JP2001212600A - Method for treating dredged sludge - Google Patents

Method for treating dredged sludge

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Publication number
JP2001212600A
JP2001212600A JP2000025051A JP2000025051A JP2001212600A JP 2001212600 A JP2001212600 A JP 2001212600A JP 2000025051 A JP2000025051 A JP 2000025051A JP 2000025051 A JP2000025051 A JP 2000025051A JP 2001212600 A JP2001212600 A JP 2001212600A
Authority
JP
Japan
Prior art keywords
mud
sludge
tank
dredged
screw decanter
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
Application number
JP2000025051A
Other languages
Japanese (ja)
Other versions
JP3783227B2 (en
Inventor
Masao Kuroiwa
正夫 黒岩
Tomoyuki Fukuda
智之 福田
Mitsuteru Sumida
光輝 炭田
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.)
Obayashi Corp
Original Assignee
Obayashi Corp
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 Obayashi Corp filed Critical Obayashi Corp
Priority to JP2000025051A priority Critical patent/JP3783227B2/en
Publication of JP2001212600A publication Critical patent/JP2001212600A/en
Application granted granted Critical
Publication of JP3783227B2 publication Critical patent/JP3783227B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the scale of a dewatering apparatus and to improve the dewatering efficiency of the apparatus. SOLUTION: In a method for treating dredged sludge, the bottom sludge 1 of seas, rivers, lakes, marshes, etc., is dredged by a dredger 2 (Fig. 1 step 101). Next, sludge stored in a raw water tank 4 is dewatered/sorted by an earth-sand separator 5 comprising a vibrating screen and a cyclone (step 2). Next, the cyclone-over portion of the sludge in the separator 5, after being stored temporarily in a drainage raw water tank 21, is sorted by a screw decanter 6, which is a centrifugal separator (step 103). Next, the overflow portion of the sludge in the sorting by the screw decanter is precipitated/separated in a concentration tank 7 (step 104). Next, the concentrated sludge 8 in the tank 7, which has been precipitated by the precipitation/separation, after being stored temporarily in a slurry tank 22, is dewatered by a filter press 9, which is a dewaterer (step 105).

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、海や湖沼あるいは
河川の底から浚渫された泥土の処理方法に関する。
The present invention relates to a method for treating mud dredged from the bottom of a sea, lake, or river.

【0002】[0002]

【従来の技術】海や湖沼あるいは河川の水質汚染が進行
している場合には、かかる水質汚染の進行を阻止して良
好な環境を取り戻すことが生態系維持の観点できわめて
重要である。
2. Description of the Related Art When water pollution of the sea, lakes, or rivers is progressing, it is extremely important from the viewpoint of maintaining an ecosystem to prevent the progress of water pollution and restore a favorable environment.

【0003】水質汚染が進行する原因としては、外部か
らの有機物流入および底泥からの栄養塩の溶出が挙げら
れ、したがって、湖沼の水質を改善するには、その底泥
を浚渫して除去してやるのが効果的である。
[0003] The cause of the progress of water pollution is the inflow of organic matter from the outside and the elution of nutrients from the bottom mud. Therefore, in order to improve the water quality of lakes and marshes, the bottom mud is removed by dredging. Is effective.

【0004】ところが、浚渫された泥土は含水比が高く
て膨大な量となり、そのままでは、処分場所を確保する
ことも再利用することも難しい。そのため、かかる浚渫
泥土の減容化および強度増大を図ることが必要不可欠と
なる。
[0004] However, the dredged mud has a high water content and an enormous amount, and it is difficult to secure a disposal site and reuse it as it is. Therefore, it is essential to reduce the volume and increase the strength of the dredged mud.

