JPS6325638B2 - - Google Patents

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Publication number
JPS6325638B2
JPS6325638B2 JP54088708A JP8870879A JPS6325638B2 JP S6325638 B2 JPS6325638 B2 JP S6325638B2 JP 54088708 A JP54088708 A JP 54088708A JP 8870879 A JP8870879 A JP 8870879A JP S6325638 B2 JPS6325638 B2 JP S6325638B2
Authority
JP
Japan
Prior art keywords
acid
rolling
oil
ester
castor 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
Application number
JP54088708A
Other languages
Japanese (ja)
Other versions
JPS56106998A (en
Inventor
Yukio Hashiguchi
Takeo Yahiro
Koji Onoda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Myoshi Oil and Fat Co Ltd
Original Assignee
Myoshi Oil and Fat Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Myoshi Oil and Fat Co Ltd filed Critical Myoshi Oil and Fat Co Ltd
Priority to JP8870879A priority Critical patent/JPS56106998A/en
Publication of JPS56106998A publication Critical patent/JPS56106998A/en
Publication of JPS6325638B2 publication Critical patent/JPS6325638B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は金属圧延油に関するものである。 従来圧延油として、鋼板用にはパーム油が古く
から使われ、それに代つて牛脂、豚脂、長須鯨硬
化油などの動植物油脂や鉱物油または、それらの
混合油をベースとして、それに極圧添加剤、油性
向上剤、酸化防止剤、界面活性剤などを配合した
ものが広く使われている。 一方、圧延機械設備の進歩は著しく、ミルスタ
ンドの大型化に伴い、パス回数の削減、圧延速度
の高速化、圧延製品の規格精度の上昇等の圧延工
程の合理化並びに精密化が要求され、それに伴い
圧延油にかかる条件も苛酷なものとなつて来てお
り、パーム油や牛脂系圧延油では最早この条件を
満足し得ないものとなりつつあるが、今だにこれ
に代る圧延油が見出されていないのが現状であ
る。 また本願発明者らは先にすぐれた潤滑性を有す
るものとして、ヒマシ油又はアルキレンオキサイ
ドを付加したヒマシ油の脂肪酸エステルを報告し
たが(特公昭52−20430)、同報告において得られ
る化合物をベースオイルとした圧延油では高圧力
かつ高速度下で行われる圧延に対して十分な高速
適性が得られず、さらにその改良の必要性が生じ
ていた。上記の特性に適応する圧延油のベースオ
イルとしては高い油膜強度を有し、かつそれが高
速における潤滑においても破断することなく維持
されるものが要望され、そのためにベースオイル
が具備すべき性状としては、付着力が高い、粘性
が高い、分子量が或る程度大きい等の性状を持つ
たものが考えられ、上記の点に着目して検討の結
果、本発明に到つたものであり、具体的にはヒマ
シ油又はアルキレンオキシドを付加したヒマシ油
の脂肪酸エステルを300〜1800cst(40℃)の粘度
にまで重合して分子量を増大せしめることによ
り、付着性、油膜強度を上昇させ、それに伴い摩
擦係数、耐圧性、圧延荷重等の潤滑性がより一層
向上することを見い出し本発明を完成した。 本発明の目的は、従来のパーム油や牛脂系の圧
延油、あるいはこれに代え得るヒマシ油の脂肪酸
エステル等よりすぐれた潤滑性能を有し、現在の
要求されている苛酷な圧延工程に対して、満足し
得る圧延油を提供せんとすることにある。 本発明は(A)ヒマシ油、(B)アルキレンオキサイド
を付加したヒマシ油、(C)、(A)または(B)と炭素数4
−60のモノカルボン酸またはおよび多価カルボン
酸と反応して得られる分子中に少なくとも1ケの
ヒドロキシル基が残存した部分エステルの、(A)、
(B)、(C)3群より選ばれたる少なくとも1種と炭素
数12〜24の不飽和脂肪酸とエステル化反応を行な
つて得られる反応生成物を熱重合して得られる重
合物を用いることを特徴とする潤滑性能のすぐれ
た高圧下圧延用金属圧延油に関するものである。 本発明は上に述べた重合物を主要なる一成分と
して用いるものであり、これに必要に応じて動植
物油脂、鉱物油、酸化防止剤、界面活性剤を混合
して用いることが出来る。 本発明のアルキレンオキサイドを付加したヒマ
シ油は常法によりヒマシ油にアルキレンオキサイ
ドを付加して得られる。またヒマシ油またはおよ
びヒマシ油誘導体と炭素数4−60のモノカルボン
酸またはおよび多価カルボン酸と反応して得られ
る部分エステルは、常法の脱水縮合によるエステ
ル化反応によつても、またそれらの脂肪酸の低級
アルキルエステルを用いてのエステル交換反応に
よつても得られる。また(A)、(B)、(C)より選ばれた
る少なくとも1種と炭素数12−24の不飽和脂肪
酸、またはそのエステルとの反応により得られる
反応生成物は常法によりエステル化反応を行なつ
て得られる。 ここに用いる炭素数4−60のモノカルボン酸ま
たはおよび多価カルボン酸としては、カプリン
酸、ラウリン酸、ミリスチン酸、パルミチン酸、
ステアリン酸、アラキン酸、ベヘン酸等の飽和脂
肪酸、ネオ酸、オキソ法により得られるα−位に
側鎖を有する側鎖性飽和脂肪酸、オレイン酸、リ
ノール酸、リノレン酸、アラキドン酸、リシノー
ル酸等の不飽和脂肪酸、コハク酸、アジピン酸、
アゼライン酸、セバシン酸、マレイン酸、フマー
ル酸、イタコン酸等の二塩基性カルボン酸並びに
これら二塩基性カルボン酸無水物、さらに不飽和
脂肪酸を重合して得られるいわゆるダイマー酸、
トリマー酸より成る重合多塩基性カルボン酸、ト
リメリツト酸等が挙げられる。これらの脂肪酸は
1種または、2種以上を混合して用いることがで
きる。 また、炭素数12−24の不飽和脂肪酸としては、
オレイン酸、リノール酸、リノレン酸、エライジ
ン酸、リシノレン酸、リシノエライジン酸等を代
表とするものであるが、これらはエステル化反応
の際には脂肪酸のまま用いても良いが、低級アル
キルエステルとしてエステル交換反応を行つても
良い。 また、(A)、(B)、(C)と炭素数12−24の不飽和脂肪
酸とより得られる不飽和二重結合をもつたエステ
ルの熱重合は常法によつて重合されるが、本発明
の重合反応はヒマシ油中のリシノレン酸の持つ二
重結合とそれに反応させた不飽和脂肪酸から来る
二重結合が複雑に関与するものであり、反応条件
の制御によつて、圧延油としての必要条件を満た
す重合物を得ることが出来る。熱重合の反応条件
は、得られたエステルまたはポリエステルをその
まま200〜300℃にて10〜30時間加熱するのである
が、反応の進行度は通常粘度を測定しながらチエ
ツクする。また、求める粘度により反応温度、時
間を選択するが、ここに得られる重合体の粘度
が、300〜1800cst(40℃)の範囲に入るように反
応条件をコントロールする。 このようにして得られた重合物は、そのまま圧
延油に使用され、優秀な性能を示す。また、本発
明の重合物は動植物油脂、鉱物油、酸化防止剤、
界面活性剤などと混合して使用することも出来
る。 以下に本発明を実施例により説明する。 合成例 1 ヒマシ油935部、ステアリン酸284部、パラトル
エンスルホン酸(以下PTSAと記す)12部を窒素
ガス(以下N2ガスと記す)気流下に150−180℃
で6時間反応し、酸価1.0、水酸基価89.5のエス
テル(エステル−1)を得た。 このエステルにオレイン酸423部、PTSA16部
を加え150−180℃で8時間反応し、酸価4.5、水
酸基価5.0、粘度105cst(40℃)を持つポリエステ
ルを得た。さらに、このポリエステルを260−280
℃で20時間熱重合し、粘度700cst(40℃)の重合
物を得た。 合成例 2 ヒマシ油935部、オレイン酸733部、PTSA16部
をN2ガス気流下に150−160℃で8時間反応し、
酸価7.8、水酸基価3.2、粘度110cst(40℃)のエス
テル(エステル−2)を得た。続いてこのエステ
ルを260−270℃で20時間熱重合し、粘度1050cst
(40℃)の重合物を得た。 合成例 3 エチレンオキサイドを30モル付加したヒマシ油
2255部、オレイン酸733部、PTSA30部をN2ガス
気流下に130−140℃で6時間反応し、酸価6.5、
水酸基価4.8、粘度102cst(40℃)のエステル(エ
ステル−3)を得た。続いて、このエステルを
220−230℃で15時間熱重合し、粘度620cst(40℃)
の重合物を得た。 合成例 4 ヒマシ油935部、蒸留米ヌカ脂肪酸(ヨウ素価
120)564部、PTSA15部をN2ガス気流下に150−
180℃で6時間反応し、続いて無水マレイン酸18
部を加え、100℃で2時間、150−160℃で4時間
反応し、酸価1.8、水酸基価4.5、粘度380cst(40
℃)のポリエステル(エステル−4)を得た。続
いて、このエステルをさらに260−270℃で15時間
熱重合を行い、粘度1350cst(40℃)の重合物を得
た。 合成例 5 ヒマシ油935部、蒸留米ヌカ脂肪酸(ヨウ素価
120)738部、PTSA12部をN2ガス気流下にて、
150−180℃で6時間反応し、酸価1.0、水酸基価
1.8、粘度100cst(40℃)のエステル(エステル−
5)を得た。 続いて、このエステルを240−260℃で15時間熱
重合して、粘度800cst(40℃)の重合物を得た。 合成例 6 プロピレンオキサイドを50モル付加したヒマシ
油3835部、蒸留米ヌカ脂肪酸(ヨウ素価120)733
部、PTSA45.5部をN2ガス気流下で、140−150℃
で7時間反応し、酸価3.6、水酸基価4.2、粘度
115cst(40℃)のエステル(エステル−6)を得
た。 このエステルをさらに240−260℃で16時間加熱
し、熱重合反応を行い、粘度750cst(40℃)の重
合物を得た。 合成例1−6の重合物を表−1に示すように単
体もしくは配合品として、実施例No.1−7を調製
し金属圧延油の潤滑性能試験を行なつた。
