JPH0329839B2 - - Google Patents
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- Publication number
- JPH0329839B2 JPH0329839B2 JP58114334A JP11433483A JPH0329839B2 JP H0329839 B2 JPH0329839 B2 JP H0329839B2 JP 58114334 A JP58114334 A JP 58114334A JP 11433483 A JP11433483 A JP 11433483A JP H0329839 B2 JPH0329839 B2 JP H0329839B2
- Authority
- JP
- Japan
- Prior art keywords
- lubricating oil
- weight
- oil
- solid impurities
- composition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- 239000010687 lubricating oil Substances 0.000 claims abstract description 40
- 239000012535 impurity Substances 0.000 claims abstract description 36
- 239000007787 solid Substances 0.000 claims abstract description 33
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims abstract description 27
- 239000011777 magnesium Substances 0.000 claims abstract description 24
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 24
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 21
- ZMRQTIAUOLVKOX-UHFFFAOYSA-L calcium;diphenoxide Chemical compound [Ca+2].[O-]C1=CC=CC=C1.[O-]C1=CC=CC=C1 ZMRQTIAUOLVKOX-UHFFFAOYSA-L 0.000 claims abstract description 20
- 239000003921 oil Substances 0.000 claims abstract description 10
- 239000002480 mineral oil Substances 0.000 claims abstract description 6
- 235000010446 mineral oil Nutrition 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims description 41
- 239000002199 base oil Substances 0.000 claims description 8
- 230000004931 aggregating effect Effects 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 8
- 238000005461 lubrication Methods 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 abstract 1
- 229910052748 manganese Inorganic materials 0.000 abstract 1
- 239000011572 manganese Substances 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 16
- 239000004071 soot Substances 0.000 description 14
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 9
- 239000011575 calcium Substances 0.000 description 9
- 229910052791 calcium Inorganic materials 0.000 description 9
- KZNICNPSHKQLFF-UHFFFAOYSA-N dihydromaleimide Natural products O=C1CCC(=O)N1 KZNICNPSHKQLFF-UHFFFAOYSA-N 0.000 description 8
- -1 alkenyl succinimide Chemical compound 0.000 description 7
- 229960002317 succinimide Drugs 0.000 description 6
- 230000003311 flocculating effect Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 230000002776 aggregation Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- WMYJOZQKDZZHAC-UHFFFAOYSA-H trizinc;dioxido-sulfanylidene-sulfido-$l^{5}-phosphane Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([S-])=S.[O-]P([O-])([S-])=S WMYJOZQKDZZHAC-UHFFFAOYSA-H 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000003749 cleanliness Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000006864 oxidative decomposition reaction Methods 0.000 description 2
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001639 boron compounds Chemical class 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 229940014800 succinic anhydride Drugs 0.000 description 1
