JPS6249914A - Treatment of oil-contaminated water - Google Patents
Treatment of oil-contaminated waterInfo
- Publication number
- JPS6249914A JPS6249914A JP18862585A JP18862585A JPS6249914A JP S6249914 A JPS6249914 A JP S6249914A JP 18862585 A JP18862585 A JP 18862585A JP 18862585 A JP18862585 A JP 18862585A JP S6249914 A JPS6249914 A JP S6249914A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- inorg
- contaminated water
- rubber
- activated carbon
- 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
Links
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、各種の油水混合物、都市下水や1潟廃水等で
、乳化安定化された油水混合物の油分を吸着除去する処
理方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a treatment method for adsorbing and removing oil from emulsion-stabilized oil-water mixtures such as various oil-water mixtures, urban sewage, Ichigata wastewater, etc.
従来の技術及びその問題点
乳化安定化した油分を含む含油廃水の処理方法として、
硫酸アルミニウムや鉄塩を多量に添加して乳化油を破壊
し、沈澱させて分離する方法があるが、装置が大規模と
なり、分離物の処理が厄介なだめ、吸着材による吸着除
去法が注目され、吸着材として種々のものが提案されて
いる0例えば特開昭52−91791号には繊維物質か
らなる成形物を重合体エマルジョンに浸漬処理後、鉄系
の化合管を付着させたものが提案されている。しかしな
がら、このものは鉄系化合物で乳化を破壊し、a継物質
に乳化を破壊して生じた油を吸着させるものと考えられ
るが、繊m物質の油吸着当量は十分でない欠点がある。Conventional techniques and their problemsAs a method for treating oil-containing wastewater containing emulsion-stabilized oil,
There is a method of adding a large amount of aluminum sulfate or iron salts to destroy the emulsified oil and precipitate it to separate it, but this requires a large-scale equipment and the treatment of the separated product is cumbersome, so the adsorption removal method using an adsorbent has attracted attention. Various types of adsorbents have been proposed.For example, Japanese Patent Application Laid-open No. 52-91791 proposes an article in which a molded article made of fiber material is immersed in a polymer emulsion and then an iron-based compound pipe is attached. has been done. However, although it is thought that this material destroys emulsification with an iron-based compound and adsorbs the oil produced by destroying the emulsification into the a-substance material, it has the drawback that the oil adsorption equivalent of the fiber m material is not sufficient.
一方、油吸着性ゴムの粉末は、油、特に石油系の油の吸
着能力が大きいが、乳化油に対しては、非乳化状態の場
合に比べて吸着能力が極めて劣っている。On the other hand, oil-absorbing rubber powder has a high ability to adsorb oil, especially petroleum-based oil, but its ability to adsorb emulsified oil is extremely inferior to that in a non-emulsified state.
問題点を解決するだめの手段
本発明者らは、油汚濁水を好適に処理するためには乳化
状態を破壊させるような状態で油分を吸着除去する必要
があることを見出し1種々の吸着剤の組合せについて検
討を重ねた結果、油吸収性又は油吸着性ゴム粉末と、活
性炭、無機質吸着剤又は無機多孔質物質から選ばれた少
なくとも11!lとの組合せが乳化油(こ対する優れた
吸着能力を示すことを見出し、本発明を完成するに至っ
た。Means to Solve the Problem The present inventors discovered that in order to properly treat oil-contaminated water, it is necessary to adsorb and remove oil in a state that destroys the emulsified state.1. As a result of repeated studies, we found that at least 11 combinations were selected from oil-absorbing or oil-absorbing rubber powder, activated carbon, inorganic adsorbent, or inorganic porous material! The present invention was completed based on the discovery that the combination with 1 exhibits excellent adsorption ability for emulsified oil.
本発明に係る油汚濁水の処理方法は、エマルジョン化し
た油分を含む汚濁水に油吸収性又は油吸着性ゴムと活性
炭、無機質吸着剤又は無機多孔質物質から選ばれた少な
くとも1種とを添加してエマルジョン化した油分を除去
することを特徴とするものである。The method for treating oil-contaminated water according to the present invention includes adding an oil-absorbing or oil-absorbing rubber and at least one selected from activated carbon, an inorganic adsorbent, or an inorganic porous material to emulsified oil-containing polluted water. This method is characterized by removing oil that has been emulsified.
