JPH03161099A - Treatment process for waste sludge containing bentonite - Google Patents

Treatment process for waste sludge containing bentonite

Info

Publication number
JPH03161099A
JPH03161099A JP1299552A JP29955289A JPH03161099A JP H03161099 A JPH03161099 A JP H03161099A JP 1299552 A JP1299552 A JP 1299552A JP 29955289 A JP29955289 A JP 29955289A JP H03161099 A JPH03161099 A JP H03161099A
Authority
JP
Japan
Prior art keywords
water
polyvalent metal
metal salt
bentonite
added
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
JP1299552A
Other languages
Japanese (ja)
Inventor
Yoshio Mishima
芳夫 三島
Kazuyuki Sato
一行 佐藤
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.)
Kyoritsu Yuki Co Ltd
Original Assignee
Kyoritsu Yuki 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 Kyoritsu Yuki Co Ltd filed Critical Kyoritsu Yuki Co Ltd
Priority to JP1299552A priority Critical patent/JPH03161099A/en
Publication of JPH03161099A publication Critical patent/JPH03161099A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To manufacture a granular material to be dehydrated by a simple operation by adding specified acrylic water-soluble polymer in the specified wt.% per suspended solid matter to sludge and mixing therein, and then adding water-soluble polyvalent metal salt in the specified wt.% per suspended solid and mixing therein. CONSTITUTION:Bentonite waste sludge is fed into a polymer mixing tank 1 and 0.2-5wt.% per suspended solid in the sludge of anionic acryl water-soluble polymer containing 15mol% or more of acrylic acid monomer unit and of 2-million or more molecular weight is added and mixed therein. After being mixed uniformly, said mixture is mixed with polyvalent metal salt water solution slowly by a multi-stage agitating element 4 of a granulating tank 3 and turned into granular slurry. The same is dehydrated by a belt press 5 and turned into a cake and discharged. The cake can be fed out easily and used for landfilling. Also, a solidifying agent such as cement can be blended in.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、泥水シールド工法、地下連続壁工法等の土木
工事から発生するベントナイト含有廃泥の脱水処理方法
に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for dewatering bentonite-containing waste mud generated from civil engineering works such as mud water shield construction method and underground continuous wall construction method.

[従来の技術] 土木工事より発生するベントナイト含有廃泥は流動性が
高く、バキューム車でM搬され産業廃果物として処理さ
れている。該廃泥を脱水し、ダンブトラックによる運搬
及び埋立て処分を可能とする為、各種の凝集方法が提案
されている。例えば、特開昭50−81963号公報に
はセメント又は水酸化カルシウムを添加後、有機高分子
凝集剤を添加する方法が開示され、特開昭52−132
548号公報には、水酸化カルシウムを添加後、静置し
た後に脱水する方法が開示されている。
[Prior Art] Bentonite-containing waste mud generated from civil engineering works has high fluidity, and is transported by vacuum truck and treated as industrial waste. Various coagulation methods have been proposed in order to dewater the waste mud so that it can be transported by dump trucks and disposed of in landfills. For example, JP-A-50-81963 discloses a method of adding an organic polymer flocculant after adding cement or calcium hydroxide;
No. 548 discloses a method in which calcium hydroxide is added, left to stand, and then dehydrated.

また、特開昭54−155186号公報、特開昭55−
44301号公報及び特開昭56−56289号公報に
は有機高分子凝集剤と水溶性カルシウム塩の混合水溶液
を添加する方法が開示されている。また特開昭55−5
1485号公報には廃泥水に鉄塩またはアルミニウム塩
を添加後アルカリを加えPHを6.5以上に11整し有
機高分子凝集剤を添加する方法が開示されている。
Also, JP-A-54-155186, JP-A-55-
44301 and JP-A-56-56289 disclose a method of adding a mixed aqueous solution of an organic polymer flocculant and a water-soluble calcium salt. Also, JP-A-55-5
Japanese Patent No. 1485 discloses a method in which an iron salt or an aluminum salt is added to waste mud water, an alkali is added thereto, the pH is adjusted to 6.5 or higher, and an organic polymer flocculant is added.

これら従来の技術は全て有機高分子凝集剤の架橋吸着作
用により凝集させるものであり、水溶性高分子添加後の
懸濁液の分散破壊現象を利用するものではない。
All of these conventional techniques involve coagulation by the crosslinking adsorption effect of an organic polymer flocculant, and do not utilize the phenomenon of dispersion destruction of a suspension after addition of a water-soluble polymer.

