JPS62153395A - Traction fluid - Google Patents

Traction fluid

Info

Publication number
JPS62153395A
JPS62153395A JP60294424A JP29442485A JPS62153395A JP S62153395 A JPS62153395 A JP S62153395A JP 60294424 A JP60294424 A JP 60294424A JP 29442485 A JP29442485 A JP 29442485A JP S62153395 A JPS62153395 A JP S62153395A
Authority
JP
Japan
Prior art keywords
traction
olefin
fluid
component
alpha
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.)
Granted
Application number
JP60294424A
Other languages
Japanese (ja)
Other versions
JPH0631374B2 (en
Inventor
Shigehiko Yoshimura
成彦 吉村
Hirotaka Tomizawa
富沢 広隆
Yasumaki Komatsu
小松 保蒔
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.)
Tonen General Sekiyu KK
Original Assignee
Toa Nenryo Kogyyo KK
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 Toa Nenryo Kogyyo KK filed Critical Toa Nenryo Kogyyo KK
Priority to JP60294424A priority Critical patent/JPH0631374B2/en
Priority to PCT/JP1987/000435 priority patent/WO1988010293A1/en
Priority to EP87904127A priority patent/EP0344307B1/en
Publication of JPS62153395A publication Critical patent/JPS62153395A/en
Publication of JPH0631374B2 publication Critical patent/JPH0631374B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • C10M169/00Lubricating compositions characterised by containing as components a mixture of at least two types of ingredient selected from base-materials, thickeners or additives, covered by the preceding groups, each of these compounds being essential
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    • C10M105/00Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
    • C10M105/08Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing oxygen
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Abstract

PURPOSE:To obtain a traction fluid which has a high coefficient of traction and is relatively inexpensive, by using a blend of a specified diester compd. or its derivative and a branched poly-alpha-olefin as a base oil. CONSTITUTION:A traction fluid contains a blend of a diester compd. of the formula or its derivative and a branched poly-alpha-olefin as a base oil. In the formula, A is an ester linkage of -COO- or -OOC-; n is 1-6; R1 is H or a 1-8C alkyl; R2 is a 1-3C alkyl. n is pref. 1-3. When n is O, the coefficient of traction is low, while when n is 7 or above, the viscosity is too high. thus, the case where n is 0 or 7 is not preferred. The poly-alpha-olefin has a quaternary or teriary carbon atom in its main chain. Examples thereof are polymers of a 3-5C alpha-olefin and hydrogenated products among which polybutene, polyisobutylene and hydrogenated products thereof are particularly preferred.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、トラクション用流体に関するもので、さらに
詳しくは二個のシクロヘキシル環を有するジエステルま
たはその誘導体と、分岐を有するポリアルファーオレフ
ィンとを基油として配合してなるトラクション用流体に
関するものである。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a traction fluid, more specifically a traction fluid based on a diester having two cyclohexyl rings or a derivative thereof and a branched polyalphaolefin. This invention relates to a traction fluid formulated as an oil.

(従来の技術) 、自動車あるいは産業用機械において、動力をトラクシ
ョンドライブ機構により被駆動部へ伝達するトラクショ
ンドライブ動力伝達装置が注目され、近年盛んに研究開
発が推進されている。トラクションドライブ機構とは、
ころがり摩擦等を利用した動力伝達機構のことで、従来
のように歯車を使用しないので振動、騒音が低減し高速
回転の変速も非常にスムーズに行なうことができる。自
動車業界では、自動車の燃費改善が重要な課題となって
いるが自動車の変速機にトラクションドライブを適用し
無段変速にすれば、常にエンジンの最高燃費領域で運転
できるので、従来のトランスミッションシステムに比べ
燃費を20%以上も減少させることができるといわれて
いる。最近の研究の成果として、高い疲労強度を持つ材
料の開発と、トラクションに関する理論的な解析があり
、トラクション流体についても成分の分子構造レベルで
のトラクション係数の相関関係が徐々に解明されつつあ
る。ここでトラクション係数とは、ころがり摩擦型動力
伝達装置において互いに接触する回転体の接触部分の、
すべりにより発生するけん引力の法線荷重に対する比と
して定義される。
(Prior Art) In automobiles and industrial machines, traction drive power transmission devices that transmit power to driven parts using traction drive mechanisms have attracted attention, and research and development have been actively promoted in recent years. What is traction drive mechanism?
This is a power transmission mechanism that uses rolling friction, etc., and does not use gears as in conventional systems, reducing vibration and noise, and allowing for extremely smooth speed changes at high speeds. Improving the fuel efficiency of cars is an important issue in the automobile industry, but if a traction drive is applied to a car's transmission to make it continuously variable, the engine can always be operated in its highest fuel efficiency range, making it easier to replace conventional transmission systems. It is said that fuel consumption can be reduced by more than 20%. Recent research results include the development of materials with high fatigue strength and theoretical analysis of traction, and the correlation between the traction coefficients of traction fluids at the level of the molecular structure of their components is gradually being clarified. Here, the traction coefficient refers to the contact area of the rotating bodies that contact each other in a rolling friction type power transmission device.
It is defined as the ratio of the traction force generated by sliding to the normal load.

