JPH06322385A - Cold rolling oil - Google Patents
Cold rolling oilInfo
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- JPH06322385A JPH06322385A JP11278693A JP11278693A JPH06322385A JP H06322385 A JPH06322385 A JP H06322385A JP 11278693 A JP11278693 A JP 11278693A JP 11278693 A JP11278693 A JP 11278693A JP H06322385 A JPH06322385 A JP H06322385A
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Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は冷間圧延油に関する。This invention relates to cold rolling oils.
【0002】[0002]
【従来の技術】近年、冷間圧延機の高速化にともない良
好な潤滑性が要求される。特にティンゲージ(例えば0.
4mm以下)等の極薄鋼用冷間圧延は圧下率が大きく、
かつ生産性を高めるためには1500m/分以上の高速
での圧延をする必要があるため、冷間圧延油に良好な潤
滑性が要求される。このため、従来、圧延油ベースとし
ては牛脂等の比較的流動点の高い天然油脂が使用されて
きた。しかしながら、この様な冷間圧延油を使用した場
合には高い流動点のためにミルハウジング内の汚れがひ
どく、圧延鋼板表面上の品質欠陥が多発するとともに、
作業環境上も問題となってきた。一方、低流動点化する
ため、低流動点油脂を圧延油ベースに使用した場合には
熱酸化安定性が低い為、油焼けや脱脂不良が発生する。2. Description of the Related Art In recent years, good lubricity is required as the speed of cold rolling mills increases. Especially the tin gauge (eg.
4mm or less) cold rolling for ultra-thin steel has a large reduction ratio,
In addition, since it is necessary to roll at a high speed of 1500 m / min or more in order to improve productivity, the cold rolling oil is required to have good lubricity. Therefore, conventionally, natural fats and oils having a relatively high pour point, such as beef tallow, have been used as rolling oil bases. However, when such a cold rolling oil is used, the stain in the mill housing is severe due to the high pour point, and many quality defects occur on the surface of the rolled steel sheet,
The work environment has also become a problem. On the other hand, since a low pour point is used, when a low pour point oil or fat is used as a rolling oil base, the thermal oxidation stability is low, so that oil burning or poor degreasing occurs.
【0003】近年、上記のような天然油脂を用いた冷間
圧延油の問題点を改善する為、合成エステルを用いた冷
間圧延油の使用も試みられ既に一部では実用的に使用さ
れている。しかしながら、圧延条件がとりわけきびしい
ティンゲージ等の極薄鋼用冷間圧延に対する冷間圧延油
の合成エステル化は未だ実用化されていない。In recent years, in order to improve the problems of the cold rolling oil using the natural fat and oil as described above, it has been attempted to use the cold rolling oil using the synthetic ester, and some of them have already been practically used. There is. However, synthetic esterification of cold rolling oil for cold rolling for ultra-thin steel such as tin gauge, which has particularly severe rolling conditions, has not yet been put to practical use.
【0004】特公昭48−27867にネオペンチルポ
リオールと脂肪酸との部分エステルを用いる冷間圧延油
が開示されている。部分エステルを用いることにより炭
素数8〜10の飽和脂肪酸のエステルで極薄鋼用冷間圧
延に適した粘度でしかも低流動点の冷間圧延油を得るこ
とができるが、粘度指数が低い為、充分な圧延特性が得
られない。JP-B-48-27867 discloses a cold rolling oil using a partial ester of neopentyl polyol and fatty acid. By using a partial ester, a cold rolling oil having a viscosity suitable for cold rolling for ultra-thin steel and a low pour point can be obtained with an ester of a saturated fatty acid having 8 to 10 carbon atoms, but the viscosity index is low. However, sufficient rolling characteristics cannot be obtained.