[従来の技術の問題点] ベントナイト含有泥水はその濃度が高い事およびベント
ナイトが親水性である事からアニオン性有機高分子凝集
剤の準独添加では凝集せず、カルシウム、鉄、アルミニ
ウム等の多価金属イオンを添加するとベントナイトが疎
水化し流動性が無くなる為に有機高分子凝集剤の混合は
困難となり、稀釈しない限り凝集フロックは強い剪断力
の為に破壊される。
[Problems with the conventional technology] Because bentonite-containing mud water has a high concentration and bentonite is hydrophilic, it does not flocculate with the addition of an anionic organic polymer flocculant, and many minerals such as calcium, iron, and aluminum cannot be flocculated. When valence metal ions are added, bentonite becomes hydrophobic and loses fluidity, making it difficult to mix with organic polymer flocculants, and unless diluted, flocs will be destroyed due to strong shearing force.

また有機高分子IMk剤を多量に添加すると液が粘性を
帯び、濾過性を悪化させたり粒子の再分散を起こしたり
する為、ベントナイト含有廃泥を凝集させ脱水する事は
困難であった。
Furthermore, when a large amount of organic polymer IMk agent is added, the liquid becomes viscous, which impairs filterability and causes redispersion of particles, making it difficult to coagulate and dehydrate bentonite-containing waste mud.

[発明の課題】 本発明の課題は高濃度のベントナイト含有廃泥を稀釈す
る事なく濾過または遠心分離により脱水可能とする事で
ある。換言すればベントナイト含有廃泥に対する有機高
分子凝集剤の適切な使用方法を開発し、都市における土
木工事現場の様な狭隘な敷地内で簡単な操作により脱水
処理可能な粒状物を得る事を目的とする。。
[Problem of the Invention] An object of the present invention is to enable dewatering of waste mud containing highly concentrated bentonite by filtration or centrifugation without diluting it. In other words, the aim is to develop an appropriate method for using organic polymer flocculants for bentonite-containing waste mud, and to obtain granular material that can be easily dehydrated in narrow spaces such as civil engineering construction sites in cities. shall be. .

[課題を解決する為の手段] 前述の目的を達成する為に本発明は次の様に構成される
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention is configured as follows.

本発明は分子量200万以上であり、アクリル酸モノマ
ー単位を15モル%以上含有するアクリル系水溶性高分
子を泥水に対し懸濁固形物あたり0.2〜5重量%添加
混合した後、水溶性多価金属塩を懸濁固形物あたり1重
量%以上を添加混合して得られた粒状物を脱水する事を
特徴とする。
In the present invention, an acrylic water-soluble polymer having a molecular weight of 2 million or more and containing 15 mol% or more of acrylic acid monomer units is added to muddy water in an amount of 0.2 to 5% by weight based on suspended solids, and then water-soluble It is characterized in that the granules obtained by adding and mixing a polyvalent metal salt in an amount of 1% by weight or more based on the suspended solids are dehydrated.

また本発明は上記多価金属塩がカルシウム塩、マグネシ
ウム塩、アルミニウム塩、及び鉄塩の中から選ばれる事
を持微とする。
Further, the present invention provides that the polyvalent metal salt is selected from calcium salts, magnesium salts, aluminum salts, and iron salts.

[作用] 本発明は前述の如くアクリル系水溶性高分子をベントナ
イト含有泥水に添加混合する第1工程と水溶性高分子を
添加混合する第2工程とから成る。
[Function] As described above, the present invention consists of a first step of adding and mixing an acrylic water-soluble polymer to muddy water containing bentonite, and a second step of adding and mixing the water-soluble polymer.

第1工程においては泥水の分散状態は変わらず、流動性
は良好である為、アクリル系水溶性高分子の混合は容易
である。次に多価金属塩を添加すると廃泥は脱水し易い
粒状固形物と清澄水に分離する。
In the first step, the dispersion state of the muddy water remains unchanged and the fluidity is good, so it is easy to mix the acrylic water-soluble polymer. Next, when a polyvalent metal salt is added, the waste mud is separated into granular solids that are easily dehydrated and clear water.

通常の凝集処理においては水溶性高分子を混合した時に
凝集が起こりフロックが生成する。この場合は水溶性高
分子の混合は不均一となり脱水性は悪い。
In normal flocculation treatment, flocs are generated when water-soluble polymers are mixed together. In this case, the water-soluble polymers are mixed non-uniformly and dehydration is poor.