【0005】従来、浚渫泥土に凝集剤を添加して土粒子
をあらかじめ凝集させ、しかる後にフィルタープレス等
で脱水を行うことによって減容化を図るとともに、凝集
剤とともに固化材を添加することによって処理土の強度
向上を図っていた。
Conventionally, a flocculant is added to a dredged mud to coagulate soil particles in advance, and then dewatering is performed by a filter press or the like to reduce the volume, and a treatment is performed by adding a solidifying material together with the flocculant. Improving the strength of the soil.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、含水比
が高い浚渫泥土を一定の割合まで減容化させるとともに
その強度を向上させるには、大量の凝集剤および固化材
が必要となり、材料コストが高くつくという問題や、フ
ィルタープレス等の脱水装置を用いた場合、全体の設備
費用が高くなるとともに、広い設置スペースを確保せね
ばならないという問題を生じる。
However, in order to reduce the volume of the dredged mud having a high water content to a certain ratio and to improve its strength, a large amount of a coagulant and a solidifying material are required, and the material cost is high. If a dewatering device such as a filter press is used, the overall equipment cost increases and a wide installation space must be secured.

【0007】そこで、本出願人は、新たな浚渫泥土の処
理方法を開発し(特開平 9-155395号公報参照)、脱水
設備の設備規模の縮小及び凝集剤や固化材の使用量の節
約を図ることに成功した。
Accordingly, the present applicant has developed a new method for treating dredged mud (see Japanese Patent Application Laid-Open No. 9-155395) to reduce the scale of dewatering equipment and to save the amount of coagulant and solidified material used. I succeeded in planning.

【0008】しかしながら、かかる処理方法は、スクリ
ューデカンタのオーバーフロー分を全量脱水処理するも
のであったため、脱水処理すべき量を減容化するにはど
うしても限度があるとともに、オーバーフロー分である
がゆえに濃度が低く、脱水効率も悪いという問題を生じ
ていた。
[0008] However, such a treatment method involves dehydrating the entire amount of the overflow of the screw decanter. Therefore, there is a limit to reducing the volume to be dehydrated, and the concentration of the overflow due to the overflow is limited. And the dewatering efficiency is low.

【0009】本発明は、上述した事情を考慮してなされ
たもので、脱水設備の規模を大幅に縮小させるとともに
脱水効率を向上させることが可能な浚渫泥土の処理方法
を提供することを目的とする。
The present invention has been made in view of the above-mentioned circumstances, and has as its object to provide a method for treating dredged mud which can greatly reduce the scale of a dewatering facility and improve the dewatering efficiency. I do.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するた
め、本発明に係る浚渫泥土の処理方法は請求項1に記載
したように、海、河川、湖沼などの底泥を浚渫し、浚渫
された泥土を遠心分離によって分級処理し、該分級処理
でオーバーフローした分を沈降分離し、しかる後、該沈
降分離で沈降した濃縮泥を所定の方法で脱水処理するも
のである。
In order to achieve the above object, a method for treating dredged mud according to the present invention is to dredge bottom mud such as seas, rivers, lakes and marshes and to draw the dredged mud. The sludge thus obtained is classified by centrifugation, the portion overflowed by the classification is sedimented and separated, and then the concentrated mud settled by the sedimentation is dehydrated by a predetermined method.

【0011】本発明に係る浚渫泥土の処理方法において
は、含水比の高い浚渫泥土をあらかじめ遠心分離によっ
て分級するが、該分級処理でオーバーフローした分を全
量脱水処理するのではなく、該オーバーフロー分を沈降
分離し、しかる後、該沈降分離で沈降した濃縮泥を所定
の方法で脱水処理する。
In the method for treating dredged mud according to the present invention, the dredged mud having a high water content is classified in advance by centrifugal separation. After sedimentation and separation, the concentrated mud sedimented by the sedimentation is dehydrated by a predetermined method.

【0012】このようにすると、脱水処理すべき量は、
本出願人が先に開発した浚渫泥土の処理方法(特開平 9
-155395号公報)に比べて、1/2〜1/10にまで減
容化される。また、脱水処理される濃縮泥の比重は、上
述したオーバーフロー分よりも大きくなるため、脱水効
率も向上する。
Thus, the amount to be dehydrated is:
A method of treating dredged mud previously developed by the present applicant (Japanese Unexamined Patent Application Publication No.
-155395), the volume is reduced to 1/2 to 1/10. In addition, the specific gravity of the concentrated mud to be dehydrated is larger than the above-mentioned overflow, so that the dewatering efficiency is also improved.

