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JPH0426008B2 - - Google Patents
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JPH0426008B2 - - Google Patents

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Publication number
JPH0426008B2
JPH0426008B2 JP60259746A JP25974685A JPH0426008B2 JP H0426008 B2 JPH0426008 B2 JP H0426008B2 JP 60259746 A JP60259746 A JP 60259746A JP 25974685 A JP25974685 A JP 25974685A JP H0426008 B2 JPH0426008 B2 JP H0426008B2
Authority
JP
Japan
Prior art keywords
continues
supplied
mud
muddy water
flocculant
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.)
Expired - Lifetime
Application number
JP60259746A
Other languages
Japanese (ja)
Other versions
JPS62121241A (en
Inventor
Sakae Hatayama
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.)
IKEHARA KOGYO KK
Original Assignee
IKEHARA KOGYO KK
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 IKEHARA KOGYO KK filed Critical IKEHARA KOGYO KK
Priority to JP25974685A priority Critical patent/JPS62121241A/en
Publication of JPS62121241A publication Critical patent/JPS62121241A/en
Publication of JPH0426008B2 publication Critical patent/JPH0426008B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は浚渫した泥水を有用な土砂に連続的
に処理できる浚渫処理装置に関し、特に貯水池の
浚渫処理に最適に利用できる浚渫処理装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a dredging processing device that can continuously process dredged muddy water into useful earth and sand, and particularly relates to a dredging processing device that can be optimally used for dredging a reservoir.

(従来の技術、発明が解決しようとする問題点) 従来よりこの種の浚渫処理手段、例えば、貯水
池の浚渫処理手段として、次のようなものがあ
る。
(Prior Art, Problems to be Solved by the Invention) Conventionally, there have been the following types of dredging processing means of this type, for example, as a dredging processing means for a reservoir.

第1に、貯水池を干してその土砂を浚い、トラ
ツクにより搬出する手段である。
The first method is to dry the reservoir, dredge up the soil, and transport it out by truck.

しかし、この手段は断水しなければならない
こと、断水後に貯水池内の土砂の乾燥期間を必
要とすること、その土砂は含水率が多い為、ト
ラツクによる搬送中、泥水が漏れて道路を汚すこ
と、等の問題点がある。
However, this method requires a water outage, requires a drying period for the sediment in the reservoir after the water outage, and because the sediment has a high moisture content, muddy water leaks during transport by truck and pollutes the roads. There are other problems.

第2の手段としては浚渫船により浚渫し、その
泥水を沈澱池に搬出して処理する手段である。
The second method is to dredge with a dredger and transport the muddy water to a settling pond for treatment.

しかし、この第2の手段は浚渫船の搬入が出
来ないと使用不可能であること、貯水池の近く
に沈澱池がないと使用できないこと、一定期間
経過後でなければ沈澱池の土砂を搬出できないこ
と等の問題点がある。
However, this second method cannot be used unless a dredger can be brought in, it cannot be used unless there is a sedimentation pond near the reservoir, and the sediment in the sedimentation pond cannot be removed until a certain period of time has elapsed. There are other problems.

