JPH08294693A - Treatment of waste water by lime milk - Google Patents

Treatment of waste water by lime milk

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Publication number
JPH08294693A
JPH08294693A JP13982895A JP13982895A JPH08294693A JP H08294693 A JPH08294693 A JP H08294693A JP 13982895 A JP13982895 A JP 13982895A JP 13982895 A JP13982895 A JP 13982895A JP H08294693 A JPH08294693 A JP H08294693A
Authority
JP
Japan
Prior art keywords
water
waste water
wastewater
lime milk
treatment
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
JP13982895A
Other languages
Japanese (ja)
Inventor
Tetsujiro Matsuhashi
鉄治郎 松橋
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Individual
Original Assignee
Individual
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Filing date
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Application filed by Individual filed Critical Individual
Priority to JP13982895A priority Critical patent/JPH08294693A/en
Publication of JPH08294693A publication Critical patent/JPH08294693A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To obtain coloress clarified treated water by decoloring orange waste water after biochemical treatment such as activated sludge treatment. CONSTITUTION: The whole of waste water is stirred and mixed in such a state that lime milk is allowed to be present in waste water in a saturated amt. or more and impurities such as chromatic matter or the like in waste water are adsorbed on lime milk to be flocculated and sedimented to obtain clarified treated water. The treated water is neutralized by the addition of aq. sulfuric acid and the dissolving action of carbon dioxide in the atmosphere. Therefore, waste water of a beverage factory of coffee or teas and other every kind of waste water can be easily and cerainly decolored and clarified.

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、飲料食品製造工場の廃
水、製紙工場の廃水、有機質を含むその他の産業廃水、
および一般雑廃水の、廃水処理に関するもので、水関係
の環境保全にも関するものである。
BACKGROUND OF THE INVENTION The present invention relates to wastewater of a beverage food manufacturing plant, wastewater of a paper mill, other industrial wastewater containing organic matter,
It also relates to wastewater treatment of general miscellaneous wastewater, and also to environmental conservation related to water.

【0002】[0002]

【従来の技術】有機質廃水について、従来一般に行なわ
れている生物化学的処理法においては、BODまたはC
OD値を一定水準に低下させ浄化することは、処理プラ
ントの運転管理さえ適正であれば比較的に容易である。
しかし、褐色に着色しているような処理水を、完全に無
色透明な処理水に仕上げることは非常に困難である。そ
のため、環境に実害はないにしても、他の冷却水排水な
どと合流希釈して着色度を緩和し、公共用水に放流する
など次善的な最終処理で妥協していることが、むしろ通
例化している。
2. Description of the Related Art Organic wastewater is treated by BOD or C in a conventional biochemical treatment method.
It is relatively easy to reduce the OD value to a certain level for purification if the operation management of the processing plant is proper.
However, it is very difficult to finish the treated water that is colored brown into a completely colorless and transparent treated water. Therefore, even if there is no real harm to the environment, it is customary to compromise with the suboptimal final treatment, such as condensing and diluting with other cooling water drainage to reduce the degree of coloring and discharging it to public water. It has become.

【0003】このような褐色排水は、製紙工場、化学寒
天工場、コーヒー・茶類の飲料製造工場等の活性汚泥法
処理水の場合に顕著である。その脱色対策として、オゾ
ン酸化、紫外線照射、次亜塩素酸ナトリウムなどによる
酸化漂白、次亜硫酸ナトリウムなどによる還元漂白など
が考えられるが、所用装置の大きさや安全管理、所用薬
品量や有害性、あるいは加熱を要する反応温度条件等の
面で実用性がない。また、それらの理化学的手段による
小規模実験でも、必ずしも満足すべき成果が得られてい
ない。
Such brown waste water is remarkable in the case of water treated by the activated sludge process at a paper manufacturing factory, a chemical agar factory, a coffee / tea beverage manufacturing factory and the like. As decoloring measures, ozone oxidation, ultraviolet irradiation, oxidative bleaching with sodium hypochlorite, reduction bleaching with sodium hyposulfite, etc. can be considered, but the size and safety management of the required equipment, the amount of harmful chemicals and harmfulness, or It is not practical in terms of reaction temperature conditions that require heating. In addition, satisfactory results have not always been obtained even in small-scale experiments using those physicochemical means.

