JPS6050481B2 - Wastewater treatment method - Google Patents
Wastewater treatment methodInfo
- Publication number
- JPS6050481B2 JPS6050481B2 JP5376277A JP5376277A JPS6050481B2 JP S6050481 B2 JPS6050481 B2 JP S6050481B2 JP 5376277 A JP5376277 A JP 5376277A JP 5376277 A JP5376277 A JP 5376277A JP S6050481 B2 JPS6050481 B2 JP S6050481B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- emulsified
- water
- wastewater
- emulsified oil
- 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
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
- Water Treatment By Sorption (AREA)
Description
【発明の詳細な説明】 本発明は乳化油含有廃水の処理方法に関する。[Detailed description of the invention] The present invention relates to a method for treating wastewater containing emulsified oil.
油分を含有する産業廃水等が河川の汚濁、海洋の汚染等
の公害を惹き起し、大きな社会問題となつている。これ
らの含有廃水の中でも例えば界面活性剤等の共存によつ
て含有油分が乳化状態にある場合、あるいは油分粒径が
極めて微細な場合などの所謂乳化油の処理は粒径の比較
的大きな分散油に較べてその油水分離処理が極めて困難
である。これらの廃水は、機械工業、化学工業、石油工
業、鉄鋼業はもとより、食品工業、塗装工業および繊維
工業等多くの業種の工場より排出されている。従来、乳
化油含有廃水の処理法としては、例えは電解による方法
、塩析剤、凝集剤、吸着剤等を添加して、加圧浮上、凝
集沈澱あるいは枦過等によつて油水分離を行なう方法、
溶剤によつて油分を溶解抽出する方法等が挙げられるが
、いずれの9■を &f■: L゛↓、^ j−、nE
、J4山^漏八゛□呻ナー榛出限界以下とするためには
大規模な設備を要したり、あるいは長時間の処理を必要
としたり、又、方法によつては現在の我国の排出基準で
ある鉱物油5pμm)動植物油30pμm以下に油分濃
度を減少させることが難しいために、何等かの二次処理
を必要とする等の欠点を有している。Industrial wastewater containing oil causes pollution such as river pollution and ocean pollution, which has become a major social problem. Among these wastewaters, when the oil content is in an emulsified state due to the coexistence of surfactants, etc., or when the oil particle size is extremely fine, treatment of so-called emulsified oil is performed using dispersed oil with relatively large particle size. The oil/water separation process is extremely difficult compared to the conventional method. These wastewaters are discharged from factories in many industries, including the machinery industry, chemical industry, petroleum industry, and steel industry, as well as the food industry, painting industry, and textile industry. Conventionally, methods for treating wastewater containing emulsified oil include, for example, electrolysis, addition of salting-out agents, flocculants, adsorbents, etc., and separation of oil and water by pressure flotation, coagulation sedimentation, or filtration. Method,
Methods include dissolving and extracting oil with a solvent, but any of the following 9■ &f■: L゛↓, ^ j-, nE
, J4 Mountain ^^ツ゛□ In order to reduce the level below the moaner eruption limit, large-scale equipment or long-term processing may be required, and depending on the method, the current emissions in Japan may be reduced. Since it is difficult to reduce the oil concentration to 30 pμm or less for animal and vegetable oils (standard mineral oil: 5 pμm), it has drawbacks such as requiring some kind of secondary treatment.
更に、例えば常温で液状のあるいは水と親和性を有する
ように変性されたアミン誘導体をエマルジョン破壊剤と
使用する方法も提案されているが、この破壊剤の使用は
、水と均一に混合されてその効果が発揮できる方法であ
る。この方法は攪拌装置を必要とするのみならず添加し
たエマルジョン破壊剤を分離することが困難であり、被
処理液のCODを規制値以下に低減することは難カルい
。本発明者は、かかる現状に鑑みて被処理水より処理材
を簡単に分離でき、しかも操作が容易な乳化油処理方法
を鋭意検討した結果、水不溶性のある種のアミン化合物
が、エマルジョン破壊及び吸着に効果を有することを見
い出し本発明に到達し1たものである。Furthermore, a method has been proposed in which, for example, an amine derivative that is liquid at room temperature or modified to have an affinity for water is used as an emulsion breaking agent. This is a method that can be effective. This method not only requires a stirring device but also makes it difficult to separate the added emulsion breaker, making it difficult to reduce the COD of the liquid to be treated below the regulatory value. In view of the current situation, the inventors of the present invention have conducted intensive studies on an emulsified oil treatment method that can easily separate the treatment material from the water to be treated and that is easy to operate. The present invention was achieved by discovering that it has an effect on adsorption.
