JPH01207535A - Vacuum air lift mud pumping device - Google Patents
Vacuum air lift mud pumping deviceInfo
- Publication number
- JPH01207535A JPH01207535A JP3237088A JP3237088A JPH01207535A JP H01207535 A JPH01207535 A JP H01207535A JP 3237088 A JP3237088 A JP 3237088A JP 3237088 A JP3237088 A JP 3237088A JP H01207535 A JPH01207535 A JP H01207535A
- Authority
- JP
- Japan
- Prior art keywords
- mud
- pipe
- air
- pump
- tank
- 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.)
- Pending
Links
- 238000005086 pumping Methods 0.000 title claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 24
- 239000004576 sand Substances 0.000 abstract description 13
- 239000002002 slurry Substances 0.000 abstract description 7
- 230000005484 gravity Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 3
- 230000002301 combined effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、水底の土砂を真空とエアリフト複合作用によ
って上昇させて排出する真空エアリフト揚泥装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a vacuum air lift mud lifting device that lifts and discharges earth and sand on the bottom of water by a combined effect of vacuum and air lift.
(従来の技術)
一般に、吸引型の浚渫揚泥作業において、実揚程が高い
場合や、大水深域での浚渫における揚泥、高濃度の泥の
揚泥、沈降速度の大きい土質の揚泥等の場合には、使用
するボン1の吸引限度、即ち、大気圧と重力との関係に
よって定まる限度により、その作業には限界がある。(Prior art) Generally, in suction type dredging and mud pumping work, when the actual pumping head is high, mud is pumped when dredging in large water depth areas, mud is pumped with high concentration, mud is pumped with soil that has a high sedimentation rate, etc. In this case, there is a limit to the operation due to the suction limit of the bong 1 used, that is, the limit determined by the relationship between atmospheric pressure and gravity.
この限界を解消する方法として、第5図(イ)に示すよ
うに、水中サンドポンプ1により通水ホース2を通して
揚泥する方法や、第5図(ロ)に示すように中空筒状の
揚泥管3の下端部にコンプレッサー4から給気管5を通
して給気し、エアーリフトによって揚泥する方法、更に
は第5図(ハ)に示すように、揚泥管6の上端にサンド
ポンプ7を連結し、下端にエジェクター8を取り付け、
駆動水ポンプ9によりエジェクター8から揚泥管6内に
押し上げ水を噴射させて吸入助勢するようにしたもの等
が考えられる。As a method to overcome this limitation, as shown in Fig. 5 (a), there is a method of pumping mud through a water flow hose 2 using a submersible sand pump 1, or a method of pumping mud through a water flow hose 2 as shown in Fig. 5 (b), There is a method in which air is supplied from a compressor 4 through an air supply pipe 5 to the lower end of the mud pipe 3 and the mud is lifted by an air lift, and a sand pump 7 is installed at the upper end of the mud pipe 6 as shown in FIG. Connect, attach the ejector 8 to the lower end,
A conceivable solution is one in which the driving water pump 9 injects water from the ejector 8 into the mud pumping pipe 6 to assist suction.
(発明が解決しようとする課!!M)
しかし、水中サンドポンプを使用する方法では、インペ
ラ部での閉塞等の保守管理が困難であり、大水深では耐
水圧構造としなければならず、高価となる、またエアリ
フトによる方法では揚泥管の下端部内外での比重差を利
用しているため、高濃度や大量の揚泥には不向きである
。更に、エジェクタによって助勢させたものでは、駆動
水用の大容量ポンプが必要であり、また必要以上に泥土
を希釈してしまうという問題があった。(The problem that the invention aims to solve!! M) However, with the method of using a submersible sand pump, maintenance such as blockage in the impeller is difficult, and it is necessary to have a water pressure resistant structure at great depths, which is expensive. Also, since the air lift method uses the difference in specific gravity between the inside and outside of the lower end of the slurry pumping pipe, it is not suitable for pumping high concentrations or large volumes of mud. Furthermore, the method assisted by an ejector requires a large-capacity pump for driving water, and has the problem of diluting the mud more than necessary.
本発明はこのような従来の問題を解決し、低コストで揚
泥能力の高い揚泥装置の提供を目的としたものである。The present invention aims to solve such conventional problems and provide a mud lifting device with high mud lifting capacity at low cost.