【0005】特開昭55−145638号公報には多価
アルコールとジグリコール酸と一塩基酸との三成分から
合成されるコンプレックスエステルが開示されているが
粘度が高く粘度指数も低い為、加速時に油膜厚が過大と
なりスリップが生じやすくなると同時に高速圧延域で油
脂破断を生じ、ヒートスクラッチが発生しやすくなり極
薄鋼板用冷間圧延油には適さない。Japanese Unexamined Patent Publication (Kokai) No. 55-145638 discloses a complex ester synthesized from three components of a polyhydric alcohol, diglycolic acid and a monobasic acid, but it has a high viscosity and a low viscosity index, and therefore is accelerated. At times, the oil film thickness becomes excessively large and slippage is likely to occur, and at the same time, oil and fat breakage occurs in the high-speed rolling region, and heat scratches easily occur, which is not suitable for cold rolling oil for ultra-thin steel sheets.
【0006】[0006]
【発明が解決しようとする課題】本発明は冷間圧延油、
特にティンゲージ等の極薄鋼板の高速冷間圧延におい
て、チャタリングによる板厚変動、ヒートスクラッチに
よる表面欠陥、脱脂不良など次工程における問題、ミル
ハウジング内の汚れ及びこれに起因する押し込みきず等
の表面欠陥を生じることなく圧延できる冷間圧延油を提
供する。The present invention is a cold rolling oil,
Especially in the high-speed cold rolling of ultra-thin steel sheets such as tin gauge, fluctuations in the thickness due to chattering, surface defects due to heat scratches, problems in the next process such as poor degreasing, dirt in the mill housing and the surface of indentation flaws resulting from this. Provided is a cold rolling oil which can be rolled without causing defects.
【0007】[0007]
【課題を解決するための手段】本発明者らは以下に述べ
る混合脂肪酸のエステルを基油とする冷間圧延油がミル
ハウジングを清浄に保つ為に必要な低い流動点と極薄鋼
板用圧延油として要求される良好な脱脂性、高い粘度指
数、適当な粘度とを同時に満足することを見出し本発明
を完成した。DISCLOSURE OF THE INVENTION The present inventors have found that cold rolling oils based on mixed fatty acid esters described below as base oils have low pour points necessary for keeping the mill housing clean and rolling for ultra-thin steel sheets. The present invention has been completed by finding that they simultaneously satisfy good degreasing properties, a high viscosity index, and an appropriate viscosity required as an oil.
【0008】本発明は(a)ラウリン酸と(b)炭素数14〜
18のモノエンカルボン酸、または(a)、(b)および(c)
炭素数14〜18の直鎖飽和脂肪酸とで構成され、その
割合が以下の(i)又は(ii)で示される混合脂肪酸と多価
アルコールとのエステルを70重量%以上含有するブリ
キ用冷間圧延油に関する。 (i)aとbの重量比が1:0.12〜1.5で全混合脂肪酸中
に占めるcの重量%が0〜25である混合脂肪酸 (ii)aとbの重量比が1:1.5〜4.0で全混合脂肪酸中
に占めるcの重量%(x)が以下の不等式の範囲内にある混
合脂肪酸。The present invention comprises (a) lauric acid and (b) 14 to 14 carbon atoms.
18 monoenecarboxylic acids, or (a), (b) and (c)
Cold tinplate comprising 70% by weight or more of an ester of a mixed fatty acid represented by the following (i) or (ii) and a polyhydric alcohol, which is composed of a linear saturated fatty acid having 14 to 18 carbon atoms. Regarding rolling oil. (i) The weight ratio of a and b is 1: 0.12 to 1.5, and the weight ratio of c in the total mixed fatty acid is 0 to 25. (ii) The weight ratio of a and b is 1: A mixed fatty acid in which the weight% (x) of c in the total mixed fatty acid in the range of 1.5 to 4.0 is within the range of the following inequality.