トラクション流体は高トラクション係数を有する潤滑油
でなければならず、その分子構造はナフテン環を有する
ものが高性能を発揮することが確認されており、市販品
としてはモンサント社の「サンドトラック■」が広く知
られている。ナフテン環を有するトラクション流体とし
て、特公昭47−j5783号公報にはジ(シクロヘキ
シル)アルカンまたはジシクロヘキサンが開示されてい
る。この特許には、当該アルカン化合物が過水素添加(
アルファーメチル)スチレン重合物あるいはヒドリンダ
ン化合物等を配合された流体のトラクション係数が高水
準である旨、記載されている。さらに、特開昭59−1
91797号公報には、ナフテン環を有するエステル化
合物を含有してなるトラクシジン流体が開示されており
、シクロへキシルジカルボン酸ジシクロヘキシルエステ
ルあるいはフタル酸ジシクロヘキシルエステルの芳香族
核水素添加により得られるエステルがトラクション流体
として好ましいとしている。
The traction fluid must be a lubricating oil with a high traction coefficient, and it has been confirmed that those with a naphthene ring molecular structure exhibit high performance.A commercially available product is Monsanto's "Sand Truck ■". is widely known. As a traction fluid having a naphthene ring, Japanese Patent Publication No. 47-J5783 discloses di(cyclohexyl)alkane or dicyclohexane. This patent states that the alkane compound is perhydrogenated (
It is stated that the traction coefficient of a fluid containing an alpha methyl) styrene polymer or a hydrindane compound is at a high level. Furthermore, JP-A-59-1
Publication No. 91797 discloses a traction fluid containing an ester compound having a naphthene ring, in which an ester obtained by aromatic nuclear hydrogenation of cyclohexyldicarboxylic acid dicyclohexyl ester or phthalic acid dicyclohexyl ester is used as a traction fluid. It is preferred as such.

(発明が解決しようとする問題点) 上記のとおり近年自動車業界では、無段変速機の開発を
積極的に推進しているが、該変速機としては潤滑流体の
トラクション係数が高いほど同一装置で許容伝達力を大
きくすることができるため装置全体を小型化しうるとと
もに公害上問題となる排ガスの発生量を低減しうるので
極力トラクション係数の高い流体が嘱望されている。し
かるに、トラクション流体の市販品として最も性能が高
いとされるサンドトラック■は、このようなトラクシジ
ンドライブ装置に用いた場合トラクション係数の点で満
足すべき性能が得られず、しかも価格が高いという問題
がある。また、特公昭48−35783号公報で提案さ
れたトラクション流体もサンドトラック■あるいはその
類似物質を一成分としているので同様に性能及び価格面
に問題がある。
(Problems to be Solved by the Invention) As mentioned above, in recent years the automobile industry has been actively promoting the development of continuously variable transmissions. Fluids with as high a traction coefficient as possible are desired because they can increase the permissible transmission force, making it possible to downsize the entire device and reducing the amount of exhaust gases that cause pollution. However, SandTrak■, which is said to have the highest performance as a commercially available traction fluid, does not provide satisfactory performance in terms of traction coefficient when used in such Traxijin drive devices, and is also expensive. There's a problem. Furthermore, the traction fluid proposed in Japanese Patent Publication No. 48-35783 also has problems in terms of performance and price since it contains Sandtrack (2) or a similar substance as one of its components.

(問題点を解決するための手段) 本発明者らは、高トラクション係数を有ししかも比較的
安価なトラクション用流体を得るべく臆念研究を重ねた
結果、二個のシクロヘキシル環を有するジエステルまた
はその誘導体に、分岐を有するポリアルファーオレフィ
ンを特定量配合することにより性能が高い基油流体を経
済的に提供しうろことを確認し本発明を完成させた。
(Means for Solving the Problems) As a result of extensive research in order to obtain a traction fluid that has a high traction coefficient and is relatively inexpensive, the present inventors have discovered a diester or a diester having two cyclohexyl rings. The present invention was completed by confirming that it is possible to economically provide a base oil fluid with high performance by blending a specific amount of branched polyalphaolefin with the derivative.