- 239000010913 used oil Substances 0.000 description 1
Landscapes
- Lubricants (AREA)
- Filtration Of Liquid (AREA)
- Lubrication Of Internal Combustion Engines (AREA)
Abstract
Description
本発明はデイーゼルエンジン用の潤滑油組成物
に関し、更に詳しくは、エンジン駆動時、不可避
的に発生する煤などの固形不純物をフイルター等
のろ過手段で除去可能な粒径に凝集せしめること
ができ、ひいては固形不純物による動弁系の摩耗
を大幅に抑制し、したがつて、更油期間が長く使
用寿命の延長した固形不純物凝集性デイーゼルエ
ンジン用潤滑油組成物に関する。
デイーゼルエンジンは、ガソリンエンジンに比
べるとその燃焼圧力が高く燃焼室内はより高温に
なり、また燃焼機構上不完全燃焼が起り易いの
で、燃焼残渣若しくは潤滑油の酸化分解による煤
など油に不溶解の固形不純物(0.2μm程度の大き
さ)を多量に発生し、これらが潤滑油や潤滑系に
混入するという事態を不可避的に生ずる。
この混入量が増大すると、まず何よりもロツカ
ーアーム、カムなどの動弁系の摩耗が激しくな
り、更には潤滑油自体の粘度の著増に基づく動力
損失の増大、ピストン−ライナー間の冷却能の低
下、潤滑系内での目詰り現象が起生してデイーゼ
ルエンジンの円滑な潤滑管理が阻害される。
このような問題を解決するために、従来から、
潤滑油の酸化分解を防止するための、例えばジチ
オりん酸亜鉛、及び上記した固形不純物を微細粒
子として油中に分散させ、それらが凝集して沈積
物になることを防止するために、いわゆる清浄分
散剤と指称される各種の化合物を潤滑油自体に添
加してその清浄性を高めるということが行なわれ
ている(日本潤滑学会編、「潤滑ハンドブツク」、
増訂後の第6版、310〜315頁,1982年参照)。
しかしながら、この場合でも、煤など固形不純
物の悪影響を解消するには限度があり、結局は比
較的短期間(通常、5000〜10000Km)で潤滑油を
更油しているのが現状である。
とりわけ、排気ガス対策として近年登場してい
るEGR(exhaust gas Recirculation:排気ガス
再循環装置)装置のデイーゼルエンジンの場合に
は、発生する煤の量が一段と多量になるため、上
記した方法では対処しきれず潤滑管理が事実上不
可能となつている。
そのため、更に清浄性が向上し動弁系の摩耗を
一層抑制し得る潤滑油の開発は強く望まれている
ことである。
本発明者らは、上記の目的を達成すべく鋭意研
究を重ねる中で、固形不純物を油中に分散させる
という従来の技術思想とは正反対の技術思想、す
なわち、沈降・堆積が起らない程度に固形不純物
を凝集せしめて粗大化しこれを循環系に配設した
バイパスフイルタで捕促・除去すれば、潤滑油は
常時清浄な状態で循環し得るとの着想を得、該着
想に基づいてかかる効果を発揮する化合物の探索
を行なつたところ、驚くべきことには、常用され
ている基油に清浄分散剤として既に知られている
カルシウムフエネート,マグネシウムスルホネー
トであつても特定範囲の塩基価のものを所定量配
合してなる潤滑油は、約0.2μmの固形不純物を約
1μmに凝集せしめるとの事実を見出し本発明の
潤滑油組成物を開発するに到つた。
すなわち、本発明の固形不純物凝集性デイーゼ
ルエンジン用潤滑油組成物は、鉱油又は/及び合
成油から成る基油に、塩基価60以上のカルシウム
フエネート1〜7重量%、塩基価100以上のマグ
ネシウムスルホネート0.1〜5重量%及びアルケ
ニルこはく酸イミド1〜5重量%を添加した組成
であることを特徴とする。
本発明の潤滑油組成物において、用いる基油は
格別限定されず、潤滑油の基油として常用されて
いる鉱油、合成油又は両者を適宜な比率で混合し
た混合油であれば何であつてもよい。この場合、
潤滑性の維持・向上、動力損失の低減、過大なオ
イル消費の防止などの点から基油の100℃での動
粘度を3〜30センチストークス(cSt)の範囲に
調整することが好ましい。
上記した基油に、後述するカルシウムフエネー
ト、マグネシウムスルホネート及びアルケニルこ
はく酸イミドが添加されて本発明の潤滑油組成物
が構成される。
まず、本発明で用いられるカルシウムフエネー
トは、その塩基価が60以上の範囲に設定される。
塩基価の上限は特に限定されないが300以下のも
のが容易に入手できて便利である。好ましくは
100〜250である。なお、本発明でいう塩基価と
は、塩基性成分の量の尺度であつてその1gに相
当する水酸化カリウムのmg数で表示するもので、
その単位はmgKOH/gである。
塩基価が60未満の場合には、燃焼生成物中の硫
酸に対する中和作用が充分に発揮されず、その結
果動弁系の腐食若しくは摩耗を防止する機能が減
退すること、又は、固形不純物が凝集し、多量に
エンジン内部に沈積するなどの不都合な事態を生
ずる。
このようなカルシウムフエネートは、通常の公
知の方法、例えば各種のアルキルフエノール若し
くは硫化アルキルフエノールのカルシウム塩又は
該カルシウム塩を炭酸化して調製される。このと
き、用いる原料の種類(例えばアルキル基の種
類)、量比、炭酸化の度合などを適宜に調節する
ことによつて全体の塩基価を上記した範囲内に設
定する。
カルシウムフエネートの添加量は調製すべき潤
滑油の全重量に対し1〜7重量%に設定される。
好ましくは3〜6重量%である。添加量が1重量
%未満のときはその効果があらわれず、逆に7重
量%を超えると動弁系の摩耗を促進するなど不都
合な事態が生ずる。
次に、本発明で用いられるマグネシウムスルホ
ネートは、その塩基価が100以上の範囲、添加量
が0.1〜5重量%に設定される。塩基価の上限は
特に限定されないが450以下のものが容易に入手
できる。好ましくは、それぞれ、200〜450、0.5
〜4重量%である。
塩基価が100未満の場合には、凝集効果が小さ
くなり、固形不純物が細かく分散されるため動弁
系の摩耗抑制効果が減退するという不都合な事態
が生ずる。
また、添加量が0.1重量%未満又は、5重量%
を超えると上記した凝集効果が発揮されない。
このようなマグネシウムスルホネートは、各種
の脂肪族スルホン酸若しくは芳香族スルホン酸の
マグネシウム塩又は該マグネシウム塩を炭酸化す
ることによつて調製することができるが、このと
きカルシウムフエネート調製の場合と同様の態様
でその塩基価を上記した100以上の範囲に調整す
ることが必要である。
本発明にかかる添加剤の第3成分であるアルケ
ニルこはく酸イミドは、主としてエンジン駆動時
の低温スラツジ対策と同時に、前記カルシウムフ
エネート、マグネシウムスルホネートと共に固形
