JP2634846B2 - Coagulation separation method of suspension in water - Google Patents
Coagulation separation method of suspension in waterInfo
- Publication number
- JP2634846B2 JP2634846B2 JP63081332A JP8133288A JP2634846B2 JP 2634846 B2 JP2634846 B2 JP 2634846B2 JP 63081332 A JP63081332 A JP 63081332A JP 8133288 A JP8133288 A JP 8133288A JP 2634846 B2 JP2634846 B2 JP 2634846B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- weight
- suspension
- solidification
- coagulant
- 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
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は河川水、工業用水の除濁および各種産業廃水
の処理工程における水中懸濁物の凝集沈降分離方法に関
する。Description: FIELD OF THE INVENTION The present invention relates to a method for clarifying river water and industrial water, and a method for coagulating sedimentation and separation of an aqueous suspension in a process of treating various types of industrial wastewater.
一般に用水または廃水を処理する工程においては、被
処理液中の懸濁固体と液体とを分離し、透明な上澄液を
得る清澄操作を伴う。用水、廃水中の懸濁質の多くは極
めて微細なものが多く、自然沈澱では沈降し難いため、
従来より沈降分離槽、凝集沈降槽へ導き、槽中で無機質
凝集剤あるいは有機質高分子凝集剤を添加して凝集し、
フロックを形成したものを槽底より抜き出し、更に固液
分離処理を施したうえ、ケーキ状にして処分することが
行われている。In general, the step of treating service water or wastewater involves a clarification operation of separating a suspended solid and a liquid in a liquid to be treated to obtain a transparent supernatant. Many of the suspended solids in service water and wastewater are extremely fine and hard to settle by natural sedimentation.
Conventionally, it is led to a sedimentation separation tank, a coagulation sedimentation tank, where an inorganic coagulant or an organic polymer coagulant is added and coagulated in the tank,
It has been practiced to extract a floc formed from the bottom of the tank, further subject it to a solid-liquid separation treatment, and then dispose it in a cake form.
ところが上記凝集剤の作用によって形成されたフロッ
クは、通常その内部に包含水を有し、またフロック間の
結合水、フロック周囲の付着水などにより、高含水膨潤
状態で沈澱しており、到底そのままでは不安定で処理し
難いものである。従って、安定化するために尚脱水作業
を行う。脱水作業は、例えば加熱濃縮による方法、振動
篩あるいは液体サイクロンなどを適用する方法、遠心分
離機による方法または3〜5kg/cm2程度の加圧下にまた
は吸引下にフィルタープレス、ベルトプレスなどにより
濾過する方法などがあるが、いずれも設備費に要するイ
ニシアルコスト、および時間、労力、熱動力等のランニ
ングコスト等、経済面において大きな不利を強いられて
いる現状にある。However, the floc formed by the action of the flocculant usually has water contained therein, and is precipitated in a highly water-swelling state due to binding water between the flocs, water attached around the flocs, etc. Is unstable and difficult to process. Therefore, a dehydration operation is still performed for stabilization. The dehydration operation can be performed, for example, by heat concentration, by using a vibrating sieve or a liquid cyclone, by a centrifuge, or by filtration under a pressure of about 3 to 5 kg / cm 2 or suction with a filter press, a belt press, or the like. However, there is a great economic disadvantage such as initial costs required for equipment costs and running costs such as time, labor, and thermal power.
また脱水ケーキは、雨水、地下水等によって含水する
と再泥化するため、露天野積みや無蓋運搬には不適であ
るという難点がある。従って、コンポスト化や焼却処分
などの極く例外的な場合を除き、一般に多用されて来た
埋め立て材としての再利用や投棄処分のためには、上記
脱水ケーキに更に石灰、セメント等の固化材を加えて固
化し、好ましくは天日乾燥に付すなどの処理を施す要が
あり、手間や経費の一層の増大をもたらすという問題点
があった。In addition, the dewatered cake is re-mudged when it is wetted by rainwater, groundwater, or the like, and thus has a drawback that it is unsuitable for open-field loading and transport without a lid. Therefore, except for extremely exceptional cases such as composting and incineration, the above dehydrated cake must be further solidified with lime, cement, etc. , And it is necessary to carry out a treatment such as solidification, preferably sun drying, which causes a problem of further increasing labor and cost.
