JPH03287925A - Device for conveying earth, sand and sludge under pressure - Google Patents
Device for conveying earth, sand and sludge under pressureInfo
- Publication number
- JPH03287925A JPH03287925A JP8752990A JP8752990A JPH03287925A JP H03287925 A JPH03287925 A JP H03287925A JP 8752990 A JP8752990 A JP 8752990A JP 8752990 A JP8752990 A JP 8752990A JP H03287925 A JPH03287925 A JP H03287925A
- Authority
- JP
- Japan
- Prior art keywords
- sand
- hopper
- sludge
- earth
- 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.)
- Granted
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 34
- 239000004576 sand Substances 0.000 title abstract description 35
- 238000005086 pumping Methods 0.000 claims description 18
- 239000013049 sediment Substances 0.000 claims description 6
- 238000013019 agitation Methods 0.000 claims description 3
- 239000010419 fine particle Substances 0.000 abstract description 17
- 239000002002 slurry Substances 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 239000002245 particle Substances 0.000 description 16
- 238000003756 stirring Methods 0.000 description 13
- 239000000463 material Substances 0.000 description 8
- 239000002689 soil Substances 0.000 description 7
- 239000012530 fluid Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000011362 coarse particle Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、土砂やヘドロ等を管路輸送する圧送装置に関
する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a pressure feeding device for transporting earth, sand, sludge, etc. through a pipe.
従来、河せんや港湾等で浚渫・揚土された土砂やヘドロ
の移送にはベルトコンベヤ方式の他、ドレツジャーポン
プ、ピストン式ポンプ、空気圧式ポンプ等による管路圧
送方式が利用されている。Conventionally, in addition to the belt conveyor system, pipe pressure pumping methods using dredger pumps, piston pumps, pneumatic pumps, etc. have been used to transfer soil and sludge dredged and lifted from river channels and ports. .
第5図にポンプによる管路圧送の場合の構成例を示す。FIG. 5 shows an example of a configuration in the case of pipe pressure feeding using a pump.
1は圧送ポンプ、2はホッパ 3は攪拌装置、4はスク
リーン、5は圧送管、12は給水管、13は土砂・ヘド
ロ導管である。攪拌装置3で水と共に攪拌混合された土
砂・ヘドロをポンプ1により土砂・ヘドロ導管13に圧
送する。1 is a pressure pump, 2 is a hopper, 3 is an agitation device, 4 is a screen, 5 is a pressure feed pipe, 12 is a water supply pipe, and 13 is a soil/sludge conduit. The earth, sand and sludge mixed with water by the stirring device 3 are pumped into the earth, sand and sludge conduit 13 by the pump 1.
(1)ベルトコンベア方式は、移送対象物の適用範囲が
広く汎用性が高いが、流動性の高いヘドロに対してはコ
ンベアの許容傾斜角が小さく、高・低差への対応が困難
である他、ベルトからの落下、イルトへの付着、臭気の
拡散等環境上の問題がある。(1) The belt conveyor system is highly versatile and can be applied to a wide range of objects to be transferred, but the permissible inclination angle of the conveyor is small for highly fluid sludge, making it difficult to respond to height differences. In addition, there are environmental problems such as falling from belts, adhesion to tiles, and diffusion of odors.
(2) ドレツジャーポンプ方式は、ベルトコンア方
式の様な問題はないが、基本的に水力輸送であり、移送
対象物に多量の水を加える必要があり(一般に含水率8
5傷以上必要とされている)、埋立地へ排出後の泥水の
処理、固化の長期化、泥土の乾燥収縮等の問題がある。(2) The dredger pump method does not have the same problems as the belt conveyor method, but it is basically a hydraulic transport method, and it is necessary to add a large amount of water to the object to be transported (generally, the water content is 8.
(more than 5 scratches are required), treatment of mud after discharge to a landfill, prolonged solidification, drying shrinkage of mud, and other problems.
