JP2006083382A - Improved viscosity control agent for lubricant oil composition - Google Patents

Improved viscosity control agent for lubricant oil composition Download PDF

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JP2006083382A
JP2006083382A JP2005242400A JP2005242400A JP2006083382A JP 2006083382 A JP2006083382 A JP 2006083382A JP 2005242400 A JP2005242400 A JP 2005242400A JP 2005242400 A JP2005242400 A JP 2005242400A JP 2006083382 A JP2006083382 A JP 2006083382A
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lubricating oil
shear
additive
oil composition
lubricating
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Sanjay Srinivasan
サンジヤイ・スリニバサン
Yoon Soo Song
ヨーン・スー・ソング
Joseph Stephen Strukl
ジヨセフ・スチーブン・ストラクル
Peter Growcott
ピーター・グローコツト
Paul G Griffin
ポール・ジー・グリフイン
Akhilesh Duggal
アキレシユ・ダガル
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Afton Chemical Corp
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    • C10M171/00Lubricating compositions characterised by purely physical criteria, e.g. containing as base-material, thickener or additive, ingredients which are characterised exclusively by their numerically specified physical properties, i.e. containing ingredients which are physically well-defined but for which the chemical nature is either unspecified or only very vaguely indicated
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an improved lubricant oil, lubricant oil composition and additives therefor, and lubricated parts and engines, and also to provide a method for lubricating movable parts. <P>SOLUTION: The lubricant oil composition comprises a lubricating viscous base oil and about 5-30 wt.% of an additive containing a shear stable olefin copolymer derived from a copolymer having a number average molecular weight of about 50,000-250,000. The shear stable olefin copolymer has about 40 or lower shear stability index, a multi-dispersibility of about 1.5 or lower, a concentration efficacy of about 1.8 or more, and it can improve a viscosity index of the composition. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

潤滑油、潤滑油組成物および潤滑油添加剤、潤滑させた部品およびエンジン、ならびに可動部を潤滑させる方法について、以下に開示する。   A lubricating oil, lubricating oil composition and lubricating oil additive, lubricated parts and engine, and method for lubricating moving parts are disclosed below.

ガソリンおよびディーゼルエンジンのクランク室に使用する潤滑油には、天然および/または合成ベースストックと、潤滑油に求められる特性を与えるために1つまたは複数の添加剤とが含まれる。一般に、そのような添加剤として、無灰性分散剤、金属清浄剤、抗酸化剤、および磨耗防止剤があげられ、これらを混合しパッケージ型添加剤とすることができる。そのような添加剤は、DIパッケージ(detergent inhibitor package:清浄剤・抑制剤パッケージ)と呼ばれることがある。   Lubricating oils used in the crankcases of gasoline and diesel engines include natural and / or synthetic base stocks and one or more additives to provide the properties required for the lubricating oil. In general, such additives include ashless dispersants, metal detergents, antioxidants, and antiwear agents, which can be mixed into a package type additive. Such an additive is sometimes called a DI package (detergent inhibitor package).

マルチグレードオイルは、通常、比較的長鎖のポリマーである1つまたは複数の摩擦調節剤をさらに含有する。そのようなポリマーは、その他の特徴をもたせるために多機能化することができ、多機能性摩擦調節剤として知られているが、主として所望の作用温度の範囲にわたり、粘度特性を向上させる作用がある。粘度調節剤は、低温で粘度を過度に増加させることなく、高温で粘度を増加させ、高速におけるエンジンをさらに保護する作用がある。低温での粘度増加は、冷えたエンジンの始動を困難にする。高温での性能は、通常、100℃における動粘度(kV:kinematic viscosity)(ASTM D445)を用いて測定し、低温での性能は、コールドクランキングシュミレーター(CCS:colod cranking siumlator)粘度(ASTM D2602が改訂されたASTM D5293)、ミニロータリー粘度計(MRV:mini−rotary viscometer;ASTM D4684)、または走査型ブルックフィールドもしくはゲル指数(ASTM D5133)を用いて測定する。   Multigrade oils typically further contain one or more friction modifiers that are relatively long chain polymers. Such polymers can be multi-functionalized to provide other characteristics and are known as multi-functional friction modifiers, but have the effect of improving viscosity characteristics primarily over a range of desired operating temperatures. is there. The viscosity modifier increases the viscosity at a high temperature without excessively increasing the viscosity at a low temperature, and has an effect of further protecting the engine at a high speed. Increased viscosity at low temperatures makes it difficult to start a cold engine. Performance at high temperatures is typically measured using kinematic viscosity (kV) (ASTM D445) at 100 ° C., and performance at low temperatures is measured by cold cranking simulator (CCS) viscosity (ASTM D2602). ASTM D5293), a mini-rotary viscometer (MRV: ASTM D4684), or a scanning Brookfield or gel index (ASTM D5133).

粘度分類は、前述の温度別測定結果に基づいて、SAE(Society of Automotive Engineers:米国自動車技術者協会)の分類方法(SAE J300)によって、定義されている。マルチグレードオイルは、低温および高温での両性能要件を満たし、対応する両方の分類が表示される。   The viscosity classification is defined by the classification method (SAE J300) of SAE (Society of Automotive Engineers) based on the above-described measurement results by temperature. Multigrade oils meet both low and high temperature performance requirements and display both corresponding classifications.

剪断安定性とは、オイルが大きな剪断作用を受けた際の永久的粘度低下に対する抵抗性の尺度である――オイルの剪断安定性が優れているほど、剪断作用を受けた場合の粘度低下が少ない。ポリマー性粘度調節剤は、100℃におけるkVを著しく向上させるが、必ずしも剪断安定性に優れているとは限らない。そのようなポリマー性粘度調節剤は、剪断安定度指数(SSI:shear stability index)によって、特徴づけられる。   Shear stability is a measure of the resistance to permanent viscosity loss when the oil is subjected to a large shearing action-the better the oil's shear stability, the lower the viscosity when subjected to shearing action. Few. Polymeric viscosity modifiers significantly improve kV at 100 ° C., but are not necessarily excellent in shear stability. Such polymeric viscosity modifiers are characterized by a shear stability index (SSI).

比較的優れた剪断安定性を示すオイルまたは添加剤は、比較的低いSSIを有する。一般的に、潤滑油に使用される高分子量ポリマーは、剪断安定性が低い(すなわちSSIが高い)。しかし、比較的低いSSIを有する粘度調節剤は、比較的分子量が低いために高い処理濃度が要求され、そのため総配合コストの増加につながる。マルチグレードオイルは、低SSIを有する高価な粘度調節剤を使用しない限り、剪断安定性が低いことが多い。剪断安定性が低い場合、複数のオイルを混ぜ合わせ、100℃におけるkVを向上させる必要があるが、オイルの混合により燃費が低下する恐れがある。したがって、潤滑油組成物中に使用する剪断安定性が比較的優れ、かつより安価な粘度調節剤を得るために粘度調節剤を改良する必要がある。   Oils or additives that exhibit relatively good shear stability have a relatively low SSI. In general, high molecular weight polymers used in lubricating oils have low shear stability (ie, high SSI). However, viscosity modifiers having a relatively low SSI require a high processing concentration due to their relatively low molecular weight, thus leading to an increase in total formulation cost. Multigrade oils often have low shear stability unless expensive viscosity modifiers with low SSI are used. When the shear stability is low, it is necessary to mix a plurality of oils to improve the kV at 100 ° C., but there is a possibility that the fuel consumption may be reduced by mixing the oils. Therefore, it is necessary to improve the viscosity modifier in order to obtain a viscosity modifier that is relatively excellent in shear stability and used at lower cost.

実施形態の概要Outline of the embodiment

本明細書の1つの実施形態において、潤滑表面を提示する。潤滑表面は、潤滑粘性の基油と、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した、剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%とを含有する潤滑油組成物の薄膜による被覆を含む。剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数を有し、多分散性が約1.5以下で、濃化効率が約1.8を上回る。   In one embodiment herein, a lubricating surface is presented. Lubricating surface is an additive comprising a shear-stable olefin copolymer, derived from a base oil of lubricating viscosity and a copolymer having a number average molecular weight in the range of about 50,000-250,000, about 5-30 Coating with a thin film of a lubricating oil composition containing: The shear stable olefin copolymer has a shear stability index of less than about 40, a polydispersity of about 1.5 or less, and a thickening efficiency of greater than about 1.8.

別の実施形態では、可動部を有し、可動部を潤滑させるための潤滑油を含有する輸送手
段を提示する。潤滑油は、潤滑粘性の油と、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した、剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%とを含有する。剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数を有し、多分散性が約1.5以下で、濃化効率が約1.8を上回る。
In another embodiment, a vehicle having a moving part and containing lubricating oil for lubricating the moving part is presented. The lubricating oil is an additive comprising a shear stable olefin copolymer, derived from an oil of lubricating viscosity and a copolymer having a number average molecular weight in the range of about 50,000 to 250,000, about 5-30 wt. %. The shear stable olefin copolymer has a shear stability index of less than about 40, a polydispersity of about 1.5 or less, and a thickening efficiency of greater than about 1.8.

さらに別の実施形態では、可動部を潤滑させる方法を提示する。この方法は、可動部を、潤滑油添加剤を含有する潤滑油組成物に接触させるステップを含む。潤滑油添加剤は、希釈用または担体としてのオイルと、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した、剪断安定性オレフィン共重合体、約5〜95重量%とを含む。剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数を有し、多分散性が約1.5以下で、濃化効率が約1.8を上回る。潤滑油組成物は、潤滑油組成物の全体量に関して約5〜30重量%の添加剤を含有する。   In yet another embodiment, a method for lubricating a moving part is presented. The method includes contacting the moving part with a lubricating oil composition containing a lubricating oil additive. The lubricating oil additive is a shear stable olefin copolymer, from about 5 to 95, derived from a diluent or carrier oil and a copolymer having a number average molecular weight in the range of about 50,000 to 250,000. Weight percent. The shear stable olefin copolymer has a shear stability index of less than about 40, a polydispersity of about 1.5 or less, and a thickening efficiency of greater than about 1.8. The lubricating oil composition contains about 5-30% by weight of the additive with respect to the total amount of the lubricating oil composition.

その上さらに別の実施形態では、潤滑油組成物の粘度指数を改善する方法を開示する。この方法は、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した、剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%を、潤滑油組成物と混合するステップを含む。剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数を有し、多分散性が約1.5以下で、濃化効率が約1.8を上回る。   In yet another embodiment, a method for improving the viscosity index of a lubricating oil composition is disclosed. The method comprises adding about 5-30% by weight of an additive comprising a shear stable olefin copolymer, derived from a copolymer having a number average molecular weight in the range of about 50,000 to 250,000, to a lubricating oil composition. Mixing with the product. The shear stable olefin copolymer has a shear stability index of less than about 40, a polydispersity of about 1.5 or less, and a thickening efficiency of greater than about 1.8.

本明細書に記載するように、剪断安定性共重合体は、添加量が少ない場合でも濃化効率が向上するという点で優れている。剪断安定性共重合体は、例えば約40〜55重量%の範囲でエチレンを含有する共重合体などの非結晶性エチレン含有低級共重合体を用いて作ることができるという点でも優れている。剪断安定性オレフィン共重合体に加え、本発明は、スチレン‐イソプレン構造の剪断安定性星型ポリマーに応用することもできる。   As described herein, the shear-stable copolymer is excellent in that the concentration efficiency is improved even when the addition amount is small. The shear-stable copolymer is also superior in that it can be made using a non-crystalline ethylene-containing lower copolymer such as a copolymer containing ethylene in the range of about 40 to 55% by weight. In addition to shear-stable olefin copolymers, the present invention can also be applied to shear-stable star polymers having a styrene-isoprene structure.

