JP4372252B2 - High-lift suction and discharge device for liquid and solid-liquid mixture - Google Patents

High-lift suction and discharge device for liquid and solid-liquid mixture Download PDF

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Publication number
JP4372252B2
JP4372252B2 JP36614498A JP36614498A JP4372252B2 JP 4372252 B2 JP4372252 B2 JP 4372252B2 JP 36614498 A JP36614498 A JP 36614498A JP 36614498 A JP36614498 A JP 36614498A JP 4372252 B2 JP4372252 B2 JP 4372252B2
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Japan
Prior art keywords
recovery tank
valve
pipe
pressure
discharge
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Expired - Lifetime
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JP36614498A
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Japanese (ja)
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JP2000186689A (en
Inventor
武幸 西村
三郎 下農
登 工岡
博志 高比良
秀明 金谷
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Tsurumi Manufacturing Co Ltd
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Tsurumi Manufacturing Co Ltd
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Priority to JP36614498A priority Critical patent/JP4372252B2/en
Publication of JP2000186689A publication Critical patent/JP2000186689A/en
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Description

【0001】
【発明の技術分野】
本発明は、例えばシールド工法におけるセグメントのインバートの泥水処理等に供せられる、液体および固液混合体の高揚程吸排装置に関するものである。
【0002】
【従来技術とその問題点】
図2に示すよう、真空ポンプ113の吸引作用により吸排タンク102内へ回収された液体または固液混合体を排水ポンプ116の吐出作用によって排送させるという吸排装置は公知である。しかし高揚程の吸排は困難であり、また、回収物中に固分が多く含まれている場合には液分のみが排出され、固分が吸排タンク102内に残存したり、揚水管108内で固分による閉塞が生じることになる。
【0003】
それを解決する対策として、吸込管路104中に固分回収タンク101を脱着可能に介装させておき、真空ポンプ113の吸引作用により吸引された固液混合体を一旦固分回収タンク101内へ収容させ、重力により分離した液分のみを吸排タンク102内へ移送して排水ポンプ116の吐出作用で揚水管108を通じて排送させ、固分が満杯となった固分回収タンク101は吸込管路104中から取り外して坑外へ引き揚げ、固分を排出したのち再び坑内へ固分回収タンク101を降下させて吸込管路104に接続させるという手段が講じられている。しかしこのような繁雑な作業に多大の労力を必要とするばかりでなく、その間吸排作業を中断しなければならないという欠点がある。
【0004】
【発明の目的】
本発明の目的は、上記従来の欠点を払拭して回収物中に固分が多く含まれている場合でも揚送管路を通じての排出が強力かつ円滑に行われ、吸排タンク内に固分が残存することなく、かつ揚送管路内に閉塞を生じさせることなく作業性に優れ、特に高濃度スラリーの高揚程吸排に極めて有効な装置を提供することにある。
【0005】
【発明の構成】
本発明に係る液体および固液混合体の高揚程吸排装置においては、上方に位置する一次回収タンクの下底部が下方に位置する二次回収タンクと切換弁を介して導通せられ、一次回収タンクから導出された吸込管の先端部が液体または固液混合体の供給源へ開口され、一次回収タンクの上方部は吸気管路により真空発生装置の吸込口へ連通され、二次回収タンクの上方部には圧力センサが付設されると共に下方部からは圧送用開閉弁を介して揚送管路が導延せられ、コンプレッサから導出された送気管が分岐されてその一路は加圧排出用開閉弁を介して二次回収タンク内へ開口され、送気管の他の一路は加圧圧送用開閉弁を介して圧送用開閉弁の二次側より揚送管路内へ開口せられ、二次回収タンクの上方部と一次回収タンクの上方部とが連通用開閉弁を介して通気管により導通され、吸込口を一次回収タンク内へ開口させ水位検出器の検出信号により作動する排水オートポンプの吐出口が吐出用逆止弁を介して揚送管路に接続されている。
【0006】
【実施例】
以下本発明実施例の図1により説明をする。
【0007】
1は一次回収タンク、2は二次回収タンクであって、上方に位置する一次回収タンク1の下底部が下方に位置する二次回収タンク2と切換弁3を介して導通されている。4は一次回収タンク1から導出された吸込管であり、その導出先端部は泥水や浚渫物などの供給源へ開口される。5は一次回収タンク1の上方部から導出されて真空発生装置6の吸込口と連通する吸気管路、7は二次回収タンク2の上方部に付設された圧力センサ、8は二次回収タンク2内の下方部から導出せられ圧送用開閉弁9を介して導延される揚送管、10は二次回収タンク2の上方部と一次回収タンク1の上方部とを導通させる通気管であり、連通用開閉弁11が介装されている。12はコンプレッサ13から導出された送気管で、二路に分岐されてその一路12Aは加圧排出用開閉弁14を介して二次回収タンク2内へ開口され、他の一路12Bは加圧圧送用開閉弁15を介して圧送用開閉弁9の二次側より揚送管路8内へ開口されている。16は水位検出器17の検出信号により作動する排水オートポンプであって、吸込口を一次回収タンク1内へ開口させ吐出口は吐出用逆止弁18を介して揚送管路8に接続する。
【0008】
【作用】
真空発生装置6が駆動し、切換弁3と連通開閉弁11が開状態で、加圧排出用開閉弁14が閉状態にあるとき、一次回収タンク1内および二次回収タンク2内は減圧される。従って吸込管4の導出先端部を泥水や浚渫物などの供給源へ開口させれば、吸引された回収物は一次回収タンク1内から切換弁3を通過して二次回収タンク2内へ流入し、回収物の吸引が続けば比重差によって固分は二次回収タンク2内に貯留されると共に一次回収タンク1内の液位も次第に上昇し、水位検出器17の検出信号により排水オートポンプ16が駆動し液分は吐出用逆止弁18を通過し揚送管路8内に至るが、コンプレッサ13が駆動し加圧圧送用開閉弁15を開状態とすることにより圧縮空気が揚送管路8内に注入され、気液混合状態となって揚送管路8により所定の廃棄場所まで排送される。他方、二次回収タンク2内に貯留された固分はタイマーにより適時排出されるが、切換弁3および連通用開閉弁11が閉成することで一次回収タンク1と二次回収タンク2とは遮蔽され、一次回収タンク1内の減圧状態は維持されているので供給源からの回収作用は継続される。そして加圧圧送用開閉弁15が閉じ圧送用開閉弁9および加圧排出用開閉弁14が開となることで、二次回収タンク2内の貯留固分は圧縮空気により一気に排出されるが、二次回収タンク2内の圧力が予め定めた所定値まで低下すれば、圧力センサ7の検知作用で二次回収タンク2内の貯留固分の排出が終了したものと判断する。それまでの間上記供給源からの回収物は一時的に一次回収タンク1内に貯留され、上記二次回収タンク2内の貯留物排出終了すなわち、上記弁作動と逆の圧送用開閉弁9および加圧排出用開閉弁14の閉作動をまって加圧圧送用開閉弁15を開とし、揚送管8に残存するスラリー閉塞を抑制しながら連通用開閉弁11が開となることにより二次回収タンク2内を一次回収タンク1内と同様の減圧状態となしたのち、切換弁3が開となり一次回収タンク1内の貯留物が二次回収タンク2内へ流下する。