(課題を解決するための手段)
上述の如き従来の問題を解決し、所期の目的を解決する
ための本発明の要旨とするところは、筒状をした揚泥管
と、該揚泥管の下部に設けろれ該揚泥管内にエアリフト
用の空気を供給する給気ノズルと、該給気ノズルに空気
を供給するコンプレッサーと、前記揚泥管の上端が連通
され該揚泥管から揚げられた固液と空気とを分離するセ
パレートタンクと、該セパレートタンク内の空気を強制
排出させて該タンク内を減圧する減圧ポンプと前記セパ
レートタンク内の泥土を大気圧下に排出させる泥土排出
手段とを備えてなる真空エアリフト揚泥装置に存する。(Means for Solving the Problems) The gist of the present invention for solving the above-mentioned conventional problems and achieving the intended purpose is to provide a cylindrical mud pumping pipe, and the mud pumping pipe. An air supply nozzle that supplies air for airlift into the mud lifting pipe, a compressor that supplies air to the air supply nozzle, and an upper end of the mud lifting pipe are communicated with each other, so that the mud is lifted from the mud lifting pipe. a separate tank for separating solid liquid and air; a pressure reducing pump for forcibly discharging the air in the separate tank to reduce the pressure in the tank; and a mud discharge means for discharging the mud in the separate tank to atmospheric pressure. A vacuum air lift mud lifting device is provided.
(作用)
この装置は、コンプレッサーで圧縮された空気か給気ノ
ズルから揚泥管内に噴射される。揚泥管の下端開口部で
は、揚泥管内外の圧力差により泥土が管内に押し込まれ
、給気ノズルからの噴射空気と混合し、気体、固体、液
体が混在した気固液三相スラリーとなる。気固液三相ス
ラリーは揚泥管の上部から真空ポンプの負圧が付加され
ており、エアリフトと負圧の複合効果により揚泥されて
セパレートタンクに送り込まれる。セパレートタンク内
では空気と泥水が分離し、空気は真空ポンプに吸引され
る。また、セパレートタンク内は負圧か付加されている
ため、泥水はタンクに設置された水中サンドポンプなど
の泥水排出手段によって大気圧下に排出される。(Function) In this device, air compressed by a compressor is injected into the mud pumping pipe from the air supply nozzle. At the bottom opening of the mud lifting pipe, mud is forced into the pipe due to the pressure difference inside and outside the mud lifting pipe, mixes with the air injected from the air supply nozzle, and becomes a gas-solid-liquid three-phase slurry containing a mixture of gas, solid, and liquid. Become. Negative pressure from a vacuum pump is applied to the gas-solid-liquid three-phase slurry from the top of the mud pumping pipe, and the combined effect of air lift and negative pressure lifts the slurry and sends it into a separate tank. Air and muddy water are separated in a separate tank, and the air is sucked into a vacuum pump. Further, since negative pressure is applied inside the separate tank, the muddy water is discharged to atmospheric pressure by a muddy water discharge means such as a submersible sand pump installed in the tank.
(実施例)
次に、本発明の実施の一例を第1図〜第4図について説
明する。(Example) Next, an example of implementation of the present invention will be described with reference to FIGS. 1 to 4.
図中11は作業台船であり、12は作業台船11から水
底に垂下した揚泥管である。揚泥管12には下端部より
稍上方に給気ノズル13か設けられている。この給気ノ
ズル13は第2図に示すように、揚泥管12の周方向に
一定間隔毎に先端を中心部上方に向けて開口されている
。給気ノズル13の基端部はリング状のマニホルド14
に連通されており、このマニホルド14に給気管15の
先端が連通されている。給気管15は作業台船11上に
股!したコンプレッサ16に連通され、コンプレッサ1
6から圧縮空気をマニホルド14を通して給気管15に
送り、揚泥管12内に噴出させるようにしている。In the figure, numeral 11 is a work barge, and 12 is a mud pumping pipe that hangs down from the work barge 11 to the bottom of the water. The mud pumping pipe 12 is provided with an air supply nozzle 13 slightly above its lower end. As shown in FIG. 2, the air supply nozzles 13 are opened at regular intervals in the circumferential direction of the slurry pumping pipe 12, with their tips directed upward toward the center. The base end of the air supply nozzle 13 is connected to a ring-shaped manifold 14.
The manifold 14 is connected to the manifold 14 and the tip of the air supply pipe 15 is connected to the manifold 14. The air supply pipe 15 is placed above the work barge 11! The compressor 1
Compressed air is sent from 6 to an air supply pipe 15 through a manifold 14, and is ejected into the mud lifting pipe 12.