(3) ピストン式ポンプや空気圧式ポンプでは、上
記(1) 、 (21項の問題はほとんどないが、移送
対象物が高濃度で流動性が極めて低い場合や、シルト等
の微粒子分をほとんど含有しない砂等では、圧送抵抗が
急激に上昇し、圧送困難・モ送手能となる問題がある。(3) Piston-type pumps and pneumatic pumps have almost no problems in (1) and (21) above, but when the material to be transferred is highly concentrated and has extremely low fluidity, or contains almost no particulate matter such as silt. With sand, etc. that cannot be used, the pumping resistance increases rapidly, causing problems such as difficulty in pumping and difficulty in pumping.
ピストン式又は空気圧式ポンプによる高濃度管路圧送に
おいて、
(1)シルト等の微粒子分を圧送用ポンプとは別置のタ
ンクに溜めて流動化、調整しておき、(2)はとんど流
動性の無い土砂や微粒子分をほとんど含有したい砂等が
圧送用ポンプのホッパに供給された場合、別置のタンク
に溜めている微粒子スラリを圧送用ポンプのホッパに補
填し、流動性のない土砂・砂等と混合・攪拌し、正送対
象物の流動性を高める。In high-concentration pipe pumping using piston-type or pneumatic pumps, (1) fine particles such as silt are collected in a tank separate from the pump for fluidization and adjustment, and (2) is mostly When non-fluid soil or sand that contains almost all fine particles is supplied to the hopper of the pressure pump, the fine particle slurry stored in a separate tank is replenished into the hopper of the pressure pump. Mixes and stirs with soil, sand, etc. to increase the fluidity of the object to be forwarded.
はとんど流動性を持たたい土砂や、微粒子分をほとんど
含有しない砂に、シルト等の流動性を持った微粒子を補
填して攪拌すると、微粒子が大径粒子相互のスキ間に入
り込み、イアリングの作用を起して大径粒子間の相対運
動が容易となり、流動性を含有する様にたる。補填する
量は、元の圧送物に対し数嘔〜1096程度で十分であ
り、大量には必要としない。When you add silt or other fluid particles to sand and sand that you want to have fluidity, or sand that contains almost no particulate matter, the particles get into the spaces between the large particles, causing earrings. Due to this action, relative movement between large-diameter particles becomes easy, and the barrel becomes fluid. The amount to be compensated is sufficient to be approximately 1,096 to 1,096 to the original pumped material, and a large amount is not required.
そこで、通常、圧送が順調な時に圧送物中より微粒子の
一部を別置の微粒子タンクに分離しく又は、別途微粒子
分を微粒子タンクに供給しても良い)、濃度を調整して
流動化させて溜めておく。Therefore, when the pumping is going smoothly, some of the particles in the pumped material are separated into a separate particle tank, or the particulates can be separately supplied to the particle tank), and the concentration is adjusted and fluidized. Save it up.
その後圧送物の内容が変化し、濃度が極めて高く流動性
を持たない土砂や、微粒子をほとんど含またい砂等が供
給された場合、そのま工では圧送抵抗が急激に上昇して
圧送困難となったり、管内で閉塞を起し圧送不能となる
ので、その様な兆候が発生した場合、前述の微粒子タン
クより圧送量に対して数多〜10嘩程度の流動性を持っ
た微粒子をホッパに供給して攪拌する事により、それ迄
圧送困難又は圧送不能であった土砂、砂等が流動性を保
有する様になり、スムーズに圧送出来る事となる。If the content of the material to be pumped changes after that, and if extremely concentrated soil with no fluidity or sand that contains almost no fine particles is supplied, the pumping resistance will rapidly increase and pumping becomes difficult in the same method. If such a symptom occurs, the fine particles with a fluidity of about 10 to 10 times the amount of pumping are supplied from the above-mentioned particle tank to the hopper. By stirring and stirring, earth, sand, etc. that were previously difficult or impossible to pump will become fluid and can be pumped smoothly.
