JPS6358879B2 - - Google Patents

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Publication number
JPS6358879B2
JPS6358879B2 JP2197987A JP2197987A JPS6358879B2 JP S6358879 B2 JPS6358879 B2 JP S6358879B2 JP 2197987 A JP2197987 A JP 2197987A JP 2197987 A JP2197987 A JP 2197987A JP S6358879 B2 JPS6358879 B2 JP S6358879B2
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Japan
Prior art keywords
parts
rolling
castor oil
acid
oil
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Expired - Lifetime
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JP2197987A
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Japanese (ja)
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JPS62270693A (en
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Priority to JP2197987A priority Critical patent/JPS62270693A/en
Publication of JPS62270693A publication Critical patent/JPS62270693A/en
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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進み、ミル
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未だこれに代る
圧延油が見出されていないのが現状である。 本発明は従来のパーム油や牛脂系の圧延油より
すぐれた圧延性能を有し、現在要求されている苛
酷な圧延工程に対して、満足し得る圧延油を提供
せんとするものである。 本発明の圧延油は次のものより構成される。 炭素数12〜22の脂肪族カルボン酸とヒマシ油ま
たは水素添加したヒマシ油とを反応して得られ
る、その分子中にヒドロキシル基を少なくとも1
個残存したる形のヒマシ油の部分エステルまたは
水素添加ヒマシ油の部分エステルに、さらにアル
キレンオキシドを付加して得られる付加反応物
(以下、「AO付加物」と略記す)と、エポキシ基
を2または3個有する多価エポキシ化合物と反応
して得られる化合物を用いることを特徴とする金
属圧延油であり、必要に応じて、それに極圧添加
剤、界面活性剤、酸化防止剤等を配合して用いる
ことも可能である。 本発明に用いる炭素数12〜22の脂肪酸カルボン
酸としては、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、オレイン酸、リノール酸、リノレ
ン酸、リシノール酸、アラキドン酸等の不飽和脂
肪酸が挙げられる。 次に炭素数12〜22の脂肪族カルボン酸と、ヒマ
シ油またはヒマシ油に水素添加反応を行つて得ら
れる水素添加ヒマシ油とを反応して、分子中に少
なくとも1ケのヒドロキシル基を残存した形のヒ
マシ油の部分エステルまたは水素添加ヒマシ油の
部分エステルを得る。 分子中に少なくとも1ケのヒドロキシル基を残
存した形のヒマシ油の部分エステル、または水素
添加ヒマシ油の部分エステルとは、エステル化後
の分子中に、平均して少なくとも1ケのヒドロキ
シル基を残存するものである。 上記ヒマシ油の部分エステルまたは水素添加ヒ
マシ油の部分エステルは常法によりヒマシ油また
は水素添加ヒマシ油と炭素数12〜22の脂肪族カル
ボン酸との間でエステル化反応を行つて得られ
る。その反応条件の一例を示せば、ヒマシ油また
は水素添加ヒマシ油1モルに対し、その分子中の
ヒドロキシル基を少なくとも1ケ残存するよう
に、脂肪族カルボン酸のモル数を求め反応に用い
る。例えば、ヒマシ油または水素添加ヒマシ油1
モルに対し、1〜2モルの脂肪族カルボン酸を加
え、窒素ガス気流下に140〜260℃の温度で2〜25
時間反応して目的の部分エステルを得る。部分エ
ステル分子中に残存するヒドロキシル基の数は水
酸基価より算出する。 次にこの部分エステル化合物にアルキレンオキ
シドを付加してAO付加物を得る。この部分エス
テル化合物へのアルキレンオキシドの付加反応も
常法により行なわれる。ここで用いられるアルキ
レンオキシドとしては、エチレンオキシド、プロ
ピレンオキシドが挙げられ、これらアルキレンオ
キシドは1種のみを付加しても、また2種をラン
ダムまたはブロツク的に付加しても良く、その付
加モル数は2〜100モル、好ましくは3〜60モル
である。 以上のようにして得られるAO付加物に、エポ
キシ基を2〜3個有する多価エポキシ化合物を反
応して本発明の金属圧延油に用いる化合物を得
る。AO付加物と多価エポキシ化合物との反応は
AO付加物1モルに多価エポキシ化合物0.3〜2モ
ルを加え、70〜120℃で反応して得られる。 本発明におけるエポキシ基を2〜3個有する多
価エポキシ化合物としては、エチレングリコール
ジグリシジルエーテル、グリセリントリグリシジ
ルエーテル、アジピン酸ジグリシジルエステル、
コハク酸ジグリシジルエステル、ポリエチレング
リコールジグリシジルエーテルが挙げられる。 上記AO付加物と多価エポキシ化合物を反応し
て得られる化合物はそのまま用いて、圧延油とし
て高い性能を有するが、従来の圧延油と混合して
使用することもでき、又必要に応じて極圧添加
剤、界面活性剤、酸化防止剤等を配合して用いる
こともできる。 以下実施例を挙げ本発明を更に説明する。実施
例中の部数は重量部を示す。 合成例 1 ラウリン酸200部、沃素価2.5の水素添加ヒマシ
油940部、パラトルエンスルホン酸(以下
「PTSA」と略記する)11部を窒素ガス気流下に
140〜160℃で8時間反応し、酸価0.9、水酸基価
96.2の分子中に平均2ケのヒドロキシル基を残存
したるエステルを得た。 このエステルにプロピオンオキシド580部を苛
性カリ2.3部の存在下に付加反応を行い、AO付加
物を得た。次にAO付加物にエチレングリコール
ジグリシジルエーテル174部、三弗化硼素エーテ
ラート2部を加え、80〜90℃にて6時間反応し、
酸価1.0、水酸基価57.5の化合物を得た。 合成例 2 イソステアリン酸568部、ヒマシ油935部、
PTSA15部を窒素ガス気流下に160〜200℃で6時
間反応し、酸価4.5、水酸基価38.2の分子中に平
均1ケのヒドロキシル基を残存したるエステルを
得た。これにプロピレンオキシド2030部を苛性カ
リの存在下に付加反応した。得られた反応生成物
にポリエステルグリコール(MW=400)ジグリ
シジルエーテル250部を加え、酸価1.6、水酸基価
15.0の化合物を得た。 合成例 3 ステアリン酸568部、沃素価2.0の水素添加ヒマ
シ油939部、PTSA15部を窒素ガス気流下に150〜
180℃で6時間反応し、酸価2.0、水酸基価39.2の
分子中に平均1ケのヒドロキシル基を残存したる
エステルを得た。 このエステルにエチレンオキシド880部を苛性
カリ3部の存在下に付加反応を行い、AO付加物
を得た。次にAO付加物2351部にコハク酸ジグリ
シジルエステル232部、三弗化硼素エーテラート
2部を加え、80℃にて6時間反応し、酸価0.8、
水酸基価30.0の化合物を得た。 合成例 4 ベヘン酸340部、ヒマシ油935部、PTSA13部を
窒素ガス気流下に170〜180℃で6時間反応し、酸
価0.8、水酸基価90.0の分子に平均2ケのヒドロ
キシル基を残存したるエステルを得た。 このエステルにエチレンオキシド1300部を苛性
カリ3部の存在下に170〜180℃で付加反応を行
い、AO付加物を得た。次にAO付加物にグリセ
リントリグリシジルエーテル130部、三弗化硼素
エーテラート2部を加え、80〜90℃で6時間反応
