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JPH06182355A - Treatment of humic acid-containing water - Google Patents

Treatment of humic acid-containing water

Info

Publication number
JPH06182355A
JPH06182355A JP35598992A JP35598992A JPH06182355A JP H06182355 A JPH06182355 A JP H06182355A JP 35598992 A JP35598992 A JP 35598992A JP 35598992 A JP35598992 A JP 35598992A JP H06182355 A JPH06182355 A JP H06182355A
Authority
JP
Japan
Prior art keywords
humic acid
water
present
treatment
basicity
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
JP35598992A
Other languages
Japanese (ja)
Inventor
Masaki Hoshina
正樹 保科
Hideo Tsugawa
秀夫 津川
Minoru Okada
岡田  稔
Hatsuichi Miwa
肇一 三輪
Takuya Hosoda
拓也 細田
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.)
Toagosei Co Ltd
Taki Chemical Co Ltd
Original Assignee
Toagosei Co Ltd
Taki Chemical 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 Toagosei Co Ltd, Taki Chemical Co Ltd filed Critical Toagosei Co Ltd
Priority to JP35598992A priority Critical patent/JPH06182355A/en
Publication of JPH06182355A publication Critical patent/JPH06182355A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

PURPOSE:To provide a simple flocculation treatment method reduced not only in the use amt. of a chemical agent but also in the generation amt. of sludge. CONSTITUTION:Flocculation treatment is performed using a mixture of aluminum chloride containing 1-5wt.% of a sulfur ion as SO4 and having basicity of 35-65% and polydimethyldiallylammonium chloride. By treating humic acid- containing water by this method, the use amt. of a chemical agent and the generation amt. of sludge are reduced as compared with a case using only a general inorg. flocculant. Further, excellent effect of extremely simplifying flocculation treatment operation is developed as compared with the combined treatment with a general high-molecular flocculant.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、フミン酸を含有する水
に対して有用な水の処理方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for treating water useful for water containing humic acid.

【0002】[0002]

【従来の技術】寒冷地或いは泥炭質の土質からなる地域
では、湖沼、河川の表流水にフミン酸を含有する場合が
多く、また山間部でも植物の枯死物、落葉等からフミン
酸成分が溶出し、これが河川水に流入することが多い。
このようなフミン酸を含有する湖沼、河川水より、工業
用水等の清澄な水を得るために、各種の凝集剤を使用す
る凝集処理方法が一般的に行われている。このような凝
集剤として、硫酸アルミニウム、ポリ塩化アルミニウム
等の無機凝集剤、或いはポリアクリルアミド、或いはそ
の部分加水分解物、アクリル酸エステル系等の有機高分
子凝集剤が一般に使用され、濁質の除去と共にフミン酸
に由来する色度成分の除去が行われている。
2. Description of the Related Art In cold regions or areas of peat soil, humic acid is often contained in the surface water of lakes and rivers, and humic acid components elute from dead plants and leaves in mountainous areas. However, this often flows into river water.
In order to obtain clear water such as industrial water from lake waters and river water containing such humic acid, a coagulation treatment method using various coagulants is generally performed. As such an aggregating agent, an inorganic aggregating agent such as aluminum sulfate or polyaluminum chloride, or a polyacrylamide, or a partial hydrolyzate thereof, or an organic polymer aggregating agent such as an acrylate ester type is generally used to remove turbidity. At the same time, the chromaticity component derived from humic acid is removed.

【0003】しかしながら、このような色度成分を除去
するためには、前述の無機凝集剤の使用では多量の添加
が必要となる。従って、このように処理を行った処理水
は、その処理水のpHが低くなるため、自ずとこの中和
のためのアルカリ剤が多く必要となり、結果として生成
する処理汚泥の量も多くなり、その処分方法が問題とな
る。また、ポリアクリルアミド等の高分子凝集剤を使用
し、このような水の処理を行うと、生成するフロックは
小さく、また軽質であるために凝集沈澱は困難となり、
色度成分は殆ど除去されず、色度成分の除去には殆ど効
果がないのが現状である。
However, in order to remove such a chromaticity component, the use of the above-mentioned inorganic coagulant requires a large amount of addition. Therefore, in the treated water treated in this way, the pH of the treated water becomes low, so naturally a large amount of the alkaline agent for this neutralization is required, and as a result, the amount of the treated sludge to be produced becomes large. Disposal method becomes a problem. Further, when a polymer flocculant such as polyacrylamide is used and such water treatment is carried out, flocs generated are small, and since flocs are light, flocculation and precipitation become difficult,
At present, the chromaticity component is hardly removed, and the removal of the chromaticity component has almost no effect.