第1図において、1は土砂・ヘドロ圧送用ポンプで、ピ
ストン式の場合を示し、101は圧送シリンダで、圧送
ピストン102の後退により、ホッパ2内に溜っている
土砂・ヘドロが吸入・吐出弁104を介して圧送シリン
ダ101内に吸込まれ、次に圧送ピストン102の前進
により、吸入・吐出弁104を介して圧送管5へ押し出
され、土砂・ヘドロの圧送が行われる。圧送ピストン1
02は油圧シリンダ103によって駆動される。このメ
カニズムは従来公知のピストン式コンクリートポンプと
何ら変わるものではない。3はホッパ2内に設置されて
いる攪拌装置で、土砂・ヘドロ導管13によってホッパ
2へ供給される土砂・ヘドロを攪拌し、土砂・ヘドロの
塊砕、均質化、流動化を図る。4はスフ−ノーンで供給
される土砂・ヘドロに含まれる粘土大塊や岩塊がホッパ
2内に入る事を防止する。In Fig. 1, 1 is a pump for pumping dirt and sludge, which is a piston type, and 101 is a pressure cylinder, and when the pump piston 102 retreats, the dirt and sludge accumulated in the hopper 2 are removed from the suction/discharge valve. The dirt and sludge are sucked into the pressure-feeding cylinder 101 via the pressure-feeding piston 104, and then pushed out into the pressure-feeding pipe 5 via the suction/discharge valve 104 by the advancement of the pressure-feeding piston 102, thereby performing the pressure-feeding of earth, sand, and sludge. Pressure feeding piston 1
02 is driven by a hydraulic cylinder 103. This mechanism is no different from conventionally known piston type concrete pumps. 3 is a stirring device installed in the hopper 2, which stirs the earth, sand, and sludge supplied to the hopper 2 through the earth, sand, and sludge conduit 13, and aims at crushing, homogenizing, and fluidizing the earth, sand, and sludge. 4 prevents large clay lumps and rock lumps contained in the earth, sand and sludge supplied by the Sukhnoon from entering the hopper 2.
6は微粒子タンクで、土砂・ヘドロ導管13の分岐管1
4を介して供給される土砂・ヘドロ中から、微粒子分を
スクリーン8でスクリーニングして溜めるタンクであり
、攪拌装置7を装備しており、給水ライン12から供給
される水(又は海水等)と微粒子タンク6内の微粒子と
を混合、攪拌し、微粒子の濃度・粘度等を調整しスラリ
化する。スクリーン8で除去された大径粒子や石はシュ
ート9により圧送ポンプ1のホッパ2側へ送られる。6 is a particulate tank, which is a branch pipe 1 of the sediment/sludge pipe 13.
This is a tank that screens fine particles from the soil and sludge supplied through the water supply line 12 with a screen 8 and collects them. The particles in the particle tank 6 are mixed and stirred, and the concentration, viscosity, etc. of the particles are adjusted to form a slurry. The large-diameter particles and stones removed by the screen 8 are sent to the hopper 2 side of the pressure pump 1 by the chute 9.
微粒子タンク6で調整された、土砂・ヘドロの微粒子分
より構成されるスラリは管路10を介して圧送ポンプ1
のホッパ2内へ供給される。管路10に設けられたパル
プ11は微粒子タンク6からホッパ2へ供給されるスラ
リの供給/停止、供給量をコントロールする。15は粘
度計でホッパ2内の圧送物の粘度を計測する。The slurry composed of fine particles of earth, sand and sludge adjusted in the fine particle tank 6 is sent to the pressure pump 1 via a pipe 10.
is supplied into the hopper 2. The pulp 11 provided in the pipe line 10 controls the supply/stop and amount of slurry supplied from the particulate tank 6 to the hopper 2 . 15 measures the viscosity of the pumped material in the hopper 2 with a viscometer.
次に本装置の作用を説明する。Next, the operation of this device will be explained.
第3図に土砂・ヘドロの一船釣々濃度−粘度曲線を示す
。同図より濃度が高くなる(=含水率が低くなる)と粘
度は急激に高くなって行<(=圧送抵抗が高くたり、圧
送性が悪化する)事が判る。Figure 3 shows the concentration-viscosity curve for one boat of sediment and sludge. From the same figure, it can be seen that as the concentration increases (=moisture content decreases), the viscosity rapidly increases (=pumping resistance increases or pumping performance deteriorates).
