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JPH0453561B2 - - Google Patents
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JPH0453561B2 - - Google Patents

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Publication number
JPH0453561B2
JPH0453561B2 JP59058163A JP5816384A JPH0453561B2 JP H0453561 B2 JPH0453561 B2 JP H0453561B2 JP 59058163 A JP59058163 A JP 59058163A JP 5816384 A JP5816384 A JP 5816384A JP H0453561 B2 JPH0453561 B2 JP H0453561B2
Authority
JP
Japan
Prior art keywords
water
bentonite
lime
present
particles
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
Application number
JP59058163A
Other languages
Japanese (ja)
Other versions
JPS60202707A (en
Inventor
Yoshiro Higuchi
Sadami Emura
Shoichi Emori
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.)
SEIKEN KAGAKU KK
Original Assignee
SEIKEN KAGAKU KK
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 SEIKEN KAGAKU KK filed Critical SEIKEN KAGAKU KK
Priority to JP5816384A priority Critical patent/JPS60202707A/en
Publication of JPS60202707A publication Critical patent/JPS60202707A/en
Publication of JPH0453561B2 publication Critical patent/JPH0453561B2/ja
Granted legal-status Critical Current

Links

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、各種産業より排出される廃水中の各
種微粒子を沈降させる方法に関するものである。 現在、各種産業において排出される微細粒子の
懸濁水の処理については、種々の無機あるいは有
機系の凝集剤を単独もしくは併用して処理を行つ
ているが、その効果はきわめて不充分であるた
め、やむをえず天日乾燥を行つている状態であ
る。 本発明者らは、上記の問題を解決するため種々
研究を行つた結果、石膏の共沈作用により容易に
処理できることを見出し、本発明を完成するに至
つた。すなわち、本発明は、微粒子懸濁水に対し
て石炭または石灰乳を石灰分として0.1〜1.0%加
えた後、硫酸を用いてPH6.0〜8.0に調整し、微粒
子を沈降させることを特徴とする微粒子懸濁水の
処理方法である。 本発明でいう微粒子懸濁水は、ベントナイト懸
濁水、粘土懸濁水、水酸化第2鉄懸濁水、パルプ
廃液、澱粉廃液、セメント廃液などであるが、も
つとも分離沈降の困難であるベントナイト懸濁水
を例にとり、本発明の方法について説明する。 周知のように、ベントナイト含有水はきわめて
安定な懸濁水を作るので、この性質を利用して土
木、建設などの工事に多量用いられているが、不
用となつたベントナイト液の処理、すなわち、水
とベントナイトとの分離はきわめて困難で、数日
間静置しても、また、遠心分離機に掛けても、透
明な上澄液を得ることはできない。本発明の方法
は、このベントナイト液に少量の石灰粉または石
灰乳を加え、均一に混合した後、希硫酸を用いて
PHを6.0〜8.0に調整するだけの簡易な処理である
が、遠心分離を行うことにより、実に総液量の80
%もの透明水を分離することが可能である。 本発明の石灰または石灰乳を加えることによる
上記作用機構は明らかではないが、ベントナイト
粒子あるいはその他の分離し難い粒子は、その粒
子が水加され比重が水に近くなつているため、遠
心力を掛けても沈降し難いもので、これら粒子に
石膏を共析させ、粒子自体の比重を重くすること
により、沈降が容易になるものと推定される。石
灰または石灰乳の添加量は、微粒子懸濁水に対し
石灰分として0.1〜1.0%であり、0.1%より少ない
と、微粒子を充分に沈降させることができなくな
り、また、1.0%より多くしても微粒子を沈降さ
せる効果は変わらなくなるので、1.0%より多く
する必要はない。 本発明と従来法との比較試験結果を示すと、次
のとおりである。 (1) 試験に使用したベントナイト液 (イ) 使用ベントナイト:西毛開発株式会社製250
メツシユベントナイト (ロ) ベントナイト液の調整:純水に上記ベントナ
イトを5%w/vの割合で添加して充分に攪拌
懸濁させる。 (2) 試験方法 上記ベントナイト液各100c.c.に各種凝集剤を添
加した後、遠心分離機(毎分3000回転)に30分間
掛けた場合の生成する透明水層の総液量に対する
比率、および分離したベントナイト層の水分を測
定した。その結果を下表に示す。
The present invention relates to a method for settling various fine particles in wastewater discharged from various industries. Currently, various inorganic or organic flocculants are used alone or in combination to treat suspended water containing fine particles discharged in various industries, but their effects are extremely insufficient. We have no choice but to dry it in the sun. The present inventors conducted various studies to solve the above-mentioned problems, and as a result, they discovered that gypsum can be easily treated by coprecipitation, and