.

以上説明したように本実施例によれば上部加圧
タンク12の均圧配管28の接続口31にフイル
ター20を設けたことにより排気弁19に上部加
圧タンク12内の粉粒体10が空気流に同伴して
侵入することがなくなり、その結果排気弁19の
弁座等に粉粒体10が詰まることがなくなる。
As explained above, according to this embodiment, the filter 20 is provided at the connection port 31 of the pressure equalizing pipe 28 of the upper pressurized tank 12, so that the powder and granular material 10 in the upper pressurized tank 12 is air-filled by the exhaust valve 19. The powder particles 10 do not enter along with the flow, and as a result, the valve seat of the exhaust valve 19 and the like are prevented from being clogged with the powder particles 10.

従がつて空気輸送装置の長時間の連続運転の安
定化が図れる。
Accordingly, long-term continuous operation of the pneumatic transport device can be stabilized.

なお本実施例では均圧操作時の空気流が第1図
に示す矢印cとなることも万が一考えられるの
で、下部加圧タンク11の均圧配管28の接続口
30にもフイルター21を設けている。このフイ
ルター21も輸送時の給気配管27からの空気流
dにより逆洗される。
In this embodiment, since it is conceivable that the air flow during the pressure equalization operation will be as shown by the arrow c shown in FIG. There is. This filter 21 is also backwashed by the air flow d from the air supply pipe 27 during transportation.

第2図は本考案に係るフイルターの断面図で、
フイルターエレメント38は上部の円筒形カバー
35と下部の逆円錐ホツパー形のケーシング36
にOリング37を介してシールし挾み込んであ
る。カバー35とケーシング36の固定は図示し
ていない緊縮専用バンドで固定できるようになつ
ている。粉粒体10を含んだ空気は矢印eのよう
に流れる。従つて捕捉された粉粒体10はフイル
ターエレメント38の下部に付着する。付着した
粉粒体10は均圧空気流fにより逆洗される。本
実施例によるフイルターはケーシング36を逆円
錐ホツパー形としたことにより、フイルターエレ
メント30の過面積を広くできると共に逆洗し
た粉粒体10がケーシング36の内壁39に沿つ
て滞留することなく上部加圧タンク12内に落下
することができ、フイルター効果を高めることが
できる。
Figure 2 is a cross-sectional view of the filter according to the present invention.
The filter element 38 has an upper cylindrical cover 35 and a lower inverted conical hopper-shaped casing 36.
It is sealed and inserted through an O-ring 37. The cover 35 and the casing 36 can be fixed with a tightening band (not shown). Air containing the granular material 10 flows as shown by arrow e. Therefore, the captured powder 10 adheres to the lower part of the filter element 38. The adhered powder 10 is backwashed by the equal pressure air flow f. In the filter according to this embodiment, by making the casing 36 into an inverted conical hopper shape, the overarea of the filter element 30 can be increased, and the backwashed powder 10 can be prevented from accumulating along the inner wall 39 of the casing 36, and the upper part can be removed. It can be dropped into the pressure tank 12 and the filter effect can be enhanced.

〔考案の効果〕[Effect of idea]

本考案によれば、上部および下部加圧タンクに
対する前記均圧配管の両接続口にフイルターを設
けるとともに、当該フイルターはフイルターエレ
メントより下位のタンク側のケーシング内面形状
が逆円錐ホツパーとされ、粉粒体の自重落下によ
るタンク内への回収を可能とした構成としたの
で、均圧配管を通じて上下加圧タンク間および上
部加圧タンクからの空気吹き上がりに伴う粉粒体
の流出を有効に防止して排気弁の粉塵による詰り
をなくすることができるとともに、各フイルター
で阻止される粉粒体を加圧タンク内に自動回収さ
せることができるので、回収効率の向上とメンテ
ナンス作業性の向上を図りつつ、排気弁の動作が
円滑化すると共に、上下部加圧タンク内の均圧時
に逆洗もされて空気輸送装置の長時間連続運転の
安定化が図れる。
According to the present invention, filters are provided at both connection ports of the pressure equalizing pipe to the upper and lower pressurized tanks, and the inner surface of the casing on the tank side below the filter element is an inverted conical hopper, and the powder particles The structure allows collection into the tank by falling under the body's own weight, which effectively prevents powder and granules from flowing out due to air blowing up between the upper and lower pressurized tanks and from the upper pressurized tank through pressure equalization piping. This eliminates clogging of the exhaust valve due to dust, and the powder and granules blocked by each filter can be automatically collected into the pressurized tank, improving collection efficiency and maintenance workability. At the same time, the operation of the exhaust valve becomes smoother, and backwashing is also performed when the pressure in the upper and lower pressurized tanks is equalized, thereby stabilizing the long-term continuous operation of the pneumatic transportation device.