これに対し本願発明においては水溶性高分子添加時には
ベントナイトは親水性であり凝集は起こらない。
On the other hand, in the present invention, when a water-soluble polymer is added, bentonite is hydrophilic and no aggregation occurs.

この時点で水溶性高分子は懸濁固形物表面に吸着してい
ると推察する。次いで多価金属塩を添加するとベントナ
イトの疎水性とともに水溶性高分子の不溶化析出現象が
発生し粒状化が起こるものと考える。この様な現象はア
クリル系水溶性高分子内のカルボキシル基と多価金属イ
オンの結合により発現するものであり、他の親水性官能
基であるスルホン基、水酸基、ア主ド基、第四級アンモ
ニウム塩基等においては多価金属イオンによる析出現象
は発生せず粒状化も起こらない。この為、本発明にはカ
ルボキシル基を多量に含有するアクリル系水溶性高分子
を使用する事が必須要件となる。また一般にベントナイ
ト泥水には低分子量のポリアクリル酸ソーダやセルロー
ズ誘導体が分散剤として添加されている。しかし分散剤
を含む廃泥に多価金属塩を添加しても粒状化は起こらな
い。これは分散剤が低分子量である為に懸濁固体を接着
する効果が小さい事に起因する。本願発明においては分
子量200万以上の高分子を使用する為に懸濁固形物を
被覆接着する効果が強力であり、ベントナイトの疎水化
にともない粒状化が起こる。この様な現象は通常の凝集
理論における架橋吸着作用では説明できず、本願発明に
特有の現象である。
At this point, it is assumed that the water-soluble polymer is adsorbed on the surface of the suspended solids. Next, when a polyvalent metal salt is added, the hydrophobicity of bentonite and the insolubilization and precipitation of water-soluble polymers occur, resulting in granulation. This phenomenon occurs due to the bond between the carboxyl group in the acrylic water-soluble polymer and the polyvalent metal ion, and other hydrophilic functional groups such as sulfone group, hydroxyl group, ado group, and quaternary In the case of ammonium base, etc., precipitation phenomenon due to polyvalent metal ions does not occur and granulation does not occur. Therefore, it is essential for the present invention to use an acrylic water-soluble polymer containing a large amount of carboxyl groups. Additionally, low molecular weight sodium polyacrylate or cellulose derivatives are generally added to bentonite mud as dispersants. However, granulation does not occur even when polyvalent metal salts are added to waste mud containing a dispersant. This is due to the fact that the dispersant has a low molecular weight and therefore has little effect in adhering suspended solids. In the present invention, since a polymer having a molecular weight of 2 million or more is used, the effect of coating and adhering suspended solids is strong, and granulation occurs as bentonite becomes hydrophobic. Such a phenomenon cannot be explained by the crosslinking adsorption effect in the usual aggregation theory, and is a phenomenon unique to the present invention.

(実施例) 図面に従い本発明に使用する装置の一例を説明する。ベ
ントナイト廃泥は高分子混和槽1に導入され、撹拌槻2
によりアクリル系水溶性高分子と均一に混合された後、
造粒槽3に導かれ、多段撹拌翼4により多価金属塩水溶
液と緩やかに混和され、粒状物スラリーとなる。該粒状
物スラリーはベルトブレス5にて脱水されケーキとなっ
て排出される。一連の操作の中で特に重要な工程は造粒
槽における多価金属塩水溶液との混和であり槽内の全て
の個所で癒拌は緩やかに行い、懸濁固形物を粒径1mm
以上に造粒する。撹拌が強いと微細粒子が生成し脱水困
難となる。アクリル系水溶性高分子と廃泥の混合は均一
に混合しさえすれば目的を達する事ができ、廃泥配管中
にて薬注混合する事も可能である。
(Example) An example of a device used in the present invention will be described with reference to the drawings. The bentonite waste sludge is introduced into the polymer mixing tank 1, and the agitator 2
After being uniformly mixed with acrylic water-soluble polymer,
It is led to a granulation tank 3 and is gently mixed with a polyvalent metal salt aqueous solution by a multistage stirring blade 4 to form a granule slurry. The granular slurry is dehydrated by a belt press 5 and discharged as a cake. A particularly important step in the series of operations is mixing with the polyvalent metal salt aqueous solution in the granulation tank. Gentle mixing is performed at all locations in the tank, and the suspended solids are reduced to a particle size of 1 mm.
Granulate the above amount. If stirring is too strong, fine particles will be generated, making dehydration difficult. The purpose of mixing the acrylic water-soluble polymer and waste mud can be achieved as long as they are mixed uniformly, and it is also possible to mix them with chemicals in the waste mud pipe.

