JPS5857357B2 - Sludge treatment method at sea - Google Patents

Sludge treatment method at sea

Info

Publication number
JPS5857357B2
JPS5857357B2 JP752778A JP752778A JPS5857357B2 JP S5857357 B2 JPS5857357 B2 JP S5857357B2 JP 752778 A JP752778 A JP 752778A JP 752778 A JP752778 A JP 752778A JP S5857357 B2 JPS5857357 B2 JP S5857357B2
Authority
JP
Japan
Prior art keywords
sludge
barge
tank
water
concentration
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
Application number
JP752778A
Other languages
Japanese (ja)
Other versions
JPS54102778A (en
Inventor
正昭 安達
実 安武
悦生 荻野
敏行 菊池
信夫 吉井
信之 吉田
和夫 斉藤
準 的場
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen 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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP752778A priority Critical patent/JPS5857357B2/en
Publication of JPS54102778A publication Critical patent/JPS54102778A/en
Publication of JPS5857357B2 publication Critical patent/JPS5857357B2/en
Expired legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 本発明は洋上におけるヘドロ処理方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating sludge on the ocean.

従来のヘドロ処理プラントは、ヘドロ浚渫船→排送管→
陸上(固定)処理プラント(主に機械脱水)で成り立っ
ているが、これによると機動性に問題があった。
A conventional sludge treatment plant consists of a sludge dredger → a discharge pipe →
It consists of land-based (fixed) treatment plants (mainly mechanical dewatering), but this poses problems in terms of mobility.

そこで最近では、処理プラントを台船にのせ、この台船
を移動させることlこより機動性を高めるべく考えられ
た。
Recently, efforts have been made to increase the mobility of the treatment plant by mounting it on a barge and moving the barge.

しかしこれによると、処理プラントの全てを台船に装備
することからこの台船が大型化し、したがって浚せっ地
域が狭い場合には十分な機動性を期待できない。
However, according to this, since the entire treatment plant is installed on a barge, this barge becomes large, and therefore sufficient maneuverability cannot be expected when the area to be dredged is narrow.

かと言って台船を小型化したときには浚せつ船側からの
高含水率のヘドロ水を濃縮させるに充分な時間を費やす
ことができず、高濃度のヘドロを投棄できない。
On the other hand, when the barge is made smaller, it is not possible to spend enough time to concentrate the sludge water with a high moisture content from the dredger side, and the high concentration sludge cannot be dumped.

そこで本発明は、狭い浚せつ地域でも高い機動性を期待
し得、しかも高濃度のヘドロを投棄し得る洋上における
ヘドロ処理方法を提供するもので、ヘドロを濃縮処理す
る複数のヘドロ濃縮台船と、ヘドロ上澄水を水処理した
後、放流するヘドロ上澄水処理台船と、濃縮ヘドロを固
化処理した後、投棄地へ排出する濃縮へドロ固化剤注入
台船とを用い、前記ヘドロ濃縮台船を浚せつ船により揚
泥されたヘドロの受は入れ工程と、濃縮工程と、水処理
台船への上澄水移送工程と、固化剤注入台船への濃縮ヘ
ドロ移送工程のサイクルでヘドロ処理を行なう構成にし
て上記目的を達成したものである。
Therefore, the present invention provides an offshore sludge treatment method that can be expected to have high maneuverability even in narrow dredging areas and can dump highly concentrated sludge. , using a sludge supernatant water treatment barge that processes and discharges sludge supernatant water, and a concentrated sludge solidifying agent injection barge that solidifies the concentrated sludge and then discharges it to a dumping site; Sludge treatment is carried out through a cycle of receiving the sludge pumped up by the dredger, concentrating it, transferring the supernatant water to the water treatment barge, and transferring the concentrated sludge to the solidification agent injection barge. The above object has been achieved with this configuration.

以下本発明の一実施例を図面に基づいて説明する。An embodiment of the present invention will be described below based on the drawings.