(問題点を解決する為の手段) そこで、この発明は前記従来の問題点を解決す
る為に、ジエツト噴射による堆積土砂の掘削及び
サンドポンプによる吸い上げを同時に行ない続け
るラダーサクシヨンポンプ船と、このポンプ船か
ら延びるサンドポンプ用吐出配管の吐出口より吐
出された泥水が供給され続けると共にその泥水中
の粗粒と細粒を除去し続ける振動フルイ及び分級
機と、これらの振動フルイ及び分級機により粗粒
と細粒とが除去された泥水が供給され続けると共
にその供給される泥水を攪拌し続ける原泥槽と、
原泥槽から遠心分離機に泥水を供給し続ける輸泥
管の途中から高分子凝集剤を自動的に添加し続け
て輸送中に均一に混合させる凝集剤供給装置と、
前記原泥槽内での攪拌により濃度が均一化され、
且つ、凝集剤供給装置により凝集剤が添加された
泥水が供給され続けると共にその供給される泥水
の強制的な固液分離と高分子凝集剤によるフロツ
ク生成とが同時進行しながら固液夫々を排出し続
ける遠心分離機とを有する浚渫処理装置に関す
る。
(Means for Solving the Problems) Therefore, in order to solve the above-mentioned conventional problems, the present invention provides a ladder suction pump ship that simultaneously excavates accumulated soil by jet injection and sucks it up by a sand pump. A vibrating sieve and a classifier that continue to supply muddy water discharged from the discharge port of a sand pump discharge pipe extending from a pump ship and that continue to remove coarse particles and fine particles from the muddy water, and these vibrating sieves and classifiers. a raw mud tank that continues to be supplied with muddy water from which coarse particles and fine grains have been removed, and that continues to stir the supplied muddy water;
A flocculant supply device that automatically continues to add polymer flocculant from the middle of the slurry pipe that continues to supply mud water from the raw mud tank to the centrifuge, and mixes it uniformly during transportation;
The concentration is made uniform by stirring in the raw mud tank,
In addition, the flocculant supply device continues to supply the muddy water to which the flocculant has been added, and the forced solid-liquid separation of the supplied muddy water and the generation of flocs by the polymer flocculant proceed simultaneously while discharging each solid-liquid. The present invention relates to a dredging processing device having a centrifugal separator that continues to operate.

(実施例) 以下、この発明に係る浚渫処理装置の最適な実
施例を図面に基づいて説明する。
(Example) Hereinafter, an optimal example of the dredging processing apparatus according to the present invention will be described based on the drawings.

図中1はラダーサクシヨンポンプ船である。こ
のポンプ船1は、船体2、サンドポンプ3、主モ
ーター4、ジエツトポンプ5、ジエツトポンプ用
モーター6、ウインチ7,8、発電機9、操作室
10、ラダー11、吸入調節カバー付のサクシヨ
ンヘツド12、吸入管13、ジエツトエゼクタ管
14、ジエツトエゼクタ用バルブ15、分水管1
6、サンドポンプ用吐出配管17、サンドポンプ
用吸入配管18、ジエツトポンプ用吐出配管1
9、ジエツトポンプ用吸入配管20等を備えてい
る。
1 in the figure is a rudder suction pump ship. This pump ship 1 includes a hull 2, a sand pump 3, a main motor 4, a jet pump 5, a jet pump motor 6, winches 7 and 8, a generator 9, an operation room 10, a rudder 11, a suction head 12 with a suction adjustment cover, and a suction head 12 with a suction adjustment cover. Pipe 13, jet ejector pipe 14, jet ejector valve 15, water distribution pipe 1
6. Sand pump discharge pipe 17, sand pump suction pipe 18, jet pump discharge pipe 1
9, is equipped with a suction pipe 20 for a jet pump, etc.

そして、このポンプ船1は自由端が所定個所に
固定されるワイヤー21をウインチ操作すること
により水面上を自在に移動できる。
The pump boat 1 can move freely on the water surface by winching a wire 21 whose free end is fixed at a predetermined location.

又、ポンプ船1は前記ジエツトポンプ5で吸い
上げられた水をサクシヨンヘツド1でジエツト噴
射し水底の堆積土砂を掘削することと、その泥水
をサンドポンプ3で吸い上げることを同時に行な
い続け、サンドポンプ用吐出配管17を通じて移
送し、その吐出口22より泥水を吐出し続ける。
In addition, the pump ship 1 continues to jet the water sucked up by the jet pump 5 through the suction head 1 to excavate accumulated sediment at the bottom of the water, and simultaneously sucks up the muddy water with the sand pump 3, and connects the sand pump discharge piping. 17, and continues to discharge muddy water from its discharge port 22.

