Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH068429B2 - Metal working oil - Google Patents
[go: Go Back, main page]

JPH068429B2 - Metal working oil - Google Patents

Metal working oil

Info

Publication number
JPH068429B2
JPH068429B2 JP25562485A JP25562485A JPH068429B2 JP H068429 B2 JPH068429 B2 JP H068429B2 JP 25562485 A JP25562485 A JP 25562485A JP 25562485 A JP25562485 A JP 25562485A JP H068429 B2 JPH068429 B2 JP H068429B2
Authority
JP
Japan
Prior art keywords
oil
polymerized
fish
oils
odor
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
JP25562485A
Other languages
Japanese (ja)
Other versions
JPS62115092A (en
Inventor
次男 沖田
昭男 中島
誠 高井
幸夫 橋口
誠二郎 宮越
昭治 荻原
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 JP25562485A priority Critical patent/JPH068429B2/en
Publication of JPS62115092A publication Critical patent/JPS62115092A/en
Publication of JPH068429B2 publication Critical patent/JPH068429B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Lubricants (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は金属加工油に関するものであり、さらに詳しく
は、水素添加魚油を重合した重合油を用いて潤滑性に優
れ、経時安定性並びに魚臭を改良した金属加工油に関す
るものである。
TECHNICAL FIELD The present invention relates to a metalworking oil, and more specifically, it uses a polymerized oil obtained by polymerizing hydrogenated fish oil and has excellent lubricity, stability over time, and fish stability. The present invention relates to a metal working oil having an improved odor.

〔従来の技術〕[Conventional technology]

従来、切削油、研削油、圧延油、プレス油、引抜油など
の金属加工油は、基油に鉱物油またはパーム油、牛脂、
豚脂等の動植物油脂あるいは脂肪酸エステルが用いられ
ている。しかし、これらの基油は金属加工技術の進展に
伴う性能を、十分満足するものでなくなり、その性能を
おぎなうために、油性向上剤、界面活性剤、錆止め剤、
極圧添加剤、消泡剤などさらに多くの添加剤を配合し用
いている。
Conventionally, metalworking oils such as cutting oils, grinding oils, rolling oils, press oils, and drawing oils are used as base oils for mineral oil or palm oil, beef tallow,
Animal and vegetable oils and fats such as lard and fatty acid esters are used. However, these base oils no longer fully satisfy the performance with the progress of metalworking technology, and in order to cover the performance, an oiliness improver, a surfactant, a rust inhibitor,
More additives such as extreme pressure additives and defoamers are blended and used.

添加剤によらずに基油の潤滑性等を改良する試みとして
は、活性白土の存在下に加熱処理した変性油脂を用いる
鋼板用冷間圧延油(特公昭51−6686)、不飽和脂肪酸を
含有するトリグリセライドを部分水素添加した油脂を用
いる冷間圧延油(特開昭60-81295)等が報告されてい
る。
As an attempt to improve the lubricity of the base oil without using additives, cold rolling oil for steel sheets (Japanese Patent Publication No. 51-6686) using modified fats and oils heat-treated in the presence of activated clay, unsaturated fatty acids were used. A cold rolling oil (Japanese Unexamined Patent Publication No. 60-81295), which uses an oil and fat containing partially hydrogenated triglyceride, has been reported.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

一方、魚油は常温で液体であり他の添加剤と配合し易
く、また安価であり、基油として多角的に利用できる可
能性を示唆している。
On the other hand, fish oil is a liquid at room temperature, is easy to mix with other additives, is inexpensive, and suggests that it can be used as a base oil in various ways.

例えば魚油は重合して潤滑油の分野にも利用された歴史
はある。しかし、魚油が唯一の国産油脂でありながら、
近年その使用量は少なくなっている。これは魚油が他の
動植物油脂と異って、魚臭が激しく、完全な脱臭がむず
かしく、また脱臭しても時間が経つと臭いが戻り、さら
に他の油脂には含まれない高度不飽和酸を多量に含んで
いるために、熱に不安定であることなど、技術的に解決
しなければならないことが多く残っているためである。
For example, fish oil has a history of being polymerized and used in the field of lubricating oil. However, while fish oil is the only domestic fat,
In recent years, the amount used has decreased. Unlike other animal and vegetable oils and fats, fish oil has a strong fish odor, complete deodorization is difficult, and even after deodorization, the odor returns with time, and highly unsaturated acids not contained in other oils and fats. This is because there are many technical problems to be solved, such as being unstable to heat because it contains a large amount of.