【0009】
上述の作動を1サイクルとしてこれを反復継続させることにより、液体または固液混合体の連続的な回収と間欠的な排出作用が円滑かつ強力に行われることになる。なお、圧送用開閉弁9が閉作動中は加圧圧送用開閉弁15は常時開状態としておいてもよい。
【0010】
【発明の効果】
本発明吸排装置によれば、真空発生装置の吸引作用によって回収された固液混合体のうち、排水オートポンプによって行われる液分の揚送作用がコンプレッサの加圧圧送作用によって強力に助勢され、固分の排送はコンプレッサから二次回収タンク内に加えられる加圧排出作用と揚送管路内に加えられる加圧圧送作用と両々相まって極めて強力に行われる。従って回収物中に固分が多く含まれいる場合でも、回収タンク内に残存することなく確実に排出せられ、特に高濃度スラリーの高揚程吸排用として極めて有効に機能する。また、構造簡潔で小型に構成し得るため狭隘な作用現場、例えばシールド工法における立坑および斜坑内に搬入して使用するのに適している。
【図面の簡単な説明】
【図1】本発明吸排装置における管路系統を示した説明図である。
【図2】従来の吸排装置における管路系統を例示した説明図である。
【符号の説明】
1 一次回収タンク
2 二次回収タンク
3 切換弁
4 吸込管
5 吸気管路
6 真空発生装置
7 圧力センサ
8 揚送管
9 圧送用開閉弁
10 通気管
11 連通用開閉弁
12 送気管
12A 送気管の分岐された一路
12B 送気管の分岐された他の一路
13 コンプレッサ
14 加圧排出用開閉弁
15 加圧圧送用開閉弁
16 排水オートポンプ
17 水位検出器
18 吐出用逆止弁
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a high-lift suction / discharge device for a liquid and a solid-liquid mixture used for, for example, a muddy water treatment of a segment invert in a shield method.
[0002]
[Prior art and its problems]
As shown in FIG. 2, a suction / discharge device is known in which the liquid or solid-liquid mixture recovered into the suction / discharge tank 102 by the suction action of the vacuum pump 113 is discharged by the discharge action of the drainage pump 116. However, it is difficult to suck and discharge at a high head, and when the collected material contains a large amount of solids, only the liquid is discharged, and the solids remain in the suction and discharge tank 102 or in the pumping pipe 108. In this case, blockage due to solid content occurs.
[0003]
As a countermeasure for solving this problem, the solid content recovery tank 101 is detachably interposed in the suction pipe 104, and the solid-liquid mixture sucked by the suction action of the vacuum pump 113 is temporarily stored in the solid content recovery tank 101. Only the liquid component separated by gravity is transferred into the suction / discharge tank 102 and discharged through the pumping pipe 108 by the discharge action of the drain pump 116, and the solid content recovery tank 101 filled with solid content is drawn into the suction pipe. A measure is taken to remove the solid from the passage 104, lift it out of the mine, discharge the solid, and lower the solid collection tank 101 again into the mine and connect it to the suction pipe 104. However, this complicated work not only requires a great deal of labor, but also has the disadvantage that the suction and discharge work must be interrupted during that time.
[0004]
OBJECT OF THE INVENTION
The object of the present invention is to eliminate the above-mentioned conventional drawbacks, and even when the collected material contains a large amount of solids, the discharge through the lifting pipeline is performed powerfully and smoothly, and the solids are contained in the suction / discharge tank. An object of the present invention is to provide an apparatus that is excellent in workability without remaining and does not cause clogging in the pumping pipe, and is extremely effective for high-pump intake / discharge of a high-concentration slurry.
[0005]
[Structure of the invention]
