JPS60114360A - Device for recovering high-concentration mud water for shield driving method - Google Patents

Device for recovering high-concentration mud water for shield driving method

Info

Publication number
JPS60114360A
JPS60114360A JP22212983A JP22212983A JPS60114360A JP S60114360 A JPS60114360 A JP S60114360A JP 22212983 A JP22212983 A JP 22212983A JP 22212983 A JP22212983 A JP 22212983A JP S60114360 A JPS60114360 A JP S60114360A
Authority
JP
Japan
Prior art keywords
mud
water
mud water
tank
sand
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
Application number
JP22212983A
Other languages
Japanese (ja)
Inventor
Masao Nagai
永井 正男
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHIYOUONPA KK
Ultrasonic Engineering Co Ltd
Original Assignee
CHIYOUONPA KK
Ultrasonic Engineering Co Ltd
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 by CHIYOUONPA KK, Ultrasonic Engineering Co Ltd filed Critical CHIYOUONPA KK
Priority to JP22212983A priority Critical patent/JPS60114360A/en
Publication of JPS60114360A publication Critical patent/JPS60114360A/en
Pending legal-status Critical Current

Links

Landscapes

  • Excavating Of Shafts Or Tunnels (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

PURPOSE:To recover and economize the clay and bentonite components in mud water by washing muck with a small amt. of dilute mud water on an excavation site, separating a gravel-component and a mud-component and reutilizing the separated mud water. CONSTITUTION:A pool part 19 is provided in a muck charging part of a screen for rough gravel of a vibration screen and the muck is charged into the pool part 19. The mud water and sand separated by screening are stored in a mixing, circulating and storing tank 4. The mud water and sand are admitted by a pump 5 into a cyclone 6 and a part of the mud water of the overflow is also admitted into the pool part. The rest is stored in a circulating mud water tank 7. The mud water from the tank 7 is further admitted into the tank 4 by a pump 8. The costly bentonite and clay components are thus recovered.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は加泥シールド工法において発生する掘削側から
高濃度泥水を回収する装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an apparatus for recovering highly concentrated muddy water from the excavation side generated in the muddy shield method.

1− (発明が解決しようとする問題点) 一般に加泥シールド工法において発生する掘削側は、掘
削機によって切羽内に圧入する高濃度泥と地山の土砂が
混合して固練りの生コンクIJ−ト状になって排出され
る。この排出硼(ブリ)は固体の空隙部を泥漿が充満し
、掘削機内では液圧が保持できる状態のものであるので
、このま\車で輸送する時等は取扱上は液性を示し、輸
送中に道路に泥漿がもれて道路を汚したり、泥をはねた
りして二次公害を発生する恐れがあった。これを防止す
るために硼を水槽に投入して洗浄し、砂礫と泥分とを分
離し、泥分を脱水処理することが行われている。しかし
乍らか\る処理には大量の水を必要とし、且つその装置
を膨大なものとなり、それが占める場所も犬となるなど
の欠点がある。またベントナイトを含む泥水は捨場にお
ける処理も難かしく、産業廃物に指定され、処理費が著
しく高価なものとなる等の欠点がある。
1- (Problems to be solved by the invention) In general, the excavation process that occurs in the muddy shield method involves the mixing of high-concentration mud, which is injected into the face by an excavator, and soil from the ground, resulting in hardened fresh concrete IJ. - It is discharged in the form of a tortoise. The solid voids in this discharge bottle are filled with slurry, and the liquid pressure can be maintained inside the excavator, so when transporting it by car, it will be handled as liquid. There was a risk that mud would leak onto the road during transportation, staining the road, or that mud would splash and cause secondary pollution. In order to prevent this, the borage is put into a water tank and washed, the sand and gravel are separated from the mud, and the mud is dehydrated. However, such treatment requires a large amount of water, requires a huge amount of equipment, and takes up a large amount of space. Furthermore, muddy water containing bentonite is difficult to dispose of at dump sites, is designated as industrial waste, and has drawbacks such as extremely high processing costs.