即ち、魚油を従来の技術に従って他の動植物油脂と同様
に利用することは困難である。
That is, it is difficult to use fish oil in the same manner as other animal and vegetable oils and fats according to the conventional technique.

例えば、魚油を加熱処理して得られる魚油の重合油は潤
滑性が向上するものの魚臭が激しく実用上使用できな
い。脱臭精製した魚油の重合油は時間が経つと魚臭が発
生し、あるいは着色して経時安定性が悪い。
For example, a polymerized oil of fish oil obtained by heat-treating fish oil has improved lubricity, but has a strong fish odor and cannot be practically used. The polymerized oil of deodorized and refined fish oil has a fishy odor over time, or is colored and has poor stability over time.

また、水素添加する方法では、水素添加の度合が高くな
ると融点が上昇して取扱上溶解したりしなければならず
用途が限られ、また鉱油等との相溶性が悪くなり、魚油
を部分的に水素添加したものでは臭気および潤滑性が不
充分であるのみでなく、曇点が高くなり、例えば鉱物油
と配合した場合10〜20℃位で白濁するなど特に低温度領
域での製品安定性に欠ける等の問題点がある。
In addition, in the method of hydrogenation, when the degree of hydrogenation increases, the melting point rises and must be dissolved during handling, which limits its use and compatibilities with mineral oil, etc. Not only is odor and lubricity insufficient with hydrogenated products, but the cloud point also becomes high.For example, when compounded with mineral oil, it becomes cloudy at around 10 to 20 ° C. Product stability especially in low temperature regions There are problems such as lack of.

本発明は上記の点に着目しなされたもので、潤滑性に優
れ、経時安定性並びに魚臭を改良した金属加工油を提供
することを目的とする。
The present invention has been made in view of the above points, and an object thereof is to provide a metalworking oil having excellent lubricity, stability over time, and improved fish odor.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは上記課題を解決するため鋭意研究を行なっ
た結果、水素添加魚油の重合油を用いることにより、潤
滑性に優れ、経時安定性並びに魚臭を改良した金属加工
油が得られることを見出し本発明に至った。
As a result of intensive studies to solve the above problems, the present inventors have found that by using a polymerized oil of hydrogenated fish oil, it is possible to obtain a metalworking oil having excellent lubricity, stability over time and fish odor. This led to the present invention.

即ち、本発明は沃素価60〜110の水素添加魚油を、加熱
または酸化により重合して得られる38℃で80〜3000セン
チポイズの粘度を有する重合油を含有するところの金属
加工油である。
That is, the present invention is a metalworking oil containing a polymerized oil having a viscosity of 80 to 3000 centipoise at 38 ° C. obtained by polymerizing hydrogenated fish oil having an iodine value of 60 to 110 by heating or oxidation.

本発明の重合油は魚油を沃素価60〜110に水素添加した
後、加熱または酸化により38℃で80〜3000センチポイズ
の粘度になるよう重合して得られる。
The polymerized oil of the present invention is obtained by hydrogenating fish oil to an iodine value of 60 to 110, and then polymerizing it by heating or oxidation so as to have a viscosity of 80 to 3000 centipoise at 38 ° C.