油吸収性又は油吸着性ゴムとしては、スチレン・ブタジ
ェンゴム、ブタジェンゴム、エチレン・プロピレンゴム
、ブチルゴム、イソプレンゴム。Examples of oil-absorbing or oil-absorbing rubbers include styrene-butadiene rubber, butadiene rubber, ethylene-propylene rubber, butyl rubber, and isoprene rubber.
天然ゴム及びノルボルネン系ゴムが挙げられ、特番こノ
ルボルネンを開環重合して得られるノルボルネン系ゴム
は、油の吸収性又は吸着性に優れ、好ましく用いられる
。Examples include natural rubber and norbornene rubber, and norbornene rubber obtained by ring-opening polymerization of norbornene is preferably used because it has excellent oil absorption or adsorption properties.
また、活性炭は、通常の吸着用活性炭が用いられ、無機
質吸着剤又は無機多孔質物質(以下、無機鉱物質という
)としては、バーミキュライト。Further, as the activated carbon, ordinary activated carbon for adsorption is used, and as the inorganic adsorbent or inorganic porous material (hereinafter referred to as inorganic mineral material), vermiculite is used.
ケイソウ土、活性白土、パーライト、タルク、ベントナ
イト、マイカ、シラスバルーン等を挙げることができる
。Examples include diatomaceous earth, activated clay, perlite, talc, bentonite, mica, and shirasu balloon.
次に、油吸収性又は油吸着性ゴム粉末としては粒度は1
朋以下殊に平均粒径α3〜α8朋程度が油吸着能力及び
取扱性の点から好ましく、また、活性炭又は無機鉱物質
の粒径は01〜5fI#Iの範囲が好ましく用いられる
。01闇以下では粉末ゴムが油を吸着したときブロック
化を生じ易く、そのため吸着能力が劣ることとなり、ま
た5簡以上では粒径が大でゴム粉末との均一混合ができ
ず偏在するからである。Next, as an oil-absorbing or oil-absorbing rubber powder, the particle size is 1
In particular, an average particle diameter of about .alpha.3 to .alpha.8 is preferable from the viewpoint of oil adsorption ability and ease of handling, and the particle diameter of the activated carbon or inorganic mineral substance is preferably in the range of 0.1 to 5 fI#I. If the powder rubber is less than 01, it tends to form blocks when it adsorbs oil, resulting in poor adsorption ability, and if it is more than 5, the particle size is large and cannot be mixed uniformly with the rubber powder, resulting in uneven distribution. .
油吸収(着]性ゴム粉末と、活性炭又は無機鉱物質(以
下、両者を併せて単に混合剤と略称する)の混合比率は
重量比で、ゴム粉末:混合剤が1=1〜1:10の範囲
が好ましく、混合剤が1以下ではエマルジョン化した油
分の除去効果が乏しく10以上では油吸着効果が低下す
るので好ましくない。The mixing ratio of the oil-absorbing rubber powder and the activated carbon or inorganic mineral substance (hereinafter, both simply referred to as the mixture) is a weight ratio of rubber powder:mixture of 1=1 to 1:10. A range of 1 or less is preferable, and if the mixture is less than 1, the effect of removing emulsified oil will be poor, and if it is more than 10, the oil adsorption effect will be reduced, which is not preferable.
作用
本発明においては、乳化油に対して、それぞれゴム粉末
、混合剤単味では見られなかった優れた相乗作用による
もので、その相乗作用の機作は明らかではないが、おそ
らく混合剤が乳化を破壊するような状態とし、油滴にゴ
ム粉末及び混合剤が優れた吸着作用を示すと共に、混合
剤粒子がゴム粒子間に介在してブロック化を防止し、処
理水の流通路を確保するものと考えられる。Effect In the present invention, this is due to an excellent synergistic effect on the emulsified oil that was not observed with the rubber powder or the mixture alone, respectively.The mechanism of this synergistic effect is not clear, but it is probably due to the emulsification of the mixture with the emulsified oil. The rubber powder and the mixture agent exhibit excellent adsorption action on the oil droplets, and the mixture agent particles intervene between the rubber particles to prevent block formation and ensure a flow path for the treated water. considered to be a thing.
実施例
以下、本発明を、さらに実施例により具体的に説明する
。EXAMPLES Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例 1.2及び比較例1〜3
被処理原水として灯油を水に添加し、これにノニオン系
界面活性剤を添加し、充分に撹拌して乳化原水を調製し
た。原水は油分が完全にエマルジョン化しており、浮上
油は全く見られなかった。Example 1.2 and Comparative Examples 1 to 3 Kerosene was added to water as raw water to be treated, a nonionic surfactant was added thereto, and the mixture was sufficiently stirred to prepare emulsified raw water. The oil in the raw water was completely emulsified, and no floating oil was observed.