本発明はか\る高濃度泥水と硼との混合物の処理装置に
関するもので、掘削時に添加する高濃度2− 泥には高価なベントナイトや粉末粘土を配合して作泥さ
れているので、掘削現場で出来るだけ少量の所要の希釈
泥水で硼を洗浄し泥分を除去した砂礫分と泥分を分離し
1分離した泥水を作泥水として再使用し、泥水中に存在
する粘土、ベントナイト分を回収し節約することを目的
とするものである。
The present invention relates to a treatment device for a mixture of high-concentration mud and borage. Wash the porcelain with as little diluted mud water as possible on site, remove the mud, separate the sand and gravel, and reuse the separated mud as mud water to remove the clay and bentonite present in the mud. The purpose is to recover and save.

(発明の構成・作用・効果) 本発明は振動篩の粗礫用スクリーンの側設入部にプール
部を設け、該プール部に礪を投入し篩分けられた泥水及
砂の混合循環貯留槽に貯留し、この泥水及び砂をポンプ
によって流入管を経てサイクロンに流入させ、オーバー
フローの泥水の一部を前記プール部に流入し、他は循環
泥水槽に貯留し、更に循環泥水槽から泥水をポンプで混
合循環泥水槽へ流入管を経て流入するようにした高濃度
泥水回収装置である。
(Structure, operation, and effect of the invention) The present invention provides a pool part in the side installation part of the screen for coarse gravel of a vibrating sieve, and puts a rice bowl into the pool part to mix the sieved muddy water and sand into a mixed circulation storage tank. This muddy water and sand are pumped into the cyclone via an inflow pipe, a part of the overflow muddy water is flowed into the pool part, the rest is stored in a circulating muddy tank, and the muddy water is pumped from the circulating muddy tank. This is a high-concentration mud water recovery device in which the mud flows into a mixed circulation mud tank via an inflow pipe.

次に本発明について図面を示して詳細に説明する。Next, the present invention will be described in detail with reference to the drawings.

第1図において、2は筒本体で、筒本体は加振体(図示
せず)によって斜方向に振動するようにな3一 つている。19は粗礫用スクリーン15の硼投入部に設
けられたプール部である。こ\に掘削現場から搬送され
た高濃度泥水と地山の土砂と混合した硼が投入される。
In FIG. 1, reference numeral 2 denotes a cylinder body, and the cylinder body is configured to vibrate in an oblique direction by a vibrator (not shown). Reference numeral 19 denotes a pool portion provided at the borium input portion of the debris screen 15. Highly concentrated mud water transported from the excavation site and borage mixed with earth and sand are added to this.

20はプールに設けられた堰板である。この粗礫用スク
リーン15の目開きは15mmである。16は細礫用ス
クリーンで粗礫用スクリーン15の下段に設けられてお
り、その目開きは例えば2.5 wunのものが使用さ
れる。lは排出硼投入口で、こXに備は矢印Aから、又
液体サイクロンからのオーバーフローの泥水の1部が流
水管18を経て供給される。
20 is a weir plate provided in the pool. The mesh size of this gravel screen 15 is 15 mm. Reference numeral 16 denotes a screen for fine gravel, which is provided at the lower stage of the screen for fine gravel 15, and has a mesh size of, for example, 2.5 wun. 1 is a drain inlet, and a portion of muddy water from the overflow from the hydrocyclone is supplied to this X from an arrow A through a water pipe 18.

す々わち、筒本体2は斜方向へ振動することにより、高
濃度泥水と地山の砂礫及び十分の混合物は技゛入部19
内で洗浄流水管18からの洗浄泥水でうすめられ、振動
により泥水中で粒子相互間の摩擦作用を受け、砂、砕肉
表面に固着した泥分は除去される。かくして固着泥分か
ら分離した砂。
In other words, as the cylinder body 2 vibrates in the oblique direction, a mixture of highly concentrated muddy water, sand and gravel from the ground, and a sufficient amount of water enters the technical input section 19.
The sand and crushed meat surfaces are diluted with washing mud water from the washing water pipe 18, and the particles are subjected to friction between particles in the mud water due to vibration, and the mud particles stuck to the sand and crushed meat surfaces are removed. The sand is thus separated from the fixed mud.

礫及び泥水は堰20を越えて粗礫用スクリーン15に移
動し、粗砕の固体粒子を分粒し、さらに細粒は細礫用ス
クリーン16に送られ細礫を分粒する。
The gravel and mud water pass over the weir 20 to the gravel screen 15, where coarsely crushed solid particles are sized, and the fine particles are further sent to the granule screen 16, where the granules are sized.