[式中、A′は−COO−又は一0OC−のエステル結
合でありnは1〜6であり、R1は水素原子、炭素数1
〜8のアルキル基から選択される1種又は2種でR2は
炭素数1〜3のアルキル基から選択される1種又は2種
である]で示されるジエステルまたはその誘導体に、分
岐を有するポリアルファーオレフィンを0.1〜70重
量%配合したことを特徴とするトラクション流体に関す
るものである。
[In the formula, A' is an ester bond of -COO- or 10OC-, n is 1 to 6, and R1 is a hydrogen atom, with a carbon number of 1
-8 alkyl groups, and R2 is one or two selected from alkyl groups having 1 to 3 carbon atoms. This invention relates to a traction fluid characterized by containing 0.1 to 70% by weight of alpha olefin.

本発明の第1の目的は、高トラクション係数を有する性
能の優れたトラクション流体を提供することである。本
発明の第2の目的は、経済的でしかも人手しやすく容易
に装置へ適用しうるトラクジョン流体を提供することで
ある。
A first object of the present invention is to provide a high performance traction fluid with a high traction coefficient. A second object of the present invention is to provide a traction fluid that is economical, easy to handle, and easy to apply to devices.

本発明のトラクション用流体は、二成分の基油からなり
A成分としてのジエステルまたはその誘導体に、B成分
としての分岐を有するポリアルファーオレフィンを特定
量配合したものである。
The traction fluid of the present invention is composed of a two-component base oil, in which a diester or its derivative as the A component is blended with a specific amount of a branched polyalphaolefin as the B component.

本発明のA成分は二個のシクロヘキシル環を冑するジエ
ステルまたはその誘導体であり、前記構造式を有するも
のである。エステル結合のA′は−COO−または−0
00−でありgem−ジアルキル構造のくり返し単位の
nは、1〜6であり特に1〜3が好ましい。nが0では
トラクション係数が低く、nが7以上では粘度が高くな
り好ましくない。このジエステルまたはその誘導体は、
下記方法に依って製造され次の性状を有するものである
Component A of the present invention is a diester having two cyclohexyl rings or a derivative thereof, and has the above structural formula. A' of the ester bond is -COO- or -0
00-, and n of the repeating unit of the gem-dialkyl structure is 1 to 6, particularly preferably 1 to 3. When n is 0, the traction coefficient is low, and when n is 7 or more, the viscosity becomes high, which is not preferable. This diester or its derivative is
It is manufactured by the method described below and has the following properties.

粘度は40℃で20〜50 cst、特に24〜30 
cstが好ましく、100℃で4〜to cst、特に
4〜6  cstが好ましい。また粘度指数は、40〜
100.特に50〜80の範囲が好ましい。
Viscosity is 20-50 cst at 40°C, especially 24-30
cst is preferred, 4 to to cst, especially 4 to 6 cst at 100°C. In addition, the viscosity index is 40~
100. Particularly preferred is a range of 50 to 80.

A成分は、次に示す方法により製造することができる。Component A can be produced by the method shown below.

