JPH09206800A - Treatment of water-area bottom mud - Google Patents

Treatment of water-area bottom mud

Info

Publication number
JPH09206800A
JPH09206800A JP8022576A JP2257696A JPH09206800A JP H09206800 A JPH09206800 A JP H09206800A JP 8022576 A JP8022576 A JP 8022576A JP 2257696 A JP2257696 A JP 2257696A JP H09206800 A JPH09206800 A JP H09206800A
Authority
JP
Japan
Prior art keywords
water
bottom mud
pellet
cement
mud
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
JP8022576A
Other languages
Japanese (ja)
Inventor
Katsuyuki Kataoka
克之 片岡
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.)
Ebara Corp
Original Assignee
Ebara 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 Ebara Corp filed Critical Ebara Corp
Priority to JP8022576A priority Critical patent/JPH09206800A/en
Publication of JPH09206800A publication Critical patent/JPH09206800A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To obviate the need for the land disposal place for dredged bottom mud by adding powdery zeolite, cement, inorg. flocculant and high molecular flocculant to the bottom mud from the water area such as lake and sea, forming the pellet in an agitating and granulating tank and depositing the pellet on the water bottom. SOLUTION: The anaerobic bottom mud 1 also called HEDORO depositing on the bottom of a lake, etc., is pumped up into an agitating and granulating tank 6, and powdery zeolite 2, cement 3 or aluminous inorg. flocculant 4 and high molecular flocculant 5 are added. An appropriate revolving flow is then given, hence the contents of the tank 6 consisting essentially of the bottom mud 1 are flocculated to form a high-strength globular pellet 7, and the pellet is thrown into the water, deposited and accumulated on the water bottom. Consequently, dissolved oxygen is easily diffused into the void between the packed pellets 7, the pellet 7 surface is kept aerobic, the org. bottom mud is decomposed by the methane fermentation in the pellet, and gaseous methane and carbon dioxide are formed.

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、湖沼、海、河川な
どの水域の富栄養化の防止に関し、特に前記水域の底泥
の処理に関するものである。
The present invention relates to the prevention of eutrophication in water bodies such as lakes, marshes, seas and rivers, and more particularly to the treatment of sediment in said water bodies.

【0002】[0002]

【従来の技術】湖沼、海、河川などの水域の富栄養化の
問題が大きく顕在化している。前記水域の底に堆積する
泥、すなわち底泥中に含有されている有機物は、嫌気分
解して酸素を消費するため、底泥からリン、窒素等を含
む栄養塩類の溶出が起こるようになる。従って、排水処
理や流路変更などの対策により湖沼、海、河川などの水
域への流入負荷を削減しても、これら水域では、底泥か
らのリン、窒素等を含む栄養塩類の溶出による富栄養化
現象によりアオコ、赤潮が発生し、水域が汚染される。
養魚池でも同じような問題が起きている。また、河川の
ダム湖には、木の葉が多量に堆積し、木の葉が腐敗し、
ダム湖の底がヘドロ化している例が多く、このヘドロの
減量処理、処分が極めて難題になっている。
2. Description of the Related Art The problem of eutrophication of water bodies such as lakes, marshes, seas, and rivers is becoming more and more apparent. The mud deposited on the bottom of the water area, that is, the organic matter contained in the bottom mud anaerobically decomposes and consumes oxygen, so that nutrient salts containing phosphorus, nitrogen and the like are eluted from the bottom mud. Therefore, even if the inflow load to water bodies such as lakes, seas, and rivers is reduced by measures such as wastewater treatment and change of flow paths, in these water bodies, the enrichment of nutrient salts containing phosphorus, nitrogen, etc. from bottom mud Due to the nutritional phenomenon, blue water and red tide are generated, and the water area is polluted.
A similar problem has occurred in fishponds. In addition, a large amount of leaves accumulate on dam lakes of rivers, causing leaves to rot,
In many cases, the bottom of the dam lake has become sludge, and it is extremely difficult to reduce the weight of this sludge and dispose of it.