4− 分離された泥水、砂は細礫用スクリーン16から流下す
る。分離された粗砕、細礫は矢印B方向へ排出される。
4- The separated muddy water and sand flow down from the gravel screen 16. The separated coarse particles and fine particles are discharged in the direction of arrow B.

筒本体2によって粗砕、細礫を分離された砂分と泥水は
篩下集水樋3から混合循環槽4に貯められ、循環ポンプ
5により泥水と砂は液体サイクロン6に送られる。液体
サイクロン6によって分離された上液は一部は管18を
経て排出砿投入口lに供給され、分岐された他の方は管
21を経て泥水循環槽7に貯えられる。
The sand and muddy water from which the coarse and fine particles have been separated by the cylinder body 2 are stored in the mixing circulation tank 4 from the under-sieve water collection gutter 3, and the muddy water and sand are sent to the liquid cyclone 6 by the circulation pump 5. A part of the upper liquid separated by the liquid cyclone 6 is supplied to the discharge masonry inlet 1 through a pipe 18, and the other part is branched off and stored in the mud water circulation tank 7 through a pipe 21.

一方液体サイクロン6の濃縮、捕集されたアンダーフロ
ーは筒本体2の砂分スクリーン17に還流される。砂分
スクリーン17に還流されたアンダーフローは振動によ
り脱液され、矢印Bから脱水された砂として排出される
。砂分スクリーン17はウェッジワイヤースクリーンで
スリット0.5+++sである。
On the other hand, the concentrated and collected underflow of the liquid cyclone 6 is returned to the sand screen 17 of the cylinder body 2. The underflow returned to the sand screen 17 is dehydrated by vibration and discharged from arrow B as dehydrated sand. The sand screen 17 is a wedge wire screen with a slit of 0.5+++s.

混合循環槽4の砂と泥水はポンプ5で循環させる。混合
循環槽4の上限レベル計10−下限レベル計11が設け
られており、水面が下限レベル計5− に達したら泥水循環槽7からポンプ8によって泥水が補
給され上限レベル計に達したら中止するようになってい
る。混合循環槽4の容量はできるだけ小さくしておき、
砂の沈着を防止する必要がある。
The sand and mud in the mixing circulation tank 4 are circulated by a pump 5. An upper limit level meter 10 and a lower limit level meter 11 are provided for the mixing circulation tank 4, and when the water surface reaches the lower limit level meter 5-, muddy water is replenished from the muddy water circulation tank 7 by the pump 8, and when the upper limit level meter is reached, the operation is stopped. It looks like this. The capacity of the mixing circulation tank 4 should be kept as small as possible.
It is necessary to prevent sand deposition.

循環泥水槽7には初期濃度を下げた泥水を張り込み、循
環洗浄している中に濃度が上昇し、比重計9に設定した
比重に達したら一時洗滌を中止し。
The circulating mud water tank 7 is filled with mud water whose initial concentration has been lowered, and the concentration increases during circulation washing, and when the specific gravity set on the hydrometer 9 is reached, the washing is temporarily stopped.

ポンプ13で循環泥水槽70レベル計10’のレベルま
で泥水を引き抜き1回収泥水槽14へ送る。
The pump 13 pulls out the muddy water from the circulating muddy water tank 70 to the level of the level meter 10' and sends it to the first recovery muddy water tank 14.

循環泥水槽70レベル計10’の信号でポンプは停止し
、給水弁12が開き口より水を加え循環泥水槽7のレベ
ル計11’に達したら弁12を閉じ洗浄を開始するよう
になっている。
The pump is stopped by a signal from the level meter 10' of the circulating mud tank 70, and the water supply valve 12 adds water through its opening, and when it reaches the level meter 11' of the circulating mud tank 7, the valve 12 is closed and cleaning begins. There is.