【0004】さらにまた、ポリ塩化アルミニウム(通
称、PAC)などの高性能凝集剤を用いても、褐色に着
色した活性汚泥処理水の脱色は技術的に困難で、仮に脱
色効果が認められる場合があったとしても、活性汚泥生
物相に対する毒性や、経済性の面で実用性がない。すな
わち、とくに用水型製造業においては、褐色排水の脱色
は工業的にほとんど不可能視されているのが現状であ
る。
Furthermore, even if a high-performance flocculant such as polyaluminum chloride (commonly known as PAC) is used, it is technically difficult to decolorize the activated sludge treated water colored in brown, and the decolorizing effect may be recognized. Even if it exists, it is not practical in terms of toxicity to the activated sludge biota and economical efficiency. That is, especially in the water-use manufacturing industry, the decolorization of brown wastewater is considered to be almost impossible industrially.

【0005】[0005]

【発明が解決しようとする課題】一般に化学反応は温度
が高いほど促進される。しかし大量の工場廃水処理にお
いて加熱を必要とする操作は現実的でない。薬品を相当
量使用するような処理法は経済的に不得策なばかりでな
く、新たに別の溶存無機物質濃度を高める不本意な技術
対策となる。主原理に電気エネルギーを利用する方法
は、やはり大量の廃水処理には不適切である。そして、
脱色目的が果せたとしても、濁度が増大するような手段
であれば、別の清澄化二次処理操作が必要になる。この
ようなことから、本発明は、活性汚泥法処理後などの状
況下にあってなお褐色を呈している廃水の、無色清澄化
を主眼として新技術開発を目指したものである。
Generally, a higher temperature promotes a chemical reaction. However, the operation that requires heating in the treatment of a large amount of industrial wastewater is not realistic. A treatment method that uses a considerable amount of chemicals is not only economically disadvantageous, but also an unintended technical measure that newly increases the concentration of another dissolved inorganic substance. The method of utilizing electric energy for the main principle is still unsuitable for the treatment of a large amount of wastewater. And
Even if the decolorization purpose can be fulfilled, another clarification secondary treatment operation is required if the turbidity is increased. In view of the above, the present invention aims at the development of a new technology with a focus on the colorless clarification of waste water that is still brown under the conditions such as after the treatment with the activated sludge method.

【0006】[0006]

【課題を解決するための手段】本発明は、褐色を呈して
いる廃水ないしは処理排水に、酸化カルシウムまたは水
酸化カルシウムを添加し全液を攪拌、混和する操作によ
り、溶解度以上の適量を石灰乳の状態に変化させる。こ
の際の乳化、攪拌過程において、褐色成分物質は石灰乳
に吸着され、石灰分と共に凝集、沈澱し、底部石灰乳以
外の上層は、無色透明水となる。この凝集・沈殿は迅速
に進行する。
Means for Solving the Problems According to the present invention, by adding calcium oxide or calcium hydroxide to brown-colored waste water or treated waste water and stirring and mixing the whole solution, a suitable amount of lime milk having a solubility or higher is obtained. Change to the state of. During the emulsification and stirring process at this time, the brown component substance is adsorbed by the lime milk, aggregates and precipitates with the lime content, and the upper layer other than the bottom lime milk becomes colorless and transparent water. This aggregation / precipitation proceeds rapidly.

【0007】水酸化カルシウムは水に難溶性であるが、
その水溶液はpH約12程度のアルカリ性を呈する。中
和を必要とする場合は、適宜の手段により固液分離した
上澄水に小量適量の硫酸水、液化炭酸など適宜の酸を加
えて中性の処理水とする。ただし、廃水中に相当量のナ
トトリウム分が存在する場合、この中和処理において塩
酸を使用することは、食塩分を生成することになるか
ら、公共用水への放流に対して好ましくない。
Calcium hydroxide is poorly soluble in water,
The aqueous solution exhibits alkalinity with a pH of about 12. When neutralization is required, a small amount of an appropriate amount of sulfuric acid, an appropriate acid such as liquefied carbonic acid is added to the supernatant water obtained by solid-liquid separation by an appropriate means to obtain neutral treated water. However, when a considerable amount of sodium is present in the waste water, the use of hydrochloric acid in this neutralization treatment produces salt, which is not preferable for discharge to public water.