【0003】従来、前記水域の富栄養化対策としては汚
濁底泥を浚渫除去し、系外へ排除する方法が主流であっ
た。すなわち、従来の底泥の処理法は、 浚渫した底泥を陸上に埋め立て処分する。 浚渫底泥を脱水後、脱水ケーキを陸上に埋め立て処
分する。 などの処分方法が採用されていた。しかし、これらの従
来技術には次の問題点があった。 埋め立て処分地として広大な面積の土地が必要であ
るが、陸上処分地の確保は極めて困難である。また、浚
渫底泥の土壌改良材、培土、土木資材への再利用の検討
が進められているが、需要が顕在化せずいきづまってい
る。 浚渫底泥を脱水すると大量の分離水がでるが、この
分離水に富栄養化の原因となるリン、窒素が含まれてい
るため、分離水の処理が大きな問題になる。最近では、
水域の富栄養化対策としては、汚濁底泥の浚渫除去の
他、覆砂などのリン、窒素溶出対策も検討されている。
Conventionally, as a measure against eutrophication in the above-mentioned water area, a method in which the polluted bottom mud is dredged and removed to the outside of the system has been the mainstream. That is, the conventional method for treating bottom mud is to dispose of the dredged bottom mud on land. After dewatering the dredged bottom mud, the dewatered cake is landfilled for disposal. Such disposal methods were adopted. However, these conventional techniques have the following problems. A large area of land is required for landfill disposal, but securing land disposal is extremely difficult. In addition, studies are being made on the reuse of dredged bottom mud for soil improvement materials, cultivation soil, and civil engineering materials, but the demand has not been apparent and has continued to increase. When the dredged bottom mud is dewatered, a large amount of separated water is generated. However, since the separated water contains phosphorus and nitrogen which cause eutrophication, treatment of the separated water is a major problem. recently,
As measures for eutrophication of water bodies, in addition to dredging removal of polluted bottom mud, phosphorus and nitrogen elution measures such as sand cover are being considered.

【0004】[0004]

【発明が解決しようとする課題】底泥内には上層水から
の酸素輸送が極めて少ないので、底泥内では有機物の嫌
気的酸発酵、硫酸塩還元、鉄の還元が活発に進行する。
この結果、アンモニア性窒素やリンが可溶化して溶出源
になる。また、硫酸塩還元により生成される硫化物がリ
ン酸鉄からのリン酸イオンの遊離を促進する。さらに、
有機物の酸発酵によって間隙水のpH低下を招き、リン
化合物の可溶化が促進される。このような背景に基づき
検討をすすめ、本発明は、嫌気化している水域の底泥の
物理化学的及び生物学的環境を根本的に改善し、底部の
環境を蘇らせると共に、栄養塩類の底泥から上層水への
溶出を抑制できる新技術を提供することにある。また本
発明は、底泥の新規な利用法を提供し、陸上に埋め立て
処分地を確保する必要が無く、脱水分離水が発生しない
底泥の処理方法を提供することを課題とする。
Since oxygen transport from the upper layer water is extremely small in the bottom mud, anaerobic acid fermentation of organic substances, sulfate reduction, and iron reduction actively proceed in the bottom mud.
As a result, ammoniacal nitrogen or phosphorus is solubilized and becomes an elution source. Further, the sulfide generated by the sulfate reduction promotes release of phosphate ions from iron phosphate. further,
The acid fermentation of the organic matter causes a decrease in the pH of the interstitial water and promotes the solubilization of phosphorus compounds. Based on such a background, the present invention fundamentally improves the physicochemical and biological environment of the bottom mud of the anaerobic water area, revives the bottom environment, and the bottom of nutrient salts. It is to provide a new technology capable of suppressing elution from mud to upper water. Another object of the present invention is to provide a novel method for utilizing bottom mud, and to provide a method for treating bottom mud that does not require landfill disposal sites on land and does not generate dehydrated separated water.

