JPS6358873B2 - - Google Patents
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- Publication number
- JPS6358873B2 JPS6358873B2 JP1387387A JP1387387A JPS6358873B2 JP S6358873 B2 JPS6358873 B2 JP S6358873B2 JP 1387387 A JP1387387 A JP 1387387A JP 1387387 A JP1387387 A JP 1387387A JP S6358873 B2 JPS6358873 B2 JP S6358873B2
- Authority
- JP
- Japan
- Prior art keywords
- rolling
- compound
- acid
- parts
- 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
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Description
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より構成される。
炭素数12〜22の脂肪族カルボン酸とポリアミン
を反応せしめて得られる1分子中に少なくとも1
個の活性水素を残存せしめたるアマイド化合物
に、さらにアルキレンオキシドを付加して得られ
る化合物(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、ポリ
アミンとを反応して分子中に少なくとも1ケのア
ミン基を残存するアマイド化合物を得るが、ここ
に用いるポリアミンとしてはエチレンジアミン、
プロピレンジアミン、ヘキサメチレンジアミン、
ジエチレントリアミン、トリエチレンテトラミ
ン、テトラエチレンペンタミン、ペンタエチレン
ヘキサミンが挙げられる。
上記のアマイド化合物は、ポリアミンと炭素数
12〜22の脂肪族カルボン酸との間でアマイド化反
応をつて得られる。その反応条件の一例を示せ
ば、ポリアミン1モルに対し、その分子中のアミ
ン基を少なくとも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、エチレンジアミン1モルに対し、ラヴ
リン酸ならば1モルを加え、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ア
マイド化合物を得る。アマイド化合物分子中に残
存するアミン基の数はアミン価より算出する。
次にこのアマイド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。このアマイド化合
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または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または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が挙げられ
る。
得られた反応生成物にアミンが残留する場合に
は必要に応じて、中和、四級化、両性化等の一般
的に知られている処理を、各々の処理に適した処
理剤を用いて行なつたのち、用いることができ
る。
これらの処理を行なうことによつて、反応生成
物の親水性を使用条件に応じて適正に調整するこ
とができるとともに、反応生成物の極性を調整
し、金属面への吸着性をコントロールすることも
できる。
これらの反応生成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詳細に説明す
る。
合成例 1
ラウリン酸200部、エチレンジアミン60部を窒
素ガス気流下150〜160℃で8時間反応した後、エ
チレンオキシド440部を140〜150℃で付加反応し
て、酸価1.8、水酸基価165.3の化合物を得た。次
いで、これにエチレングリコールジグリシジルエ
ーテル174部を加え、80〜90℃で6時間反応し、
酸価1.2、水酸基価2.0の化合物を得た。
合成例 2
ステアリン酸568部、ジエチレントリアミン103
部を窒素ガス気流下230〜240℃で6時間反応した
後、エチレンオキシド220部を170〜180℃で付加
反応し、次いで、プロピオンオキシド174部を170
〜190℃で化加反応して、酸価1.2、水酸基価79.5
の化合物を得た。これにアジピン酸ジグリシジル
エステル146部を加え、90〜110℃で6時間反応
し、酸価0.5、水酸基価25.0の化合物を得た。
合成例 3
ベヘン酸684部、トリエチレンテトラミン146部
を素気流下200〜240℃で20時間反応した後、エチ
レンオキシド880部を160〜180℃で付加反応して、
酸価3.5、水酸基価63の化合物を得た。次いで、
これにグリセリントリグリシジルエーテル130部
を加え、80〜90℃で6時間反応し、酸価2.7、水
酸基価30.1の化合物を得た。
合成例 4
オレイン酸202部、ヘキサメチレンジアミン116
部を窒素ガス気流下180〜190℃で10時間反応した
後、プロピレンオキシド870部を170〜180℃で付
加反応して、酸価1.5、水酸基価88.5の化合物を
得た。次いで、これにコハク酸ジグリシジルエス
テル230部を加え、80〜90℃で6時間反応し、酸
価1.0、水酸基価2.3の化合物を得た。
合成例 5
リシノール残894部、ペンタエチレンヘキサミ
ン232部を窒素ガス気流下190〜200℃で8時間反
応した後、エチレンオキシド880部を160〜170℃
で付加反応し、次いで、プロピレンオキシド580
部を180〜190℃で付加反応して、酸価1.5、水酸
基価130.0の化合物を得た。次いで、これにアジ
ピン酸ジグリシジルエステル260部を加え、80〜
90℃で5時間反応し、酸価1.1、水酸基価78.8の
化合物を得た。
合成例1〜5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1〜5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
料の付着油量は、実施例1〜5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 1 in 1 molecule obtained by reacting an aliphatic carboxylic acid having 12 to 22 carbon atoms with a polyamine.
