JP3345670B2 - Flocculant for wastewater treatment - Google Patents
Flocculant for wastewater treatmentInfo
- Publication number
- JP3345670B2 JP3345670B2 JP31596693A JP31596693A JP3345670B2 JP 3345670 B2 JP3345670 B2 JP 3345670B2 JP 31596693 A JP31596693 A JP 31596693A JP 31596693 A JP31596693 A JP 31596693A JP 3345670 B2 JP3345670 B2 JP 3345670B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- aluminum sulfate
- flocculant
- agent
- 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 - Fee Related
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は土木工事又は各種工場
から排出される有機系廃水及び無機系廃水の双方に有効
な凝集剤に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flocculant effective for both organic wastewater and inorganic wastewater discharged from civil engineering works or various factories.
【0002】[0002]
【従来の技術】従来の凝集剤は有機系、無機系に分類さ
れる。有機系凝集剤は有機系高分子を主剤とするもので
凝集によって形成されるフロックが大きくて強い反面、
処理水及び処理スラッジが粘性をもつので後の脱水処理
操作に難点がある他、処理水中に残存する有機質成分が
微生物環境に悪影響を及ぼすおそれがある。また有機系
凝集剤は原水のPHに対して処理水のPHを大きく変化
させる結果、後に薬品による中和工程を必要とする上、
中和槽の設置及び放流までの滞留時間を必要とするので
連続的に排出される汚濁水等の処理には不向きである。
一方、無機系凝集剤は主としてアルミニウムイオンの凝
集力を利用するものであって、処理水の分離性は良好で
あるが有機系凝集剤と比較して凝集力が弱い他、概して
PH値を低下させるので放流前に中和工程が必要とな
る。2. Description of the Related Art Conventional flocculants are classified into organic type and inorganic type. Organic flocculants are based on organic polymers and have large and strong flocs formed by flocculation.
Since the treated water and the treated sludge are viscous, there is a problem in the subsequent dehydration treatment operation, and the organic components remaining in the treated water may adversely affect the microbial environment. In addition, the organic coagulant greatly changes the pH of the treated water with respect to the pH of the raw water, and thus requires a neutralization step with a chemical later,
It is not suitable for treatment of continuously discharged polluted water and the like because it requires a neutralization tank and a residence time until discharge.
On the other hand, inorganic coagulants mainly use the cohesive force of aluminum ions and have good separability of treated water, but have low cohesive force compared to organic coagulants and generally lower the PH value. Therefore, a neutralization step is required before release.
【0003】[0003]
【解決しようとする問題点】望ましい凝集剤は、原水中
の有機質及び無機質成分に影響されずに少ない添加量で
有機系凝集剤と同程度の大きさと強度をもつフロックを
形成することができ、フロックの沈降性が良好で放流に
際して中和処理を必要としないものである。The desired flocculant is capable of forming a floc having the same size and strength as an organic flocculant with a small addition amount without being affected by organic and inorganic components in raw water. The floc has good sedimentation properties and does not require a neutralization treatment when discharged.
【0004】[0004]
【解決手段】本発明凝集剤は、硫酸アルミニウム、硫酸
カルシウム、アルカリ金属炭酸塩及びセメント粉末の配
合物を主剤とし、これにゼオライト粉粒体及び/又はカ
チオン系凝集剤を添加してなるものである。本発明にお
いて凝集主剤自体は公知であって硫酸アルミニウム20
〜40重量部、硫酸カルシウム30〜60重量部、被処
理水のPH低下を5〜9の範囲に調整する炭酸ナトリウ
ム等のアルカリ金属炭酸塩が硫酸アルミニウムに対する
重量比で約3:2の割合で添加され、更に凝集フロック
の強化と沈降性を向上させるセメント粉末が5〜15重
量部配合されてなるものである。なお、硫酸アルミニウ
ムが20重量部より少ないと凝集力が失われ、40重量
部を超えると白濁する。硫酸カルシウムについては30
重量部より少ないとフロックが小さ過ぎ、60重量部に
近づくにつれて白濁が増す。上記凝集主剤を単独で使用
した場合、一般に生成フロックが微細で上澄みにも微細
粒子が浮遊するので処理水の清澄度もよくない。The present invention provides a flocculant comprising a mixture of aluminum sulfate, calcium sulfate, alkali metal carbonate and cement powder as a main component, to which zeolite powder and / or a cationic flocculant are added. is there. In the present invention, the coagulation main agent itself is known, and aluminum sulfate 20
4040 parts by weight, calcium sulfate 30 カ ル シ ウ ム 60 parts by weight, alkali metal carbonates such as sodium carbonate for adjusting the pH reduction of the water to be treated within the range of 599 at a weight ratio of about 3: 2 to aluminum sulfate. The cement powder further contains 5 to 15 parts by weight of a cement powder which is added and further improves cohesive floc and improves sedimentation. If the amount of aluminum sulfate is less than 20 parts by weight, the cohesive force is lost, and if the amount exceeds 40 parts by weight, it becomes cloudy. 30 for calcium sulfate
If the amount is less than 10 parts by weight, the floc is too small, and the cloudiness increases as the amount approaches 60 parts by weight. When the above-mentioned flocculant is used alone, the generated floc is generally fine and fine particles float in the supernatant, so that the clarity of the treated water is not good.