本発明に用いる魚油としては、例えばイワシ油、タラ
油、イカ油、ニシン油、アイザメ肝油、アブラザメ肝
油、サバ油及びこれらの魚油を混合して得られる混合魚
油等が挙げられる。また精製の如何によらず用いられる
が好ましくは常法により、苛性ソーダ水溶液で脱酸後水
洗し、活性白土、活性炭で脱色し精製した魚油が良い。
水素添加反応は通常の水添条件及び触媒が使用されて行
なわれる。例えば、ニッケル系触媒を対油脂の0.2〜
1.0重量%用い、水素圧1.0〜4.0kg/cm2
て、温度160〜200℃で水素添加反応を行ない、IV60〜11
0に水素添加した魚油を水素添加魚油として用いる。水
素添加魚油のIVが60以下では重合反応が進みにくく、水
素添加魚油の融点が高く得られる重合油が、特に低温に
おける鉱物油との相溶性が悪いものとなり、また潤滑性
も十分でない。IVが110以上では、得られる重合油に魚
臭が残るとともに時間が経つと臭気が強くなり、特に高
温度下での使用に問題が生じる。
Examples of the fish oil used in the present invention include sardine oil, cod oil, squid oil, herring oil, shark liver oil, blister shark oil, mackerel oil, and mixed fish oil obtained by mixing these fish oils. Although it may be used regardless of purification, it is preferable to use fish oil which is deoxidized with an aqueous solution of caustic soda and washed with water, decolorized with activated clay and activated carbon and purified by a conventional method.
The hydrogenation reaction is carried out using conventional hydrogenation conditions and catalysts. For example, a nickel-based catalyst is used in an amount of 0.2 to
1.0% by weight is used, hydrogenation reaction is carried out at a hydrogen pressure of 1.0 to 4.0 kg / cm 2 at a temperature of 160 to 200 ° C., IV60 to 11
Fish oil hydrogenated to 0 is used as hydrogenated fish oil. When the IV of hydrogenated fish oil is 60 or less, the polymerization reaction is difficult to proceed, and the polymerized oil obtained with a high melting point of hydrogenated fish oil has poor compatibility with mineral oil, especially at low temperatures, and its lubricity is also insufficient. When the IV is 110 or more, a fishy odor remains in the obtained polymerized oil, and the odor becomes strong over time, which causes a problem particularly when used at high temperatures.

本発明に用いる水素添加魚油を重合した重合油(以下
「重合油」と称する)の製造方法は加熱による方法また
は酸化による方法があり、38℃における粘度が80〜3000
センチポイズ(以下「CP」と記す)の範囲になるよう重
合反応を行なう。例えば加熱による方法では、窒素ガス
または二酸化炭素ガス等の不活性ガス雰囲気中で水素添
加魚油を280〜320℃に加熱し、同温度で2〜30時間撹拌
することにより重合することができる。また酸化による
方法では水素添加魚油を120〜200℃に加熱し、酸素また
は空気を導入しながら同温度で2〜30時間撹拌すること
により反応を行なうことができる。
The method for producing a polymerized oil obtained by polymerizing hydrogenated fish oil used in the present invention (hereinafter referred to as “polymerized oil”) includes a method by heating or a method by oxidation, and the viscosity at 38 ° C. is 80 to 3000.
Polymerization reaction is performed within the range of centipoise (hereinafter referred to as “CP”). For example, in the method by heating, hydrogenated fish oil can be polymerized by heating the hydrogenated fish oil to 280 to 320 ° C. in an inert gas atmosphere such as nitrogen gas or carbon dioxide gas and stirring at the same temperature for 2 to 30 hours. In the oxidation method, the reaction can be carried out by heating hydrogenated fish oil to 120 to 200 ° C and stirring at the same temperature for 2 to 30 hours while introducing oxygen or air.

ここで本願の重合油は38℃に於ける粘度が80〜3000CPの
範囲のものが魚臭、潤滑性、低温での鉱物油との相溶性
などの点で好ましく、粘度80以下では重合油に魚臭が若
干残り、さらに経日により残り臭を発生すること、低温
での鉱物油との相溶性が十分でないこと、近年の高速度
加工に対しての潤滑性が十分でない等の欠点がある。又
粘度が3000CP以上になると重合油の油性、溶解性の低
下、並びに炭化物の生成等が見られるようになり潤滑性
が低下し、また鉱物油との相溶性が低下する等から好ま
しくない。
Here, the polymerized oil of the present application preferably has a viscosity in the range of 80 to 3000 CP at 38 ° C. in terms of fish odor, lubricity, compatibility with mineral oil at low temperature, etc. It has some drawbacks such as a slight fishy odor, a residual odor over time, insufficient compatibility with mineral oil at low temperatures, and insufficient lubricity for recent high speed processing. . Further, when the viscosity is 3000 CP or more, the oiliness and solubility of the polymerized oil are reduced, and the formation of carbides and the like are observed, the lubricity is reduced, and the compatibility with mineral oil is reduced, which is not preferable.

