JPH0563509B2 - - Google Patents

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Publication number
JPH0563509B2
JPH0563509B2 JP63065934A JP6593488A JPH0563509B2 JP H0563509 B2 JPH0563509 B2 JP H0563509B2 JP 63065934 A JP63065934 A JP 63065934A JP 6593488 A JP6593488 A JP 6593488A JP H0563509 B2 JPH0563509 B2 JP H0563509B2
Authority
JP
Japan
Prior art keywords
parts
weight
formula
carbon atoms
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 - Lifetime
Application number
JP63065934A
Other languages
Japanese (ja)
Other versions
JPS63254161A (en
Inventor
Deeru Gurooenhofu Yuujin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Silicones Corp
Original Assignee
Dow Corning Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dow Corning Corp filed Critical Dow Corning Corp
Publication of JPS63254161A publication Critical patent/JPS63254161A/en
Publication of JPH0563509B2 publication Critical patent/JPH0563509B2/ja
Granted legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M111/00—Lubrication compositions characterised by the base-material being a mixture of two or more compounds covered by more than one of the main groups C10M101/00 - C10M109/00, each of these compounds being essential
    • C10M111/04—Lubrication compositions characterised by the base-material being a mixture of two or more compounds covered by more than one of the main groups C10M101/00 - C10M109/00, each of these compounds being essential at least one of them being a macromolecular organic compound
    • C—CHEMISTRY; METALLURGY
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    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
    • C10M107/02—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
    • C10M107/18—Hydrocarbon polymers modified by oxidation
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    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
    • C10M107/50—Lubricating compositions characterised by the base-material being a macromolecular compound containing silicon
    • C—CHEMISTRY; METALLURGY
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    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/028—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms
    • C—CHEMISTRY; METALLURGY
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    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/12—Oxidised hydrocarbons, i.e. oxidised subsequent to macromolecular formation
    • C10M2205/123—Oxidised hydrocarbons, i.e. oxidised subsequent to macromolecular formation used as base material
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/02—Hydroxy compounds
    • C10M2207/023—Hydroxy compounds having hydroxy groups bound to carbon atoms of six-membered aromatic rings
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2211/00—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
    • C10M2211/04—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen, halogen, and oxygen
    • C10M2211/044—Acids; Salts or esters thereof
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    • C10M2215/00—Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant Compositions
    • C10M2215/02—Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/06—Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
    • C10M2215/064—Di- and triaryl amines
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    • C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/06—Thio-acids; Thiocyanates; Derivatives thereof
    • C10M2219/062—Thio-acids; Thiocyanates; Derivatives thereof having carbon-to-sulfur double bonds
    • C10M2219/066—Thiocarbamic type compounds
    • C10M2219/068—Thiocarbamate metal salts
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    • C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
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    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
    • C10M2223/041—Triaryl phosphates
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    • C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04—Phosphate esters
    • C10M2223/042—Metal salts thereof
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    • C10M2229/02—Unspecified siloxanes; Silicones