【0005】しかしながら、ゼオライト粉粒体が同時に
添加されるとゼオライト粉粒体自体がフロックの核を形
成することからフロックの生長が促進され、より大きな
強いフロックが形成され、脱水工程における水分離性も
向上する。加えてゼオライトはそのイオン交換能力によ
って、凝集反応に伴って増加する処理水中の硫酸イオン
やカルシウムイオンを減少させる効果がみられる。即
ち、硫酸アルミニウム及び硫酸カルシウムの配合量が前
記上限値に近づくにつれて上澄み水が白濁してくるが、
同量配合物であってもゼオライトを混合した凝集剤は白
濁がなく、清澄度において顕著な差異がみられる。ゼオ
ライト粉粒体の配合量は5〜20重量部の範囲であり、
好ましい範囲は8〜15重量部である。また前記主剤に
カチオン系高分子凝集剤を添加することによって有機質
を含有する被処理水に対しても有効に作用し、無機系、
有機系両水質及びこれらの混合水質に対しても良好な凝
集効果がみられる。これはPHの上昇(PH9以上)に
よって液中のアルミニウムイオンが負荷電になるのを防
ぎ、最適PH域を長時間保持して、より有効に硫酸アル
ミニウムの凝集力を発揮させると共に有機系凝集剤とし
ての機能と相俟って凝集力を高めるものと考えられる。
更にこの場合、ゼオライトが存在するとカチオン系凝集
剤によって低下する被処理水の過度のPH低下を防止で
き、この結果、より多量のカチオンポリマーを混入でき
るものと推測される。但し、カチオンポリマーは1重量
部でも効果があるが、約30重量部を限度として水の分
離性が極めて低下することからカチオン凝集剤の多量添
加は特殊な用途に限定される。However, when the zeolite powder is added at the same time, the growth of the floc is promoted because the zeolite powder itself forms the core of the floc, a larger strong floc is formed, and the water separation property in the dehydration step is increased. Also improve. In addition, zeolite has the effect of reducing sulfate ions and calcium ions in the treated water, which increase with the agglutination reaction, due to its ion exchange capacity. That is, the supernatant water becomes cloudy as the blending amount of aluminum sulfate and calcium sulfate approaches the upper limit,
Even with the same amount of blend, the flocculant mixed with zeolite does not have white turbidity and shows a remarkable difference in clarity. The amount of the zeolite powder is in the range of 5 to 20 parts by weight,
The preferred range is 8 to 15 parts by weight. In addition, by adding a cationic polymer flocculant to the main agent, it effectively acts on water to be treated containing organic substances,
A good coagulation effect is also observed on both organic and mixed water qualities. This prevents aluminum ions in the solution from becoming negatively charged due to a rise in pH (pH 9 or more), maintains the optimum pH range for a long time, more effectively exerts the cohesive force of aluminum sulfate, and an organic coagulant. It is considered that the cohesive force is enhanced in combination with the function as the above.
Further, in this case, it is presumed that the presence of zeolite can prevent an excessive decrease in pH of the water to be treated, which is lowered by the cationic coagulant, and as a result, a larger amount of cationic polymer can be mixed. However, the cationic polymer is effective even at 1 part by weight, but the separation of water is extremely reduced up to about 30 parts by weight. Therefore, the addition of a large amount of the cationic flocculant is limited to a special use.
【0006】[0006]
【実施例】硫酸アルミニウム30重量部、硫酸カルシウ
ム50重量部、炭酸ナトリウム20重量部の割合の混合
物を100としてポルトランドセメント10重量部、ゼ
オライト粉粒体10重量部及びカチオン系有機高分子凝
集剤10重量部を添加配合して凝集剤とした。EXAMPLE A mixture of 30 parts by weight of aluminum sulfate, 50 parts by weight of calcium sulfate, and 20 parts by weight of sodium carbonate was defined as 100, and 10 parts by weight of Portland cement, 10 parts by weight of zeolite powder and 10 parts by weight of a cationic organic polymer flocculant were used. A part by weight was added and blended to form a flocculant.
【0007】[0007]
【試験例1】沖縄県の赤土1000ppm溶液(酸化鉄
を主体とし若干の硫化鉄を含む無機質泥水)1lに対し
て上記凝集剤を20ppm添加した。フロックと上澄み
清澄度を観察した結果は表1のようであった。Test Example 1 20 ppm of the above coagulant was added to 1 liter of a 1,000 ppm solution of red clay in Okinawa (inorganic muddy water containing mainly iron oxide and some iron sulfide). Table 1 shows the results of observing the floc and supernatant clarity.