本発明に用いるアクリル系水溶性高分子は少くとも20
0万以上、望ましくは300万以上の分子量を有し、高
分子構造内に少くとも15モル%以上、望ましくは25
モル%以上のアクリル酸モノマー単位を有するものが好
ましい。
The acrylic water-soluble polymer used in the present invention has at least 20
It has a molecular weight of 0,000 or more, preferably 3,000,000 or more, and contains at least 15 mol% or more, preferably 25,000,000 or more in the polymer structure.
Those having acrylic acid monomer units of mol % or more are preferred.

この様な分子構造を有する高分子としてポリアクリルア
ミド加水分解物、ポリアクリル酸塩、アクリルアミド・
アクリル酸塩共重合物等をあげる事ができる。カルボキ
シル基による析出作用を防害しない範囲において他のモ
ノマー単位を含有する事も許される。アクリル系水溶性
高分子は粘度10,ooocp以下の水i8′液または
油中水型エマルジョンの如き液状で添加する事が好まし
く、通常市販されている粉末状態のまま廃泥に添加する
と、ママ粉をつくり溶解不十分となる為、必要添加量が
多くなる欠点がある。
Polymers with such a molecular structure include polyacrylamide hydrolyzate, polyacrylate, and acrylamide.
Examples include acrylate copolymers. It is also permissible to contain other monomer units as long as they do not prevent the precipitation effect due to carboxyl groups. It is preferable to add the acrylic water-soluble polymer in a liquid form such as a water solution or water-in-oil emulsion with a viscosity of 10, ooocp or less. This has the disadvantage that the required amount of addition is large because it creates insufficient dissolution.

油中水型エマルジ3ンを直接添加する場合は廃泥と接触
直後に強撹拌を行い分散を促進させる必要はあるものの
溶解操作が不要となる利点がある。
When water-in-oil emulsion is added directly, it is necessary to perform strong stirring immediately after contact with the waste mud to promote dispersion, but there is an advantage that no dissolution operation is required.

これらアクリル系水溶性高分子は!!濁固形物に対し0
.5〜5重量%添加混合される。
These acrylic water-soluble polymers! ! 0 for cloudy solids
.. 5 to 5% by weight is added and mixed.

0.5重量%以下では多量のベントナイトを含有する廃
泥を粒状化する事ができず、あまり多量に添加する事は
経済的に不利である。
If the amount is less than 0.5% by weight, waste mud containing a large amount of bentonite cannot be granulated, and adding too much is economically disadvantageous.

高分子を混合した廃泥を粒状化する為に用いる水溶性多
価金属塩としてはカルシウム塩、マグネシウム塩、アル
ミニウム塩、鉄塩が用いられる。亜鉛塩、銅塩等は有毒
であり不適である。ポリアミン等の有機ポリカチオンも
造粒効果はあるが金属塩に比較してあまりにも高価であ
る。
Calcium salts, magnesium salts, aluminum salts, and iron salts are used as water-soluble polyvalent metal salts used to granulate waste mud mixed with polymers. Zinc salts, copper salts, etc. are toxic and unsuitable. Organic polycations such as polyamines also have a granulation effect, but are too expensive compared to metal salts.