実施形態のさらなる特徴および利点は、良好な実施形態に関する詳細な説明を、以下の図面とあわせて参照することによって明らかになるであろう。図面中、使用する参照番号は複数の図面間で共通である。   Additional features and advantages of the embodiments will be apparent from the detailed description of the preferred embodiments, taken in conjunction with the following drawings. In the drawings, the reference numbers used are common among a plurality of drawings.

良好な実施形態に関する詳細な説明Detailed description of the preferred embodiment

本明細書中、「ヒドロカルビル置換基」または「ヒドロカルビル基」という用語は、一般に使われる意味で用いられ、当業者には周知である。具体的には、分子の残りの部分に直接付加する炭素原子を有し、圧倒的に炭化水素的な性質を示す基を指す。ヒドロカルビル基の例として、下記のようなものがあげられる:
(1)炭化水素置換基、すなわち脂肪族(例えばアルキルまたはアルケニル)置換基、脂環式(例えばシクロアルキル、シクロアルケニル)置換基、ならびに芳香族置換、脂肪族置換および脂環式置換の芳香族置換基。さらに、環が分子の別の部分で閉じている環式置換基(例えば2つの置換基が結合して脂環式ラジカルを形成する);
(2)置換炭化水素置換基、すなわち炭化水素以外の基を含有する置換基であって、本明細書では、圧倒的に炭化水素的な性質を示す基の性質を変えない置換基(例えばハロ(特にクロロおよびフルオロ)、ヒドロキシ、アルコキシ、メルカプト、アルキルメルカプト、ニトロ、ニトロソおよびスルホキシ);
(3)へテロ置換基、すなわち本明細書では、圧倒的に炭化水素的な性質を示す一方で、炭素原子からなる環または鎖の中に炭素以外の原子を含有する置換基。ヘテロ原子として、イオウ、酸素、窒素、ならびにピリジル、フリル、チエニルおよびイミダゾリルなどの環状の置換基があげられる。一般に、ヒドロカルビル基中の炭素原子10個あたり、炭化水素以外の置換基は2個以下、好ましくは1個以下の割合で存在し、典型的には、ヒドロカルビル基中には炭化水素以外の置換基は存在しない。
In this specification, the terms "hydrocarbyl substituent" or "hydrocarbyl group" are used in a commonly used meaning and are well known to those skilled in the art. Specifically, it refers to a group having a carbon atom that is directly added to the rest of the molecule and that exhibits overwhelming hydrocarbon character. Examples of hydrocarbyl groups include the following:
(1) Hydrocarbon substituents, ie aliphatic (eg alkyl or alkenyl) substituents, alicyclic (eg cycloalkyl, cycloalkenyl) substituents, and aromatic, aliphatic and alicyclic substituted aromatics Substituents. In addition, cyclic substituents in which the ring is closed at another part of the molecule (eg, two substituents combine to form an alicyclic radical);
(2) Substituted hydrocarbon substituents, that is, substituents containing groups other than hydrocarbons, and in this specification, substituents that do not change the properties of groups that are predominantly hydrocarbon-like (for example, halo (Especially chloro and fluoro), hydroxy, alkoxy, mercapto, alkyl mercapto, nitro, nitroso and sulfoxy);
(3) Hetero substituent, that is, a substituent that contains an atom other than carbon in a ring or chain consisting of carbon atoms while exhibiting overwhelming hydrocarbon properties in the present specification. Heteroatoms include sulfur, oxygen, nitrogen, and cyclic substituents such as pyridyl, furyl, thienyl and imidazolyl. Generally, there are no more than 2 and preferably no more than 1 substituent per hydrocarbon atom per 10 carbon atoms in the hydrocarbyl group, typically in the hydrocarbyl group a substituent other than hydrocarbon. Does not exist.

本発明の実施形態はいずれも、特定の潤滑油成分、すなわち添加剤を提供する。この添加剤は、一般に、多機能性粘度指数調節剤と呼ばれる。具体的には、この潤滑油添加剤は、約15,000から約500,000以上の範囲の数平均分子量を有する共重合体から誘導した、剪断安定性オレフィン共重合体を含む。剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数を有し、多分散性が約1.5以下であることができる。本明
細書に記載するように、この剪断安定性オレフィン共重合体を、Solvent Neutral 150のような適当な溶剤に溶解させ、添加剤成分を得る。
All embodiments of the present invention provide specific lubricating oil components, or additives. This additive is generally called a multifunctional viscosity index modifier. Specifically, the lubricating oil additive comprises a shear stable olefin copolymer derived from a copolymer having a number average molecular weight in the range of about 15,000 to about 500,000 or more. The shear stable olefin copolymer can have a shear stability index of less than about 40 and a polydispersity of about 1.5 or less. As described herein, the shear stable olefin copolymer is dissolved in a suitable solvent such as Solvent Neutral 150 to obtain the additive component.

多様な共重合体および3元重合体を、本発明の剪断安定性共重合体を形成するための出発物質として使うことができる。本発明の共重合体は、通常、オレフィン共重合体を指すが、開示の実施形態は、スチレン‐イソプレンから誘導した共重合体にも応用することができる。本発明の共重合体は、一般に、約15,000〜500,000、好ましくは約20,000〜300,000、より好ましくは約100,000〜200,000の数平均分子量を有する。本発明の剪断安定性共重合体は、通常、狭い範囲の分子量を有し、これは数平均分子量(Mn)に対する重量平均分子量(Mw)の比(以下、多分散性と呼ぶ)として求められる。適切なオレフィン共重合体の多分散性は10を下回り、好ましくは7を下回り、より好ましくは、4以下である。共重合体のMnおよびMw/Mnは、周知の方法である蒸気圧浸透圧法(VPO:vapor phase osmometry)、膜浸透圧法、およびゲル浸透クロマトグラフィーによって測定する。オレフィン共重合体から誘導した本発明の剪断安定性共重合体は、約1.5以下の多分散性を有することができる。   A wide variety of copolymers and terpolymers can be used as starting materials to form the shear stable copolymers of the present invention. The copolymers of the present invention typically refer to olefin copolymers, but the disclosed embodiments can also be applied to copolymers derived from styrene-isoprene. The copolymers of the present invention generally have a number average molecular weight of about 15,000 to 500,000, preferably about 20,000 to 300,000, more preferably about 100,000 to 200,000. The shear-stable copolymer of the present invention usually has a narrow range of molecular weight, which is determined as the ratio of the weight average molecular weight (Mw) to the number average molecular weight (Mn) (hereinafter referred to as polydispersity). . Suitable polydispersities of olefin copolymers are less than 10, preferably less than 7, and more preferably 4 or less. The Mn and Mw / Mn of the copolymer are measured by the well-known methods of vapor pressure osmometry (VPO: vapor phase osmometry), membrane osmometry, and gel permeation chromatography. The shear-stable copolymers of the present invention derived from olefin copolymers can have a polydispersity of about 1.5 or less.

通常、狭い範囲の分子量を有する剪断安定性共重合体は、比較的低温で、機械的に剪断することによって得ることができる。従来からの共重合体剪断法は、約100°C(212°F)を上回る温度において押出し剪断を施す。それに対して、本発明の共重合体剪断法は、ホモゲナイザー中で、約100°C(212°F)を下回る温度、通常、約35°C(95°F)〜85°C(135°F)でおこなわれる。したがって、「比較的低温」という表現は、共重合体を剪断するための押出し剪断方法(従来法)に用いられる温度より低い温度を意味する。   Usually, shear-stable copolymers having a narrow range of molecular weight can be obtained by mechanical shearing at relatively low temperatures. Conventional copolymer shearing processes provide extrusion shear at temperatures above about 100 ° C (212 ° F). In contrast, the copolymer shear process of the present invention is performed in a homogenizer at temperatures below about 100 ° C (212 ° F), typically from about 35 ° C (95 ° F) to 85 ° C (135 ° F). ). Thus, the expression “relatively low temperature” means a temperature that is lower than the temperature used in the extrusion shear method (conventional method) for shearing the copolymer.

本法に用いるホモゲナイザーは、500ポンド/平方インチ(35 kg/cm)を超える圧力を発生させることが可能であれば、ホモゲナイザーの種類は問わない。このようなホモゲナイザー内で、前記圧力が開放されるときに強力な剪断作用が生成物に及ぶことになる。使用することができる典型的なホモゲナイザーは、乳製品の均質化や、研磨剤、化粧品、医薬品および液体洗剤として使われるエマルションの調製に使用する従来からあるホモゲナイザーである。共重合体をホモゲナイザーで複数回(例えば約2〜10回)処理して、共重合体の剪断をおこなうことができる。 The homogenizer used in this method is not limited as long as it can generate a pressure exceeding 500 pounds per square inch (35 kg / cm 2 ). Within such a homogenizer, a strong shearing action will be exerted on the product when the pressure is released. Typical homogenizers that can be used are conventional homogenizers used to homogenize dairy products and to prepare emulsions used as abrasives, cosmetics, pharmaceuticals and liquid detergents. The copolymer can be sheared by treating the copolymer with a homogenizer a plurality of times (for example, about 2 to 10 times).

ホモゲナイザー内で剪断されるオレフィン共重合体は、エチレン、ならびに3〜28個の炭素原子(例えば2〜18個の炭素原子)を含有する環式、脂環式および非環式化合物をはじめとするエチレン系不飽和炭化水素から調製することができる。エチレン共重合体は、エチレンを約15〜90重量%、好ましくは約30〜80重量%、最も好ましく約70重量%より少ない量で含有することができる。さらに共重合体は、約10〜85重量%、好ましくは20〜70重量%の量で、1つまたは複数のC〜C28、好ましくはC〜C18、より好ましくはC〜C10の不飽和炭化水素、好ましくはα‐オレフィンを含有することができる。 Olefin copolymers sheared in a homogenizer include ethylene and cyclic, alicyclic and acyclic compounds containing 3 to 28 carbon atoms (eg 2 to 18 carbon atoms). It can be prepared from ethylenically unsaturated hydrocarbons. The ethylene copolymer can contain ethylene in an amount of about 15-90% by weight, preferably about 30-80% by weight, most preferably less than about 70% by weight. Furthermore copolymer, about 10 to 85 wt%, preferably in an amount of 20 to 70 wt%, one or more C 3 -C 28, preferably C 3 -C 18, more preferably C 3 -C It can contain 10 unsaturated hydrocarbons, preferably α-olefins.

エチレンとプロピレンとからなる共重合体が最も好ましい。しかしその他に、プロピレンに代わり共重合体を形成することができるα−オレフィン、またはエチレンおよびプロピレンと組み合わせて用い3元重合体、4元重合体などを形成することができるα−オレフィンがある。例として、これらに限定されるわけではないが、1−ペンテン、1−ヘキセン、1−ヘプテン、1−オクテン、1−ノネン、1−デセンなど、さらに、4−メチル−1−ペンテン、4−メチル−1−ヘキセン、5−メチルペンテン−1,4,4−ジメチル−1−ペンテン、6−メチルヘプテン−1などの分枝鎖状α‐オレフィン、およびこれらの混合物があげられる。   Most preferred is a copolymer of ethylene and propylene. However, there are other α-olefins that can form copolymers instead of propylene, or α-olefins that can be used in combination with ethylene and propylene to form terpolymers and quaternary polymers. Examples include, but are not limited to, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, and the like, and 4-methyl-1-pentene, 4- Examples thereof include branched α-olefins such as methyl-1-hexene, 5-methylpentene-1,4,4-dimethyl-1-pentene, and 6-methylheptene-1, and mixtures thereof.