【0009】[0009]
【数2】 [Equation 2]
【0010】本発明圧延油の基油として用いられるエス
テルは上記脂肪酸と多価アルコール、特にトリメチロー
ルプロパンとの完全エステルである。多価アルコール成
分の少なくとも80重量%以上、より好ましくは90重
量%以上がトリメチロールプロパンである。エステル分
子内に1個以上の水酸基を有する部分エステルでは粘度
指数が低く、また粘度も高いためブリキ鋼板等の極薄鋼
板用冷間圧延油の基油としては適当でない。ネオペンチ
ルグリコール等のジオールのエステルでは粘度が低く高
温時に十分な油膜を確保できない。又グリセリン、ジグ
リセリン等のポリグリセリン、ペンタエリスリトール、
ジペンタエリスリトールのエステルではトリメチロール
プロパンのエステルに比べ流動点が高く、ミルハウジン
グを清浄に維持するための圧延油の流動点条件と圧延後
の脱脂性条件を同時に満たすことができない。しかしな
がらトリメチロールプロパン以外の上記多価アルコール
類のエステルを一部混合して用いてもよい。その場合
も、多量に混合すると本発明の効果が損われるので、全
エステルの20重量%以下とすべきである。The ester used as the base oil of the rolling oil of the present invention is a complete ester of the above fatty acid and a polyhydric alcohol, particularly trimethylolpropane. At least 80% by weight, more preferably 90% by weight or more of the polyhydric alcohol component is trimethylolpropane. A partial ester having one or more hydroxyl groups in the ester molecule has a low viscosity index and a high viscosity, and is not suitable as a base oil for cold rolling oil for ultra-thin steel sheets such as tin steel sheet. Esters of diols such as neopentyl glycol have low viscosity and cannot secure a sufficient oil film at high temperatures. Also, polyglycerin such as glycerin and diglycerin, pentaerythritol,
The ester of dipentaerythritol has a higher pour point than the ester of trimethylol propane, and it is not possible to simultaneously satisfy the pour point condition of rolling oil for keeping the mill housing clean and the degreasing condition after rolling. However, the esters of the above polyhydric alcohols other than trimethylolpropane may be partially mixed and used. Also in this case, the effect of the present invention is impaired if a large amount is mixed, so the content should be 20% by weight or less based on the total ester.
【0011】エステルを構成する脂肪酸はラウリン酸、
炭素数14〜18のモノエンカルボン酸例えばミリスト
レイン酸、パルミトレイン酸、オレイン酸等と炭素数1
4〜18の直鎖飽和脂肪酸、例えばミリスチン酸、パル
ミチン酸、ステアリン酸等の混合脂肪酸であるがその割
合は以下の(i)又は(ii)の範囲内でなければならない。 (i)ラウリン酸と炭素数14〜18のモノエンカルボン
酸の重量比が1:0.12〜1.5で炭素数14〜18の
直鎖飽和脂肪酸の全脂肪酸に占める重量%が0〜25で
ある混合脂肪酸。The fatty acids constituting the ester are lauric acid,
A monoenecarboxylic acid having 14 to 18 carbon atoms such as myristoleic acid, palmitoleic acid, oleic acid and the like and 1 carbon atom
4-18 linear saturated fatty acids, for example, mixed fatty acids such as myristic acid, palmitic acid, stearic acid, etc., but the ratio must be within the following range (i) or (ii). (i) The weight ratio of lauric acid to the monoenecarboxylic acid having 14 to 18 carbon atoms is 1: 0.12 to 1.5, and the straight chain saturated fatty acid having 14 to 18 carbon atoms accounts for 0 to 25% by weight of the total fatty acids. Is a mixed fatty acid.
【0012】ラウリン酸に対する炭素数14〜18のモ
ノエンカルボン酸の重量比が0.12以下では流動点が
0℃を越える。ミル清浄性を維持するには流動点は低け
れば低いほどよいが最もミル雰囲気温度が低い冬季を考
慮すると流動点は0℃以下である必要がある。又、炭素
数14〜18のモノエンカルボン酸の重量比が1.5以
上では直鎖飽和脂肪酸量によっては実施例で述べる脱脂
方法で脱脂率90%以上を確保することが出来ない。When the weight ratio of the monoenecarboxylic acid having 14 to 18 carbon atoms to lauric acid is 0.12 or less, the pour point exceeds 0 ° C. A lower pour point is better for maintaining mill cleanliness, but the pour point needs to be 0 ° C. or lower in consideration of the winter season when the mill atmosphere temperature is the lowest. Further, if the weight ratio of the monoenecarboxylic acid having 14 to 18 carbon atoms is 1.5 or more, the degreasing rate of 90% or more cannot be secured by the degreasing method described in the examples depending on the amount of the linear saturated fatty acid.