【0005】[0005]

【課題を解決するための手段】本発明の上記課題は、本
発明の水域底泥の処理方法によって達成される。すなわ
ち、 (1)湖沼、海、河川などの水域からの底泥に粉末ゼオ
ライト、セメント、無機凝集剤及び高分子凝集剤を添加
し、攪拌造粒槽でペレットを形成し、該ペレットを水底
に沈積させることを特徴とする水域底泥の処理方法であ
る。
The above-mentioned object of the present invention can be achieved by the method for treating aquatic bottom mud of the present invention. That is, (1) powdered zeolite, cement, an inorganic coagulant and a polymer coagulant are added to bottom mud from a body of water such as a lake, sea, or river, and a pellet is formed in a stirring granulation tank, and the pellet is placed on the bottom of the water. It is a method of treating bottom mud in water bodies, which is characterized by sedimentation.

【0006】[0006]

【発明の実施の形態】本発明の水域底泥の処理方法の処
理フローを図1に示し、以下に図1を用いて本発明を説
明する。図1において、湖沼、海、河川の底に堆積して
いる、ヘドロとも呼ばれる、嫌気性の底泥1を攪拌造粒
槽6中にポンプアップし、粉末ゼオライト2、セメント
3、鉄もしくはアルミニウム系の無機凝集剤4、高分子
凝集剤5を添加した後、適度の旋回流を与えると、攪拌
造粒槽6中の底泥1を主とする内容物が凝集し、球形の
強度の大きいペレット7が生成する。このペレット7を
水中に投入すると、急速に沈降し、水底に沈降堆積す
る。前記粉末ゼオライト、セメント、無機凝集剤及び高
分子凝集剤の添加量は、底泥の性状により適宜決められ
るが、好ましい添加範囲は下記第1表に示す通りであ
る。
BEST MODE FOR CARRYING OUT THE INVENTION A processing flow of a method for treating water bottom mud of the present invention is shown in FIG. 1, and the present invention will be described below with reference to FIG. In FIG. 1, an anaerobic bottom mud 1, also called sludge, deposited at the bottom of lakes, seas, and rivers is pumped up into a stirring granulation tank 6, and powdered zeolite 2, cement 3, iron or aluminum system is used. After adding the inorganic coagulant 4 and the polymer coagulant 5 in (1), when an appropriate swirling flow is applied, the contents mainly composed of the bottom mud 1 in the stirring granulation tank 6 are agglomerated, and spherical pellets having high strength 7 is generated. When these pellets 7 are put into water, they settle down rapidly and settle and accumulate on the bottom of the water. The amount of the powdered zeolite, cement, inorganic coagulant and polymer coagulant added is appropriately determined depending on the properties of the bottom mud, but the preferable range of addition is as shown in Table 1 below.

【0007】[0007]

【表1】 [Table 1]

【0008】水底に沈降堆積させたペレットの作用につ
いて以下に説明する。水底に堆積させると、ペレット相
互の充填空隙部に溶存酸素が拡散し易くなり、ペレット
の表面が好気的に維持され易くなる。最近、ヘドロ層か
らの栄養塩類の溶出を防止するためヘドロ層の上に砂を
散布するいわゆる覆砂が行われるが、ヘドロ層の上に本
発明のペレットを堆積させると、前記覆砂と同様の効果
も発揮される。沈降堆積した有機性底泥は嫌気状態であ
る。しかして、底泥中に自然に存在しているメタン菌を
内部に含有しているペレットを水底に堆積させると、ペ
レットの内部に固定化されているメタン菌によるメタン
発酵作用によって有機性底泥は分解され、メタンガス、
炭酸ガスを生成する。従来のヘドロ層が堆積した水域で
は、メタン発酵は有機物の酸発酵が進んだ後起きるの
で、先に進んだ酸発酵によってヘドロ層のpHが酸性側
に偏る。メタン菌は中性領域で活性の高い菌であるの
で、ヘドロ層のpHが酸性側に偏るとメタン菌の活動が
停止してしまう。しかし、本発明ではペレットの内部に
アルカリ性のセメント粒子が閉じ込められているので酸
発酵によるpHの過度の低下が起きず、効果的にメタン
酸発酵が進む。以上が水底に沈降堆積させたペレットの
作用である。
The operation of the pellets settled and deposited on the water bottom will be described below. When they are deposited on the water bottom, dissolved oxygen is likely to diffuse into the filling voids between the pellets, and the pellet surface is likely to be maintained aerobically. Recently, in order to prevent the nutrient salts from leaching from the sludge layer, so-called cover sand is sprayed on the sludge layer. However, when the pellets of the present invention are deposited on the sludge layer, the same as the cover sand is obtained. The effect of is also exhibited. The sedimented organic bottom mud is anaerobic. Therefore, when pellets containing methane bacteria that are naturally present in the bottom mud are deposited on the water bottom, the organic bottom mud is produced by the methane fermentation action of the methane bacteria immobilized inside the pellets. Is decomposed, methane gas,
Generates carbon dioxide. In the conventional water area where the sludge layer is accumulated, methane fermentation occurs after the acid fermentation of the organic matter progresses, so that the pH of the sludge layer is biased to the acidic side due to the advanced acid fermentation. Since the methane bacterium has high activity in the neutral region, the activity of the methane bacterium stops when the pH of the sludge layer is biased to the acidic side. However, in the present invention, since the alkaline cement particles are confined inside the pellets, the pH is not excessively lowered by the acid fermentation, and the methane acid fermentation effectively proceeds. The above is the action of the pellets settled and deposited on the water bottom.