    • C10M2229/025—Unspecified siloxanes; Silicones used as base material
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    • C10M2229/04—Siloxanes with specific structure
    • C10M2229/0405—Siloxanes with specific structure used as base material
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    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00—Metal present as such or in compounds
    • C10N2010/10—Groups 5 or 15
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    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01—Physico-chemical properties
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    • C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00—Specified use or application for which the lubricating composition is intended
    • C10N2040/08—Hydraulic fluids, e.g. brake-fluids

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Lubricants (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、広い温度範囲にわたつて使用するこ
とができ、しかも比較的高い引火点を示す作動液
組成物に関する。より詳しく述べるならば、この
発明の液体は本質的に、合成水素化ポリα−オレ
フインを配合したジメチルシロキサン/アルキル
メチルシロキサンコポリマーからなる。この発明
は更に、上記の組成物を油圧系統に使用する方法
に関する。 〔従来の技術及び発明が解決しようとする課題〕 一定のシリコーン流体は、耐剪断性、耐熱劣化
性、及び耐酸化性劣化性が優れていることが知ら
れている。更に、典型的な炭化水素潤滑油又は作
動液とは違つて、それらは比較的平たい粘度−温
度プロフアイルを維持する。その反面、一般にこ
れらのシリコーンには、多くの油圧用途において
きわめて重要な性質である、鉱油のような炭化水
素により例示される鋼−鋼接触における高度の潤
滑性がない。この問題は、シリコーン「基礎液」
に一定の潤滑性添加剤を混ぜ合わせることにより
ある程度まで解決することができる。 これらの液体タイプの両方の基本的に有利な点
を同時に利用することに苦心するうちに、何人か
の研究者はそれらを種々の潤滑剤組成物において
組み合わせた。例えば、英国特許第1224885号明
細書において、マツケンジー(Mackenzie)は、
鉱油と、これのための粘度指数向上剤としてのホ
モポリマーのジオルガノポリシロキサンであつて
有機基の大部分がメチル基であるものとを含んで
なる組成物を開示する。これらの組成物のシロキ
サンポリマーでは、残りの有機基は、それらを鉱
油に溶解性にするのに十分なだけの量の6〜30個
の炭素原子を有するアルキル基、アルカリール
基、又はアラルキル基より選択することができ
る。 モロ(Morro)らは、米国特許第4059534号明
細書において、100〓(38℃)での粘度が100000
〜1000000cSであるポリジメチルシロキサンを1
〜50重量%含んでなる潤滑油組成物であつて、こ
の組成物の残りは、アルケン、イソパラフイン、
及びナフテン類より選択することができる。−65
〓(−54℃)での粘度が40000cS未満の炭化水素
油であるものを教示する。この開示により主張さ
れた当該技術への主要な貢献は、炭化水素油に高
粘度ポリジメチルシロキサンを溶解させて、粘度
−温度特性を改善した潤滑用組成物であつて低温
において当該組成物よりシロキサン成分が分離し
ないものを提供することである。 1986年4月16日に公表された欧州特許出願第
0177825A1号公報は、有機基が炭素原子数1〜7
のアルキル基又はフエニル基より選択されるオル
ガノメチルシロキサン単位と、アルキル基が6〜
16個の炭素原子を有することのできるアルキルメ
チルシロキサン単位とを含有しているシリコーン
コポリマーを含んでなる潤滑油の調製を記載す
る。 これらのコポリマーは、流動点が−15℃未満で
なければならず、且つ鉱油、合成潤滑油、及びそ
のような油に一般に使用される潤滑性添加剤と混
和可能でなければならないという点で、更に制限
を有する。 より最近になつて、使用温度範囲の広い耐火性
の軍用航空機作動液の必要性が、グシユウエンダ
ー(Gschwender)らにより潤滑工学
(Lubrieation Engineering)第42巻、第485〜490
頁(1986年)において実証された。一方では、鉱
油に基づく作動液(MIL−H−5606)は広範囲
にわたつて軍用航空機に使用されており、−54℃
まで下げて運転されると考えられてはいるけれど
も、この流体には二つの大きな欠点がある。比較
的低いおよそ100〜110℃の引火点は、この流体を
危険なまでに簡単に発火しやすく、また一度燃焼
が始まれば速い速度で伝播しやすいものにする。
更に、この流体の剪断安定性は、特に近代的空軍
航空機におけるより高い作動圧力(及びそれに関
連する大きな剪断速度)に向けての設計の傾向を
考慮すれば、望ましい剪断安定性よりも低い。他
方では、合成水素化ポリα−オレフイン流体での
経験は、これらの流体は引火点が高く(>205℃)
また剪断に対して比較的安定であるという点で良
好であつた。あいにくながら、そのようなポリα
−オレフインに基づく作動液は、極寒での運転に
使用するためには低温での粘度があまりに高い
か、あるいはそれらの引火点が低過ぎる(すなわ
ち低分子量のポリα−オレフインを使用する場
合)。 従つて、グシユウエンダーらは、いわゆる「低
温MIL−H−83282」液についての目標特性の一
覧表であつて、両方のMIL仕様の見地を組合わ
せ且つ次に示すとおりの粘度の制限を包含するも
のを提示する。温度(℃) 粘度(eS) −54 2500(最大) −40 500(最大) 100 3.5(最小) 135 1.5(最小) 上記のMIL−H−83282液の高い引火点は、上
記の低温粘度と共には両立できないということが
更に認められ、そして、少なくとも163℃及び191
℃の析衷目標値がそれそれ引火点及び燃焼点につ
いて設定された。その上、成功する候補の流体の
主要必要条件は、現行の油圧系統における「排液
−充液(drain−and−fill)」置換を可能にするよ
うに、この流体が既存の軍用液(すなわちMIL
−H−5606及びMIL−H−83282の液)と相容性
である、ということであつた。 上述の特許明細書の技術的開示のいずれも、−
54℃から135℃までの耐火性作動液に使用するの
に適した候補の必要とする粘度−温度プロフアイ
ルと引火点とを組合せた基礎液組成物を形成す
る、ジメチルシロキサン/アルキルメチルシロキ
サンコポリマーとポリα−オレフインとの混合物
を教示しない。 先に説明した低温粘度は、一定のジメチルシロ
キサン/アルキルメチルシロキサンコポリマーに
デセン−1のオリゴマーに基づく水素化ポリα−
オレフインを混合することにより達成することが
できる、ということが発見された。思いもよらぬ
ことながら、これは、油圧用途に使用するための
ジメチルシロキサン/アルキルメチルシロキサン
コポリマー液及びポリα−オレフイン液の両者の
望ましい他の特徴はもちろん、少なくとも163℃
の引火点をなお維持しながら果すことができる。
更に、このように形成された組成物は、既存の軍
用液(すなわちMIL−H−5606及びMIL−H−
83282の液)と相容性であり、そのため現行の油
圧系統での「排液−充液」置換が可能である。 〔課題を解決するための手段及び作用効果〕 従つて、この発明は、(A)ジメチルシロキサン/
アルキルメチルシロキサンコポリマーであつて、
下記の平均式、すなわち、 (この式において、Meはメチル基を表わし、
R′は炭素原子数1〜10のアルキル基より独立に
選択され、Rは炭素原子数4〜10のアルキル基を
表わし、xは5から15までの平均値を有し、yの
値は0.5から4までであり、そしてy/xの比率
は0.3以下である)により表わされるもの40〜90
重量部、及び、(B)下記の式、すなわち、 で表わされる合成水素化ポリα−オレフイン10〜
60重量部から本質的になる均一作動液組成物であ
つて、上記の成分(A)及び(B)を合計100重量部有す
るものに関する。 この発明は更に、成分(B)が下記の式、すなわ
ち、 で表わされる同様の組成物に関する。 この発明はなお更に、成分(B)がデセン−1の二