A成分は、グリコール化合物とシクロヘキサンカルボン
酸化合物とのエステル化反応によって得ることができる
。グリコール化合物としてはgeal−ジアルキル構造
を1〜6個有するものが選択され、ネオペンチルグリコ
ールが好ましい。シクロヘキサンカルボン酸化合物とし
ては、シクロヘキサンカルボン酸のほかに炭素数1〜8
のアルキル基を有するもので例えばメチルシクロヘキサ
ンカルボン酸あるいはエチルシクロヘキサンカルボン酸
等が挙げられる。特に好ましいのは、シクロヘキサンカ
ルボン酸である。エステル化反応は、はぼ反応等量付近
で行なうか酸過剰条件で行なうが、前者では触媒が必要
でしかもモノアルコールの副生物が生成する等の問題が
あるので酸過剰条件を採用するのが好ましい。すなわち
、グリコール化合物1モルに対し酸を2〜5倍モル(特
に好ましくは2.5〜4倍モル)反応させる。反応温度
は約150〜250℃、好ましくは170〜230℃と
し、反応時間は10〜40時間、好ましくは15〜25
時間とする。反応圧力は加圧、減圧でも良いが反応操作
の点で常圧が好ましい。この条件下では、過剰の酸が触
媒として作用する。また溶媒としてキシレン、トルエン
等のアルキルベンゼンを適当量加えることができる。溶
媒の添加により、反応と温度を容易に制御することがで
きる。反応の進行にともない、生成した水が蒸発してく
るが、この水がアルコールの2倍モルとなった時点で反
応を終了する。過剰の酸は、アルカリ水溶液で中和し水
洗により除去する。酸がアルカリ洗で取り出しにくい場
合は、酸をアルコールの2〜265倍モルにして触媒を
用いて反応させる。触媒としては、リン酸、パラトルエ
ンスルホン酸、硫酸等を使用することができるが、反応
速度を高めエステルの収率を上げる点で、リン酸を使用
するのが最も好ましい。本発明のジエステル化合物は、
最後に反応生成物を減圧蒸留して水と溶媒を流出するこ
とにより得られる。本発明のA成分はシクロヘキサノー
ル化合物と第4級炭素を有するジカルボン酸とのエステ
ル化によっても製造することができる。この場合、シク
ロヘキサノール化合物としては、シクロヘキサノールあ
るいはメチルシクロヘキサノール等、またジカルボン酸
としては、ネオペンチルジカルボン酸等を使用すればよ
い。
Component A can be obtained by an esterification reaction between a glycol compound and a cyclohexanecarboxylic acid compound. As the glycol compound, one having 1 to 6 gel-dialkyl structures is selected, and neopentyl glycol is preferred. In addition to cyclohexanecarboxylic acid, the cyclohexanecarboxylic acid compound has 1 to 8 carbon atoms.
Examples of those having an alkyl group include methylcyclohexanecarboxylic acid and ethylcyclohexanecarboxylic acid. Particularly preferred is cyclohexanecarboxylic acid. The esterification reaction can be carried out around the equivalent of the Habo reaction or under acidic excess conditions, but the former requires a catalyst and has problems such as the production of monoalcohol by-products, so it is better to use acidic conditions. preferable. That is, the acid is reacted in an amount of 2 to 5 times the mole (particularly preferably 2.5 to 4 times the mole) per mole of the glycol compound. The reaction temperature is about 150-250°C, preferably 170-230°C, and the reaction time is 10-40 hours, preferably 15-25 hours.
Time. The reaction pressure may be increased or reduced pressure, but normal pressure is preferred from the viewpoint of reaction operation. Under this condition, excess acid acts as a catalyst. Further, an appropriate amount of alkylbenzene such as xylene or toluene can be added as a solvent. By adding a solvent, the reaction and temperature can be easily controlled. As the reaction progresses, the water produced evaporates, and the reaction is terminated when the amount of water becomes twice the mole of alcohol. Excess acid is neutralized with an aqueous alkaline solution and removed by washing with water. If the acid is difficult to remove by alkaline washing, the acid is made 2 to 265 times the mole of the alcohol and reacted using a catalyst. As the catalyst, phosphoric acid, para-toluenesulfonic acid, sulfuric acid, etc. can be used, but it is most preferable to use phosphoric acid in terms of increasing the reaction rate and increasing the yield of ester. The diester compound of the present invention is
Finally, the reaction product is distilled under reduced pressure to remove water and solvent. Component A of the present invention can also be produced by esterifying a cyclohexanol compound and a dicarboxylic acid having a quaternary carbon. In this case, the cyclohexanol compound may be cyclohexanol or methylcyclohexanol, and the dicarboxylic acid may be neopentyldicarboxylic acid or the like.

B成分としてのポリアルファーオレフィンは、四級炭素
原子や三級炭素原子を主鎖に有するもので、炭素数が3
〜5のアルファーオレフィンの重合体およびその水添物
である。例えば、ポリプロピレン、ポリブテン、ポリイ
ソブチレン、ポリベンテン及びそれらの水添物であるが
、特に好ましいものはポリブテン、ポリイソブチレンお
よびその水添物である。ポリイソブチレンは、次の構造
式で示すことができる。
The polyalphaolefin as component B has a quaternary carbon atom or a tertiary carbon atom in the main chain, and has a carbon number of 3.
-5 alpha olefin polymers and hydrogenated products thereof. Examples include polypropylene, polybutene, polyisobutylene, polybentene, and hydrogenated products thereof, and particularly preferred are polybutene, polyisobutylene, and hydrogenated products thereof. Polyisobutylene can be represented by the following structural formula.

また、その水添物は次の構造式で示される。Moreover, the hydrogenated product is shown by the following structural formula.

但し、上記の重合度nは6〜200である。However, the above degree of polymerization n is 6 to 200.

