JPH02125029A - Mixture force feeding device - Google Patents
Mixture force feeding deviceInfo
- Publication number
- JPH02125029A JPH02125029A JP27450988A JP27450988A JPH02125029A JP H02125029 A JPH02125029 A JP H02125029A JP 27450988 A JP27450988 A JP 27450988A JP 27450988 A JP27450988 A JP 27450988A JP H02125029 A JPH02125029 A JP H02125029A
- Authority
- JP
- Japan
- Prior art keywords
- feed pipe
- force feed
- pipe
- ejector
- long
- 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.)
- Granted
Links
- 239000000203 mixture Substances 0.000 title claims 2
- 238000005086 pumping Methods 0.000 claims description 11
- 239000010802 sludge Substances 0.000 claims description 5
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 description 7
- 238000007664 blowing Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
Landscapes
- Air Transport Of Granular Materials (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、例えば、海底9発電所の取水口、湖沼、河川
9港湾などに堆積したヘドロ、軟泥などの半流動物質の
混気圧送装置に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention is directed to a mixed pumping device for semi-fluid substances such as sludge and soft mud deposited in, for example, water intakes of 9 submarine power plants, lakes, rivers and 9 ports. It is related to.
[従来の技術]
従来においては、給泥部近傍で常時排送管内に圧縮エア
を送入することによって輸送物を圧送するプラグ輸送(
栓流輸送)を行なっていた。そして0′S2図に示すよ
うに、その排送管はエア吹込口から排送管出口まで同一
口径であった。[Conventional technology] Conventionally, plug transport (
Plug flow transport) was being carried out. As shown in Figure 0'S2, the discharge pipe had the same diameter from the air inlet to the discharge pipe outlet.
[発明が解決しようとする課題]
しかしながら、従来の混気圧送装置では、単に圧縮エア
をエジェクタを介して圧送管に吹き込むだけの輸送装置
であり、ヘドロや軟泥などの性状によっては配管抵抗の
大きなものを扱う必要に迫られるが、こういったものは
輸送中に配管途中で正常なプラグ・フロー(栓流)が形
成され難く、しばしば詰まり現象を起すことがあった。[Problems to be Solved by the Invention] However, the conventional mixed pumping device simply blows compressed air into the pumping pipe through an ejector, and depending on the nature of the sludge, soft mud, etc., the pipe resistance may be large. It is necessary to handle materials, but during transportation, it is difficult for normal plug flow to form in the pipes, which often causes clogging.
[課題を解決するための手段] 本発明では、これらの課題を解決するために。[Means to solve the problem] The present invention aims to solve these problems.
ヘドロ、軟泥、その他の半流動物質の混気圧送装置であ
って、輸送装置と輸送装置の吐出口に連結される圧送管
と該圧送管に圧送エアを供給する圧縮エア供給装置およ
びエジェクタを備えてなる混気圧送装置において、該圧
送管の直径を上流側から下流側に向かって段階的に大き
くした。A mixed pumping device for sludge, soft mud, and other semi-liquid substances, comprising a transport device, a pressure pipe connected to a discharge port of the transport device, a compressed air supply device that supplies pressurized air to the pressure pipe, and an ejector. In the mixed pressure feeding device, the diameter of the pressure feeding pipe was increased stepwise from the upstream side to the downstream side.
そして、第2の発明では、圧送管の口径を、最上流では
150A(JIS規格)、最下流では300A(JIS
規格)とした。In the second invention, the diameter of the pressure pipe is 150A (JIS standard) at the most upstream side and 300A (JIS standard) at the most downstream side.
standard).
[作用]
本発明の混気圧送装置においては、輸送装置の吐出口か
ら送られてくる輸送物を、圧送管の途中に設けたエア吹
込管を通じてエジェクタから圧送エアを吹き込んでプラ
グ輸送する。輸送物は、このようにして排送管内をプラ
グ・フロー(栓(転)となって流れ、長距離にわたって
円滑に輸送され、陸上あるいは船倉に排出される。[Function] In the mixed pumping device of the present invention, the transported material sent from the discharge port of the transport device is transported by plugging by blowing pressurized air from the ejector through the air blowing pipe provided in the middle of the pressurizing pipe. In this way, the cargo flows in the discharge pipe as a plug flow, is smoothly transported over long distances, and is discharged onto land or into a ship's hold.
そして、本発明の混気圧送装置における圧送管はエジェ
クタ近辺では比較的小径でプラグ・フロー(栓流)の形
成が容易であり、−足形成されたプラグ、フローは下流
に行くにしたがって、圧送管の径が大径となるので断面
積が大きくなってその分配管抵抗が小さくなるのでその
後円滑に流れていく。The pressure pipe in the mixed pressure feeding device of the present invention has a relatively small diameter in the vicinity of the ejector, and it is easy to form a plug flow. As the diameter of the pipe becomes larger, the cross-sectional area becomes larger and the resistance of the pipe becomes smaller, so that the water flows smoothly thereafter.