In the high-lift suction / discharge device for liquid and solid-liquid mixture according to the present invention, the lower bottom portion of the primary recovery tank located above is electrically connected to the secondary recovery tank located below via the switching valve, and the primary recovery tank The leading end of the suction pipe led out from is opened to the supply source of the liquid or solid-liquid mixture, and the upper part of the primary recovery tank is communicated with the suction port of the vacuum generator via the intake pipe, and the upper part of the secondary recovery tank A pressure sensor is attached to the part, and a pumping pipe is extended from the lower part via a pressure-feeding on-off valve. It opens into the secondary recovery tank through the valve, and the other passage of the air supply pipe is opened from the secondary side of the on-off valve for pressure feed into the uplift pipe line through the on-off valve for pressurization and pressure. The upper part of the recovery tank communicates with the upper part of the primary recovery tank The discharge port of the drainage auto pump, which is conducted by the vent pipe through the on-off valve, opens the suction port into the primary recovery tank and operates according to the detection signal of the water level detector, is connected to the pumping line through the discharge check valve. It is connected.
[0006]
【Example】
The embodiment of the present invention will be described below with reference to FIG.
[0007]
Reference numeral 1 denotes a primary recovery tank, and reference numeral 2 denotes a secondary recovery tank, and a lower bottom portion of the primary recovery tank 1 positioned above is connected to a secondary recovery tank 2 positioned below via a switching valve 3. Reference numeral 4 denotes a suction pipe led out from the primary recovery tank 1, and the leading end of the suction pipe is opened to a supply source such as muddy water and freight. 5 is an intake pipe that is led out from the upper part of the primary recovery tank 1 and communicates with the suction port of the vacuum generator 6, 7 is a pressure sensor attached to the upper part of the secondary recovery tank 2, and 8 is a secondary recovery tank A lifting pipe 10 led out from a lower part in 2 and led through a pressure on / off valve 9 is a ventilation pipe for electrically connecting an upper part of the secondary recovery tank 2 and an upper part of the primary recovery tank 1. Yes, a communication on-off valve 11 is interposed. An air supply pipe 12 is led out from the compressor 13 and is branched into two paths. One path 12A is opened into the secondary recovery tank 2 through a pressure discharge on / off valve 14, and the other one path 12B is pressurized and pressurized. An opening / closing valve 15 opens from the secondary side of the pressure-feeding opening / closing valve 9 into the lifting pipeline 8. Reference numeral 16 denotes a drainage autopump that operates in accordance with a detection signal from the water level detector 17. .
[0008]
[Action]
When the vacuum generator 6 is driven, the switching valve 3 and the communication on-off valve 11 are open, and the pressure discharge on-off valve 14 is closed, the pressure in the primary recovery tank 1 and the secondary recovery tank 2 is reduced. The Therefore, if the leading end of the suction pipe 4 is opened to a supply source such as muddy water or waste, the collected material that has been sucked flows from the primary recovery tank 1 through the switching valve 3 into the secondary recovery tank 2. If the collected material continues to be sucked, the solid content is stored in the secondary recovery tank 2 due to the difference in specific gravity, and the liquid level in the primary recovery tank 1 gradually rises. 