量体、三量体、又四量体から選択され、且つ上記
の均一作動液の粘度が−54℃において2500cS以
下、100℃において少なくとも3.5cSであり、開放
式引火点が少なくとも163℃である同様の組成物
に関する。 この発明はまた、油圧系統で力を伝達する方法
における改良であつて、当該系統における作動液
として先に説明した組成物を用いることを包含す
るものに関する。 本発明は、(A)ジメチルシロキサン/アルキルメ
チルシロキサンコポリマーと(B)合成水素化ポリα
−オレフインとの均一混合物から本質的になる作
動液組成物に関する。 本発明の成分(A)は、下記の平均式、すなわち、 で表わすことができ、この式においてMeがメチ
ル基を表わし、そしてRが炭素原子数4〜10の直
線状又は技分れしたアルキル基、例えばn−ペン
チル基、イソペンチル基、n−ヘキシル基、n−
ヘプチル基、n−オクチル基、ジイソブチル基、
n−ノニル基、又はn−デシル基のようなもので
あるコポリマーである。直鎖アルキル基は枝分れ
構造以上に好ましい。Rがn−ヘキシル基又はn
−オクチル基より選択されることが、更に好まし
い。末端のケイ素原子についてのR′基は、1〜
10の炭素原子を有する同一又は別個の短鎖アルキ
ル基、例えばメチル基、エチル基、プロピル基、
ブチル基、ヘキシル基、オクチル基、又はデシル
基のようなものであり、メチル基が好ましい。 上記の式中のxの値は、5から15までの範囲で
よく、好ましくは6から12までである。yの値
は、相応じて0.5〜4までの範囲でよく、好まし
くは0.5から3までである。しかしながら、yの
値は、y/xの比率が0.3以下となるように制限
される。上記の一般式においては、当該コポリマ
ー液の粘度が25℃において約5〜50センチストー
クス(cS)の範囲であるようにx及びyを選定
することが好ましい。好ましくは、この粘度は約
10〜20cSである。本発明の大いに好ましい態様
は、Rがn−ヘキシル基、R′がメチル基であり、
xが約6、そしてyが約1である場合、又はRが
n−オクチル基、R′がメチル基であり、xが約
8、そしてyが0.5である場合に得られる。 本発明の上記のコポリマーは、当業界において
周知の方法により調製されよう。例えば、それら
は適当なジオルガノジアルコキシシラン又はジオ
ルガノジクロロシランの共加水分解及びその後の
縮合により合成することができる。このアプロー
チでは、所望量の末端キヤツピング反応物
(R′)3SiZを反応混合物に含ませて、生成物の分子
量を調節する(すなわち、末端キヤツピング反応
物が多くなればより低分子量の生成物が生じる)。
この末端キヤツピング反応物のR′基は、成分(A)
について先に示したものと同じである。Z基は、
ハロゲン(例えば塩素、フツ素、もしくは臭素)
又はアルコキシ基(例えばメトキシ基、エトキシ
基)のような加水分解可能種である。 当該コポリマーを合成するのに当てることがで
きるもう一つの方法は、前述の末端キヤツピング
反応物の存在下における酸又は塩基に触媒される
ジオルガノシクロシロキサンの平衡反応である。 更にもう一つの好ましい方法は、次に掲げる一
般式、すなわち、 (この式において、Meはメチル基を表わし、ま
たR′は先に定義されたものである)のSiH官能性
コポリマー中間体を調製する工程を含むものであ
る。これらの中間体は、当業者において周知のも
のであつて、種々の割合での商業的に入手可能な
ポリメチル水素シロキサンと環式ジメチルシロキ
サンとの酸平衡により調製されよう。この中間体
の分子量は、ヘキサメチルジシロキサンのような
末端キヤツピング単量体を適当量加えることによ
り調節されよう。SiH官能性中間体は、その後お
よそ25%過剰の所望のアルケンと反応させて、前
者のSiH原子団に後者を化学的に付加させる。 この付加反応は、当業界において公知の白金錯
体によつて触媒される。 本発明の成分(B)は、デセン−1の二量体、三量
体、又は四量体より選択した少なくとも一つの合
成水素化ポリα−オレフインであつて、下記の式
により表わすことができる。 (二量体) (三量体) (四量体) この発明の好ましい態様においては、成分(B)は
ポリα−オレフイン三量体である。しかしなが
ら、低温MIL−H−83282の目標の必要条件を満
たすのに必要な高引火点及び粘度−温度プロフア
イルを、成分(A)に上記の二量体、三量体、及び四
量体の混合物を混ぜ合わせることにより達成する
ことが可能であり、これは日常的な実験により決
めることができよう。 ポリα−オレフイン液は、当業界においてよく
知られており、触媒重合及び水素添加により単量
体のデセン−1から調製することができる。興味
があれば、例えば、カツプルス(Cupples)らに
より1981年10月の米政府報告書AFWAL−TR−
81−4109(ライト−パターソン(Wright−
Patterson)空軍基地、空軍ライト(Wright)航
空研究所、材料実験室)に概説された方法に参照
されたい。これらの液は、テキサス州ヒユースト
ンのガルフ・オイル・ケミカルズ社(Gulf Oil
Chemicals Co.)より、シンフルイド
(SYNFLUID)の商品名で商業的に入手可能で
ある。 本発明の組成物は、成分(A)及び(B)を単純に混合
してそれらの均質混合物を形成させて調製されよ
う。混合方法は、特に重要というわけではなく、
当業界において知られている通常使用される方法
のうちのどれを用いてもよい。そのように作られ
た混合物は、通常は、後に説明する潤滑性添加剤
及び他の補助剤がそれに組み合わされて完全に配
合された作動液が作られるという点で、「基礎液」
と呼ばれる。 成分(B)がデセン三量体である場合、40〜90重量
部の成分(A)を60〜10部の成分(B)と混合して本発明
の組成物100部を作る。しかしながら、40〜60重
量部の成分(A)を60〜40部のデセン三量体と混合す
ることが好ましい。最も好ましくは、等重量のデ
セン三量体と成分(A)のジメチルシロキサン/アル
キルメチルシロキサンコポリマー液とを使用し、
この場合のジメチルシロキサン/アルキルメチル
シロキサンコポリマー成分は先に説明した好まし
い範囲によつて描写される。 成分(B)がデセン四量体である場合、80〜90重量
部の成分(A)を20〜10部の成分(B)と混合して本発明
の組成物100部を作る。 これとは別に、本発明の組成物は、低温MIL
−H−83282の目標により要求される基本的な物
理的性質によつて定義してもよい。この場合に
は、100重量部の組成物は、成分(A)10〜90重量部
と、デセン−14の二量体、三量体、又は四量体よ
り選択した少なくとも一つの合成水素化ポリα−
オレフイン90〜10重量部とからなり、−54℃にお
ける粘度が2500cS以下、100℃における粘度が少
なくとも3.5cSあり、且つ開放式引火点が少なく
とも163℃であるようなものである。好ましくは、
40〜60重量部の成分(A)を60〜40部の成分(B)と混合
する。これらの性質は、上記の開示に照して当業
者による日常的な実験によつて容易に得られよ
う。 先に述べたように、一般には種々の添加剤をこ
の発明の基礎液に混入させて完全に配合された作
動液を調製する。リン酸トリクレシル、ジブチル
クロレンデート、及びアンチモンジアルキルージ
チオカルバメートのような、耐摩耗性、又は潤滑
性添加剤は、約1〜10重量パーセントで好ましく
混和される。 ジ(2−エチルヘキシル)セバケート又はリン
酸トリブチルのようなゴム膨潤添加剤は、約1〜
5重量パーセントで混入されよう。これらは、こ
れらの基礎液がゴム成分より可塑剤を滲出させる
ことによりゴム成分を収縮させる傾向があるの
で、典型的にはポリジメチルシロキサンと共に用
いられる。一般には、成分(A)のアルキル含有量も
しくはアルキル基の大きさが増加し、又は成分(B)
がより多く利用されるにつれて、膨潤添加剤の必
要は少なくなる。 約0.1〜0.5重量パーセントの濃度の、p,p′−
ジオクチルジフエニルアミンやブチル化ヒドロキ
シトルエンのような酸化防止剤が、高い使用温度
での酸化からアルキル基を保護するのに一般的に
必要とされる。染料も、主として識別用に低濃度
で加えることができる。 必須のものでない他の添加剤、例えば難燃剤、
脱泡剤、腐食防止剤のようなものも、本発明の基
礎液と組合わせることに有用性が見いだされるか
もしれない。 成分(A)のアルキルメチルシロキサン含有量を増
加させて100%に近づけることは、その結果とし
て得られた基礎液を低温MIL−H−83282の目標
の粘度の必要条件に適合するように配合すること
ができないという点で意に満たないポリマーに帰
着した。その上、アルキル含有量が増加するにつ
れて、油圧系統におけるいずれのゴル成分の膨潤
もまた増加し、いくつかの系統においては望まし
くない結果になつた。 当業者には、低温MIL−H−83282の目標の必
要条件のうちいくつかは基礎液組成物の分子量を
変化させることによつて及び/又は種々の添加剤
を配合することによつて満たすことができるとは
言うものの、先に提示された重要な性質は通常そ
のような操作では調節されない、ということが認
められよう。従つて、例えば、基礎液(すなわち
本発明のシロキサンコポリマーとポリα−オレフ
インとの組成物)が要求される粘度−温度プロフ
アイルと十分に高い引火点とを同時には示さない
場合には、その基礎液を混ぜ合わせて試験のため
に完全に配合された作動液にすることは、一般的
に低温MIL−H−83282の目標の特性を満たすこ