【0004】[0004]

【発明が解決しようとする課題】本発明者らはこのよう
な実状に鑑み、フミン酸成分を含む湖沼、河川水より工
業用水等の清澄な水を得る方法について鋭意検討を重ね
た結果、ポリ塩化アルミニウムとポリジメチルジアリル
アンモニウムクロライドとの混合物が、一般の濁質成分
と共にフミン酸成分の除去に顕著な効果を有することを
見出し、本発明を完成したものである。
In view of such circumstances, the present inventors have conducted extensive studies on a method of obtaining clear water such as industrial water from lakes and river water containing humic acid components, and as a result, The present invention has been completed by finding that a mixture of aluminum chloride and polydimethyldiallylammonium chloride has a remarkable effect on the removal of humic acid components as well as general suspended components.

【0005】[0005]

【課題を解決するための手段】即ち本発明は、硫酸イオ
ンをSO4として1〜5重量%の範囲で含有し、且つ塩基度
が35〜65%の範囲のポリ塩化アルミニウムとポリジメチ
ルジアリルアンモニウムクロライドとの混合物を使用す
ることからなるフミン酸含有水の処理方法に関する。
Means for Solving the Problems That is, the present invention provides polyaluminum chloride and polydimethyldiallylammonium containing sulfate ions as SO 4 in the range of 1 to 5% by weight and having a basicity of 35 to 65%. It relates to a method for treating humic acid-containing water, which comprises using a mixture with chloride.

【0006】[0006]

【作用】本発明は、硫酸イオンをSO4として1〜5重量%
の範囲で含有し、且つ塩基度が35〜65%の範囲のポリ塩
化アルミニウム(以下、PACと略記する)とポリジメチ
ルジアリルアンモニウムクロライド(以下、DMDAC
と略記する)とを混合して使用することに特徴を有す
る。
[Function] The present invention uses 1 to 5% by weight of sulfate ion as SO 4.
In the range of 35 to 65% in basicity, and polyaluminum chloride (hereinafter abbreviated as PAC) and polydimethyldiallylammonium chloride (hereinafter DMDAC).
And abbreviated) are used as a mixture.

【0007】本発明で使用するPACは、硫酸イオンを
SO4として1〜5重量%の範囲で含有し、且つ塩基度が35
〜65%の範囲のものを使用することが必要である。即
ち、硫酸イオン量に関しては、この範囲を逸脱しSO4が1
重量%を下廻ると、その凝集効果が低下し、また反対に
SO4が5重量%を上廻ると、ポリ塩化アルミニウム自体が
不安定なものとなり、沈澱物を生成することから同様に
凝集効果は低下し、以て本発明の効果が得られないもの
となる。また塩基度に関しても、この範囲を逸脱する
と、混合した凝集剤は凝集効果が低下するだけでなく不
安定となり、同様に本発明の効果が得られない。また、
DMDACは、その25℃に於ける固有粘度が0.6dl/g以
上のものを使用する。
The PAC used in the present invention contains sulfate ion
It is contained in the range of 1 to 5% by weight as SO 4 , and has a basicity of 35.
It is necessary to use one in the range of ~ 65%. That is, with respect to the amount of sulfate ion, SO 4 deviates from this range and becomes 1
If it is less than wt%, its cohesive effect will decrease, and vice versa.
When SO 4 exceeds 5% by weight, the polyaluminum chloride itself becomes unstable and precipitates are similarly formed, so that the coagulation effect is similarly reduced, and thus the effect of the present invention cannot be obtained. . With respect to the basicity, if the basicity is deviated from this range, the aggregating agent mixed will not only deteriorate the aggregating effect but also become unstable, and similarly the effect of the present invention cannot be obtained. Also,
DMDAC has an intrinsic viscosity of 0.6 dl / g or more at 25 ° C.