すなわち、本発明は、乳化油含有廃水を処理するに際し
、炭素数6〜60を有するアミン化合物及び/又はその
誘導体と該廃水とを接触せしめることを特徴とする廃水
の処理方法である。That is, the present invention is a method for treating wastewater, which is characterized in that when treating emulsified oil-containing wastewater, the wastewater is brought into contact with an amine compound and/or a derivative thereof having 6 to 60 carbon atoms.
本発明の方法に用いられる炭素数6〜60の炭化水素鎖
を有するアミン化合物としては、1級アミン、2級アミ
ン、3級アミン及びその誘導体であり、より好ましくは
1級アミン、2級アミン及びその誘導体、特に好ましく
は1級アミン(例えばステアルリアミン)及びその誘導
体である。The amine compounds having a hydrocarbon chain having 6 to 60 carbon atoms used in the method of the present invention include primary amines, secondary amines, tertiary amines and derivatives thereof, and more preferably primary amines and secondary amines. and derivatives thereof, particularly preferred are primary amines (eg stearlyamine) and derivatives thereof.
これらのアミン化合物としては、例えばヘキシルアミン
、ヘプチルアミン、オクチルアミン、ノニルアミン、デ
シルアミン、ラウリルアミン、ミリスチルアミン、パル
ミチルアミン、オレイルアミン、ステアリルアミン等の
一級アミン、又はこれらの炭化水素鎖を有するジアミン
、トリアミン等の二級アミン及び三級アミンあるいはそ
のビクラート、種々の塩(例えば塩酸、硫酸、リン酸、
炭酸、酢酸等の塩)、さらにこれらの炭化水素鎖を有す
る一級アミン及び二級アミンの酸アミド、アミジン類、
尿素類及びチオ尿素類や一級アミンのシッフ塩基物等が
ある。なお、アミドとしてはN−ステアリルアセトアミ
ドが好ましい。その他、例えばステアリルプロピレンジ
アミン、半硬化牛脂ジアミン等の多価アミンを用いるこ
ともできる。さらに、硬化牛脂アミン、ココナツトアミ
ン等の炭素数の異なる炭化水素鎖を有するアミン類の混
合物を用いることも可能である。なお、アミン化合物の
一成分が常温で非固体状であつても他のアミン化合物と
の混合物の状態が固体であれば好ましく使用できる。本
発明の方法に用いられるアミン化合物及び/又はその誘
導体は水に不溶性であることが必要である。These amine compounds include, for example, primary amines such as hexylamine, heptylamine, octylamine, nonylamine, decylamine, laurylamine, myristylamine, palmitylamine, oleylamine, and stearylamine, or diamines having a hydrocarbon chain thereof; Secondary amines such as triamines, tertiary amines or their viclates, various salts (e.g. hydrochloric acid, sulfuric acid, phosphoric acid,
salts of carbonic acid, acetic acid, etc.), acid amides and amidines of primary amines and secondary amines having these hydrocarbon chains,
These include ureas and thioureas, and Schiff bases of primary amines. Note that N-stearylacetamide is preferred as the amide. In addition, polyvalent amines such as stearylpropylene diamine and semi-hardened tallow diamine can also be used. Furthermore, it is also possible to use a mixture of amines having hydrocarbon chains having different numbers of carbon atoms, such as hardened tallow amine and coconut amine. Note that even if one component of the amine compound is non-solid at room temperature, it can be preferably used as long as the mixture with other amine compounds is solid. It is necessary that the amine compound and/or its derivative used in the method of the present invention be insoluble in water.