図中23はその泥水を受ける2段の振動フル
イ、24はグランベル分級機である。前記吐出口
22より吐出された泥水はそれらの振動フルイ2
3、グランベル分級機24の順に供給される。そ
して、前記振動フルイ23は泥水中の粗粒25を
除去し、又、前記グランベル分級機24は粗粒が
除去された後の泥水中の細粒26を除去し、その
細粒26はベルトコンベアー27により所定の場
所に搬送される。
In the figure, 23 is a two-stage vibrating sieve that receives the muddy water, and 24 is a Granbell classifier. The muddy water discharged from the discharge port 22 is passed through the vibrating sieve 2.
3. Granbell classifier 24 is supplied in this order. The vibrating sieve 23 removes coarse particles 25 from the muddy water, and the Granbell classifier 24 removes fine particles 26 from the muddy water after the coarse particles have been removed. 27 to a predetermined location.

又、図中28は濃縮タンクである。この濃縮タ
ンク28には前記粗粒及び細粒が除去された泥水
(5mm以下の微粒状の泥水)が供給され続け、そ
して、攪拌され、ポンプ29により原泥槽30へ
供給され続ける。この原泥槽30に供給された泥
水は更に攪拌され濃度が均一化されながら、ポン
プ31により輸泥管を通つて遠心分離機32に供
給され続ける。
Further, 28 in the figure is a concentration tank. Mud water from which the coarse particles and fine particles have been removed (mud water in the form of fine particles of 5 mm or less) is continuously supplied to the thickening tank 28 , and is continued to be stirred and supplied to the raw mud tank 30 by the pump 29 . The mud water supplied to the raw mud tank 30 is further stirred to have a uniform concentration, and continues to be supplied to the centrifugal separator 32 through the mud infusion pipe by the pump 31.

図中33は石灰溶解槽である。この石灰溶解槽
33は原泥槽30から遠心分離機32に供給され
る途中の泥水に石灰を添加し続ける。つまり、泥
水が酸性である場合にそのPHを調整する為のもの
である。
33 in the figure is a lime dissolution tank. This lime dissolving tank 33 continues to add lime to the mud water that is being supplied from the raw mud tank 30 to the centrifugal separator 32. In other words, it is used to adjust the pH of muddy water if it is acidic.

又、図中34は凝集剤供給装置である。この凝
集剤供給装置34は原泥槽30から遠心分離機3
2に供給され続ける泥水に輸泥管の途中から高分
子凝集剤を自動的に添加し続ける。高分子凝集剤
と泥水は輸送される内に管内で均一に混合され
る。遠心分離機32に於ける分離効率を向上させ
る為に高分子凝集剤を添加するものである。
Further, numeral 34 in the figure is a flocculant supply device. This flocculant supply device 34 is connected from the raw mud tank 30 to the centrifugal separator 3.
The polymer flocculant continues to be automatically added to the muddy water continuously supplied from the middle of the mud infusion pipe. The polymer flocculant and muddy water are uniformly mixed within the pipe while being transported. A polymer flocculant is added to improve the separation efficiency in the centrifugal separator 32.

尚、図中35は高分子凝集剤溶解装置、36は
高分子凝集剤溶解槽、37はホツパー、38はコ
ンプレツサー、39はエアードライヤー、40は
ポンプ、41は洗浄水供給管を夫々示す。
In the figure, 35 is a polymer flocculant dissolving device, 36 is a polymer flocculant dissolving tank, 37 is a hopper, 38 is a compressor, 39 is an air dryer, 40 is a pump, and 41 is a washing water supply pipe.

又、前記遠心分離機32には前述のように石灰
や高分子凝集剤等が添加された泥水が供給され続
け、そして分離機内で、遠心力による機械的強制
脱水と高分子凝集剤による化学的フロツク生成脱
水が同時に効率的に行なわれる。泥水を固形物と
液体とに強制分離しながら夫々を排出し続ける。
固形物は回転する遠心分離機32内周壁に貼付い
て脱水され液体は遠心分離機32から排出され
る。固形物は遠心分離機32の内周壁に内接して
回転するスクリユータイプの固形物排出装置49
により排出され続ける。排出された固形物42は
ベルトコンベアー43で所定の場所に搬送され
る。又、液体は分離液用管44を通じて分離液槽
45に供給され、ポンプ46により貯水池等に還
元される。
Furthermore, the centrifugal separator 32 continues to be supplied with muddy water to which lime, a polymer flocculant, etc. have been added as described above, and inside the separator, forced mechanical dehydration by centrifugal force and chemical dehydration by the polymer flocculant are carried out in the separator. Flock generation and dehydration are simultaneously carried out efficiently. The muddy water is forcibly separated into solids and liquids while continuing to discharge each.
The solids stick to the inner peripheral wall of the rotating centrifuge 32 and are dehydrated, and the liquid is discharged from the centrifuge 32. The solid matter is removed by a screw-type solid matter discharge device 49 that rotates while being inscribed in the inner circumferential wall of the centrifugal separator 32.
continues to be emitted. The discharged solid matter 42 is conveyed to a predetermined location by a belt conveyor 43. Further, the liquid is supplied to a separated liquid tank 45 through a separated liquid pipe 44, and is returned to a reservoir or the like by a pump 46.