本発明の重合油はそのまま、またはそれを基油としそれ
に他の添加剤、油性向上剤を加えて用いることができ、
また油性向上剤としての他の動植物油、エステル類、合
成油及び鉱物油と混合して使用することもできる。さら
に本発明の金属加工油は公知の潤滑油添加剤、例えば極
圧添加剤、酸化防止剤、消泡剤、防錆剤、界面活性剤等
をその目的に応じて添加することができる。
The polymerized oil of the present invention can be used as it is, or can be used by adding it to other additives and an oiliness improver using it as a base oil,
It can also be used as a mixture with other animal and vegetable oils, esters, synthetic oils and mineral oils as oiliness improvers. Further, the metalworking oil of the present invention may be added with known lubricating oil additives such as extreme pressure additives, antioxidants, antifoaming agents, rust preventives, surfactants and the like depending on the purpose.

以下実施例により本発明を詳細に説明するが、本発明の
範囲はこれらに限定されるものではない。
Hereinafter, the present invention will be described in detail with reference to Examples, but the scope of the present invention is not limited thereto.

〔実施例〕〔Example〕

実施例1 常法に従い脱酸、脱色した精製魚油(主にタラ油を含む
混合魚油、IV 175)1000gをステンレス製2のオート
クレーブに仕込みNi系触媒0.4Wt%、水素圧1.5kg
/cm2、反応温度160±2℃で水素添加反応を行ない、IV
60の水素添加魚油980gを得た。
Example 1 1000 g of purified fish oil (mixed fish oil mainly containing cod oil, IV 175) deoxidized and decolorized according to a conventional method was charged into an autoclave 2 made of stainless steel, a Ni-based catalyst was 0.4 Wt%, and a hydrogen pressure was 1.5 kg.
/ Cm 2 , hydrogenation reaction at reaction temperature 160 ± 2 ℃, IV
980 g of 60 hydrogenated fish oil was obtained.

この水素添加魚油900gをステンレス製2の反応釜に仕
込み、窒素ガスを吹き込みながら撹拌し、1.5時間で
280℃まで昇温し、さらに同温度で7時間反応して粘度1
000CPの重合油800gを得た。
900 g of this hydrogenated fish oil was charged into a stainless steel 2 reaction kettle and stirred while blowing nitrogen gas.
Raise the temperature to 280 ℃ and react at the same temperature for 7 hours to obtain a viscosity of 1
800 g of polymerized oil of 000 CP was obtained.

得られた重合油の臭気(重合油製造後および25℃で30日
経過後)、焼付荷重(30wt%スピンドル油溶液)、鉱油
との相溶性を測定し、その結果を表−1のNo.2に示
す。
The odor of the polymerized oil obtained (after polymerized oil production and after 30 days at 25 ° C), baking load (30 wt% spindle oil solution), and compatibility with mineral oil were measured, and the results are shown in Table-1 No. 2 Shown in.

上記で用いた精製魚油(IV 175)を上記と同様に水素添
加し各々IVが50、70、80、90、100、110、120である水
素添加魚油を得、これを窒素ガス導入下に加熱重合して
粘度約1000CPの重合油を得た。得られた重合油の臭気、
焼付荷重、鉱油との相溶性を測定し、その結果を表−1
のNo.1およびNo.3〜8に示す。
The purified fish oil (IV 175) used above was hydrogenated in the same manner as above to obtain hydrogenated fish oil with IV of 50, 70, 80, 90, 100, 110 and 120, respectively, and heating it under nitrogen gas introduction. Polymerization gave a polymerized oil having a viscosity of about 1000 CP. Odor of the obtained polymerized oil,
The baking load and the compatibility with mineral oil were measured, and the results are shown in Table-1.
No. 1 and Nos. 3-8.

表−1のうち、IV50の水素添加魚油から得られた重合油
は鉱油との相溶性が悪く、またIV 110の水素添加魚油か
ら得られた重合油は臭気が悪く、それぞれ本発明の範囲
外である。
In Table 1, the polymerized oil obtained from the hydrogenated fish oil of IV50 has poor compatibility with mineral oil, and the polymerized oil obtained from the hydrogenated fish oil of IV110 has a bad odor. Is.

