JPH08168607A - Cutting oil flocculating treatment agent - Google Patents
Cutting oil flocculating treatment agentInfo
- Publication number
- JPH08168607A JPH08168607A JP31165994A JP31165994A JPH08168607A JP H08168607 A JPH08168607 A JP H08168607A JP 31165994 A JP31165994 A JP 31165994A JP 31165994 A JP31165994 A JP 31165994A JP H08168607 A JPH08168607 A JP H08168607A
- Authority
- JP
- Japan
- Prior art keywords
- flocculation
- cutting oil
- colloid
- sulfate
- treatment agent
- 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.)
- Ceased
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、切削油凝集処理剤に
関するものである。さらに詳しくは、この発明は、切削
油のコロイド状廃棄物を分離処理するのに有用な、新し
い、凝集処理剤に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cutting oil aggregating treatment agent. More specifically, the present invention relates to a new flocculating agent useful for separating colloidal waste of cutting oil.
【0002】[0002]
【従来の技術とその課題】従来より、切削油の使用にと
もなうコロイド状廃棄物についてコロイド粒子固形分を
効果的に分離するために各種の凝集剤が使用されてきて
いる。その代表的なものとしては、イオン性高分子系凝
集剤が知られている。また、無機系のものとしても、塩
化アルミニウム系のもの等が知られている。2. Description of the Related Art Conventionally, various flocculants have been used to effectively separate the solid content of colloidal particles from colloidal wastes resulting from the use of cutting oil. An ionic polymer flocculant is known as a typical example. Also, as an inorganic type, an aluminum chloride type is known.
【0003】しかしながら、これまでに知られている凝
集剤の場合には、そのコロイド凝集作用は必ずしも満足
できるものでなく、凝集速度が遅く、固形分の分離能が
充分でないという欠点があった。また、従来の高分子系
の凝集剤の場合には、そのもの自身の廃棄処理が別途必
要になるという問題があった。そこで、このような従来
の欠点を解消するものとして、凝集分離効果が顕著であ
って、しかも後処理が必要でない、新しい切削油コロイ
ドの凝集処理剤の実現が望まれていた。However, in the case of the aggregating agents known so far, the colloid aggregating action is not always satisfactory, and there are drawbacks that the aggregating speed is slow and the solid content separating ability is not sufficient. Further, in the case of the conventional polymer-based coagulant, there is a problem that a separate disposal process of the polymer itself is required. Therefore, as a solution to these conventional drawbacks, it has been desired to realize a new cutting oil colloid aggregating agent that has a remarkable effect of aggregating and separating and does not require post-treatment.
【0004】この発明は、以上の通りの事情に鑑みてな
されたものであって、上記の通りの凝集分離作用に優
れ、しかも後処理の必要もない、新しい切削油凝集処理
剤を提供することを目的としている。The present invention has been made in view of the above circumstances, and provides a new cutting oil aggregating agent which is excellent in the aggregating and separating action as described above and which does not require post-treatment. It is an object.
【0005】[0005]
【課題を解決するための手段】この発明は、上記の課題
を解決するものとして、凝集活性成分が、重量百分率
で、 硫酸第一鉄 10〜60 水酸化カルシウム 10〜30 硫酸カリウム 1〜10 硫酸マグネシウム 1〜10 珪酸塩 1〜10 両性イオン活性剤 0.5〜 5 の組成を有することを特徴とする切削油凝集処理剤を提
供する。In order to solve the above-mentioned problems, the present invention provides a flocculation active ingredient, in terms of weight percentage, of ferrous sulfate 10-60 calcium hydroxide 10-30 potassium sulfate 1-10 sulfuric acid. Provided is a cutting oil aggregating treatment agent having a composition of magnesium 1-10 silicate 1-10 zwitterionic activator 0.5-5.
【0006】[0006]
【作用】この発明は、上記の組成とすることにより、速
い凝集とより効率的なコロイド粒子固形分の分離性を実
現する。さらに切削油の特徴や、この発明の処理剤の個
々の成分の作用について説明すると、以下の通り詳述さ
れる。切削油コロイドの性状 液中のコロイドはゼータ電位、電気二重層により反発し
あい、ブランウン運動により重力の影響を受けずに分散
浮遊している。さらに、油脂成分混入の為に水分子間に
水素結合が見られる。With the above composition, the present invention realizes quick aggregation and more efficient separation of colloidal particle solids. Further, the characteristics of the cutting oil and the action of the individual components of the treatment agent of the present invention will be described in detail below. Properties of cutting oil colloid The colloid in the liquid repels each other due to the zeta potential and the electric double layer, and is dispersed and suspended without being affected by gravity due to the Brownian motion. Furthermore, hydrogen bonds are seen between water molecules due to the inclusion of oil and fat components.
【0007】電気二重層も大きな反発力で各コロイドが
維持されている。凝集疎水化(不可逆性)の原理 コロイドに付着する強固な水分子の極を破壊する合理的
な方法は、より大きな力で粒子の電荷を中和し粒子間り
距離を狭め、ファン,デル,ワールスの法則にて吸引さ
せ、同時に正負イオン交換活性剤、イオン界面活性剤等
による相互誘因作用を起し、異性電荷の強い衝突結合に
よりコロイド微粒子と拘束水分子の殻を破壊し自由水と
ならしめてコロイドの凝集、疎水を図る。The electric double layer also maintains each colloid with a large repulsive force. The principle of cohesive hydrophobization (irreversibility) The rational method of destroying the strong poles of water molecules attached to the colloid is to neutralize the charge of the particles with a larger force to reduce the distance between particles, and van Inhalation is carried out according to Wars's law, and at the same time, mutual attraction by positive and negative ion exchange activators, ionic surfactants, etc. is caused, and colloidal fine particles and bound water molecules are destroyed by strong collision bonding of isomer charges to form free water. Tighten the colloid to make it hydrophobic.
【0008】この働きを高めるために開発されたのが、
正荷電無機電解剤としてのこの発明の処理剤である。薬剤の反応と効果 a.硫酸第一鉄 水和反応により水酸化塩となり、主成分である塩基性酸
化物の働きによりコロイドの電気二重層が圧縮され層の
厚さが薄くなる。What has been developed to enhance this function is
It is the treating agent of the present invention as a positively charged inorganic electrolytic agent. Drug response and effect a. Ferrous sulfate hydrates to form a hydroxide salt, and the basic oxide, which is the main component, acts to compress the electric double layer of the colloid and reduce the thickness of the layer.
【0009】水酸化塩と同時に生成されるイオン高分子
体SO4 2+ が他成分より生成される各イオンと重合し強
力な相互誘因作用を引起す。次にイオン界面活性剤によ
る異性電荷の強い衝突結合がおこり電気二重層の殻を破
壊し電荷を中和する。その結果、拘束水分子が自由水と
なりコロイドの凝集疎水化を促進させる結果となる。 b.水酸化カルシウム 水和反応によりカルシウムイオンが生成され、硫酸第一
鉄の添加によりPH低下による酸性化した領域において
ふりまかれるSO4 2+ イオンに対しCa4 2- イオンとの
相互作用を引起す事によってCaSO4 2+ を生成する。The ionic polymer SO 4 2+, which is produced at the same time as the hydroxide salt, is polymerized with each ion produced from other components to cause a strong mutual attraction action. Next, strong collision bonding of isomer charges occurs due to the ionic surfactant, destroying the shell of the electric double layer and neutralizing the charges. As a result, the bound water molecules become free water, which promotes aggregation and hydrophobization of the colloid. b. Calcium hydroxide Calcium ion is generated by the hydration reaction, and the addition of ferrous sulfate causes an interaction with Ca 4 2− ion to SO 4 2+ ion which is sprinkled in the acidified area due to the decrease of PH. To produce CaSO 4 2+ .
【0010】この結果が凝集反応と疎水化を促進させ同
時にPHの調整をする。 c.硫酸カリウムと硫酸マグネシウム カリウムは水和反応により負電荷に対し対イオン価数2
のイオン性界面活性剤として作用する。正荷電に対し凝
集剤として強くふるまう。(負荷電に対する約7倍の効
力を有する)これに両性イオン活性剤の助力を受け正電
荷に対して強力な中和力を有することとなる。As a result, the aggregation reaction and the hydrophobization are promoted, and at the same time, the pH is adjusted. c. Due to the hydration reaction, potassium sulphate and magnesium sulphate potassium have a counterion valency of 2 for negative charges
Acts as an ionic surfactant. Behaves strongly as a flocculant against positive charges. The zwitterionic activator assists this (having about 7 times the effect against negative charge) and has a strong neutralizing power against positive charges.
【0011】一方マグネシウムは水和反応により水酸化
マグネシウムとなり各薬剤による重合イオンにより形成
されたフロック粒子の結合に役立ち、イオン活性剤と共
に大きなフロックを形成させると同時に疎水沈降剤の役
割を果たす。d.ゼオライト粉体等の珪酸塩と両性イオ
ン活性剤珪酸塩は水和反応によりアルカリ金属塩とな
り、極性の吸着、触媒作用、イオン交換能力を有し、酸
性イオン、アルカリイオン等の弊害を防止すると共に上
澄水の透明度を良好なものとする。又全体のPHを押し
下げる効果もあり、カルシウムイオンの活性効果をも引
き出す働きをする。On the other hand, magnesium turns into magnesium hydroxide by a hydration reaction and serves to bind the floc particles formed by the polymerized ions of each drug, and forms a large floc together with the ionic activator and at the same time acts as a hydrophobic precipitant. d. Silicates such as zeolite powder and zwitterionic activator silicates become alkali metal salts by hydration reaction and have polar adsorption, catalytic action and ion exchange ability, and prevent harmful effects of acidic ions, alkali ions, etc. The clarity of the clear water should be good. It also has the effect of pushing down the overall PH, and also works to bring out the activation effect of calcium ions.
【0012】一方両性イオン活性剤はその交換能力から
処理水pHによってアニオン、カチオンいずれにも解離
し、アルカリ側ではアニオン、酸性側ではカチオン、中
性では非イオンとして強く働きかけ、そのイオン交換能
力から同時に大きなフロックが形成される。又色素分散
能力を有しておりゼオライトと共に清澄水作用を発揮す
る。On the other hand, the zwitterionic activator dissociates into both anions and cations depending on the pH of the treated water due to its exchange ability, and strongly acts as an anion on the alkaline side, a cation on the acidic side, and a nonion on the neutral side. At the same time large flock is formed. It also has the ability to disperse dyes and exerts a clear water action together with zeolite.
【0013】このような作用を有するこの発明の凝集処
理剤は、その組成割合を上記の通りとするか、より好ま
しくは 硫酸第一鉄 40〜55 水酸化カルシウム 20〜30 硫酸カリウム 4〜 8 硫酸マグネシウム 4〜 8 珪 酸 塩 4〜 8 両性イオン活性剤 1〜 3 の割合とする。The aggregating treatment agent of the present invention having such an action has the composition ratio as described above, or more preferably ferrous sulfate 40 to 55 calcium hydroxide 20 to 30 potassium sulfate 4 to 8 sulfuric acid. Magnesium 4 to 8 Silicic acid salt 4 to 8 Zwitterionic activator 1 to 3
【0014】この凝集処理剤は粉末、顆粒状態等で使用
されるが、その際には分割して添加してもよいし、まと
めて対象処理物に添加してもよい。また、上記の各成分
についても、部分的にまとめて複合化してもよい。より
好ましくは、たとえばまず硫酸第一鉄を添加し、次いで
残りのものを添加して攪拌混合する。This aggregating treatment agent is used in the form of powder, granules or the like. In that case, it may be added in divided portions or may be added to the target treated material all at once. Further, each of the above-mentioned components may be partially combined into a composite. More preferably, for example, ferrous sulfate is added first, and then the rest are added and mixed with stirring.
【0015】以下、実施例を示し、さらに詳しくこの発
明について説明する。もちろん、この発明は、以下の実
施例によって限定されるものではない。The present invention will be described in more detail below with reference to examples. Of course, the present invention is not limited by the following embodiments.
【0016】[0016]
【実施例】表1の組成からなる凝集処理剤を表2の手順
に沿って使用済みの植物系切削油に添加した。また比較
のために市販の有機高分子イオン凝集剤も別途添加し
た。EXAMPLE A flocculant having the composition shown in Table 1 was added to a used plant-based cutting oil according to the procedure shown in Table 2. For comparison, a commercially available organic polymer ion coagulant was also added separately.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【表2】 [Table 2]
【0019】この発明の凝集疎水剤の場合と、高分子イ
オン凝集剤との場合についてその作用効果を比較する
と、次の表3の通り、この発明のものは極めて優れてい
た。When the action and effect of the aggregated hydrophobic agent of the present invention and that of the polymeric ion aggregating agent are compared, as shown in Table 3 below, the one of the present invention was extremely excellent.
【0020】[0020]
【表3】 [Table 3]
【0021】[0021]
【発明の効果】この発明により、以上詳しく説明した通
り、切削油のコロイド凝集による分離が速みやかに進行
し、分離能も極めて良好となる。また、後処理が必要と
されない。As described in detail above, according to the present invention, the separation of the cutting oil by the colloid agglomeration progresses rapidly and the separation ability becomes extremely good. Also, no post-treatment is required.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31165994A JPH08168607A (en) | 1994-12-15 | 1994-12-15 | Cutting oil flocculating treatment agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31165994A JPH08168607A (en) | 1994-12-15 | 1994-12-15 | Cutting oil flocculating treatment agent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08168607A true JPH08168607A (en) | 1996-07-02 |
Family
ID=18019945
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31165994A Ceased JPH08168607A (en) | 1994-12-15 | 1994-12-15 | Cutting oil flocculating treatment agent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08168607A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999024365A1 (en) * | 1997-11-07 | 1999-05-20 | Magyar Tudományos Akadémia Kémiai Kutatóközpont | Composition and process for the removal of the phosphate ion content of waters |
KR100397327B1 (en) * | 2000-12-01 | 2003-09-06 | 미래화학 주식회사 | Elution Preventing Composition Of Harmful Material And Method Of Treating Harmful Material By Utilizing The Same |
-
1994
- 1994-12-15 JP JP31165994A patent/JPH08168607A/en not_active Ceased
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999024365A1 (en) * | 1997-11-07 | 1999-05-20 | Magyar Tudományos Akadémia Kémiai Kutatóközpont | Composition and process for the removal of the phosphate ion content of waters |
GB2346875A (en) * | 1997-11-07 | 2000-08-23 | Magyar Tudomanyos Akademia | Composition and process for the removal of the phosphate ion content of waters |
AU749564B2 (en) * | 1997-11-07 | 2002-06-27 | Magyar Tudomanyos Akademia Kemiai Kutatokozpont | Composition and process for the removal of the phosphate ion content of waters |
KR100397327B1 (en) * | 2000-12-01 | 2003-09-06 | 미래화학 주식회사 | Elution Preventing Composition Of Harmful Material And Method Of Treating Harmful Material By Utilizing The Same |
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Legal Events
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Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20050405 |
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