The present invention relates to metal rolling oil. Conventionally, palm oil has been used as a rolling oil for steel plates for a long time, but instead, animal and vegetable oils such as beef tallow, lard, Nagasu whale hardened oil, mineral oils, or mixtures of these oils are used as base oils, and extreme pressure additives are added to them. , oiliness improvers, antioxidants, surfactants, etc. are widely used. On the other hand, the progress of rolling machinery equipment has been remarkable, and with the increase in the size of mill stands, rationalization and precision of the rolling process are required, such as reducing the number of passes, increasing rolling speed, and increasing the standard accuracy of rolled products. As a result, the conditions for rolling oils have become more severe, and palm oil and beef tallow-based rolling oils are no longer able to satisfy these conditions, but there are still rolling oils that can replace them. The current situation is that it has not been released. In addition, the inventors of the present application have previously reported castor oil or a fatty acid ester of castor oil to which alkylene oxide has been added as having excellent lubricity (Japanese Patent Publication No. 52-20430). The rolling oil used in this invention was not sufficiently suitable for high speed rolling under high pressure and high speed, and there was a need for further improvement. The base oil for rolling oil that meets the above characteristics is required to have high oil film strength and maintain it without breaking even during high-speed lubrication. It is conceivable that the material has properties such as high adhesive strength, high viscosity, and a certain degree of molecular weight, and as a result of studies focusing on the above points, the present invention was arrived at. By polymerizing castor oil or fatty acid ester of castor oil to which alkylene oxide has been added to a viscosity of 300 to 1800cst (40℃) and increasing the molecular weight, adhesion and oil film strength are increased, and the friction coefficient and pressure resistance are increased accordingly. The present invention was completed based on the discovery that the lubrication properties such as rolling strength and rolling load can be further improved. The purpose of the present invention is to have a lubricating performance superior to conventional palm oil or tallow-based rolling oils, or substituted fatty acid esters of castor oil, and to be suitable for the harsh rolling process currently required. The objective is to provide a satisfactory rolling oil. The present invention consists of (A) castor oil, (B) castor oil to which alkylene oxide has been added, (C), (A) or (B) and carbon number 4.
(A) of a partial ester in which at least one hydroxyl group remains in the molecule obtained by reacting with -60 monocarboxylic acid or polyhydric carboxylic acid,
(B) and (C) A polymer obtained by thermally polymerizing a reaction product obtained by performing an esterification reaction with an unsaturated fatty acid having 12 to 24 carbon atoms and at least one selected from the three groups is used. The present invention relates to a metal rolling oil for high pressure rolling with excellent lubrication performance. The present invention uses the above-described polymer as one of the main components, and if necessary, animal and vegetable oils, mineral oils, antioxidants, and surfactants can be mixed therein. The alkylene oxide-added castor oil of the present invention can be obtained by adding alkylene oxide to castor oil by a conventional method. In addition, partial esters obtained by reacting castor oil or castor oil derivatives with monocarboxylic acids or polyhydric carboxylic acids having 4 to 60 carbon atoms can be produced by an esterification reaction by conventional dehydration condensation. It can also be obtained by transesterification using lower alkyl esters of fatty acids. In addition, the reaction product obtained by reacting at least one selected from (A), (B), and (C) with an unsaturated fatty acid having 12 to 24 carbon atoms or an ester thereof can be subjected to an esterification reaction by a conventional method. You can get it by doing it. Examples of monocarboxylic acids or polycarboxylic acids having 4 to 60 carbon atoms used here include capric acid, lauric acid, myristic acid, palmitic acid,
Saturated fatty acids such as stearic acid, arachidic acid, behenic acid, neo acids, side chain saturated fatty acids with a side chain in the α-position obtained by the oxo method, oleic acid, linoleic acid, linolenic acid, arachidonic acid, ricinoleic acid, etc. unsaturated fatty acids, succinic acid, adipic acid,
So-called dimer acids obtained by polymerizing dibasic carboxylic acids such as azelaic acid, sebacic acid, maleic acid, fumaric acid, itaconic acid, their dibasic carboxylic acid anhydrides, and unsaturated fatty acids;
Examples include polymerized polybasic carboxylic acids consisting of trimer acids, trimellitic acids, and the like. These fatty acids can be used alone or in combination of two or more. In addition, as unsaturated fatty acids with 12-24 carbon atoms,