【0013】脱水処理方法は、フィルタープレス等の加
圧脱水方式を採用してもよいし、スクリューデカンタ等
の遠心分離方式を採用してもよい。ちなみに、後者の方
法によれば、設備規模をさらにコンパクトにすることが
可能となる。
The dewatering method may be a pressure dehydration method such as a filter press, or a centrifugal separation method such as a screw decanter. Incidentally, according to the latter method, it is possible to further reduce the equipment scale.

【0014】[0014]

【発明の実施の形態】以下、本発明に係る浚渫泥土の処
理方法の実施の形態について、添付図面を参照して説明
する。なお、従来技術と実質的に同一の部品等について
は同一の符号を付してその説明を省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a method for treating dredged mud according to the present invention will be described below with reference to the accompanying drawings. It is to be noted that the same reference numerals are given to components and the like that are substantially the same as those in the conventional technology, and description thereof will be omitted.

【0015】図1は、本実施形態に係る浚渫泥土の処理
方法の流れを示したフローチャート、図2及び図3は、
同じく設備構成図である。これらの図でわかるように、
本実施形態に係る浚渫泥土の処理方法は、まず、海、河
川、湖沼などの底泥1を浚渫船2によって浚渫する(図
1、ステップ101)。浚渫された底泥1は、スクリー
ン3でレキ分等の異物を取り除いた後、原水槽4に貯留
しておく。
FIG. 1 is a flow chart showing the flow of a method for treating dredged mud according to the present embodiment, and FIGS.
FIG. As you can see in these figures,
In the method for treating dredged mud according to the present embodiment, first, bottom mud 1 such as the sea, a river, a lake or the like is dredged by a dredger 2 (FIG. 1, step 101). The dredged bottom mud 1 is stored in a raw water tank 4 after removing foreign matters such as recreation by a screen 3.

【0016】次に、原水槽4に貯留された泥土を振動ふ
るい及びサイクロンからなる土砂分離装置5で脱水分級
処理する(ステップ102)。
Next, the mud stored in the raw water tank 4 is subjected to dewatering and classification by a sediment separating apparatus 5 comprising a vibrating sieve and a cyclone (step 102).

【0017】次に、土砂分離装置5のサイクロンオーバ
ー分を排水原水槽21にいったん貯留した後、遠心分離
機であるスクリューデカンタ6で分級処理する(ステッ
プ103)。分級処理で生じたアンダー分は、ケーキと
して排出する。
Next, after the cyclone excess of the earth and sand separation device 5 is temporarily stored in the raw water tank 21, the classification process is performed by the screw decanter 6, which is a centrifugal separator (step 103). The under part generated in the classification process is discharged as cake.

【0018】次に、スクリューデカンタ6による分級処
理でオーバーフローした分を濃縮槽7に入れ、該濃縮槽
内で沈降分離する(ステップ104)。濃縮槽7の上澄
み水については、必要に応じて後述するpH調整槽14
でpH調整し、しかる後、元の水域に放流する。
Next, the portion which has overflowed in the classification process by the screw decanter 6 is put into the concentration tank 7 and settled and separated in the concentration tank (step 104). About the supernatant water of the concentration tank 7, a pH adjustment tank
The pH is adjusted with, and then discharged into the original water area.

【0019】次に、沈降分離で沈降した濃縮槽7内の濃
縮泥8をスラリー槽22にいったん貯留し、必要に応じ
て凝集剤を添加した後、脱水機であるフィルタープレス
9で脱水処理する(ステップ105)。脱水処理で生じ
たアンダー分は、ケーキとして排出する。
Next, the concentrated mud 8 in the concentration tank 7 settled by the sedimentation separation is once stored in the slurry tank 22, and a coagulant is added as required, and then dewatered by a filter press 9 which is a dehydrator. (Step 105). The under part generated in the dehydration treatment is discharged as cake.