不純物の凝集力を調節する目的で添加される。そ
の添加量は潤滑油組成物の全重量に対し1〜5重
量%に設定される。好ましくは2〜4重量%であ
る。
添加量が1重量%未満の場合には、その添加効
果が表われず、逆に5重量%を超えると固形不純
物の凝集効果を妨げるという不都合な事態を生ず
る。
アルケニルこはく酸イミドとしては、例えば、
分子量300〜5000のポリオレフインを無水マレイ
ン酸と反応させてモノアルケニル無水こはく酸と
した後、更にテトラエチレンペンタミンのような
ポリアミンを反応させてイミド化したものが用い
られる。また、特公昭42−8013,特公昭42−
8014,特開昭51−52381,特開昭51−130408,特
開昭54−87705で記載されているようなアルケニ
ルこはく酸イミドのホウ素化合物誘導体も使用す
ることができる。本発明にあつては、テトラエチ
ルペンタミンのポリプテニルこはく酸イミドが好
ましい。
本発明の潤滑油組成物は以上の成分を基本とし
て構成されるが、効果をさらに増大させるため
に、塩基価80以下のカルシウムスルホネートを20
重量%以下好ましくは0.5〜10重量%添加すれば
潤滑油中のすすや動弁系の摩耗状態がより一層改
善される。また常用されている油性剤(高級アル
コールなど)、極圧剤(鉛石けんなど)、粘度指数
向上剤(イソブチレンポリマーなど)、消泡剤
(シリコン油など)、酸化防止剤(ジチオリン酸亜
鉛など)のような各種添加剤を更にここに添加し
てもよいことは言うまでもない。
本発明の潤滑油組成物を用いれば、燃焼室で
発生した微細な固形不純物を凝集せしめて粗大化
でき、したがつて該不純物のフイルタ除去が容
易となり、潤滑油又は潤滑系への該不純物の混
入を防止できるので、動弁系の摩耗を著しく抑制
することができ、しかも潤滑油自体の劣化も抑
制されてその使用寿命は延長し、したがつて更
油期間も長くなつて経済的である、などの有益な
効果を得ることが可能となり、各種内燃機関とり
わけデイーゼルエンジン用の潤滑油としてその工
業的価値は極めて大である。
以下に、本発明を実施例に基づいて更に詳細に
説明する。
実施例
第1表に示した組成の各種潤滑油を調製した。
The present invention relates to a lubricating oil composition for diesel engines, and more specifically, it is capable of agglomerating solid impurities such as soot, which are inevitably generated during engine operation, into a particle size that can be removed by a filter or other filtration means. Furthermore, the present invention relates to a lubricating oil composition for a diesel engine that can agglomerate solid impurities, which significantly suppresses wear in a valve train system due to solid impurities, and therefore has a long oil change period and extended service life. Compared to gasoline engines, diesel engines have higher combustion pressure and higher temperatures in the combustion chamber, and due to their combustion mechanism, incomplete combustion is more likely to occur.As a result, diesel engines produce combustion residues or soot caused by oxidative decomposition of lubricating oil, which is insoluble in the oil. A large amount of solid impurities (about 0.2 μm in size) are generated, which inevitably leads to a situation where these contaminate the lubricating oil or lubricating system. If the amount of this mixture increases, first of all, the wear of the valve train such as the Rocker arm and cam becomes severe, and furthermore, the viscosity of the lubricating oil itself increases, resulting in an increase in power loss and a decrease in the cooling ability between the piston and liner. , a clogging phenomenon occurs in the lubrication system, which impedes smooth lubrication management of the diesel engine. In order to solve such problems, traditionally,
In order to prevent oxidative decomposition of lubricating oil, for example, zinc dithiophosphate and the solid impurities mentioned above are dispersed in the oil as fine particles, and in order to prevent them from agglomerating into deposits, so-called cleaning agents are used. Various compounds called dispersants are added to the lubricating oil itself to improve its cleanliness (Japan Lubrication Society, ``Lubrication Handbook'', ed.