Typical examples include oleic acid, linoleic acid, linolenic acid, elaidic acid, ricinolenic acid, and ricinoelaidic acid.These fatty acids may be used as they are in the esterification reaction, but lower alkyl esters A transesterification reaction may also be carried out. In addition, thermal polymerization of esters with unsaturated double bonds obtained from (A), (B), and (C) and unsaturated fatty acids having 12 to 24 carbon atoms is carried out by conventional methods. The polymerization reaction of the present invention involves a complex relationship between the double bonds of ricinolenic acid in castor oil and the double bonds of unsaturated fatty acids reacted with it, and by controlling the reaction conditions, it can be used as rolling oil. It is possible to obtain a polymer that satisfies the necessary conditions. The reaction conditions for thermal polymerization are that the obtained ester or polyester is heated as it is at 200 to 300°C for 10 to 30 hours, and the progress of the reaction is usually checked by measuring the viscosity. In addition, the reaction temperature and time are selected depending on the desired viscosity, and the reaction conditions are controlled so that the viscosity of the obtained polymer falls within the range of 300 to 1800 cst (40°C). The polymer thus obtained is used as it is as a rolling oil and exhibits excellent performance. In addition, the polymer of the present invention includes animal and vegetable oils, mineral oils, antioxidants,
It can also be used in combination with a surfactant or the like. The present invention will be explained below using examples. Synthesis Example 1 935 parts of castor oil, 284 parts of stearic acid, and 12 parts of para-toluenesulfonic acid (hereinafter referred to as PTSA) were heated at 150-180°C under a stream of nitrogen gas (hereinafter referred to as N2 gas).
The mixture was reacted for 6 hours to obtain an ester (ester-1) with an acid value of 1.0 and a hydroxyl value of 89.5. 423 parts of oleic acid and 16 parts of PTSA were added to this ester and reacted at 150-180°C for 8 hours to obtain a polyester having an acid value of 4.5, a hydroxyl value of 5.0, and a viscosity of 105cst (40°C). Furthermore, this polyester is 260−280
Thermal polymerization was carried out at ℃ for 20 hours to obtain a polymer having a viscosity of 700 cst (40 ℃). Synthesis Example 2 935 parts of castor oil, 733 parts of oleic acid, and 16 parts of PTSA were reacted at 150-160°C for 8 hours under a stream of N2 gas.
An ester (Ester-2) having an acid value of 7.8, a hydroxyl value of 3.2, and a viscosity of 110 cst (40°C) was obtained. Subsequently, this ester was thermally polymerized at 260-270℃ for 20 hours, resulting in a viscosity of 1050cst.
(40°C) was obtained. Synthesis example 3 Castor oil with 30 moles of ethylene oxide added
2255 parts of oleic acid, 733 parts of oleic acid, and 30 parts of PTSA were reacted at 130-140°C for 6 hours under a N2 gas stream to give an acid value of 6.5.
An ester (Ester-3) having a hydroxyl value of 4.8 and a viscosity of 102 cst (40°C) was obtained. Next, add this ester
Thermal polymerization at 220-230℃ for 15 hours, viscosity 620cst (40℃)
A polymer was obtained. Synthesis example 4 935 parts of castor oil, distilled rice bran fatty acid (iodine value
120) 564 parts and 15 parts of PTSA were heated under a stream of N2 gas for 150−
React at 180°C for 6 hours, followed by maleic anhydride 18
The reaction was carried out at 100℃ for 2 hours and at 150-160℃ for 4 hours, resulting in an acid value of 1.8, a hydroxyl value of 4.5, and a viscosity of 380 cst (40
℃) polyester (ester-4) was obtained. Subsequently, this ester was further thermally polymerized at 260-270°C for 15 hours to obtain a polymer having a viscosity of 1350cst (40°C). Synthesis example 5 935 parts of castor oil, distilled rice bran fatty acid (iodine value
120) 738 parts and 12 parts of PTSA under N2 gas flow,
Reacted at 150-180℃ for 6 hours, acid value 1.0, hydroxyl value
1.8, viscosity 100cst (40℃) ester (ester-
5) was obtained. Subsequently, this ester was thermally polymerized at 240-260°C for 15 hours to obtain a polymer having a viscosity of 800cst (40°C). Synthesis Example 6 3835 parts of castor oil with 50 moles of propylene oxide added, distilled rice bran fatty acid (iodine value 120) 733
and 45.5 parts of PTSA at 140-150℃ under N2 gas flow.
Reacted for 7 hours, acid value 3.6, hydroxyl value 4.2, viscosity
An ester (ester-6) of 115 cst (40°C) was obtained. This ester was further heated at 240-260°C for 16 hours to carry out a thermal polymerization reaction to obtain a polymer having a viscosity of 750cst (40°C). Example No. 1-7 was prepared using the polymer of Synthesis Example 1-6 alone or as a blend as shown in Table 1, and a metal rolling oil lubrication performance test was conducted.