第1図に示すように浚せつ区域1で活動する浚せつ船2
と、複数のヘドロ濃縮台船3と、ヘドロ上澄氷水処理台
船4と、投棄地5近くに係留される濃縮ヘト宅固化剤注
入台船6が準備される。
Dredger 2 operating in dredging area 1 as shown in Figure 1
A plurality of sludge concentration barges 3, a sludge supernatant ice water treatment barge 4, and a concentrated sludge solidifying agent injection barge 6 moored near the dumping site 5 are prepared.

前記浚せつ船2は従来の一般的なものが使用されるので
その詳細は省略するが、各台船3,4,6の構成、作用
については以下に述べる。
Since the dredger 2 is a conventional dredge, its details will be omitted, but the structure and operation of each barge 3, 4, and 6 will be described below.

ヘドロ濃縮台船3は第2図〜第5図に示すように、ヘド
ロ浚渫船2に近接する洋上に係留しており、その船中方
向の中央に、船首尾方向に複数(実施例では4)のへp
o濃縮槽7を設け、そしてヘドロ濃縮槽7の両側に上澄
水槽8を設けている。
As shown in FIGS. 2 to 5, the sludge enrichment barge 3 is moored on the ocean near the sludge dredger 2, and a plurality of barges (four in the embodiment) are placed at the center of the ship in the bow and aft direction. Nohep
o A concentration tank 7 is provided, and supernatant water tanks 8 are provided on both sides of the sludge concentration tank 7.

なお上澄水槽8は脚荷水槽を兼ねている。上甲板9にそ
の基端が浚渫船側に接続するヘドロ供給管10を設け、
その配管中にヘドロ混和槽11やバルブ12を設けると
共に、分岐した先端を各ヘドロ濃縮槽7に至らしめてい
る。
Note that the supernatant water tank 8 also serves as a leg water tank. A sludge supply pipe 10 whose base end is connected to the dredger side is provided on the upper deck 9,
A sludge mixing tank 11 and a valve 12 are provided in the piping, and branched ends lead to each sludge concentration tank 7.

上甲板9上を船首尾方向に走行可能なトラベリングクレ
ーン13は濃縮ヘドロ移送ポンプ(水中ポンプ)14を
吊下げており、このポンプ14からの濃縮ヘドロ移送ホ
ース15は、各ヘドロ濃縮槽7の上部にその分岐基端が
位置する濃縮ヘドロ排出管16に接続可能である。
A traveling crane 13 that can travel in the bow and stern direction on the upper deck 9 suspends a concentrated sludge transfer pump (submersible pump) 14, and a concentrated sludge transfer hose 15 from this pump 14 is connected to the upper part of each sludge concentration tank 7. It can be connected to the concentrated sludge discharge pipe 16 whose branched proximal end is located at.

この濃縮ヘドロ排出管16にはバルブ17が設けられる
This concentrated sludge discharge pipe 16 is provided with a valve 17 .

なおヘドロ供給管10には、浚せつ船2からの排泥管1
8が接続可能であり、また濃縮ヘドロ排出管16には、
固化剤注入台船6への濃縮ヘドロ輸送ホース19が接続
可能である。
Note that the sludge supply pipe 10 includes a sludge removal pipe 1 from the dredger 2.
8 can be connected to the concentrated sludge discharge pipe 16,
A concentrated sludge transport hose 19 can be connected to the solidifying agent injection barge 6.

前記ヘドロ濃縮槽7の上部は、オーバーフローバルブ2
0を介して上澄水槽8に開放し、また各上澄水槽8内に
開口する上澄水移送管21は、水処理台船4への上澄水
移送ホース22に接続可能である。
The upper part of the sludge concentration tank 7 is connected to an overflow valve 2.
A supernatant water transfer pipe 21 that opens into the supernatant water tank 8 through the water treatment barge 0 and into each supernatant water tank 8 can be connected to a supernatant water transfer hose 22 to the water treatment barge 4 .

またヘドロ濃縮槽7には、水処理台船4からのスラッジ
移送ホース23が開口可能である。
Furthermore, a sludge transfer hose 23 from the water treatment barge 4 can be opened into the sludge concentration tank 7 .