(See expanded 6th edition, pp. 310-315, 1982). However, even in this case, there is a limit to the ability to eliminate the negative effects of solid impurities such as soot, and the current situation is that the lubricating oil is changed after a relatively short period of time (usually 5,000 to 10,000 km). In particular, in the case of diesel engines equipped with EGR (exhaust gas recirculation) devices, which have been introduced in recent years as an exhaust gas countermeasure, the amount of soot generated is even greater, so it is difficult to deal with it using the methods described above. It has become virtually impossible to manage lubrication. Therefore, there is a strong desire to develop a lubricating oil that can further improve cleanliness and further suppress wear in valve train systems. While conducting extensive research to achieve the above objective, the present inventors discovered a technical idea that is completely opposite to the conventional technical idea of dispersing solid impurities in oil. Based on this idea, he came up with the idea that if solid impurities were aggregated into coarse particles and captured and removed by a bypass filter installed in the circulation system, the lubricating oil could be circulated in a clean state at all times. When we searched for compounds that would be effective, we were surprised to find that even calcium phenate and magnesium sulfonate, which are already known as detergent and dispersants in commonly used base oils, have base numbers within a specific range. A lubricating oil made by blending a predetermined amount of
We discovered that the lubricating oil composition of the present invention can be aggregated to a size of 1 μm, and developed the lubricating oil composition of the present invention. That is, the solid impurity agglomerating diesel engine lubricating oil composition of the present invention contains 1 to 7% by weight of calcium phenate with a base number of 60 or more and magnesium with a base number of 100 or more in a base oil consisting of mineral oil and/or synthetic oil. The composition is characterized by the addition of 0.1 to 5% by weight of sulfonate and 1 to 5% by weight of alkenylsuccinimide. In the lubricating oil composition of the present invention, the base oil used is not particularly limited, and any mineral oil, synthetic oil, or a mixture of both in an appropriate ratio that is commonly used as a base oil for lubricating oils may be used. good. in this case,
From the viewpoint of maintaining and improving lubricity, reducing power loss, and preventing excessive oil consumption, it is preferable to adjust the kinematic viscosity of the base oil at 100° C. to a range of 3 to 30 centistokes (cSt). The lubricating oil composition of the present invention is constructed by adding calcium phenate, magnesium sulfonate, and alkenyl succinimide, which will be described later, to the base oil described above. First, the base number of the calcium phenate used in the present invention is set in a range of 60 or more.
The upper limit of the base number is not particularly limited, but those with a base value of 300 or less are easily available and convenient. Preferably
It is 100-250. In addition, the base number as used in the present invention is a measure of the amount of basic components, and is expressed in mg of potassium hydroxide equivalent to 1 g of basic components.
Its unit is mgKOH/g. If the base number is less than 60, the neutralizing effect on sulfuric acid in the combustion products will not be sufficiently exerted, and as a result, the function to prevent corrosion or wear of the valve train will be reduced, or solid impurities will be present. This can cause problems such as agglomeration and large amounts of deposits inside the engine. Such calcium phenotes are prepared by conventional known methods, such as by carbonating calcium salts of various alkylphenols or sulfurized alkylphenols. At this time, the overall base number is set within the above range by appropriately adjusting the type of raw materials used (for example, the type of alkyl group), the quantitative ratio, the degree of carbonation, etc. The amount of calcium phenate added is set at 1 to 7% by weight based on the total weight of the lubricating oil to be prepared.
Preferably it is 3 to 6% by weight. If the amount added is less than 1% by weight, no effect will be obtained, and if it exceeds 7% by weight, disadvantages such as accelerated wear of the valve train will occur. Next, the magnesium sulfonate used in the present invention is set to have a base value of 100 or more, and an addition amount of 0.1 to 5% by weight. The upper limit of the base number is not particularly limited, but those with a base value of 450 or less are easily available. Preferably 200-450, 0.5, respectively
~4% by weight. When the base number is less than 100, the aggregation effect is reduced and solid impurities are finely dispersed, resulting in an inconvenient situation in which the wear-inhibiting effect on the valve train is reduced. In addition, the amount added is less than 0.1% by weight or 5% by weight
If it exceeds this amount, the above-mentioned aggregation effect will not be exhibited. Such magnesium sulfonates can be prepared by carbonating magnesium salts of various aliphatic sulfonic acids or aromatic sulfonic acids, and in this case, the same steps as in the case of calcium phenate preparation are made. In this embodiment, it is necessary to adjust the base number to the above-mentioned range of 100 or more. Alkenyl succinimide, which is the third component of the additive according to the present invention, is added mainly to prevent low-temperature sludge during engine operation and to adjust the cohesive force of solid impurities together with the calcium phenate and magnesium sulfonate. . The amount added is set at 1 to 5% by weight based on the total weight of the lubricating oil composition. Preferably it is 2 to 4% by weight. If the amount added is less than 1% by weight, the effect of the addition will not be exhibited, and if it exceeds 5% by weight, an inconvenient situation will occur in which the effect of aggregating solid impurities is hindered. Examples of alkenyl succinimide include:
A polyolefin having a molecular weight of 300 to 5,000 is reacted with maleic anhydride to form monoalkenyl succinic anhydride, which is then further reacted with a polyamine such as tetraethylenepentamine to be imidized. Also, special public service 1977-8013, special public service 1977-8013,
Boron compound derivatives of alkenylsuccinimides such as those described in JP-A No. 8014, JP-A No. 51-52381, JP-A No. 51-130408, and JP-A No. 54-87705 can also be used. In the present invention, polyptenyl succinimide of tetraethylpentamine is preferred. The lubricating oil composition of the present invention is basically composed of the above ingredients, but in order to further increase the effect, calcium sulfonate with a base number of 80 or less is added to 20% of the lubricating oil composition.