し、酸価0.4、水酸基価40.2の化合物を得た。 合成例 5 オレイン酸282部、ヒマシ油935部、PTSA12部
を窒素ガス気流下に150〜180℃で6時間反応し、
酸価1.1、水酸基価89.5の分子中に平均2ケのヒ
ドロキシル基を残存したるエステルを得た。 このエステルにエチレンオキシド264部を苛性
カリ3部の存在下に付加反応を行い、AO付加物
を得た。次にこのAO付加物にアジピン酸シグリ
シジルエーテル258部、三弗化硼素エーテラート
2部を加え、80℃にて6時間反応し、酸価0.8、
水酸基価64.1の化合物を得た。 合成例 6 リシノール酸300部、ヒマシ油935部、PTSA12
を窒素ガス気流下に160〜170℃で5時間反応し、
酸価1.1、水酸基価137.5の分子中に平均3ケのヒ
ドロキシル基を残存したるエステルを得た。 このエステルに苛性カリ3部の存在下に、エチ
レンオキシド440部を160〜170℃で付加反応し、
さらにプロピオンオキシド290部を170〜180℃で
付加反応を行い、AO付加物を得た。次にAO付
加物にエチレングリコールジグリシジルエーテル
87部、三弗化硼素エーテラート2部を加え、80℃
で6時間反応し、酸価0.8、水酸基価55.4の化合
物を得た。 合成例1〜6で得た化合物を用いた表―1に示
す組成の圧延油の実施例1〜6の摩擦係数(μ)、
耐圧性の測定を行つた。その結果を比較例として
牛脂系圧延油の測定結果とともに表―2に示し
た。また、圧延性能試験は実施例1,2について
は圧延材料に一定量の圧延油をそのまま塗布し、
また実施例3〜5および比較例については5%濃
度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1〜6及び比較
例のすべて1g/m2となるようにした。 試験の結果を圧下率(%)と圧延荷重(ton)
との関係をもつて圧延性能評価とし、図―1に示
した。 本発明の圧延油の潤滑性能に関する試験方法は
次の通りである。 摩擦係数(μ)試験法 曽田式振り子型油性試験機N型 耐荷重能試験法 シエル型高速四球式摩擦試験機
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 additives and oil-based oils are used as rolling oils. Products containing improvers, antioxidants, surfactants, etc. are widely used. On the other hand, the progress of rolling machinery equipment has progressed significantly, and as mills have become larger, there has been a demand for rationalization and precision of the rolling process, 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 oil are becoming more severe.
Palm oil and tallow-based rolling oils are no longer able to satisfy this condition, but at present no alternative rolling oil has yet been found. The present invention aims to provide a rolling oil that has better rolling performance than conventional palm oil or beef tallow-based rolling oils and can satisfy the harsh rolling processes currently required. The rolling oil of the present invention is composed of the following. At least one hydroxyl group in the molecule obtained by reacting an aliphatic carboxylic acid having 12 to 22 carbon atoms with castor oil or hydrogenated castor oil.
An addition reaction product (hereinafter abbreviated as "AO adduct") obtained by further adding an alkylene oxide to a partial ester of castor oil or a partial ester of hydrogenated castor oil in the form of an epoxy group It is a metal rolling oil characterized by using a compound obtained by reacting with a polyvalent epoxy compound having 2 or 3 epoxy compounds, and if necessary, extreme pressure additives, surfactants, antioxidants, etc. are added thereto. It is also possible to use it as The fatty acid carboxylic acids having 12 to 22 carbon atoms used in the present invention include saturated fatty acids such as lauric acid, myristic acid, palmitic acid, stearic acid, arachic acid, behenic acid, oleic acid, linoleic acid, linolenic acid, ricinoleic acid, Examples include unsaturated fatty acids such as arachidonic acid. Next, an aliphatic carboxylic acid having 12 to 22 carbon atoms is reacted with castor oil or hydrogenated castor oil obtained by hydrogenating castor oil, so that at least one hydroxyl group remains in the molecule. to obtain a partial ester of castor oil in the form or a partial ester of hydrogenated castor oil. Partial esters of castor oil with at least one hydroxyl group remaining in the molecule or partial esters of hydrogenated castor oil are those with at least one hydroxyl group remaining on average in the molecule after esterification. It is something to do. The above partial ester of castor oil or partial ester of hydrogenated castor oil can be obtained by carrying out an esterification reaction between castor oil or hydrogenated castor oil and an aliphatic carboxylic acid having 12 to 22 carbon atoms in a conventional manner. To give an example of the reaction conditions, the number of moles of aliphatic carboxylic acid is determined and used in the reaction so that at least one hydroxyl group remains in the molecule per mole of castor oil or hydrogenated castor oil. For example, castor oil or hydrogenated castor oil 1