ヘドロ浚渫船2により揚泥され排泥管18にて送込まれ
た高い含水率のヘドロ水は、ヘドロ混和槽11にて沈降
促進剤(凝集沈降剤)と混和され、ヘドロ供給管10を
経てヘドロ濃縮槽7に投入される。
The sludge water with a high water content that is lifted by the sludge dredger 2 and sent through the sludge removal pipe 18 is mixed with a sedimentation accelerator (coagulation sedimentation agent) in the sludge mixing tank 11, and the sludge is passed through the sludge supply pipe 10. It is put into the concentration tank 7.

そしてヘドロ濃縮槽7にて成る時間静置され、上澄水と
濃縮ヘドロとに分離される。
The sludge is then allowed to stand still in the sludge concentration tank 7 for a period of time, and is separated into supernatant water and concentrated sludge.

上澄水は、オーバーフローバルブ20を介して上澄水槽
8に重力にてオーバーフローされる。
The supernatant water overflows by gravity into the supernatant water tank 8 via the overflow valve 20.

ここで元々高含水率で受入れされたヘドロ水は脱水(水
切り)をされ、濃度の高い濃縮ヘドロとなる。
The sludge water originally received with a high water content is dehydrated (drained) and becomes concentrated sludge with a high concentration.

これをトラベリングクレーン13に吊した濃縮ヘドロ移
送ポンプ14で揚泥し、移送ホース15、排水管16な
らひに濃縮ヘドロ輸送ホース19を介して固化剤注入台
船6側に送られる。
This sludge is lifted up by a concentrated sludge transfer pump 14 suspended from a traveling crane 13, and sent to the solidifying agent injection barge 6 via a transfer hose 15, a drain pipe 16, and a concentrated sludge transport hose 19.

一方、上澄水槽8にオーバーフローされた上澄水は未だ
ヘドロが浮遊しており、直ぐに放流するわけにはいかな
い。
On the other hand, the supernatant water overflowing into the supernatant water tank 8 still has sludge floating in it, and cannot be discharged immediately.

これは移送管21ならひに移送ホース22を介して水処
理台船4側に送られる。
This is sent to the water treatment barge 4 side via a transfer pipe 21 and a transfer hose 22.

なお台船3上を走行するトラへリングクレーン13は、
濃縮ヘドロ移送ポンプ14を移動しサクションさせるだ
けでなく、浚渫船2からの排泥管18のジヨイントや薬
液などの受入管のジヨイントとして使用され、さらに船
内の各機械の修理などにも使用できる多目的の機能を有
するクレーンである。
The tiger herring crane 13 running on the barge 3 is
In addition to moving and suctioning the concentrated sludge transfer pump 14, it is also used as a joint for the sludge removal pipe 18 from the dredger 2, a joint for receiving pipes for chemical solutions, etc., and can also be used for repairing various machines on board the ship. It is a crane with functions.

ヘドロ上澄氷水処理台船4は第6図〜第8図に示すよう
に、その船中方向の中央に、船首尾方向に複数(実施例
では2)の水処理沈殿槽24とポンプ室25とを設け、
そして水処理沈殿槽24の両側に脚荷水槽26、燃料油
槽27、清水槽28を設けると共に、ポンプ室25の両
側に薬剤槽29を設けている。
As shown in FIGS. 6 to 8, the sludge supernatant ice water treatment barge 4 has a plurality of water treatment sedimentation tanks 24 (two in the embodiment) and a pump chamber 25 in the center of the ship in the bow and aft direction. and
A leg water tank 26, a fuel oil tank 27, and a fresh water tank 28 are provided on both sides of the water treatment sedimentation tank 24, and a chemical tank 29 is provided on both sides of the pump chamber 25.