Adding less than 0.5% by weight, preferably 0.5 to 10% by weight, will further improve the soot in the lubricating oil and the wear condition of the valve train. In addition, commonly used oil-based agents (higher alcohols, etc.), extreme pressure agents (lead soap, etc.), viscosity index improvers (isobutylene polymers, etc.), antifoaming agents (silicone oil, etc.), and antioxidants (zinc dithiophosphate, etc.) It goes without saying that various additives such as the following may be further added here. By using the lubricating oil composition of the present invention, fine solid impurities generated in the combustion chamber can be agglomerated and coarsened, making it easy to remove the impurities through a filter, thereby preventing the impurities from entering the lubricating oil or lubricating system. Since contamination can be prevented, wear in the valve train system can be significantly suppressed, and deterioration of the lubricating oil itself is also suppressed, extending its service life and, therefore, requiring longer oil replacement periods, making it more economical. It is possible to obtain beneficial effects such as , etc., and its industrial value as a lubricating oil for various internal combustion engines, especially diesel engines, is extremely large. The present invention will be explained in more detail below based on examples. Examples Various lubricating oils having the compositions shown in Table 1 were prepared.
【表】【table】
【表】
各潤滑油につき、潤滑系に網目寸法0.8μmのバ
イパスフイルタを備え、かつEGRを装着したト
ヨタL型デイーゼルエンジン(排気量2200c.c.)を
用いて、第2表に示した条件でサイクルテストを
行なつて性能を評価した。[Table] For each lubricating oil, the conditions shown in Table 2 were used using a Toyota L-type diesel engine (displacement 2200c.c.) equipped with a bypass filter with a mesh size of 0.8μm in the lubrication system and equipped with EGR. A cycle test was conducted to evaluate the performance.
【表】
48サイクル運転後、各潤滑油を取り出し、その
100℃における動粘度(cSt)をJISK2283法で測
定し、潤滑油中に混入している固形不純物を
ASTM D893B法に従つて計量した。また、試験
後のロツカーパツドの損傷状態を0〜100のデメ
リツト評点で表わし(0:最良,100:最悪)動
弁系の摩耗状態を評定した。以上の結果を第1表
に一括して示した。
なお、第1表中参考例の試験結果は、潤滑系に
バイパスフイルタを設けなかつたときのデータで
ある。
試験例
試料として以下のものを用いた。
(イ) 実施例1の組成物
(ロ) 実施例6の 〃
(ハ) 鉱油88.2%、塩基価330のカルシウムスルホ
ネート3.0%、テトラエチレンペンタミンのポ
リブテニルこはく酸イミド(ポリブテニル基の
分子量1000)3.0%、ジチオリン酸亜鉛0.8%及
びエチレン−プロピレン共重合体5.0%(いず
れも重量%)の組成物
(ニ) 鉱油85.7%、塩基価25のカルシウムスルホネ
ート2.5%、塩基価330のカルシウムスルホネー
ト3.0%、テトラエチレンペンタミンのポリブ
テニルこはく酸イミド(ポリブテニル基の分子
量1000)3.0%、ジチオリン酸亜鉛0.8%及びエ
チレン−プロピレン共重合体5.0%(いずれも
重量%)の組成物
(ホ) 比較例3の組成物
試料99gと標準煤(カーボンブラツクHAF,
旭カーボン(株)製)1gとを混合し、80℃で8時間
加熱撹拌した。
このものをセル上に滴下し、昇温機構付顕微鏡
にセツトした後、10℃/分で昇温させながら倍率
200倍で観察した。100〜150℃における煤の分散
状態で凝集性の有無を判断した。顕微鏡視野の様
子をスケツチしたものを第1図b〜dに示した。
実施例の組成物である試料イ及び試料ロのそれぞ
れを用いて昇温させた後の煤は、双方とも良好に
凝集した。そのときの煤の概略図を第1図dに示
す。比較例の組成物である試料ハを用いて昇温さ
せた後の煤は、凝集が不十分であつた。そのとき
の煤の概略図を第1図bに示す。比較例の組成物
である試料ニ及び試料ホのそれぞれを用いて昇温
させた後の煤は、双方ともほとんど凝集しなかつ
た。そのときの煤の概略図を第1図Cに示す。な
お、第1図aには、試料イ〜ホを用いて昇温する
前の煤の概略図を示す。
第1図a〜dより、本発明の組成物である試料
イ及びロは温度を上げると明らかに凝集すること
がわかる。それに対し、従来のタイプの組成物で
ある試料ハ,ニ及びホは凝集性が小さく、分散剤
として働いていることがわかる。
評価
本発明の組成物とマグネシウムスルホネート
を含有しない組成物との対比(比較例2と実施
例1〜12)
マグネシウムスルホネートを含有しない比較例
2の動弁系摩耗評点(デメリツト評点)は49であ