又、図中47は前記遠心分離機32の冷却の為
の冷却水を供給する冷却水用管、48はその冷却
能力を失つた冷却水を排出する為の排出管を夫々
示す。
Further, in the figure, 47 indicates a cooling water pipe for supplying cooling water for cooling the centrifugal separator 32, and 48 indicates a discharge pipe for discharging the cooling water that has lost its cooling ability.

(効果) 以上のように構成されたこの発明に係る浚渫処
理装置は、ラダーサクシヨンポンプ船による堆積
土砂の掘削、その泥水の吸い上げ、サンドポンプ
用吐出配管を通じての泥水の振動フルイ及び分級
機のへの供給、これらの振動フルイ及び分級機に
よる泥水中の粗粒と細粒の除去、粗粒と細粒とが
除去された泥水の原泥槽内での攪拌、その攪拌に
よる濃度の均一化、凝集剤供給装置による原泥槽
と遠心分離機を結ぶ輸泥管の途中から泥水中への
凝集剤の添加、輸泥管による輸送中に泥水と高分
子凝集剤が均一に混合、遠心分離機内で固形物と
液体との強制分離とフロツク生成の同時進行、固
液分離しながらの夫々の排出と云う連続した工程
により、貯水池等の堆積土砂を効率的に浚渫処理
できる。しかも、全工程を切目なく運転して連続
した処理をすることができると云う特有の効果を
奏する。
(Effects) The dredging treatment device according to the present invention configured as described above is capable of excavating accumulated earth and sand using a ladder suction pump boat, sucking up the muddy water, using a vibration sieve for the muddy water through the sand pump discharge piping, and using a classifier. Removal of coarse and fine particles from the muddy water using these vibrating sieves and classifiers, stirring of the muddy water from which the coarse and fine grains have been removed in the raw mud tank, and homogenization of the concentration through the stirring. The flocculant is added to the mud from the middle of the mud pipe connecting the raw mud tank and the centrifuge using the flocculant supply device, and the mud and polymer flocculant are uniformly mixed during transportation through the mud pipe and centrifuged. The continuous process of forcibly separating solids and liquids, simultaneously producing flocs, and discharging each while separating solids and liquids allows for efficient dredging of sediments in reservoirs, etc. In addition, it has the unique effect of being able to run all the processes seamlessly and perform continuous processing.

従つて、従来のこの種の浚渫処理手段を解消す
ることができる浚渫処理装置として、極めて有効
に利用することができるものである。
Therefore, it can be used extremely effectively as a dredging processing device that can eliminate the need for conventional dredging processing means of this type.

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

図面はこの発明に係る浚渫処理装置の実施例を
示し、第1図は平面図、第2図は立体図である。 図中の主な符号の説明、1……ラダーサクシヨ
ンポンプ船、3……サンドポンプ、17……サン
ドポンプ用吐出配管、22……吐出口、23……
振動フルイ、24……分級機、30……原泥槽、
34……凝集剤供給装置、32……遠心分離機。
The drawings show an embodiment of the dredging processing apparatus according to the present invention, with FIG. 1 being a plan view and FIG. 2 being a three-dimensional view. Explanation of main symbols in the diagram: 1...Ladder suction pump ship, 3...Sand pump, 17...Discharge piping for sand pump, 22...Discharge port, 23...
Vibrating sieve, 24... Classifier, 30... Raw mud tank,
34...Flocculant supply device, 32...Centrifugal separator.