【0008】[0008]
【表1】 A剤とは実施例凝集剤からゼオライト粉粒体及びカチオ
ン系凝集剤を除去したものであり、B剤とはカチオン系
凝集剤を除去したものであり、またC剤とはゼオライト
を除去したものである。表記したように上澄みに浮遊微
細粒子がなく清澄度は最高であって、凝集によって生成
したフロックは2〜3mmであった。[Table 1] Agent A is the one obtained by removing the zeolite powder and the cationic coagulant from the coagulant of the example, Agent B is the one obtained by removing the cationic coagulant, and Agent C is the one obtained by removing the zeolite It is. As indicated, there was no suspended fine particles in the supernatant, the clarity was the highest, and the floc generated by aggregation was 2-3 mm.
【0009】[0009]
【試験例2】腐食土や有機肥料が混入されている園芸用
黒土の1000ppm溶液1lに対し、フロックの形成
を視認できるまで各凝集剤を添加した。凝集結果は表2
のようであった。Test Example 2 Each flocculant was added to 1 liter of a 1000 ppm solution of horticultural black soil mixed with corroded soil and organic fertilizer until the formation of flocs was visible. Table 2 shows the aggregation results.
It was like.
【0010】[0010]
【表2】 [Table 2]
【0011】[0011]
【試験例3】ベントナイト、CMCを含む土木廃泥水
(川崎市土木局の「大師橋架替下部工事現場」から採取
した)1lに対しA剤及び実施例凝集剤を夫々フロック
の生成が視認できるまで添加した。結果は表3のようで
あった。[Test Example 3] 1 A of the civil engineering waste mud containing bentonite and CMC (collected from the "Dashibashi Bridge Replacement Lower Construction Site" of the Civil Affairs Bureau of Kawasaki City) until the floc formation was visually confirmed with the agent A and the example flocculant, respectively. Was added. The results were as shown in Table 3.
【0012】[0012]
【表3】 なお、実施例品について対液添加率を80にしても40
の場合と同様の結果であり、更に100とした場合も適
正添加量と同様であったが、ろ液がやや白濁した。[Table 3] In addition, even if the rate of addition of the solution to the example product was 80, 40
The results were the same as in the case of (1), and when the value was further set to 100, the amount was the same as the appropriate addition amount, but the filtrate became slightly cloudy.
【0013】A剤はジャーテストによる適正添加率に対
して75〜200%程度まで広い範囲をもっていて廃水
の連続処理に使用可能であるが、前記各データにみるよ
うに使用量が多量であって実用的でない。これに比して
本発明品は75〜250%と更に広い範囲で反応性が認
められ、常時濃度が変化する廃泥水の連続処理にも経済
的に使用できることが明らかである。但し適正添加率の
200%を超えると若干白濁が残る。The agent A has a wide range from about 75% to 200% with respect to the appropriate addition rate according to the jar test and can be used for continuous treatment of wastewater. Not practical. On the other hand, the reactivity of the product of the present invention is recognized in a much wider range of 75 to 250%, and it is clear that it can be economically used for continuous treatment of waste mud whose concentration constantly changes. However, if it exceeds 200% of the appropriate addition rate, a slight cloudiness remains.
【0014】試験例3の被処理水の処理前後の水質変化
は表4のようであって、BOD除去率95%、COD除
去率96.3%、SS除去率は99.9%である。The change in water quality before and after treatment of the water to be treated in Test Example 3 is as shown in Table 4. The BOD removal rate is 95%, the COD removal rate is 96.3%, and the SS removal rate is 99.9%.
【0015】[0015]
【表4】 [Table 4]
【0016】[0016]
【効果】本発明凝集剤は有機系廃水、無機系廃水及び両
者の混合廃水をも処理対象水として有効に使用できるも
のであり、しかも使用量が少なくて済むので経済的であ
る。また、本剤添加によって生成されるフロック径が大
きく脱水に有利である上、適正添加率の範囲が40〜8
0mg/lまで広い範囲で使用できる。処理水のPH変
動が少ない上、硫酸アルミニウムと炭酸ナトリウムの配
合比率を調整することによって処理水のPH値を常に中
性域に留めることもできる。更に本発明凝集剤中の有機
剤量は僅かであって従来の有機剤のみによる処理と異な
り処理水中の残存有機物が少ないから処理水の水質は良
好であって微生物環境に与える影響も少なくて済む効果
がある。The coagulant of the present invention can effectively use organic wastewater, inorganic wastewater, and wastewater mixed with both as wastewater to be treated, and is economical because the amount used is small. In addition, the floc diameter generated by the addition of the present agent is large, which is advantageous for dehydration, and the range of the appropriate addition rate is 40 to 8
It can be used in a wide range up to 0 mg / l. The pH value of the treated water is small, and the PH value of the treated water can always be kept in a neutral range by adjusting the mixing ratio of aluminum sulfate and sodium carbonate. Further, the amount of the organic agent in the flocculant of the present invention is small, and unlike the conventional treatment using only an organic agent, the amount of residual organic matter in the treated water is small, so that the quality of the treated water is good and the influence on the microbial environment can be reduced. effective.