本明細書中、「共重合体」という用語は、別途明示しない限り、エチレン、およびC3〜28α−オレフィン、および/または非共役ジオレフィンもしくは使用可能なそれらのジオレフィンの混合物からなる3元重合体、4元重合体、共重合体などを含む。このような材料は、本発明のオレフィン共重合体の基本的特徴を物理的に変えない限り、若干量のその他のオレフィン系モノマーを含有することができる。非共役ジオレフィンの量は、一
般に、存在するエチレンおよびα‐オレフィンの総量に関し約0.5〜20モル%、好ましくは約1〜7モル%の範囲である。
In this specification, the term “copolymer”, unless stated otherwise, consists of ethylene and C 3 -28 α-olefins and / or non-conjugated diolefins or mixtures of those diolefins that can be used 3. Including terpolymer, quaternary polymer, copolymer and the like. Such materials can contain some amount of other olefinic monomers as long as the basic characteristics of the olefin copolymer of the present invention are not physically altered. The amount of non-conjugated diolefin is generally in the range of about 0.5 to 20 mole percent, preferably about 1 to 7 mole percent, based on the total amount of ethylene and α-olefin present.

3元重合体に含むことができる非共役ジエンの代表例として、以下のようなものがあげられる:1,4−ヘキサジエン、1,5−ヘプタジエン、1,6−オクタジエンなどの直鎖非環式ジエン;5−メチル−1,4−ヘキサジエン、3,7−ジメチル−1,6−オクタジエン、3,7−ジメチル−1,7−オクタジエンなどの分枝鎖状非環式ジエン;ジヒドロミルセンおよびジヒドロシメンの異性体混合物;1,4−シクロヘキサジエン、1,5−シクロオクタジエン、1,5−シクロドデカジエン、4−ビニルシクロヘキセン、1−アリル−4−イソプロピリデンシクロへキサン、3−アリルシクロペンテン、4−アリルシクロヘキセン、1−イソプロペニル−4−(4−ブテニル)シクロヘキサンなどの単環脂環式ジエン;4,4−ジシクロペンテニルジエンおよび4,4−ジシクロヘキセニルジエンなどの複単環脂環式ジエン;テトラヒドロインデン、メチルテトラヒドロインデン、ジシクロペンタジエン、ビシクロ[2.2.1]ヘプタ−2,5−ジエンなどの複環脂環式融合および橋かけ環ジエン;エチルノルボルネン、5−メチレン−6−メチル−2−ノルボルネン、5−メチレン−6,6−ジメチル−2−ノルボルネン、5−プロペニル−2−ノルボルネン、5−(3−シクロペンテニル)−2−ノルボルネン、5−シクロヘキシリデン−2−ノルボルネン、ノルボルナジエンなどのアルキル、アルケニル、アルキリデン、シクロアルケニルおよびシクロアルキリデンノルボルネン。   Typical examples of non-conjugated dienes that can be included in the terpolymer include the following: linear acyclic such as 1,4-hexadiene, 1,5-heptadiene, 1,6-octadiene Dienes; branched acyclic dienes such as 5-methyl-1,4-hexadiene, 3,7-dimethyl-1,6-octadiene, 3,7-dimethyl-1,7-octadiene; dihydromyrcene and Dihydrocymene isomer mixture; 1,4-cyclohexadiene, 1,5-cyclooctadiene, 1,5-cyclododecadiene, 4-vinylcyclohexene, 1-allyl-4-isopropylidenecyclohexane, 3-allyl Monocyclic alicyclic dienes such as cyclopentene, 4-allylcyclohexene, 1-isopropenyl-4- (4-butenyl) cyclohexane; 4,4-disi Bimonocyclic alicyclic dienes such as lopentenyl diene and 4,4-dicyclohexenyl diene; such as tetrahydroindene, methyltetrahydroindene, dicyclopentadiene, bicyclo [2.2.1] hepta-2,5-diene Polycyclic alicyclic fused and bridged ring dienes; ethyl norbornene, 5-methylene-6-methyl-2-norbornene, 5-methylene-6,6-dimethyl-2-norbornene, 5-propenyl-2-norbornene, 5 -(3-Cyclopentenyl) -2-norbornene, 5-cyclohexylidene-2-norbornene, alkyl such as norbornadiene, alkenyl, alkylidene, cycloalkenyl and cycloalkylidene norbornene.

具体的には、剪断安定性オレフィン共重合体は、エチレン‐プロピレン、エチレン‐プロピレン‐ジエン、スチレン‐ネオプレン、スチレン‐イソプレンなどの複数単量体の重合反応物から誘導することができる。   Specifically, the shear stable olefin copolymer may be derived from a multi-monomer polymerization reaction product such as ethylene-propylene, ethylene-propylene-diene, styrene-neoprene, styrene-isoprene.

エチレン‐プロピレン、またはこれより炭素数の多いα‐オレフィン共重合体は、約15〜80重量%のエチレンと、約85〜20重量%のC〜C23α‐オレフィンとから構成される。これらの割合は、好ましくはエチレンが約35〜75重量%、C〜C23α‐オレフィンが約65〜25重量%、より好ましくはエチレンが約50〜70重量%、C〜C23α‐オレフィンが約50〜30重量%、最も好ましくはエチレンが約55〜65重量%、C〜C23α‐オレフィンが約45〜35重量%である。 The ethylene-propylene or higher α-olefin copolymer is composed of about 15 to 80% by weight of ethylene and about 85 to 20% by weight of C 3 to C 23 α-olefin. These proportions are preferably about 35 to 75% by weight of ethylene, about 65 to 25% by weight of C 3 to C 23 α-olefin, more preferably about 50 to 70% by weight of ethylene, C 3 to C 23 α. - olefin of about 50 to 30 wt%, and most preferably ethylene about 55 to 65 wt%, C 3 -C 23 alpha-olefin is about 45 to 35 wt%.

さらに、本明細書に記載の剪断安定性オレフィン共重合体を作るためのオレフィン共重合体には、フリーラジカルグラフト反応またはグラフト重合によって官能基を付与されたオレフィン共重合体も含まれる。そのようなグラフト共重合体自体は、当業者には周知である。   Furthermore, the olefin copolymers for making the shear-stable olefin copolymers described herein also include olefin copolymers that have been functionalized by free radical grafting or graft polymerization. Such graft copolymers themselves are well known to those skilled in the art.

オレフィン共重合体に官能基を付与するためのグラフト単量体は、無水マレイン酸、アクリル酸、メタクリル酸、またはそれらのエステルなどのオレフィン系不飽和カルボキシル基含有モノマーの誘導体である。これらもまた当業者に周知である。一般に、アクリル酸およびメタクリル酸誘導体は、4〜16個の炭素原子を含有する。特に好ましいアクリルまたはメタクリル系グラフト単量体として、メタクリル酸グリシジル、メタクル酸塩、メタクリル酸メチル、メタクリル酸エチル、メタクリル酸アミノプロピル、およびアクリルアミドがあげられる。   The graft monomer for imparting a functional group to the olefin copolymer is a derivative of an olefinic unsaturated carboxyl group-containing monomer such as maleic anhydride, acrylic acid, methacrylic acid, or an ester thereof. These are also well known to those skilled in the art. Generally, acrylic acid and methacrylic acid derivatives contain 4 to 16 carbon atoms. Particularly preferred acrylic or methacrylic graft monomers include glycidyl methacrylate, methacrylate, methyl methacrylate, ethyl methacrylate, aminopropyl methacrylate, and acrylamide.

炭素原子2〜25個を含有するビニルアミン(好ましくは複素環ビニルアミン)は、オレフィン共重合体に官能基を付与するために使用することができる別の種類のグラフト単量体である。そのようなアミン自体は、官能基付与グラフト単量体として知られており、アリルアミン、N−ビニルピリジン、N−ビニルピロリドン、ビニルラクタム、ビニルカルバゾール、ビニルイミダゾール、およびビニルチアゾールが含まれ、具体例として、2−ビニルピリジン、N−ビニルピロリドン、ビニルカプロラクタム、1−ビニルイミダゾール、アリルアミン、4−メチル−5−ビニルチアゾール、および9−ビニルカルバゾールがあげられる。そのようなグラフト単量体は、米国特許第4,340,689号に詳細に記載されており、これは本明細書に参照文献として組み込まれている。   Vinylamines containing 2 to 25 carbon atoms (preferably heterocyclic vinylamines) are another type of grafting monomer that can be used to impart functional groups to olefin copolymers. Such amines themselves are known as functionalized graft monomers and include allylamine, N-vinyl pyridine, N-vinyl pyrrolidone, vinyl lactam, vinyl carbazole, vinyl imidazole, and vinyl thiazole, specific examples 2-vinylpyridine, N-vinylpyrrolidone, vinylcaprolactam, 1-vinylimidazole, allylamine, 4-methyl-5-vinylthiazole, and 9-vinylcarbazole. Such graft monomers are described in detail in US Pat. No. 4,340,689, which is incorporated herein by reference.

オレフィン共重合体に官能基を付与するのに適すると先行技術文献に記載されているその他のビニル単量体も、同様に、本発明を実施するにあたって使用できることが、当業者には理解されるであろう。そのようなさらに別のビニル化合物は、ビニルシランおよびビ
ニルベンジルハロゲン化物などであり、具体例として、ビニルトリメトキシシラン、ビニルジエチルクロロシラン、ビニルベンジルクロリドなどがあげられる。適切なシラングラフト単量体は、米国特許第4,340,689号にさらに詳細に記載されており、これは本明細書に参照文献として組み込まれている。
Those skilled in the art will appreciate that other vinyl monomers described in the prior art documents as suitable for imparting functional groups to the olefin copolymer can also be used in the practice of this invention. Will. Such further vinyl compounds are vinyl silane and vinyl benzyl halide, and specific examples include vinyl trimethoxy silane, vinyl diethyl chloro silane, vinyl benzyl chloride and the like. Suitable silane grafting monomers are described in more detail in US Pat. No. 4,340,689, which is incorporated herein by reference.

本明細書に記載の剪断安定性オレフィン共重合体は、好都合に潤滑油組成物に組み入れられる。剪断安定性オレフィン共重合体は、潤滑油組成物に直接添加することできる。しかし、ある実施形態では、鉱油、合成油(例えばジカルボン酸のエステル)、ナフサ、アルキル化(例えばC10〜C13アルキル)ベンゼン、トルエン、またはキシレンなどの実質的に不活性で、通常は液体の有機希釈液を用い、この共重合体を希釈し、添加剤濃縮物を形成する。剪断安定性オレフィン共重合体濃縮物は、通常、約0〜99重量%の希釈油を含有する。 The shear stable olefin copolymers described herein are conveniently incorporated into the lubricating oil composition. The shear stable olefin copolymer can be added directly to the lubricating oil composition. However, in some embodiments, a substantially inert, usually liquid, such as mineral oil, synthetic oil (eg, an ester of a dicarboxylic acid), naphtha, alkylated (eg, C 10 -C 13 alkyl) benzene, toluene, or xylene. The copolymer is diluted with an organic dilution of to form an additive concentrate. Shear stable olefin copolymer concentrates usually contain about 0-99% by weight diluent oil.

潤滑油配合物の調製において、添加剤を、鉱油系潤滑油やその他の適切な溶剤などの炭化水素油中に1〜99重量%の有効成分を有する濃縮物の形態で導入するのが、通常の方法である。通常、パッケージ型添加剤(additive package)1重量部に対し潤滑油0.05〜10重量部を、これらの濃縮物に加え、クランク室モーターオイルなどの潤滑油の完成品を得る。当然のことながら、最終混合物中への溶解または分散を容易にし、かつ種々の材料の取り扱いにまつわる煩雑さを減らす目的で、濃縮物とする。   In the preparation of lubricating oil formulations, it is common to introduce the additive in the form of a concentrate having from 1 to 99% by weight of the active ingredient in a hydrocarbon oil such as a mineral-based lubricating oil or other suitable solvent. It is a method. Usually, 0.05 to 10 parts by weight of lubricating oil per 1 part by weight of package type additive (additive package) is added to these concentrates to obtain a finished product of lubricating oil such as crankcase motor oil. As a matter of course, the concentrate is used for the purpose of facilitating dissolution or dispersion in the final mixture and reducing the complexity associated with handling various materials.