ポリブテン、ポリイソブチレンは市販品を使用すればよ
いが公知の方法で重合することにより製造することがで
きる。また、その水添物はポリイソブチレン等を水素の
存在下に反応させて製造する。特に好ましいポリアルフ
ァーオレフィンは、分子量500〜10,000の範囲
にあるものでより好ましくは900〜5.000の分子
量範囲にあるものを使用する。分子量の調整は高分子量
のポリアルファーオレフィンの分解、低分子量ポリアル
ファーオレフィンの混合等に依ればよい。なお、ポリア
ルファーオレフィンと一部製造原料が同一な高分子重合
体に、アルファーオレフィン共重合体(QCP)がある
が、このOCPは本発明のB成分として1用いるには適
切ではない。その理由は、OCPが2以上のアルファー
オレフィンの重合によって得られそれらが不規則に連結
した構造を有し、本発明のポリブテン等の如き規則的な
gem−ジメチル型構造ではないためである。
Polybutene and polyisobutylene may be commercially available products, but they can be produced by polymerization using known methods. Further, the hydrogenated product is produced by reacting polyisobutylene or the like in the presence of hydrogen. Particularly preferred polyalphaolefins have molecular weights in the range of 500 to 10,000, more preferably 900 to 5.000. The molecular weight may be adjusted by decomposing a high molecular weight polyalphaolefin, mixing a low molecular weight polyalphaolefin, or the like. Incidentally, an alpha olefin copolymer (QCP) is a polymer whose manufacturing raw materials are partially the same as polyalpha olefin, but this OCP is not suitable for use as component B in the present invention. This is because OCP is obtained by polymerizing two or more alpha olefins and has a structure in which they are irregularly connected, and is not a regular gem-dimethyl type structure like the polybutene of the present invention.

本発明におけるA成分、例えばネオペンチルグリコール
シクロヘキサンカルボン酸ジエステルは、トラクション
係数が0.100〜0.104を示し、B成分、例えば
ポリブテンは、トラクション係数が0.075〜0.0
85の値を示すものである。
In the present invention, component A, such as neopentyl glycol cyclohexane carboxylic acid diester, exhibits a traction coefficient of 0.100 to 0.104, and component B, such as polybutene, exhibits a traction coefficient of 0.075 to 0.0.
This shows a value of 85.

本発明のA成分はトラクション係数が高いのでA成分を
単独でトラクションドライブ装置に適用しても、高性能
を発揮することができる。しかしながら、このA成分に
B成分のポリアルファーオレフィンを0.1〜70重量
%配合することにより更に好ましいトラクション用流体
とすることができる。すなわち、B成分はA成分よりも
トラクション係数は低いものの、B成分のgem−ジメ
チル基がA成分のシクロヘキシル環と相乗効果によって
トラクション係数向上作用を発揮し、しかも価格が安く
粘度特性に優れているので、B成分をA成分に対し0.
1〜70重量%配合することによりトラクション係数を
下げることなく経済的にトラクション用流体を得ること
ができるわけである。
Since component A of the present invention has a high traction coefficient, even if component A is applied alone to a traction drive device, high performance can be achieved. However, by blending 0.1 to 70% by weight of polyalphaolefin as component B with component A, a more preferable traction fluid can be obtained. That is, although component B has a lower traction coefficient than component A, the gem-dimethyl group of component B exerts a synergistic effect with the cyclohexyl ring of component A to improve the traction coefficient, and it is also inexpensive and has excellent viscosity characteristics. Therefore, the B component is 0.
By blending 1 to 70% by weight, it is possible to economically obtain a traction fluid without lowering the traction coefficient.

本発明のトラクション流体には、用途に応じて種々の添
加剤を配合することもできる。すなわち、トラクション
装置が高温、大荷重を受けるものであれば酸化防止剤、
摩耗防止剤あるいは防せい剤の一種または2種以上の添
加剤を0.01〜5重量%程度配合することができる。
The traction fluid of the present invention may also contain various additives depending on the intended use. In other words, if the traction device is subject to high temperatures and heavy loads, antioxidants,
Approximately 0.01 to 5% by weight of one or more types of additives such as anti-wear agents or anti-rust agents can be blended.

同様に高粘度指数が要求される場合には、公知の粘度指
数向上剤を1〜10重量%配合すればよい。但し、ポリ
メタクリレートやオレフィン共重合体を用いると逆にト
ラクション係数を低下するので°、これらの添加量は4
重量%以下にする必要がある。
Similarly, when a high viscosity index is required, 1 to 10% by weight of a known viscosity index improver may be added. However, if polymethacrylate or olefin copolymer is used, the traction coefficient will decrease, so the amount of these added should be 4.
Must be less than % by weight.