り、潤滑油中の固形不純物量は3.3重量%である。
これに対し、実施例1〜12では、いずれも摩耗評
点が、6.0以下であり、固形不純物量が、1.4重量
%以下である。
つまり、カルシウムフエネートのみでは、固形
不純物に対し、凝集効果を示さない。
本発明の組成物とマグネシウムスルホネート
に代えてカルシウムスルホネートを用いた組成
物との対比(比較例3及び12と実施例10)
マグネシウムスルホネートを塩基価330のカル
シウムスルホネートに置き換えた比較例12では、
摩耗評点が、48であり、固形不純物量が、3.4重
量%である。
これは、マグネシウムスルホネートを用いた実
施例10の摩耗評点が、1.0であり、固形不純物量
が、1.0重量%であることからも明らかなように、
この置き換えによつて、潤滑油中の固形不純物量
が増加し、動弁系の摩耗が著しくなつたことを示
す。
また、マグネシウムスルホネートを塩基価25の
カルシウムスルホネートに置き換えた比較例3も
同様の傾向を示す(摩耗評点40、固形不純物量
2.2重量%)。
つまり、カルシウムフエネートとカルシウムス
ルホネートとを組み合わせても固形不純物に対
し、凝集効果を示さない。
本発明の組成物とマグネシウムスルホネート
の塩基価が100未満の組成物との対比(比較例
8及び9と実施例1〜12)
マグネシウムスルホネートの塩基価が50及び80
の比較例8及び9の摩耗評点は、32及び45であ
り、また固形不純物量は、2.3及び3.2であつて、
実施例1〜12のいずれよりも大幅に高い値を示
す。
つまり、カルシウムフエネートとマグネシウム
スルホネートとの組み合わせであつても、マグネ
シウムスルホネートの塩基価が100未満では、固
形不純物に対し、凝集効果を示さない。
本発明の組成物とカルシウムフエネートに代
えてマグネシウムフエネートを用いた組成物と
の対比(比較例7と実施例10)
マグネシウムフエネートを用いた比較例7で
は、摩耗評点が32であり、固形不純物量が2.3重
量%である。
これは、カルシウムフエネートを用いた実施例
10と対比すると、効果の差が著しい。
つまり、マグネシウムフエネートと塩基価が
100以上のマグネシウムスルホネートとの組み合
わせでは、固形不純物に対し、凝集効果を示さな
い。
本発明の組成物とカルシウムフエネートの塩
基価が60未満の組成物との対比(比較例5及び
6と実施例1〜12)
カルシウムフエネートの塩基価が25及び50の比
較例6及び5の摩耗評点は、ともに36であり、ま
た固形不純物量は、2.8及び2.0であつて、実施例
1〜12のいずれよりも高い値を示す。
つまり、塩基価が60未満のカルシウムフエネー
トと塩基価が100以上のマグネシウムスルホネー
トとの組み合わせでは、固形不純物に対し、凝集
効果を示さない。
その他
カルシウムフエネートの配合量が1重量%未満
の組成物(比較例10及び11)、またアルケニルこ
はく酸イミドを含有しない組成物(比較例4及び
5)も上記〜と同様の傾向を示す。
以上のことからも明らかなように、塩基価が60
以上のカルシウムフエネートと、塩基価が100以
上のマグネシウムスルホネートと、アルケニルこ
はく酸イミドとを特定の配合量で組み合わせてな
る本発明の固形不純物凝集性デイーゼルエンジン
用潤滑油組成物は、固形不純物を良好に凝集させ
ることによりこれをろ過することができ、デイー
ゼルエンジンにおける動弁系の摩耗を大幅に抑制
している。[Table] After 48 cycles of operation, remove each lubricating oil and
The kinematic viscosity (cSt) at 100℃ is measured using the JISK2283 method, and solid impurities mixed in the lubricating oil are determined.
Weighed according to ASTM D893B method. In addition, the state of damage to the rocker pad after the test was expressed on a demerit rating scale of 0 to 100 (0: best, 100: worst) to evaluate the wear state of the valve train. The above results are collectively shown in Table 1. The test results of the reference examples in Table 1 are data obtained when no bypass filter was provided in the lubrication system. Test Example The following samples were used. (a) Composition of Example 1 (b) Example 6 (c) 88.2% mineral oil, 3.0% calcium sulfonate with base number 330, polybutenyl succinimide of tetraethylenepentamine (molecular weight of polybutenyl group 1000) 3.0 %, zinc dithiophosphate 0.8% and ethylene-propylene copolymer 5.0% (all % by weight) (d) 85.7% mineral oil, 2.5% calcium sulfonate with a base number of 25, 3.0% calcium sulfonate with a base number of 330, Composition of 3.0% polybutenylsuccinimide (polybutenyl group molecular weight 1000) of tetraethylenepentamine, 0.8% zinc dithiophosphate, and 5.0% ethylene-propylene copolymer (all weight %) (E) Composition of Comparative Example 3 99g of sample and standard soot (carbon black HAF,
(manufactured by Asahi Carbon Co., Ltd.) and heated and stirred at 80° C. for 8 hours. Drop this onto the cell, set it on a microscope with a heating mechanism, and increase the magnification while raising the temperature at 10℃/min.