上記の剪断安定性オレフィン共重合体を用いて調整した潤滑油組成物は、非常に広範な適用例で使用される。圧縮点火エンジンおよびスパーク点火エンジンに対しては、潤滑油組成物が公表されているGF−4またはAPI−CI−4基準を満たすか上回るのが好ましい。上記のGF−4またはAPI−CI−4基準に基づく潤滑油組成物は、潤滑油の完成品を提供するための基油および潤滑油用パッケージ型添加剤を含んでいる。ここに開示する潤滑油の基油は、天然潤滑油、合成潤滑油、およびそれらの混合物から選ばれた潤滑粘性の油である。そのような基油には、自動車用およびトラック用エンジン、ならびに船舶用および鉄道用ディーゼルエンジンなどのようなスパーク点火および圧縮点火内燃機関のためのクランク室潤滑油として従来から使われている基油が含まれる。   Lubricating oil compositions prepared using the above shear stable olefin copolymers are used in a very wide range of applications. For compression ignition and spark ignition engines, it is preferred that the lubricating oil composition meets or exceeds the published GF-4 or API-CI-4 standards. Lubricating oil compositions based on the above GF-4 or API-CI-4 standards contain a base oil and a lubricating oil package type additive to provide a finished lubricating oil. The base oil of the lubricating oil disclosed herein is an oil of lubricating viscosity selected from natural lubricating oils, synthetic lubricating oils, and mixtures thereof. Such base oils include those conventionally used as crankcase lubricants for spark ignition and compression ignition internal combustion engines such as automotive and truck engines and marine and railroad diesel engines. Is included.

天然油には、動物油および植物油(例えばヒマシ油、ラード油)、液体石油およびパラフィン系、ナフテン系、および混合パラフィン‐ナフテン系の水素添加精製、溶剤処理、または酸処理鉱油系潤滑油が含まれる。さらに石炭または頁岩から得られる潤滑粘性の油も有用な基油である。本発明に使われる合成潤滑油には、一般に使用される多くの合成炭化水素油のいずれかを含み、例として、これらに限定されるわけではないが、ポリ−α−オレフィン、アルキル化芳香族、アルキレンオキシド重合体、インターポリマー、共重合体、エステル化およびエーテル化などにより末端水酸基が修飾されているこれらの誘導体、ジカルボン酸のエステル、ならびにケイ素からなる油があげられる。   Natural oils include animal and vegetable oils (eg, castor oil, lard oil), liquid petroleum and paraffinic, naphthenic, and mixed paraffin-naphthenic hydrorefining, solvent treatment, or acid treated mineral oils . Oils of lubricating viscosity obtained from coal or shale are also useful base oils. Synthetic lubricating oils used in the present invention include any of a number of commonly used synthetic hydrocarbon oils, including, but not limited to, poly-α-olefins, alkylated aromatics. , Alkylene oxide polymers, interpolymers, copolymers, derivatives thereof whose terminal hydroxyl groups have been modified by esterification and etherification, esters of dicarboxylic acids, and oils of silicon.

潤滑油の完成品は、従来どおり、本明細書では分散剤/抑制剤パッケージ(dispsersant/inhibitor package)またはDIパッケージと呼ぶ、パッケージ型添加剤を含有し、これによって配合剤に求められる特性が与えられる。適切なDIパッケージが、例えば米国特許第5,204,012号および第6,034,040号などに記載されている。パッケージ型添加剤に含まれる添加剤として、清浄剤、分散剤、摩擦調節剤、シール膨張剤(seal swell agent)、抗酸化剤、消泡剤、潤滑剤、防錆剤、腐食防止剤、解乳化剤、および粘度指数向上剤などがある。これらの成分のいくつかは、当業者の間では周知であり、本明細書に記載の添加剤および組成物とともに通常の量で用いるのが望ましい。   The finished lubricants, as before, contain package-type additives, referred to herein as dispersant / inhibitor packages or DI packages, which give the required properties to the formulation. It is done. Suitable DI packages are described, for example, in US Pat. Nos. 5,204,012 and 6,034,040. Additives included in package-type additives include detergents, dispersants, friction modifiers, seal swell agents, antioxidants, antifoaming agents, lubricants, rust inhibitors, corrosion inhibitors, solutions Emulsifiers, viscosity index improvers and the like. Some of these components are well known to those skilled in the art and are desirably used in conventional amounts with the additives and compositions described herein.

例えば、無灰性分散剤は、分散させようとする粒子と結合可能な官能基を有する油溶性ポリマー性炭化水素骨格を含む。通常、このような分散剤は、しばしば橋かけ結合できる基を介してポリマー骨格に結合するアミン、アルコール、アミドまたはエステルの極性を有する部分を備えている。無灰性分散剤は、例えば、長鎖炭化水素置換モノおよびジカルボン酸、またはその無水物の油溶性塩、エステル、アミノエステル、アミド、イミドおよびオキサゾリン;長鎖炭化水素のチオカルボン酸塩誘導体;ポリアミンが直接結合している長鎖脂肪族炭化水素;ならびに長鎖置換フェノールをホルムアルデヒドおよびポリアル
キレンポリアミンと縮合させることによって形成するマンニッヒ縮合生成物から選ぶことができる。
For example, the ashless dispersant includes an oil-soluble polymeric hydrocarbon skeleton having a functional group capable of binding to the particles to be dispersed. Typically, such dispersants comprise an amine, alcohol, amide or ester polar moiety that is attached to the polymer backbone, often through groups that can be cross-linked. Ashless dispersants include, for example, oil-soluble salts, esters, aminoesters, amides, imides and oxazolines of long-chain hydrocarbon-substituted mono- and dicarboxylic acids or anhydrides; thiocarboxylate derivatives of long-chain hydrocarbons; polyamines Can be selected from Mannich condensation products formed by condensing long chain substituted hydrocarbons with formaldehyde and polyalkylene polyamines.

酸化防止剤または抗酸化剤は、ベースストックの使用中の劣化を抑える。その劣化は、スラッジおよび金属表面のワニス様沈殿物などの酸化生成物、ならびに粘度の上昇として認められる。そのような酸化防止剤として、立体障害性基を有するフェノール、好ましくはC〜C12のアルキル側鎖を有するアルキルフェノールチオエステルのアルカリ土類金属塩、カルシウムノニルフェノールスルフィド、無灰性油溶性フェネートおよび硫化フェネート、リンとイオウ、またはイオウが結合した炭化水素、リン酸エステル、チオカルバミン酸の金属塩、ならびに米国特許第4,867,890号に記載の油溶性銅化合物があげられる。 Antioxidants or antioxidants reduce degradation during use of the base stock. The degradation is observed as oxidation products such as sludge and metal surface varnish-like precipitates, as well as increased viscosity. Such antioxidants include phenols having sterically hindered groups, preferably alkaline earth metal salts of alkylphenol thioesters having C 5 to C 12 alkyl side chains, calcium nonylphenol sulfides, ashless oil-soluble phenates and sulfides. Examples include phenates, phosphorus and sulfur, or hydrocarbons bonded with sulfur, phosphate esters, metal salts of thiocarbamic acid, and oil-soluble copper compounds described in US Pat. No. 4,867,890.

非イオン性ポリオキシアルキレンポリオールおよびそのエステル、ポリオキシアルキレンフェノール、ならびにアニオン性アルキルスルホン酸からなるグループから選択される防錆剤を使うことができる。   Rust inhibitors selected from the group consisting of nonionic polyoxyalkylene polyols and esters thereof, polyoxyalkylene phenols, and anionic alkyl sulfonic acids can be used.

少量の解乳化剤を使用することができる。好ましい解乳化成分は欧州特許第EP330,522号に記載されている。これは、ビス‐エポキシドを反応させて得た付加生成物を有するアルキレンオキシドを多価アルコールと反応させて得られる。解乳化剤は、有効成分が0.1質量%を越えない濃度で使用されなければならない。有効成分0.001〜0.05質量%の処理濃度が便利である。   A small amount of demulsifier can be used. A preferred demulsifying component is described in EP 330,522. This is obtained by reacting an alkylene oxide having an addition product obtained by reacting a bis-epoxide with a polyhydric alcohol. The demulsifier must be used at a concentration where the active ingredient does not exceed 0.1% by weight. A treatment concentration of 0.001 to 0.05 mass% active ingredient is convenient.

流動点降下剤は、潤滑油流動性向上剤としても知られるが、流動体が流れる、すなわち流動体を注ぐことができる最低温度を下げる作用がある。そのような添加剤はよく知られている。流動体の低温流動性を向上させる添加剤の代表例として、C〜C18ジアルキルフマラート/酢酸ビニル共重合体、およびポリアルキルメタクリレートなどがある。 Pour point depressants, also known as lube oil flow improvers, have the effect of lowering the minimum temperature at which the fluid flows, i.e. the fluid can be poured. Such additives are well known. Representative examples of additives that improve the low temperature fluidity of the fluid include C 8 to C 18 dialkyl fumarate / vinyl acetate copolymers and polyalkyl methacrylates.

シリコーン油またはポリジメチルシロキサンなどのポリシロキサン系の泡止め剤をはじめとする多くの化合物によって、泡を抑制することができる。   Foaming can be suppressed by many compounds including anti-foaming agents such as silicone oil or polydimethylsiloxane.

さらに、例えば米国特許第3,794,081号および第4,029,587号に記載のシール膨張剤(seal swell agent)を使うことができる。   Furthermore, for example, seal swell agents described in US Pat. Nos. 3,794,081 and 4,029,587 can be used.

上記の添加剤はそれぞれ、使用にあたっては、機能を発揮する量で用い、潤滑油に所望の特性を与える。したがって、例えば、添加剤が腐食防止剤である場合、この腐食防止剤の機能を発揮する量とは、潤滑油に所望の腐食防止特性を与えるのに十分な量である。一般に、これらの添加剤のそれぞれの濃度は、使用にあたっては、潤滑油組成物の重量に関し上限約20重量%である。潤滑油組成物の重量に関し、ある実施形態では約0.001〜20重量%、および別の実施形態では約0.01〜10重量%である。   In use, each of the above additives is used in an amount that exhibits a function, and imparts desired characteristics to the lubricating oil. Thus, for example, when the additive is a corrosion inhibitor, the amount that exerts the function of the corrosion inhibitor is an amount sufficient to impart the desired corrosion prevention properties to the lubricating oil. Generally, the concentration of each of these additives is, in use, an upper limit of about 20% by weight with respect to the weight of the lubricating oil composition. With respect to the weight of the lubricating oil composition, in one embodiment about 0.001 to 20% by weight, and in another embodiment about 0.01 to 10% by weight.

潤滑油組成物の完成品4種を調製し、これら組成物の粘度および剪断強度を比較した。各潤滑油組成物はそれぞれ、潤滑油組成物に対し11重量%の従来のDIパッケージを含有した。DIパッケージは、清浄剤、分散剤、耐磨耗性添加剤、摩擦調節剤、消泡剤、および抗酸化剤を従来量で含有した。さらに、これらの配合物は、約0.1重量%流動点降下剤、約58〜64重量% 150溶剤系中性オイル、約12〜18重量% 600溶剤系中性オイルを含有した。サンプル1〜3からは、摩擦調節剤として市販されているオレフィン共重合体の特性が得られる。サンプル4からは、本発明により作られた剪断安定性オレフィン共重合体の特性が得られる。
表中、以下の略語を使用する。

VII・・・・・粘度指数改善剤(viscosity index improver)
KV・・・・・動粘度(kinematic viscosity)
CCS・・・・・コールドクランキングシュミレーター(cold cranking simulator)
MRV・・・・・ミニロータリー粘度計(mini rotary viscometer)――ASTM D4684に従い試験を実施
HTHS・・・・・高温高剪断(high temperature high shear)――ASTM D−4683、D−4781、およびD−5481に従い試験を実施
Four finished lubricating oil compositions were prepared and the viscosity and shear strength of these compositions were compared. Each lubricating oil composition contained 11% by weight conventional DI package based on the lubricating oil composition. The DI package contained conventional amounts of detergents, dispersants, anti-wear additives, friction modifiers, antifoam agents, and antioxidants. In addition, these formulations contained about 0.1% by weight pour point depressant, about 58-64% by weight 150 solvent-based neutral oil, about 12-18% by weight 600 solvent-based neutral oil. From samples 1 to 3, the characteristics of an olefin copolymer commercially available as a friction modifier can be obtained. Sample 4 provides the properties of a shear stable olefin copolymer made according to the present invention.
The following abbreviations are used in the table.