作泥に必要な泥水は掘削体積に対比して30%以下で、
濃度は50%前後である。また排出される硼中の泥分の
泥分と水とを加えたものとの比、すなわち泥分濃度Cd
は、泥分をSd ton 、水分をWd ton とす
ると 6− おける粘土丹と含水比および切羽に圧入する高濃度泥の
濃度と、注量率〔地山掘削体積当りの注入量体積の比率
(掘削量1m3に付0−2m!を20%と云う)〕、逸
泥率〔地山に侵入して失われ掘削土砂と共に排出されな
いもの〕より計算することができる。
The mud water required for mud production is less than 30% of the excavation volume.
The concentration is around 50%. Also, the ratio of the mud content in the discharged pot to the mud content plus water, that is, the mud content concentration Cd
Let Sd ton be the mud content and Wd ton be the moisture content, then the clay to water content ratio, the concentration of high-concentration mud injected into the face, and the injection rate [ratio of volume of injection volume per volume of excavated rock ( It can be calculated from the amount of excavated soil (0-2 m! per 1 m3 of excavation is 20%)] and the loss rate of mud (sludge that penetrates into the ground and is lost and is not discharged with the excavated soil).

一方作泥に必要とする水は次のようになる。On the other hand, the water required for mud cultivation is as follows.

作泥配合の例 粘 土 0.5 t/7r?C作泥) ベントナイト 0.15 p (p )水 0.75 
〃(tr ) 計 1.42 t/n?(tr ) 掘削量に対して泥漿の注入率を20%とすると。
Example of mud composition: Clay 0.5t/7r? C) Bentonite 0.15 p (p) Water 0.75
〃(tr) Total 1.42 t/n? (tr) Assuming that the slurry injection rate is 20% of the excavation amount.

注入量は掘削量1rr?につき0.2−となる。す々わ
ち 粘土 0.1t/靜 ベントナイト 0.03 t/d 水 0.1!5t、/77/ 7− である。
Is the injection amount 1rr excavation amount? It becomes 0.2- for each. Susuwachi clay 0.1t/silent bentonite 0.03t/d water 0.1!5t, /77/7-.

従って何らかの方法で掘削量を脱水し、砂礫と泥水に分
離回収し、掘削量1m3分の砺から回収した泥水中の水
が上記の水0.15m’以下であれば、粘土、ベントナ
イト、水の夫々を上記数値との差だけ補給すれば注入量
として再使用できる。また回収した泥水中の水が上記の
水0.15772’より大きいときは水が0.1577
1’に相当する粘土、ベントナイトが再利用でき、過剰
分は廃棄処分することになる。再利用するときには粘土
、ベントナイトが少い根回収率が高い。然しシールドマ
シンから排出されてくる砺の状態では濃度が高すぎ直接
泥分と分離することができないので、洗浄用に濃度の低
い泥水を使用する必要がある。
Therefore, if the excavated amount is dehydrated by some method, separated into sand and gravel and muddy water, and the water in the muddy water recovered from the excavated amount of 1 m3 is less than 0.15 m', clay, bentonite, and If each is replenished by the difference from the above values, it can be reused as the injection amount. Also, if the water in the collected muddy water is larger than the above water 0.15772', the water is 0.1577
Clay and bentonite equivalent to 1' can be reused, and the excess will be disposed of. When reusing, there is less clay and bentonite and the root recovery rate is high. However, the concentration of mud discharged from the shield machine is too high to be directly separated from the mud, so it is necessary to use mud water with a low concentration for cleaning.

洗浄に際して洗浄水量が一定であれば洗浄水濃度が低い
程洗浄効果があるが、濃度を下げることにより洗浄後の
水の量が作泥用の水量より多くなれば前述の如く過剰水
となって廃棄することに々るので回収したことにならな
い。本発明はこのようなバランスを考えて発明されたも
のである。
If the amount of washing water is constant during washing, the lower the concentration of washing water, the more effective the washing will be, but if the amount of water after washing becomes larger than the amount of water for mud making by lowering the concentration, as mentioned above, it will be excessive water. Since it often ends up being disposed of, it cannot be considered as being collected. The present invention was invented with such balance in mind.