本発明においてトラクション流体とは、回転トルクを点
接触あるいは線接触により伝達する装置、さらにはこれ
らと同様な構造を有する伝達装置において用いられる流
体をいう。本発明のトラクション流体は、従来知られて
いる流体よりも高いトラクション係数を有し、粘度等の
性状にもよるが従来品よりも1〜5%高いトラクション
係数を有するものである。このため、本発明のトラクシ
ョン流体は小型乗用車等の内燃機関をはじめ、紡績機械
や食品製造機械といった比較的低動力の伝達装置はもち
ろんのこと、大動力の産業機械等のトラクションドライ
ブ装置にも好ましく適用することができる。
In the present invention, the traction fluid refers to a fluid used in a device that transmits rotational torque through point contact or line contact, or a transmission device having a similar structure. The traction fluid of the present invention has a higher traction coefficient than conventionally known fluids, and has a traction coefficient 1 to 5% higher than conventional products, depending on properties such as viscosity. Therefore, the traction fluid of the present invention is suitable for use in internal combustion engines such as small passenger cars, relatively low-power transmission devices such as spinning machines and food manufacturing machines, as well as traction drive devices of large-power industrial machines. Can be applied.

(作 用) 本発明のトラクション流体は、公知の流体に比べて格段
に優れたトラクション係数を有するものであるが、いか
なる理由で高トラクション係数を示現しうるのであるか
については未だ完全には解明されていない。基本的には
、本発明のトラクション流体が有する特有な分子構造に
基づくものと考えられる。
(Function) Although the traction fluid of the present invention has a much superior traction coefficient compared to known fluids, it is still not completely clear why it exhibits such a high traction coefficient. It has not been. Basically, it is thought that this is based on the unique molecular structure of the traction fluid of the present invention.

まず、本発明のトラクション流体はジエステルであって
、化合物分子中にシクロヘキシル環を二個もっており、
それらがエステル結合しているため分子間相互に双極子
開力が働くことになる。そしてこの双極子開力がトラク
ション装置の高負荷条件下で流体を安定なガラス状態に
変え抗せん断力を増大せしめるものと考えられる。さら
に、本発明のトラクション流体は、A成分B成分ともに
g8111−ジアルキル型第四級炭素を有し、A成分は
これがメトキシカルボニル結合手を介して二個のシクロ
ヘキシル環と結合しているので分子内回転がしにくい構
造をしている。従って、トラクション装置の高負荷時に
はシクロヘキシル環と第四級炭素のgem−ジアルキル
部とがあたかもギアのように固くかみ合い、負荷から開
放された時には速かに離脱し流動化するものと考えられ
る。
First, the traction fluid of the present invention is a diester and has two cyclohexyl rings in the compound molecule.
Because they are ester-bonded, dipole opening force acts between the molecules. It is believed that this dipole opening force changes the fluid into a stable glass state under high load conditions of the traction device, increasing the anti-shear force. Furthermore, the traction fluid of the present invention has a g8111-dialkyl type quaternary carbon in both the A component and the B component, and the A component is bonded to two cyclohexyl rings via a methoxycarbonyl bond, so that it is in the molecule. It has a structure that makes it difficult to rotate. Therefore, it is thought that when the traction device is under high load, the cyclohexyl ring and the gem-dialkyl part of the quaternary carbon are tightly engaged like gears, and when the load is released, they quickly separate and become fluidized.

(実施例) 実施例1〜11 本発明のネオペンチルグリコールシクロヘキサンカルボ
ン酸ジエステルを、次の方法に依り合成した。
(Example) Examples 1 to 11 Neopentyl glycol cyclohexane carboxylic acid diester of the present invention was synthesized by the following method.

ネオペンチルグリコール1モルを、シクロヘキサンカル
ボン酸3倍モルと混合し反応温度200℃、常圧で20
時間反応させる。酸過剰の条件なため、触媒は用いず、
溶媒としてキシレンを用いる。反応とともに蒸発してき
た水が、アルコールの2倍モルとなった時点で反応を終
了する。過剰の酸はアルカリ(カセイソーダ)で洗い流
し、中性になるまで水洗する。反応生成物を減圧蒸留す
ることにより、水とキシレンを留去して本発明のジエス
テルを単離する。
One mole of neopentyl glycol was mixed with three times the mole of cyclohexanecarboxylic acid, and the reaction temperature was 200°C and 20% at normal pressure.
Allow time to react. Due to the excessive acid conditions, no catalyst was used.
Xylene is used as a solvent. The reaction is terminated when the amount of water that evaporates during the reaction reaches twice the mole of alcohol. Wash away excess acid with alkali (caustic soda) and rinse with water until neutral. The diester of the present invention is isolated by distilling the reaction product under reduced pressure to remove water and xylene.