【0008】[0008]

【作用】肉眼的にほぼ透明である活性汚泥法の褐色処理
水は、瀘紙濾過しても色度は変らない。しかし本発明に
よると、褐色成分物質はすぺて石灰乳に吸着され凝集す
る結果、No.2の瀘紙を通過しない大きさの凝集物と
なる。また、石灰分の比重も大きいことにより、凝集物
は、分単位の短い時間で沈降し、水溶液分はすべて無色
透明になる。また、いかなる方法であろうとも固液分離
は容易である。
The brown treated water of the activated sludge method, which is almost transparent to the naked eye, does not change its chromaticity even when filtered with a paper filter. However, according to the present invention, as a result of the brown component material being adsorbed and aggregated by the lime milk, No. It becomes an agglomerate of a size that does not pass through the No. 2 paper. In addition, since the specific gravity of the lime component is also large, the agglomerates settle in a short time of minute unit, and all the aqueous solution components become colorless and transparent. Moreover, solid-liquid separation is easy by any method.

【0009】上記の反応系を開放的な条件で野外に例え
ば1週間放置しても、この清澄化した水質状態は変化せ
ず、安定である。そして、上澄水の大部分を取り捨て、
あるいは上澄水量をそのままにして、これに新たな褐色
廃水を補給し、前記同様に攪拌、静置すると、全く同様
の凝集・沈殿反応が起こり、無色透明水が得られる。つ
まり一般には、微小量の褐色成分物質に対して石灰乳が
充分量存在するので吸着能力限度まで所期の目的反応が
持続する。ちなみに、水酸化カルシウムの溶解度は、2
0℃において、水1kgに対して1.26gに留まる。
Even if the above reaction system is left outdoors under open conditions, for example, for one week, the clarified water quality state does not change and is stable. Then, discard most of the clear water,
Alternatively, when the amount of the supernatant water is left as it is, new brown wastewater is replenished to the solution, and the same aggregation / precipitation reaction occurs by stirring and standing as described above to obtain colorless transparent water. That is, in general, a sufficient amount of lime milk is present with respect to a minute amount of brown component substance, so that the desired target reaction is continued up to the adsorption capacity limit. By the way, the solubility of calcium hydroxide is 2
At 0 ° C., 1.26 g remain for 1 kg of water.

【0010】固液分離した上澄水に酸を加えて中和して
も、もはや無色透明性は変化せず、時日を経過しても安
定な清澄水の状態を維持する。本発明の処理の結果、脱
色効果とともに、COD値も、さらに一段と低下する事
実も、中和による水質の安定性を裏書きしている。
Even if an acid is added to the supernatant water which has been solid-liquid separated to neutralize it, the colorless and transparent property no longer changes, and a stable clear water state is maintained over time. As a result of the treatment of the present invention, the decolorizing effect as well as the fact that the COD value further decreases further endorses the stability of water quality due to neutralization.

【0011】[0011]

【実施例1】コーヒー、茶類、各種果汁等の飲料工場の
活性汚泥法処理施設から排出される最終放流水は清澄化
されてはいるが常に褐色を帯びている。この褐色放流水
11(1kg)に酸化カルシウム約10gを投入し、白
色乳化した沈殿を生成させた。ついで液相全体が一様に
懸濁するように攪拌すると、凝集反応が起こったことが
肉眼的にも明らかに認められた。液相の攪拌運動が止ま
るとともに、凝集物は2〜3分のうちに器底に沈降し、
液相は無色透明に変化した。沈殿部分は褐色成分物質を
吸着したため赤みを帯びた石灰乳となった。
[Example 1] The final discharged water discharged from the activated sludge method treatment facility of a beverage factory for coffee, tea, various fruit juices, etc. is clarified but always brownish. About 10 g of calcium oxide was added to this brown discharged water 11 (1 kg) to generate a white emulsified precipitate. Then, when the whole liquid phase was stirred so as to be uniformly suspended, it was clearly macroscopically recognized that an aggregation reaction had occurred. As the stirring motion of the liquid phase stopped, the agglomerates settled to the bottom in a few minutes,
The liquid phase changed to colorless and transparent. The precipitated portion became a reddish lime milk due to the adsorption of the brown component material.