16 is driven, and the liquid passes through the discharge check valve 18 and reaches the inside of the lifting pipe 8. However, the compressor 13 is driven to open the pressurized / pressure-feeding on / off valve 15, so that the compressed air is pumped up. It is injected into the pipe line 8, becomes a gas-liquid mixed state, and is discharged to a predetermined disposal place by the lifting pipe line 8. On the other hand, the solids stored in the secondary recovery tank 2 are discharged timely by a timer, but the primary recovery tank 1 and the secondary recovery tank 2 are defined by closing the switching valve 3 and the on-off valve 11 for communication. Since it is shielded and the decompressed state in the primary recovery tank 1 is maintained, the recovery operation from the supply source is continued. The pressurized pressure on-off valve 15 is closed and the pressure on-off valve 9 and the pressure discharge on-off valve 14 are opened, so that the stored solids in the secondary recovery tank 2 are discharged at once by the compressed air. If the pressure in the secondary recovery tank 2 decreases to a predetermined value, it is determined that the discharge of the stored solids in the secondary recovery tank 2 has been completed by the detection action of the pressure sensor 7. Until then, the recovered material from the supply source is temporarily stored in the primary recovery tank 1 and the discharge of the stored material in the secondary recovery tank 2 is completed, that is , the pressure on-off valve 9 reverse to the valve operation and Secondary operation is performed by closing the pressurizing discharge on / off valve 14 and opening the pressurizing / pressure feeding on / off valve 15 and opening the communication on / off valve 11 while suppressing clogging of the slurry remaining in the lifting pipe 8. After the inside of the recovery tank 2 is decompressed in the same manner as in the primary recovery tank 1, the switching valve 3 is opened and the stored matter in the primary recovery tank 1 flows down into the secondary recovery tank 2.
[0009]
By repeating this operation as one cycle, the continuous recovery and intermittent discharge action of the liquid or solid-liquid mixture can be performed smoothly and powerfully. Note that the pressurizing and pressure-feeding on / off valve 15 may be normally opened while the pressure-feeding on / off valve 9 is closed .
[0010]
【The invention's effect】
According to the suction and discharge device of the present invention, among the solid-liquid mixture recovered by the suction action of the vacuum generator, the liquid pumping action performed by the drain auto pump is strongly assisted by the pressurizing and pumping action of the compressor, The discharge of solids is extremely powerful in combination with the pressurized discharge action applied from the compressor into the secondary recovery tank and the pressurized pressure delivery action applied into the lifting line. Therefore, even if the recovered material contains a large amount of solids, it is reliably discharged without remaining in the recovery tank, and functions extremely effectively as a high-pump intake / exhaust for high-concentration slurry. Further, since the structure is simple and can be configured in a small size, it is suitable for use in a narrow working site, for example, a shaft and a shaft shaft in a shield method.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing a pipeline system in the suction / discharge device of the present invention.
FIG. 2 is an explanatory view illustrating a pipeline system in a conventional suction / discharge device.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Primary collection tank 2 Secondary collection tank 3 Switching valve 4 Suction pipe 5 Intake pipe line 6 Vacuum generation device 7 Pressure sensor 8 Lifting pipe 9 Pressure on-off valve 10 Vent pipe 11 Communication on-off valve 12 Inlet pipe 12A Inlet pipe Branched one path 12B Other branched path 13 Compressor 14 Pressurization discharge on / off valve 15 Pressurization / pressure feed on / off valve 16 Drain autopump 17 Water level detector 18 Discharge check valve