又、砂の含有比率が増加する(=粒度構成が粗くなる)
とその傾向が増々顕着となり、ついには僅か数多の温度
変化で圧送困難となる。Also, the content ratio of sand increases (= grain size structure becomes coarser)
This tendency becomes more and more obvious, and eventually it becomes difficult to pump the material even with just a few temperature changes.
一方圧送動が粗い粒子のみ(例えば砂だけ)の場合は、
粒子量子がブリッジを構成しく第4図(a)参照)、相
互のズレを起し難く、はとんど流動性を持たず、管路内
では閉塞を起す。On the other hand, if the pumping movement is only for coarse particles (for example, only sand),
Particle quanta constitute a bridge (see Fig. 4(a)), and are difficult to cause mutual displacement, have almost no fluidity, and cause blockages in pipes.
そこで通常の圧送中、前述の如き圧送困難や閉塞を発生
させる高濃度の土砂・ヘドロや、多量の砂が供給される
とホッパ2内に装着しである粘度計15の指示値が高く
なるので、その状態となった場合、パルプ11を開口し
て微粒子タンク6からスラリ化された微粒子分をホッパ
2内へ圧送量の数%〜10優程度供程度、攪拌装置3で
混合・攪拌すると第3図に於て矢印の方へ性状が変化し
、急激に圧送抵抗が減少して圧送可能となる。又、粗い
粒子が多く閉塞を発生する状態であっても、微粒子が大
径粒子間に入り込む事(第4図(b)参照)により、ベ
アリング使用を起して流動性を持つ事となり、スムーズ
に圧送出来る様になる。Therefore, during normal pressure feeding, if highly concentrated earth, sand, sludge, or a large amount of sand is supplied, which causes difficulty in pumping or blockage as described above, the reading on the viscometer 15 installed in the hopper 2 will become high. If this happens, open the pulp 11 and mix and stir the slurry of fine particles from the fine particle tank 6 into the hopper 2 by a few percent to more than 10 percent of the amount fed into the hopper 2. In Figure 3, the properties change in the direction of the arrow, the pumping resistance suddenly decreases, and pumping becomes possible. In addition, even if there are many coarse particles that cause blockages, fine particles can get between large diameter particles (see Figure 4 (b)), which will cause fluidity due to the use of bearings, resulting in smooth flow. It will be possible to pump it to
微粒子タンク6からのスラリ供給の判断は、前述の粘度
計15の指示値のみに限定されるものではなく、圧送ポ
ンプの負荷圧力の変化や、圧送物の視覚によるチエツク
によっても十分可能である。Judgment about the supply of slurry from the particulate tank 6 is not limited to the indicated value of the viscometer 15 described above, but can also be determined by changes in the load pressure of the pressure pump or by visually checking the material to be pumped.
第2図に示した実施例は、第1図中のパルプ11をスラ
リポンプ110に置換したもので、微粒子タンク6内の
調整済スラリを強制的にホッパ2へ供給可能としたもの
である。In the embodiment shown in FIG. 2, the pulp 11 shown in FIG.
又、上記実施例では圧送ポンプ1はピストン式ポンプで
示したが、圧送ポンプ1の型式は、特に限定されるもの
ではなく、スクイズ式、空気圧送式等でも勿論かまわな
い。Further, in the above embodiment, the pressure pump 1 is shown as a piston type pump, but the type of the pressure pump 1 is not particularly limited, and may of course be a squeeze type, an air pressure type, etc.
本発明による土砂・ヘドロ圧送装置は、攪拌装置を内厳
したホッパと、前記ホッパの上方に配置され攪拌装置を
内蔵した微粒子タンクと、前記ホッパの上部に接続する
土砂・ヘドロ導管と、前記土砂・ヘドロ導管から分岐し
て前記微粒子タンクの上部に接続する分岐管と、前記微
粒子タンクの下部と前記ホッパの上部とを接続する管路
と、前記管路に設けられたバルブと、前記ホッパの下部
に設げられた圧送ポンプとを具えたことにより、次の効
果を有する。The earth, sand and sludge pumping device according to the present invention includes a hopper with a stirring device inside, a particulate tank placed above the hopper and equipped with a stirring device, a sediment and sludge conduit connected to the upper part of the hopper, and the earth and sand. - A branch pipe that branches from the sludge conduit and connects to the upper part of the particulate tank, a pipe line that connects the lower part of the particulate tank and the upper part of the hopper, a valve provided in the pipe line, and By including the pressure pump provided at the bottom, the following effects are achieved.