Claims (4)
酸カルシウム30〜60重量部と、PH調整剤として前
記硫酸アルミニウムに対して重量比で約3:2の割合の
アルカリ金属炭酸塩と凝集フロック沈降剤としてセメン
ト粉末5〜15重量部が配合された凝集主剤に対してゼ
オライト粉粒体が5〜20重量部均一に配合されてなる
凝集剤。1. 20 to 40 parts by weight of aluminum sulfate, 30 to 60 parts by weight of calcium sulfate, an alkali metal carbonate as a pH adjuster in a weight ratio of about 3: 2 with respect to the aluminum sulfate, and flocculent flocculation. An aggregating agent comprising 5 to 20 parts by weight of a zeolite powder uniformly mixed with 5 to 15 parts by weight of a cement powder as an agent.
酸カルシウム30〜60重量部と、PH調整剤として前
記硫酸アルミニウムに対して重量比で約3:2の割合の
アルカリ金属炭酸塩と凝集フロック沈降剤としてセメン
ト粉末5〜15重量部が配合された凝集主剤に対してカ
チオン系凝集剤が1〜20重量部均一に配合されてなる
凝集剤。2. 20 to 40 parts by weight of aluminum sulfate, 30 to 60 parts by weight of calcium sulfate, an alkali metal carbonate as a pH adjuster in a weight ratio of about 3: 2 with respect to the aluminum sulfate, and flocculent flocculation. A coagulant comprising 1 to 20 parts by weight of a cationic coagulant uniformly mixed with 5 to 15 parts by weight of a cement powder as an agent.
酸カルシウム30〜60重量部と、PH調整剤として前
記硫酸アルミニウムに対して重量比で約3:2の割合の
アルカリ金属炭酸塩と凝集フロック沈降剤としてセメン
ト粉末5〜15重量部が配合された凝集主剤に対してゼ
オライト粉粒体5〜20重量部とカチオン系凝集剤1〜
30重量部が均一に配合されてなる凝集剤。3. An aluminum sulfate (20 to 40 parts by weight), calcium sulfate (30 to 60 parts by weight), an alkali metal carbonate in a weight ratio of about 3: 2 with respect to the aluminum sulfate as a pH adjuster, and flocculated floc sedimentation. 5 to 20 parts by weight of zeolite powder and cationic coagulant 1 to 5 to 15 parts by weight of cement powder as an agent
A coagulant in which 30 parts by weight are uniformly blended.
シウム50重量部、炭酸ナトリウム20重量部、セメン
ト10重量部、ゼオライト粉粒体10重量部及びカチオ
ン系凝集剤10重量部が均一に配合されてなる凝集剤。4. A mixture of 30 parts by weight of aluminum sulfate, 50 parts by weight of calcium sulfate, 20 parts by weight of sodium carbonate, 10 parts by weight of cement, 10 parts by weight of zeolite powder and 10 parts by weight of a cationic coagulant. Flocculant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31596693A JP3345670B2 (en) | 1993-11-22 | 1993-11-22 | Flocculant for wastewater treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31596693A JP3345670B2 (en) | 1993-11-22 | 1993-11-22 | Flocculant for wastewater treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07136409A JPH07136409A (en) | 1995-05-30 |
JP3345670B2 true JP3345670B2 (en) | 2002-11-18 |
Family
ID=18071733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31596693A Expired - Fee Related JP3345670B2 (en) | 1993-11-22 | 1993-11-22 | Flocculant for wastewater treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3345670B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09276604A (en) * | 1996-02-16 | 1997-10-28 | Chiiki Shinko Jigyodan:Kk | Flocculant |
JP2004305893A (en) * | 2003-04-07 | 2004-11-04 | Junsuke Haruna | Solid-state waste water treating agent using artificial zeolite |
JP2005007250A (en) * | 2003-06-17 | 2005-01-13 | Fumiyoshi Yoshioka | Sludge treatment apparatus and sludge treatment method |
CN112194230A (en) * | 2020-09-27 | 2021-01-08 | 水之清环保科技(上海)有限公司 | Composite flocculant for wastewater treatment |
-
1993
- 1993-11-22 JP JP31596693A patent/JP3345670B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JPH07136409A (en) | 1995-05-30 |
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