これは本処理材が水中に乳濁する乳化油を除去処理する
ものである為に、処理時に水に溶解.して流出し、除去
処理に必要な有効成分が失われることがないことが望ま
れるからである。本発明に用いられるアミン化合分及び
/又はその誘導体は、分子中に疎水性の炭化水素鎖と親
水性の基とを有する構造になつているが、これはこ5の
疎水性部分と親水性部分とのバランスがエマルジョン粒
子に対して好適に作用し、エマルジョン粒子を親和吸着
し、吸着されたエマルジョン粒子はやがて会合すること
によつて粒子が粗大化され、エマルジョン破壊現象が惹
き起されるものと・考えられる。This is because this treated material removes emulsified oil that becomes emulsified in water, so it dissolves in water during treatment. This is because it is desirable that the active ingredients necessary for the removal treatment not be lost due to leakage. The amine compound and/or its derivative used in the present invention has a structure having a hydrophobic hydrocarbon chain and a hydrophilic group in the molecule. The emulsion particles have a favorable balance with the emulsion particles, and the emulsion particles are adsorbed with affinity, and the adsorbed emulsion particles eventually coalesce to coarsen the particles, causing an emulsion destruction phenomenon. it is conceivable that.
この場合、これらアミン化合物のHl.B価は比較的低
い値のものが有効に作用するので、一般的に炭素類6未
満のアミン化合物では、疎水性部分の占める比率が小さ
く、エマルジョン粒子に対して好適な疎水性、親水性の
バランスが得られない為に、エマルジョン粒子の吸着破
壊の効果は少ないものと考えられる。一方、炭水数が6
0を超えると、疎水性部分の比率が高過ぎるのでやはり
同様にエマルジョン粒子に対して好適な親和性を付与す
ることができないものと考えられる。本発明の方法が対
象とする乳化油とは、液状媒体(主として水)中て乳濁
し得る性質を有する化)合物であり、乳化状の油(例え
ば動、植物の油、鉱物油)を通常示す。In this case, the Hl. A relatively low B number works effectively, so in general, amine compounds with less than 6 carbon atoms have a small proportion of hydrophobic moieties, and have suitable hydrophobic and hydrophilic properties for emulsion particles. Since no balance is obtained, the effect of adsorption and destruction of emulsion particles is considered to be small. On the other hand, the number of carbon dioxide is 6
If it exceeds 0, the ratio of the hydrophobic portion is too high, and it is considered that suitable affinity cannot be imparted to the emulsion particles. The emulsified oil targeted by the method of the present invention is a chemical compound that has the property of being emulsifiable in a liquid medium (mainly water), and emulsified oil (for example, animal or vegetable oil, mineral oil). Usually shown.
しかし、フリーオイルであつても、あるいは通常のオイ
ルの名称で言われないものであつても条件によつて乳化
し得る状態であるなら、本発明の対象とする乳化油に含
まれ・る。本発明になる処理材は、特に微細油滴状物を
粗粒化し、エマルジョン破壊する能力を主として有する
ものである。However, even if it is a free oil or one that is not commonly referred to as an oil, if it can be emulsified under certain conditions, it is included in the emulsified oil that is the object of the present invention. The processing material of the present invention mainly has the ability to coarsen fine oil droplets and destroy emulsions.
従つて、もし仮に油分を吸着して飽和点に達してもなお
かつエマルジョン破壊能・は持続する現象が見られる楊
合は、本処理材で処理した水溶液は乳濁していることが
あるが、これを従来から存在する疎水性のみを有するフ
リーオイル吸着用の油吸着材で処理することによつて乳
濁物を完全に分離することが可能である。従つて、本発
明になる処理材は、フリーオイル処理用の油吸着材と組
合せて用いることによつても有効に乳濁性化合物を処理
てきる。本発明の乳化油を分離する方法は、基本的には
該アミン化合物類と乳化油を含有する水、殊に廃水を効
率よく接触させることによつて行ない得るものである。Therefore, even if oil is adsorbed and the saturation point is reached, the emulsion breaking ability persists, and the aqueous solution treated with this treated material may become emulsified; It is possible to completely separate the emulsion by treating it with a conventionally existing oil adsorbent for free oil adsorption that has only hydrophobicity. Therefore, the treatment material of the present invention can effectively treat emulsifying compounds even when used in combination with an oil adsorbent for free oil treatment. The method of separating emulsified oil of the present invention can basically be carried out by efficiently bringing the amine compounds into contact with water containing emulsified oil, especially waste water.