【0009】前記底泥の添加した添加物中、セメントは
ペレット内部をアルカリ性に維持するほか、ペレットを
固化する作用がある。攪拌造粒槽から流出する時点のペ
レットは指で摘むと壊れる程度の強度であるが、水中に
放置すると、セメントの作用により固化し強度が著しく
増す。本発明にいう「ペレット」はフロックとは異な
り、ピンセットで摘んで水中から取り出すことが可能
な、緻密で、やや強度が大きい球形の造粒物を意味す
る。これに対して、フロックは、ピンセットでつまみ出
すことはできず、フワフワした綿状のものである。
Among the additives added with the above-mentioned bottom mud, the cement not only keeps the inside of the pellet alkaline but also has the function of solidifying the pellet. The pellets at the time of flowing out from the agitation granulation tank have such strength that they can be broken by picking them with fingers, but when left in water, they are solidified by the action of cement and the strength is remarkably increased. The term "pellet" as used in the present invention means, unlike flocs, a dense, slightly spherical, granulated substance that can be picked up from water by pinching with tweezers. On the other hand, the flock cannot be picked up by tweezers, but is a fluffy cotton-like thing.

【0010】ペレットの内部には前記底泥に添加した前
記セメントの他、粉末ゼオライト、無機凝集剤及び高分
子凝集剤が閉じ込められている。これら添加物中、粉末
ゼオライトはアンモニアを吸着除去する。また、水酸化
鉄または水酸化アルミニウムなどの無機凝集剤はリンを
除去するほか、ペレットの強度を高める作用がある。
(リンはカルシウム、鉄またはアルミニウムと結合して
不溶化するのでペレットの内部から溶出しない。)
Inside the pellets, in addition to the cement added to the bottom mud, powdered zeolite, an inorganic coagulant and a polymer coagulant are enclosed. Among these additives, powdered zeolite adsorbs and removes ammonia. In addition, an inorganic coagulant such as iron hydroxide or aluminum hydroxide removes phosphorus and has the effect of increasing the strength of pellets.
(Phosphorus does not elute from the inside of the pellet because it binds to calcium, iron or aluminum and becomes insoluble.)