Add 1 to 2 moles of aliphatic carboxylic acid per mole, and heat at a temperature of 140 to 260℃ under a nitrogen gas flow for 2 to 25 hours.
The desired partial ester is obtained by a time reaction. The number of hydroxyl groups remaining in the partial ester molecule is calculated from the hydroxyl value. Next, an alkylene oxide is added to this partial ester compound to obtain an AO adduct. The addition reaction of alkylene oxide to this partial ester compound is also carried out by a conventional method. Examples of the alkylene oxide used here include ethylene oxide and propylene oxide, and these alkylene oxides may be added alone or in a random or block manner, and the number of moles added is The amount is from 2 to 100 mol, preferably from 3 to 60 mol. The AO adduct obtained as described above is reacted with a polyvalent epoxy compound having 2 to 3 epoxy groups to obtain a compound used in the metal rolling oil of the present invention. The reaction between AO adduct and polyepoxy compound is
It is obtained by adding 0.3 to 2 moles of a polyvalent epoxy compound to 1 mole of the AO adduct and reacting at 70 to 120°C. Examples of the polyepoxy compound having 2 to 3 epoxy groups in the present invention include ethylene glycol diglycidyl ether, glycerin triglycidyl ether, adipic acid diglycidyl ester,
Examples include succinic acid diglycidyl ester and polyethylene glycol diglycidyl ether. The compound obtained by reacting the above-mentioned AO adduct with a polyepoxy compound has high performance as a rolling oil when used as it is, but it can also be used by mixing with conventional rolling oil, or if necessary, it can be used as a rolling oil. It is also possible to mix and use additives, surfactants, antioxidants, etc. The present invention will be further explained below with reference to Examples. The numbers in the examples indicate parts by weight. Synthesis Example 1 200 parts of lauric acid, 940 parts of hydrogenated castor oil with an iodine value of 2.5, and 11 parts of para-toluenesulfonic acid (hereinafter abbreviated as "PTSA") were added under a nitrogen gas stream.
Reacted at 140-160℃ for 8 hours, acid value 0.9, hydroxyl value
An ester having an average of 2 hydroxyl groups remaining in the molecule of 96.2 was obtained. An addition reaction of 580 parts of propion oxide to this ester was carried out in the presence of 2.3 parts of caustic potassium to obtain an AO adduct. Next, 174 parts of ethylene glycol diglycidyl ether and 2 parts of boron trifluoride etherate were added to the AO adduct and reacted at 80 to 90°C for 6 hours.
A compound with an acid value of 1.0 and a hydroxyl value of 57.5 was obtained. Synthesis example 2 568 parts of isostearic acid, 935 parts of castor oil,
15 parts of PTSA was reacted at 160 to 200°C for 6 hours under a nitrogen gas stream to obtain an ester having an acid value of 4.5 and a hydroxyl value of 38.2, with an average of one hydroxyl group remaining in the molecule. To this was added 2030 parts of propylene oxide in the presence of caustic potash. 250 parts of polyester glycol (MW=400) diglycidyl ether was added to the obtained reaction product to give an acid value of 1.6 and a hydroxyl value.
15.0 compound was obtained. Synthesis Example 3 568 parts of stearic acid, 939 parts of hydrogenated castor oil with an iodine value of 2.0, and 15 parts of PTSA were mixed under a stream of nitrogen gas to