【0008】本発明はPACとこのDMDACとの混合
物を、フミン酸含有水に添加して凝集処理を行うが、本
発明はこれらを予め混合しておくことが殊に重要であ
り、処理を行う際にこれらを別々に添加し使用しても本
発明の効果は得られない。更に、PACとDMDACと
の混合割合に関して云えば、PACのAl2O3量とDMD
ACの固形分量が、重量比で100:4〜50の範囲となるよ
うに混合を行う。即ち、両者の混合割合がこの範囲を逸
脱すると、各々単独で使用する場合と効果は変わらず、
本発明の効果は得られない。この混合した薬剤を、攪拌
を行いながらフミン酸を含有する対象水に添加すると、
フロックは速やかに生成し、静置により急速に沈降す
る。これを適当な固液分離手段を用いることによって、
濁質成分と共にフミン酸成分は分離除去される。
In the present invention, a mixture of PAC and this DMDAC is added to humic acid-containing water for coagulation treatment. In the present invention, it is particularly important to premix these, and the treatment is carried out. At this time, the effects of the present invention cannot be obtained even if these are added separately and used. Further, regarding the mixing ratio of PAC and DMDAC, the amount of Al 2 O 3 in PAC and DMD
Mixing is performed so that the solid content of AC is in the range of 100: 4 to 50 by weight. That is, if the mixing ratio of both deviates from this range, the effect is the same as when used alone,
The effect of the present invention cannot be obtained. When this mixed drug is added to the target water containing humic acid while stirring,
Flocs quickly form and settle rapidly upon standing. By using an appropriate solid-liquid separation means,
The humic acid component is separated and removed together with the suspended component.

【0009】[0009]

【実施例】以下に本発明の実施例を掲げ更に説明を行う
が、本発明はこれら実施例に限定されるものではない。
また、本発明に於いて%は特に断らない限り全て重量%
を示す。
The present invention will be further described below with reference to examples of the present invention, but the present invention is not limited to these examples.
Further, in the present invention, all% are by weight unless otherwise specified.
Indicates.

【0010】(実施例1)PAC(Al2O310%,SO43%,塩
基度50%,多木化学(株)製,商品名PAC250A)とDMDAC
(固形分20%,固有粘度1.3dl/g,東亜合成化学工業(株)
製,商品名アロンフロックC-70)を使用し、表1に示した割合で
これらを混合し凝集試験を行った。フミン酸(試薬,和光
純薬(株)製)10gを水道水3Lに加え、更にこれに水酸化ナ
トリウム1.5gを加えて攪拌溶解させた。これを一昼夜放
置した後、濾紙(東洋濾紙No.5A)を使用して吸引濾過を
行った。この濾液を色度が約450度となるように水道水
で希釈し、これを供試原水とした。尚、この供試原水の
アルカリ度は34.9mg/l、pHは7.45であった。
(Example 1) PAC (Al 2 O 3 10%, SO 4 3%, basicity 50%, Taki Chemical Co., Ltd., trade name PAC250A) and DMDAC
(Solid content 20%, Intrinsic viscosity 1.3dl / g, Toa Gosei Chemical Industry Co., Ltd.
Manufactured by Aron Flock C-70) was used, and these were mixed at the ratios shown in Table 1 to carry out an aggregation test. Humic acid (reagent, manufactured by Wako Pure Chemical Industries, Ltd.) (10 g) was added to tap water (3 L), and sodium hydroxide (1.5 g) was further added thereto and dissolved by stirring. After leaving this for one day and night, suction filtration was performed using a filter paper (Toyo Filter Paper No. 5A). This filtrate was diluted with tap water so that the chromaticity was about 450 degrees, and this was used as the test raw water. In addition, the alkalinity of this test raw water was 34.9 mg / l and the pH was 7.45.

【0011】供試原水の500mlを500ml容のビーカーに採
り、ジャーテスターで120rpmで攪拌を行いながら、これ
に表1に示した本発明の混合凝集剤の所定量を添加し
た。攪拌を10分間行い、次いでこれを10分間静置した
後、上澄水の100mlを採取し、濾紙(東洋濾紙No.5A)で濾
過を行った。また、比較のためにポリ塩化アルミニウム
とDMDACとを各々単独で使用し、同様に凝集処理を
行った。尚、二種の凝集剤を使用した場合には、第一の
凝集剤の添加後、5分遅れて第二の凝集剤を添加し、以
下上記と同様に試験を行った。濾過水の色度とpHを測
定し、その結果を表1に示した。尚、色度の測定は410m
μの吸収波長における比色法により行った。また、凝集
剤の添加量は各凝集剤の有姿量で表記した。
500 ml of the test raw water was placed in a 500 ml beaker, and a predetermined amount of the mixed flocculant of the present invention shown in Table 1 was added thereto while stirring with a jar tester at 120 rpm. After stirring for 10 minutes and then allowing it to stand for 10 minutes, 100 ml of supernatant water was collected and filtered through filter paper (Toyo Roshi Paper No. 5A). For comparison, polyaluminum chloride and DMDAC were used alone and similarly subjected to coagulation treatment. When two kinds of coagulant were used, the second coagulant was added 5 minutes after the addition of the first coagulant, and the same test as above was performed. The chromaticity and pH of the filtered water were measured, and the results are shown in Table 1. The measurement of chromaticity is 410m
It was performed by a colorimetric method at an absorption wavelength of μ. In addition, the addition amount of the aggregating agent is represented by the amount of each aggregating agent.