本発明は、凝集沈降させて形成したフロックをそのま
ま固化沈積させることにより清澄水と容易に分離し、且
つ頗る安定にして取扱い至便なケーキ状凝固物を簡単な
工程を以て経済的極めて有利に取得ることを目的として
なされたものである。In the present invention, a floc formed by coagulation and sedimentation is easily separated from clarified water by solidification and sedimentation as it is, and a very solid and easy-to-handle cake-like coagulate is obtained at a very economical advantage with a simple process. It is done for the purpose of.
上記目的を達成するために本発明にかかる水中懸濁物
の凝固分離方法は、懸濁物を含有する用水または廃水に
無機および有機凝集剤の少なくとも一種と共に、主とし
てアルミナセメントと石膏とを含んでなるセメント/石
膏系の水硬性無機固化材を、該凝集剤と該固化材との混
合物重量として上記用水または廃水中の懸濁固形分重量
に対し5〜20%添加することにより懸濁物を凝集沈降さ
せつつ固化して少なくとも0.1kg/cm2好ましくは0.1〜0.
3kg/cm2の一軸圧縮強度を有する凝固物となすことより
なる。In order to achieve the above object, the method for coagulating and separating a suspension in water according to the present invention comprises at least one of inorganic and organic flocculants in service water or wastewater containing the suspension, mainly comprising alumina cement and gypsum. By adding 5 to 20% of a cement / gypsum-based hydraulic inorganic solidifying material as a mixture weight of the coagulant and the solidifying material with respect to the weight of the suspended solids in the above-mentioned water or wastewater. at least 0.1 kg / cm 2, preferably 0.1 to 0 solidifies while flocculated.
The solidified product has a uniaxial compressive strength of 3 kg / cm 2 .
本発明方法は、河川、湖沼、貯水池、工業用水等の除
濁、各種産業廃水、生活廃水等の処理に対して適用し得
る。The method of the present invention can be applied to the turbidity of rivers, lakes and marshes, reservoirs, industrial water, and the like, and the treatment of various industrial wastewaters, domestic wastewaters, and the like.
本発明方法において懸濁物を含有する用水または廃水
に添加する凝集剤は、例えば、硫酸アルミニウム、塩化
アルミニウム等の無機質酸性凝集剤、アルミン酸ソー
ダ、ポリ塩化アルミニウム、低塩基性アルミニウム等の
無機質塩基性凝集剤、硫酸アルミニウムとポリ塩化アル
ミニウムとを併用した無機質両性凝集剤およびポリアク
リルアミド、ポリアクリル酸ソーダ、ポリアクリル酸ア
ミノエステル、ジアミンジアミド、アルギン酸ソーダ等
の有機高分子凝集剤等、公知の凝集沈降剤を含み、これ
らは一種以上を、水質、懸濁物の性状等に応じて適宜使
用する。また凝縮剤は必要に応じて活性炭、次亜塩素酸
ソーダ等の塩素酸化剤、イオン交換樹脂などを、その性
能を損なわない限り、併用してもよい。In the method of the present invention, a flocculant to be added to the water or wastewater containing the suspension includes, for example, an inorganic acidic flocculant such as aluminum sulfate and aluminum chloride, an inorganic base such as sodium aluminate, polyaluminum chloride and low basic aluminum. Known coagulants, such as inorganic coagulants, inorganic amphoteric coagulants using aluminum sulfate and polyaluminum chloride in combination, and organic polymer coagulants such as polyacrylamide, sodium polyacrylate, aminoester polyacrylate, diaminediamide, sodium alginate, etc. A sedimentation agent is used, and one or more of these are used as appropriate depending on the water quality, the properties of the suspension, and the like. As the condensing agent, activated carbon, a chlorine oxidizing agent such as sodium hypochlorite, an ion exchange resin or the like may be used in combination, as long as the performance is not impaired.
本発明方法における最大の特色は、沈降槽等の凝集沈
降ゾーンにおいて、上記凝集剤と共に水硬性無機固化材
を添加して生成フロックの粗大化と沈降固化とを同時に
達成し、凝集沈降ゾーン底部に、適宜な固化強度に凝固
したケーキ状凝固物を沈澱堆積させる点にある。The greatest feature of the method of the present invention is that, in a coagulation sedimentation zone such as a sedimentation tank, a hydraulic inorganic solidifying material is added together with the coagulant to simultaneously achieve coarsening and sedimentation and solidification of the generated floc. The point is that the cake-like solidified solidified to an appropriate solidification strength is deposited and deposited.