【0011】セメントとしては、ポルトランドセメント
でも良いが、アルミナセメントやジェットセメントなど
のような早強性セメントがペレットを短時間で固化する
ためより好ましい。無機凝集剤としては、硫酸アルミ、
ポリ塩化アルミ、塩化第2鉄、ポリ硫酸第2鉄など水処
理の分野で公知のものを適用すれば良い。高分子凝集剤
としては、公知の種々の市販ポリマが適用できる。本発
明のペレットの形成に効果的なポリマは、分子量が10
00万以上のポリアクリルアミド系のポリマが適してい
る。またカチオンポリマ、アニオンポリマを併用すると
さらに強度の大きいペレットが形成できる。攪拌造粒槽
としては、本発明の出願人が既に開発した装置、商品名
ボルテペレッタが好適に使用することができる。この攪
拌水中造粒装置の詳細は、例えば、文献:ヘドロ誌 2
3号、58〜64頁、1982年 社団法人底質浄化協
会発行 に記載されている。
As the cement, Portland cement may be used, but an early-strength cement such as alumina cement or jet cement is more preferable because it solidifies the pellet in a short time. As the inorganic coagulant, aluminum sulfate,
Materials known in the field of water treatment such as polyaluminum chloride, ferric chloride, and ferric polysulfate may be applied. As the polymer flocculant, various known commercially available polymers can be applied. Polymers effective in forming the pellets of the present invention have a molecular weight of 10
Polymers of the polyacrylamide type of more than 1,000,000 are suitable. When a cationic polymer and an anionic polymer are used in combination, a pellet having higher strength can be formed. As the stirring and granulating tank, an apparatus already developed by the applicant of the present invention and a product name of Volte Peretta can be preferably used. Details of this agitated underwater granulation apparatus are described in, for example, Reference: Hedro 2
No. 3, pp. 58-64, published in 1982 by the Japan Sediment Purification Association.

【0012】[0012]

【実施例】図1の処理フローに従って、本発明の水域底
泥の処理の実証試験を行った。 実施例1 茨城県K湖から採取した底泥(含泥率8%、リンイオン
10.5mg/リットル、アンモニア8.1mg/リッ
トル)に粉末ゼオライトを2重量%、早強性セメントを
5重量%添加し、さらに無機凝集剤としてポリ塩化アル
ミニウム(PAC)を1000mg/リットル、高分子
凝集剤としてアニオン系ポリアクリルアミドを250m
g/リットル添加して攪拌造粒槽(液滞留時間6分)に
供給した結果、底泥SS、ゼオライト、セメント、水酸
化アルミニウムが一体となったペレット(粒径2〜4m
m)が形成された。このペレットをカラム内に30cm
堆積させ、水道水を2m満たし、1年間放置した。1年
後、底泥層の上部10cmの位置から採水し、リン、ア
ンモニアを分析した。この結果リン濃度は1.1mg/
リットル,アンモニア濃度は、1.8mg/リットルで
あった。また、ペレットの高さは1年後に3cm低下し
た。定期的にカラム水面に上昇して来る気泡を採取し、
検知管で定性分析したところメタン、炭酸ガスであっ
た。ペレット充填層内の間隙水のpHは6.7であり、
メタン菌の活動に好適であった。
EXAMPLE A verification test of the treatment of the marine sediment of the present invention was conducted according to the treatment flow of FIG. Example 1 2 wt% of powdered zeolite and 5 wt% of early-strength cement were added to bottom mud (mud content 8%, phosphorus ion 10.5 mg / liter, ammonia 8.1 mg / liter) collected from Lake K, Ibaraki Prefecture. In addition, 1000 mg / liter of polyaluminum chloride (PAC) as an inorganic coagulant and 250 m of anionic polyacrylamide as a polymer coagulant
As a result of adding g / l and supplying to a stirring granulation tank (liquid retention time 6 minutes), pellets (bottom particle diameter 2 to 4 m) in which bottom mud SS, zeolite, cement and aluminum hydroxide are integrated
m) was formed. 30 cm of this pellet in the column
It was deposited, filled with tap water for 2 m, and left for 1 year. One year later, water was sampled from a position 10 cm above the bottom mud layer and analyzed for phosphorus and ammonia. As a result, the phosphorus concentration was 1.1 mg /
The liter and the ammonia concentration were 1.8 mg / liter. Also, the height of the pellet decreased by 3 cm after one year. Collect air bubbles rising to the surface of the column regularly,
Qualitative analysis with a detector tube revealed methane and carbon dioxide. The pH of the pore water in the pellet packed bed is 6.7,
It was suitable for the activity of methane bacteria.