揚泥管12の上端は作業台船11上に設置したセパレー
トタンク17の上部に連通開口されている。セパレート
タンク17は、その頂部に吸引管18の一端が連通され
ている。吸引管18のfl!!端は真空ポンプ19に連
通され、この吸引管18を通して真空ポンプ19により
セパレートタンク17内を減圧させるようにしている。The upper end of the mud pumping pipe 12 is opened to communicate with the upper part of a separate tank 17 installed on the work barge 11. The top of the separate tank 17 is connected to one end of a suction pipe 18 . Fl of suction tube 18! ! The end is connected to a vacuum pump 19, and the inside of the separate tank 17 is reduced in pressure by the vacuum pump 19 through this suction pipe 18.
セパレートタンク17内には泥土排出手段として水中サ
ンドポンプ20が底部に設置され、その水中サンドボン
フ゛20に通じる排砂管21がセパレートタンク17外
に導出され、これによってセパレートタンク17内の泥
土が強制排出されるようにしている。A submersible sand pump 20 is installed at the bottom of the separate tank 17 as a mud discharge means, and a sand discharge pipe 21 leading to the submersible sand pump 20 is led out of the separate tank 17, thereby forcibly discharging the mud in the separate tank 17. I'm trying to make it happen.
次に、このように構成される揚泥装置の作用について説
明する。Next, the operation of the mud pumping device configured as described above will be explained.
まず、揚泥管12の下端を水底の泥土内に向かわせた状
態でコンプレッサ16と真空ポンプ19とを同時に動作
させる。コンプレッサ16で圧縮された空気は、給気管
15を通りマニホルド14から給気ノズル13に送られ
揚泥管12内に噴射される。これと同時に真空ポンプ1
9によってセパレートタンク17内が減圧される。これ
によって揚泥管12の下端開口部12aでは、給気ノズ
ル13からの空気噴射によるエアリフト作用及び真空ポ
ンプ19による吸引によって減圧され、管内外の圧力差
により泥土が揚泥管12内に押し込まれ、気体、固体、
液体が混合された気固液三相スラリーとなって揚泥管1
2内を上昇し、作業台船11上のセパレートタンク17
内に送り込まれる。First, the compressor 16 and the vacuum pump 19 are operated simultaneously with the lower end of the mud pumping pipe 12 facing into the mud at the bottom of the water. The air compressed by the compressor 16 is sent from the manifold 14 to the air supply nozzle 13 through the air supply pipe 15 and is injected into the mud lifting pipe 12. At the same time, vacuum pump 1
9, the pressure inside the separate tank 17 is reduced. As a result, the pressure at the lower end opening 12a of the mud pumping pipe 12 is reduced by the air lift effect caused by the air injection from the air supply nozzle 13 and the suction by the vacuum pump 19, and the mud is pushed into the mud pumping pipe 12 due to the pressure difference inside and outside the pipe. , gas, solid,
The liquid becomes a gas-solid-liquid three-phase slurry, which is pumped into the mud pumping pipe 1.
Separate tank 17 on the work barge 11
sent inside.
セパレートタンク17内では、比重差によって空気と泥
水とが分離され、空気は真空ポンプ19により、泥水は
水中サンドポンプ20によって強制的にセパレートタン
ク17から排出される。Inside the separate tank 17, air and muddy water are separated by a difference in specific gravity, and the air is forcibly discharged from the separate tank 17 by a vacuum pump 19 and the muddy water by a submersible sand pump 20.
真空エアリフト福泥の基本式は、作業台船11の給気ノ
ズル13位置における圧力の平衡から、γ ・D−H−
γ ・(D+H) 十h fW
v m・・・・・・・・・(1)
γ :管外液比型
γ :管内見掛は比重(気固液)
H:真空ポンプ負圧(負値) (m)■
D :給気ノズル位置水深 (m)H:実揚程
(m)hf:管摩擦損失揚程
(m)となり、式の左辺は駆動エネルギー、右辺
は消費エネルギーとなる。The basic formula for vacuum airlift Fukudo is, from the equilibrium of pressure at the position of the air supply nozzle 13 of the work barge 11, γ ・D−H−
γ ・(D+H) 10h fW
v m・・・・・・・・・(1) γ: Liquid ratio type outside the tube γ: Apparent inside the tube is specific gravity (gas solid liquid) H: Vacuum pump negative pressure (negative value) (m)■ D: Supply Nozzle position water depth (m) H: Actual lifting head
(m) hf: Pipe friction loss head
(m), the left side of the equation is the driving energy, and the right side is the consumed energy.