Claims (1)

【特許請求の範囲】[Claims] 1 ジエツト噴射による堆積土砂の掘削及びサン
ドポンプによる吸い上げを同時に行ない続けるラ
ダーサクシヨンポンプ船と、このポンプ船から延
びるサンドポンプ用吐出配管の吐出口より吐出さ
れた泥水が供給され続けると共にその泥水中の粗
粒と細粒を除去し続ける振動フルイ及び分級機
と、これらの振動フルイ及び分級機により粗粒と
細粒とが除去された泥水が供給され続けると共に
その供給される泥水を攪拌し続ける原泥槽と、原
泥槽から遠心分離機に泥水を供給し続ける輸泥管
の途中から高分子凝集剤を自動的に添加し続けて
輸送中に均一に混合させる凝集剤供給装置と、前
記原泥槽内での攪拌により濃度が均一化され、且
つ、凝集剤供給装置により凝集剤が添加された泥
水が供給され続けると共にその供給される泥水の
強制的な固液分離と高分子凝集剤によるフロツク
生成とが同時進行しながら固液夫々を排出し続け
る遠心分離機とを有する浚渫処理装置。
1. A ladder suction pump ship that continues to simultaneously excavate accumulated soil by jet injection and suck it up by a sand pump, and muddy water discharged from the outlet of the sand pump discharge pipe extending from this pump ship continues to be supplied, and the muddy water continues to be supplied. vibrating sieves and classifiers that continue to remove coarse particles and fine particles; muddy water from which coarse particles and fine particles have been removed by these vibrating sieves and classifiers continues to be supplied, and the supplied muddy water continues to be stirred. A flocculant supply device that automatically continues to add a polymer flocculant from the middle of a raw mud tank and a mud transfer pipe that continues to supply mud water from the raw mud tank to a centrifugal separator and mixes it uniformly during transportation; The concentration is made uniform by stirring in the raw mud tank, and the flocculant-added mud water is continuously supplied by the flocculant supply device, and the supplied mud is forced to undergo solid-liquid separation and polymer flocculant. This dredging treatment equipment includes a centrifugal separator that continues to discharge each solid and liquid while simultaneously producing flocs.
JP25974685A 1985-11-21 1985-11-21 Dredging treatment apparatus Granted JPS62121241A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25974685A JPS62121241A (en) 1985-11-21 1985-11-21 Dredging treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25974685A JPS62121241A (en) 1985-11-21 1985-11-21 Dredging treatment apparatus

Publications (2)

Publication Number Publication Date
JPS62121241A JPS62121241A (en) 1987-06-02
JPH0426008B2 true JPH0426008B2 (en) 1992-05-06

Family

ID=17338371

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25974685A Granted JPS62121241A (en) 1985-11-21 1985-11-21 Dredging treatment apparatus

Country Status (1)

Country Link
JP (1) JPS62121241A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2221771B1 (en) * 2002-04-23 2006-10-01 Ecodragados, S.L. DRUG PROCEDURE AND EQUIPMENT.
CN102775040B (en) * 2012-08-02 2013-11-13 上海市离心机械研究所有限公司 Shipborne centrifugal dewatering system
CN111519734B (en) * 2020-04-24 2021-06-08 中国电建集团华东勘测设计研究院有限公司 Silt dredging method for river channel hidden culvert

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS531972A (en) * 1976-06-25 1978-01-10 Keijirou Gotou Method of carring out sludge and such
JPS596972B2 (en) * 1977-04-06 1984-02-15 日立造船株式会社 High concentration dredging treatment method
JPS5575032A (en) * 1978-12-01 1980-06-06 Osaka Sosenjo:Kk Dredging method
JPS5824037A (en) * 1981-08-06 1983-02-12 Kamino Kaiji Kogyo Kk Dredging treatment
JPS6073922A (en) * 1983-09-29 1985-04-26 Nakao Ishido Dredging method for settled mud

Also Published As

Publication number Publication date
JPS62121241A (en) 1987-06-02

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