とにはならない。それゆえに、これらの重要な性
質の必要条件に合格しない基礎液組成物は、低温
MIL−H−83282に目標に適合しないと判断され
た。 この発明はまた、油圧系統において作動力(圧
力)を伝えるための改良方法にも関連し、この場
合、作動液は本質的に説明したがシロキサンコポ
リマーとポリα−オレフインとの組成物のうちの
一つからなる。この改良方法では、当該油圧系統
の構成要素のうちの流体含有部は、先に開示した
この発明の組成物で満たされる。ここで考えられ
る油圧系統構成要素の例には、ポンプや、ダイヤ
フラム、油圧管路手段、弁のような流体カツプリ
ング装置や、油圧モーター、ピストン、サーボバ
ルブのような油圧作動手段が含まれる。 この発明の作動基礎液の利用から最も利益を受
ける油圧系統は、−54℃及び135℃の温度極値の間
で運転することが要求され、且つ同時に、作動液
として鉱油を使用する系統以上に向上した耐火性
を要求する油圧系統である。従つて、本発明の方
法は、軍用航空機の油圧系統に関連して最も適当
に使用される。本発明の方法を有利に使用するこ
とができる他の油圧系統には、民間航空機、陸上
及び海上用の軍用輸送車両及び戦闘車両、宇宙
船、及び寒帯領域又は他の寒冷環境で使用するた
めの機械類が含まれる。 〔実施例〕 以下の例は、この発明の組成物を更に説明する
ために提供するものであつて、本発明を限定する
ものと解釈すべきではない。本発明は、特許請求
の範囲に示されている。下記の例における部及び
百分率は全て、反する指示がない限り重量に基づ
くものである。 例 1 スターラー、温度計、凝縮器、添加漏斗、及び
乾燥窒素ガスでパージするための手段を備えたフ
ラスコに、316gのヘキセン−1と、0.7重量パー
セントの白金を与えるようジメチルビニルシロキ
シ基で末端をブロツクしたポリジメチルシロキサ
ンで希釈したジビニルテトラメチルジシロキサン
の塩化白金酸錯体(ウイリング(Willing)の米
国特許第3419593号明細書の例1に従つて調製さ
れた)0.1mlとを加えた。この混合物に、下記の
平均組成、すなわち、 Me3SiO(MeHSiO)4.4(Me2SiO)9.8SiMe3(この式
においてMeはメチル基を表わす)のシロキサン
コポリマー800gを、2時間かけて加えた。反応
は発熱反応であり、温度を25℃と50℃との間に保
持するように内容物を冷却した。結果として得ら
れたコポリマーの計算された平均構造式は、次の
示すとおりであつた。 例 2 上記の例1で調製されたコポリマー400g、平
均式Me3SiO(Me2SiO)4.7SiMe3を有するシロキサ
ン500gと、3個、4個、及び5個のジメチルシ
ロキサン単位を有するジメチルシクロシロキサン
の混合物100gと、水酸化カリウム(KOH)1g
との混合物を、窒素雰囲気下でかき混ぜそして約
160℃に加熱した。約20mlの揮発性生成物を蒸留
により取除いた。残りの混合物は160℃で4時間
更に反応させ、その後室温まで冷却した。トリメ
チルクロロシランを1g加え、その結果得られた
混合物を更に30分間かき混ぜた。生成物を加圧ろ
過して、塩基触媒を中和する間に生じた塩化カリ
ウム(KCl)を取除いた。最後に、生成物を20mm
Hgで250℃の容器(pot)温度(蒸気温度208℃)
までストリツピングした。残留物は、重量が579
g、比重が0.927、25℃における粘度が11.55cSで
あり、計算されたその平均構造式は、次のとおり
であつた。 例 3 例2で調製された液と4cSのシンフルイド(テ
キサス州ヒユーストンのガルフ・オイル・ケミカ
ルズ社)とを等部数混ぜ合わせて均質組成物を調
製した。後者の流体は、下記の式、すなわち、 を有するデセンの三量体であると説明されてい
る。この組成物について、種々の温度での粘度、
そしてまた開放式引火点及び燃焼点を測定した。
その結果を下記の第1表で報告する。 例 4 例1で説明した上記の方法に従つて、次の平均
構造式、すなわち、 を有するシロキサンコポリマーを調製した。この
流体を例3におけるように等量の4cSのシンフル
イドと混合し、そしてこの組成物の粘度並びに引
火点及び燃焼点を測定した。これらの結果も第1
表に示される。 例 5 比較例 538gのオクテン−1と、塩化白金酸の0.1モル
イソプロピルアルコール溶液0.05mlとの溶液を、
窒素雰囲気下で120℃に加熱した。この混合物に、
下記の平均組成、すなわち、 Me3SiO(MeHSiO)1.3SiMe3 (この式においてMeはメチル基を表わす)を
有するシロキサンポリマー480gを、40分かけて
加えた。反応は、約130℃に至る熱量を発生し、
この温度は反応を完了するため80分間維持され
た。生成物を10mmHgで240℃の容器温度(蒸気温
度191℃)までストリツピングし、次いで加圧ろ
過した。このホモポリマーは、25℃における粘度
が14.1cSであり、計算されたその構造式は、次の
とおりであつた。 この流体に、等量の、例3に記載した上記のデ
セン三量体(4cSのシンフルイド)を混ぜ合わせ
た。この組成物についての粘度及び引火点の試験
結果も、第1表に報告される。 第1表から分るように、本発明の組成物のみ
が、空軍の低温MIL−H−83282の目標の粘度及
び引火点の必要条件を同時に満たす。
[Industrial Application Field] The present invention relates to a hydraulic fluid composition that can be used over a wide temperature range and exhibits a relatively high flash point. More specifically, the fluid of this invention consists essentially of a dimethylsiloxane/alkylmethylsiloxane copolymer loaded with a synthetic hydrogenated poly-alpha-olefin. The invention further relates to the use of the above composition in hydraulic systems. [Prior Art and Problems to be Solved by the Invention] Certain silicone fluids are known to have excellent resistance to shear, thermal degradation, and oxidative degradation. Furthermore, unlike typical hydrocarbon lubricating oils or hydraulic fluids, they maintain a relatively flat viscosity-temperature profile. On the other hand, these silicones generally do not have a high degree of lubricity in steel-to-steel contacts, as exemplified by hydrocarbons such as mineral oil, a property that is extremely important in many hydraulic applications. This problem is caused by silicone "base fluid"
This problem can be solved to some extent by incorporating certain lubricity additives into the mixture. In an effort to take advantage of the fundamental advantages of both of these liquid types at the same time, some researchers have combined them in various lubricant compositions. For example, in British Patent No. 1224885, Mackenzie
A composition is disclosed comprising a mineral oil and a homopolymeric diorganopolysiloxane as a viscosity index improver therefor, the organic groups being predominantly methyl groups. In the siloxane polymers of these compositions, the remaining organic groups are alkyl, alkaryl, or aralkyl groups having 6 to 30 carbon atoms in sufficient amount to render them soluble in mineral oil. You can choose from more. In U.S. Pat. No. 4,059,534, Morro et al.