A compound obtained by further adding an alkylene oxide to an amide compound in which active hydrogens remain (hereinafter abbreviated as AO adduct) is reacted with a polyepoxy compound having two or three epoxy groups. This is a metal rolling oil characterized by using a compound obtained by using a compound obtained by using a metal rolling oil.If necessary, it is also possible to mix and use extreme pressure additives, surfactants, antioxidants, etc. 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 a polyamine to obtain an amide compound in which at least one amine group remains in the molecule.The polyamine used here is ethylenediamine,
propylene diamine, hexamethylene diamine,
Examples include diethylenetriamine, triethylenetetramine, tetraethylenepentamine, and pentaethylenehexamine. The above amide compound has a polyamine and a carbon number
It is obtained through an amide reaction with 12 to 22 aliphatic carboxylic acids. 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 amine group remains in the molecule per mole of polyamine. For example, add 1 mole of lavric acid to 1 mole of ethylenediamine, and add it under a nitrogen gas stream.
The desired amide compound is obtained by reacting at a temperature of 140 to 260°C for 2 to 25 hours. The number of amine groups remaining in the amide compound molecule is calculated from the amine value. Next, an alkylene oxide is added to this amide compound to obtain an AO adduct. The addition reaction of alkylene oxide to this amide 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 two or three epoxy groups to obtain a compound used in the metal rolling oil of the present invention. In the reaction between the AO adduct and the polyepoxy compound, 1 mole of the AO adduct is mixed with 0.3 to 2 polyepoxy compounds.
It is obtained by adding moles and reacting at 70-120℃. Examples of the polyepoxy compound having two or three epoxy groups in the present invention include ethylene glycol diglycidyl ether, glycerin triglycidyl ether, adipic acid diglycidyl ester, and succinic acid diglycidyl ester. If amines remain in the resulting reaction product, generally known treatments such as neutralization, quaternization, and amphotericization may be performed as necessary using processing agents suitable for each treatment. After doing so, it can be used. By performing these treatments, the hydrophilicity of the reaction product can be adjusted appropriately according to the usage conditions, and the polarity of the reaction product can also be adjusted to control adsorption to metal surfaces. You can also do it. These reaction products have high performance as rolling oil when used as is, but they can also be used by mixing with conventional rolling oil, and if necessary, extreme pressure additives, surfactants, and antioxidants may be added. It is also possible to use a mixture of the following. The present invention will be explained in more detail with reference to Examples below. Synthesis Example 1 After reacting 200 parts of lauric acid and 60 parts of ethylenediamine at 150 to 160°C under a nitrogen gas stream for 8 hours, addition reaction with 440 parts of ethylene oxide at 140 to 150°C produced a compound with an acid value of 1.8 and a hydroxyl value of 165.3. I got it. Next, 174 parts of ethylene glycol diglycidyl ether was added to this and reacted at 80 to 90°C for 6 hours.
A compound with an acid value of 1.2 and a hydroxyl value of 2.0 was obtained. Synthesis example 2 568 parts of stearic acid, 103 parts of diethylenetriamine
After reacting for 6 hours at 230 to 240°C under a nitrogen gas stream, 220 parts of ethylene oxide was added at 170 to 180°C, and then 174 parts of propion oxide was added to 170 parts of propion oxide.