なお原水及び処理水の水質(油含有量]はJIS法で規
定されたノルマルヘキサン抽出物質法で測定した。The water quality (oil content) of raw water and treated water was measured by the normal hexane extract method specified by JIS method.
油吸収(着]性ゴム粉末としてノルボルネン系ゴム粉末
を用い、活性炭、及び無機鉱物質吸着剤としてパーライ
トを選んだ。ノルボルネン系ゴム粉末の平均粒径はα3
簡、活性炭の平均粒径は07朋、パーライトのそれは0
.6朋であった。Norbornene rubber powder was used as the oil-absorbing rubber powder, and perlite was selected as the activated carbon and inorganic mineral adsorbent.The average particle size of the norbornene rubber powder was α3.
Simple, the average particle size of activated carbon is 07, and that of pearlite is 0.
.. It was 6 friends.
ノルボルネン系ゴムと活性炭又はパーライトの割合が重
量比で1=2になるように添加し、充分に混合し、均一
混合物を調製した。この混合物を内径30間、高さ30
0閣の充填塔に150朋充填し、原水を上方から流下さ
せ、下方から処理水を排出セシめ、空間速度(Spac
e Velocity、 S 。Norbornene rubber and activated carbon or pearlite were added so that the ratio by weight was 1=2, and thoroughly mixed to prepare a homogeneous mixture. Spread this mixture between 30 mm in inner diameter and 30 mm in height.
A packed tower with 150 liters of water is filled, raw water is allowed to flow down from above, treated water is discharged from below, and the space velocity (Spac
e Velocity, S.
■、と略称する)が2.0 (1/hrlになるよう
をこ流速を規制した。なお、比較のため、バルブ不a市
中に前記ノルボルネン系ゴム粉末を分散付着させたもの
(比較例1]、ポリプロピレン不織布中にノルボルネン
系ゴムを分散付着させたもの(比較例2)及び市販繊維
系吸着材(商品名 パルクロス] (比較例3)を充填
して試験した。結果を次の第1表に示す。The flow rate was regulated so that 2.0 (1/hrl) was obtained.For comparison, the norbornene-based rubber powder was dispersed and adhered to the valve material (comparative example). 1], a polypropylene nonwoven fabric with norbornene rubber dispersed in it (Comparative Example 2), and a commercially available fiber-based adsorbent (trade name Palcross) (Comparative Example 3) were filled and tested.The results are as follows: Shown in the table.
なお、比較例1〜3では処理水に濁りが残り、実施例1
では処理水の濁りは極めて薄く、実施例2では処理水に
濁りは全く見られず、除去率も極めて優れている。In addition, in Comparative Examples 1 to 3, turbidity remained in the treated water, and in Example 1
In Example 2, the turbidity of the treated water was extremely low, and in Example 2, no turbidity was observed in the treated water, and the removal rate was also extremely excellent.
第1表
注 何れも空間速WE(S、V−5=2.0 (1/h
rl原水質:200ppm
実施例 3〜6
実施例1と同様にして300 ppmの処理用原水をm
製し、実施例1で使用したと同一のノルボルネン系ゴム
・パーライト混合物を用い、充填塔における空間速度を
変えて実験を行なった。結果を第2表に示す。Note to Table 1: Space velocity WE (S, V-5=2.0 (1/h
rl raw water quality: 200 ppm Examples 3 to 6 In the same manner as in Example 1, 300 ppm raw water for treatment was
Using the same norbornene-based rubber/perlite mixture as that prepared and used in Example 1, an experiment was conducted by changing the space velocity in the packed column. The results are shown in Table 2.
第2表
第2表で示されるように、空間速度を大とした場合、す
なわち、S、V、1 !>0とした極めて接触時間が短
い場合においても、エマルジョン破壊及び油分の吸着が
充分に行なわれ、処理水質も目標値15 ppm以下で
あり、高い油分除去系を示している。又、上記実施例3
〜6では、何れも処理水(こ濁りは認められなかった。Table 2 As shown in Table 2, when the space velocity is increased, that is, S, V, 1! Even when the contact time was extremely short (>0), emulsion destruction and oil adsorption were sufficiently carried out, and the quality of the treated water was below the target value of 15 ppm, indicating a high oil removal system. In addition, the above Example 3
-6, the treated water (no turbidity was observed).