【0013】[0013]

【発明の効果】本発明の底泥の処理方法では、 (i) 浚渫した底泥は、各機能をもつ粉末ゼオライ
ト、セメント、鉄もしくはアルミニウム系の無機凝集剤
及び高分子凝集剤を添加した後ペレットにして、再び水
域底部に返送するので、浚渫底泥の陸上処分地が不要で
ある。 (ii) 水域底部に返送したペレットは、底泥中の有機
物がメタン発酵により分解減量化する。 (iii) 水域底部に返送したペレットは、底泥からのリ
ン、アンモニウムの溶出を抑制できる。 (iii) 浚渫底泥を脱水する必要がないので、脱分離水
が発生せず、分離水の処理が不要である。
According to the method for treating bottom mud of the present invention, (i) the dredged bottom mud is prepared by adding powdered zeolite, cement, iron- or aluminum-based inorganic coagulant and polymer coagulant having various functions. Since it is made into pellets and returned to the bottom of the water area again, the land disposal site of the dredged bottom mud is unnecessary. (Ii) In the pellets returned to the bottom of the water area, the organic matter in the bottom mud is decomposed and reduced by methane fermentation. (Iii) The pellets returned to the bottom of the water body can suppress the elution of phosphorus and ammonium from the bottom mud. (Iii) Since it is not necessary to dehydrate the dredged bottom mud, de-separated water does not occur and the separated water treatment is unnecessary.

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

【図1】本発明の水域の底泥の処理設備のフローの1例
を示す説明図である。
FIG. 1 is an explanatory diagram showing an example of a flow of a treatment facility for sludge in a water area according to the present invention.

【符号の説明】[Explanation of symbols]

1 底泥 2 粉末ゼオライト 3 セメント 4 無機凝集剤 5 高分子凝集剤 6 攪拌造粒槽 7 ペレット 1 Bottom Mud 2 Powder Zeolite 3 Cement 4 Inorganic Flocculant 5 Polymer Flocculant 6 Stirring Granulator 7 Pellets

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 湖沼、海、河川などの水域からの底泥に
粉末ゼオライト、セメント、無機凝集剤及び高分子凝集
剤を添加し、攪拌造粒槽でペレットを形成し、該ペレッ
トを水底に沈積させることを特徴とする水域底泥の処理
方法。
1. A powder mud, cement, an inorganic coagulant and a polymer coagulant are added to bottom mud from water bodies such as lakes, seas and rivers to form pellets in a stirring granulation tank, and the pellets are placed on the bottom of the water. A method for treating bottom sediment in a water area, characterized by depositing.
JP8022576A 1996-02-08 1996-02-08 Treatment of water-area bottom mud Pending JPH09206800A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8022576A JPH09206800A (en) 1996-02-08 1996-02-08 Treatment of water-area bottom mud

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8022576A JPH09206800A (en) 1996-02-08 1996-02-08 Treatment of water-area bottom mud

Publications (1)

Publication Number Publication Date
JPH09206800A true JPH09206800A (en) 1997-08-12

Family

ID=12086705

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8022576A Pending JPH09206800A (en) 1996-02-08 1996-02-08 Treatment of water-area bottom mud

Country Status (1)