次にこうして製造したジエステルに平均分子量が420
〜2350のポリブテンを配合してトラクション係数を
判定した。トラクション係数の測定条件は次のとおりで
ある。
Next, the diester thus produced had an average molecular weight of 420.
-2350 polybutene was blended and the traction coefficient was determined. The conditions for measuring the traction coefficient are as follows.

測定装置二曽田式40−ラートラクション試験機 試験条件:湯温20℃、ローラ一温度30℃平均ヘルツ
圧1 、2GPa。
Measuring device Nisota type 40-L traction tester Test conditions: Water temperature 20°C, roller temperature 30°C, average Hertzian pressure 1.2 GPa.

ころがり速度3.6m/s。Rolling speed 3.6m/s.

すべり率3.0% 本発明のトラクション用流体は、第1表に示すように従
来のトラクション流体と比べ格段に優れたトラクション
性能を有することがわかった。
Slip rate: 3.0% As shown in Table 1, the traction fluid of the present invention was found to have significantly superior traction performance compared to conventional traction fluids.

比較例1〜7 B成分100重量%、B成分90重量%を配合したトラ
クション流体、A成分にOCPまたはPMAを配合した
トラクション流体および市販のトラクション流体を用い
て、実施例に示した条件でトラクション係数を測定した
Comparative Examples 1 to 7 Traction was carried out under the conditions shown in the examples using a traction fluid containing 100% by weight of component B and 90% by weight of component B, a traction fluid containing OCP or PMA as component A, and a commercially available traction fluid. The coefficient was measured.

この結果第1表に示すようにいずれも本発明のトラクシ
ョン用流体よりもトラクション係数が1〜b オレフィン共重合体で具体的にはエチレンとプロピレン
との重合体く平均分子量15万〜30万)を用い、また
、PMAは、ポリメタクリレートで具体的には平均分子
量5万〜30万の重合体を用いた。
As a result, as shown in Table 1, all of the traction fluids have a traction coefficient of 1 to 1b higher than the traction fluid of the present invention. PMA was polymethacrylate, specifically a polymer having an average molecular weight of 50,000 to 300,000.

(発明の効果) 本発明は、シクロヘキシル環を二個有するジエステル等
のA成分へ、分岐を有するポリアルファーオレフィンの
B成分を特定量配合したトラクション用流体であり極め
て高いトラクション係数を有するだけでなく、安価でし
かも粘度特性に優れるものである。
(Effects of the Invention) The present invention is a traction fluid in which component A, such as a diester having two cyclohexyl rings, is blended with a specific amount of component B, which is a branched polyalphaolefin, and not only has an extremely high traction coefficient. It is inexpensive and has excellent viscosity characteristics.

従って、動力伝達装置とくにトラクションドライブ装置
に使用すれば、高負荷時におけるせん断力を飛躍的に増
大できるので装置を小型化できるとともに経済的な装置
を供給しうるという効果がある。
Therefore, when used in a power transmission device, particularly a traction drive device, the shearing force under high loads can be dramatically increased, so the device can be miniaturized and an economical device can be provided.

Claims (1)

【特許請求の範囲】 1)一般式 ▲数式、化学式、表等があります▼ [式中、A′は−COO−又は−OOC−のエステル結
合でありnは1〜6、R_1は水素原子、炭素数1〜8
のアルキル基から選択される1種又は2種、R_2は炭
素数1〜3のアルキル基から選択される1種又は2種で
ある]で示されるジエステル化合物またはその誘導体に
、分岐を有するポリアルファ−オレフィンを0.1〜7
0重量%配合したことを特徴とするトラクション流体。 2)ポリアルファ−オレフィンがポリブデンである特許
請求の範囲第1項に記載の流体。 3)ポリアルファ−オレフィンの配合量が10〜50重
量%である特許請求の範囲第1項に記載の流体。 4)ジエステル化合物のR_1が、水素原子、炭素数1
〜4のアルキル基から選択される1種又は2種である特
許請求の範囲第1項に記載の流体。 5)ポリアルファ−オレフィンの平均分子量が、500
〜10,000である特許請求の範囲第1項に記載の流
体。 6)ジエステル化合物のnが1〜3である特許請求の範
囲第1項に記載の流体。 7)ジエステルのR_2が、メチル基である特許請求の
範囲第1項に記載の流体。
[Claims] 1) General formula ▲ Numerical formula, chemical formula, table, etc. ▼ [In the formula, A' is an ester bond of -COO- or -OOC-, n is 1 to 6, R_1 is a hydrogen atom, Carbon number 1-8
and R_2 is one or two selected from alkyl groups having 1 to 3 carbon atoms. -Olefin from 0.1 to 7
A traction fluid characterized by containing 0% by weight. 2) The fluid according to claim 1, wherein the polyalpha-olefin is polybutene. 3) The fluid according to claim 1, wherein the amount of polyalpha-olefin is 10 to 50% by weight. 4) R_1 of the diester compound is a hydrogen atom and has 1 carbon number
The fluid according to claim 1, wherein the fluid is one or two selected from the group consisting of -4 alkyl groups. 5) The average molecular weight of the polyalpha-olefin is 500
10,000 to 10,000. 6) The fluid according to claim 1, wherein n of the diester compound is 1 to 3. 7) The fluid according to claim 1, wherein R_2 of the diester is a methyl group.
JP60294424A 1985-12-27 1985-12-27 Fluid for Traction Expired - Lifetime JPH0631374B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP60294424A JPH0631374B2 (en) 1985-12-27 1985-12-27 Fluid for Traction
PCT/JP1987/000435 WO1988010293A1 (en) 1985-12-27 1987-06-26 Traction fluid
EP87904127A EP0344307B1 (en) 1985-12-27 1987-06-26 Traction fluid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60294424A JPH0631374B2 (en) 1985-12-27 1985-12-27 Fluid for Traction