【0020】なお、脱水処理でオーバーフローした分に
ついては、ろ水槽10にいったん貯留した後、無機凝集
剤タンク11に収容された無機凝集剤および高分子溶解
貯蔵タンク12に貯蔵された高分子凝集剤を添加して角
形シックナ13で凝集沈降させるとともに、その上澄み
分をpH調整槽14で中和して放流し、凝集沈降分を濃
縮槽7に戻す(ステップ106)。
The portion overflowed during the dehydration treatment is once stored in the drainage tank 10 and then stored in the inorganic coagulant tank 11 and the polymer coagulant stored in the polymer dissolution storage tank 12. Is added to cause coagulation and sedimentation in the square thickener 13, and the supernatant is neutralized in the pH adjustment tank 14 and discharged, and the coagulation and sediment is returned to the concentration tank 7 (step 106).

【0021】ここで、無機凝集剤としては、硫酸バンド
やPACと呼ばれるポリ塩化アルミニウム等を使用し、
高分子凝集剤としては、水溶性ポリアクリルアミドから
製造された市販品から適宜選択することができる。
Here, as the inorganic coagulant, a sulfate band or polyaluminum chloride called PAC is used.
The polymer flocculant can be appropriately selected from commercial products produced from water-soluble polyacrylamide.

【0022】以上説明したように、本実施形態に係る浚
渫泥土の処理方法によれば、スクリューデカンタ6によ
る分級処理でオーバーフローした分を全量脱水処理する
のではなく、該オーバーフロー分を濃縮槽7にて沈降分
離し、しかる後、該沈降分離で沈降した濃縮泥8を脱水
処理するようにしたので、フィルタープレス9で必要と
なる脱水処理量を、本出願人が先に開発した浚渫泥土の
処理方法(特開平 9-155395号公報)に比べて、1/2
〜1/10にまで減容化することが可能となるととも
に、脱水処理される対象が濃縮泥8であるため、スクリ
ューデカンタからのオーバーフロー分を直接脱水処理す
る場合に比べて脱水処理対象物、すなわち濃縮泥8の比
重を大きくすることが可能となり、フィルタープレス9
での脱水効率が飛躍的に向上する。
As described above, according to the method for treating dredged mud according to the present embodiment, not the entire amount of the overflow caused by the classification by the screw decanter 6 is dehydrated, but the overflow is stored in the concentration tank 7. Then, the concentrated mud 8 settled by the sedimentation is subjected to dehydration treatment. Therefore, the amount of dehydration treatment required by the filter press 9 is reduced by the dredging mud treatment previously developed by the present applicant. Method (Japanese Patent Laid-Open No. 9-155395)
It is possible to reduce the volume to 〜 1/10, and since the object to be dewatered is the concentrated mud 8, the object to be dewatered compared to the case where the overflow from the screw decanter is directly dewatered, That is, it is possible to increase the specific gravity of the concentrated mud 8, and the filter press 9
The efficiency of dehydration in the system is dramatically improved.

【0023】そのため、脱水機であるフィルタープレス
9の規模を大幅に縮小することができるとともに、それ
に伴って設備のイニシャルコストの低減及び設置スペー
スの縮小を図ることが可能となる。
As a result, the scale of the filter press 9 as a dehydrator can be significantly reduced, and the initial cost of equipment and the installation space can be reduced accordingly.

【0024】次に、本実施形態に係る浚渫泥土の処理方
法の作用効果を確認する実験を行ったので、その概要に
ついて以下に説明する。
Next, an experiment was conducted to confirm the operation and effect of the method for treating dredged mud according to the present embodiment, and the outline thereof will be described below.

【0025】実験には、土粒子比重が2.6の浚渫泥土
を使用し、上述の手順で浚渫泥土を処理した。結果を表
1に示す。
In the experiment, dredged mud having a specific gravity of soil particles of 2.6 was used, and the dredged mud was treated according to the above-described procedure. Table 1 shows the results.