従つて、アミン化合物類と乳化油廃水とを効率よく接触
できるものであれば如何なる方法を用いてもよいが、一
般的には乳化油廃水をアミン化合物中を通過せしめる方
法が用いられる。例えば、該アミン化合物類の顆粒、細
片または粉末(必要に応じてアミン化合物を粘土物質等
と混練したものを用い得る)をカラムに充填して、乳化
油含有廃水をポンプ等を用いて通液する方法である。ま
た、乳化油含有廃水の貯槽中に該化合物類を投入添加し
、混合攪拌したのち淵過することによつても乳化油を処
理するにとが可能である。この場合、乳化油はエマルジ
ョン破壊され該化合物に吸着される為に、所謂フロック
を生成することなく、簡単な沖過によつて被処理水と油
類とを分離することができる。本発明の処理方法によつ
て、鉱物油、動植物油等からなる乳化油含有廃水の処理
に有効である。Therefore, any method may be used as long as the amine compounds and the emulsified oil wastewater can be brought into contact with each other efficiently, but generally a method of passing the emulsified oil wastewater through the amine compound is used. For example, a column is filled with granules, pieces, or powder of the amine compound (the amine compound may be kneaded with a clay material, etc., if necessary), and emulsified oil-containing wastewater is passed through using a pump or the like. This is a method of making liquid. It is also possible to treat emulsified oil by adding the compounds into a storage tank of emulsified oil-containing wastewater, mixing and stirring, and then filtering. In this case, since the emulsion of the emulsified oil is broken and adsorbed by the compound, the water to be treated and the oils can be separated by simple filtration without forming so-called flocs. The treatment method of the present invention is effective in treating wastewater containing emulsified oils such as mineral oils, animal and vegetable oils, and the like.
例えば、コンプレッサードレイン、界面活性剤を含有す
る水溶性切削油含有廃水、圧延鋼板洗浄廃水、自動車洗
車廃水、あるいは食品工業より排出される動植物油から
なる乳化油等を効率よく処理することができる。本発明
の処理方法は非常に簡単な方法で種々の乳化油含有廃水
を処理することができる。For example, compressor drain, wastewater containing water-soluble cutting oil containing a surfactant, wastewater from washing rolled steel plates, wastewater from car washing, or emulsified oil made of animal and vegetable oils discharged from the food industry can be efficiently treated. The treatment method of the present invention can treat various emulsified oil-containing wastewaters in a very simple manner.
乳化油の分離効果は、粒径10μ以下の微細油滴からな
る乳化油においてn−ヘキサン抽出法による油分濃度測
定によつて検出できない程度にまでに油水を分離し得る
場合もあり、排出基準以下の濃度にまで油分濃度を低下
させることが可能となる。本発*3明は、工業上利用価
値の大きい乳化油廃水処理方法である。以下実施例をあ
げて本発明を説明する。The separation effect of emulsified oil is that it may be possible to separate oil and water to an extent that cannot be detected by measuring the oil concentration using the n-hexane extraction method in emulsified oil that consists of fine oil droplets with a particle size of 10μ or less, and is below the emission standard. It becomes possible to reduce the oil concentration to a concentration of . The present invention*3 is a method for treating emulsified oil wastewater that has great industrial value. The present invention will be explained below with reference to Examples.
実施例中の濃度を表わす「Ppm」はすべて重量基準で
ある。なお、実施例の油分濃度はJISK−0102に
基ずくn−ヘキサン抽出法によつて測定した。All "Ppm" representing concentrations in the examples are based on weight. Note that the oil concentration in Examples was measured by the n-hexane extraction method based on JISK-0102.