【表】 実施例No.1−7の摩擦係数(μ)、耐圧性の測
定を行い、その結果を表−2に示す。また、圧延
試験は実施例No.1−6については圧延材料に一定
量そのまま塗布し、またNo.7は15%のエマルジヨ
ンとして供給して、試験を行つた。圧延材料への
付着油量は実施例No.1−7すべて1g/m2となる
ようにした。試験の結果を圧下率(%)と圧下力
(ton)との関係をもつて圧延性能評価とし、図−
1に示した。 比較例として市販の牛脂系圧延油を用いた。 なお、合成例1〜6で得たエステル1〜6につ
いて、その単体を試料とし実施例と同様に摩擦係
数、耐圧性、圧下率が60%の時の圧延荷重を測定
した。 その結果を表−2(参考例)に示す。 本発明の鋼板用圧延油の潤滑性能に関する試験
法は下記の通りである。 摩擦係数試験法 曽田式振子型油性試験機N−型 耐荷重能試験法 シエル型高速四球式摩擦試験機 圧延試験法 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)の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 またその時圧延荷重(ton)をロードセルにて
測定した。
[Table] The friction coefficient (μ) and pressure resistance of Example No. 1-7 were measured, and the results are shown in Table-2. In addition, the rolling test was conducted by applying a fixed amount of Example No. 1-6 to the rolled material as it was, and by supplying Example No. 7 as a 15% emulsion. The amount of oil adhering to the rolled material was set to 1 g/m 2 in all Examples Nos. 1-7. The test results are used to evaluate rolling performance based on the relationship between rolling reduction ratio (%) and rolling force (ton), and are shown in Figure-
Shown in 1. As a comparative example, commercially available tallow-based rolling oil was used. For the esters 1 to 6 obtained in Synthesis Examples 1 to 6, the friction coefficient, pressure resistance, and rolling load at a rolling reduction of 60% were measured using single samples as in the same manner as in the examples. The results are shown in Table 2 (Reference Example). The test method regarding the lubrication performance of the rolling oil for steel plates of the present invention is as follows. Friction coefficient test method Soda type pendulum type oil tester N-type load carrying capacity test method Shell type high speed four ball friction tester rolling test method Rolling mill: Four-roll rolling mill Work roll diameter 150mm Width 140mm Back-up roll diameter 250mm Width 140mm Roll material Chrome steel roll circumferential speed 30m/min Rolling material: SPC-C Thickness 0.60mm x Width 50mm x Length 150mm Method of measuring rolling performance Two rolls with a spacing of 50mm (l 1 ) are placed on the steel plate before rolling. A line was drawn, the line was rolled, the distance (l 2 ) after rolling was measured, and the rolling reduction was determined using the following formula. Rolling ratio (%)=l 2 -l 1 /l 2 At that time, the rolling load (ton) was measured using a load cell.

