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JPS6358878B2 - - Google Patents
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JPS6358878B2 - - Google Patents

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Publication number
JPS6358878B2
JPS6358878B2 JP2197887A JP2197887A JPS6358878B2 JP S6358878 B2 JPS6358878 B2 JP S6358878B2 JP 2197887 A JP2197887 A JP 2197887A JP 2197887 A JP2197887 A JP 2197887A JP S6358878 B2 JPS6358878 B2 JP S6358878B2
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JP
Japan
Prior art keywords
parts
acid
rolling
castor oil
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 - Lifetime
Application number
JP2197887A
Other languages
Japanese (ja)
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JPS62270692A (en
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
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Priority to JP2197887A priority Critical patent/JPS62270692A/en
Publication of JPS62270692A publication Critical patent/JPS62270692A/en
Publication of JPS6358878B2 publication Critical patent/JPS6358878B2/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により構成される。 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、ジカルボン酸
とを反応して得られる化合物を用いることを特徴
とする金属圧延油であり、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、ジカ
ルボン酸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付加物とジカルボン酸との反
応はAO付加物1モルにジカルボン酸0.3〜2モル
を加え、130〜200℃で反応して得られる。 本発明におけるジカルボン酸には、コハク酸、
アジピン酸、アゼライン酸、セバシン酸、マレイ
ン酸が挙げられる。 上記AO付加物とジカルボン酸とを反応して得
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。 以下実施例を挙げて本発明をさらに詳細に説明
する。実施例中の部数は重量部を示す。 合成例 1 ステアリン酸284部、ヒマシ油935部、パラトル
エンスルホン酸(以下「PTSA」と略記す)12部
を反応器に入れ、窒素ガス気流下に150〜180℃で
6時間反応し、酸価1.0、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180〜200℃にて付加
反応してAO付加物を得た。得られたAO付加物
にセバシン酸202部、PTSA7部を加え、180〜200
℃で8時間反応し、酸価4.8、水酸基価11の化合
物を得た。 合成例 2 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。得られたAO付加物にアゼ
ライン酸188部、PTSA8.5部を加え180〜200℃で
12時間反応し、酸価6.0、水酸基価5.0の化合物を
得た。 合成例 3 ラウリン酸200部、沃素価2.5の水素添加ヒマシ
油940部、PTSA11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と残存したる
エステルを得た。このエステルにプロピレンオキ
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。得られたAO付加物にコ
ハク酸118部、PTSA6部を加え180〜200℃で8時
間反応し、酸価3.8、水酸基価7.5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85.6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1300部を苛性カリ3部
の存在下に170〜180℃で反応を行いAO付加物を
得た。得られたAO付加物にアジピン酸146部、
PTSA6部を加え180〜200℃で8時間反応し、酸
価5.4、水酸基価10.2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
ドロキシル化合物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。得られたAO付加物に無水マレイン酸49部、
PTSA4部を加え180〜200℃に8時間反応し、酸
価2.6、水酸基価31.6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
部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137.6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
にプロピレンオキシド290部を170〜180℃で付加
反応を行い、AO付加物を得た。得られたAO付
加物に無水マレイン酸98部、PTSA6部を加え、
180〜200℃に8時間反応し、酸価1.2、水酸基価
17.5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)、
耐圧性の測定を行い、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3〜6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。
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 a residual form of a dicarboxylic acid It is a metal rolling oil characterized by using a compound obtained by reaction, and if necessary, it is also possible to mix and use extreme pressure additives, surfactants, antioxidants, etc. This invention Examples of fatty acid carboxylic acids having 12 to 22 carbon atoms include saturated fatty acids such as lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, and behenic acid, oleic acid, linoleic acid, linolenic acid, ricinoleic acid, and arachidonic acid. Unsaturated fatty acids such as A partial ester of castor oil with at least one hydroxyl group remaining or a hydrogenated partial ester of castor oil is obtained.A partial ester of castor oil with at least one hydroxyl group remaining in the molecule or a hydrogenated partial ester is obtained. A partial ester of castor oil is one in which on average at least one hydroxyl group remains in the molecule after esterification.The above partial ester of castor oil or partial ester of hydrogenated castor oil is prepared by a conventional method. It is obtained by performing an esterification reaction between castor oil or hydrogenated castor oil and an aliphatic carboxylic acid having 12 to 22 carbon atoms.An example of the reaction conditions is that 1 mole of castor oil or hydrogenated castor oil is On the other hand, 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.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. Only one type of these alkylene oxides may be added, or two types may be added randomly or in blocks, 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 dicarboxylic acid to obtain a compound used in the metal rolling oil of the present invention. The reaction between the AO adduct and dicarboxylic acid is obtained by adding 0.3 to 2 moles of dicarboxylic acid to 1 mole of the AO adduct and reacting at 130 to 200°C. Dicarboxylic acids in the present invention include succinic acid,
Examples include adipic acid, azelaic acid, sebacic acid, and maleic acid. The compound obtained by reacting the above-mentioned AO adduct with dicarboxylic acid has high performance as a rolling oil when used as is, but it can also be used by mixing with conventional rolling oil, and if necessary, extreme pressure Additives, surfactants, antioxidants, etc. may also be added. EXAMPLES The present invention will be explained in more detail below with reference to Examples. The numbers in the examples indicate parts by weight. Synthesis Example 1 284 parts of stearic acid, 935 parts of castor oil, and 12 parts of para-toluene sulfonic acid (hereinafter abbreviated as "PTSA") were placed in a reactor and reacted at 150 to 180°C for 6 hours under a nitrogen gas flow to react with the acid. An ester having an average value of 1.0 and a hydroxyl value of 89.5 and having an average of 2 hydroxyl groups remaining in the molecule was obtained. Ethylene oxide 264 to this ester