【0012】[0012]

【表1】 注) 凝集剤の混合比はPACのAl2O3量とDMDACの固形分量
の比で示し、凝集剤の添加量は混合物有姿の添加量で示
した。(以下同じ)
[Table 1] Note: The mixing ratio of the coagulant is shown by the ratio of Al 2 O 3 content of PAC and the solid content of DMDAC, and the addition amount of the coagulant is shown by the addition amount of the mixture. (same as below)

【0013】(実施例2)実施例1のフミン酸を使用
し、同様に供試原水を調製した。尚、この供試原水の色
度は419度、アルカリ度は40.5mg/l、pHは7.29であっ
た。表2に示したように、実施例1で使用したPACと
DMDACを用い、これらの混合割合が各々異なった凝
集剤を調製し、これを用いて実施例1と同様に凝集試験
を行った。試験結果を表2に示した。
Example 2 Using the humic acid of Example 1, a test raw water was prepared in the same manner. The chromaticity of this test raw water was 419 degrees, the alkalinity was 40.5 mg / l, and the pH was 7.29. As shown in Table 2, the PAC and DMDAC used in Example 1 were used to prepare aggregating agents having different mixing ratios thereof, and the aggregating test was conducted in the same manner as in Example 1 using the aggregating agents. The test results are shown in Table 2.

【0014】[0014]

【表2】 [Table 2]

【0015】(実施例3)フミン酸(試薬,和光純薬(株)
製)5gを0.05%水酸化ナトリウム1Lに溶解し、これを濾
紙(東洋濾紙No.5A)で濾過し、この濾液の色度が200度に
なるように水道水で希釈した。この希釈液の10Lを採
り、これにカオリナイト(メルク社製)の300mgを添加
し、よく攪拌を行った後、これを一日放置して供試原水
として用いた。尚、この供試原水は色度200度、アルカ
リ度34.9mg/l、濁度29.0ppm、pHは7.25であった。こ
の供試原水を使用し、実施例1の凝集剤を用いて同様に
凝集試験を行い、上澄水を採取して、その色度、濁度、
pHを測定した。結果を表3に示した。
(Example 3) Humic acid (reagent, Wako Pure Chemical Industries, Ltd.)
5 g) was dissolved in 1 L of 0.05% sodium hydroxide, filtered through filter paper (Toyo Filter Paper No. 5A), and diluted with tap water so that the filtrate had a chromaticity of 200 degrees. 10 L of this diluted solution was taken, 300 mg of kaolinite (manufactured by Merck & Co., Inc.) was added thereto, and after stirring well, this was left for one day and used as a test raw water. The sample raw water had a chromaticity of 200 degrees, an alkalinity of 34.9 mg / l, a turbidity of 29.0 ppm, and a pH of 7.25. Using this test raw water, the coagulation test was conducted in the same manner using the coagulant of Example 1, and the supernatant water was collected to determine its chromaticity, turbidity,
The pH was measured. The results are shown in Table 3.

【0016】[0016]

【表3】 [Table 3]

【0017】(実施例4)実施例1と同様に、フミン酸
を使用し供試原水を調製した。尚、この供試原水の色度
は167度、アルカリ度は45.5mg/l、pHは7.54であっ
た。表4に示した本発明の凝集剤及びDMDACに代え
て他の種類の高分子凝集剤とPACとを混合した混合凝
集剤を使用し、実施例1と同様に凝集試験を行った。試
験結果を表5に示した。
(Example 4) As in Example 1, humic acid was used to prepare a test raw water. The chromaticity of this test raw water was 167 degrees, the alkalinity was 45.5 mg / l, and the pH was 7.54. A coagulation test was conducted in the same manner as in Example 1 except that the coagulant of the present invention and DMDAC shown in Table 4 were replaced with a mixed coagulant obtained by mixing another type of polymer coagulant with PAC. The test results are shown in Table 5.