水硬性無機固化材としては、一般に水硬性セメントと
称さえるポルトランドセメント、アルミナセメントを主
として含有する。水硬性石灰、天然セメントなども適用
可能であるが前二者、特にアルミナセメントが最も好ま
しく、更にこれを適量の石膏と併用すると優れた固化性
能を発揮する。最適の処方は、アルミナセメント90〜80
重量%と石膏10〜20重量%との混合物である。The hydraulic inorganic solidifying material mainly contains Portland cement and alumina cement, which are generally called hydraulic cement. Hydraulic lime, natural cement and the like are also applicable, but the former two, especially alumina cement, are most preferable. When this is used in combination with an appropriate amount of gypsum, excellent solidification performance is exhibited. The optimal formula is alumina cement 90-80
% Of gypsum and 10-20% by weight of gypsum.
かかる固化材は前記凝集剤と固化材とが重量比で1/1
〜1/5、好ましくは1/2〜1/4の割合となるよう予め混合
して用いるか、または凝集剤が液体の場合には別個にま
たは添加直前に混合して用いる。In the solidified material, the coagulant and the solidified material are 1/1 by weight.
凝集 1/5, preferably 〜 to し て, and used in advance, or when the flocculant is a liquid, used separately or mixed immediately before addition.
凝集剤および固化材の被処理水への添加量は、両者の
混合物重量として被処理水中の懸濁固形分重量に対し5
〜20%、好ましくは10〜15%程度が適当である。5重量
%未満では凝集沈降並びに固化効果が乏しく、満足すべ
き固化強度の凝固物が得られない。また20重量%を超え
ても効果の増大は伴わず、却って経済的に不利である。The amount of the coagulant and the solidifying agent added to the water to be treated is 5 wt.
-20%, preferably about 10-15%. If it is less than 5% by weight, the coagulation sedimentation and solidification effects are poor, and a solidified product having satisfactory solidification strength cannot be obtained. If the content exceeds 20% by weight, the effect is not increased, and it is rather economically disadvantageous.
沈降分離槽、または凝集沈降槽内で上記凝集剤並びに
固化材の作用により微粒子懸濁物はフロック状となり、
更に急速に凝集し粗大粒子となって槽底に沈澱堆積す
る。その状態で数時間の養生時間を経過すると一軸圧縮
強度(qu)が少なくとも0.1kg/cm2程度のハンドリング
可能な状態にまで固化する。これは例えば石灰アルミナ
セメント(3CaO・Al2O3)成分と、石膏(CaSO4・2H2O)
の成分とを約0.85:0.15の重量比を以て混合した固化材
を用いた場合について見れば、沈降したケーキ状凝固物
に、エトリンガイト相、Ca6Al2(SO4)3(OH)2・26H
2Oを主成分とする無機質水和物マトリックスを形成し、
水中で沈降と同時に固化が行われるものである。In the sedimentation separation tank or the coagulation sedimentation tank, the fine particle suspension becomes a floc due to the action of the coagulant and the solidifying material,
Further, they rapidly aggregate and become coarse particles, and precipitate and deposit on the tank bottom. When a curing time of several hours elapses in this state, the material is solidified to a handleable state with a uniaxial compressive strength (qu) of at least about 0.1 kg / cm 2 . This is, for example, a lime alumina cement (3CaO.Al 2 O 3 ) component and a gypsum (CaSO 4 .2H 2 O)
Component and from about 0.85: Looking at the case where a solidified material obtained by mixing with a weight ratio of 0.15, the cake coagulum settled, ettringite phase, Ca 6 Al 2 (SO 4 ) 3 (OH) 2 · 26H
Form an inorganic hydrate matrix composed mainly of 2 O,
Solidification occurs simultaneously with sedimentation in water.
搬送可能な固化強度に達した頃を見計らって上澄水を
排出または放流し、槽底のケーキ状凝固物は、一軸圧縮
強度が0.1〜0.3kg/cm2の範囲内にあれば、槽底排出口よ
りコンベア、運搬車等適宜な搬送手段上に落下するか、
またはバックホーその他の浚渫手段で容易に取り出すこ
とができる。The upper supernatant water is discharged or released by sure to allow time for reaching the transportable solidification strength, cake coagulum tank bottom, uniaxial compressive strength if in the range of between 0.1 and 0.3 kg / cm 2, Sosokohai From the exit, drop onto a suitable transport means such as a conveyor or a transport vehicle,
Alternatively, it can be easily taken out by a backhoe or other dredging means.