8− 循環泥水槽の初期張込泥水を循環して洗浄を継続してゆ
くと循環泥水の濃度は排出硼の土丹を溶解して連続的に
高くなってゆく、第2図は洗浄回収操作の1サイクルの
状況を示すグラフである。すなわち(1)泥水濃度は洗
浄回数の増加と共に高くなってゆき、排出硼の泥水濃度
に漸近線となって近付く。(2)余剰泥水量はl IJ
ング掘削毎(シールドセグメント1リング分が掘削の単
位になっている)に作泥をするものとして計算したもの
で、lリング掘削完了時には1リング分の作泥水を分離
すると2.7−の余剰泥水が発生する。2リング(R)
掘削完了時には2リング分の作泥をするときには2.4
−の余剰泥水が発生する。同様にして5Rを掘削して作
泥するときには余剰泥水をOにすることができる。
8- As the muddy water initially charged in the circulating muddy water tank is circulated and cleaning continues, the concentration of the circulating muddy water becomes higher as it dissolves the mud in the discharge tank. Figure 2 shows the washing and recovery operation. It is a graph showing the situation of one cycle. That is, (1) the concentration of muddy water increases as the number of washings increases, and approaches the concentration of muddy water in the discharge bowl as an asymptote. (2) The amount of surplus muddy water is l IJ
This calculation is based on the assumption that mud is produced every time one ring of shield segment is excavated (the unit of excavation is one ring of shield segment), and when one ring of mud is separated at the completion of one ring excavation, there will be a surplus of 2.7-. Muddy water occurs. 2 rings (R)
2.4 when making mud for 2 rings upon completion of excavation
− Surplus muddy water is generated. Similarly, when excavating 5R and producing mud, excess mud water can be turned into O.

余剰泥水が減少する理由は砂礫の表面付着水が泥分を持
ち出すためで、初期には泥分濃度が低いため砂礫付着泥
分の持ち出しが少く、濃度の上昇に伴って持ち出し量も
増加する。
The reason why the surplus mud water decreases is that the water adhering to the surface of sand and gravel carries out mud.In the initial stage, the mud concentration is low, so less mud is carried out, and as the concentration increases, the amount carried out increases.

この傾向は初期張込み水量の絶体量と地山含水比。This tendency is due to the extreme amount of water initially charged and the water content ratio of the ground.

9− 地山粒度構成時の砂の比率により著しく変化がある。こ
のようにして洗浄することにより。
9- The grain size of the ground changes significantly depending on the ratio of sand in the composition. By washing in this way.

(1)回収率が高いため高価なベントナイト、粘土丹の
使用量が著しく減少し工事費の低減となる。
(1) Due to the high recovery rate, the amount of expensive bentonite and red clay used is significantly reduced, resulting in a reduction in construction costs.

(2)初期と終期の砂礫を混合平均すれば洗浄効果のよ
い砂礫が得られ骨材資源として有効利用できる。
(2) By mixing and averaging the initial and final stages of sand and gravel, sand and gravel with good cleaning effects can be obtained and can be effectively used as an aggregate resource.

(3)排出硼の輸送、捨場などでの二次公害が解決する
(3) Secondary pollution caused by the transportation of waste bottlings, disposal sites, etc. will be resolved.

(4)余剰泥水が発生しないので濾過性の悪いベントナ
イト泥水の処理設備が不要となる。
(4) Since surplus mud water is not generated, there is no need for treatment equipment for bentonite mud water, which has poor filterability.

彦どの利点があり1本発明の効果は非常に大きい。There are several advantages, and the effects of the present invention are very large.

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

第1図は本発明のシールド工法の高濃度泥水回収装置、
第2図は本発明の装置を使用する場合の洗浄リング数と
その余剰泥水量及び泥水濃度との関係を示すグラフであ
る。 l・・・排出礪投入口 2・・・筒本体 3・・・篩下集水樋 4・・・混合循環槽 10− 5・・・循環ポンプ 6・・・液体サイクロン 7・・・泥水循環槽 8・・・ポンプ 9・・・比重計 10.10’・・・下限レベル計 11.11’・・・上限レベル計 12・・・弁 13・・・ポンプ 14・・・回収泥水槽 15・・・粗礫用スクリーン 16・・・細礫用スクリーン 17・・・砂分スクリーン 18・・・流水管 19・・・プール部 20・・・堰板 21・・・管 代理人 弁理士 吉 島 寧 11−
Figure 1 shows a highly concentrated mud water recovery device using the shield method of the present invention.
FIG. 2 is a graph showing the relationship between the number of cleaning rings, the amount of surplus mud water, and the concentration of mud water when using the apparatus of the present invention. l...Discharge basin input port 2...Cylinder body 3...Sieve water collection gutter 4...Mixing circulation tank 10-5...Circulation pump 6...Liquid cyclone 7...Muddy water circulation Tank 8...Pump 9...Hydrometer 10.10'...Lower limit level gauge 11.11'...Upper level gauge 12...Valve 13...Pump 14...Recovered mud water tank 15 ...Gravel screen 16...Fine gravel screen 17...Sand screen 18...Water pipe 19...Pool section 20...Weir board 21...Administrative agent Patent attorney Yoshi Shima Nei 11-