1 part was subjected to an addition reaction at 180 to 200°C in the presence of 3 parts of caustic potassium to obtain an AO adduct. Add 202 parts of sebacic acid and 7 parts of PTSA to the obtained AO adduct to give 180 to 200
The reaction was carried out at ℃ for 8 hours to obtain a compound having an acid value of 4.8 and a hydroxyl value of 11. Synthesis Example 2 568 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. 188 parts of azelaic acid and 8.5 parts of PTSA were added to the obtained AO adduct at 180-200℃.
After reacting for 12 hours, a compound with an acid value of 6.0 and a hydroxyl value of 5.0 was obtained. Synthesis Example 3 200 parts of lauric acid, 940 parts of hydrogenated castor oil with an iodine value of 2.5, and 11 parts of PTSA were mixed under a stream of nitrogen gas to
The reaction was carried out at 160° C. for 8 hours to obtain an ester having an acid value of 0.9 and a hydroxyl value of 96.2, with an average of 2 hydroxyl groups in the molecule and remaining esters. An addition reaction of 580 parts of propylene oxide to this ester was carried out in the presence of 2.3 parts of caustic potassium to obtain an AO adduct. 118 parts of succinic acid and 6 parts of PTSA were added to the obtained AO adduct and reacted at 180 to 200°C for 8 hours to obtain a compound with an acid value of 3.8 and a hydroxyl value of 7.5. 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 nitrogen gas flow, leaving an average of 2 hydroxyl groups in the molecule with an acid value of 0.8 and a hydroxyl value of 85.6. A dripping ester was obtained. This ester was reacted with 1300 parts of ethylene oxide in the presence of 3 parts of caustic potassium at 170-180°C to obtain an AO adduct. 146 parts of adipic acid to the obtained AO adduct;
6 parts of PTSA was added and reacted at 180 to 200°C for 8 hours to obtain a compound with an acid value of 5.4 and a hydroxyl value of 10.2. 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 was obtained in which an average of 2 hydroxyl compounds remained in the molecule.
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. 49 parts of maleic anhydride to the obtained AO adduct;
4 parts of PTSA was added and reacted at 180-200°C for 8 hours to obtain a compound with an acid value of 2.6 and a hydroxyl value of 31.6. Synthesis example 6 ricinoleic acid 300 parts, castor oil 935 parts, PTSA12
The mixture was reacted for 5 hours at 160-170°C under a nitrogen gas stream to obtain an ester having an acid value of 1.1 and a hydroxyl value of 137.6, with an average of 3 hydroxyl groups remaining in the molecule.
This ester was subjected to an addition reaction of 440 parts of ethylene oxide at 160 to 170°C in the presence of 3 parts of caustic potassium, and then an addition reaction of 290 parts of propylene oxide at 170 to 180°C to obtain an AO adduct. Add 98 parts of maleic anhydride and 6 parts of PTSA to the obtained AO adduct,
Reacted at 180-200℃ for 8 hours, acid value 1.2, hydroxyl value
17.5 compounds were obtained. 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,
Pressure resistance was measured, and the results are shown in Table 2 along with the measurement results for tallow-based rolling oil as a comparative example.
In addition, rolling performance tests were conducted by applying a certain amount of rolling oil to the rolled material as it was for Examples 1 and 2, and by supplying it as a 5% concentration emulsion for Examples 3 to 6 and Comparative Examples. . The amount of oil attached to the rolled material was set to 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 rolling performance and rolling performance is evaluated and shown in Figure 1.

【表】【table】

【表】 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 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] 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 capacity test method Shell type high speed four ball friction tester rolling test method Rolling mill: Four-roll rolling mill 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 x width 50mm x length 150mm Measuring method of rolling performance 50mm intervals (l 1 ) on the steel plate before rolling Two lines were drawn, the lines were 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 ×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1〜5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 5 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、ジカルボン酸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; A metal rolling oil characterized in that 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 dicarboxylic acid is used.
JP2197887A 1987-02-02 1987-02-02 Metal rolling oil Granted JPS62270692A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2197887A JPS62270692A (en) 1987-02-02 1987-02-02 Metal rolling oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2197887A JPS62270692A (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
JPS62270692A JPS62270692A (en) 1987-11-25
JPS6358878B2 true JPS6358878B2 (en) 1988-11-17

Family

ID=12070113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2197887A Granted JPS62270692A (en) 1987-02-02 1987-02-02 Metal rolling oil

Country Status (1)

Country Link
JP (1) JPS62270692A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2008331637B2 (en) * 2007-11-28 2011-10-06 Colgate-Palmolive Company Ethoxylated and / or hydrogenated oil adduct

Also Published As

Publication number Publication date
JPS62270692A (en) 1987-11-25

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