試験法 粘度:38℃の粘度をB型粘度計で測定した。 Test method Viscosity: The viscosity at 38 ° C. was measured with a B-type viscometer.

焼付荷重:シェル型高速四球摩擦試験機 ボール 1/2インチ 測定温度 70℃ 立軸回転数 800 rpm 試 料 重合油:60スピンドル油 (wt比30:70)の混合油 鉱油との相溶性:重合油を60スピンドル油に溶解し、30
wt%溶液を作り、それを0℃に7日間放置した後、分離
の程度を肉眼で判定した。
Baking load: Shell type high-speed four-ball friction tester Ball 1/2 inch Measuring temperature 70 ° C Vertical shaft speed 800 rpm Sample polymer oil: 60 spindle oil (wt ratio 30:70) mixed oil Compatibility with mineral oil: polymer oil Dissolve 30 in 60 spindle oil and
After making a wt% solution and leaving it at 0 ° C. for 7 days, the degree of separation was visually judged.

○:良好、 △:若干分離または下部に若干沈澱物あり、 ×:二層に分離している 臭気:重合反応後放冷し、常温での臭気及び室温で30日
間放置後の臭気を次の基準により判定した。
◯: Good, Δ: Slightly separated or a little precipitate in the lower part, ×: Separated into two layers Odor: After polymerization reaction, the odor after standing to cool for 30 days at room temperature was It was judged according to the standard.

○:魚臭がない △:若干魚臭がある ×:魚臭が激しい 実施例2 脱酸、脱色した精製魚油(タラを主とする混合魚油、IV
170)10kgをステンレス製20のオートクレーブに仕込
み、Ni系触媒0.4wt%、水素圧1.8kg/cm2、反応
温度160±2℃で水添し、IV85.5、AV0.60の水素添加魚
油9.5kgを得た。
◯: No fish odor Δ: Slight fish odor ×: Violent fish odor Example 2 Deoxidized and decolorized refined fish oil (mixed fish oil mainly containing cod, IV
170) 10 kg was charged into a stainless steel 20 autoclave, hydrogenated at 0.4 wt% Ni-based catalyst, hydrogen pressure 1.8 kg / cm 2 , reaction temperature 160 ± 2 ° C., hydrogenation of IV85.5, AV0.60. 9.5 kg of fish oil was obtained.

この水素添加魚油1000gをステンレス製2の反応釜に
仕込み、空気を吹き込みながら撹拌し、30分で160℃に
昇温後、同温度で1.5時間重合して、粘度(38℃)10
0 CPの重合油980gを得た。
1000g of this hydrogenated fish oil was charged into a stainless steel 2 reaction kettle, stirred while blowing air, heated to 160 ° C in 30 minutes, polymerized at the same temperature for 1.5 hours, and viscosity (38 ° C) 10
980 g of 0 CP polymerized oil was obtained.

得られた重合油の臭気、焼付荷重、鉱油との相溶性を測
定しその結果を表−2のNo.3に示す。
The odor, baking load, and compatibility with mineral oil of the obtained polymerized oil were measured, and the results are shown in No. 3 of Table-2.

また上記水素添加反応で得たIV85.5、AV0.60の水素添加
魚油を用いて上記と同様の方法で重合し各々粘度(38
℃)が70CP、80CP、500CP、1000CP、2000CP、3000CP、3
300CPの重合油を合成し、得られた重合油の臭気、焼付
荷重、鉱油との相溶性を実施例1と同様に測定し、その
結果を表−2のNo.1、2及び4〜8に示す。
Further, using the hydrogenated fish oils of IV85.5 and AV0.60 obtained by the above hydrogenation reaction, polymerization was carried out in the same manner as above and the viscosity (38
℃) 70CP, 80CP, 500CP, 1000CP, 2000CP, 3000CP, 3
300 CP of polymerized oil was synthesized, and the odor, baking load, and compatibility with mineral oil of the obtained polymerized oil were measured in the same manner as in Example 1, and the results are shown in Table 2, Nos. 1, 2 and 4 to 8. Shown in.