【表】 以上のように本発明で得られるヒマシ油または
その誘導体を熱重合して得られる重合物又はそれ
をベースオイルとした金属圧延油(実施例1〜
7)は、熱重合を行わないエステル(参考例のエ
ステル1〜6)に比較して摩擦係数は低く、高速
回転における耐圧性が高く、また圧延荷重も低
く、すぐれた潤滑性及び圧延性能を示している。
これらの結果より高い油膜強度を有し、高速適性
を持つた圧延油が得られ、これを用いることによ
り高圧下、高速度下での圧延が行われ、より高能
率で圧延鋼板を製造することができる。
[Table] Polymers obtained by thermally polymerizing castor oil or its derivatives obtained in the present invention as described above, or metal rolling oils using the same as base oil (Examples 1 to 3)
7) has a lower coefficient of friction than esters that do not undergo thermal polymerization (esters 1 to 6 in reference examples), has higher pressure resistance at high speed rotation, and has a lower rolling load, providing excellent lubricity and rolling performance. It shows.
From these results, a rolling oil with high oil film strength and suitability for high speeds was obtained, and by using this oil, rolling could be performed under high pressure and high speed, and rolled steel sheets could be manufactured with higher efficiency. Can be done.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は実施例及び比較例の圧延性能を圧延荷重
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 diagram showing the rolling performance of Examples and Comparative Examples in terms of the relationship between rolling load and rolling reduction.