さらに反応槽30とろ過槽31を設け、前記水処理沈殿
槽24からの処理水排出管32をこのろ過槽31に接続
すると共に、配管中にはポンプ室25内に位置する放流
水ポンプ33を設けている。
Furthermore, a reaction tank 30 and a filtration tank 31 are provided, and a treated water discharge pipe 32 from the water treatment sedimentation tank 24 is connected to this filtration tank 31, and a discharge water pump 33 located in the pump chamber 25 is connected to the pipe. It is set up.

前記ヘドロ濃縮台船3側からの上澄水移送ホース22は
ポンプ室25内のポンプ34に接続可能であり、さらに
ポンプ34は上澄水移送管35を介して反応槽30に連
通ずる。
The supernatant water transfer hose 22 from the sludge concentration barge 3 side can be connected to a pump 34 in the pump chamber 25, and the pump 34 communicates with the reaction tank 30 via a supernatant water transfer pipe 35.

この反応槽30からの上澄水供給管36は前記水処理沈
殿槽24に開口する。
A supernatant water supply pipe 36 from this reaction tank 30 opens into the water treatment sedimentation tank 24 .

また水処理沈殿槽24の下部に連通ずるスラッジ移送管
37はポンプ38に連通し、このポンプ38に、ヘドロ
濃縮台船3に至る前記スラッジ移送ホース23が接続可
能である。
Further, a sludge transfer pipe 37 communicating with the lower part of the water treatment sedimentation tank 24 communicates with a pump 38, and the sludge transfer hose 23 leading to the sludge concentration barge 3 can be connected to this pump 38.

ヘドロ濃縮台船3にて濃縮により分離された上澄水には
未だヘドロが浮遊しており、直ぐに放流するわけにはい
かない。
Sludge is still floating in the supernatant water separated by concentration in the sludge concentration barge 3, and it cannot be discharged immediately.

これを上澄水移送ホース22を介してポンプ34にて吸
引し、さらに上澄水移送管35を介して反応槽30に送
る。
This is sucked by a pump 34 through a supernatant water transfer hose 22 and further sent to a reaction tank 30 via a supernatant water transfer pipe 35.

ここで上澄水に薬剤槽29からの薬剤が混合され、共沈
しやすい状態tこしたのち水処理沈殿槽24に投入する
Here, the supernatant water is mixed with the drug from the drug tank 29 and is put into a water treatment sedimentation tank 24 after the supernatant water is brought into a state where it is easy to co-precipitate.

この水処理沈殿槽24の底部に沈殿したヘト川1、ポン
プ38によりスラッジ移送管37ならびにスラッジ移送
ホース23を介して再度ヘドロ濃縮台船3に戻され、前
述のへドロ固化プロセスで処理される。
The Heto River 1 precipitated at the bottom of the water treatment sedimentation tank 24 is returned to the sludge concentration barge 3 again by the pump 38 via the sludge transfer pipe 37 and the sludge transfer hose 23, and is treated in the sludge solidification process described above. .

また水処理沈殿槽24で清澄になった上澄水は、放流水
ポンプ33により処理水排出管32を介してろ過槽31
に送られ、ここで高度な清澄水にされたのち放流される
In addition, the supernatant water that has become clear in the water treatment sedimentation tank 24 is sent to the filtration tank 31 via the treated water discharge pipe 32 by the discharge water pump 33.
The water is sent to the river, where it is made into highly clear water and then released.

なおこの放流水の性状は、如何なる放流基準にも適応で
きるような計画が可能である。
The properties of this discharged water can be planned to meet any discharge standards.

濃縮へドロ固化剤注入台船6は第9図、第10図に示す
ように、上手端に濃縮ヘドロ輸送ホース19が接続可能
で且つ下手端には投棄地5側への濃縮ヘドロ排出ホース
39が接続可能な濃縮ヘドロ輸送管40を有し、この輸
送管40に、前後二段のラインミキサー4L42と、こ
れらラインミキサー4L42の下手に位置する濃縮ヘド
ロ輸送ポンプ43とを設けている。
As shown in FIGS. 9 and 10, the concentrated sludge solidifying agent injection barge 6 has a concentrated sludge transport hose 19 connectable to its upper end, and a concentrated sludge discharge hose 39 to the dumping site 5 at its lower end. This transport pipe 40 is provided with two stages of line mixers 4L42, front and rear, and a concentrated sludge transport pump 43 located downstream of these line mixers 4L42.