【0013】直鎖飽和脂肪酸量の全脂肪酸に占める重量
%が25を越えると流動点は0℃を越え、適当でない。 (ii)ラウリン酸と炭素数14〜18のモノエンカルボン
酸の重量比が1:1.5〜4.0で全脂肪酸中に占める炭
素数14〜18の直鎖飽和脂肪酸の重量%(x)が以下の
不等式の範囲内にある混合脂肪酸。If the weight percentage of the straight chain saturated fatty acid in the total fatty acids exceeds 25, the pour point exceeds 0 ° C., which is not suitable. (ii) The weight ratio of lauric acid to the monoenecarboxylic acid having 14 to 18 carbon atoms is 1: 1.5 to 4.0, and the weight% of the linear saturated fatty acid having 14 to 18 carbon atoms in the total fatty acid (x) A mixed fatty acid wherein is within the following inequality:
【0014】[0014]
【数3】 ラウリン酸に対する炭素数14〜18のモノカルボン酸
の重量比が4.0を越えると炭素数14〜18の直鎖飽
和脂肪酸量にかかわらず流動点を脱脂性との両方の条件
を同時に満足することができない。[Equation 3] When the weight ratio of the monocarboxylic acid having 14 to 18 carbon atoms to lauric acid exceeds 4.0, both the conditions of pour point and degreasing property are simultaneously satisfied regardless of the amount of the linear saturated fatty acid having 14 to 18 carbon atoms. I can't.
【0015】又、全脂肪酸に占める炭素数14〜18の
直鎖飽和脂肪酸量が(0.4−0.6/y)×100重量%
以下の場合には脱脂率90%以上を確保することができ
ず、25重量%以上では流動点を0℃以下にすることが
できない。The amount of linear saturated fatty acids having 14 to 18 carbon atoms in the total fatty acids is (0.4-0.6 / y) × 100% by weight.
In the following cases, the degreasing rate of 90% or more cannot be secured, and in the case of 25% by weight or more, the pour point cannot be 0 ° C. or less.
【0016】ラウリン酸の代わりに炭素数8〜10の直
鎖飽和脂肪酸たとえばカプリン酸、カプリル酸、ペラル
ゴン酸を用いた場合臭気が強くなり好ましくない。ラウ
リン酸に混入する場合でも10重量%以下、望ましくは
5重量%以下でなければならない。When a straight chain saturated fatty acid having 8 to 10 carbon atoms such as capric acid, caprylic acid, or pelargonic acid is used instead of lauric acid, the odor becomes strong, which is not preferable. Even when mixed with lauric acid, it should be 10% by weight or less, preferably 5% by weight or less.
【0017】リノール酸等のジエンカルボン酸、リノレ
ン酸等のトリエンカルボン酸は脱脂性を著しく低下させ
るのでモノエンカルボン酸に混入する場合でもジエンカ
ルボン酸は10重量%以下望ましくは5重量%以下、ト
リエンカルボン酸は可及的少ない方がよい。Since diene carboxylic acids such as linoleic acid and triene carboxylic acids such as linolenic acid remarkably deteriorate the degreasing property, the diene carboxylic acid is contained in the monoene carboxylic acid in an amount of 10% by weight or less, preferably 5% by weight or less. It is better to use as little carboxylic acid as possible.
【0018】分岐脂肪酸たとえばイソステアリン酸はモ
ノエンカルボン酸と同様に流動点を下げる効果を持つが
粘度指数を低下させるので好ましくない。モノエンカル
ボン酸と混合使用する場合でも10重量%以下、好まし
くは5重量%以下にする。Branched fatty acids such as isostearic acid have the same effect of lowering the pour point as monoenecarboxylic acid, but are not preferred because they lower the viscosity index. Even when used in combination with a monoenecarboxylic acid, the amount is 10% by weight or less, preferably 5% by weight or less.