Claims (1)

【特許請求の範囲】[Claims] 1 (A)ヒマシ油、(B)アルキレンオキサイドを付加
したヒマシ油、(C)、(A)または(B)と炭素数4−60の
モノカルボン酸またはおよび多価カルボン酸と反
応して得られる分子中に少なくとも1ケのヒドロ
キシル基が残存した部分エステルの、(A)、(B)、(C)
3群より選ばれたる少なくとも1種と、炭素数12
−24の不飽和脂肪酸とエステル化反応を行つて得
られる反応生成物を熱重合して得られる重合物を
用いることを特徴とする金属圧延油。
1. Obtained by reacting (A) castor oil, (B) castor oil with alkylene oxide added, (C), (A) or (B) with a monocarboxylic acid or polycarboxylic acid having 4 to 60 carbon atoms. (A), (B), (C) of a partial ester in which at least one hydroxyl group remains in the molecule
At least one species selected from group 3 and carbon number 12
A metal rolling oil characterized by using a polymer obtained by thermally polymerizing a reaction product obtained by carrying out an esterification reaction with a -24 unsaturated fatty acid.
JP8870879A 1979-07-14 1979-07-14 Metal rolling oil Granted JPS56106998A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8870879A JPS56106998A (en) 1979-07-14 1979-07-14 Metal rolling oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8870879A JPS56106998A (en) 1979-07-14 1979-07-14 Metal rolling oil

Publications (2)

Publication Number Publication Date
JPS56106998A JPS56106998A (en) 1981-08-25
JPS6325638B2 true JPS6325638B2 (en) 1988-05-26

Family

ID=13950384

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8870879A Granted JPS56106998A (en) 1979-07-14 1979-07-14 Metal rolling oil

Country Status (1)

Country Link
JP (1) JPS56106998A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02126940U (en) * 1989-03-29 1990-10-19

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5220430A (en) * 1975-08-09 1977-02-16 Azuma Tetsukou Kk Knife valve and it*s making method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5220430A (en) * 1975-08-09 1977-02-16 Azuma Tetsukou Kk Knife valve and it*s making method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02126940U (en) * 1989-03-29 1990-10-19

Also Published As

Publication number Publication date
JPS56106998A (en) 1981-08-25

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