表−2で水素添加魚油の重合油(No.1〜8)のうち重
合油の粘度が70CPのものは鉱油との相溶性、臭気が悪
く、また粘度が3300CPのものは鉱油との相溶性が悪くと
もに本発明の範囲外である。
In Table 2, among the polymerized oils of hydrogenated fish oil (No. 1 to 8), those with a viscosity of 70CP have good compatibility with mineral oil and bad odor, and those with a viscosity of 3300CP have compatibility with mineral oil. However, both are out of the scope of the present invention.

比較例1、2 実施例2に用いた精製魚油(IV 170)を実施例2と同様
に水素添加しIV8.7(比較例1)、IV85.5(比較例
2)の水素添加魚油を合成して、その諸物性を測定し、
その結果を表−2のNo.9、10に示す。
Comparative Examples 1 and 2 The purified fish oil (IV 170) used in Example 2 was hydrogenated in the same manner as in Example 2 to synthesize hydrogenated fish oils of IV8.7 (Comparative Example 1) and IV85.5 (Comparative Example 2). And then measuring its physical properties,
The results are shown in Nos. 9 and 10 of Table-2.

比較例3、4 実施例2に用いた精製魚油(IV 170)を実施例2と同様
に重合し38℃の粘度500 CP(比較例3)、1200CP(比較
例4)の重合油を合成し、得られた重合油の諸物性を測
定し、その結果を表−2のNo.11、12に示す。
Comparative Examples 3 and 4 The purified fish oil (IV 170) used in Example 2 was polymerized in the same manner as in Example 2 to synthesize polymer oils having a viscosity of 38 ° C. of 500 CP (Comparative Example 3) and 1200 CP (Comparative Example 4). Various physical properties of the obtained polymerized oil were measured, and the results are shown in Nos. 11 and 12 of Table-2.

実施例3 精製魚油(タラを主とする混合魚油、IV 170.2)及び精
製魚油(イワシを主とする混合魚油、IV 175.6)を用い
て実施例1と同様に水素添加反応し、得られた水素添加
魚油を実施例1と同じ条件で加熱重合、または実施例2
と同じ条件の下で酸化重合し表−3に示す重合油A〜D
を得た。
Example 3 A hydrogenation reaction was carried out in the same manner as in Example 1 using purified fish oil (mixed fish oil mainly containing cod, IV 170.2) and purified fish oil (mixed fish oil mainly containing sardine, IV 175.6) to obtain hydrogen. Heat-polymerization of the added fish oil under the same conditions as in Example 1, or Example 2
Polymerized oils A to D shown in Table 3 by oxidative polymerization under the same conditions as
Got

得られた重合油A〜Dを試料油として下記に示す切削試
験を行ない、その切削加工における潤滑性能を評価し
た。その結果を表−4に示す。
Using the obtained polymerized oils A to D as sample oils, the following cutting test was performed to evaluate the lubricating performance in the cutting process. The results are shown in Table-4.

なお比較例としてナタネ油(IV 104.4)を用いて同様に
切削試験を行なった。
As a comparative example, rapeseed oil (IV 104.4) was used for the same cutting test.

切削試験方法 試料油を60スピンドル油に溶解して20wt%の溶液とし、
この溶液を用いて立型内面引抜ブローチ試験機により切
削抵抗値を測定し、また切削した表面のアラサを触針式
アラサ測定機で切削方向に測定し切削加工時の潤滑性能
を評価した。
Cutting test method Dissolve sample oil in 60 spindle oil to make 20wt% solution,
Using this solution, the cutting resistance value was measured by a vertical internal drawing broach tester, and the roughness of the cut surface was measured in the cutting direction by a stylus type roughness measuring machine to evaluate the lubricating performance during cutting.

切削条件 試験機:3ton立型内面引抜きブローチ盤 工具:1刃当り切込み最大0.05mm、巾7mm、ピッチ
8mm、材質SKH55のキーブローチ工具 被削材質:S−45C 切削速度:2m/min 実施例4 実施例3で得た重合油A〜Dを試料油とし、この試料油
をパラフィン系鉱油(日石タービンオイル32)に溶解
し、3wt%の溶液とした。この溶液のアルミニウムの深
絞り加工試験における潤滑性能を、高速深絞り試験機に
より評価した。その結果を図−1に示す。
Cutting condition Tester: 3ton vertical inner surface drawing broaching machine Tool: Max. 0.05mm per blade, width 7mm, pitch 8mm, key broaching tool with material SKH55 Work material: S-45C Cutting speed: 2m / min Example 4 Polymerized oils A to D obtained in Example 3 were used as sample oils, and the sample oils were dissolved in paraffinic mineral oil (Nisseki turbine oil 32) to prepare a 3 wt% solution. The lubricating performance of this solution in the aluminum deep drawing test was evaluated by a high speed deep drawing tester. The results are shown in Figure 1.