VII ... viscosity index improver
KV: kinematic viscosity (kinematic viscosity)
CCS: Cold cranking simulator
MRV—Mini rotary viscometer—performed in accordance with ASTM D4684 HTHS—High temperature high shear—ASTM D-4683, D-4781, and Tested according to D-5481

Figure 2006083382
Figure 2006083382

Figure 2006083382
Figure 2006083382

上記の表1および表2に示すように、サンプル4は、非常に優れた粘度調節剤である。サンプル1〜3に比べ、サンプル4は潤滑油組成物中のポリマー添加量が最も少ない(サンプル1〜3では1.38〜1.69であるのに対し、1.32)。さらに、サンプル4は、剪断安定度指数(SSI)が最も高く、MRV試験およびCCS試験に合格した。一方、サンプル3は、MRV試験および粘度低下試験に不合格であった。全体的に、サンプル4には、市販のエチレン系オレフィン共重合体製品を上回る粘度および剪断強度が認められた。   As shown in Tables 1 and 2 above, Sample 4 is a very good viscosity modifier. Compared to samples 1 to 3, sample 4 has the least amount of polymer in the lubricating oil composition (1.32 versus 1.38 to 1.69 for samples 1 to 3). Furthermore, Sample 4 had the highest shear stability index (SSI) and passed the MRV test and the CCS test. On the other hand, Sample 3 failed the MRV test and the viscosity reduction test. Overall, Sample 4 showed a viscosity and shear strength that exceeded the commercially available ethylene-based olefin copolymer product.

本発明に基づく剪断安定性オレフィン共重合体を作るために、気相クロマトグラフィー(GPC:gas phase chromatography)により測定した数平均分子量179,192および重量平均分子量332,930を有するエチレン‐プロピレン共重合体10重量部と、作業油90重量部とを混合した。この油と共重合体の混合物を、GAULINホモゲナイザーで1〜10回処理し、多分散性が1.5より小さい剪断安定性オレフィン共重合体を得た。   Ethylene-propylene copolymer having a number average molecular weight of 179,192 and a weight average molecular weight of 332,930 measured by gas phase chromatography (GPC) to make a shear stable olefin copolymer according to the present invention 10 parts by weight of the coalescence and 90 parts by weight of working oil were mixed. This mixture of oil and copolymer was treated 1 to 10 times with a GAULIN homogenizer to obtain a shear stable olefin copolymer having a polydispersity of less than 1.5.

ホモゲナイザーによる処理0〜10回後のオレフィン共重合体の特徴を、以下の表および図1〜3に示す。図4および図5は、濃化効率および動粘度について、処理0〜10回後のオレフィン共重合体と、HiTEC(R) 5748およびLUBRIZOL 7077(LZ 7077)(それぞれサンプル6およびサンプル7)とを比較したグラフである。比較は、表に示す粘度を有する対照油中で1%オレフィン共重合体を用いて実施した。サンプルの100℃における動粘度は、約5cStの対照油に各サンプルを1重量%溶解し、熱重量分析(TGA:thermogravimetric analysis)法により評価した(図4)。 The characteristics of the olefin copolymer after 0 to 10 treatments with the homogenizer are shown in the following table and FIGS. 4 and 5 show the olefin copolymer after treatment 0 to 10 times, HiTEC (R) 5748 and LUBRIZOL 7077 (LZ 7077) (sample 6 and sample 7 respectively) with respect to the concentration efficiency and kinematic viscosity. It is the graph compared. The comparison was performed using a 1% olefin copolymer in a control oil having the viscosity shown in the table. The kinematic viscosity at 100 ° C. of the sample was evaluated by a thermogravimetric analysis (TGA) method by dissolving 1% by weight of each sample in a control oil of about 5 cSt (FIG. 4).

Figure 2006083382
Figure 2006083382

Figure 2006083382
Figure 2006083382

上記の表および図1〜5に示すように、共重合体をホモゲナイザーで10回以上処理して調製した剪断安定性共重合体は、剪断安定度指数の基準値(約23)を満たす粘度調節剤(サンプル5)とすることができ、かつ従来のオレフィン共重合体粘度調節剤(サンプル6および7)に比べ、明らかに高い濃化効率を示した(サンプル5)。機械的に剪断することによって、さらに、多分散性が1.5より低い剪断安定性オレフィン共重合体(図3中のサンプル5)を得ることができるという利点もある。   As shown in the above table and FIGS. 1 to 5, the shear-stable copolymer prepared by treating the copolymer 10 times or more with a homogenizer has viscosity adjustment that satisfies the standard value (about 23) of the shear stability index. The sample (sample 5) can be used as an additive, and clearly has a higher concentration efficiency (sample 5) than the conventional olefin copolymer viscosity modifiers (samples 6 and 7). Mechanical shearing also has the advantage that a shear-stable olefin copolymer (sample 5 in FIG. 3) having a polydispersity of less than 1.5 can be obtained.

本明細書の様々な箇所で、いくつかの米国特許を参照した。これらの参照文献は全て、その全体が本明細書に組み込まれていることを明記しておく。   At various places throughout this specification, reference has been made to a number of US patents. It is noted that all of these references are incorporated herein in their entirety.

上記の実施形態は、実際の場面において、かなりの変更を加えることが可能である。したがって、実施形態は、本明細書中の上記の特定の実施例に限定されるものではない。上記の実施形態は、特許法の下における均等物を含む本発明の精神および範囲の内に入るものである。   The above embodiment can be considerably changed in actual situations. Thus, embodiments are not limited to the specific examples described above. The above embodiments are within the spirit and scope of the present invention, including equivalents under the patent law.

特許出願人は、いずれの実施形態も、一般に提供するために開示したわけではなく、開示内容の変更例や改変例が特許請求の範囲に文字どおりおさまらない場合であっても、それらは、均等論の下、特許請求の範囲の一部であるとみなされる。   Applicants did not disclose any embodiment for general provision, and even if changes or modifications to the disclosure do not literally fall within the scope of the claims, they are And is considered to be part of the claims.