44は凝結剤(水ガラス系凝結剤で5IL−B剤という
)を希釈、溶解する凝結剤溶解槽で、ここからの供給管
45は前段のラインミキサー41の上手において濃縮ヘ
ドロ輸送管40に接続する。
44 is a coagulant dissolving tank for diluting and dissolving a coagulant (water glass coagulant, referred to as 5IL-B agent), and a supply pipe 45 from this tank is connected to a concentrated sludge transport pipe 40 above the line mixer 41 in the previous stage. do.

46は例えば硅酸塩硬化剤を希釈、溶解する硬化剤溶解
槽で、ここからの供給管47は両ラインミキサー41.
42間において濃縮ヘドロ輸送管40に接続する。
46 is a curing agent dissolving tank for diluting and dissolving a silicate curing agent, and a supply pipe 47 from this tank is connected to both line mixers 41.
42 and connected to the concentrated sludge transport pipe 40.

48,49はポンプを示す。濃縮ヘト加輸送ホース19
から濃縮ヘドロ輸送管40へと輸送中の濃縮ヘドロに対
して、先ず凝結剤溶解槽44からの水ガラス系凝結剤が
注入されたのちラインミキサー41にて攪拌混合され、
そして硬化剤溶解槽46からの硅酸塩硬化剤が注入され
たのちラインミキサー42にて攪拌混合される。
48 and 49 indicate pumps. Concentrated hetotransport hose 19
The water glass coagulant from the coagulant dissolving tank 44 is first injected into the concentrated sludge being transported from the sludge to the concentrated sludge transport pipe 40, and then stirred and mixed in the line mixer 41.
After the silicate curing agent is injected from the curing agent dissolving tank 46, it is stirred and mixed in the line mixer 42.

このように固化剤を注入された濃縮ヘドロは直ぐには固
化せず、未だ流動状態であるので、濃縮ヘドロ輸送ポン
プ43により濃縮ヘドロ排出ホース39を介して投棄地
5へ輸送され、そしてゲル化(固化)されること(こな
る。
The concentrated sludge into which the solidifying agent has been injected in this way does not solidify immediately and is still in a fluid state, so it is transported to the dumping site 5 via the concentrated sludge discharge hose 39 by the concentrated sludge transport pump 43, and then gelled ( to solidify) to be (kanaru).

上述したように各台船3,4.6は夫々独自の作用を行
なうものであり、ここで第1図fこ示すように、投棄地
5近くの洋上に水処理台船4と固化剤注入台船6を係留
させておき、そして固化剤注入台船6からの濃縮ヘト狛
排出ホース39を投棄地5に至らしめる。
As mentioned above, each of the barges 3 and 4.6 performs its own function, and as shown in Fig. The barge 6 is moored, and the concentrated sludge discharge hose 39 from the solidifying agent injection barge 6 is led to the dumping site 5.

さらに複数のヘドロ濃縮台船3のうちの1つを浚せつ船
2の近くに係留して鉄液せつ船2からの排泥管18を接
続し、以って受入れ中イとする。
Further, one of the plurality of sludge thickening barges 3 is moored near the dredger 2, and the sludge removal pipe 18 from the iron liquefier 2 is connected to it, and the sludge is being received.

そして別のヘドロ濃縮台船3を水処理台船4の近くに係
留して両台船3,4を上澄水移送ホース22で接続し、
以って水処理中口とする。
Then, another sludge concentration barge 3 is moored near the water treatment barge 4, and both barges 3 and 4 are connected with a supernatant water transfer hose 22.
This is referred to as the water treatment center.