このときhf、即ち、[γい・D−Hv−γ□・ (D
’r−H)コが大きく取れるほど、大水Jl(?L遠
大)で揚泥できることとなる。At this time, hf, that is, [γi・D−Hv−γ□・(D
The larger the 'r-H) is, the more mud can be pumped with Dasui Jl (?L Endai).
通常のエアリフトの場合(1)式においてHv−〇とな
るから
γ ・D=γ ・<D十H) 十h f・・・・・・(
2)W In
となり、この式からも明らかに、真空エアリフトの方が
駆動エネルギーが大きく、大量揚泥が可能であることが
分かる。In the case of a normal air lift, Hv-〇 is obtained in equation (1), so γ ・D=γ ・<D0H) 10h f・・・・・・(
2) W In From this equation, it is clear that the vacuum air lift has greater driving energy and is capable of lifting a large amount of mud.
また、エアリフトで揚泥するための必要条件はり、〉0
であるから(2)式より
γ□・(1)+H)<γ ・D
故に γ < [D/ (D+H)] ・γ となる。In addition, the necessary conditions for lifting mud with an air lift are:
Therefore, from equation (2), γ□・(1)+H)<γ・D Therefore, γ<[D/ (D+H)]・γ.
m
Wこのことは、通常のエアリフトは実揚程
Hに比べ給気ノズル位置水深りを十分に大きくとらねば
ならず、またγ はγ 以下にしなければならないm
W
ため、揚泥時には大量の空気を送り込む必要がある。こ
れに対し、真空エアリフトは、−Hの分■
たけ余裕があるため、Dはそれほど大きくとる必要はな
く、γ がγ 以上であっても揚泥可能でm
W
ある。m
W This means that in a normal airlift, the depth of the supply air nozzle position must be sufficiently large compared to the actual lifting height H, and γ must be less than γ.
W, so it is necessary to pump a large amount of air when pumping mud. On the other hand, vacuum airlift has a margin of -H, so D does not need to be so large, and even if γ is more than γ, it is possible to lift m
W Yes.
また、吸引式揚泥(通常のポンプ船のタービンポンプも
含む)の場合、吸引揚程はポンプの吸入服界により制限
を受け、−760I1mh(−1011IAQ )を越
えることはない0例えば地山比重γ、=1.7の水底地
山を、真空ポンプで無希釈揚泥(見掛は容積金泥率10
0%)する場合、真空限界 Hv=−9,2m (70
01111H(1)実揚程 H=Om、γ =1.0
とすると、γ =γ、=0.7 基本式(1)より1
.0xD−(−9,2)=1.7xD+hf揚泥開始時
にはhf>Oであるから、
9.2−0.7×D=hf〉O
D<13.1m
よって、上記条件のもとでは、13.1m以上の水深で
は揚泥不可能である。尚、タービンポンプでは吸入限界
が小さいため、揚泥限界水深は更に小さくなる。In addition, in the case of suction pumping (including turbine pumps of ordinary pumping ships), the suction lift is limited by the suction capacity of the pump, and does not exceed -760I1mh (-1011IAQ).For example, the specific gravity of the ground γ , = 1.7, was pumped with a vacuum pump without dilution (apparently the volumetric gold mud ratio was 10).
0%), vacuum limit Hv=-9,2m (70
01111H (1) Actual head H=Om, γ =1.0
Then, γ = γ, = 0.7 From basic formula (1), 1
.. 0xD-(-9,2)=1.7xD+hfSince hf>O at the start of mud pumping, 9.2-0.7xD=hf>O D<13.1m Therefore, under the above conditions, It is impossible to pump mud at a depth of 13.1 m or more. In addition, since the suction limit of a turbine pump is small, the limit water depth for pumping mud is even smaller.
上記条件下において、真空エアリフトで泥土体積の1/
2の空気を噴出させると、
管内見掛は比重
γ =1.7/ (1+0. 5)=1. 13上
記と同様(1)式より
1、OxD士9.2=1.13xD+hf9.2−0.
13xD>O
D<70.8m
上記条件下では、真空エアリフトの揚泥限界は70.8
mと、大幅に増大することがわかる。Under the above conditions, 1/1 of the volume of mud is removed by vacuum air lift.