Claims (1)

【特許請求の範囲】[Claims] 上段に砂用スクリーン、下段に粗砂用スクリーンを備え
、該粗砂用スクリーンの石投入部にプール部を設けた振
動篩の下に泥水及びl少す脹合楕4貯留槽を設け、該混
合貯留槽の設゛及び泥水をサイクロンに供給し、サイク
ロンのアンダーフローはるようにしたことを特徴とする
シールド工法の高濃度泥水回収装置。
A sand screen is provided on the upper stage and a coarse sand screen is provided on the lower stage, and a 4-inflated elliptical storage tank for muddy water and l is provided below the vibrating sieve, which has a pool part in the stone input part of the coarse sand screen. A high-concentration muddy water recovery device using the shield method, which is characterized by a mixing storage tank, supplying muddy water to a cyclone, and causing underflow of the cyclone.
JP22212983A 1983-11-28 1983-11-28 Device for recovering high-concentration mud water for shield driving method Pending JPS60114360A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22212983A JPS60114360A (en) 1983-11-28 1983-11-28 Device for recovering high-concentration mud water for shield driving method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22212983A JPS60114360A (en) 1983-11-28 1983-11-28 Device for recovering high-concentration mud water for shield driving method

Publications (1)

Publication Number Publication Date
JPS60114360A true JPS60114360A (en) 1985-06-20

Family

ID=16777618

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22212983A Pending JPS60114360A (en) 1983-11-28 1983-11-28 Device for recovering high-concentration mud water for shield driving method

Country Status (1)

Country Link
JP (1) JPS60114360A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112757470A (en) * 2020-12-31 2021-05-07 中铁工程服务有限公司 Brick-making recycling method for shield muck
CN112794606A (en) * 2020-12-24 2021-05-14 山东大学 Muck treatment system and method for shield

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112794606A (en) * 2020-12-24 2021-05-14 山东大学 Muck treatment system and method for shield
CN112757470A (en) * 2020-12-31 2021-05-07 中铁工程服务有限公司 Brick-making recycling method for shield muck

Similar Documents

Publication Publication Date Title
CN110303033B (en) Shield construction muck treatment system and treatment method
CN103769312A (en) Construction method for processing and recycling slurry shield muck
CN210305011U (en) Shield constructs construction dregs processing system
CN107585838A (en) A kind of sandstone separates Disposal of Sewages
CN210367083U (en) Shield constructs and washs muddy water recovery clean system
CN104858174B (en) Process and system for cleaning waste residues in quarries and building sand
CN218755384U (en) Engineering waste slurry in-situ separation device
JP2002028698A (en) Method and device for separating soil and sand from drilled muddy water
JPS60114360A (en) Device for recovering high-concentration mud water for shield driving method
CN111135949A (en) Method for producing sand by using building waste soil
KR101489713B1 (en) Washing water dehydrator for separating system recycled gravel from wastebuilding products
JP2565482B2 (en) Method and device for treating muddy water and industrial wastewater in muddy water excavation method
CN214183982U (en) Based on quartz sand sieve is washed with high-efficient sieve and is washed device
JP2807657B2 (en) Method and apparatus for treating muddy water and industrial wastewater in muddy water drilling method
JPS6014953A (en) Washing vibrating screen
CN113236157A (en) Drilling pile-forming construction system and working method thereof
JPH1018746A (en) Dual system muddy water treatment method and treatment device
JPH03157154A (en) Vibrating and cleaning screen
CN110304746A (en) A kind of concrete sewage processing recycling and reusing system
JP2000237714A (en) Treatment of waste ready-mixed concrete
CN215292397U (en) Drilling pile-forming construction system
CN212790099U (en) Concrete grit sewage recovery device
JP3798351B2 (en) Surplus mud recycling equipment
KR101320302B1 (en) Method for processing muddy water in the huge tunnel
JP3031912B1 (en) Turbid water treatment system and turbid water treatment method