【0019】本発明に用いられるエステルは実質上、完
全なエステルである。多価アルコールとしてトリメチロ
ールプロパンを用いるときの混合脂肪酸とのモル比は
1:2.6〜3.0が好ましい混合脂肪酸の比率が2.6以
下の場合には粘度指数が低下する。The ester used in the present invention is essentially a complete ester. When trimethylolpropane is used as the polyhydric alcohol, the molar ratio with the mixed fatty acid is preferably 1: 2.6 to 3.0. When the ratio of the mixed fatty acid is 2.6 or less, the viscosity index decreases.
【0020】本発明圧延油には上記エステルを2種以上
混合して使用することもできる。本発明に用いられるダ
イマー酸はオレイン酸の2量体等の炭素数21〜36の
二塩基酸で圧延油に対し1〜3重量%添加される。ダイ
マー酸の添加量が1重量%未満では高速圧延時のヒート
スクラッチの発生を防止することができず、3重量%以
上ではワークロールの摩耗が問題となる。The rolling oil of the present invention may be used as a mixture of two or more kinds of the above esters. The dimer acid used in the present invention is a dibasic acid having 21 to 36 carbon atoms, such as a dimer of oleic acid, and is added in an amount of 1 to 3% by weight based on the rolling oil. If the amount of dimer acid added is less than 1% by weight, heat scratches cannot be prevented during high-speed rolling, and if it is 3% by weight or more, wear of work rolls becomes a problem.
【0021】本発明圧延油に添加してもよい他の成分と
しては脂肪酸、極圧添加剤特にリン酸エステル系、乳化
剤、酸化防止剤等が例示される。本発明圧延油は水で
0.5〜20体積%に稀釈して用いる。Examples of other components which may be added to the rolling oil of the present invention include fatty acids, extreme pressure additives, particularly phosphate ester type, emulsifiers, antioxidants and the like. The rolling oil of the present invention is used by diluting it with water to 0.5 to 20% by volume.
【0022】以下実施例および比較例をあげて本発明を
説明する。The present invention will be described below with reference to examples and comparative examples.
実施例1 表1に本発明の圧延油に使用される合成エステルの脂肪
酸およびアルコールの仕込比とその合成エステルを用
い、下記の圧延油処方に基づいて作成した圧延油の物性
値を示す。Example 1 Table 1 shows the charging ratio of the fatty acid and alcohol of the synthetic ester used in the rolling oil of the present invention and the physical properties of the rolling oil prepared based on the following rolling oil formulation using the synthetic ester.
【0023】実施例No.1に用いたトリメチロールプロ
パン混合脂肪酸エステル、トリメチロールプロパン1
5.86重量部、炭素数14〜18のモノエンカルボン
酸48.80重量部、炭素数14〜18の直鎖飽和脂肪
酸11.78重量部を窒素気流下に260℃で8時間反
応させ得られた酸価5のエステル。実施例No.2〜No.
7、比較例No.9〜No.17のエステルも同様の方法で
得られた。Trimethylolpropane 1 as a mixed fatty acid ester of trimethylolpropane used in Example No. 1
5.86 parts by weight, 48.80 parts by weight of monoenecarboxylic acid having 14 to 18 carbon atoms, and 11.78 parts by weight of linear saturated fatty acid having 14 to 18 carbon atoms were obtained by reacting at 260 ° C. for 8 hours under a nitrogen stream. Acid number 5 ester. Examples No. 2 to No.
7 and the esters of Comparative Examples No. 9 to No. 17 were obtained in the same manner.