~1000000cS of polydimethylsiloxane
A lubricating oil composition comprising ~50% by weight, the remainder of the composition comprising alkenes, isoparaffins,
and naphthenes. −65
It teaches a hydrocarbon oil with a viscosity of less than 40,000 cS at (-54°C). The major contribution to the art claimed by this disclosure is a lubricating composition that has improved viscosity-temperature characteristics by dissolving high viscosity polydimethylsiloxane in a hydrocarbon oil, and that the composition has better siloxane properties at low temperatures. The purpose is to provide a product whose components do not separate. European Patent Application No. published on April 16, 1986
No. 0177825A1 discloses that the organic group has 1 to 7 carbon atoms.
an organomethylsiloxane unit selected from an alkyl group or a phenyl group;
The preparation of a lubricating oil comprising a silicone copolymer containing alkylmethylsiloxane units which can have 16 carbon atoms is described. These copolymers must have pour points below -15°C and must be miscible with mineral oils, synthetic lubricating oils, and lubricity additives commonly used in such oils. There are further limitations. More recently, the need for fire-resistant military aircraft hydraulic fluids with a wide operating temperature range has been recognized by Gschwender et al., Lubrication Engineering, Vol. 42, No. 485-490.
(1986). On the one hand, mineral oil-based hydraulic fluids (MIL-H-5606) are used extensively in military aircraft and are
Although it is considered possible to operate down to a low temperature, this fluid has two major drawbacks. The relatively low flash point of approximately 100-110°C makes this fluid dangerously easy to ignite and propagate at a high rate once combustion begins.
Furthermore, the shear stability of this fluid is less than desired, especially given the design trend toward higher operating pressures (and associated large shear rates) in modern Air Force aircraft. On the other hand, experience with synthetic hydrogenated polyalpha-olefin fluids indicates that these fluids have high flash points (>205°C).
It was also good in that it was relatively stable against shearing. Unfortunately, such polyα
- Hydraulic fluids based on olefins either have too high a viscosity at low temperatures or have too low a flash point (i.e. when using low molecular weight poly-alpha-olefins) for use in very cold operations. Therefore, Guschewender et al. lists target properties for so-called "low-temperature MIL-H-83282" fluids that combine aspects of both MIL specifications and include viscosity limits as shown below. Present what you want. Temperature (°C) Viscosity (eS) -54 2500 (max) -40 500 (max) 100 3.5 (min) 135 1.5 (min) The high flash point of the MIL-H-83282 liquid mentioned above is It is further recognized that they are incompatible, and that at least 163°C and 191°C
Analysis targets in °C were set for flash point and combustion point respectively. Moreover, a key requirement for a successful candidate fluid is that the fluid be compatible with existing military fluids (i.e. MIL
-H-5606 and MIL-H-83282). None of the technical disclosures of the above-mentioned patent specifications -
A dimethylsiloxane/alkylmethylsiloxane copolymer that forms a base fluid composition that combines the required viscosity-temperature profile and flash point of a suitable candidate for use in fire-resistant hydraulic fluids from 54°C to 135°C. and poly-alpha-olefins. The low-temperature viscosities described above are derived from hydrogenated polyalpha-
It has been discovered that this can be achieved by mixing olefins. Unexpectedly, this, as well as other desirable characteristics of both dimethylsiloxane/alkylmethylsiloxane copolymer fluids and polyalpha-olefin fluids for use in hydraulic applications,
can be achieved while still maintaining the flash point of
Additionally, the compositions thus formed are compatible with existing military fluids (i.e. MIL-H-5606 and MIL-H-
83282), making it possible to perform "drain-fill" replacement in current hydraulic systems. [Means and effects for solving the problem] Therefore, the present invention provides (A) dimethylsiloxane/
an alkylmethylsiloxane copolymer,
The average formula below, i.e. (In this formula, Me represents a methyl group,
R' is independently selected from alkyl groups having from 1 to 10 carbon atoms, R represents an alkyl group having from 4 to 10 carbon atoms, x has an average value from 5 to 15, and the value of y is 0.5 to 4 and the ratio of y/x is 0.3 or less) 40 to 90
Parts by weight, and (B) the following formula, i.e. Synthetic hydrogenated polyα-olefin 10~
A homogeneous hydraulic fluid composition consisting essentially of 60 parts by weight, having a total of 100 parts by weight of components (A) and (B) as described above. This invention further provides that component (B) has the following formula: Regarding a similar composition represented by The invention further provides that component (B) is selected from a dimer, trimer, or tetramer of decene-1, and the viscosity of the homogeneous hydraulic fluid is 2500 cS or less at -54°C and at 100°C. and an open flash point of at least 163°C. The present invention also relates to improvements in methods of transmitting force in hydraulic systems, including the use of the compositions described above as the hydraulic fluid in such systems. The present invention comprises (A) dimethylsiloxane/alkylmethylsiloxane copolymer and (B) synthetic hydrogenated polyα
- Relating to a hydraulic fluid composition consisting essentially of a homogeneous mixture with an olefin. Component (A) of the present invention has the following average formula: In this formula, Me represents a methyl group and R is a straight or specialized alkyl group having 4 to 10 carbon atoms, such as n-pentyl group, isopentyl group, n-hexyl group, n-
heptyl group, n-octyl group, diisobutyl group,
Copolymers such as n-nonyl or n-decyl groups. Straight chain alkyl groups are more preferred than branched structures. R is n-hexyl group or n
-octyl group is more preferred. The R′ group for the terminal silicon atom is 1 to
identical or separate short-chain alkyl groups having 10 carbon atoms, such as methyl, ethyl, propyl,
Such as butyl, hexyl, octyl, or decyl, with methyl being preferred. The value of x in the above formula may range from 5 to 15, preferably from 6 to 12. The value of y may correspondingly range from 0.5 to 4, preferably from 0.5 to 3. However, the value of y is limited so that the ratio of y/x is 0.3 or less. In the above general formula, x and y are preferably chosen such that the viscosity of the copolymer liquid is in the range of about 5 to 50 centistokes (cS) at 25°C. Preferably, this viscosity is about
It is 10-20cS. A highly preferred embodiment of the invention is that R is n-hexyl, R' is methyl,
This is obtained when x is about 6 and y is about 1, or when R is n-octyl and R' is methyl, x is about 8 and y is 0.5. The above copolymers of the invention may be prepared by methods well known in the art. For example, they can be synthesized by cohydrolysis and subsequent condensation of appropriate diorganodialkoxysilanes or diorganodichlorosilanes. In this approach, a desired amount of end-capping reactant (R′) 3 SiZ is included in the reaction mixture to control the molecular weight of the product (i.e., more end-capping reactant produces a lower molecular weight product). occur).