The reaction was carried out at 180° C. for 6 hours to obtain an ester having an acid value of 2.0 and a hydroxyl value of 39.2, with an average of one hydroxyl group remaining in the molecule. An addition reaction of 880 parts of ethylene oxide to this ester was carried out in the presence of 3 parts of caustic potassium to obtain an AO adduct. Next, 232 parts of succinic acid diglycidyl ester and 2 parts of boron trifluoride etherate were added to 2351 parts of the AO adduct, and the mixture was reacted at 80°C for 6 hours.
A compound with a hydroxyl value of 30.0 was obtained. Synthesis Example 4 340 parts of behenic acid, 935 parts of castor oil, and 13 parts of PTSA were reacted at 170 to 180°C for 6 hours under a stream of nitrogen gas, and an average of 2 hydroxyl groups remained in the molecule with an acid value of 0.8 and a hydroxyl value of 90.0. An ester was obtained. An addition reaction of 1300 parts of ethylene oxide to this ester was carried out at 170 to 180°C in the presence of 3 parts of caustic potassium to obtain an AO adduct. Next, 130 parts of glycerin triglycidyl ether and 2 parts of boron trifluoride etherate were added to the AO adduct and reacted at 80 to 90°C for 6 hours to obtain a compound with an acid value of 0.4 and a hydroxyl value of 40.2. Synthesis Example 5 282 parts of oleic acid, 935 parts of castor oil, and 12 parts of PTSA were reacted at 150 to 180°C for 6 hours under a nitrogen gas flow.
An ester having an acid value of 1.1 and a hydroxyl value of 89.5 and having an average of two hydroxyl groups remaining in the molecule was obtained. An addition reaction of 264 parts of ethylene oxide to this ester was carried out in the presence of 3 parts of caustic potassium to obtain an AO adduct. Next, 258 parts of adipic acid siglycidyl ether and 2 parts of boron trifluoride etherate were added to this AO adduct, and the mixture was reacted at 80°C for 6 hours.
A compound with a hydroxyl value of 64.1 was obtained. Synthesis example 6 ricinoleic acid 300 parts, castor oil 935 parts, PTSA12
was reacted at 160 to 170℃ for 5 hours under a nitrogen gas flow,
An ester having an acid value of 1.1 and a hydroxyl value of 137.5 and having an average of 3 hydroxyl groups remaining in the molecule was obtained. Addition reaction of 440 parts of ethylene oxide to this ester at 160 to 170°C in the presence of 3 parts of caustic potassium,
Further, an addition reaction was carried out with 290 parts of propion oxide at 170 to 180°C to obtain an AO adduct. Next, ethylene glycol diglycidyl ether is added to the AO adduct.
Add 87 parts and 2 parts of boron trifluoride etherate, and heat at 80°C.
The mixture was reacted for 6 hours to obtain a compound with an acid value of 0.8 and a hydroxyl value of 55.4. Friction coefficient (μ) of Examples 1 to 6 of rolling oil having the composition shown in Table 1 using the compounds obtained in Synthesis Examples 1 to 6,
The pressure resistance was measured. The results are shown in Table 2 along with the measurement results for tallow-based rolling oil as a comparative example. In addition, in the rolling performance test for Examples 1 and 2, a certain amount of rolling oil was directly applied to the rolled material,
Further, in Examples 3 to 5 and Comparative Examples, tests were conducted by supplying the emulsion as a 5% concentration emulsion.
The amount of oil adhering to the rolled material was 1 g/m 2 in all Examples 1 to 6 and Comparative Example. Test results are shown in rolling reduction ratio (%) and rolling load (ton)
The relationship between the rolling performance and the rolling performance is evaluated and shown in Figure 1. The test method regarding the lubrication performance of the rolling oil of the present invention is as follows. Friction coefficient (μ) test method Soda pendulum type oil tester N type load-bearing capacity test method Shell type high speed four-ball friction tester