比較例としてオレイン酸の3wt%パラフィン系鉱油溶液
を用いて上記と同様にアルミニウムの深絞り加工試験を
行なった。
As a comparative example, a deep drawing test of aluminum was conducted in the same manner as above using a 3 wt% paraffinic mineral oil solution of oleic acid.

試験条件 試験機:東京試験機(株)製深絞り試験機 ポンチ径32mmφ、ダイス径35mmφ、加工速度1m/秒 加工材:アルミ板(JIS A1100.0厚さ1mm)の円盤を用
いて1試料油につき径62.4mmφ(絞り比1.95)から68.0
mmφ(絞り比2.125)までの8点(径の増加率0.8m
m)を試験 試料油塗布量:1g/m3、加工材の両面に塗布 実施例5 実施例3で得た重合油A〜Dを試料油とし、下記の圧延
試験を行ない圧延加工における潤滑性能を評価した。そ
の結果を図−2に示す。
Test condition Tester: Deep drawing tester manufactured by Tokyo Tester Co., Ltd. Punch diameter 32mmφ, Die diameter 35mmφ, Processing speed 1m / sec. Processing material: One sample using aluminum plate (JIS A1100.0 thickness 1mm) Diameter 62.4 mmφ (drawing ratio 1.95) to 68.0 per oil
8 points up to mmφ (drawing ratio 2.125) (diameter increase rate 0.8m
m) test sample oil application amount: 1 g / m 3 , applied to both sides of processed material Example 5 Polymerized oils A to D obtained in Example 3 were used as sample oils, and the following rolling test was performed to perform lubrication performance in rolling. Was evaluated. The results are shown in Figure 2.

比較例として牛脂(IV48.5)を用いて上記と同様に圧延
試験を行なった。
As a comparative example, beef tallow (IV48.5) was used to perform a rolling test in the same manner as above.

圧延試験方法 圧延前の鋼板に50mmの間隔(l)の2本の線を引き、
この鋼板に試料油を塗布し、これを圧延して圧延後、2
本の線の間隔(l)を測定し、次式により圧下率を求
めた。またその時の圧延荷重(ton)をロードセルにて
測定した。
Rolling test method Draw two lines with a spacing of 50 mm (l 1 ) on the steel sheet before rolling,
After applying the sample oil to this steel plate, rolling it and rolling it, 2
The interval (l 2 ) between the lines was measured, and the rolling reduction was calculated by the following formula. The rolling load (ton) at that time was measured with a load cell.

圧延試験の条件は次の通り。 The rolling test conditions are as follows.

圧延機:四段ロール式圧延機 ワークロール 径150mm×巾140mm バックアップロール 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 試料油の塗布量:1g/m2 〔発明の効果〕 以上説明したように本発明の金属加工油は、水素添加魚
油の重合油を含有するものであり、魚油を一定のIVに水
素添加した後、特定の粘度範囲に重合した重合油を基油
あるいは油性向上剤として用いるもので、本発明は従来
金属加工油の基油として用いられている牛脂、ラード等
と比べて、潤滑性に優れるため金属の切削、研削、圧
延、プレス、引抜等の金属加工に用いて仕上り表面の良
い加工物が得られ、少ない使用量で良好な性能を発揮し
経済性に優れる。また魚臭等の臭気が少なく、高温下で
の金属加工に用いることができるとともに労働環境を改
善することができ、本発明の金属加工油を長期間放置し
ても臭気の発生、着色が無い等の経時安定性が良く、保
存性、商品性が高い等の効果を有する。
Rolling machine: Four-stage rolling mill Work roll Diameter 150 mm x Width 140 mm Backup roll Diameter 250 mm x Width 140 mm Roll material Chrome steel roll peripheral speed 30 m / min Rolling material: SPC-C Thickness 0.6 mm x Width 50 mm x Length 150 mm Sample oil coating amount: 1 g / m 2 [Effect of the invention] As described above, the metalworking oil of the present invention contains the polymerized oil of hydrogenated fish oil, and the fish oil is hydrogenated to a certain IV. After that, the polymerized oil polymerized in a specific viscosity range is used as a base oil or an oiliness improver, and the present invention has a higher lubricity than beef tallow, which is conventionally used as a base oil for metalworking oils. Because it is excellent, it can be used for metal processing such as metal cutting, grinding, rolling, pressing, drawing, etc. to obtain a processed product with a good finished surface, exhibiting good performance with a small usage amount and being excellent in economic efficiency. Further, it has little odor such as fish odor, can be used for metal working under high temperature and can improve working environment, and no odor is generated or coloring even when the metal working oil of the present invention is left for a long time. Etc. have good effects such as good stability over time, high storability and high commercialability.