[実施例] 以下、実施例に基づいて本発明の詳細な説明する。[Example] Hereinafter, the present invention will be described in detail based on Examples.
第1図は本発明の1実施例を示す全体系統図であり、第
2図に示す従来例とは主要機器は基本的には同一のもの
で構成される。第1図において、lは給泥ホッパ22は
スクリュコンベヤ、3はスクリュコンベヤの吐出管、4
は加圧装置、5は圧送管(5aは小径管、5bは中径管
、5cは大径管)、6はエジェクタ、7はMl電磁開閉
弁8は圧縮エア供給管、9はコンプレッサ、1oは′r
rf、磁開閉弁磁水閉弁第2図においては圧送管5が同
一径(200A)である以外は第1図と同様である。FIG. 1 is an overall system diagram showing one embodiment of the present invention, and the main equipment is basically the same as that of the conventional example shown in FIG. In FIG. 1, l indicates the slurry supply hopper 22 is a screw conveyor, 3 indicates a discharge pipe of the screw conveyor, and 4 indicates a screw conveyor.
is a pressurizing device, 5 is a pressure feed pipe (5a is a small diameter pipe, 5b is a medium diameter pipe, 5c is a large diameter pipe), 6 is an ejector, 7 is an Ml electromagnetic on-off valve 8 is a compressed air supply pipe, 9 is a compressor, 1o is'r
rf, magnetic on-off valve, magnetic water-off valve In Fig. 2, it is the same as in Fig. 1 except that the pressure feed pipe 5 has the same diameter (200A).
次に、本発明の実施例における作動について説明する。Next, the operation in the embodiment of the present invention will be explained.
まず、給泥ホッパlに貯溜された輸送物は、輸送装置と
してのスクリュコンベヤ2を駆動することにより、スク
リュコンベヤ2の吐出口3より加圧!H!!(加圧ポン
プ)4により付勢され、エジェクタ6へ向かう、そして
、コンプレー、す9より供給される圧縮エアが圧縮エア
供給管8を経由して開状態に保たれた電磁開閉弁7を通
過してエア吹込管6aより圧送管5内に吹込まれる。First, the transported material stored in the mud supply hopper 1 is pressurized from the discharge port 3 of the screw conveyor 2 by driving the screw conveyor 2 as a transportation device! H! ! Compressed air is energized by (pressurizing pump) 4 and directed to ejector 6, and then supplied from compressor 9. The compressed air passes through compressed air supply pipe 8 and through electromagnetic on-off valve 7, which is kept open. Then, the air is blown into the pressure feeding pipe 5 from the air blowing pipe 6a.
この結果、圧送管5内でヘドロまたは軟泥などの輸送物
は輸送物の塊りとエアの塊りとが交互に配列された、い
わゆるプラグφフロー(栓流)の状態で圧送管および排
送管を輸送される0以上が正常な輸送状態である。As a result, the transported material such as sludge or soft mud is discharged into the pressure feeding pipe 5 in a so-called plug flow state in which lumps of the transported material and air lumps are arranged alternately. 0 or more being transported through the tube is a normal transport condition.
以上述べた作動については第1因に示す本発明の実施例
と同様、第2図に示した従来例においても基本的には同
じである。The operations described above are basically the same in the conventional example shown in FIG. 2 as in the embodiment of the present invention shown in the first factor.
しかし、輸送距離が特に長い場合や輸送物の性状により
、高粘度や高比重で配管抵抗が大きく、正常なプラグ・
フローを形成し難いものであるなど輸送条件が悪い場合
には1本発明では第1図の実施例に示すように、エジェ
クタの近辺では比較的口径の小さい圧送管であるので、
同一のエア混合比(エア量kg/輸送物乾燥重量kg)
で圧送する場合、輸送断面積が小さい分エア管内流速が
大きくなってプラグ形成が容易である。また、プラグ1
個の量も小さいので搬送エア量も小さくて済む。However, if the transportation distance is particularly long or the nature of the transported material is high, piping resistance may be large due to high viscosity or high specific gravity, and normal plugs or
If transport conditions are poor, such as when it is difficult to form a flow, in the present invention, as shown in the embodiment of FIG.
Same air mixing ratio (air amount kg/dry weight of transported material kg)
In the case of pressure-feeding, the flow velocity in the air pipe increases due to the small transport cross-sectional area, making it easy to form a plug. Also, plug 1
Since the amount of particles is small, the amount of conveying air can also be small.