【0024】[0024]
【表1】 [Table 1]
【0025】 圧延油処方 合成エステル 88.9(%) 混合脂肪酸 3.0 ダイマー酸 2.0 有機酸性リン酸エステル芳香族アミン塩 2.0 非イオン界面活性剤 2.9 アミン系酸化防止剤 1.0 防ばい剤 0.2Rolling oil formulation Synthetic ester 88.9 (%) Mixed fatty acid 3.0 Dimer acid 2.0 Organic acid phosphoric acid ester Aromatic amine salt 2.0 Nonionic surfactant 2.9 Amine antioxidant 1 0.0 Anti-bacterial agent 0.2
【0026】実施例2 表1の圧延油について以下の条件で脱脂試験を行なっ
た。 脱脂条件 供試鋼板:ワークロール径100mmロール周速12mpmの
圧延機を用い、板厚0.8mmのSPCC冷間鋼板を各圧
延油の4%エマルションをスプレーしながら、圧下率2
0%で圧延する。さらにこの鋼板を積み重ね、130℃
の恒温槽で12時間設置した。 電解液 :2%水酸化ナトリウム水溶液に電解脱脂用添
加剤フォーミュラ613H−X0.3%添加した。 温 度 :80℃ 電流密度:10A/dm2 電解時間:3秒 試験結果を表2に示す。Example 2 A degreasing test was conducted on the rolling oils in Table 1 under the following conditions. Degreasing conditions Test steel sheet: Using a rolling machine with a work roll diameter of 100 mm and a roll peripheral speed of 12 mpm, a SPCC cold steel sheet with a plate thickness of 0.8 mm was sprayed with a 4% emulsion of each rolling oil, and the rolling reduction was 2
Roll at 0%. Further stacking this steel plate, 130 ℃
It was installed in a constant temperature bath for 12 hours. Electrolytic solution: An electrolytic degreasing additive formula 613H-X 0.3% was added to a 2% aqueous sodium hydroxide solution. Temperature: 80 ° C. Current density: 10 A / dm 2 Electrolysis time: 3 seconds The test results are shown in Table 2.
【0027】[0027]
【表2】 [Table 2]
【0028】実施例3 表1の本発明品No.2および比較品No.8、No.12を
下記の条件でブリキ原板のタンデム高速圧延に供した。 圧延機 :リサーキューレーションクーラントシ
ステムを有する5スタンドタンデム圧延機 圧延速度 :2100mpm Max ワークロール径:576mm(1〜4スタンド) 425mm(5スタンド) 圧延鋼柱 :C:0.03〜0.06%,Si:0〜0.
03% Mn:0.2〜0.3%,P:0〜0.015% S:0.01〜0.025%,N:0.0025〜0.006
% Sol−Al:0.02〜0.06%,Cr:0〜0.06% 原板板厚 :2mm 仕上板厚 :0.2mm 圧下率 : 1 → 2 → 3 → 4 → 5 37.3% 42.6% 38.6% 33.6% 32.0% 圧延油濃度 :4% 圧延油温度 :60℃Example 3 Inventive product No. 2 and comparative products No. 8 and No. 12 in Table 1 were subjected to tandem high speed rolling of tin plate under the following conditions. Rolling mill: 5 stand tandem rolling mill with recirculation coolant system Rolling speed: 2100 mpm Max Work roll diameter: 576 mm (1 to 4 stands) 425 mm (5 stands) Rolled steel column: C: 0.03 to 0.06% , Si: 0 to 0.
03% Mn: 0.2 to 0.3%, P: 0 to 0.015% S: 0.01 to 0.025%, N: 0.0025 to 0.006
% Sol-Al: 0.02 to 0.06%, Cr: 0 to 0.06% Original plate thickness: 2 mm Finished plate thickness: 0.2 mm Reduction ratio: 1 → 2 → 3 → 4 → 5 37.3% 42.6% 38.6% 33.6% 32.0% Rolling oil concentration: 4% Rolling oil temperature: 60 ° C
【0029】[0029]
【表3】 [Table 3]
【0030】[0030]
【発明の効果】本発明圧延油剤を用いることにより、チ
ャタリングによる板厚変動やヒートスクラッチによる表
面欠陥のない極薄鋼板、特にブリキ板として優れた品質
の鋼板を得ることができる。その際ハウジングへの汚れ
付着、脱脂不良が著るしく軽減される。EFFECTS OF THE INVENTION By using the rolling oil of the present invention, it is possible to obtain an ultra-thin steel sheet free from fluctuations in sheet thickness due to chattering and surface defects due to heat scratch, particularly a steel sheet having excellent quality as a tin plate. At that time, the adhesion of dirt to the housing and the poor degreasing are significantly reduced.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 守田 義之 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 徳永 宗康 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 池田 俊和 大阪府八尾市渋川町二丁目1番3号 日本 クエーカー・ケミカル株式会社内 (72)発明者 林 弘 大阪府八尾市渋川町二丁目1番3号 日本 クエーカー・ケミカル株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshiyuki Morita 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Inside Nihon Kokan Co., Ltd. (72) In-house 1-2-1 Marunouchi, Chiyoda-ku, Tokyo Nippon Steel Tube Co., Ltd. (72) Inventor Toshikazu Ikeda 2-3 1-3 Shibukawa-cho, Yao-shi, Osaka Japan Quaker Chemical Co., Ltd. (72) Hiroshi Hayashi 2-3 1-3 Shibukawa-cho, Yao-shi, Osaka No. Japan Quaker Chemical Co., Ltd.