【図面の簡単な説明】[Brief description of drawings]

図−1 …… 本発明の実施例4に係るアルミニウムの
深絞り加工試験結果を示す荷重−絞り比相関図。 図−2 …… 本発明の実施例5に係る圧延試験結果を
示す荷重−圧下率相関図。
FIG. 1 ... A load-drawing ratio correlation diagram showing the results of a deep drawing test of aluminum according to Example 4 of the present invention. Fig. 2 ... A load-reduction ratio correlation diagram showing rolling test results according to Example 5 of the present invention.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C10N 30:08 40:20 Z 8217−4H ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location C10N 30:08 40:20 Z 8217-4H

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】沃素価60〜110の水素添加魚油を、加熱ま
たは酸化により重合して得られる38℃で80〜3000センチ
ポイズの粘度を有する重合油を含有することを特徴とす
る金属加工油。
1. A metalworking oil comprising a polymerized oil having a viscosity of 80 to 3000 centipoise at 38 ° C. obtained by polymerizing hydrogenated fish oil having an iodine value of 60 to 110 by heating or oxidation.
JP25562485A 1985-11-14 1985-11-14 Metal working oil Expired - Lifetime JPH068429B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25562485A JPH068429B2 (en) 1985-11-14 1985-11-14 Metal working oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25562485A JPH068429B2 (en) 1985-11-14 1985-11-14 Metal working oil

Publications (2)

Publication Number Publication Date
JPS62115092A JPS62115092A (en) 1987-05-26
JPH068429B2 true JPH068429B2 (en) 1994-02-02

Family

ID=17281336

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25562485A Expired - Lifetime JPH068429B2 (en) 1985-11-14 1985-11-14 Metal working oil

Country Status (1)

Country Link
JP (1) JPH068429B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000017714A (en) * 1999-08-03 2000-04-06 곽한용 Fish oil refine a precess and refined fish oil

Also Published As

Publication number Publication date
JPS62115092A (en) 1987-05-26

Similar Documents

Publication Publication Date Title
US4885104A (en) Metalworking lubricants derived from natural fats and oils
US4978465A (en) Sulfurized metalworking lubricants derived from modified natural fats and oils and formulations
JP3354024B2 (en) Lubricants for low-temperature forming of aluminum and aluminum alloy sheets
US3298954A (en) Metal working lubricant
US3995465A (en) Method of coldworking metal pieces
JPH0221438B2 (en)
US5706684A (en) Metalworking process
JPH068429B2 (en) Metal working oil
US3983044A (en) Low smoking lubricating composition for cold heading operations
CN115505442A (en) Hot rolling oil composition and preparation method and application thereof
JP2580008B2 (en) Lubricant
JP3320642B2 (en) Hot rolling oil and hot rolling method
JPH01301793A (en) Lubricating oil
JPH0631372B2 (en) Metal working oil
JP2984026B2 (en) Metal working oil and metal working method
JP2955894B2 (en) Metal working oil
JP2955891B2 (en) Metal working oil
JP2635376B2 (en) Lubricant
JPH0221437B2 (en)
US3002926A (en) Heat-stable greases and method of preparation
JPS6128590A (en) Metal working oil
SU883158A1 (en) Method of producing grease for cold pressure-working of metals
JP2571101B2 (en) Lubricant
JPH066712B2 (en) Lubricant
JPH0631367B2 (en) Lubricant