さらに別のヘドロ濃縮台船3を固化剤注入台船6の近く
に係留して両台船3,6を濃縮ヘドロ輸送ホース19で
接続し、以って固化剤注入中ハとする。
Furthermore, another sludge concentrating barge 3 is moored near the solidifying agent injection barge 6, and both barges 3 and 6 are connected by a concentrated sludge transporting hose 19, so that the solidifying agent is being injected.

また残りのヘドロ濃縮台船3は濃縮中二と受は入れ待機
中ホとする。
In addition, the remaining sludge enrichment barge 3 is currently in the process of concentrating and receiving the sludge and is on standby.

これにより、浚せつ船2には1つのヘドロ濃縮台船3の
みを近づけて受は入れ中イとすればよく、また水処理中
口、固化剤注入中ハも同様になり、さらに濃縮中二のヘ
ドロ濃縮台船3の数を増すことにより濃縮時間、すなわ
ち静置分離時間を充分に長く取れる。
As a result, it is only necessary to bring only one sludge concentrating barge 3 close to the dredger 2 while receiving the sludge, and the same goes for the water treatment center and the solidifying agent injection port. By increasing the number of sludge concentration barges 3, the concentration time, that is, the stationary separation time can be made sufficiently long.

上述のことかられかるように、ヘドロ濃縮台船3は、受
は入れ中イ→濃縮中二→水処理中ロ→固化剤注入中ハ→
受は入れ待機中ホ→受は入れ中イのサイクルで移動する
のであるが、ここでヘドロの性状や浚せつ船2の浚せつ
能力に応じて船団の数が決められる。
As can be seen from the above, the sludge concentrating barge 3 is in the process of receiving (a) → concentrating (2) → water treatment (b) → solidifying agent being injected (c) →
The receiving vessel moves in a cycle of waiting (ho) → receiving vessel (while waiting), and the number of vessels is determined according to the properties of the sludge and the dredging ability of the dredger 2.

すなわち例えば高含水率のヘドロの場合にはヘドロ濃縮
台船3や水処理台船4が増加されるものであり、 以上、実施例で述へた本発明によると次のような効果を
期待できる。
That is, for example, in the case of sludge with a high water content, the number of sludge concentration barges 3 and water treatment barges 4 is increased. According to the present invention described in the embodiments, the following effects can be expected. .

・各台船は分割されたために、より高い機動性を発揮す
る。
・Since each barge is divided, it exhibits higher maneuverability.

すなわち、分割により夫々を小型化でき、浚せつ区域が
狭い場合でもヘドロ濃縮台船だけが浚せつ船に近づきヘ
ドロを受は入れることができ、以って浚せつ区域に対す
る機動性を高めることができる。
In other words, by dividing, each can be made smaller, and even if the dredging area is narrow, only the sludge concentrating barge can approach the dredging vessel and receive the sludge, thereby increasing the mobility of the dredging area. can.

・複数のヘドロ濃縮台船によりサイクルを組んで使用す
ることにより、静置分離(ヘドロ濃縮)に長い時間を掛
けることができ、高濃度の濃縮ヘドロを得ることができ
る。
- By using multiple sludge concentration barges in a cycle, it is possible to take a long time for static separation (sludge concentration) and obtain highly concentrated sludge.

O船団の数により、或いは船団における各台船の数によ
り処理能力を決めることができ、どのような規模の処理
にも対応できて処理容量の広範囲な選択を可能にできる
The processing capacity can be determined by the number of O-fleets or by the number of each barge in the fleet, and it is possible to handle processing of any scale and enable a wide range of selection of processing capacity.