本発明の主な態様及び特徴を挙げれば以下のとおりである。
1.潤滑粘性の基油と、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%とを含有する潤滑油組成物の薄膜による被覆を備える潤滑表面であって、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)潤滑表面。
2.潤滑表面が、エンジンの動力伝達路を備える、上記1に記載の潤滑表面。
3.潤滑表面が、内燃機関の内部表面または構成要素を備える、上記1に記載の潤滑表面。
4.潤滑表面が、圧縮点火エンジンの内部表面または構成要素を備える、上記1に記載の
潤滑表面。
5.剪断安定性共重合体が、エチレン‐プロピレンの単量体の組合せ、エチレン‐プロピレン‐ジエンの単量体の組合せ、スチレン‐イソプレンの単量体の組合せ、およびスチレン‐ネオプレンの単量体の組合せからなるグループからから誘導される、上記1に記載の潤滑表面。
6.剪断安定性共重合体が、比較的低温においてホモゲナイズされた共重合体から誘導される、上記1に記載の潤滑表面。
7.剪断安定性共重合体の各単量体単位がそれぞれ、約2〜10個の炭素原子を含有する、上記1に記載の潤滑表面。
8.剪断安定性共重合体が、非結晶性エチレンを備え、エチレン含有量が共重合体の重量の約70%を下回る共重合体を含有する、上記1に記載の潤滑表面。
9.上記1に記載の潤滑表面を備える自動車。
10.可動部を有し、かつ可動部を潤滑させるための潤滑油を含有する輸送手段であって、潤滑油が、潤滑粘性の基油と、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%とを備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油中の添加剤の量は、潤滑油の全量に関する量である)輸送手段。
11.剪断安定性共重合体が、エチレン‐プロピレンの単量体の組合せ、エチレン‐プロピレン‐ジエンの単量体の組合せ、スチレン‐イソプレンの単量体の組合せ、およびスチレン‐ネオプレンの単量体の組合せからなるグループからから誘導される、上記10に記載の輸送手段。
12.剪断安定性共重合体が、ホモゲナイザー中で機械的に剪断されたオレフィン共重合体を備える、上記10に記載の輸送手段。
13.可動部が、排気ガス再循環装置と、エンジンを潤滑させるシステムとを含むヘビー・デューティ・ディーゼル・エンジンを備える、上記10に記載の輸送手段。
14.剪断安定性共重合体の各単量体単位がそれぞれ、約2〜10個の炭素原子を含有する、上記10に記載の輸送手段。
15.剪断安定性共重合体が、非結晶性エチレンを備え、エチレン含有量が共重合体の重量の約70%を下回る共重合体を含有する、上記10に記載の輸送手段。
16.潤滑粘性の基油成分と、約5〜30重量%の添加剤とを備える潤滑油組成物の完成品であって、添加剤が、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)潤滑油組成物の完成品。
17.剪断安定性共重合体が、エチレン‐プロピレンの単量体の組合せ、エチレン‐プロピレン‐ジエンの単量体の組合せ、スチレン‐イソプレンの単量体の組合せ、およびスチレン‐ネオプレンの単量体の組合せからなるグループからから誘導される、上記16に記載の潤滑油組成物。
18.剪断安定性共重合体が、ホモゲナイザー中で機械的に剪断されたオレフィン共重合体を備える、上記16に記載の潤滑油組成物。
19.剪断安定性共重合体の各単量体単位がそれぞれ、約2〜10個の炭素原子を含有する、上記16に記載の潤滑油組成物。
20.剪断安定性共重合体が、非結晶性エチレンを備え、エチレン含有量が約70重量%を下回る共重合体を含有する、上記16に記載の潤滑油組成物。
21.潤滑油組成物を約5〜30重量%の添加剤と混合するステップを備える潤滑油組成物の粘度指数を改善する方法であって、添加剤が、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多
分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)方法。
22.潤滑油組成物が、多粘性(multi−viscosity)潤滑油を備える、上記21に記載の方法。
23.剪断安定性共重合体が、エチレン‐プロピレンの単量体の組合せ、エチレン‐プロピレン‐ジエンの単量体の組合せ、スチレン‐イソプレンの単量体の組合せ、およびスチレン‐ネオプレンの単量体の組合せからなるグループからから誘導される、上記21に記載の方法。
24.剪断安定性共重合体が、ホモゲナイザー中で機械的に剪断されたオレフィン共重合体を備える、上記21に記載の方法。
25.剪断安定性共重合体の各単量体単位がそれぞれ、約2〜10個の炭素原子を含有する、上記21に記載の方法。
26.剪断安定性共重合体が、非結晶性エチレンを備え、エチレン含有量が約70重量%を下回る共重合体を含有する、上記21に記載の方法。
27.希釈用または担体オイルと、約5〜90重量%の添加剤とを備える潤滑油添加剤濃縮物であって、添加剤が、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし添加剤濃縮物中の添加剤の量は、添加剤濃縮物の全量に関する量である)潤滑油添加剤濃縮物。
28.剪断安定性共重合体が、エチレン‐プロピレンの単量体の組合せ、エチレン‐プロピレン‐ジエンの単量体の組合せ、スチレン‐イソプレンの単量体の組合せ、およびスチレン‐ネオプレンの単量体の組合せからなるグループからから誘導される、上記27に記載の添加剤濃縮物。
29.剪断安定性共重合体が、ホモゲナイザー中で機械的に剪断されたオレフィン共重合体を備える、上記27に記載の添加剤濃縮物。
30.剪断安定性共重合体の各単量体単位がそれぞれ、約2〜10個の炭素原子を含有する、上記27に記載の添加剤濃縮物。
31.剪断安定性共重合体が、非結晶性エチレンを備え、エチレン含有量が約70重量%を下回る共重合体を含有する、上記27に記載の添加剤濃縮物。
32.基油と、上記27に記載の添加剤濃縮物とを備える潤滑油組成物。
33.輸送手段の可動部を潤滑させる方法であって、方法が、輸送手段の1つまたは複数の可動部のための潤滑油として、基油と潤滑油添加剤とを含有する潤滑油組成物を使用するステップを備え、潤滑油添加剤が、希釈・担体オイルと、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した、所定量の剪断安定性オレフィン共重合体とを備え、潤滑油組成物中に約5〜30重量%の剪断安定性オレフィン共重合体を供給することができ、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)輸送手段の可動部を潤滑させる方法。
34.剪断安定性共重合体が、エチレン‐プロピレンの単量体の組合せ、エチレン‐プロピレン‐ジエンの単量体の組合せ、スチレン‐イソプレンの単量体の組合せ、およびスチレン‐ネオプレンの単量体の組合せからなるグループからから誘導される、上記33に記載の方法。
35.剪断安定性共重合体が、ホモゲナイザー中で機械的に剪断されたオレフィン共重合体を備える、上記33に記載の方法。
36.剪断安定性共重合体の各単量体単位がそれぞれ、約2〜10個の炭素原子を含有する、上記33に記載の方法。
37.剪断安定性共重合体が、非結晶性エチレンを備え、エチレン含有量が約70重量%を下回る共重合体を含有する、上記33に記載の方法。
38.輸送手段がディーゼルエンジンを含み、かつ可動部がエンジンの可動部を含む、上記33に記載の方法。
39.輸送手段がエンジンを有する航海用輸送手段を含み、かつ可動部がエンジンの可動部を含む、上記33に記載の方法。
40.輸送手段がスパーク点火エンジンを含み、かつ可動部がエンジンの可動部を含む、上記33に記載の方法。
41.輸送手段が動力伝達路を含み、かつ可動部が動力伝達路の可動部を含む、上記33に記載の方法。
42.輸送手段が、クランク室を有する内燃機関を含み、かつ潤滑油組成物が、輸送手段のクランク室内に存在するクランク室油を備える、上記33に記載の方法。
43.潤滑油組成物が、輸送手段の自動動力伝達路内に存在する動力伝達路潤滑油を備える、上記33に記載の方法。
44.可動部を、潤滑油添加剤を含有する潤滑油組成物に接触させるステップを備える可動部を潤滑させる方法であって、潤滑油添加剤が、希釈・担体オイルと、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体、約5〜95重量%とを備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物は、潤滑油組成物の全量に関し約5〜30重量%の添加剤を含有する)可動部を潤滑させる方法。
45.可動部が、輸送手段の可動部を備える、上記44に記載の方法。
46.輸送手段がエンジンを有する航海用輸送手段を含み、かつ可動部がエンジンの可動部を含む、上記44に記載の方法。
47.輸送手段が、クランク室を有する内燃機関を含み、かつ潤滑油組成物が、輸送手段のクランク室内に存在するクランク室油を備える、上記44に記載の方法。
48.潤滑油組成物が、輸送手段の自動動力伝達路内に存在する動力伝達路潤滑油を備える、上記44に記載の方法。
The main aspects and features of the present invention are as follows.
1. Contains a base oil of lubricating viscosity and an additive comprising a shear-stable olefin copolymer derived from a copolymer having a number average molecular weight in the range of about 50,000 to 250,000, about 5-30% by weight A lubricating surface comprising a coating of a lubricating oil composition with a thin film, wherein the shear stable olefin copolymer has a shear stability index less than about 40, a polydispersity of about 1.5 or less, and about 1. A lubricating surface having a thickening efficiency greater than 8 (where the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition).
2. The lubricated surface according to 1 above, wherein the lubricated surface comprises a power transmission path of the engine.
3. The lubricating surface of claim 1, wherein the lubricating surface comprises an internal surface or component of an internal combustion engine.
4). The lubricated surface of claim 1, wherein the lubricated surface comprises an internal surface or component of a compression ignition engine.
5. A shear-stable copolymer comprising an ethylene-propylene monomer combination, an ethylene-propylene-diene monomer combination, a styrene-isoprene monomer combination, and a styrene-neoprene monomer combination The lubricating surface of claim 1, wherein the lubricating surface is derived from the group consisting of:
6). The lubricating surface of claim 1, wherein the shear-stable copolymer is derived from a copolymer that is homogenized at a relatively low temperature.
7). The lubricating surface of claim 1, wherein each monomer unit of the shear-stable copolymer each contains about 2 to 10 carbon atoms.
8). The lubricated surface of claim 1, wherein the shear-stable copolymer comprises a copolymer comprising amorphous ethylene and the ethylene content is less than about 70% of the weight of the copolymer.
9. An automobile comprising the lubricating surface according to 1 above.
10. A transportation means having a movable part and containing a lubricating oil for lubricating the movable part, wherein the lubricating oil is a base oil having a lubricating viscosity and a number average molecular weight in the range of about 50,000 to 250,000. An additive comprising a shear-stable olefin copolymer derived from a copolymer having a shear stability olefin copolymer of less than about 40, A means of transport having a polydispersity of 1.5 or less and a thickening efficiency greater than about 1.8 (where the amount of additive in the lubricating oil is relative to the total amount of lubricating oil).
11. A shear-stable copolymer comprising an ethylene-propylene monomer combination, an ethylene-propylene-diene monomer combination, a styrene-isoprene monomer combination, and a styrene-neoprene monomer combination 11. The vehicle of claim 10, wherein the vehicle is derived from a group consisting of:
12 11. A means of transportation as described in 10 above, wherein the shear stable copolymer comprises an olefin copolymer mechanically sheared in a homogenizer.
13. The vehicle of claim 10, wherein the movable part comprises a heavy duty diesel engine including an exhaust gas recirculation device and a system for lubricating the engine.
14 11. The means of transportation as described in 10 above, wherein each monomer unit of the shear-stable copolymer contains about 2 to 10 carbon atoms.
15. 11. The means of transport of claim 10, wherein the shear-stable copolymer comprises a copolymer comprising amorphous ethylene and the ethylene content is less than about 70% of the weight of the copolymer.
16. A finished lubricating oil composition comprising a base oil component of lubricating viscosity and about 5 to 30 weight percent additive, wherein the additive has a number average molecular weight in the range of about 50,000 to 250,000. A shear-stable olefin copolymer derived from the copolymer having a shear stability olefin copolymer of less than about 40, a polydispersity of about 1.5 or less, and about 1. A finished lubricating oil composition having a thickening efficiency greater than 8, wherein the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition.
17. A shear-stable copolymer comprising an ethylene-propylene monomer combination, an ethylene-propylene-diene monomer combination, a styrene-isoprene monomer combination, and a styrene-neoprene monomer combination The lubricating oil composition of claim 16, derived from the group consisting of:
18. 17. The lubricating oil composition of claim 16, wherein the shear stable copolymer comprises an olefin copolymer mechanically sheared in a homogenizer.
19. 17. The lubricating oil composition as described in 16 above, wherein each monomer unit of the shear-stable copolymer contains about 2 to 10 carbon atoms.
20. The lubricating oil composition of claim 16, wherein the shear stable copolymer comprises a copolymer comprising amorphous ethylene and having an ethylene content of less than about 70% by weight.
21. A method of improving the viscosity index of a lubricating oil composition comprising the step of mixing the lubricating oil composition with about 5 to 30 weight percent additive, wherein the additive is in the range of about 50,000 to 250,000. A shear-stable olefin copolymer derived from a copolymer having a number average molecular weight, wherein the shear-stable olefin copolymer has a shear stability index of less than about 40 and a polydispersity of about 1.5 or less. A thickening efficiency greater than about 1.8 (where the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition).
22. The method of claim 21, wherein the lubricating oil composition comprises a multi-viscosity lubricating oil.
23. A shear-stable copolymer comprising an ethylene-propylene monomer combination, an ethylene-propylene-diene monomer combination, a styrene-isoprene monomer combination, and a styrene-neoprene monomer combination The method of claim 21, wherein the method is derived from a group consisting of:
24. The method of claim 21, wherein the shear-stable copolymer comprises an olefin copolymer mechanically sheared in a homogenizer.
25. The method of claim 21, wherein each monomer unit of the shear-stable copolymer each contains about 2 to 10 carbon atoms.
26. The method of claim 21, wherein the shear stable copolymer comprises a copolymer comprising amorphous ethylene and having an ethylene content of less than about 70% by weight.
27. A lubricating oil additive concentrate comprising a diluent or carrier oil and about 5 to 90% by weight additive, wherein the additive has a number average molecular weight in the range of about 50,000 to 250,000. A shear-stable olefin copolymer derived from a polymer, wherein the shear-stable olefin copolymer has a shear stability index of less than about 40, a polydispersity of about 1.5 or less, and about 1.8. Lubricating oil additive concentrate having a thickening efficiency that is greater (where the amount of additive in the additive concentrate is relative to the total amount of additive concentrate).
28. A shear-stable copolymer comprising an ethylene-propylene monomer combination, an ethylene-propylene-diene monomer combination, a styrene-isoprene monomer combination, and a styrene-neoprene monomer combination 28. The additive concentrate of claim 27, derived from the group consisting of:
29. 28. The additive concentrate of claim 27, wherein the shear stable copolymer comprises an olefin copolymer mechanically sheared in a homogenizer.
30. 28. The additive concentrate as described in 27 above, wherein each monomer unit of the shear-stable copolymer each contains about 2 to 10 carbon atoms.
31. 28. The additive concentrate of claim 27, wherein the shear stable copolymer comprises a copolymer comprising amorphous ethylene and having an ethylene content of less than about 70% by weight.
32. A lubricating oil composition comprising a base oil and the additive concentrate as described in 27 above.
33. A method of lubricating a moving part of a vehicle, wherein the method uses a lubricating oil composition containing a base oil and a lubricating oil additive as a lubricating oil for one or more moving parts of the vehicle A predetermined amount of a shear-stable olefin copolymer, wherein the lubricant additive is derived from a diluent / carrier oil and a copolymer having a number average molecular weight in the range of about 50,000 to 250,000. About 5 to 30% by weight of the shear stable olefin copolymer in the lubricating oil composition, wherein the shear stable olefin copolymer has a shear stability index of less than about 40; Transportation means having a polydispersity of about 1.5 or less and a thickening efficiency greater than about 1.8 (where the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition) To lubricate the moving parts of the machine.
34. A shear-stable copolymer comprising an ethylene-propylene monomer combination, an ethylene-propylene-diene monomer combination, a styrene-isoprene monomer combination, and a styrene-neoprene monomer combination 34. The method of claim 33, derived from the group consisting of:
35. 34. The method of claim 33, wherein the shear stable copolymer comprises an olefin copolymer mechanically sheared in a homogenizer.
36. 34. The method of claim 33, wherein each monomer unit of the shear stable copolymer contains from about 2 to 10 carbon atoms.
37. 34. The method of claim 33, wherein the shear-stable copolymer comprises a copolymer comprising amorphous ethylene and having an ethylene content below about 70% by weight.
38. 34. The method of claim 33, wherein the vehicle comprises a diesel engine and the moving part comprises a moving part of the engine.
39. 34. The method of claim 33, wherein the means of transportation comprises a nautical means of transportation having an engine and the moving part comprises a moving part of the engine.
40. 34. The method of claim 33, wherein the vehicle comprises a spark ignition engine and the moving part comprises a moving part of the engine.
41. 34. The method of claim 33, wherein the transportation means includes a power transmission path and the movable part includes a movable part of the power transmission path.
42. 34. The method of claim 33, wherein the vehicle comprises an internal combustion engine having a crankcase and the lubricating oil composition comprises crankcase oil present in the crankcase of the vehicle.
43. 34. The method of claim 33, wherein the lubricating oil composition comprises a power transmission line lubricant present in an automatic power transmission path of the vehicle.
44. A method of lubricating a movable part comprising the step of contacting the movable part with a lubricating oil composition containing a lubricating oil additive, wherein the lubricating oil additive is diluted with carrier oil and about 50,000-250, A shear-stable olefin copolymer derived from a copolymer having a number average molecular weight in the range of 000, from about 5 to 95% by weight, the shear-stable olefin copolymer having a shear stability index of less than about And a polydispersity of about 1.5 or less and a thickening efficiency of greater than about 1.8 (provided that the lubricating oil composition comprises about 5 to 30% by weight additive based on the total amount of the lubricating oil composition). A method of lubricating a moving part (containing).
45. 45. A method according to 44, wherein the movable part comprises a movable part of the vehicle.
46. 45. The method of claim 44, wherein the vehicle comprises a nautical vehicle having an engine and the movable part comprises a movable part of the engine.
47. 45. The method of claim 44, wherein the vehicle comprises an internal combustion engine having a crankcase and the lubricating oil composition comprises crankcase oil present in the crankcase of the vehicle.
48. 45. The method of claim 44, wherein the lubricating oil composition comprises a power transmission line lubricating oil present in an automatic power transmission path of the vehicle.