The R′ group of this end-capping reactant is the component (A)
This is the same as shown above. The Z group is
Halogens (e.g. chlorine, fluorine, or bromine)
or a hydrolyzable species such as an alkoxy group (eg, methoxy group, ethoxy group). Another method that can be applied to synthesize the copolymers is the acid- or base-catalyzed equilibrium reaction of diorganocyclosiloxanes in the presence of the aforementioned end-capping reactants. Yet another preferred method is based on the following general formula: (wherein Me represents a methyl group and R' is as defined above). These intermediates are well known to those skilled in the art and may be prepared by acid equilibration of commercially available polymethylhydrogensiloxanes and cyclic dimethylsiloxanes in various proportions. The molecular weight of this intermediate may be adjusted by adding an appropriate amount of an end capping monomer such as hexamethyldisiloxane. The SiH functional intermediate is then reacted with approximately 25% excess of the desired alkene to chemically add the latter to the former SiH group. This addition reaction is catalyzed by platinum complexes known in the art. Component (B) of the present invention is at least one synthetic hydrogenated poly-α-olefin selected from dimer, trimer, or tetramer of decene-1, and can be represented by the following formula: . (dimer) (trimer) (Tetramer) In a preferred embodiment of the present invention, component (B) is a poly-α-olefin trimer. However, component (A) contains the above dimers, trimers, and tetramers to provide the high flash point and viscosity-temperature profile necessary to meet the target requirements of low temperature MIL-H-83282. This can be achieved by mixing the mixture, and this can be determined by routine experimentation. Poly alpha-olefin fluids are well known in the art and can be prepared from monomeric decene-1 by catalytic polymerization and hydrogenation. If you are interested, see, for example, the October 1981 US government report AFWAL-TR- by Cupples et al.
81-4109 (Wright-Patterson)
Reference is made to the method outlined by the Air Force Wright Aeronautical Research Laboratory, Materials Laboratory, Patterson Air Force Base. These fluids are manufactured by Gulf Oil Chemicals in Hyeuston, Texas.
Chemicals Co., Ltd. under the trade name SYNFLUID. The compositions of the invention may be prepared by simply mixing components (A) and (B) to form a homogeneous mixture thereof. The mixing method is not particularly important;
Any of the commonly used methods known in the art may be used. The mixture so made is typically a "base fluid" in that the lubricity additives and other adjuvants described below are combined with it to create a fully formulated hydraulic fluid.
It is called. When component (B) is a decene trimer, 40 to 90 parts by weight of component (A) are mixed with 60 to 10 parts of component (B) to make 100 parts of the composition of the invention. However, it is preferred to mix 40 to 60 parts by weight of component (A) with 60 to 40 parts of decene trimer. Most preferably, equal weights of decene trimer and component (A) dimethylsiloxane/alkylmethylsiloxane copolymer liquid are used;
The dimethylsiloxane/alkylmethylsiloxane copolymer component in this case is delineated by the preferred ranges set forth above. When component (B) is a decene tetramer, 80 to 90 parts by weight of component (A) are mixed with 20 to 10 parts of component (B) to make 100 parts of the composition of the invention. Apart from this, the composition of the present invention can be used in low temperature MIL
- May be defined by the basic physical properties required by the goals of H-83282. In this case, 100 parts by weight of the composition comprises 10 to 90 parts by weight of component (A) and at least one synthetic hydrogenated polyamide selected from dimers, trimers, or tetramers of decene-14. α−
90 to 10 parts by weight of olefin, the viscosity at -54°C is 2500 cS or less, the viscosity at 100°C is at least 3.5 cS, and the open flash point is at least 163°C. Preferably,
40-60 parts by weight of component (A) are mixed with 60-40 parts of component (B). These properties will be readily available to those skilled in the art through routine experimentation in light of the above disclosure. As previously stated, various additives are generally incorporated into the base fluid of this invention to prepare a fully formulated hydraulic fluid. Antiwear or lubricity additives, such as tricresyl phosphate, dibutyl chlorendate, and antimony dialkyl dithiocarbamates, are preferably incorporated at about 1 to 10 weight percent. Rubber swell additives such as di(2-ethylhexyl) sebacate or tributyl phosphate may contain from about 1 to
It will be incorporated at 5% by weight. These are typically used with polydimethylsiloxanes as these base fluids tend to shrink the rubber components by leaching plasticizers from the rubber components. Generally, the alkyl content or alkyl group size of component (A) is increased, or component (B) is increased.