Claims (1)

上方に位置する一次回収タンクの下底部が下方に位置する二次回収タンクと切換弁を介して導通せられ、一次回収タンクから導出された吸込管の先端部が液体または固液混合体の供給源へ開口され、一次回収タンクの上方部は吸気管路により真空発生装置の吸込口へ連通され、二次回収タンクの上方部には圧力センサが付設されると共に下方部からは圧送用開閉弁を介して揚送管路が導延せられ、コンプレッサから導出された送気管が分岐されてその一路は加圧排出用開閉弁を介して二次回収タンク内へ開口され、送気管の他の一路は加圧圧送用開閉弁を介して圧送用開閉弁の二次側より揚送管路内へ開口せられ、二次回収タンクの上方部と一次回収タンクの上方部とが連通用開閉弁を介して通気管により導通され、吸込口を一次回収タンク内へ開口させ水位検出器の検出信号により作動する排水オートポンプの吐出口が吐出用逆止弁を介して揚送管路に接続されていることを特徴とする、液体および固液混合体の高揚程吸排装置。The lower bottom of the primary recovery tank located above is connected to the lower secondary recovery tank via a switching valve, and the tip of the suction pipe led out from the primary recovery tank supplies liquid or solid-liquid mixture. The upper part of the primary recovery tank is connected to the suction port of the vacuum generator by an intake pipe, and a pressure sensor is attached to the upper part of the secondary recovery tank, and a pressure-feeding on-off valve is provided from the lower part. The air supply pipe is extended through the air supply pipe, the air supply pipe led out from the compressor is branched, and one path is opened into the secondary recovery tank through the pressure discharge on-off valve, and the other air supply pipe is One path is opened from the secondary side of the pressure-feeding on / off valve through the pressurized pressure-feeding on-off valve into the pumping pipe, and the upper part of the secondary recovery tank and the upper part of the primary recovery tank are connected to the on-off valve. Through the vent pipe, the suction port is the primary recovery tank The discharge port of a drainage autopump that is opened by a water level detector and is operated by a detection signal from a water level detector is connected to a pumping line through a discharge check valve. About intake and exhaust device.
JP36614498A 1998-12-24 1998-12-24 High-lift suction and discharge device for liquid and solid-liquid mixture Expired - Lifetime JP4372252B2 (en)

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Application Number Priority Date Filing Date Title
JP36614498A JP4372252B2 (en) 1998-12-24 1998-12-24 High-lift suction and discharge device for liquid and solid-liquid mixture

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JP36614498A JP4372252B2 (en) 1998-12-24 1998-12-24 High-lift suction and discharge device for liquid and solid-liquid mixture

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JP2000186689A JP2000186689A (en) 2000-07-04
JP4372252B2 true JP4372252B2 (en) 2009-11-25

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