取り出したケーキ状凝固物の見掛け容量をさらに減じ
る為には、それに前記凝集固化材を適宜添加して脱水機
にて脱水すれば、脱水ケーキ自身に固化能があり、時間
の経過と共に逐次固化強度を上昇させることができ、得
られた固化物は含水しても再泥化し難い特長がある。In order to further reduce the apparent volume of the cake-like coagulated product taken out, if the coagulated solidification material is appropriately added thereto and dewatered by a dehydrator, the dewatered cake itself has a solidifying ability, and the solidification strength gradually increases with time. , And the obtained solidified product has a feature that it is difficult to re-mud even if it contains water.
〔実施例〕 本発明方法を以下実施例について説明する。実施例
中、「部」および「パーセント」はすべて重量基準であ
る。[Examples] The method of the present invention will be described below with reference to examples. In the examples, "parts" and "percent" are all based on weight.
実施例1 懸濁物凝集固化用混合剤として、オートセット 固化
剤〔大阪市、(株)オートセット製、セメント/石膏系
固化材の商品名〕8部とムキフロックTM凝集剤〔同社
製、アルミニウム系凝集剤の商品名〕2部とを混合し
た。Example 1 Autoset was used as a mixture for coagulating and solidifying a suspension. Solidification
Agent [Osaka City, manufactured by Autoset Co., Ltd., cement / gypsum system
Product name of solidified material] 8 parts and MukifrockTMFlocculant
Product name of aluminum-based flocculant]
Was.
下水管シールド工事現場から発生する泥水を凝集槽へ
導いた。泥水中の固形分流入量は1500kg/Hr.であった。
この泥水にその含有固形分に対し10%の上記混合剤を添
加したところ、懸濁固形分は急速にフロックを形成しさ
らに粗大粒子に凝集して沈降した。養生時間6〜8Hrで
上澄水を放流し、槽底のケーキ状凝固物の一軸圧縮強度
(qu)を測定したところ0.2kg/cm2のハンドリング可能
強度に達していた。Mud water generated from the sewer pipe shield construction site was led to the coagulation tank. The solid content in the mud was 1500 kg / Hr.
When the mixture was added to the muddy water at 10% of the solid content, the suspended solids rapidly formed flocs, further aggregated into coarse particles, and settled. The supernatant water was discharged at a curing time of 6 to 8 hours, and the uniaxial compressive strength (qu) of the cake-like solidified product at the bottom of the tank was measured. As a result, the handleable strength reached 0.2 kg / cm 2 .
実施例2 オートセット 固化剤7部とキムフロックTM凝集剤3
部との混合剤を調製し、河川浚渫工事現場から発生する
泥水に貯槽中で添加した。泥水中の固形分濃度は6%で
あり、この固形分重量を基準として上記混合剤の添加量
を15%とした。懸濁固形分が凝集沈降した後、上澄水を
放流し、堆積ケーキ状凝固物を更に約8時間養生したと
ころ、搬送可能な固化強度、すなわち、一軸圧縮強度qu
=0.15〜0.25kg/cm2が確保された。Example 2 Automatic set 7 parts of solidifying agent and Kim FlockTMCoagulant 3
Prepare a mixture with the part, generated from the river dredging construction site
It was added to the mud in a storage tank. The solids concentration in the muddy water is 6%
Yes, based on the weight of this solid content,
Was set to 15%. After the suspended solids coagulate and settle, the supernatant water is removed.
It was released, and the solidified cake was cured for about 8 hours.
Roller, solidification strength that can be transported, that is, uniaxial compression strength qu
= 0.15-0.25 kg / cmTwoWas secured.
本発明は、以上説明したような構成と作用とを具える
ので、以下に記載するような効果を奏する。Since the present invention has the configuration and operation as described above, the following effects can be obtained.