【0018】[0018]

【表4】 注) タキフロックC-403,C-420,C-804,C-808は共に多木化学
(株)製商品名
[Table 4] Note) Takiflock C-403, C-420, C-804, C-808 are all Taki Chemical
Product name

【0019】[0019]

【表5】 [Table 5]

【0020】(比較例1)カオリナイト(メルク社製)の
0.5gを水10Lに添加し、これをよく攪拌した後、一日放
置して供試原水として用い凝集試験を行った。尚、この
供試原水はアルカリ度37.5mg/l、濁度44.2ppm、pHは
6.79であり、色度は0度であった。実施例1で使用した
凝集剤を用い、以下実施例1と同様に凝集試験を行い、
上澄水100mlを採取して、その濁度、pHを測定した。
尚、凝集効果の判定は、積分球式濁度計を用いた上澄水
濁度の測定により行った。結果を表6に示した。
Comparative Example 1 Kaolinite (Merck)
0.5 g was added to 10 L of water, stirred well, and allowed to stand for one day to be used as test raw water for a coagulation test. The sample raw water had an alkalinity of 37.5 mg / l, a turbidity of 44.2 ppm and a pH of
It was 6.79 and the chromaticity was 0 degree. Using the flocculant used in Example 1, a flocculation test is performed in the same manner as in Example 1 below.
100 ml of supernatant water was sampled and its turbidity and pH were measured.
The aggregation effect was determined by measuring the supernatant turbidity using an integrating sphere turbidimeter. The results are shown in Table 6.

【0021】[0021]

【表6】 [Table 6]

【0022】実施例1〜4のようなフミン酸を含有する
水に対しては、本発明の方法は優れた凝集性能を示す
が、フミン酸を含有しない水に対しては、表6の結果か
ら明らかなように、本発明の方法はその効果が殆どな
い。従って、本発明の方法はフミン酸を含有する水に対
してのみ、その効果を有するものである。
For water containing humic acid as in Examples 1 to 4, the method of the present invention exhibits excellent flocculation performance, while for water containing no humic acid the results of Table 6 As is clear from the above, the method of the present invention has almost no effect. Therefore, the method of the present invention has its effect only on water containing humic acid.

【0023】(実施例5)PAC(Al2O310%,SO43%,塩
基度50%,多木化学(株)製,商品名PAC250A)とDMDAC
(固形分20%,固有粘度1.3dl/g,東亜合成化学工業(株)
製,商品名アロンフロックC-70)を使用し、これらを100/5の割合
で混合し凝集剤とした。また比較のために、ポリ塩化ア
ルミニウムについて、硫酸根の無含有品(PAC-1;Al2O310
%,SO40%,塩基度50%)、低塩基度品(PAC-2;Al2O310%,
SO43%,塩基度30%)及び高塩基度品(PAC-3;Al2O310%,S
O43%,塩基度70%)を各々試作し、これらと上記のDM
DACとを100/5の割合で混合し、比較のための凝集剤
とした。実施例1で使用した供試原水を用い、実施例1
と同様に凝集試験を行った。尚、この原水のアルカリ度は3
4.9mg/lであり、pHは7.45であった。試験結果を表7
に示した。
(Example 5) PAC (Al 2 O 3 10%, SO 4 3%, basicity 50%, Taki Chemical Co., Ltd., trade name PAC250A) and DMDAC
(Solid content 20%, Intrinsic viscosity 1.3dl / g, Toa Gosei Chemical Industry Co., Ltd.
Manufactured by Aron Flock C-70), and mixed at a ratio of 100/5 to obtain a flocculant. For comparison, polyaluminum chloride containing no sulfate group (PAC-1; Al 2 O 3 10
%, SO 40 %, basicity 50%), low basicity product (PAC-2; Al 2 O 3 10%,
SO 4 3%, basicity 30%) and highly basic products (PAC-3; Al 2 O 3 10%, S
O 4 3%, basicity 70%) were prototyped respectively, and these and the above DM
DAC was mixed at a ratio of 100/5 to obtain a flocculant for comparison. Using the sample raw water used in Example 1, Example 1
A coagulation test was conducted in the same manner as in. The alkalinity of this raw water is 3
It was 4.9 mg / l and pH was 7.45. Table 7 shows the test results
It was shown to.

【0024】[0024]

【表7】 [Table 7]

【0025】[0025]

【発明の効果】本発明の水処理方法は、特定割合のPA
CとDMDACとを混合して使用することにより、これ
らを別々に添加して使用する場合に比べ、その効果が一
段と優れたものとなる。また、一般に無機凝集剤のみを
使用する場合に比べ、その使用量が少なくなり、発生す
るスラッジの量も少なくなる。
The water treatment method of the present invention has a specific proportion of PA.
By using C and DMDAC as a mixture, the effect becomes more excellent as compared with the case where these are added separately. In addition, compared with the case where only the inorganic coagulant is used, the amount used is generally smaller and the amount of sludge generated is also smaller.