発明の効果
本発明によれば、上記実施例に示す如く、優れたエマル
ジョン破壊特性と高い油分除去率を示し、更にこの効果
は接触時間を短時間としても発揮され、油吸収性ゴムの
油分吸収能力が効果的に発揮される。原水質の処理範囲
としては、油分800ppm〜20 ppmの広い範囲
にわたり優れたエマルジョン破壊及び油分除去率を有し
、上記実施例に示す如く処理困難なノニオン界面活性剤
で安定化されたエマルジョンに対しても優れたエマルジ
ョン破壊特性を有し、都市下水、工場廃水等の乳化含油
廃水処理方法として極めて効果の大きなものである。Effects of the Invention According to the present invention, as shown in the above examples, excellent emulsion breaking properties and a high oil removal rate are exhibited, and furthermore, this effect is exhibited even when the contact time is short, and the oil absorption of the oil-absorbing rubber is improved. Ability is effectively demonstrated. As for raw water quality treatment range, it has excellent emulsion breaking and oil removal rates over a wide range of oil content from 800 ppm to 20 ppm, and is superior to emulsions stabilized with nonionic surfactants that are difficult to treat as shown in the above examples. It has excellent emulsion breaking properties, and is extremely effective as a method for treating emulsified oil-containing wastewater such as urban sewage and industrial wastewater.
Claims (1)
は油吸着性ゴムと活性炭、無機質吸着剤又は無機多孔質
物質から選ばれた少なくとも1種とを添加してエマルジ
ョン化した油分を除去することを特徴とする油汚濁水の
処理方法。1. Adding an oil-absorbing or oil-absorbing rubber and at least one selected from activated carbon, an inorganic adsorbent, or an inorganic porous substance to polluted water containing emulsified oil to remove the emulsified oil. A method for treating oil-contaminated water, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18862585A JPS6249914A (en) | 1985-08-29 | 1985-08-29 | Treatment of oil-contaminated water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18862585A JPS6249914A (en) | 1985-08-29 | 1985-08-29 | Treatment of oil-contaminated water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6249914A true JPS6249914A (en) | 1987-03-04 |
Family
ID=16226960
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18862585A Pending JPS6249914A (en) | 1985-08-29 | 1985-08-29 | Treatment of oil-contaminated water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6249914A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5404209A (en) * | 1993-01-13 | 1995-04-04 | Fuji Xerox Co., Ltd. | Apparatus and method for forming images which are treated with an oil absorbent |
WO2001048042A1 (en) * | 1999-12-24 | 2001-07-05 | Sabanci Universitesi | Superabsorbent materials based on butyl rubber process for making said materials and use of them |
EP1288164A1 (en) * | 2001-08-31 | 2003-03-05 | Adsoca AG | Process and mobile plant for purifying waste water containing organic substances |
WO2010021568A1 (en) * | 2008-08-05 | 2010-02-25 | ЮШКОВ Вадим Валерьевич | Material and a method for treating oil and / or oil product pollutions |
JP2012206084A (en) * | 2011-03-30 | 2012-10-25 | Cci Corp | Treatment method for fat-containing wastewater and wastewater treatment material therefor |
CN113811388A (en) * | 2019-05-09 | 2021-12-17 | 阿布特克工业公司 | Compositions, articles and methods for reducing hydrocarbon, metal and organic contaminants |
-
1985
- 1985-08-29 JP JP18862585A patent/JPS6249914A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5404209A (en) * | 1993-01-13 | 1995-04-04 | Fuji Xerox Co., Ltd. | Apparatus and method for forming images which are treated with an oil absorbent |
WO2001048042A1 (en) * | 1999-12-24 | 2001-07-05 | Sabanci Universitesi | Superabsorbent materials based on butyl rubber process for making said materials and use of them |
EP1288164A1 (en) * | 2001-08-31 | 2003-03-05 | Adsoca AG | Process and mobile plant for purifying waste water containing organic substances |
WO2010021568A1 (en) * | 2008-08-05 | 2010-02-25 | ЮШКОВ Вадим Валерьевич | Material and a method for treating oil and / or oil product pollutions |
JP2012206084A (en) * | 2011-03-30 | 2012-10-25 | Cci Corp | Treatment method for fat-containing wastewater and wastewater treatment material therefor |
CN113811388A (en) * | 2019-05-09 | 2021-12-17 | 阿布特克工业公司 | Compositions, articles and methods for reducing hydrocarbon, metal and organic contaminants |
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