Claims (7)
モノエンカルボン酸、または(a)、(b)および(c)炭素数
14〜18の直鎖飽和脂肪酸とで構成され、その割合が
以下の(i)又は(ii)で示される混合脂肪酸と多価アルコ
ールとのトリエステルを70重量%以上含有する冷間圧
延油。 (i)aとbの重量比が1:0.12〜1.5で全混合脂肪酸中
に占めるcの重量%が0〜25である混合脂肪酸 (ii)aとbの重量比が1:1.5〜4.0で全混合脂肪酸中
に占めるcの重量%(x)が以下の不等式の範囲内にある混
合脂肪酸。 【数1】 1. A composition comprising (a) lauric acid and (b) a monoenecarboxylic acid having 14 to 18 carbon atoms, or (a), (b) and (c) a linear saturated fatty acid having 14 to 18 carbon atoms. A cold rolling oil containing at least 70% by weight of a triester of a mixed fatty acid and a polyhydric alcohol represented by the following (i) or (ii). (i) The weight ratio of a and b is 1: 0.12 to 1.5, and the weight ratio of c in the total mixed fatty acid is 0 to 25. (ii) The weight ratio of a and b is 1: A mixed fatty acid in which the weight% (x) of c in the total mixed fatty acid in the range of 1.5 to 4.0 is within the range of the following inequality. [Equation 1]
ンである請求項1の冷間圧延油。2. The cold rolling oil according to claim 1, wherein the polyhydric alcohol is trimethylolpropane.
〜10の直鎖飽和脂肪酸に置き換えられた請求項1の冷
間圧延油。3. 10% by weight or less of lauric acid has 8 carbon atoms
The cold rolling oil according to claim 1, which is substituted with a linear saturated fatty acid of 10 to 10.
の10重量%以下が炭素数16〜18のジエンカルボン
酸に置き換えられた請求項1の冷間圧延油。4. The cold rolling oil according to claim 1, wherein 10% by weight or less of the monoenecarboxylic acid having 14 to 18 carbon atoms is replaced with a dienecarboxylic acid having 16 to 18 carbon atoms.
の10重量%以下がイソステアリン酸に置き換えられた
請求項1の冷間圧延油。5. The cold rolling oil according to claim 1, wherein 10% by weight or less of the monoenecarboxylic acid having 14 to 18 carbon atoms is replaced with isostearic acid.
のモル比が1:2.6〜3.0である請求項2の冷間圧延
油。6. The cold rolling oil according to claim 2, wherein the molar ratio of trimethylolpropane to the mixed fatty acid is 1: 2.6 to 3.0.
求項1の冷間圧延油。7. The cold rolling oil according to claim 1, which contains 1 to 3% by weight of dimer acid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11278693A JPH06322385A (en) | 1993-05-14 | 1993-05-14 | Cold rolling oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11278693A JPH06322385A (en) | 1993-05-14 | 1993-05-14 | Cold rolling oil |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06322385A true JPH06322385A (en) | 1994-11-22 |
Family
ID=14595480
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11278693A Pending JPH06322385A (en) | 1993-05-14 | 1993-05-14 | Cold rolling oil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06322385A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09249889A (en) * | 1996-03-18 | 1997-09-22 | Nippon Quaker Chem Kk | Lubricating oil |
-
1993
- 1993-05-14 JP JP11278693A patent/JPH06322385A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09249889A (en) * | 1996-03-18 | 1997-09-22 | Nippon Quaker Chem Kk | Lubricating oil |
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