【0026】[0026]

【表1】 [Table 1]

【0027】ここで、同表中、ρSIはスクリューデカン
タの供給側での比重、ρSOFは同じくオーバーフロー側
での比重をそれぞれ示し、C1はスクリューデカンタか
らのオーバーフロー分に対する濃縮泥の容量比、C
2は、スクリューデカンタへの供給分に対する濃縮泥の
容量比をそれぞれ示す。また、濃縮泥の比重は、スクリ
ューデカンタの供給側での比重に依存せず、約1.16
となった。
In the table, ρ SI indicates the specific gravity at the supply side of the screw decanter, ρ SOF indicates the specific gravity at the overflow side, and C 1 indicates the volume ratio of the concentrated mud to the overflow from the screw decanter. , C
2 shows the volume ratio of the concentrated mud to the amount supplied to the screw decanter, respectively. The specific gravity of the concentrated mud does not depend on the specific gravity on the supply side of the screw decanter, but is about 1.16.
It became.

【0028】以上の結果から、容量比C2(濃縮泥の容
量/スクリューデカンタへの供給分の容量)、すなわち
脱水処理前での減容化率は、10.5〜33.3%(1
/10〜1/3)となることがわかる。また、脱水処理
前での比重1.16は、オーバーフロー側での比重ρ
SOFよりも上回っていることがわかる。
From the above results, the volume ratio C 2 (volume of concentrated mud / volume supplied to the screw decanter), that is, the volume reduction rate before the dehydration treatment is 10.5 to 33.3% (1
/ 10 to 1/3). The specific gravity 1.16 before the dehydration treatment is the specific gravity ρ on the overflow side.
It turns out that it is higher than SOF .

【0029】本実施形態では、スクリューデカンタ6に
よる分級処理でオーバーフローした分をそのまま濃縮槽
7に入れて沈降分離させるようにしたが、スクリューデ
カンタ6のオーバーフロー分に無機凝集剤(PAC)や
消石灰を添加して沈降分離の促進を図るようにしてもよ
い。
In the present embodiment, the portion overflowed in the classification treatment by the screw decanter 6 is directly placed in the concentration tank 7 for sedimentation and separation. However, an inorganic flocculant (PAC) or slaked lime is added to the overflow of the screw decanter 6. It may be added to promote sedimentation and separation.

【0030】[0030]

【発明の効果】以上述べたように、本発明の浚渫泥土の
処理方法によれば、脱水処理を行う工程での脱水処理量
を大幅に減容化することが可能となるとともに、脱水処
理される対象が濃縮泥であるため、遠心分離工程後のオ
ーバーフロー分を直接脱水処理する場合に比べて、脱水
処理対象物、すなわち濃縮泥の比重を大きくすることが
可能となり、脱水処理工程での脱水効率が飛躍的に向上
する。
As described above, according to the method for treating dredged mud according to the present invention, it is possible to greatly reduce the amount of dewatering treatment in the step of performing dehydration treatment, and at the same time, to carry out dehydration treatment. Since the object to be concentrated is concentrated mud, the specific gravity of the substance to be dehydrated, that is, the concentrated mud, can be increased as compared with the case where the overflow component after the centrifugation step is directly dehydrated. The efficiency is dramatically improved.

【0031】[0031]

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

【図1】本実施形態に係る浚渫泥土の処理方法の流れを
示したフローチャート。
FIG. 1 is a flowchart showing a flow of a method for treating dredged mud according to the present embodiment.

【図2】本実施形態に係る浚渫泥土の処理方法を実施す
るための設備構成図。
FIG. 2 is an equipment configuration diagram for carrying out a method for treating dredged mud according to the present embodiment.

【図3】同じく本実施形態に係る浚渫泥土の処理方法を
実施するための設備構成図。
FIG. 3 is an equipment configuration diagram for implementing the dredging mud treatment method according to the embodiment.