When air of 2 is blown out, the apparent inside of the pipe is specific gravity γ = 1.7/ (1 + 0. 5) = 1. 13 As above, from equation (1), 1, OxD9.2=1.13xD+hf9.2-0.
13xD>O D<70.8m Under the above conditions, the vacuum airlift lift limit is 70.8m
It can be seen that the value increases significantly as m.
第1表及び第2表に、清水で行った本発明の真空エアリ
フトによる場合と、従来のエアリフトと真空ポンプによ
る場合との揚水の対比実験の結果を示す。Tables 1 and 2 show the results of a comparison experiment of pumping water using fresh water using the vacuum air lift of the present invention and using a conventional air lift and vacuum pump.
第 1 表
第 2 表
尚、セパレートタンク17からの泥水排出手段は上述の
ほか、第3図に示すように、揚泥管12の頂部に設けた
セパレートタンク17の底部に戻り管22を接続し、セ
パレートタンク17内の液面高さを、
固液柱圧(m)≧1真空ポンプ負圧l (m)となる
ようにすることによって、固液は吐出口で大気圧以上の
圧力を持たせ、逆流せずに排出できる。Table 1 Table 2 In addition to the above-mentioned means for discharging muddy water from the separate tank 17, as shown in FIG. By setting the liquid level height in the separate tank 17 so that the solid-liquid column pressure (m)≧1 vacuum pump negative pressure l (m), the solid-liquid has a pressure higher than atmospheric pressure at the discharge port. It can be discharged without backflow.
また高1度揚泥に際しては、第4図に示すように揚泥管
12の下端に可視管23を介して集泥カバー24を取り
付け、これをウィンチ25をもって水底の泥土表面まで
垂下させ、水の吸引を少なくして揚泥させる。In addition, when lifting mud at a height of 1 degree, as shown in Fig. 4, a mud collecting cover 24 is attached to the lower end of the mud lifting pipe 12 via a visible pipe 23, and this is lowered down to the mud surface at the bottom of the water using a winch 25. Reduce suction and lift mud.
(発明の効果)
上述の如き構成の本発明の真空エアリフト揚泥装置は、
次の如き効果がある。(Effect of the invention) The vacuum air lift mud lifting device of the present invention configured as described above has the following features:
It has the following effects.
■ ポンプの吸入限界以上の揚泥が可能となり、大水深
揚泥、高濃度揚泥、高実揚程揚泥が従来方式に比べ、能
率良くできる。■ It is possible to pump more mud than the suction limit of the pump, and it is possible to pump mud at deep water depths, pump mud at high concentrations, and pump mud at high lifting heights more efficiently than with conventional methods.
■ 流送ラインに、インペラ等の機械的部分かないため
、故障が少なく、障害物による閉塞の虞がなく管断面積
近くの大きさの物まで通過させることができる。■ Since there are no mechanical parts such as impellers in the flow line, there are fewer failures and there is no risk of blockage due to obstacles, allowing objects as large as the pipe cross-sectional area to pass through.
■ 粒径又は比重がおおきいために沈降速度の大きい揚
泥対象物を扱うとき、損失揚程を大きくとれるため、管
内流速を上げることができ、作業能率を高いものとする
ことができる。■ When handling objects to be lifted that have a large sedimentation rate due to their large particle size or specific gravity, it is possible to increase the head loss, thereby increasing the flow velocity in the pipe and increasing work efficiency.
■ 機械部分が全て水上にあるため、保守管理が容易で
ある。■ Maintenance is easy because all mechanical parts are above water.
第1図は本発明装置の実施例の全体の概略を示す縦断面
図、第2図は給気ノズル部分の拡大断面図、第3図は泥
土排出手段の他の例の概略を示す縦断面図、第4図は高
濃度揚泥を行う場合の一例の概略を示す側面図、第5図
(イ)〜(ハ)はそれぞれ従来の揚泥装置の概略を示す
側面図である。
11・・・・・・作業台船、12・・・・・・揚泥管、
13・・・・・・給気ノズル、15・・・・・・給気管
、16・・・・・・コンプレッサ、17・・・・・・セ
パレートタンク、18・・・・・・吸引管、19・・・
・・・真空ポンプ、20・・・・・・水中サンドポンプ
、21・・・・・・排砂管。Fig. 1 is a vertical cross-sectional view schematically showing the entire embodiment of the device of the present invention, Fig. 2 is an enlarged cross-sectional view of the air supply nozzle portion, and Fig. 3 is a longitudinal cross-sectional view schematically showing another example of the mud discharge means. Figures 4 and 4 are side views schematically showing an example of a case in which high-concentration mud pumping is performed, and Figs. 5 (a) to (c) are side views schematically showing conventional mud pumping devices, respectively. 11...Work barge, 12...Sludge lifting pipe,
13... Air supply nozzle, 15... Air supply pipe, 16... Compressor, 17... Separate tank, 18... Suction pipe, 19...