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

図面は本発明の一実施例を示し、第1図は作業状態を示
す概略平面図、第2図〜第5図はへド狛濃縮台船を示し
、第2図は側面図、第3図は平面図、第4図は水平断面
図、第5図は横断面図、第6図〜第8図はヘドロ上澄氷
水処理台船を示し、第6図は側面図、第7図は平面図、
第8図は水平断面図、第9図、第10図は濃縮へドロ固
化剤注入台船を示し、第9図は側所図、第10図は平直
図である。 1・・・・・・浚せつ区域、2・・・・・・浚せっ船、
3・・・・・・ヘドロ濃縮台船、4・・・・・・ヘドロ
上澄氷水処理台船、5・・・・・・投棄地、6・・・・
・・濃縮へドロ固化剤注入台船、T・・・・・・ヘドロ
濃縮槽、8・・・・・・上澄水槽、18・・・・・・排
泥管、19・・・・・・濃縮ヘドロ輸送ホース、22・
・・・・・上澄水移送ホース、23・・・・・・スラッ
ジ移送ホース、24・・・・・・水処理沈殿槽、31・
・・・・・ろ過槽、39・・・・・・濃縮ヘドロ排出ホ
ース、44・・・・・・凝結剤溶解槽、46・・・・・
・硬化剤溶解槽。
The drawings show one embodiment of the present invention, with Fig. 1 being a schematic plan view showing the working state, Figs. 2 to 5 showing the Hedo Koma enrichment barge, Fig. 2 being a side view, and Fig. 3 is a plan view, Fig. 4 is a horizontal sectional view, Fig. 5 is a cross sectional view, Figs. 6 to 8 show the sludge supernatant ice water treatment barge, Fig. 6 is a side view, and Fig. 7 is a plan view. figure,
FIG. 8 is a horizontal sectional view, FIGS. 9 and 10 show the concentrated sludge solidifying agent injection barge, FIG. 9 is a side view, and FIG. 10 is a horizontal view. 1... Dredging area, 2... Dredger,
3...Sludge concentration barge, 4...Sludge supernatant ice water treatment barge, 5...Dumping site, 6...
...Concentrated sludge solidifying agent injection barge, T...Sludge concentration tank, 8...Supernatant water tank, 18...Sludge removal pipe, 19...・Concentrated sludge transport hose, 22・
...Supernatant water transfer hose, 23...Sludge transfer hose, 24...Water treatment sedimentation tank, 31.
...Filter tank, 39...Concentrated sludge discharge hose, 44...Coagulant dissolving tank, 46...
・Hardening agent dissolution tank.

Claims (1)

【特許請求の範囲】[Claims] 1 ヘドロを濃縮処理する複数のヘドロ濃縮台船と、ヘ
ドロ上澄水を水処理した後、放流するヘドロ上澄水処理
台船と、濃縮ヘドロを固化処理した後、投棄地へ排出す
る濃縮へドロ固化剤注入台船とを用い、前記ヘドロ濃縮
台船を浚せつ船により揚泥されたヘドロの受は入れ工程
と、濃縮工程と、水処理台船への上澄水移送工程と、固
化剤注入台船への濃縮ヘドロ移送工程のサイクルでヘド
ロ処理を行なう事を特徴とする洋上lこおけるヘドロ処
理方法。
1. A plurality of sludge concentration barges that concentrate sludge, a sludge supernatant water treatment barge that processes and discharges sludge supernatant water, and a sludge solidification barge that solidifies concentrated sludge and then discharges it to a dumping site. a step of receiving the sludge pumped up by the dredger using the sludge concentration barge, a concentration step, a step of transferring supernatant water to the water treatment barge, and a solidifying agent injection table. A method for treating sludge in an offshore tank, characterized by treating sludge in a cycle of transferring concentrated sludge to a ship.
JP752778A 1978-01-25 1978-01-25 Sludge treatment method at sea Expired JPS5857357B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP752778A JPS5857357B2 (en) 1978-01-25 1978-01-25 Sludge treatment method at sea

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP752778A JPS5857357B2 (en) 1978-01-25 1978-01-25 Sludge treatment method at sea

Publications (2)

Publication Number Publication Date
JPS54102778A JPS54102778A (en) 1979-08-13
JPS5857357B2 true JPS5857357B2 (en) 1983-12-20

Family

ID=11668244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP752778A Expired JPS5857357B2 (en) 1978-01-25 1978-01-25 Sludge treatment method at sea

Country Status (1)

Country Link
JP (1) JPS5857357B2 (en)

Also Published As

Publication number Publication date
JPS54102778A (en) 1979-08-13

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