被処理液に対して凝集剤と共に固化材をも添加して、
懸濁物のフロック化、凝集粗大化、沈降、固化までを単
一工程を以て一挙に達成するから、従来の如く、高含水
フロックの抜き取り、脱水、固化、乾燥など一連の煩雑
な処理工程が不要となる。従って、従来の工程に要して
いた設備費、運転経費が大幅に節約され、工程の合理化
が達成される。Add a solidifying material together with the flocculant to the liquid to be treated,
Since flocking, flocculation, sedimentation, and solidification of the suspension can be achieved in a single operation in a single operation, a series of complicated processing steps such as extraction, dehydration, solidification, and drying of high water content flocs are not required as in the past. Becomes Therefore, equipment costs and operation costs required for the conventional process are greatly reduced, and the process is rationalized.
得られたケーキ状凝固物は、清澄水と容易に分離し得
るのみならず、再び水と接触しても再泥化することがな
い極めて安定した状態にあるため、雨中無蓋運搬が可能
であり、かつ露天に野積み状態で貯蔵することができる
など、多くの利便がある。The obtained cake-like solidified product can be easily separated from the clarified water, and is in a very stable state without re-mudging even when it comes into contact with water again, so that it can be transported without a lid in the rain. There are many advantages, such as being able to be stored in the open-air and in the open state.
またケーキ状凝固物が適度な固化強度を有するため機
械的取扱が容易で移動、搬送上特段の問題を提起するこ
とがない。Further, since the cake-like solidified material has an appropriate solidification strength, it can be easily handled mechanically and does not pose any particular problem in moving and transporting.
Claims (2)
及び有機凝集剤の少なくとも一種の1重量部と共に、主
としてアルミナセメント90〜80重量%と石膏10〜20重量
%との混合物を含んでなるセメント/石膏系の水硬性無
機固化材の2〜4重量部を、該凝集剤と該固化材との混
合物重量として上記用水または廃水中の懸濁固形分重量
に対し5〜20%添加することにより懸濁物を凝集沈降さ
せつつ固化して0.1〜0.3kg/cm2の一軸圧縮強度を有する
凝固物となすことよりなる水中懸濁物の凝固分離方法。1. The water or wastewater containing suspension contains a mixture of mainly 90 to 80% by weight of alumina cement and 10 to 20% by weight of gypsum together with 1 part by weight of at least one of inorganic and organic flocculants. 2 to 4 parts by weight of the cement / gypsum-based hydraulic inorganic solidifying material consisting of 5 to 20% based on the weight of the suspended solids in the above-mentioned water or wastewater as the weight of the mixture of the coagulant and the solidifying material A method of coagulating and separating a suspension in water, comprising coagulating and sedimenting a suspension to form a coagulate having a uniaxial compressive strength of 0.1 to 0.3 kg / cm 2 .
前記懸濁固形分重量に対し10〜15%である請求項1に記
載の方法。2. The method according to claim 1, wherein the weight of the mixture of the coagulant and the solidifying material is 10 to 15% based on the weight of the suspended solids.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63081332A JP2634846B2 (en) | 1988-04-04 | 1988-04-04 | Coagulation separation method of suspension in water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63081332A JP2634846B2 (en) | 1988-04-04 | 1988-04-04 | Coagulation separation method of suspension in water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01254292A JPH01254292A (en) | 1989-10-11 |
JP2634846B2 true JP2634846B2 (en) | 1997-07-30 |
Family
ID=13743426
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JP63081332A Expired - Lifetime JP2634846B2 (en) | 1988-04-04 | 1988-04-04 | Coagulation separation method of suspension in water |
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JP (1) | JP2634846B2 (en) |
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US5391597A (en) * | 1993-10-04 | 1995-02-21 | Cytec Technology Corp. | Composition and process for increasing the shear strength of processing wastes used for tip building and underground consolidation |
CN109833586B (en) * | 2019-01-23 | 2022-02-25 | 东南大学 | Efficient low-cost treatment method for liquid waste |
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JPS5119240A (en) * | 1974-08-05 | 1976-02-16 | Nippon Soken | KIKAKI |
JPS52101697A (en) * | 1976-02-24 | 1977-08-25 | Denki Kagaku Kogyo Kk | Recovery of iron oxide |
JPS5397251A (en) * | 1977-02-03 | 1978-08-25 | Kajima Corp | Treatment of turbid water |
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1988
- 1988-04-04 JP JP63081332A patent/JP2634846B2/en not_active Expired - Lifetime
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