フロントページの続き (72)発明者 岡田 稔 愛知県名古屋市港区船見町一番地の1東亞 合成化学工業株式会社名古屋総合研究所内 (72)発明者 三輪 肇一 兵庫県加古川市別府町新野辺1296−10番地 (72)発明者 細田 拓也 兵庫県加古川市別府町新野辺1406−1番地 神鍬寮内Front page continuation (72) Minoru Okada 1 Minami-ku, Funami-cho, Minato-ku, Nagoya, Aichi Prefecture Toagosei Chemical Industry Co., Ltd. Nagoya Research Institute (72) Inventor Hajime Miwa 1296 Shinnobe, Beppu-cho, Kakogawa-shi, Hyogo −10 Address (72) Takuya Hosoda, Inventor Takuya Hosoda, 1406-1 Shinnobe, Beppu Town, Kakogawa City, Hyogo Prefecture

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 硫酸イオンをSO4として1〜5重量%の範
囲で含有し、且つ塩基度が35〜65%の範囲のポリ塩化ア
ルミニウムとポリジメチルジアリルアンモニウムクロラ
イドとの混合物を使用することからなるフミン酸含有水
の処理方法。
1. A mixture of polyaluminum chloride and polydimethyldiallylammonium chloride containing SO 4 in the range of 1 to 5% by weight as SO 4 and having a basicity in the range of 35 to 65% is used. A method for treating humic acid-containing water.
JP35598992A 1992-12-18 1992-12-18 Treatment of humic acid-containing water Pending JPH06182355A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35598992A JPH06182355A (en) 1992-12-18 1992-12-18 Treatment of humic acid-containing water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35598992A JPH06182355A (en) 1992-12-18 1992-12-18 Treatment of humic acid-containing water

Publications (1)

Publication Number Publication Date
JPH06182355A true JPH06182355A (en) 1994-07-05

Family

ID=18446762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35598992A Pending JPH06182355A (en) 1992-12-18 1992-12-18 Treatment of humic acid-containing water

Country Status (1)

Country Link
JP (1) JPH06182355A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001094265A1 (en) * 2000-06-06 2001-12-13 Mileta Perisic Method for treatment of water containing humic matter for the production of drinking water with enhanced coagulation stage using inorganics polymers of al and activated sio2
KR100350993B1 (en) * 2000-06-21 2002-08-30 주식회사 씨엠아이 Water treatment agent for decomposing fumic acid and manufacturing method of the same
JP2007167721A (en) * 2005-12-20 2007-07-05 Taki Chem Co Ltd Flocculant for wastewater treatment
JP2009101260A (en) * 2007-10-22 2009-05-14 Hymo Corp Humin removing agent and removing method of humin contained in water
WO2016158632A1 (en) * 2015-03-31 2016-10-06 栗田工業株式会社 Flocculant for treating waste water, and method for flocculation treatment of waste water

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001094265A1 (en) * 2000-06-06 2001-12-13 Mileta Perisic Method for treatment of water containing humic matter for the production of drinking water with enhanced coagulation stage using inorganics polymers of al and activated sio2
EA005501B1 (en) * 2000-06-06 2005-02-24 Милета Перишич METHOD FOR TREATMENT OF WATER CONTAINING HUMUS MATTER FOR THE PRODUCTION OF DRINKING WATER WITH ENHANCED COAGULATION STAGE USING INORGANICS POLYMERS OF Al AND ACTIVATED SiO2
KR100350993B1 (en) * 2000-06-21 2002-08-30 주식회사 씨엠아이 Water treatment agent for decomposing fumic acid and manufacturing method of the same
JP2007167721A (en) * 2005-12-20 2007-07-05 Taki Chem Co Ltd Flocculant for wastewater treatment
JP2009101260A (en) * 2007-10-22 2009-05-14 Hymo Corp Humin removing agent and removing method of humin contained in water
WO2016158632A1 (en) * 2015-03-31 2016-10-06 栗田工業株式会社 Flocculant for treating waste water, and method for flocculation treatment of waste water
JP2016190222A (en) * 2015-03-31 2016-11-10 栗田工業株式会社 Flocculant for waste water treatment and waste water agglomeration method

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