As more and more are utilized, the need for swelling additives becomes less. p,p'- at a concentration of about 0.1 to 0.5 weight percent
Antioxidants such as dioctyl diphenylamine and butylated hydroxytoluene are generally required to protect alkyl groups from oxidation at high service temperatures. Dyes can also be added at low concentrations, primarily for identification purposes. Other non-essential additives, e.g. flame retardants,
Defoamers, corrosion inhibitors, and the like may also find utility in combination with the base fluids of the present invention. Increasing the alkylmethylsiloxane content of component (A) to approach 100% allows the resulting base solution to be formulated to meet the target viscosity requirements of low temperature MIL-H-83282. The result was a polymer that was unsatisfactory in that it could not be used. Moreover, as the alkyl content increased, the swelling of any Gol component in the hydraulic system also increased, leading to undesirable results in some systems. It will be appreciated by those skilled in the art that some of the target requirements of low temperature MIL-H-83282 can be met by varying the molecular weight of the base fluid composition and/or by incorporating various additives. Although it is possible to do so, it will be recognized that the important properties presented above are not usually modulated by such operations. Thus, for example, if the base fluid (i.e., the composition of the siloxane copolymer and polyalpha-olefin of the present invention) does not simultaneously exhibit the required viscosity-temperature profile and a sufficiently high flash point; Combining base fluids into a fully formulated hydraulic fluid for testing generally does not meet the target properties of low temperature MIL-H-83282. Therefore, base fluid compositions that do not pass these critical property requirements are
It was determined that the target did not meet MIL-H-83282. The invention also relates to an improved method for transmitting actuating force (pressure) in a hydraulic system, where the actuating fluid is essentially of a composition of a siloxane copolymer and a polyalpha-olefin as described. Consists of one. In this improved method, the fluid-containing portion of the hydraulic system component is filled with the composition of the invention as previously disclosed. Examples of hydraulic system components contemplated herein include pumps, fluid coupling devices such as diaphragms, hydraulic line means, valves, and hydraulic actuation means such as hydraulic motors, pistons, and servo valves. Hydraulic systems that would benefit most from the use of the working base fluid of this invention are those that are required to operate between temperature extremes of -54°C and 135°C, and that simultaneously use mineral oil as the hydraulic fluid. This is a hydraulic system that requires improved fire resistance. The method of the invention is therefore most suitably used in connection with military aircraft hydraulic systems. Other hydraulic systems in which the method of the invention may be advantageously used include civil aircraft, land and sea military transport and combat vehicles, spacecraft, and systems for use in boreal regions or other cold environments. Includes machinery. EXAMPLES The following examples are provided to further illustrate the compositions of this invention and should not be construed as limiting the invention. The invention is set out in the claims. All parts and percentages in the examples below are by weight unless indicated to the contrary. Example 1 Into a flask equipped with a stirrer, thermometer, condenser, addition funnel, and means for purging with dry nitrogen gas, 316 g of hexene-1 is charged with a dimethylvinylsiloxy group terminated to give 0.7 weight percent platinum. 0.1 ml of a chloroplatinic acid complex of divinyltetramethyldisiloxane (prepared according to Example 1 of Willing, US Pat. No. 3,419,593) diluted with blocked polydimethylsiloxane was added. To this mixture, 800 g of a siloxane copolymer of the following average composition: Me 3 SiO (MeHSiO) 4.4 (Me 2 SiO) 9.8 SiMe 3 (in which Me represents a methyl group) were added over a period of 2 hours. The reaction was exothermic and the contents were cooled to maintain the temperature between 25°C and 50°C. The calculated average structural formula of the resulting copolymer was as shown below. Example 2 400 g of copolymer prepared in Example 1 above, 500 g of siloxane with average formula Me 3 SiO (Me 2 SiO) 4.7 SiMe 3 and dimethylcyclosiloxane with 3, 4 and 5 dimethylsiloxane units. 100g of a mixture of and 1g of potassium hydroxide (KOH)
Stir the mixture with under nitrogen atmosphere and approx.
Heated to 160°C. Approximately 20 ml of volatile products were removed by distillation. The remaining mixture was further reacted at 160°C for 4 hours and then cooled to room temperature. 1 g of trimethylchlorosilane was added and the resulting mixture was stirred for an additional 30 minutes. The product was pressure filtered to remove potassium chloride (KCl) generated during neutralization of the base catalyst. Finally, add the product to 20mm
Pot temperature of 250℃ with Hg (steam temperature 208℃)
Stripped up to. The residue weighs 579
g, specific gravity was 0.927, viscosity at 25°C was 11.55 cS, and the calculated average structural formula was as follows. Example 3 A homogeneous composition was prepared by mixing equal parts of the solution prepared in Example 2 and 4cS Synfluid (Gulf Oil Chemicals, Inc., Hyuston, Texas). The latter fluid has the following formula, namely: It is described as a trimer of decene with . For this composition, the viscosity at various temperatures,
The open flash point and combustion point were also measured.
The results are reported in Table 1 below. Example 4 Following the above method described in Example 1, the following average structural formula, i.e. A siloxane copolymer was prepared with This fluid was mixed with an equal volume of 4 cS of synfluid as in Example 3, and the viscosity and flash and fire points of the composition were measured. These results are also the first
Shown in the table. Example 5 Comparative Example A solution of 538 g of octene-1 and 0.05 ml of a 0.1 molar isopropyl alcohol solution of chloroplatinic acid was
Heated to 120°C under nitrogen atmosphere. In this mixture,
480 g of a siloxane polymer having the following average composition: Me 3 SiO (MeHSiO) 1.3 SiMe 3 (in which Me represents a methyl group) were added over 40 minutes. The reaction generates heat up to approximately 130°C,
This temperature was maintained for 80 minutes to complete the reaction. The product was stripped at 10 mm Hg to a vessel temperature of 240°C (steam temperature 191°C) and then pressure filtered. This homopolymer had a viscosity of 14.1 cS at 25°C, and its calculated structural formula was as follows. To this fluid was mixed an equal volume of the decene trimer described above in Example 3 (4 cS synfluid). Viscosity and flash point test results for this composition are also reported in Table 1. As can be seen from Table 1, only the compositions of the present invention simultaneously meet the target viscosity and flash point requirements of Air Force Low Temperature MIL-H-83282.