Country Link
JP (1) JPH09206800A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005113025A (en) * 2003-10-08 2005-04-28 Takataro Mizuta Aggregate-shaped solidifying material for stabilizing soil, containing inorganic macromolecular coagulant and organic macromolecular coagulant
JP2006159027A (en) * 2004-12-03 2006-06-22 Institute Of National Colleges Of Technology Japan Sludge treatment apparatus and sludge treatment method
CN104276741A (en) * 2014-09-24 2015-01-14 江苏赛欧环保设备有限公司 Horizontal heavy sludge flocculation reaction device
CN110839509A (en) * 2019-11-12 2020-02-28 江苏澳洋生态园林股份有限公司 Method for treating river and lake sludge and then using water-land interlaced belt plant planting matrix
EP3301078B1 (en) * 2016-09-29 2020-12-09 Vesirakennus Ojanen Oy Method for treating dredged material or sludge
CN113023819A (en) * 2021-03-16 2021-06-25 水发规划设计有限公司 Composite material covering piece for inhibiting nitrogen and phosphorus release of landscape lake sediment
CN114775646A (en) * 2022-04-11 2022-07-22 天津大学前沿技术研究院 Method for slope curing and protection by using solidified soil prepared from lake and reservoir sediment
CN115466036A (en) * 2022-09-30 2022-12-13 安吉国千环境科技有限公司 Biological flocculant, bottom sludge treatment method and ecological restoration system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005113025A (en) * 2003-10-08 2005-04-28 Takataro Mizuta Aggregate-shaped solidifying material for stabilizing soil, containing inorganic macromolecular coagulant and organic macromolecular coagulant
JP2006159027A (en) * 2004-12-03 2006-06-22 Institute Of National Colleges Of Technology Japan Sludge treatment apparatus and sludge treatment method
CN104276741A (en) * 2014-09-24 2015-01-14 江苏赛欧环保设备有限公司 Horizontal heavy sludge flocculation reaction device
CN104276741B (en) * 2014-09-24 2016-01-06 江苏赛欧环保设备有限公司 A kind of horizontal heavy sludge flocculation reaction unit
EP3301078B1 (en) * 2016-09-29 2020-12-09 Vesirakennus Ojanen Oy Method for treating dredged material or sludge
CN110839509A (en) * 2019-11-12 2020-02-28 江苏澳洋生态园林股份有限公司 Method for treating river and lake sludge and then using water-land interlaced belt plant planting matrix
CN113023819A (en) * 2021-03-16 2021-06-25 水发规划设计有限公司 Composite material covering piece for inhibiting nitrogen and phosphorus release of landscape lake sediment
CN114775646A (en) * 2022-04-11 2022-07-22 天津大学前沿技术研究院 Method for slope curing and protection by using solidified soil prepared from lake and reservoir sediment
CN115466036A (en) * 2022-09-30 2022-12-13 安吉国千环境科技有限公司 Biological flocculant, bottom sludge treatment method and ecological restoration system

Similar Documents

Publication Publication Date Title
CN104261536B (en) For quickly removing the efficient flocculant of heavy metal in water
CN101412547B (en) Mineral composite material for removing lake endogenous pollution and use thereof
US4721569A (en) Phosphorus treatment process
CN104071962A (en) Treatment method of river or lake sediments
KR970001445B1 (en) Method for improving bottom and water quality in water area and a set of agents used in the method
CN109502720A (en) A method of nitrogen phosphorus in waste water is removed using magnesium salts in desulfurization wastewater
CN102775021B (en) Method of advanced treatment of high concentration phosphorus sewage and recycling of phosphorus
JP2007283223A (en) Method for recovering phosphorus from sludge
CN104528868A (en) Application of magnetic particles in in-situ treatment of eutrophic water and sedimentary phosphate
CN106517591A (en) Reverse osmosis concentration treatment system and method
JPH09206800A (en) Treatment of water-area bottom mud
JP2009142783A (en) Method and material for modifying bottom mud in closed water area or tidal flat
JP2014223612A (en) Denitrification treatment method for nitrate nitrogen and denitrification treatment device
JP3797296B2 (en) Purification method of bottom sludge
JP2913632B2 (en) Dredging mud treatment method and treatment equipment
JP4144952B2 (en) Purification methods for rivers and lakes
JP4368159B2 (en) Method for treating wastewater containing phosphate
EP0612692B1 (en) Method for production of water purifying substances
CN104150602B (en) The sewage water treatment method that nitrogen phosphorus removes in right amount is carried out according to secondary effluent nitrogen content
KR20140128717A (en) Waste water treatment agent for phosphorus removal andpreparation method thereof
JPH10277307A (en) Adsorption flocculant and water treating method
JPH09206799A (en) Treatment of water-area bottom mud and device therefor
JP3013249B1 (en) Coagulating sedimentation agent
JP3103473B2 (en) Water purification material and its production method
Choi et al. Behavior characteristics of phosphorus and capping effect of microbubble flotation to control phosphorus release in the benthic sediment