【0012】この脱色反応前後の水質を比較すると、表
1のようであった。
A comparison of the water quality before and after the decolorization reaction is shown in Table 1.

【0013】なお、同じ褐色放流水11(1kg)に飽
和水酸化カルシウム水溶液を10〜100ml添加、攪
拌したものは、ある程度の凝集沈殿効果が認められた
が、清澄化は不充分であった。
In addition, 10 to 100 ml of saturated calcium hydroxide aqueous solution was added to the same brown discharged water 11 (1 kg) and stirred, but some aggregation and precipitation effect was observed, but clarification was insufficient.

【0014】[0014]

【実施例2】実施例1の脱色反応後の無色透明水を傾斜
して500ml分け取り、硫酸水溶液を用いて中和し
た。中和処理の後も無色透明水としての性状に変化はな
く、常温1週間保持後も変色や沈殿生成は見られなかっ
た。なお、脱色中和水のCOD値は表2のように低下し
た。
Example 2 The colorless transparent water after the decolorization reaction of Example 1 was decanted into 500 ml and neutralized with an aqueous sulfuric acid solution. There was no change in the properties as colorless and transparent water after the neutralization treatment, and no discoloration or precipitate formation was observed even after holding at room temperature for 1 week. The COD value of the decolorized neutralized water decreased as shown in Table 2.

【0015】 電気伝導度の増加は、脱色・中和処理に伴う無機塩の増
加を示す。
[0015] The increase in electrical conductivity indicates an increase in the amount of inorganic salt that accompanies the decolorization / neutralization treatment.

【0016】[0016]

【実施例3】実施例1と同し工場廃水の活性汚泥法処理
最終工程施設、クラリファイヤー上層の褐色水 約10
lをプラスチック容器に汲み取り、酸化カルシウム約2
0gを投入し、器底に石灰乳が生成するのを待って、全
液を攪拌すると、直ちに凝集反応が起こり、数分後沈降
し、液相の褐色は完全に消失し、無色透明に変化した。
これを開放的な状態で野外に自然放置したところ、1週
間後も無色透明の水質を維持した。次にその上澄水の約
3分の2量を傾斜して抜き去り、再びクラリファイヤー
上層の褐色水を追加し、全液を攪拌したところ、やはり
前回同様の凝集・沈殿が起こり、全液相は無色透明化す
こと、そして以後の経時変化がないことが確かめられ
た。
[Embodiment 3] Same as Embodiment 1, the final process facility for the activated sludge process of the factory waste water, the brown water of the upper layer of the clarifier is about 10
Pump 1 l into a plastic container and
When 0 g was added and the lime milk was formed on the bottom of the vessel and the whole solution was stirred, an agglutination reaction occurred immediately and the solution settled after a few minutes, and the brown color of the liquid phase disappeared completely and became colorless and transparent. did.
When this was left to stand outdoors in an open state, colorless and transparent water quality was maintained even after 1 week. Next, about 2/3 of the supernatant water was decanted and removed, and the brown water in the upper layer of the clarifier was added again, and when the whole solution was stirred, the same aggregation and precipitation as before occurred and the whole liquid phase It was confirmed that the sample became colorless and transparent and that it did not change with time.

【0017】傾斜分離した上澄み水を上記のように野外
放置すると、清澄水のpHが経過時日とともに低下し、
pHは11ないしは11以下になった。これは、大気中
の二酸化炭素の溶解による現象と考えられ、気温、水温
および風の条件により数値的な影響度に変化があると認
められた。
When the supernatant water separated by tilting is left outdoors as described above, the pH of the clear water decreases with the passage of time,
The pH dropped to 11 or below 11. It is considered that this is a phenomenon due to the dissolution of carbon dioxide in the atmosphere, and it was recognized that the numerical degree of influence changed depending on the temperature, water temperature and wind conditions.