【符号の説明】[Explanation of symbols]

1 底泥 6 スクリューデカンタ(遠心分離によ
る分級処理を行う設備) 7 濃縮槽(沈降分離を行う設備) 8 濃縮泥 9 フィルタープレス(脱水処理を行う
設備)
1 bottom mud 6 screw decanter (equipment for classifying by centrifugation) 7 thickening tank (equipment for sedimentation) 8 thickened mud 9 filter press (equipment for dewatering)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 炭田 光輝 東京都清瀬市下清戸4丁目640 株式会社 大林組技術研究所内 Fターム(参考) 4D059 AA09 BE16 BE31 BE38 BE39 BE49 BE55 BE56 BK30 CA24 CA25 DA05 DA16 DA17 DB24 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Mitsuteru Sumita 4-640 Shimoseito, Kiyose-shi, Tokyo F-term in Obayashi Corporation Research Laboratory Co., Ltd. 4D059 AA09 BE16 BE31 BE38 BE39 BE49 BE55 BE56 BK30 CA24 CA25 DA05 DA16 DA17 DB24

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 海、河川、湖沼などの底泥を浚渫し、浚
渫された泥土を遠心分離によって分級処理し、該分級処
理でオーバーフローした分を沈降分離し、しかる後、該
沈降分離で沈降した濃縮泥を所定の方法で脱水処理する
ことを特徴とする浚渫泥土の処理方法。
1. Dredging of sediment in the sea, river, lake, marsh, etc., classification of the dredged mud by centrifugal separation, sedimentation and separation of the overflowed part by the classification, and sedimentation by sedimentation A method for treating dredged mud, wherein the concentrated mud is dewatered by a predetermined method.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030064901A (en) * 2002-01-29 2003-08-06 주식회사 천보환경 Construction aggrigate production method and systems of river dredged soils
KR100440197B1 (en) * 2001-06-19 2004-07-14 산양환경산업 주식회사 The System of for the using Recycled of Dredged Soils
KR100859874B1 (en) 2008-04-16 2008-09-24 (주)케이디에스 Method and treatment apparatus of dredged sediment
KR100863349B1 (en) 2008-04-16 2008-10-15 (주)케이디에스 Method and treatment apparatus of dredged sediment
KR100942444B1 (en) 2008-01-31 2010-02-17 우진개발 주식회사 Sludge handling method utilyzing a dredging vessel
KR101030581B1 (en) * 2010-06-28 2011-04-21 남선개발 주식회사 Dredging soil treating system
JP2014018774A (en) * 2012-07-23 2014-02-03 Toa Harbor Works Co Ltd Method and system for processing earth and sand
JP2016023426A (en) * 2014-07-17 2016-02-08 初雁興業株式会社 Dredging system
CN110156292A (en) * 2019-05-29 2019-08-23 中清深利(深圳)科技有限公司 A kind of slurry dewatering solidifying and resource utilization method

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CN106237708A (en) * 2016-09-23 2016-12-21 苏州三体智能科技有限公司 A kind of Coal Preparation Plant coal slime dewatering system and method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100440197B1 (en) * 2001-06-19 2004-07-14 산양환경산업 주식회사 The System of for the using Recycled of Dredged Soils
KR20030064901A (en) * 2002-01-29 2003-08-06 주식회사 천보환경 Construction aggrigate production method and systems of river dredged soils
KR100942444B1 (en) 2008-01-31 2010-02-17 우진개발 주식회사 Sludge handling method utilyzing a dredging vessel
KR100859874B1 (en) 2008-04-16 2008-09-24 (주)케이디에스 Method and treatment apparatus of dredged sediment
KR100863349B1 (en) 2008-04-16 2008-10-15 (주)케이디에스 Method and treatment apparatus of dredged sediment
KR101030581B1 (en) * 2010-06-28 2011-04-21 남선개발 주식회사 Dredging soil treating system
JP2014018774A (en) * 2012-07-23 2014-02-03 Toa Harbor Works Co Ltd Method and system for processing earth and sand
JP2016023426A (en) * 2014-07-17 2016-02-08 初雁興業株式会社 Dredging system
CN110156292A (en) * 2019-05-29 2019-08-23 中清深利(深圳)科技有限公司 A kind of slurry dewatering solidifying and resource utilization method

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