Publications (2)

Publication Number Publication Date
JPS62153395A true JPS62153395A (en) 1987-07-08
JPH0631374B2 JPH0631374B2 (en) 1994-04-27

Family

ID=17807579

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60294424A Expired - Lifetime JPH0631374B2 (en) 1985-12-27 1985-12-27 Fluid for Traction

Country Status (3)

Country Link
EP (1) EP0344307B1 (en)
JP (1) JPH0631374B2 (en)
WO (1) WO1988010293A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
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EP0344307A1 (en) * 1985-12-27 1989-12-06 Tonen Corporation Traction fluid
JPWO2004026998A1 (en) * 2002-09-18 2006-01-19 出光興産株式会社 Fluid composition for traction drive
JP2018095840A (en) * 2016-12-13 2018-06-21 花王株式会社 Lubricant base oil, and lubricant composition including the same
WO2018110142A1 (en) * 2016-12-13 2018-06-21 花王株式会社 Lubricant base oil and lubricant composition including said lubricant base oil
WO2020080269A1 (en) * 2018-10-19 2020-04-23 新日本理化株式会社 Power transmission lubricant oil base oil
JP2020180284A (en) * 2019-04-24 2020-11-05 Eneos株式会社 Lubricant composition and method for producing the same

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JPH0631374B2 (en) * 1985-12-27 1994-04-27 東燃株式会社 Fluid for Traction
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JPS59191797A (en) * 1983-04-14 1984-10-30 Nippon Petrochem Co Ltd Fluid for traction drive

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0344307A1 (en) * 1985-12-27 1989-12-06 Tonen Corporation Traction fluid
JPWO2004026998A1 (en) * 2002-09-18 2006-01-19 出光興産株式会社 Fluid composition for traction drive
JP4521275B2 (en) * 2002-09-18 2010-08-11 出光興産株式会社 Fluid composition for traction drive
JP2018095840A (en) * 2016-12-13 2018-06-21 花王株式会社 Lubricant base oil, and lubricant composition including the same
WO2018110142A1 (en) * 2016-12-13 2018-06-21 花王株式会社 Lubricant base oil and lubricant composition including said lubricant base oil
CN110036095A (en) * 2016-12-13 2019-07-19 花王株式会社 Lube base oil and lubricant oil composite containing the lube base oil
US10745635B2 (en) 2016-12-13 2020-08-18 Kao Corporation Lubricant base oil and lubricant composition including said lubricant base oil
WO2020080269A1 (en) * 2018-10-19 2020-04-23 新日本理化株式会社 Power transmission lubricant oil base oil
JPWO2020080269A1 (en) * 2018-10-19 2021-09-09 新日本理化株式会社 Lubricating oil for power transmission Base oil
US11414615B2 (en) 2018-10-19 2022-08-16 New Japan Chemical Co., Ltd. Power transmission lubricant oil base oil
JP2020180284A (en) * 2019-04-24 2020-11-05 Eneos株式会社 Lubricant composition and method for producing the same

Also Published As

Publication number Publication date
EP0344307B1 (en) 1993-08-11
EP0344307A4 (en) 1989-08-09
JPH0631374B2 (en) 1994-04-27
EP0344307A1 (en) 1989-12-06
WO1988010293A1 (en) 1988-12-29

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