(1)ホッパへ供給される土砂・ヘドロが、流動性のな
い状態であったり、大半が砂であったりした場合、その
ままでは圧送ポンプにょる圧送は困難又は不能となるが
、その場合予め微粒子タンクに調整・溜めていた微粒子
よりなるスラリをホッパへ補填(補填量は数多〜1(l
程度で良い)し、攪拌装置によって攪拌・混合する事に
より、流動性のなかった土砂や砂が流動性を持つ様にな
り、スムーズに圧送可能となる。(1) If the earth, sand, or sludge supplied to the hopper is in a non-flowing state or is mostly sand, it will be difficult or impossible to pump it with a pressure pump, but in that case, fine particles should be prepared in advance. Replenish the hopper with slurry made of fine particles that has been adjusted and stored in the tank (replenishment amount ranges from several to 1 (l)
By stirring and mixing with a stirring device, earth and sand that had no fluidity become fluid and can be pumped smoothly.
(2)従来圧送困難、又は不能であったものが、上記の
通り極めて簡単な装置で、流動化剤等の特殊な材料も必
要とせず安価に圧送可能となる。(2) What was conventionally difficult or impossible to pump can now be pumped at low cost with an extremely simple device as described above and without the need for special materials such as a fluidizing agent.
第1図及び第2図は本発明の実施例における構成図を示
し、第3図は土砂・ヘドロの砂含有比率に対する濃度−
粘度曲線を示す。第4図(a) 、 (b)はそれぞれ
砂粒子の構成状態を示す。第5図は従来の圧送ポンプの
構成を示す。
1・・・圧送ポンプ 201.ホッパ3・・攪W
装fl 6−・微粒子タンク7・・・攪拌装
置 1o・・・管路11 ・パルプ
13・・・土砂・ヘドロ導管14・・・分岐管Figures 1 and 2 show configuration diagrams in an embodiment of the present invention, and Figure 3 shows the concentration of soil and sludge relative to the sand content ratio.
The viscosity curve is shown. FIGS. 4(a) and 4(b) each show the configuration of sand particles. FIG. 5 shows the configuration of a conventional pressure pump. 1...Pressure pump 201. Hopper 3... Stirring W
Equipment fl 6-・Particle tank 7... Stirring device 1o... Pipe line 11 ・Pulp
13... Sediment/sludge pipe 14... Branch pipe
Claims (1)
置され攪拌装置を内蔵した微粒子タンクと、前記ホッパ
の上部に接続する土砂・ヘドロ導管と、前記土砂・ヘド
ロ導管から分岐して前記微粒子タンクの上部に接続する
分岐管と、前記微粒子タンクの下部と前記ホッパの上部
とを接続する管路と、前記管路に設けられたバルブと、
前記ホッパの下部に設けられた圧送ポンプとを具えたこ
とを特徴とする土砂・ヘドロ圧送装置。A hopper with a built-in agitation device, a particulate tank placed above the hopper and with a built-in agitation device, a sediment/sludge conduit connected to the upper part of the hopper, and a particulate tank branched from the sediment/sludge conduit. a branch pipe connected to the upper part, a pipe line connecting the lower part of the particulate tank and the upper part of the hopper, and a valve provided in the pipe line;
A device for pumping earth and sludge, comprising a pressure pump provided at the bottom of the hopper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8752990A JP2643005B2 (en) | 1990-04-03 | 1990-04-03 | Sediment and sludge pumping equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8752990A JP2643005B2 (en) | 1990-04-03 | 1990-04-03 | Sediment and sludge pumping equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03287925A true JPH03287925A (en) | 1991-12-18 |
JP2643005B2 JP2643005B2 (en) | 1997-08-20 |
Family
ID=13917528
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8752990A Expired - Fee Related JP2643005B2 (en) | 1990-04-03 | 1990-04-03 | Sediment and sludge pumping equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2643005B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2323874A (en) * | 1995-12-08 | 1998-10-07 | Hydraplant Equipment Pty Ltd | A mobile pumping station |
AU717486B2 (en) * | 1995-12-08 | 2000-03-30 | Hydraplant Equipment Pty Ltd | A mobile pumping station |
JP2007050374A (en) * | 2005-08-19 | 2007-03-01 | Sumitomo Osaka Cement Co Ltd | Method for transporting sludge with low water content, transporting device therefor, and cement production equipment |