By chemical addition reaction at ~190℃, acid value 1.2, hydroxyl value 79.5
The compound was obtained. 146 parts of adipic acid diglycidyl ester was added to this and reacted at 90 to 110°C for 6 hours to obtain a compound with an acid value of 0.5 and a hydroxyl value of 25.0. Synthesis Example 3 684 parts of behenic acid and 146 parts of triethylenetetramine were reacted at 200 to 240°C for 20 hours under a stream of air, and then 880 parts of ethylene oxide was added to the reaction mixture at 160 to 180°C.
A compound with an acid value of 3.5 and a hydroxyl value of 63 was obtained. Then,
130 parts of glycerin triglycidyl ether was added to this and reacted at 80 to 90°C for 6 hours to obtain a compound with an acid value of 2.7 and a hydroxyl value of 30.1. Synthesis example 4 202 parts of oleic acid, 116 parts of hexamethylene diamine
After reacting for 10 hours at 180-190°C under a nitrogen gas stream, 870 parts of propylene oxide was added at 170-180°C to obtain a compound with an acid value of 1.5 and a hydroxyl value of 88.5. Next, 230 parts of succinic acid diglycidyl ester was added thereto, and the mixture was reacted at 80 to 90°C for 6 hours to obtain a compound having an acid value of 1.0 and a hydroxyl value of 2.3. Synthesis Example 5 After reacting 894 parts of ricinol residue and 232 parts of pentaethylenehexamine at 190 to 200°C under a nitrogen gas stream for 8 hours, 880 parts of ethylene oxide was reacted at 160 to 170°C.
addition reaction with propylene oxide 580
A portion was subjected to an addition reaction at 180 to 190°C to obtain a compound having an acid value of 1.5 and a hydroxyl value of 130.0. Next, 260 parts of adipic acid diglycidyl ester was added to this, and 80~
The reaction was carried out at 90°C for 5 hours to obtain a compound with an acid value of 1.1 and a hydroxyl value of 78.8. Friction coefficient (μ) of Examples 1 to 5 of rolling oil having the composition shown in Table 1 using the compounds obtained in Synthesis Examples 1 to 5,
The pressure resistance was measured and the results are shown in Table 2 along with the measurement results for tallow 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 5 and Comparative Examples. . The amount of oil attached to the rolled material was set to 1 g/m 2 in all Examples 1 to 5 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.
【表】【table】
【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×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 50mm x length 150mm Measuring method of rolling performance Rolling performance is measured by applying 50mm spacing (l 1 ) to 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―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)
ミンを反応せしめて得られる、1分子中に少なく
とも1個の活性水素を残存せしめたるアマイド化
合物にさらにアルキレンオキシドを付加して得ら
れる化合物と、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 compound obtained by further adding an alkylene oxide to an amide compound in which at least one active hydrogen remains in one molecule, which is obtained by reacting an aliphatic carboxylic acid having 12 to 22 carbon atoms with a polyamine; A metal rolling oil characterized by using a compound obtained by reacting with a polyvalent epoxy compound having two or three epoxy groups.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1387387A JPS6339987A (en) | 1987-01-23 | 1987-01-23 | Metal rolling oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1387387A JPS6339987A (en) | 1987-01-23 | 1987-01-23 | Metal rolling oil |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1086180A Division JPS56109297A (en) | 1980-02-02 | 1980-02-02 | Metal rolling oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6339987A JPS6339987A (en) | 1988-02-20 |
| JPS6358873B2 true JPS6358873B2 (en) | 1988-11-17 |
Family
ID=11845349
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1387387A Granted JPS6339987A (en) | 1987-01-23 | 1987-01-23 | Metal rolling oil |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6339987A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01311193A (en) * | 1988-06-08 | 1989-12-15 | Dai Ichi Kogyo Seiyaku Co Ltd | Additive for metal cold rolling oil |
-
1987
- 1987-01-23 JP JP1387387A patent/JPS6339987A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6339987A (en) | 1988-02-20 |
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