... Vacuum pump, 20 ... Submersible sand pump, 21 ... Sand discharge pipe.
Claims (1)
泥管内にエアリフト用の空気を供給する給気ノズルと、
該給気ノズルに空気を供給するコンプレッサーと、前記
揚泥管の上端が連通され該揚泥管から揚げられた固液と
空気とを分離するセパレートタンクと、該セパレートタ
ンク内の空気を強制排出させて該タンク内を減圧する減
圧ポンプと前記セパレートタンク内の泥土を大気圧下に
排出させる泥土排出手段とを備えてなる真空エアリフト
揚泥装置。a cylindrical mud lifting pipe; an air supply nozzle provided at the bottom of the mud lifting pipe for supplying air for air lift into the mud lifting pipe;
a compressor that supplies air to the air supply nozzle; a separate tank that communicates with the upper end of the mud lift pipe and separates air from the solid liquid lifted from the mud lift pipe; and a forced discharge of the air in the separate tank. A vacuum air lift mud pumping device comprising: a pressure reducing pump for reducing the pressure inside the tank; and mud discharge means for discharging the mud in the separate tank to atmospheric pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3237088A JPH01207535A (en) | 1988-02-15 | 1988-02-15 | Vacuum air lift mud pumping device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3237088A JPH01207535A (en) | 1988-02-15 | 1988-02-15 | Vacuum air lift mud pumping device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01207535A true JPH01207535A (en) | 1989-08-21 |
Family
ID=12357057
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3237088A Pending JPH01207535A (en) | 1988-02-15 | 1988-02-15 | Vacuum air lift mud pumping device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01207535A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998020208A1 (en) * | 1996-11-02 | 1998-05-14 | Moburon Design Office Co., Ltd. | Dredging method and dredging apparatus |
JP2006307490A (en) * | 2005-04-27 | 2006-11-09 | Hokuriyou Denko Kk | Ground installation type water intake apparatus |
WO2012001415A1 (en) | 2010-06-29 | 2012-01-05 | Coldharbour Marine Limited | Shockwave generation device and method of delivering a shockwave |
CN102650138A (en) * | 2012-04-28 | 2012-08-29 | 朱知富 | Mud/sand suction ship with air suction and exhaust pump as power |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60208525A (en) * | 1984-03-31 | 1985-10-21 | Toyo Kensetsu Kk | Control on operation of pump dredger |
JPS62284831A (en) * | 1986-05-30 | 1987-12-10 | Furukawa Mining Co Ltd | Dredging apparatus of air lift system |
-
1988
- 1988-02-15 JP JP3237088A patent/JPH01207535A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60208525A (en) * | 1984-03-31 | 1985-10-21 | Toyo Kensetsu Kk | Control on operation of pump dredger |
JPS62284831A (en) * | 1986-05-30 | 1987-12-10 | Furukawa Mining Co Ltd | Dredging apparatus of air lift system |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998020208A1 (en) * | 1996-11-02 | 1998-05-14 | Moburon Design Office Co., Ltd. | Dredging method and dredging apparatus |
US6189243B1 (en) | 1996-11-02 | 2001-02-20 | Moburon Design Office Co., Ltd. | Dredging method and dredging apparatus |
JP2006307490A (en) * | 2005-04-27 | 2006-11-09 | Hokuriyou Denko Kk | Ground installation type water intake apparatus |
JP4565280B2 (en) * | 2005-04-27 | 2010-10-20 | 北菱電興株式会社 | On-site water intake system |
WO2012001415A1 (en) | 2010-06-29 | 2012-01-05 | Coldharbour Marine Limited | Shockwave generation device and method of delivering a shockwave |
CN102650138A (en) * | 2012-04-28 | 2012-08-29 | 朱知富 | Mud/sand suction ship with air suction and exhaust pump as power |
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