【0018】[0018]

【実施例4】海藻オゴノリをアルカリ処理して粉末寒天
を製造する化学寒天工場廃水の活性汚泥処理ばっき槽か
ら、ばっき処理中の汚い黄褐色廃水を、いわゆる活性汚
泥菌を含有するままの状態で採取した。この廃水1.8
lをPETボトルにとり、小型エアーポンプにつないだ
エアーストーンを沈めて24時間ばっきを続行し、難消
化性有機物である寒天・海藻の溶解成分および懸濁物質
をさらにいつそう分解させた状態において、酸化カルシ
ウム約5gを投入し、10分後ばっきを停止した。表3
にその効果を示す。
[Example 4] A chemical agar factory wastewater for producing powder agar by treating seaweed Ogonori with alkali was treated from an activated sludge treatment agitation tank. It was collected in the state. This wastewater 1.8
1 in a PET bottle, submerge an air stone connected to a small air pump, and continue the exposure for 24 hours. When the dissolved components and suspended substances of agar and seaweed, which are indigestible organic substances, are further decomposed. Then, about 5 g of calcium oxide was added, and the exposure was stopped after 10 minutes. Table 3
The effect is shown in.

【0019】 [0019]

【0020】酸化カルシウムを添加しなかった対照試験
区は通常のスラッジ沈降性、すなわち30分後のスラッ
ジ容積(SV30)50%であり、通常の上澄み液色
調、すなわち黄褐色であった。 これに対して、酸化カ
ルシウムを添加した本試験区はスラッジの沈降は極めて
速く、10分後のスラッジ容積が約25%となり、上澄
み液はほとんど無色透明になった。
The control test group to which calcium oxide was not added had a normal sludge sedimentation property, that is, a sludge volume after 30 minutes (SV 30 ) of 50%, and a normal supernatant liquid color, that is, a yellowish brown color. On the other hand, in this test section to which calcium oxide was added, sedimentation of sludge was extremely fast, the sludge volume after 10 minutes was about 25%, and the supernatant became almost colorless and transparent.

【0021】[0021]

【実施例5】一般家庭雑廃水の3槽式簡易浄化槽におい
て半嫌気半好気的に生物処理されている腐熟水に、充分
な飽和量の消石灰を投入し、全液を攪拌混和し放置する
と、数分のうちに懸濁物は凝集沈澱し、無臭、無色の清
澄水が得られた。
[Embodiment 5] When a sufficient amount of slaked lime is added to the saponified water that is semianaerobically and semiaerobically biologically treated in the three-tank type simple septic tank of general domestic wastewater, and the whole liquid is stirred and mixed and left to stand. In a few minutes, the suspension was coagulated and precipitated, and odorless and colorless clear water was obtained.

【0022】[0022]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。
Since the present invention is configured as described above, it has the following effects.

【0023】活性汚泥法などの生物処理後、なお褐色に
着色している産業廃水の脱色が、化学的、物理的に単純
な方法、操作により効果的に達成され、無色透明な放流
水とすることができる。しかも、COD値のいっそうの
低減化、廃水および環境の完全な無臭化に貢献する。
After biological treatment such as activated sludge method, decolorization of industrial wastewater which is still colored brown is effectively achieved by a chemically and physically simple method and operation, resulting in colorless and transparent discharged water. be able to. Moreover, it contributes to further reduction of COD value and complete deodorization of wastewater and environment.

【0024】使用する石灰は日常的な化学物質で安全性
に問題はなく、低廉な製品であり、しかも溶解度の小さ
い化合物であるから、経済的な負担が軽い。また、脱色
後の中和処理に、大気中の二酸化炭素の溶解を利用する
ことにより所用酸量をpH値でおよそ1ないしは1以上
低減できる。このことも処理経費の軽減に大いに有効で
ある。
Since the lime used is a daily chemical substance, there is no problem in safety, it is a low-priced product, and it is a compound with low solubility, so the economical burden is low. Further, by utilizing the dissolution of carbon dioxide in the atmosphere for the neutralization treatment after decolorization, the required acid amount can be reduced by about 1 to 1 or more in terms of pH value. This is also very effective in reducing processing costs.