【表】 * テキサス州ヒユーストンのガルフ・オイル・ケミ
カルズ社の製品
[Table] *Products from Gulf Oil Chemicals of Hyeuston, Texas

Claims (1)

【特許請求の範囲】 1 (A) 下記の平均式、すなわち、 (この式において、Meはメチル基を表わし、
R′は炭素原子数1〜10のアルキル基より独立に
選択され、Rは炭素原子数4〜10のアルキル基を
表わし、xは5から15まで、yは0.5から4まで
であり、そしてy/xの比率は0.3以下である)
により表わされるシロキサンコポリマー40〜90重
量部、及び、 (B) 下記の式、すなわち、 により表わされる合成水素化ポリα−オレフイン
60〜10重量部、 から本質的になり、上記の成分(A)及び(B)を合計で
100重量部有する組成物。 2 40〜60重量部の成分(A)に60〜40重量部の成分
(B)が混合されている、請求項1記載の組成物。 3 (A) 下記の平均式、すなわち、 (この式において、Meはメチル基を表わし、
R′は炭素原子数1〜10のアルキル基より独立に
選択され、Rは炭素原子数4〜10のアルキル基を
表わし、xは5から15まで、yは0.5から4まで
であり、そしてy/xの比率は0.3以下である)
により表わされるジメチルシロキサン/アルキル
メチルシロキサンコポリマー80〜90重量部、及
び、 (B) 下記の式、すなわち、 により表わされる合成水素化ポリα−オレフイン
20〜10重量部、 から本質的になり、上記の成分(A)及び(B)を合計で
100重量部有する組成物。 4 (A) 下記の平均式、すなわち、 (この式において、Meはメチル基を表わし、
R′は炭素原子数1〜10のアルキル基より独立に
選択され、Rは炭素原子数4〜10のアルキル基を
表わし、xは5から15まで、yは0.5から4まで
であり、そしてy/xの比率は0.3以下である)
により表わされるシロキサンコポリマー10〜90重
量部、及び、 (B) デセン−1の二量体、三量体、又は四量体よ
り選択された少なくとも一つの合成水素化ポリα
−オレフイン90〜10重量部、 から本質的になり、上記の成分(A)及び(B)を合計で
100重量部有し、且つ、−54℃における粘度が
2500cS以下、100℃における粘度が少なくとも
3.5cSであり、開放式引火点が少なくとも163℃で
ある組成物。 5 作動液として請求項1記載の組成物を使用す
ることを含む、油圧系統における力伝達方法。 6 作動液として請求項3記載の組成物を使用す
ることを含む、油圧系統における力伝達方法。 7 作動液として請求項4記載の組成物を使用す
ることを含む、油圧系統における力伝達方法。
[Claims] 1 (A) The following average formula, that is, (In this formula, Me represents a methyl group,
R' is independently selected from alkyl groups having from 1 to 10 carbon atoms, R represents an alkyl group having from 4 to 10 carbon atoms, x is from 5 to 15, y is from 0.5 to 4, and y /x ratio is less than 0.3)
40 to 90 parts by weight of a siloxane copolymer represented by, and (B) the following formula, i.e. Synthetic hydrogenated polyα-olefin represented by
60 to 10 parts by weight, consisting essentially of the above ingredients (A) and (B) in total
A composition having 100 parts by weight. 2 60 to 40 parts by weight of component (A) in 40 to 60 parts by weight
The composition according to claim 1, wherein (B) is mixed. 3 (A) The following average formula, i.e. (In this formula, Me represents a methyl group,
R' is independently selected from alkyl groups having from 1 to 10 carbon atoms, R represents an alkyl group having from 4 to 10 carbon atoms, x is from 5 to 15, y is from 0.5 to 4, and y /x ratio is less than 0.3)
80 to 90 parts by weight of dimethylsiloxane/alkylmethylsiloxane copolymer represented by, and (B) the following formula, i.e. Synthetic hydrogenated polyα-olefin represented by
20 to 10 parts by weight, consisting essentially of the above components (A) and (B) in total
A composition having 100 parts by weight. 4 (A) The following average formula, i.e. (In this formula, Me represents a methyl group,
R' is independently selected from alkyl groups having from 1 to 10 carbon atoms, R represents an alkyl group having from 4 to 10 carbon atoms, x is from 5 to 15, y is from 0.5 to 4, and y /x ratio is less than 0.3)
10 to 90 parts by weight of a siloxane copolymer represented by (B) at least one synthetic hydrogenated polyα selected from a dimer, trimer, or tetramer of decene-1;
- 90 to 10 parts by weight of olefin, consisting essentially of the above components (A) and (B) in total;
Contains 100 parts by weight, and has a viscosity at -54℃
2500cS or less, viscosity at 100℃ is at least
3.5cS and an open flash point of at least 163°C. 5. A method for transmitting force in a hydraulic system, comprising using the composition according to claim 1 as a hydraulic fluid. 6. A method for transmitting force in a hydraulic system, comprising using the composition according to claim 3 as a hydraulic fluid. 7. A method for transmitting force in a hydraulic system, comprising using the composition according to claim 4 as a hydraulic fluid.
JP63065934A 1987-03-23 1988-03-22 Siloxane/poly-alpha-olefin hydraulic liquid and its use Granted JPS63254161A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US2895087A 1987-03-23 1987-03-23
US28950 1987-03-23

Publications (2)

Publication Number Publication Date
JPS63254161A JPS63254161A (en) 1988-10-20
JPH0563509B2 true JPH0563509B2 (en) 1993-09-10

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Application Number Title Priority Date Filing Date
JP63065934A Granted JPS63254161A (en) 1987-03-23 1988-03-22 Siloxane/poly-alpha-olefin hydraulic liquid and its use

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EP (1) EP0283922B1 (en)
JP (1) JPS63254161A (en)
AU (1) AU597804B2 (en)
BR (1) BR8801276A (en)
CA (1) CA1334966C (en)
DE (1) DE3861601D1 (en)

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DE4204200A1 (en) * 1992-02-13 1993-08-19 Daimler Benz Ag Liq. useful as heat transfer and insulating media - comprises mixt. of poly-alpha-olefin(s) and/or isoparaffin(s) with poly:di:methyl:siloxane(s) and/or poly:alkyl -/poly:aryl:siloxane(s)
JP3341318B2 (en) * 1992-10-21 2002-11-05 エヌオーケー株式会社 Low temperature hydraulic oil
JP3344852B2 (en) * 1994-10-28 2002-11-18 東レ・ダウコーニング・シリコーン株式会社 Liquid composition
GB201214473D0 (en) * 2012-08-14 2012-09-26 Dow Corning Lubricant compostion
FR3021665B1 (en) * 2014-05-30 2018-02-16 Total Marketing Services PROCESS FOR THE PREPARATION OF LOW VISCOSITY LUBRICATING POLYOLEFINS
FR3021664B1 (en) * 2014-05-30 2020-12-04 Total Marketing Services LOW VISCOSITY LUBRICATING POLYOLEFINS
FR3037969B1 (en) 2015-06-29 2017-08-11 Total Marketing Services LOW VISCOSITY LUBRICATING POLYOLEFINS
FR3037968A1 (en) * 2015-06-29 2016-12-30 Total Marketing Services POLYOLEFINS AS SPECIAL FLUID
FR3037949B1 (en) * 2015-06-29 2017-08-11 Total Marketing Services LOW VISCOSITY LUBRICATING POLYOLEFINS
CN105754692A (en) * 2016-04-14 2016-07-13 上海禾泰特种润滑科技股份有限公司 Air compressor oil composition and preparation method thereof
WO2018236591A1 (en) * 2017-06-22 2018-12-27 Exxonmobil Research And Engineering Company Low viscosity lubricants based on methyl paraffin containing hydrocarbon fluids

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Also Published As

Publication number Publication date
CA1334966C (en) 1995-03-28
EP0283922B1 (en) 1991-01-23
AU1337588A (en) 1988-09-22
EP0283922A3 (en) 1988-10-26
AU597804B2 (en) 1990-06-07
JPS63254161A (en) 1988-10-20
EP0283922A2 (en) 1988-09-28
DE3861601D1 (en) 1991-02-28
BR8801276A (en) 1988-10-25

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