Observed at 200x magnification. The presence or absence of cohesion was determined based on the state of soot dispersion at 100-150°C. Sketches of the microscopic field of view are shown in Figures 1 b to d.
After raising the temperature using each of Sample A and Sample B, which are compositions of Examples, both soots coagulated well. A schematic diagram of the soot at that time is shown in Figure 1d. The soot after heating using Sample C, which is a composition of a comparative example, was insufficiently agglomerated. A schematic diagram of the soot at that time is shown in Figure 1b. After raising the temperature using each of Sample 2 and Sample E, which are compositions of comparative examples, soot hardly aggregated in both samples. A schematic diagram of the soot at that time is shown in Figure 1C. In addition, FIG. 1a shows a schematic diagram of soot before heating using samples I to E. From FIGS. 1a to 1d, it can be seen that Samples A and B, which are the compositions of the present invention, clearly aggregate when the temperature is increased. In contrast, Samples C, D, and E, which are conventional compositions, have low agglomeration, indicating that they function as a dispersant. Evaluation Comparison between the composition of the present invention and a composition that does not contain magnesium sulfonate (Comparative Example 2 and Examples 1 to 12) The valve train wear score (disadvantage score) of Comparative Example 2 that does not contain magnesium sulfonate is 49. , the amount of solid impurities in the lubricating oil is 3.3% by weight.
On the other hand, in Examples 1 to 12, the wear score is 6.0 or less, and the amount of solid impurities is 1.4% by weight or less. In other words, calcium phenate alone does not exhibit a flocculating effect on solid impurities. Comparison between the composition of the present invention and a composition using calcium sulfonate in place of magnesium sulfonate (Comparative Examples 3 and 12 and Example 10) In Comparative Example 12, in which magnesium sulfonate was replaced with calcium sulfonate having a base number of 330,
The wear rating is 48 and the amount of solid impurities is 3.4% by weight. This is clear from the fact that the wear score of Example 10 using magnesium sulfonate was 1.0 and the amount of solid impurities was 1.0% by weight.
This replacement increased the amount of solid impurities in the lubricating oil, indicating that the wear of the valve train became significant. Comparative Example 3, in which magnesium sulfonate was replaced with calcium sulfonate with a base number of 25, also showed a similar tendency (wear rating: 40, amount of solid impurities).
2.2% by weight). In other words, even when calcium phenate and calcium sulfonate are combined, they do not exhibit a flocculating effect on solid impurities. Comparison between the composition of the present invention and a composition in which the base number of magnesium sulfonate is less than 100 (Comparative Examples 8 and 9 and Examples 1 to 12) The base number of magnesium sulfonate is 50 and 80
The wear ratings of Comparative Examples 8 and 9 were 32 and 45, and the solid impurity amounts were 2.3 and 3.2.
This value is significantly higher than any of Examples 1-12. In other words, even in the case of a combination of calcium phenate and magnesium sulfonate, if the base number of the magnesium sulfonate is less than 100, no flocculating effect is shown on solid impurities. Comparison between the composition of the present invention and a composition using magnesium phenate instead of calcium phenate (Comparative Example 7 and Example 10) In Comparative Example 7 using magnesium phenate, the wear rating was 32, The amount of solid impurities is 2.3% by weight. This is an example using calcium phenate
When compared with 10, the difference in effectiveness is remarkable. In other words, magnesium phenate and base number are
In combination with magnesium sulfonate of 100 or more, it shows no flocculating effect on solid impurities. Comparison between the composition of the present invention and a composition in which calcium phenate has a base number of less than 60 (Comparative Examples 5 and 6 and Examples 1 to 12) Comparative Examples 6 and 5 in which calcium phenate has a base number of 25 and 50 The wear scores of both examples are 36, and the amount of solid impurities is 2.8 and 2.0, which are higher values than any of Examples 1 to 12. In other words, the combination of calcium phenate with a base number of less than 60 and magnesium sulfonate with a base number of 100 or more does not exhibit a flocculating effect on solid impurities. Others Compositions containing less than 1% by weight of calcium phenate (Comparative Examples 10 and 11) and compositions containing no alkenylsuccinimide (Comparative Examples 4 and 5) also exhibit the same tendency as described above. As is clear from the above, the base number is 60
The solid impurity agglomerating diesel engine lubricating oil composition of the present invention is a combination of the above calcium phenate, magnesium sulfonate having a base number of 100 or more, and alkenyl succinimide in specific amounts. By aggregating it well, it can be filtered, and wear of the valve train in diesel engines is greatly suppressed.