本発明のオレフィン共重合体を機械的に剪断した場合の剪断安定度指数の変化を示す。The change of the shear stability index at the time of mechanically shearing the olefin copolymer of the present invention is shown. 本発明のオレフィン共重合体を機械的に剪断した場合の多分散性の変化を示す。The change of polydispersity when the olefin copolymer of the present invention is mechanically sheared is shown. 本発明のオレフィン共重合体を機械的に剪断した場合の粘度の変化を示すグラフである。It is a graph which shows the change of the viscosity at the time of carrying out mechanical shearing of the olefin copolymer of this invention. 本発明のオレフィン共重合体を作業オイル中で機械的剪断した場合の粘度変化を、従来のオレフィン共重合体に押出し機により高温で剪断・直接仕上げをおこなった場合の粘度変化と比較したグラフである。A graph comparing the viscosity change when the olefin copolymer of the present invention is mechanically sheared in working oil with the viscosity change when the conventional olefin copolymer is sheared and directly finished at high temperature by an extruder. is there. 本発明のオレフィン共重合体を機械的に剪断した場合の濃化効率の変化を、従来のオレフィン共重合体に押出し機により高温で剪断・直接仕上げをおこなった場合の濃化効率の変化と比較したグラフである。Comparison of change in concentration efficiency when the olefin copolymer of the present invention is mechanically sheared with change in concentration efficiency when the conventional olefin copolymer is sheared and directly finished at high temperature by an extruder. It is a graph.

Claims (7)

潤滑粘性の基油と、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%とを含有する潤滑油組成物の薄膜による被覆を備える潤滑表面であって、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)潤滑表面。   Contains a base oil of lubricating viscosity and an additive comprising a shear-stable olefin copolymer derived from a copolymer having a number average molecular weight in the range of about 50,000 to 250,000, about 5-30% by weight A lubricating surface comprising a coating of a lubricating oil composition with a thin film, wherein the shear stable olefin copolymer has a shear stability index less than about 40, a polydispersity of about 1.5 or less, and about 1. A lubricating surface having a thickening efficiency greater than 8 (where the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition). 可動部を有し、かつ可動部を潤滑させるための潤滑油を含有する輸送手段であって、潤滑油が、潤滑粘性の基油と、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備える添加剤、約5〜30重量%とを備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油中の添加剤の量は、潤滑油の全量に関する量である)輸送手段。   A transportation means having a movable part and containing a lubricating oil for lubricating the movable part, wherein the lubricating oil is a base oil having a lubricating viscosity and a number average molecular weight in the range of about 50,000 to 250,000. An additive comprising a shear-stable olefin copolymer derived from a copolymer having a shear stability olefin copolymer of less than about 40, A means of transport having a polydispersity of 1.5 or less and a thickening efficiency greater than about 1.8 (where the amount of additive in the lubricating oil is relative to the total amount of lubricating oil). 潤滑粘性の基油成分と、約5〜30重量%の添加剤とを備える潤滑油組成物の完成品であって、添加剤が、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)潤滑油組成物の完成品。   A finished lubricating oil composition comprising a base oil component of lubricating viscosity and about 5 to 30 weight percent additive, wherein the additive has a number average molecular weight in the range of about 50,000 to 250,000. A shear-stable olefin copolymer derived from the copolymer having a shear stability olefin copolymer of less than about 40, a polydispersity of about 1.5 or less, and about 1. A finished lubricating oil composition having a thickening efficiency greater than 8, wherein the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition. 潤滑油組成物を約5〜30重量%の添加剤と混合するステップを備える潤滑油組成物の粘度指数を改善する方法であって、添加剤が、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)方法。   A method of improving the viscosity index of a lubricating oil composition comprising the step of mixing the lubricating oil composition with about 5 to 30 weight percent additive, wherein the additive is in the range of about 50,000 to 250,000. A shear-stable olefin copolymer derived from a copolymer having a number average molecular weight, wherein the shear-stable olefin copolymer has a shear stability index of less than about 40 and a polydispersity of about 1.5 or less. A thickening efficiency greater than about 1.8 (where the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition). 希釈用または担体オイルと、約5〜90重量%の添加剤とを備える潤滑油添加剤濃縮物であって、添加剤が、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン共重合体を備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし添加剤濃縮物中の添加剤の量は、添加剤濃縮物の全量に関する量である)潤滑油添加剤濃縮物。   A lubricating oil additive concentrate comprising a diluent or carrier oil and about 5 to 90% by weight additive, wherein the additive has a number average molecular weight in the range of about 50,000 to 250,000. A shear-stable olefin copolymer derived from a polymer, wherein the shear-stable olefin copolymer has a shear stability index of less than about 40, a polydispersity of about 1.5 or less, and about 1.8. Lubricating oil additive concentrate having a thickening efficiency that is greater (where the amount of additive in the additive concentrate is relative to the total amount of the additive concentrate). 輸送手段の可動部を潤滑させる方法であって、方法が、輸送手段の1つまたは複数の可動部のための潤滑油として、基油と潤滑油添加剤とを含有する潤滑油組成物を使用するステップを備え、潤滑油添加剤が、希釈・担体オイルと、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した、所定量の剪断安定性オレフィン共重合体とを備え、潤滑油組成物中に約5〜30重量%の剪断安定性オレフィン共重合体を供給することができ、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物中の添加剤の量は、潤滑油組成物の全量に関する量である)輸送手段の可動部を潤滑させる方法。   A method of lubricating a moving part of a vehicle, wherein the method uses a lubricating oil composition containing a base oil and a lubricating oil additive as a lubricating oil for one or more moving parts of the vehicle A predetermined amount of a shear-stable olefin copolymer, wherein the lubricant additive is derived from a diluent / carrier oil and a copolymer having a number average molecular weight in the range of about 50,000 to 250,000. About 5 to 30% by weight of the shear stable olefin copolymer in the lubricating oil composition, wherein the shear stable olefin copolymer has a shear stability index of less than about 40; Transportation means having a polydispersity of about 1.5 or less and a thickening efficiency greater than about 1.8 (where the amount of additive in the lubricating oil composition is relative to the total amount of the lubricating oil composition) To lubricate moving parts. 可動部を、潤滑油添加剤を含有する潤滑油組成物に接触させるステップを備える可動部を潤滑させる方法であって、潤滑油添加剤が、希釈・担体オイルと、約50,000〜250,000の範囲の数平均分子量を有する共重合体から誘導した剪断安定性オレフィン
共重合体、約5〜95重量%とを備え、剪断安定性オレフィン共重合体は、約40を下回る剪断安定度指数と、約1.5以下の多分散性と、約1.8を上回る濃化効率とを有する(ただし潤滑油組成物は、潤滑油組成物の全量に関し約5〜30重量%の添加剤を含有する)可動部を潤滑させる方法。
A method of lubricating a movable part comprising the step of contacting the movable part with a lubricating oil composition containing a lubricating oil additive, wherein the lubricating oil additive is diluted with carrier oil and about 50,000-250, A shear-stable olefin copolymer derived from a copolymer having a number average molecular weight in the range of 000, from about 5 to 95% by weight, the shear-stable olefin copolymer having a shear stability index of less than about 40 And a polydispersity of about 1.5 or less and a thickening efficiency of greater than about 1.8 (provided that the lubricating oil composition comprises about 5 to 30% by weight additive based on the total amount of the lubricating oil composition). A method of lubricating a moving part (containing).
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008093446A1 (en) * 2007-01-31 2008-08-07 Nippon Oil Corporation Lubricant oil composition

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080085847A1 (en) * 2006-10-10 2008-04-10 Kwok-Leung Tse Lubricating oil compositions
JP5330716B2 (en) * 2008-03-17 2013-10-30 出光興産株式会社 Lubricating oil composition
WO2009125075A1 (en) * 2008-04-11 2009-10-15 Total Raffinage Marketing Multipurpose lubricant fluid
US20100256026A1 (en) * 2009-04-03 2010-10-07 Margaret May-Som Wu Lubricant composition containing Ethylene-Alpha Olefin Copolymer viscosity modifier
WO2010140446A1 (en) * 2009-06-04 2010-12-09 新日本石油株式会社 Lubricant oil composition
US8415284B2 (en) * 2009-11-05 2013-04-09 Afton Chemical Corporation Olefin copolymer VI improvers and lubricant compositions and uses thereof
WO2012076676A1 (en) 2010-12-10 2012-06-14 Evonik Rohmax Additives Gmbh A viscosity index improver comprising a polyalkyl(meth)acrylate polymer
CN104245906A (en) * 2012-02-17 2014-12-24 卢布里佐尔公司 Mixtures of olefin-ester copolymer with polyolefin as viscosity modifier
JP6720142B2 (en) 2014-08-21 2020-07-08 ダウ グローバル テクノロジーズ エルエルシー Adhesive composition
US9354180B2 (en) * 2014-09-16 2016-05-31 Afron Chemical Corporation Quantifying the level of intermacromolecular interactions by using pyrene excimer formation
KR102295932B1 (en) * 2017-06-26 2021-08-30 에스케이이노베이션 주식회사 Viscosity improver for lubricating oils and lubricant compositions using thereof