JP2009297703A (en) * | 2008-05-13 | 2009-12-24 | Mitsubishi Heavy Industries Environment & Chemical Engineering Co Ltd | Method and apparatus for transporting organic dewatered sludge |
-
1990
- 1990-04-03 JP JP8752990A patent/JP2643005B2/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2323874A (en) * | 1995-12-08 | 1998-10-07 | Hydraplant Equipment Pty Ltd | A mobile pumping station |
GB2323874B (en) * | 1995-12-08 | 1999-10-06 | Hydraplant Equipment Pty Ltd | A mobile pumping station |
AU717486B2 (en) * | 1995-12-08 | 2000-03-30 | Hydraplant Equipment Pty Ltd | A mobile pumping station |
US6129520A (en) * | 1995-12-08 | 2000-10-10 | Hydraplant Equipment Pty Ltd | Mobile pumping station |
JP2007050374A (en) * | 2005-08-19 | 2007-03-01 | Sumitomo Osaka Cement Co Ltd | Method for transporting sludge with low water content, transporting device therefor, and cement production equipment |
JP2009297703A (en) * | 2008-05-13 | 2009-12-24 | Mitsubishi Heavy Industries Environment & Chemical Engineering Co Ltd | Method and apparatus for transporting organic dewatered sludge |
Also Published As
Publication number | Publication date |
---|---|
JP2643005B2 (en) | 1997-08-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2018100993A4 (en) | Cyclonic separation systems and hydro excavation vacuum apparatus incorporating same | |
US6168352B1 (en) | Apparatus for producing high density slurry and paste backfills | |
US5020858A (en) | Method of and apparatus for forming and transporting mud clogs | |
CN108661703A (en) | coarse fraction tailing paste filling method and filling system | |
CN101935143A (en) | Sludge curing system and sludge curing process | |
PL116553B1 (en) | Apparatus for producing and transporting suspensions consisting of comminuted solids dispersed in liquid carrier media | |
CA1161084A (en) | Method of disposal or temporary storage of waste material | |
US6129520A (en) | Mobile pumping station | |
CN1202569A (en) | High concentrate paste-filling technology and equipment in mine | |
JPH03287925A (en) | Device for conveying earth, sand and sludge under pressure | |
CN210875766U (en) | Tailless mine separation and filling system based on skid-mounted all-in-one machine | |
US5042178A (en) | Apparatus and process for solid dredge material disposal | |
JP2010089016A (en) | Method and apparatus for treating dredged soil | |
JP2947647B2 (en) | Prevention device for clogging of pressure feed line | |
CN208280092U (en) | One kind, which is blown sand, makes island curing apparatus | |
US5888026A (en) | Backfill paste production facility and method and apparatus for producing high density slurry and paste backfills | |
CN115680527A (en) | Cross-layer drilling coal slime water separation system | |
JP2607146B2 (en) | Pressure transmitter | |
JP4332080B2 (en) | Excavation soil treatment equipment in shield excavator | |
AU717486B2 (en) | A mobile pumping station | |
RU2044892C1 (en) | Method for filling underground workings with self-cementing metallurgical wastes and device for its realization | |
JP2005330731A (en) | Artificial tidal flat material using clay soil, manufacturing equipment and artificial tidal flat construction method. | |
RU2789770C1 (en) | Device and method for hydromechanized development of deposits of non-metallic building materials occurring in rocks with a high content of clay fraction | |
JPH0663261B2 (en) | Method and apparatus for pumping earth and sand | |
RU2164213C2 (en) | Loose materials pressure hydraulic transportation method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |