JPS6013892A - Hydraulic fluid - Google Patents

Hydraulic fluid

Info

Publication number
JPS6013892A
JPS6013892A JP59123901A JP12390184A JPS6013892A JP S6013892 A JPS6013892 A JP S6013892A JP 59123901 A JP59123901 A JP 59123901A JP 12390184 A JP12390184 A JP 12390184A JP S6013892 A JPS6013892 A JP S6013892A
Authority
JP
Japan
Prior art keywords
weight
glycol
fluid
component
hydraulic fluid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP59123901A
Other languages
Japanese (ja)
Other versions
JPH0458520B2 (en
Inventor
フランコ・ガラテイ
マリオ・ムスコ
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.)
Montedison SpA
Original Assignee
Montedison SpA
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=11185563&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=JPS6013892(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Montedison SpA filed Critical Montedison SpA
Publication of JPS6013892A publication Critical patent/JPS6013892A/en
Publication of JPH0458520B2 publication Critical patent/JPH0458520B2/ja
Granted legal-status Critical Current

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    • C10M111/00Lubrication 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
    • C10M111/04Lubrication 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
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2227/00Organic non-macromolecular compounds containing atoms of elements not provided for in groups C10M2203/00, C10M2207/00, C10M2211/00, C10M2215/00, C10M2219/00 or C10M2223/00 as ingredients in lubricant compositions
    • C10M2227/06Organic compounds derived from inorganic acids or metal salts
    • C10M2227/061Esters derived from boron
    • C10M2227/062Cyclic esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2227/00Organic non-macromolecular compounds containing atoms of elements not provided for in groups C10M2203/00, C10M2207/00, C10M2211/00, C10M2215/00, C10M2219/00 or C10M2223/00 as ingredients in lubricant compositions
    • C10M2227/06Organic compounds derived from inorganic acids or metal salts
    • C10M2227/061Esters derived from boron
    • C10M2227/062Cyclic esters
    • C10M2227/0625Cyclic esters used as base material
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2020/00Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
    • C10N2020/01Physico-chemical properties
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/08Hydraulic fluids, e.g. brake-fluids

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、動力を伝達するための液圧流体特に、各種分
子量のグリコール、グリコールエーテルおよび随意成分
としてのほう酸グリコールエステルの混合物よりなる臭
素含量0〜1重景装置液圧ブレーキ流体として適合せる
液状組成物に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a hydraulic fluid for transmitting power, particularly a bromine content 0-1 bromine fluid comprising a mixture of glycols of various molecular weights, glycol ethers and boric acid glycol esters as an optional component. The present invention relates to a liquid composition suitable as a pressure brake fluid.

自動車用ブレーキ系統は重要な安全要素を代表する。ブ
レーキの効率的な作動は、ブレーキ系統に用いられる液
圧流体の特性値によって大巾に決定される。そのため、
現行法規により、液圧流体には、沸点、粘度(高温時お
よび低温時)、pH値、安定性(高温時および低温時)
、金属に対する腐蝕作用、ゴムに対する膨潤作用の如き
規定特性値に関する非常に厳格な必要条件が課されるこ
とになる。
Automotive brake systems represent an important safety element. Efficient operation of brakes is determined to a large extent by the characteristics of the hydraulic fluid used in the brake system. Therefore,
According to current regulations, hydraulic fluids have boiling point, viscosity (at high and low temperatures), pH value, and stability (at high and low temperatures).
Very strict requirements regarding specified properties such as corrosion effects on metals, swelling effects on rubber, etc. will be imposed.

ここに挙げた特性値のうち特に、ブレーキ流体の適性又
は不適性を確かめるのに決定的なのは、加湿後の全還流
時沸点(WET PERT )と低温時の粘度である。
Among the characteristic values listed here, those that are decisive for confirming the suitability or unsuitability of a brake fluid are the total reflux boiling point after humidification (WET PERT) and the viscosity at low temperatures.

かかる特性値は、考慮される流体の吸湿性と密接に結び
ついている。
Such characteristic values are closely linked to the hygroscopicity of the considered fluid.

事実、この水に対する親和性は、多湿気体周囲(雰囲気
)からの水吸収において明示されるのみならず、大気圧
での全還流沸とう温度(Pg)L’l’ )および低温
流動性に影響する分子内結合強度の測ににおいても明示
される。
In fact, this affinity for water is not only manifested in the absorption of water from the humid surroundings (atmosphere), but also influences the total reflux boiling temperature at atmospheric pressure (Pg) and low-temperature fluidity. This is also clearly demonstrated in the measurement of intramolecular bond strength.

ブレーキ流体による漸次的湿り吸収がどのように生じよ
うとも、それは沸点を漸減させるものとなる。この沸点
低下は、流体を、ブレーキへの使用で信頼性の低いもの
とする。なぜなら、近頃の自動車は相当量の摩擦熱を生
じてブレーキ液の沸とうを生起し得面してその結果気相
が形成して動力伝達の達成に必要な液の非圧縮性を無効
にするからである。
Whatever gradual moisture uptake by the brake fluid occurs, it results in a gradual decrease in boiling point. This boiling point reduction makes the fluid unreliable for use in brakes. This is because modern automobiles generate significant amounts of frictional heat that can cause boiling of the brake fluid, resulting in the formation of a gas phase that negates the incompressibility of the fluid necessary to achieve power transmission. It is from.

かかる現象は間違いなく生ずるので、どんな流体も、走
行距離が長くなるとき使用不適性の状態に達する。その
効果的な救済手段は、ブレーキ系統の液を定期的に変え
ることである。
Such a phenomenon is bound to occur, so that any fluid reaches a state of unsuitability as the mileage increases. An effective remedy is to periodically change the brake system fluid.

而して、ブレーキ流体の定期的交換の原則は依然妥当で
はあるが、交換作業が常にきわめて簡単というわけでな
く、また少べとも幾分コスト高であるため、水吸収の有
害な影響を減じ且つ該結果十分な適性状態下で作動期間
を延長することのできるブレーキ流体の開発が待たれて
いた。
Thus, although the principle of periodic replacement of brake fluid remains valid, the replacement process is not always extremely easy and is at least somewhat costly, making it difficult to reduce the harmful effects of water absorption. As a result, the development of a brake fluid that can extend the operating period under sufficiently suitable conditions has been awaited.

標準使用される液圧ブレーキ流体はFMVSS 116
、DOT−xおよびDOT−4(すなわち連邦自動車安
全規格−運輸省)並びにSAE J1703(自動車技
術渚協会、N、Y、)の規格を全て満たさねばならない
The standard hydraulic brake fluid used is FMVSS 116
, DOT-x and DOT-4 (i.e., Federal Motor Vehicle Safety Standards - Department of Transportation) and SAE J1703 (Automotive Technology Association, N.Y.) must all be met.

D 01” −3およびDOT−4の分類に属するブレ
ーキ液は下記特性値を有する: DOT−3DOT−4 沸点 (乾燥状態) PEI(T 最低205℃ 最低230
6C沸点 (湿り状態) VVET PEI(T 最低140°C
最低 55℃粘度(−40°C) 最高 150[1c
St最高1800cSt過去数十年間の特許および技術
文献から、液圧ブレーキ流体全体はほとんど、アルコー
ル、グリコール、クリコールエーテル、ポリクリコール
、ポリグリコールエーテルおよびこれら誘導体の混合物
よりなることが知られている。
Brake fluids belonging to the classification D 01"-3 and DOT-4 have the following characteristic values: DOT-3 DOT-4 Boiling point (dry state) PEI (T min. 205 °C min. 230
6C boiling point (wet state) VVET PEI (T minimum 140°C
Minimum 55℃ viscosity (-40℃) Maximum 150 [1c
St up to 1800 cSt It is known from the patent and technical literature of the past few decades that hydraulic brake fluids as a whole consist mostly of alcohols, glycols, glycol ethers, polyglycols, polyglycol ethers and mixtures of these derivatives.

例えば、フランス国特許第2.158.523号は、L
)OT−4の分類に属するもので、テトラエチレングリ
コール、エーテルグリコールおよび低級グリコールエー
テルの混合物よりなるブレーキ液組成物を開示している
。この組成物は、テトラエチレングリコールの存在ゆえ
に高い低温粘度値(−40℃で1590 cSt、例1
)を有し、また155℃よりわずかに高いWET PE
RT (最高156、5℃、例2)を有する。
For example, French Patent No. 2.158.523
) discloses a brake fluid composition belonging to the OT-4 classification consisting of a mixture of tetraethylene glycol, ether glycol and lower glycol ether. This composition has a high low temperature viscosity value (1590 cSt at -40°C, Example 1) due to the presence of tetraethylene glycol.
) and slightly above 155°C.
RT (up to 156, 5°C, Example 2).

低温時の高すぎる粘度が液圧ブレーキにとってマイナス
特性を表わし、それがブレーキ流体の実際上の使用を危
うくすることは自明である。
It is obvious that too high a viscosity at low temperatures represents a negative characteristic for hydraulic brakes, which jeopardizes the practical use of the brake fluid.

WE’l’ PERTが155℃より常に高く、しかも
−40℃での粘度が1500C8tより高くないブレー
キ流体を取得しようとして、多くの研究が行なわれた。
Much research has been carried out in an attempt to obtain a brake fluid whose WE'l' PERT is always higher than 155°C, and whose viscosity at -40°C is not higher than 1500C8t.