実施例1
水溶性切削油カットウェル40(エツソ石油製)を含有
する乳化油含有廃水中にステアリルアミンの粉末を添加
し、マグネテイツクスターラーで攪拌したのちろ過し無
色透明の処理水を得た。Example 1 Stearylamine powder was added to emulsified oil-containing wastewater containing water-soluble cutting oil Cutwell 40 (manufactured by Etsuo Oil Co., Ltd.), stirred with a magnetic stirrer, and then filtered to obtain colorless and transparent treated water. .
該処理水中の油分濃度を測定し、結果を表1にまとめた
。実施例2−3
水溶性切削油カットウェル40(エツソ石油製)を50
ppm含有する乳化油含有廃水中に長鎖脂肪族炭化水素
基を有する1級アミンの粉末を添加〉戸し、マグネテイ
ツクスターラーで攪拌したのち?過し、沖液中の油分濃
度を測定し、結果を表−2に示した。The oil concentration in the treated water was measured and the results are summarized in Table 1. Example 2-3 Water-soluble cutting oil Cutwell 40 (manufactured by Etsuo Oil) 50
Powder of a primary amine having a long-chain aliphatic hydrocarbon group was added to wastewater containing emulsified oil containing ppm and stirred with a magnetic stirrer. The oil concentration in the offshore liquid was measured and the results are shown in Table 2.
実施例4−6
水溶性切削油カットウェル40(エツソ石油製)を50
ppm含有する乳化油含有廃水中に長鎖脂肪族炭化水素
基を有する2級アミンもしくはジアミンの粉末を添加し
、マグネティックスターラーで攪拌したのち濾過し、濾
液中の油分濃度を測定し結果を表−3に示した。Example 4-6 Water-soluble cutting oil Cutwell 40 (manufactured by Etsuo Oil) 50
Powder of a secondary amine or diamine having a long-chain aliphatic hydrocarbon group is added to emulsified oil-containing wastewater containing ppm, stirred with a magnetic stirrer, filtered, and the oil concentration in the filtrate is measured and the results are shown in the table. Shown in 3.
実施例7
300メッシュのステアリルアミン粉末5.0yを直径
147Trmのガラスカラムに充填し、水溶性切削油カ
ットウェル40(エツソ石油製)100ppmを含有す
る乳化油廃水を5m1/分の流速で通液し、カラムより
流出する処理水中の油分濃度を測定したところ、油分濃
度は1.0ppmであつた。Example 7 A glass column with a diameter of 147 Trm was filled with 5.0y of stearylamine powder of 300 mesh, and emulsified oil wastewater containing 100 ppm of water-soluble cutting oil Cutwell 40 (manufactured by Etsuo Oil) was passed through it at a flow rate of 5 ml/min. However, when the oil concentration in the treated water flowing out from the column was measured, the oil concentration was 1.0 ppm.
Claims (1)
を有する水不溶性のアミン化合物及び/又はその誘導体
と該廃水とを接触せしめることを特徴とする乳化油含有
廃水の処理方法。1 When treating wastewater containing emulsified oil, carbon number 6-60
A method for treating emulsified oil-containing wastewater, which comprises bringing the wastewater into contact with a water-insoluble amine compound and/or its derivative having the following.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5376277A JPS6050481B2 (en) | 1977-05-12 | 1977-05-12 | Wastewater treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5376277A JPS6050481B2 (en) | 1977-05-12 | 1977-05-12 | Wastewater treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53138990A JPS53138990A (en) | 1978-12-04 |
| JPS6050481B2 true JPS6050481B2 (en) | 1985-11-08 |
Family
ID=12951818
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5376277A Expired JPS6050481B2 (en) | 1977-05-12 | 1977-05-12 | Wastewater treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6050481B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6238208A (en) * | 1985-08-10 | 1987-02-19 | New Japan Chem Co Ltd | Waste water treatment agent |
-
1977
- 1977-05-12 JP JP5376277A patent/JPS6050481B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53138990A (en) | 1978-12-04 |
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