本発明に用いる水溶性多価金属塩は塩化物が最も好まし
く硫酸塩はこれに次ぐ。具体的には塩化カルシウム、塩
化マグネシウム、(ポリ)塩化アルミニウム、塩化第一
鉄及び塩化第二鉄が最も好ましく硫酸マグネシウム、硫
酸アルミニウム、硫酸第一鉄、(ポリ)硫酸第二鉄等は
これに次ぐ。これら水溶性多価金属塩は泥中の懸濁固形
物に対して1重量%以上を水溶性の形態で添加する。多
価金属塩の溶解に利用する水は特別な水質を要求されず
、粒状物スラリーを脱水した脱#液を用いると排出水量
を増加させる事が無い。また、この脱離液中には未利用
の多価金属イオンが存在する為、その一部を造粒槽に注
入し、利用効率を上げる事もできる。造粒槽から取り出
きれた粒状物スラリーは野積みによる自然脱水ならびに
ナイロンスクリーンや金網による重力濾過等を行う事も
できるが、含水率を下げる為にはベルトプレス、フィル
タープレス、デカンター等の脱水機を用いる事が望まし
い。特にベルトプレスはコンパクトであり工事現場で用
いるには最も望ましい脱水機である。
The most preferred water-soluble polyvalent metal salt used in the present invention is chloride, followed by sulfate. Specifically, calcium chloride, magnesium chloride, (poly)aluminum chloride, ferrous chloride, and ferric chloride are most preferred, and magnesium sulfate, aluminum sulfate, ferrous sulfate, (poly)ferric sulfate, etc. Next. These water-soluble polyvalent metal salts are added in a water-soluble form in an amount of 1% by weight or more based on the suspended solids in the mud. The water used for dissolving the polyvalent metal salt does not require any special water quality, and if a dehydrating solution obtained by dehydrating the granular material slurry is used, the amount of discharged water will not increase. Furthermore, since unused polyvalent metal ions are present in this desorbed liquid, some of them can be injected into the granulation tank to increase utilization efficiency. The granular slurry that has been removed from the granulation tank can be naturally dehydrated by piling it up in the open or gravity filtered using a nylon screen or wire mesh, but in order to lower the moisture content, dewatering using a belt press, filter press, decanter, etc. It is preferable to use a machine. In particular, belt presses are compact and are the most desirable dewatering machines for use at construction sites.

脱水機から排出されたケーキはダンブトラックで容易に
搬出し埋め立てに用いる事ができる。また重力濾過で簡
易に脱水した後セメント等の固化剤を配合する事も可能
である。以下具体例を用いてさらに詳しく説明する。
The cake discharged from the dehydrator can be easily transported by dump truck and used for landfill. It is also possible to simply dehydrate by gravity filtration and then add a solidifying agent such as cement. This will be explained in more detail below using specific examples.

実施例−1 有機高分子凝集剤として市販されているポリアクリルア
ミド部分加水分解物、及びポリアクリル酸ソーダの粉末
を試験に供した。
Example 1 A partially hydrolyzed polyacrylamide commercially available as an organic polymer flocculant and a powder of sodium polyacrylate were subjected to a test.

各高分子の物性を表−1に示す。Table 1 shows the physical properties of each polymer.

表−1 ・AAM−AMPS共重合物とはアクリルアミドと2−
アクリルアミドメチルプロパンスルホン酸ソーダ共重合
物を示す。
Table-1 ・AAM-AMPS copolymer is acrylamide and 2-
This shows a copolymer of sodium acrylamide methylpropanesulfonate.

某泥水シールド工事現場より発生した廃泥の脱水試験を
行った。該廃泥の物性値は懸濁固形物濃度13.8%フ
ァンネル粘度44秒 PH11.1であった。
A dewatering test was conducted on waste mud generated from a certain mud water shield construction site. The physical properties of the waste mud were as follows: suspended solids concentration: 13.8%, funnel viscosity: 44 seconds, and pH: 11.1.

表−1に記載した高分子粉末を1%水溶液とし高分子混
和槽1へ添加し、多価金属塩は10%水溶液として造粒
槽に添加した。
The polymer powders listed in Table 1 were made into a 1% aqueous solution and added to the polymer mixing tank 1, and the polyvalent metal salt was made into a 10% aqueous solution and added to the granulation tank.

粒状物スラリーをベルトプレスで脱水した試験結果を表
−2に示す。
Table 2 shows the test results of dewatering the granular material slurry using a belt press.

高分子試料及び多価金属塩の薬注量は懸濁固形物あたり
の純分添加量である。なお、表−2と同一の薬注量で多
価金属塩と高分子試料をあらかじめ混合した液を高分子
混和槽へ添加した場合、および造粒槽へ添加した場合、
および造粒槽へ添加した場合、ならびに多価金属塩を高
分子混和槽へ添加後、造粒槽へ高分子試料を添加した場
合は全て脱水不能であった。
The dosing amount of the polymer sample and polyvalent metal salt is the pure amount added per suspended solid. In addition, when adding a solution in which a polyvalent metal salt and a polymer sample were mixed in advance at the same dosage amount as shown in Table 2 to the polymer mixing tank, and when adding it to the granulation tank,
Dehydration was impossible in all cases when the polyvalent metal salt was added to the granulation tank, and when the polymer sample was added to the granulation tank after the polyvalent metal salt was added to the polymer mixing tank.