Family Cites Families (80)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2326595A (en) * 1942-01-01 1943-08-10 Jasco Inc Size reduction and stabilization of oil thickening polymers
US3541015A (en) * 1965-12-20 1970-11-17 Gaf Corp Lubricating oil containing methyl vinyl ether copolymers
US3676408A (en) * 1965-12-20 1972-07-11 Gaf Corp Methyl vinyl ether copolymers
US3758519A (en) * 1966-04-07 1973-09-11 Uniroyal Inc Derivatives of diphenylamine
US3666716A (en) * 1966-04-07 1972-05-30 Uniroyal Inc Derivatives of diphenylamine and the phenylnaphthylamines as antioxidants and as synergists with dialkyl 3,3{40 -thiodipropionates
US3944492A (en) * 1966-04-07 1976-03-16 Uniroyal, Inc. Lubricant compositions containing N-substituted naphthylamines as antioxidants
US3488721A (en) * 1967-06-12 1970-01-06 Texaco Inc Preparation of a grease additive concentrate containing a water-soluble inorganic compound
FR1552150A (en) * 1967-11-20 1969-01-03
US3634381A (en) * 1968-04-27 1972-01-11 Basf Ag Degradation of high molecular weight polyisobutylene in extruders
US3785196A (en) * 1972-04-03 1974-01-15 Exxon Research Engineering Co Apparatus for testing shear stability of lubricants
FR2223450B1 (en) * 1973-03-29 1976-05-21 Rhone Progil
US4018695A (en) * 1974-03-04 1977-04-19 Gulf Research & Development Company Polymer-modified automatic transmission fluid
US3974081A (en) * 1974-07-31 1976-08-10 Exxon Research And Engineering Company Biodegradable seal swell additive with low toxicity properties for automatic transmission fluids, power transmission fluids and rotary engine oil applications
FR2293485A1 (en) * 1974-12-03 1976-07-02 Inst Francais Du Petrole LUBRICANT COMPOSITIONS IMPROVED BY THE ADDITION OF COPOLYMERS GRAFTS
US4181618A (en) * 1974-12-03 1980-01-01 Institut Francais Du Petrole Grafted copolymers and their use as additives for lubricating oils
US4092255A (en) * 1974-12-12 1978-05-30 Entreprise De Recherches Et D'activites Petrolieres (E.R.A.P.) Novel lubricating compositions containing nitrogen containing hydrocarbon backbone polymeric additives
US4170561A (en) * 1974-12-12 1979-10-09 Entreprise De Recherches Et D'activities Petrolieres (E.R.A.P.) Lubricating compositions with lactam or thiolactam-containing copolymers
US4068058A (en) * 1975-03-05 1978-01-10 Exxon Research And Engineering Company Aminated polymeric additives for fuel and lubricants
US4068057A (en) * 1975-03-05 1978-01-10 Exxon Research And Engineering Company Aminated polymeric additives for fuel and lubricants
US4042747A (en) * 1975-03-14 1977-08-16 Joseph A. Teti, Jr. Gasket and sealing structures of filled polytetrafluoroethylene resins
US4029587A (en) * 1975-06-23 1977-06-14 The Lubrizol Corporation Lubricants and functional fluids containing substituted sulfolanes as seal swelling agents
US4372863A (en) * 1977-04-13 1983-02-08 Exxon Research & Engineering Co. Oil compositions containing oil-soluble, oxidatively and mechanically degraded ethylene copolymers
US4933099A (en) * 1979-01-09 1990-06-12 Exxon Research And Engineering Company Oil compositions containing ethylene copolymers
DE3070952D1 (en) * 1979-06-26 1985-09-12 British Petroleum Co Plc Cross-linked polymer compositions and production thereof
GB2056482A (en) * 1979-08-13 1981-03-18 Exxon Research Engineering Co Lubricating oil compositions
US4340689A (en) * 1979-09-17 1982-07-20 Copolymer Rubber & Chemical Corporation Method of grafting EPM and EPDM polymers
FR2497822A1 (en) * 1981-01-12 1982-07-16 Organo Synthese Ste Fse ADDITIVES FOR LUBRICATING OILS BASED ON STYRENE AND C12-C20 ALKYL HEAVY METHACRYLATES, MANUFACTURING METHOD AND APPLICATIONS
US4629753A (en) * 1981-11-18 1986-12-16 The Lubrizol Corporation Water dispersed rust inhibitive coating compositions
JPS58104999A (en) * 1981-12-18 1983-06-22 Kao Corp Metal rolling oil composition
US4434270A (en) * 1982-12-06 1984-02-28 Standard Oil Company (Indiana) Ethylene/propylene/vinyl alkyl ketone polymers
US4533482A (en) * 1982-12-30 1985-08-06 Rohm And Haas Company Hydrogenated diolefin-lower alkyl acrylate or methacrylate viscosity index improving copolymers for lubricating oils
JPS61246293A (en) * 1985-04-03 1986-11-01 Kao Corp Cold rolling oil for steel
FR2589866B1 (en) * 1985-11-07 1988-07-15 Inst Francais Du Petrole COPOLYMER COMPOSITIONS FOR USE AS ADDITIVES FOR LUBRICATING OILS
US4804794A (en) * 1987-07-13 1989-02-14 Exxon Chemical Patents Inc. Viscosity modifier polymers
IL89210A (en) 1988-02-26 1992-06-21 Exxon Chemical Patents Inc Lubricating oil compositions containing demulsifiers
US5006608A (en) * 1988-09-08 1991-04-09 Exxon Chemical Patents, Inc. Catalytic process for oxidative, shear accelerated polymer degradation
FR2642435B1 (en) * 1989-01-27 1994-02-11 Organo Synthese Ste Fse VISCOSITY ADDITIVE FOR LUBRICATING OILS, PROCESS FOR THE PREPARATION THEREOF, AND LUBRICANT COMPOSITIONS BASED ON SAID ADDITIVE
US5204012A (en) * 1989-01-31 1993-04-20 Ethyl Corporation Supplemental rust inhibitors and rust inhibition in internal combustion engines
US5110490A (en) * 1989-06-27 1992-05-05 Exxon Research And Engineering Company Water resistant grease composition
US5244590A (en) * 1989-10-12 1993-09-14 Exxon Chemical Patents Inc. Viscosity index improver
US5075383A (en) * 1990-04-11 1991-12-24 Texaco Inc. Dispersant and antioxidant additive and lubricating oil composition containing same
US5302667A (en) * 1990-04-16 1994-04-12 Shell Oil Company Asymmetrical radial polymer and composition of matter comprising the same
US5356999A (en) * 1990-10-29 1994-10-18 Texaco Inc. Multifunctional viscosity index improvers based on polymers containing sulfonamides
US5162086A (en) * 1991-05-22 1992-11-10 Texaco Inc. Dispersant additive and lubricating oil composition containing same
US5188745A (en) * 1991-12-23 1993-02-23 Texaco Inc. Viton seal compatible dispersant and lubricating oil composition containing same
US5276227A (en) * 1992-02-03 1994-01-04 Mobil Oil Corporation C2 -C5 olefin oligomer compositions as shear stable viscosity index improvers
US5217636A (en) * 1992-03-10 1993-06-08 Albright & Wilson Americas Inc. Lubricating oil viscosity index improver composition
US6117825A (en) * 1992-05-07 2000-09-12 Ethyl Corporation Polyisobutylene succinimide and ethylene-propylene succinimide synergistic additives for lubricating oils compositions
US6656888B1 (en) * 1992-08-28 2003-12-02 Cognis Corporation Biodegradable two-cycle engine oil compositions, grease compositions, and ester base stocks use therein
US5474694A (en) * 1992-09-21 1995-12-12 Texaco Inc. Lubricating oil composition
US6090755A (en) * 1994-03-28 2000-07-18 Skf Industrial Trading & Development Company, B.V. Use of bismuth compounds in extreme pressure grease lubricant compositions for rolling bearing applications with extended service life
US5451630A (en) * 1994-08-02 1995-09-19 Dsm Copolymer, Inc. Solid sheared polymer blends and process for their preparation
US5540851A (en) * 1995-03-02 1996-07-30 The Lubrizol Corporation Dispersant-viscosity improvers for lubricating oil compositions
US5538651A (en) * 1995-06-19 1996-07-23 The Lubrizol Corporation Additive to improve fluidity of oil solutions of sheared polymers
US6077455A (en) * 1995-07-17 2000-06-20 Exxon Chemical Patents Inc Automatic transmission fluid of improved viscometric properties
US5641733A (en) * 1995-07-17 1997-06-24 Exxon Chemical Patents Inc. Automatic transmission fluids of improved viscometric properties
US5641732A (en) * 1995-07-17 1997-06-24 Exxon Chemical Patents Inc. Automatic transmission fluids of improved viscometric properties
SG64414A1 (en) * 1996-01-16 1999-04-27 Lubrizol Corp Lubricating compositions
US5817606A (en) * 1996-08-08 1998-10-06 Rohm And Haas Company Viscosity index improving additives for phosphate ester-containing hydraulic fluids
US5811378A (en) * 1997-01-21 1998-09-22 The Lubrizol Corporation Metal containing dispersant-viscosity improvers for lubricating oils
US6140431A (en) * 1997-02-27 2000-10-31 Rohm And Haas Company Process for preparing continuously variable-composition copolymers
US6117941A (en) * 1997-06-05 2000-09-12 The Lubrizol Corporation Intermediates useful for preparing dispersant-viscosity improvers for lubricating oils
CN1147515C (en) * 1997-10-28 2004-04-28 卡斯特罗尔有限公司 Processes for preparing grafted copolymers
US6288013B1 (en) * 1997-12-03 2001-09-11 The Lubrizol Corporation Nitrogen containing dispersant-viscosity improvers
US6265358B1 (en) * 1997-12-03 2001-07-24 The Lubrizol Corporation Nitrogen containing dispersant-viscosity improvers
US6034040A (en) * 1998-08-03 2000-03-07 Ethyl Corporation Lubricating oil formulations
DE69926015T2 (en) * 1998-12-09 2006-05-18 Mitsui Chemicals, Inc. VIKOSITY CHANGERS FOR LUBRICATING OILS AND LUBRICATING OIL COMPOSITION
KR100662062B1 (en) * 1999-03-30 2006-12-27 미쓰이 가가쿠 가부시키가이샤 Viscosity regulator for lubricating oil and lubricating oil composition
US6380297B1 (en) * 1999-08-12 2002-04-30 Nexpress Solutions Llc Polymer particles of controlled shape
US6403725B1 (en) * 1999-08-20 2002-06-11 The Lubrizol Corporation Metal containing dispersant polymers from condensation of polymers containing acidic group with overbased compositions containing reactive nucleophilic group
CA2394823A1 (en) * 1999-12-30 2001-07-12 Uniroyal Chemical Company, Inc. Antioxidant amines based on n-(4-anilinophenyl)amides
BR0106323B1 (en) * 2000-05-10 2011-09-06 viscosity modifier for lubricating oil and lubricating oil compositions.
EP1294776A2 (en) * 2000-05-18 2003-03-26 The Lubrizol Corporation Process for reacting large hydrophobic molecules with small hydrophilic molecules
US6472353B1 (en) * 2000-09-14 2002-10-29 The Lubrizol Corporation Dispersant-viscosity improvers for lubricating oil compositions
US20030013623A1 (en) * 2001-05-01 2003-01-16 Kwok-Leung Tse Olefin copolymer viscocity index improvers
US7022766B2 (en) * 2001-05-31 2006-04-04 Mitsui Chemicals, Inc. Olefin block copolymer, viscosity index improver for lubricating oils and lubricating oil composition
US6677282B2 (en) * 2001-06-21 2004-01-13 The Lubrizol Corporation Dispersant-viscosity improvers for lubricating oil and fuels
WO2003038017A1 (en) * 2001-11-01 2003-05-08 Mitsui Chemicals, Inc. Additive for lubricating oil and lubricating oil composition
US6753381B2 (en) * 2002-03-15 2004-06-22 Ethyl Corporation Polymer blends and their application as viscosity index improvers
ITMI20040751A1 (en) * 2004-04-16 2004-07-16 Polimeri Europa Spa PROCEDURE FOR MODIFYING THE RHEOLOGICAL PROPERTIES OF EP D M POLYMERS AND MIXTURES OF EP D M WITH POLY-ALFAOLEFINS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008093446A1 (en) * 2007-01-31 2008-08-07 Nippon Oil Corporation Lubricant oil composition

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CA2514499A1 (en) 2006-03-17
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US20070191242A1 (en) 2007-08-16
AU2005203438A1 (en) 2006-04-06
KR100724328B1 (en) 2007-06-04
AU2005203438B2 (en) 2007-08-30
SG121118A1 (en) 2006-04-26
KR20060051400A (en) 2006-05-19

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