【表】【table】

【表】 圧延試験法 圧延機 :四段ロール式圧延機 ワークロール径150mm×巾140mm バツクアツプロール径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0.6mm×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/l2×100 またその時の圧延荷重(ton)をロードセルに
て測定した。
[Table] Rolling test method Rolling machine: Four-high roll rolling machine Work roll diameter 150mm x width 140mm Back-up roll diameter 250mm x width 140mm Roll material Chrome steel Roll circumferential speed 30m/min Rolling material: SPC-C Thickness 0.6mm × Width 50 mm × Length 150 mm Method for measuring rolling performance Draw two lines with a spacing of 50 mm (l 1 ) on the steel plate before rolling, roll this, measure the spacing 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.

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

図―1は、本発明圧延油実施例1〜6と、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。
FIG. 1 is a rolling performance comparison diagram showing the rolling performance of Examples 1 to 6 of the rolling oil of the present invention and a comparative example based on the relationship between rolling load and rolling reduction.

Claims (1)

【特許請求の範囲】[Claims] 1 炭素数12〜22の脂肪族カルボン酸と、ヒマシ
油または水素添加したヒマシ油とを反応して得ら
れる、その分子中にヒドロキシル基を少なくとも
1個残存したる形のヒマシ油の部分エステルまた
は水素添加ヒマシ油の部分エステルに、さらにア
ルキレンオキシドを付加して得られる付加反応物
と、エポキシ基を2または3個有する多価エポキ
シ化合物とを反応して得られる化合物を用いるこ
とを特徴とする金属圧延油。
1 A partial ester of castor oil in which at least one hydroxyl group remains in the molecule, obtained by reacting an aliphatic carboxylic acid having 12 to 22 carbon atoms with castor oil or hydrogenated castor oil; It is characterized by using a compound obtained by reacting an addition reaction product obtained by further adding an alkylene oxide to a partial ester of hydrogenated castor oil and a polyvalent epoxy compound having 2 or 3 epoxy groups. Metal rolling oil.
JP2197987A 1987-02-02 1987-02-02 Metal rolling oil Granted JPS62270693A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2197987A JPS62270693A (en) 1987-02-02 1987-02-02 Metal rolling oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2197987A JPS62270693A (en) 1987-02-02 1987-02-02 Metal rolling oil

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP1086080A Division JPS56109295A (en) 1980-02-02 1980-02-02 Metal rolling oil

Publications (2)

Publication Number Publication Date
JPS62270693A JPS62270693A (en) 1987-11-25
JPS6358879B2 true JPS6358879B2 (en) 1988-11-17

Family

ID=12070140

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2197987A Granted JPS62270693A (en) 1987-02-02 1987-02-02 Metal rolling oil

Country Status (1)

Country Link
JP (1) JPS62270693A (en)

Also Published As

Publication number Publication date
JPS62270693A (en) 1987-11-25

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