第1図a〜dは、デイーゼルエンジン潤滑油組
成物と標準煤を混合して昇温した際の試料を顕微
鏡で観察した時の概略図(スケツチ)である。第
1図aはコントロールで、試験例中の各試料の昇
温前の状態、第1図bは試料ハ、第1図cは試料
ニ及びホ、第1図dは試料イ及びロに対応してい
る。
FIGS. 1A to 1D are schematic views (sketches) of a sample obtained by mixing a diesel engine lubricating oil composition and standard soot and heating the mixture and observing it under a microscope. Figure 1a shows the control, and corresponds to the state of each sample in the test example before heating up, Figure 1b corresponds to sample C, Figure 1c corresponds to samples D and H, and Figure 1d corresponds to samples A and B. are doing.
Claims (1)
価60以上のカルシウムフエネート1〜7重量%、
塩基価100以上のマグネシウムスルホネート0.1〜
5重量%及びアルケニルこはく酸イミド1〜5重
量%を添加した組成であることを特徴とする固形
不純物凝集性デイーゼルエンジン用潤滑油組成
物。 2 該基油の動粘度が、100℃で3〜30センチス
トークスである特許請求の範囲第1項記載の固形
不純物凝集性デイーゼルエンジン用潤滑油組成
物。[Claims] 1. 1 to 7% by weight of calcium phenate having a base value of 60 or more in a base oil consisting of mineral oil or/and synthetic oil;
Magnesium sulfonate with base number 100 or more 0.1~
1. A lubricating oil composition for a diesel engine capable of aggregating solid impurities, characterized in that the composition contains 5% by weight of an alkenylsuccinimide and 1 to 5% by weight of an alkenylsuccinimide. 2. The solid impurity agglomerating diesel engine lubricating oil composition according to claim 1, wherein the base oil has a kinematic viscosity of 3 to 30 centistokes at 100°C.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58114334A JPS606790A (en) | 1983-06-27 | 1983-06-27 | Lubricating oil composition for diesel engine |
| JP4103823A JPH0670236B2 (en) | 1983-06-27 | 1992-03-31 | Method for removing solid impurities from diesel engine lubricating oil |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58114334A JPS606790A (en) | 1983-06-27 | 1983-06-27 | Lubricating oil composition for diesel engine |
| JP4103823A JPH0670236B2 (en) | 1983-06-27 | 1992-03-31 | Method for removing solid impurities from diesel engine lubricating oil |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4103823A Division JPH0670236B2 (en) | 1983-06-27 | 1992-03-31 | Method for removing solid impurities from diesel engine lubricating oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS606790A JPS606790A (en) | 1985-01-14 |
| JPH0329839B2 true JPH0329839B2 (en) | 1991-04-25 |
Family
ID=26444413
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58114334A Granted JPS606790A (en) | 1983-06-27 | 1983-06-27 | Lubricating oil composition for diesel engine |
| JP4103823A Expired - Lifetime JPH0670236B2 (en) | 1983-06-27 | 1992-03-31 | Method for removing solid impurities from diesel engine lubricating oil |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4103823A Expired - Lifetime JPH0670236B2 (en) | 1983-06-27 | 1992-03-31 | Method for removing solid impurities from diesel engine lubricating oil |
Country Status (1)
| Country | Link |
|---|---|
| JP (2) | JPS606790A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0660317B2 (en) * | 1986-07-07 | 1994-08-10 | 日立建機株式会社 | Diesel engine lubrication system |
| GB9519668D0 (en) * | 1995-09-27 | 1995-11-29 | Exxon Chemical Patents Inc | Low chlorine low ash crankcase lubricant |
| JP2000080388A (en) | 1998-09-03 | 2000-03-21 | Tonen Corp | Lubricating oil composition |
| JP2000087067A (en) | 1998-07-17 | 2000-03-28 | Tonen Corp | Lubricating oil composition for internal combustion engines |
| US6191081B1 (en) | 1999-12-15 | 2001-02-20 | Exxonmobil Research And Engineering Company | Long life medium and high ash oils with enhanced nitration resistance |
| US6140282A (en) * | 1999-12-15 | 2000-10-31 | Exxonmobil Research And Engineering Company | Long life lubricating oil composition using particular detergent mixture |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3853774A (en) * | 1972-12-20 | 1974-12-10 | Chevron Res | Process for preparing oil-soluble basic magnesium salts |
| JPS54103404A (en) * | 1978-02-02 | 1979-08-14 | Nippon Oil Co Ltd | Lublicant composition for an internal combustion engine |
| AU549639B2 (en) * | 1981-07-01 | 1986-02-06 | Chevron Research Company | Lubricating oil composition to improve fuel economy |
| AU550869B2 (en) * | 1981-08-03 | 1986-04-10 | Chevron Research Company | Lubricating oil with borated long chain 1,2 alkane diol friction modifier |
-
1983
- 1983-06-27 JP JP58114334A patent/JPS606790A/en active Granted
-
1992
- 1992-03-31 JP JP4103823A patent/JPH0670236B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS606790A (en) | 1985-01-14 |
| JPH05295382A (en) | 1993-11-09 |
| JPH0670236B2 (en) | 1994-09-07 |
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