have completed the present invention. That is, the present invention is characterized in that after adding 0.1 to 1.0% of coal or milk of lime as a lime content to the fine particle suspension water, the pH is adjusted to 6.0 to 8.0 using sulfuric acid, and the fine particles are precipitated. This is a method for treating fine particle suspension water. The particulate suspension water referred to in the present invention includes bentonite suspension water, clay suspension water, ferric hydroxide suspension water, pulp waste liquid, starch waste liquid, cement waste liquid, etc. Bentonite suspension water, which is difficult to separate and settle, is an example. Firstly, the method of the present invention will be explained. As is well known, bentonite-containing water forms extremely stable suspended water, and is used in large quantities in civil engineering and construction projects due to this property. It is extremely difficult to separate the bentonite from the bentonite, and it is not possible to obtain a clear supernatant even after leaving it for several days or using a centrifuge. In the method of the present invention, a small amount of lime powder or lime milk is added to this bentonite liquid, mixed uniformly, and then diluted sulfuric acid is used.
Although it is a simple process that only adjusts the pH to 6.0 to 8.0, centrifugation actually reduces the total liquid volume by 80%.
It is possible to separate as much as % of clear water. Although the mechanism of action of the addition of lime or milk of lime of the present invention is not clear, bentonite particles or other particles that are difficult to separate do not absorb centrifugal force because the particles are added with water and have a specific gravity close to that of water. It is difficult to settle even if the particles are multiplied, and it is presumed that by making these particles eutectoid with gypsum and increasing the specific gravity of the particles themselves, sedimentation becomes easier. The amount of lime or milk of lime to be added is 0.1 to 1.0% as lime content to the fine particle suspension water; if it is less than 0.1%, the fine particles cannot be sufficiently settled, and even if it is more than 1.0%, Since the effect of settling fine particles remains the same, there is no need to increase the amount more than 1.0%. The comparative test results between the present invention and the conventional method are as follows. (1) Bentonite liquid used in the test (a) Bentonite used: 250 manufactured by Nishige Kaihatsu Co., Ltd.
Mesh bentonite (b) Preparation of bentonite liquid: Add the above bentonite to pure water at a ratio of 5% w/v and stir and suspend thoroughly. (2) Test method: After adding various flocculants to 100 c.c. of each of the above bentonite liquids, the ratio of the transparent water layer to the total liquid volume that is generated when the mixture is placed in a centrifuge (3000 revolutions per minute) for 30 minutes, And the water content of the separated bentonite layer was measured. The results are shown in the table below.