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

第1図は本考案の一実施例を示す全体構成図、
第2図は本考案に係るフイルターの断面図であ
る。 10……粉粒体、11……下部加圧タンク、1
2……上部加圧タンク、14……一次受入弁、1
5……二次受入弁、16……給気弁、17……加
給弁、18……均圧弁、19……排気弁、20…
…フイルター、22……輸送管、24……コンプ
レツサー、27……給気配管、28……均圧配
管、29……排気配管、a……均圧空気流、b…
…排気空気流。
FIG. 1 is an overall configuration diagram showing an embodiment of the present invention;
FIG. 2 is a sectional view of a filter according to the present invention. 10... Powder, 11... Lower pressurized tank, 1
2... Upper pressurized tank, 14... Primary receiving valve, 1
5... Secondary intake valve, 16... Air supply valve, 17... Boosting valve, 18... Pressure equalization valve, 19... Exhaust valve, 20...
...filter, 22...transport pipe, 24...compressor, 27...air supply piping, 28...equalizing pressure piping, 29...exhaust piping, a...equalizing air flow, b...
...exhaust air flow.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 上部の粉粒体受入口に受入弁を設けた加圧タン
クを上下二段に重ね、上下部加圧タンク間を連絡
する均圧配管と、均圧配管途中に設けた均圧弁
と、均圧弁と上部加圧タンク接続口間の均圧配管
途中から分岐して排気弁を有する排気配管と、均
圧弁と上部加圧タンク接続口間の均圧配管途中か
ら分岐して排気弁を有する排気配管と、均圧弁と
下部加圧タンク接続口間の均圧配管途中に接続し
て給気弁を有する前記給気配管より成る空気輸送
装置用加圧タンクにおいて、前記上部および下部
加圧タンクに対する前記均圧配管の両接続口にフ
イルターを設けるとともに、当該フイルターはフ
イルターエレメントより下位のタンク側のケーシ
ング内面形状が逆円錐ホツパーとされ、粉粒体の
自重落下によるタンク内への回収を可能としてい
ることを特徴とする空気輸送装置用加圧タンク。
Pressurized tanks with receiving valves installed at the upper powder/granular material receiving ports are stacked in upper and lower layers, and pressure equalizing piping connects the upper and lower pressurizing tanks, a pressure equalizing valve installed in the middle of the pressure equalizing piping, and a pressure equalizing valve. Exhaust piping with an exhaust valve that branches off from the middle of the pressure equalization piping between the pressure equalization valve and the upper pressurized tank connection port; and Exhaust piping that has an exhaust valve that branches off from the middle of the pressure equalization piping between the pressure equalization valve and the upper pressure tank connection port. and a pressurized tank for a pneumatic transport device comprising the air supply pipe having an air supply valve connected in the middle of the pressure equalization pipe between the pressure equalization valve and the lower pressure tank connection port, wherein Filters are installed at both connection ports of the pressure equalization piping, and the inner surface of the casing on the tank side below the filter element is an inverted conical hopper, making it possible to collect powder and granules into the tank by falling under their own weight. A pressurized tank for pneumatic transportation equipment, characterized by:
JP1987155772U 1987-10-12 1987-10-12 Expired JPH0454971Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987155772U JPH0454971Y2 (en) 1987-10-12 1987-10-12

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987155772U JPH0454971Y2 (en) 1987-10-12 1987-10-12

Publications (2)

Publication Number Publication Date
JPH0162221U JPH0162221U (en) 1989-04-20
JPH0454971Y2 true JPH0454971Y2 (en) 1992-12-24

Family

ID=31433694

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987155772U Expired JPH0454971Y2 (en) 1987-10-12 1987-10-12

Country Status (1)

Country Link
JP (1) JPH0454971Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5027283A (en) * 1973-06-05 1975-03-20

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5027283A (en) * 1973-06-05 1975-03-20

Also Published As

Publication number Publication date
JPH0162221U (en) 1989-04-20

Similar Documents

Publication Publication Date Title
DE60128381T2 (en) SYSTEN AND METHOD FOR UNLOADING BULK TANK FILLED WITH POWDER PRODUCT
CA1101380A (en) Constant vacuum barge unloading system
JP2003502242A5 (en)
US4362442A (en) Venturi barge unloading system
GB2089330A (en) Discharging storage containers
US20050269365A1 (en) System for pneumatically conveying bulk materials with improved discharge arrangement
JPS61211226A (en) Material shifter
CN202935945U (en) Positive-negative pressure combination type pneumatic conveying device for dense-phase powder materials
CS206656B1 (en) Apparatus for conversion of pulverized or powder containing rigid substances into system of higher pressure
CN108067025A (en) A kind of device for filtering impurities and filter method with automatic backwash
JPH0454971Y2 (en)
JPS58212526A (en) Pneumatic transportation apparatus
US20110048541A1 (en) Vacuum Saturation Technique for Porous Aggregate Material
US4734110A (en) Method and apparatus for removing solids from pressurized process system
CN207226132U (en) A kind of powder stores feed bin fluidization system
EP0105249A1 (en) Apparatus for handling particulate material.
CN210012337U (en) Powder fluidizing device
CN208327929U (en) Energy-efficient fine coal pressurization conveying system
US4172618A (en) Apparatus for assisting movement of a flowable material
WO1997040916A1 (en) Device for bag house filter
CN218753647U (en) Pneumatic conveying and sending system for pulverized coal conveying
JPH0720001Y2 (en) Granule filling device
CN213799388U (en) Multi-point fluidization suction and exhaust device for suction and exhaust vehicle
CN203699049U (en) Cement tank container
CN210236416U (en) Pressure relief filtering structure of powder fluidizing device