【0025】中和反応において生成するであろう硫酸カ
ルシウム(俗称、石膏)や炭酸カルシウムはいずれも水
に難溶性の化合物であるから、最終処理水の無機塩類濃
度は硬度の高い天然水程度に留まる。
Since calcium sulfate (commonly known as gypsum) and calcium carbonate which are likely to be produced in the neutralization reaction are hardly water-soluble compounds, the concentration of inorganic salts in the final treated water should be as high as natural water with high hardness. stay.

【0026】特にコーヒー・茶類等の飲料工場廃水に画
期的な処理法であるが、その他、各種の産業廃水の脱
色、清澄化に応用でき、さらに、公共用水域に連接する
汚濁水の浄化にも利用できる方法である。
This is an epoch-making treatment method especially for drinking factory wastewater such as coffee and tea, but it can also be applied to decolorization and clarification of various industrial wastewater, and further, contaminated water connected to public water areas. It is also a method that can be used for purification.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 廃水に酸化カルシウム又は水酸化カルシ
ウムを加え、飽和量以上の石灰乳が存在する状態で全液
と攪拌混和し、静置することにより、廃水中の着色成分
物質等の不純分を石灰乳に吸着・凝集沈殿させ、清澄な
処理水に加工する廃水処理法。
1. Calcium oxide or calcium hydroxide is added to wastewater, and the mixture is stirred and mixed with all liquids in the presence of lime milk in a saturated amount or more, and allowed to stand, whereby impurities such as coloring component substances in wastewater are mixed. A wastewater treatment method in which lime milk is adsorbed and coagulated and precipitated, and processed into clear treated water.
【請求項2】 請求項1の方法により得られる清澄な上
澄み水を適宜の方法により固液分離し、硫酸水などの酸
を添加、中和することにより、清澄で中性の処理水に加
工する廃水処理法。
2. The clear supernatant water obtained by the method of claim 1 is subjected to solid-liquid separation by an appropriate method, and an acid such as sulfuric acid is added to neutralize the solution to process it into clear, neutral treated water. Wastewater treatment method.
【請求項3】 請求項2の中和処理の工程の前、又は後
に、上澄み水を大気下にさらし、空気中の二酸化炭素を
自然溶解、あるいは半強制的に溶解させることにより、
アルカリ性被処理水のpHを中性側に低下させる廃水処
理法。
3. Before or after the step of the neutralization treatment of claim 2, by exposing the supernatant water to the atmosphere, the carbon dioxide in the air is naturally dissolved or semi-forced to be dissolved,
A wastewater treatment method that lowers the pH of alkaline water to be neutralized.
JP13982895A 1995-04-26 1995-04-26 Treatment of waste water by lime milk Pending JPH08294693A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13982895A JPH08294693A (en) 1995-04-26 1995-04-26 Treatment of waste water by lime milk

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13982895A JPH08294693A (en) 1995-04-26 1995-04-26 Treatment of waste water by lime milk

Publications (1)

Publication Number Publication Date
JPH08294693A true JPH08294693A (en) 1996-11-12

Family

ID=15254436

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13982895A Pending JPH08294693A (en) 1995-04-26 1995-04-26 Treatment of waste water by lime milk

Country Status (1)

Country Link
JP (1) JPH08294693A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012035183A (en) * 2010-08-05 2012-02-23 Ishii Shoji Kk Method for decoloring and purifying water
CN102718233A (en) * 2011-12-15 2012-10-10 沈阳化工大学 Method for combined treatment on chlorinated waste molten salts and Cl-containing waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012035183A (en) * 2010-08-05 2012-02-23 Ishii Shoji Kk Method for decoloring and purifying water
CN102718233A (en) * 2011-12-15 2012-10-10 沈阳化工大学 Method for combined treatment on chlorinated waste molten salts and Cl-containing waste water

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