【表】【table】

【表】 以下、本発明の実施例を挙げて説明する。 実施例 1 ベントナイト液(水分94%)10に7.5%石灰
乳1を加え、攪拌した後、10%硫酸1.02を加
えてPH8.0とし、遠心分離(毎分3000回転)を30
分行つたところ、6.9の透明水が分離し、ベン
トナイト層の水分は76%であつた。なお、ベント
ナイト液をそのまゝ遠心分離機に掛けても、透明
水は得られなかつた。 実施例 2 粘土懸濁水(水分97.5%)10に石灰粉末75g
を加え、均一に混合した後、10%希硫酸740mlを
加えてPH6.9とし、遠心分離(毎分3000回転)を
30分行つたところ、8.8の透明水が分離し、分
離した粘土層の水分は68.3%であつた。なお、粘
土液をそのまゝ遠心分離機に掛けても、透明水は
得られなかつた。 実施例 3 水酸化第2鉄2.5%懸濁水10を実施例1と同
様の操作を行つたところ、8.4の透明水が得ら
れ、その水酸化第2鉄層の水分は76%であつた。
水酸化第2鉄液をそのまゝ遠心分離した場合に
は、透明水7.0が得られ、その水酸化第2鉄層
の水分は91.7%であつた。
[Table] The present invention will be described below with reference to Examples. Example 1 Add 1 part of 7.5% milk of lime to 10 parts of bentonite liquid (moisture 94%), stir, add 1.0 parts of 10% sulfuric acid to adjust the pH to 8.0, and centrifuge (3000 revolutions per minute) for 30 parts.
After 6.9 minutes of separation, clear water of 6.9% was separated, and the moisture content of the bentonite layer was 76%. Note that even if the bentonite liquid was directly applied to a centrifuge, clear water could not be obtained. Example 2 75 g of lime powder in clay suspension water (moisture 97.5%) 10
After adding and mixing uniformly, add 740 ml of 10% dilute sulfuric acid to adjust the pH to 6.9, and centrifuge (3000 revolutions per minute).
After 30 minutes, 8.8 ml of clear water was separated, and the moisture content of the separated clay layer was 68.3%. Note that even if the clay solution was directly applied to a centrifuge, clear water could not be obtained. Example 3 When a 2.5% ferric hydroxide suspension water 10 was subjected to the same operation as in Example 1, 8.4% transparent water was obtained, and the water content of the ferric hydroxide layer was 76%.
When the ferric hydroxide solution was centrifuged as it was, clear water of 7.0% was obtained, and the water content of the ferric hydroxide layer was 91.7%.

Claims (1)

【特許請求の範囲】[Claims] 1 微粒子懸濁水に対して石灰または石灰乳を石
灰分として0.1〜1.0%加えた後、硫酸を用いてPH
6.0〜8.0に調整し、微粒子を沈降させることを特
徴とする微粒子懸濁水の処理方法。
1. Add 0.1 to 1.0% of lime or milk of lime to the fine particle suspension water, then PH it with sulfuric acid.
A method for treating fine particle suspended water, the method comprising adjusting the water to 6.0 to 8.0 and allowing the fine particles to settle.
JP5816384A 1984-03-28 1984-03-28 Treatment of suspension water of fine granule Granted JPS60202707A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5816384A JPS60202707A (en) 1984-03-28 1984-03-28 Treatment of suspension water of fine granule

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5816384A JPS60202707A (en) 1984-03-28 1984-03-28 Treatment of suspension water of fine granule

Publications (2)

Publication Number Publication Date
JPS60202707A JPS60202707A (en) 1985-10-14
JPH0453561B2 true JPH0453561B2 (en) 1992-08-27

Family

ID=13076321

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5816384A Granted JPS60202707A (en) 1984-03-28 1984-03-28 Treatment of suspension water of fine granule

Country Status (1)

Country Link
JP (1) JPS60202707A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0813357B2 (en) * 1990-06-05 1996-02-14 株式会社海洋蘇生技術研究所 Treatment method of sludge water collected from aquaculture fishing grounds
JPH04161293A (en) * 1990-10-26 1992-06-04 Sato Kogyosho:Kk Treatment of fine particle suspended water

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57140694A (en) * 1981-02-24 1982-08-31 Nippon Chem Ind Co Ltd:The Purification of waste water in construction work

Also Published As

Publication number Publication date
JPS60202707A (en) 1985-10-14

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