表−2 実施例−2 某地下連続壁工事現場より発生した廃泥の脱水試験を実
施例−1の試料と装置を用いて行った。
Table 2 Example 2 A dewatering test of waste mud generated from a certain underground continuous wall construction site was conducted using the sample and device of Example 1.

該廃泥の物性値は懸濁固形物濃度12.5%ファンネル
粘度36.8秒 PH11.9であった。
The physical properties of the waste mud were as follows: suspended solids concentration: 12.5%, funnel viscosity: 36.8 seconds, and pH: 11.9.

表−3 多m甜嘱 4 出■人 株式会社 協立冑硼工llI研究所 図−1 手 続 補 正 書 〈方 式〉 平戒 2年 3月 3日Table-3 Tama sweets 4 People coming out Co., Ltd. Kyoritsu Kogyo llI Research Institute Figure-1 hand Continued Supplementary Positive book <direction formula> peace precepts 2 years March 3rd

Claims (3)

【特許請求の範囲】[Claims] (1)分子量200万以上であり、アクリル酸モノマー
単位を15モル%以上含有するアニ オン性アクリル系水溶性高分子を泥中の懸 濁固形物あたり0.2〜5重量%添加混合 した後に水溶性多価金属塩を添加混合して 得られた粒状物を脱水する事を特徴とする ベントナイト含有排泥の処理方法。
(1) Anionic acrylic water-soluble polymer having a molecular weight of 2 million or more and containing 15 mol% or more of acrylic acid monomer units is added and mixed in an amount of 0.2 to 5% by weight based on the suspended solids in the mud, and then dissolved in water. A method for treating waste sludge containing bentonite, which comprises dehydrating granules obtained by adding and mixing polyvalent metal salts.
(2)水溶性多価金属塩がカルシウム塩、マグネシウム
塩、アルミニウム塩、鉄塩及びこれ らの混合物の中から選ばれる事を特徴とす る請求項1に記載のベントナイト含有廃泥 の処理方法。
(2) The method for treating bentonite-containing waste mud according to claim 1, wherein the water-soluble polyvalent metal salt is selected from calcium salts, magnesium salts, aluminum salts, iron salts, and mixtures thereof.
(3)水溶性多価金属塩の添加量が泥中の懸濁固形物あ
たり1重量%以上である事を特徴と する請求項1に記載のベントナイト含有廃 泥の処理方法。
(3) The method for treating bentonite-containing waste mud according to claim 1, wherein the amount of the water-soluble polyvalent metal salt added is 1% by weight or more based on the suspended solids in the mud.
JP1299552A 1989-11-20 1989-11-20 Treatment process for waste sludge containing bentonite Pending JPH03161099A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1299552A JPH03161099A (en) 1989-11-20 1989-11-20 Treatment process for waste sludge containing bentonite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1299552A JPH03161099A (en) 1989-11-20 1989-11-20 Treatment process for waste sludge containing bentonite

Publications (1)

Publication Number Publication Date
JPH03161099A true JPH03161099A (en) 1991-07-11

Family

ID=17874096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1299552A Pending JPH03161099A (en) 1989-11-20 1989-11-20 Treatment process for waste sludge containing bentonite

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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5858214A (en) * 1996-10-17 1999-01-12 Arr-Maz Products, L.P. Phosphate beneficiation process using polymers as slime flocculants
JP2000189999A (en) * 1998-12-25 2000-07-11 Terunaito:Kk Volume reducing method of high water content dredged bottom mud
JP2008080278A (en) * 2006-09-28 2008-04-10 Kurita Water Ind Ltd Flocculation method of highly hydratable sludge
JP2008229611A (en) * 2007-02-22 2008-10-02 Ohbayashi Corp Dehydrator of excavated earth and sand

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49104874A (en) * 1973-02-09 1974-10-03
JPS50110972A (en) * 1974-01-11 1975-09-01

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49104874A (en) * 1973-02-09 1974-10-03
JPS50110972A (en) * 1974-01-11 1975-09-01

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5858214A (en) * 1996-10-17 1999-01-12 Arr-Maz Products, L.P. Phosphate beneficiation process using polymers as slime flocculants
JP2000189999A (en) * 1998-12-25 2000-07-11 Terunaito:Kk Volume reducing method of high water content dredged bottom mud
JP2008080278A (en) * 2006-09-28 2008-04-10 Kurita Water Ind Ltd Flocculation method of highly hydratable sludge
JP2008229611A (en) * 2007-02-22 2008-10-02 Ohbayashi Corp Dehydrator of excavated earth and sand

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