反面、エア速度が大きいために配管抵抗も大きいため長
距離輸送は難かしい、したがって、−旦プラグ形成がな
された後の配管では、今度は配管抵抗を減少させるため
に圧送管5の口径を次第に大きくしたのである0本実施
例の場合、圧送管5のうち、エジェクタ6に近い圧送管
5aは150A(JIS規格)とし、一方、下流側の圧
送管5Cは300A(JIS規格)を採用し、中間の圧
送管5bは200Aを採用すると好結果が得られ、輸送
距離は200mを越えたが、安定した正常な輸送を実現
できた。On the other hand, since the air velocity is high and the piping resistance is also large, long-distance transportation is difficult.Therefore, in the piping after the plug has been formed, the diameter of the pressure feeding pipe 5 is gradually changed to reduce the piping resistance. In the case of this embodiment, among the pressure feed pipes 5, the pressure feed pipe 5a near the ejector 6 is 150A (JIS standard), while the pressure feed pipe 5C on the downstream side is 300A (JIS standard). Good results were obtained when a 200A pipe was used for the intermediate pressure feed pipe 5b, and although the transport distance exceeded 200 m, stable and normal transport could be achieved.
また、圧送管5の口径をすべて200Aとしたときには
、配管抵抗は小さいが、断面積が大きいためエジェクタ
付近のエア管内流速が遅くプラグ形成に難があり、運転
初期の段階でしばしば詰まりを生じて安定した操業がで
きなかった。In addition, when the diameters of all the pressure feed pipes 5 are set to 200A, the pipe resistance is small, but because the cross-sectional area is large, the flow velocity in the air pipe near the ejector is slow, making it difficult to form a plug, which often causes clogging in the early stages of operation. Stable operations were not possible.
[発明の効果]
以上、説明した通り、本発明の構成を採ることにより、
安定したプラグ形成が容易に達成でき、かつ、配管抵抗
も小さいので長距離輸送が可能であり、輸送物の性状変
化に対しても十分対応できる信頼性の高い混気圧送装置
を供給できる。また、配管抵抗が減少するので圧縮空気
供給装置のイニシャルコスト、ランニングコストを低減
できる。[Effect of the invention] As explained above, by adopting the configuration of the present invention,
Stable plug formation can be easily achieved, piping resistance is low, so long-distance transportation is possible, and a highly reliable mixed pumping device that can adequately respond to changes in the properties of transported objects can be provided. Furthermore, since piping resistance is reduced, the initial cost and running cost of the compressed air supply device can be reduced.
第1図は本発明の1実施例を示す全体系統図、第2図は
従来の混気圧送装置を示す全体系統図である。
1・・・・・・給泥ホッパ、 2・・・・・・スクリ
ュコンベヤ、3・・・・・・吐出口、 4・・・
・・・加圧装置、5・・・・・・圧送管、 6・
・・・・・エジェクタ、6a・・・エア吹込管、 9
・・・・・・コンプレッサ、20・・・・・・プラグ。
特許出願人 宇部興産株式会社
第
図
第
凶FIG. 1 is an overall system diagram showing one embodiment of the present invention, and FIG. 2 is an overall system diagram showing a conventional mixed pumping device. 1...Mud supply hopper, 2...Screw conveyor, 3...Discharge port, 4...
... Pressure device, 5 ... Pressure feed pipe, 6.
... Ejector, 6a... Air blowing pipe, 9
...Compressor, 20...Plug. Patent applicant Ube Industries Co., Ltd.
Claims (2)
置であって、輸送装置と輸送装置の吐出口に連結される
圧送管と該圧送管に圧送エアを供給する圧縮エア供給装
置およびエジェクタを備えてなる混気圧送装置において
、該圧送管の直径を上流側から下流側に向かって段階的
に大きくしたことを特徴とする混気圧送装置。(1) A mixed pumping device for sludge, soft mud, and other semi-liquid substances, including a transport device, a pressure pipe connected to the discharge port of the transport device, and a compressed air supply device that supplies pressurized air to the pressure pipe; A mixture pumping device comprising an ejector, characterized in that the diameter of the pumping pipe is gradually increased from the upstream side to the downstream side.
、かつ、最下流の口径を300Aとした混気圧送装置。(2) A mixed pumping device according to claim 1, in which the most upstream diameter of the pressure feeding pipe is 150A and the most downstream diameter is 300A.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63274509A JP2618700B2 (en) | 1988-11-01 | 1988-11-01 | Pressure transmitter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63274509A JP2618700B2 (en) | 1988-11-01 | 1988-11-01 | Pressure transmitter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02125029A true JPH02125029A (en) | 1990-05-14 |
JP2618700B2 JP2618700B2 (en) | 1997-06-11 |
Family
ID=17542688
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63274509A Expired - Fee Related JP2618700B2 (en) | 1988-11-01 | 1988-11-01 | Pressure transmitter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2618700B2 (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6168168U (en) * | 1984-10-02 | 1986-05-10 | ||
JPS61191731A (en) * | 1985-02-18 | 1986-08-26 | Katsuyoshi Harada | Sludge pressure feeder |
-
1988
- 1988-11-01 JP JP63274509A patent/JP2618700B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6168168U (en) * | 1984-10-02 | 1986-05-10 | ||
JPS61191731A (en) * | 1985-02-18 | 1986-08-26 | Katsuyoshi Harada | Sludge pressure feeder |
Also Published As
Publication number | Publication date |
---|---|
JP2618700B2 (en) | 1997-06-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |