JPH0473477B2 - - Google Patents
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- Publication number
- JPH0473477B2 JPH0473477B2 JP15104784A JP15104784A JPH0473477B2 JP H0473477 B2 JPH0473477 B2 JP H0473477B2 JP 15104784 A JP15104784 A JP 15104784A JP 15104784 A JP15104784 A JP 15104784A JP H0473477 B2 JPH0473477 B2 JP H0473477B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- oils
- rolling
- maleated
- fish 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
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Description
本発明は金属加工油に関するものであり、さら
に詳しくは、水系の金属加工油にも、非水系の金
属加工油にも用い得る、乳化安定性並びに潤滑性
のすぐれた金属加工油に関するものである。
金属加工油には、たとえば、切削油、研削油、
圧延油、プレス油、引抜油、塑性加工油など加工
方式による呼び方と使い方によつて、水系で使用
される水溶性金属加工油、非水系(油系)で使用
される油溶性金属加工油などいろいろの分類の仕
方がある。
このような金属加工油組成物には、基油に油性
向上剤、界面活性剤、錆止め剤、極圧添加剤、消
泡剤など各種の添加剤が配合されている。
油性向上剤としては、一般に高級脂肪酸、高級
脂肪酸エステル、動植物油脂、ダイマー酸、トリ
マー酸、ポリブテンなど天然または合成の化合物
が使用されている。しかし、潤滑性の点で十分に
満足されるものではなく、その性能をおぎなうた
めに、さらに多くの添加剤を配合している。
また、水溶性金属加工油には、基油のほかに油
性向上剤が添加されるが、これらの油成分を乳化
または可溶化するために、数種の界面活性剤を多
量に使用しないと、安定した乳化分散系または可
溶化系が得られない。多量の界面活性剤で乳化ま
たは可溶化すると潤滑性が低下するばかりでな
く、使用時に泡が多量に発生して、そのために加
工工程で好ましくない問題が発生する。
本発明は従来の金属加工油のこれらの欠点を解
決すべく検討した結果、本発明に至つたものであ
る。
すなわち本発明は、魚油は水素添加して沃素価
50〜120の水素添加魚油を得、それに無水マレイ
ン酸を反応して得られる。38.8℃で40〜20000セ
ンチポイズの範囲の粘度を有する水添魚油のマレ
イン化物(以下「マレイン化油」と称す)を含有
する金属加工油であり、100%のマレイン化油よ
り成るもの、並びにマレイン化油と動植物油脂や
鉱物油の基油及び添加剤、乳化剤と混合して成る
ものがある。
本発明のマレイン化油の濃度が高い程、高い潤
滑性が得られるが、動植物油脂、鉱物油、他の油
性向上剤、極圧添加剤と配合して使用する場合に
は、マレイン化油を少くとも4%配合したもの
が、金属加工上の潤滑性から見て好ましく、これ
以下では、その効果は著しく低下してくる。さら
に本願に使用するマレイン化油は自己乳化性を有
しているため、水系の金属加工油として利用する
場合には、界面活性剤の使用量が極めて少量です
み、経済的であるばかりでなく、泡立ちの著しく
少ない金属加工油が得られる。一方、鉱物油また
は合成潤滑基油に、あるいはまた動植物油脂に本
発明のマレイン化油を配合した油溶性金属加工油
及び潤滑油は、極めてすぐれた潤滑性を示す。
本発明の特長は、特に適当の範囲になるように
水素添加した半硬化魚油をマレイン化したことに
よつて得られる。魚油は重合して潤滑油の分野に
も利用された歴史はあるが、魚油が唯一の国産油
脂でありながら、近年その使用量は少なくなつて
いる。これは魚油が他の動植物油脂と異つて、魚
臭が激しく、完全な脱臭がむずかしく、さらに他
の油脂には含まれない高度不飽和酸を多量に含ん
でいるために、熱に不安定であることなど、技術
的に解決しなければならないことが多く残つてい
るためである。
本発明のマレイン化油は、まず、精製した魚油
を常法によつて水添触媒をもちいて沃素価が50〜
120になるまで水素添加した後、無水マレイン酸
を無触媒またはマレイン化のための公知の触媒を
使用して、150〜250℃で反応することによつて得
られる。本発明に使用される魚油は著しく酸化ま
たは重合が起つている魚油でない限り、その種類
は選ばない。しかし、好ましくは常法で精製した
魚油がよい。水素添加反応は通常の水添条件及び
触媒が使用されて行なわれる。例えば、ニツケル
系触媒を対油脂の0.2〜1.0重量%用い、水素圧1.0
〜4.0Kg/cm2にて、温度160〜200℃で水素添加反
応を行う。水素添加後の沃素価は50〜120である
が、好ましくは60〜100である。沃素価(以下
「IV」と記す)が50以下ではマレイン化の反応が
進行しにくく、生成したマレイン化魚油の融点が
高く、潤滑性も十分ではない。IVが120以上で
は、魚臭が激しく、工業的にはその製造が限定さ
れる。水添魚油と無水マレイン酸の反応モル比は
水添魚油1モルに対し、無水マレイン酸を0.1〜
4.0モル、好ましくは0.5〜2.5モル反応させたもの
が、金属加工油として用いるに適している。無水
マレイン酸のモル数が0.1〜0.5モルでは潤滑性能
がやや低下してくる。また、2.5〜4.0モルでは、
潤滑性能は十分あるが、鉱物油、動植物油脂との
相溶性が低下してくるが、実用的には十分使用出
来る。
粘度は40〜20000の範囲のものが、最も他の油
脂及び鉱物油との相溶性がよく、潤滑性もすぐれ
ている。粘度が40以下では他の油との相溶性はよ
いが、潤滑性が十分ではなく、粘度が2000以上で
は他の油脂、鉱物油との相溶性が低くなり、その
ために一定した潤滑性が得られない。一般に動植
物油脂をマレイン化することは公知であるが、そ
の生成物は複雑で、何種類かの反応が起つている
ことも知られている。特に多量の高度不飽和酸を
含む魚油を水添して得られた水添魚油をマレイン
化する場合には、他の動植物油脂とは、また一層
その反応生成物はことなり複雑なものと推定して
いる。しかし、その反応及び反応生成物を完全に
解析または分析できていない。しかし、検討を重
ねた結果、本発明のように限定された粘度に達し
たマレイン化油であれば、本発明の特長が得られ
ることを発見した。本願はこの発明に基くもので
ある。
本発明のマレイン化油は、単独で金属加工油の
基油として、または油性向上剤として使用するこ
ともできるが、あらかじめ、他の動植物油脂、エ
ステル類、合成油及び鉱物油と混合して同様の目
的に使用してもよい。さらに、本発明の潤滑油組
成物に公知の潤滑油添加剤、たとえば極圧添加
剤、酸化防止剤、消泡剤、界面活性剤などは自由
にその目的のために添加される。以下実施例を示
して、本発明を具体的に説明する。
実施例 1
沃素価175の精製魚油を常法によりNi系触媒0.4
%、水素圧1.5Kg/cm2、温度160±2℃で水添し、
沃素価91、酸価0.5の水添魚油を得た。
この水添魚油1モルに無水マレイン酸0.5モル
を33ツ口フラスコを用いて180℃3時間反応
させた後、過剰の無水マレイン酸を減圧にて留去
し酸価84.7、粘度430(センチポイズ38℃以下同
様)のマレイン化油を得た。
実施例 2
実施例1と同一の条件にて得られた沃素価61、
酸価0.5の水添魚油1モルに無水マレイン酸2モ
ルを33ツ口フラスコを用いて、190℃2時間
反応させた後、過剰の無水マレイン酸を減圧にて
留去し、酸価102、粘度1276センチポイズのマレ
イン化油を得た。
実施例 3
実施例1の条件で得られた沃素価71、酸価0.5
の水添魚油1モルに無水マレイン酸1モルを3
3ツ口フラスコを用いて170℃5時間反応させた
後、過剰の無水マレイン酸を減圧にて留去し、酸
価67.7、粘度320センチポイズのマレイン化油を
得た。
実施例 4
実施例1〜3で得られたマレイン化油を表−1
に示す様に単体もしくは配合品とし、乳化性と潤
滑性能の評価を行なつた。
比較例として牛脂に乳化剤を添加したものを用
いた。
The present invention relates to a metalworking oil, and more specifically, to a metalworking oil with excellent emulsion stability and lubricity that can be used for both aqueous and non-aqueous metalworking oils. . Metalworking oils include cutting oils, grinding oils,
Water-soluble metal working oil used in water-based systems, oil-soluble metal working oil used in non-aqueous (oil-based) systems, depending on the name and usage depending on the processing method, such as rolling oil, press oil, drawing oil, plastic working oil, etc. There are various ways of classification. Such metal working oil compositions contain various additives such as oil property improvers, surfactants, rust inhibitors, extreme pressure additives, and antifoaming agents in the base oil. As oiliness improvers, natural or synthetic compounds such as higher fatty acids, higher fatty acid esters, animal and vegetable oils, dimer acids, trimer acids, and polybutenes are generally used. However, it is not fully satisfied in terms of lubricity, and in order to improve its performance, more additives are added. In addition to the base oil, oiliness improvers are added to water-soluble metalworking oils, but in order to emulsify or solubilize these oil components, large amounts of several types of surfactants are not used. A stable emulsified dispersion or solubilized system cannot be obtained. Emulsification or solubilization with a large amount of surfactant not only reduces the lubricity but also generates a large amount of foam during use, which causes undesirable problems in the processing process. The present invention was developed as a result of studies aimed at solving these drawbacks of conventional metal working oils. In other words, in the present invention, fish oil is hydrogenated to increase its iodine value.
50-120 hydrogenated fish oil is obtained by reacting it with maleic anhydride. Metalworking oils containing maleated hydrogenated fish oils (hereinafter referred to as "maleated oils") having a viscosity in the range of 40 to 20000 centipoise at 38.8°C, consisting of 100% maleated oils, as well as maleated oils. Some products are made by mixing synthetic oils with base oils such as animal and vegetable fats and mineral oils, additives, and emulsifiers. The higher the concentration of the maleated oil of the present invention, the higher the lubricity obtained, but when used in combination with animal and vegetable oils, mineral oils, other oiliness improvers, and extreme pressure additives, A content of at least 4% is preferable from the viewpoint of lubricity in metal processing, and if the content is less than this, the effect will be significantly reduced. Furthermore, since the maleated oil used in this application has self-emulsifying properties, when used as a water-based metalworking oil, the amount of surfactant used is extremely small, which is not only economical but also , a metalworking oil with significantly less foaming can be obtained. On the other hand, oil-soluble metalworking oils and lubricating oils in which the maleated oil of the present invention is blended with mineral oil or synthetic lubricating base oil, or with animal or vegetable oil, exhibit extremely excellent lubricity. The features of the present invention are particularly achieved by maleating semi-hydrogenated fish oil which has been hydrogenated to an appropriate range. Fish oil has a history of being polymerized and used in the field of lubricants, but although fish oil is the only domestically produced oil, its usage has been decreasing in recent years. This is because fish oil, unlike other animal and vegetable oils, has a strong fishy odor, is difficult to completely deodorize, and contains a large amount of polyunsaturated acids, which are not found in other fats and oils, making it unstable to heat. This is because there are still many technical issues that need to be resolved. The maleated oil of the present invention is produced by firstly processing refined fish oil using a hydrogenation catalyst in a conventional manner to achieve an iodine value of 50 to 50.
It is obtained by hydrogenating to 120° C. and then reacting maleic anhydride at 150 to 250° C. without a catalyst or using a known catalyst for maleation. The type of fish oil used in the present invention is not limited as long as it is not significantly oxidized or polymerized. However, fish oil purified by conventional methods is preferred. The hydrogenation reaction is carried out using conventional hydrogenation conditions and catalysts. For example, using a nickel-based catalyst of 0.2 to 1.0% by weight based on oil and fat, hydrogen pressure of 1.0
The hydrogenation reaction is carried out at ~4.0 Kg/cm 2 and a temperature of 160-200°C. The iodine value after hydrogenation is 50-120, preferably 60-100. If the iodine value (hereinafter referred to as "IV") is less than 50, the maleation reaction will be difficult to proceed, the resulting maleated fish oil will have a high melting point, and its lubricity will not be sufficient. When the IV is 120 or more, the fishy odor is so strong that industrial production is limited. The reaction molar ratio of hydrogenated fish oil and maleic anhydride is 0.1 to 1 mole of hydrogenated fish oil to 0.1 to 1 mole of maleic anhydride.
4.0 mol, preferably 0.5 to 2.5 mol reacted, is suitable for use as a metalworking fluid. If the number of moles of maleic anhydride is 0.1 to 0.5 moles, the lubricating performance will decrease somewhat. Also, at 2.5 to 4.0 mol,
Although it has sufficient lubricating performance, its compatibility with mineral oil and animal and vegetable oils and fats decreases, but it can be used satisfactorily for practical purposes. A viscosity in the range of 40 to 20,000 has the best compatibility with other oils and fats and mineral oil, and has excellent lubricity. If the viscosity is less than 40, the compatibility with other oils is good, but the lubricity is not sufficient, and if the viscosity is more than 2000, the compatibility with other oils, fats, and mineral oils is low, and therefore constant lubricity is not achieved. I can't. It is generally known to maleate animal and vegetable oils and fats, but it is also known that the product is complex and that several types of reactions occur. In particular, when maleating hydrogenated fish oil obtained by hydrogenating fish oil containing a large amount of highly unsaturated acids, the reaction products are estimated to be different and more complex than other animal and vegetable oils. are doing. However, the reaction and reaction products have not been completely analyzed. However, as a result of repeated studies, it was discovered that the features of the present invention can be obtained if the maleated oil reaches a viscosity as limited as the present invention. This application is based on this invention. The maleated oil of the present invention can be used alone as a base oil for metal working oil or as an oiliness improver, but it can be mixed in advance with other animal and vegetable oils, esters, synthetic oils, and mineral oils. May be used for this purpose. Furthermore, known lubricating oil additives, such as extreme pressure additives, antioxidants, antifoaming agents, surfactants, etc., may be optionally added for that purpose to the lubricating oil compositions of the present invention. The present invention will be specifically explained below with reference to Examples. Example 1 Refined fish oil with an iodine value of 175 was treated with a Ni-based catalyst of 0.4 using a conventional method.
%, hydrogenated at a hydrogen pressure of 1.5Kg/cm 2 and a temperature of 160±2℃,
Hydrogenated fish oil with an iodine value of 91 and an acid value of 0.5 was obtained. After reacting 1 mole of hydrogenated fish oil with 0.5 mole of maleic anhydride at 180°C for 3 hours using a 33-necked flask, excess maleic anhydride was distilled off under reduced pressure to give an acid value of 84.7 and a viscosity of 430 (centipoise: 38 centipoise). A maleated oil was obtained. Example 2 Iodine value 61 obtained under the same conditions as Example 1,
After reacting 1 mole of hydrogenated fish oil with an acid value of 0.5 and 2 moles of maleic anhydride at 190°C for 2 hours using a 33-necked flask, excess maleic anhydride was distilled off under reduced pressure to obtain an acid value of 102, A maleated oil with a viscosity of 1276 centipoise was obtained. Example 3 Iodine value 71 and acid value 0.5 obtained under the conditions of Example 1
1 mole of maleic anhydride to 1 mole of hydrogenated fish oil
After reacting for 5 hours at 170°C using a three-necked flask, excess maleic anhydride was distilled off under reduced pressure to obtain a maleated oil with an acid value of 67.7 and a viscosity of 320 centipoise. Example 4 Maleated oils obtained in Examples 1 to 3 are shown in Table-1.
The emulsifying properties and lubrication performance were evaluated using either a single product or a combination product as shown in the figure below. As a comparative example, beef tallow with an emulsifier added was used.
【表】
1 乳化性
表−1のNo.1,3,7につき、乳化分離度およ
びESIを測定し、表−2に示した。[Table] 1 Emulsifying property Emulsification separation degree and ESI were measured for Nos. 1, 3, and 7 in Table 1, and are shown in Table 2.
【表】
1 乳化分離度試験方法
各試料の5%溶液を1のトールビーカーに
800ml作成しホモミキサーを用いて5分間撹拌後
静置し、経過時間2分、5分後の分離油層量を測
定し、仕込試料油量に対する百分率にて示した。
2 ESI(乳化安定指数)
各試料の5%溶液を1のトールビーカーに
800ml作成し、常温にてホモミキサーを用いて5
分間撹拌後、直ちに分液ロートに300ml採取、2
分間経過後、上層、下層より各100mlのエマルジ
ヨンを取り出し、その各々の中の油分(%)を測
定し、次式によりESIを算出した。
ESI%=下層油分(%)/上層油分(%)×100
次に潤滑性能の試験として、耐荷重能試験リン
グ圧縮試験、圧延試験を行つた。その方法は、以
下に述べる方法によつた。結果を表−3、表−
4、図−1に示す。
2 耐荷重能試験
シエル型高速四球式摩擦試験機
1/2インチボール
測定温度 50±2℃
立軸回転数 1500rpm[Table] 1 Emulsification separation test method Add 5% solution of each sample to tall beaker 1.
A sample of 800 ml was prepared, stirred for 5 minutes using a homomixer, and left to stand.The amount of separated oil layer was measured after an elapsed time of 2 minutes and 5 minutes, and expressed as a percentage of the amount of sample oil charged. 2 ESI (Emulsification Stability Index) Add 5% solution of each sample to 1 tall beaker.
Make 800ml and use a homo mixer at room temperature for 5 minutes.
After stirring for a minute, immediately collect 300ml into a separating funnel.
After 100 ml of each emulsion was taken out from the upper and lower layers, the oil content (%) in each was measured, and the ESI was calculated using the following formula. ESI% = Lower layer oil content (%) / Upper layer oil content (%) x 100 Next, as a test of lubrication performance, a load carrying capacity test, a ring compression test, and a rolling test were conducted. The method was as described below. The results are shown in Table-3, Table-
4. Shown in Figure-1. 2 Load-bearing capacity test Shell-type high-speed four-ball friction tester 1/2 inch ball Measurement temperature 50±2℃ Vertical rotation speed 1500rpm
【表】【table】
【表】 3 リング圧縮試験 圧縮荷重 80t リング寸法 外径20mm、内径10mm 厚さ 5mm 測定温度 常温【table】 3 Ring compression test Compression load 80t Ring dimensions: outer diameter 20mm, inner diameter 10mm Thickness: 5mm Measurement temperature: normal temperature
【表】
4 圧延試験
圧延機 :四段ロール式圧延機
ワークロール直径150mm
巾140mm
バツクアツプロール直径250mm
巾140mm
ロール材質:クロム鋼
ロール周速:30m/min
圧延材料:SPC−C
厚さ0.60mm×巾50mm×長さ150mm
圧延性能の測定法
圧延前の鋼板に50mmの間隔(l1)で2本の線を
引き、これを圧延して圧延後の間隔(l2)を測定
し、次式により圧下率を求めた。
圧下率(%)=l2−l1/l2×100
またその時の圧延荷重(ton)をロードセルにて
測定した。
給油方法:試料の5%(重量)濃度にて、50℃で
ホモキミサーで撹拌してエマルジヨン
とし、圧延時に鋼板の噛込部とロール
にスプレー給油して圧延を行つた。
5 結果
i 表−2の結果、本発明の実施例の1,3はセ
ミ・タイトエマルジヨンを示し、乳化剤を加え
なくても極めて高い乳化安定性を示すのに対
し、牛脂のみでは乳化安定性が悪く、実施例
1,3と同等にするためには、乳化剤を1.7%
添加する必要がある。
表−3の耐荷重能並びに表−4の摩擦係数の
結果は本発明のマレイン化油を含むものはいず
れも、対象試料(牛脂、ナタネ油)に比較し
て、耐荷重能並びに摩擦系数共にすぐれており
潤滑性の高いことを示している。
図−1の圧延試験の結果より、本発明の実施
例のNo.1〜6はいずれもNo.7(牛脂)に比較し
て、すぐれた圧延性能を示しており、表−2の
結果の、乳化安定性が同じであつても圧延性能
には著しい差があることが認められる。[Table] 4 Rolling test Rolling mill: Four-roll rolling mill Work roll diameter 150mm Width 140mm Backup roll diameter 250mm Width 140mm Roll material: Chrome steel Roll circumferential speed: 30m/min Rolling material: SPC-C Thickness 0.60mm × Width 50 mm × Length 150 mm Method for measuring rolling performance Draw two lines at a 50 mm interval (l 1 ) on the steel plate before rolling, roll this, measure the interval after rolling (l 2 ), and then The rolling reduction ratio was calculated using the formula. Rolling ratio (%)=l 2 −l 1 /l 2 ×100 Further, the rolling load (ton) at that time was measured using a load cell. Lubricating method: At 5% (weight) concentration of the sample, it was stirred with a homochimiser at 50°C to form an emulsion, and during rolling, the biting part of the steel plate and the rolls were sprayed with oil and rolled. 5 Results i The results in Table 2 show that Examples 1 and 3 of the present invention are semi-tight emulsions and exhibit extremely high emulsion stability even without the addition of an emulsifier, whereas emulsion stability is poor with beef tallow alone. However, in order to make it equivalent to Examples 1 and 3, the emulsifier should be added at 1.7%.
need to be added. The results of the load-bearing capacity shown in Table 3 and the friction coefficient shown in Table 4 show that all the products containing the maleated oil of the present invention have both load-bearing capacity and friction coefficient compared to the target samples (beef tallow and rapeseed oil). This shows that it has excellent lubricity. From the results of the rolling test shown in Figure 1, Examples Nos. 1 to 6 of the present invention all showed superior rolling performance compared to No. 7 (beef tallow). It is recognized that there is a significant difference in rolling performance even if the emulsion stability is the same.
図面は表−1の組成で行なつた圧延性能を圧延
荷重(ton)と圧下率(%)の関係により示した
圧延性能比較線図である。
The drawing is a rolling performance comparison chart showing the rolling performance of the compositions shown in Table 1 in terms of the relationship between rolling load (ton) and rolling reduction (%).
Claims (1)
イン酸を反応して得られる38.8℃で40〜20000セ
ンチポイズの粘度を有する水添魚油のマレイン化
物を含有することを特徴とする金属加工油。1. A metalworking oil characterized by containing a maleated product of hydrogenated fish oil having a viscosity of 40 to 20,000 centipoise at 38.8°C obtained by reacting hydrogenated fish oil with an iodine value of 50 to 120 and maleic anhydride.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15104784A JPS6128590A (en) | 1984-07-20 | 1984-07-20 | Metal working oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15104784A JPS6128590A (en) | 1984-07-20 | 1984-07-20 | Metal working oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6128590A JPS6128590A (en) | 1986-02-08 |
| JPH0473477B2 true JPH0473477B2 (en) | 1992-11-20 |
Family
ID=15510134
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15104784A Granted JPS6128590A (en) | 1984-07-20 | 1984-07-20 | Metal working oil |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6128590A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005071050A1 (en) * | 2004-01-09 | 2005-08-04 | The Lubrizol Corporation | Maleated vegetable oils and derivatives, as self-emulsifying lubricants in metalworking |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6160793A (en) * | 1984-09-01 | 1986-03-28 | Miyoshi Oil & Fat Co Ltd | Metal working oil |
| JP2006249325A (en) * | 2005-03-11 | 2006-09-21 | Tokai Rika Co Ltd | Metal processing oil |
-
1984
- 1984-07-20 JP JP15104784A patent/JPS6128590A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005071050A1 (en) * | 2004-01-09 | 2005-08-04 | The Lubrizol Corporation | Maleated vegetable oils and derivatives, as self-emulsifying lubricants in metalworking |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6128590A (en) | 1986-02-08 |
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