前記のDOT−3若しくはD OT−4と呼はれるブレ
ーキ液は、グリコール・のほう酸エステル、特ニアルコ
ール、グリコール、グリコールエーテル、ポリグリコー
ルおよびソリグリコールエーテルを基剤とする慣用処方
物の成分のうち1種ないしそれ以上の、はう酸による部
分エステル化物又は完全エステル化物の中に選抜されて
きた。
The brake fluids referred to as DOT-3 or DOT-4 contain the components of conventional formulations based on glycol-borate esters, especially dialcohols, glycols, glycol ethers, polyglycols and solyglycol ethers. Of these, one or more of these have been selected as partially or completely esterified products with halonic acid.

例えは、はう酸エステルに関する最初の特許である米国
特許第5.625.899号は、エーテル性グリコール
、ポリグリコールのほう酸エステル少くとも1種とモノ
エーテル若しくはジエーテルグリコールとの混合物より
なる液圧ブレーキ組成物を開示している。
For example, US Patent No. 5.625.899, the first patent related to oxide ester, is a liquid that is a mixture that is one type at an ether -based glycol, polyglycoles, one type and a mixture of monoethel glycol. A pressure brake composition is disclosed.

この特許の過程段階で、異なる流れの研究が追跡されて
いる。而して、これらの研究は、特定タイプのほう酸エ
ステルを強調する仕方において互いに異なってはいるが
、しかしそれら全ては、組成物が1)OT−4の分類に
入るために組成物中に臭素が限定値より高い濃度で存在
する必要のある点で共通している。
At this patent process stage, different streams of research are being pursued. Thus, although these studies differ from each other in the way they emphasize specific types of borate esters, they all require that the composition: 1) contain bromine in the composition in order to enter the OT-4 classification; They have in common that they must exist at a concentration higher than the limiting value.

この組成物において、吸収された水の一部分はエステル
の加水分解反応により除かれるが、それに伴ってほう酸
の沈殿という望ましくなへ・傾向が生ずる。
In this composition, a portion of the absorbed water is removed by the hydrolysis reaction of the ester, with an associated undesirable tendency to precipitation of boric acid.

また、この方法に用いられる有機はう酸塩はゴムの膨晶
を終始惹起しくエーテル性グリコールのエステル)或い
は高い粘度をもたらす(グリコールのエステル)が、い
ずれにしても、慣用処方物との比較において避は難い高
コストに帰着するという欠点を有する。この理由で、有
機はう酸塩含有処方物は従前、市場に広く出回ることは
なかった。
Furthermore, the organic balate salts used in this method consistently cause swelling of the rubber (esters of ethereal glycols) or high viscosity (esters of glycols), but in any case, comparison with conventional formulations However, it has the disadvantage that it results in unavoidably high costs. For this reason, organic balate-containing formulations have not hitherto been widely available on the market.

かくして、はう素不在でもDOT−4となり得そしてよ
り一般的には、僅量のほう酸エステル存在下、でも、す
ぐれた耐湿り特性を示すブレーキ流体への需要が感得さ
れた。
Thus, a need was felt for brake fluids that can be DOT-4 in the absence of boronate and, more generally, exhibit excellent moisture resistance properties even in the presence of small amounts of boric esters.

従って、本発明の目的は、はう素化合物を含まなくても
155℃より高いWET PERT沸点および1500
 cstより低い粘度(−40℃)を有する液圧流体す
なわち粘度に関してはDOT−3にまf、=WETPE
RT K12j L、 テハD OT −4ニ属する流
体として用いるのに適合せる組成物を提供することであ
る。
It is therefore an object of the present invention to achieve a WET PERT boiling point higher than 155°C and a
Hydraulic fluids with a viscosity lower than cst (-40°C), i.e. DOT-3 in terms of viscosity, = WETPE
It is an object of the present invention to provide a composition suitable for use as a fluid belonging to RT K12j L, TehaDOT-4.

本発明の別の目的は、同じほう素含量で、従来法の組成
物より高いWET PIMRT値を有するほう酸エステ
ル基剤組成物を提供することである。
Another object of the present invention is to provide a borate ester based composition that has higher WET PIMRT values than prior art compositions with the same boron content.

本発明の他の目的は、DOT−3規格およびL) OT
 −4規格の全てを満たし、特にブレーキ系統に存在す
る金属およびゴムに対する非攻撃規格を満たすブレーキ
流体を提供することである。他の目的および利益につい
ては、以下の記載から当業渚には明らかであろう。
Another object of the invention is that the DOT-3 standard and L) OT
The object of the present invention is to provide a brake fluid that satisfies all of the -4 standards and in particular the non-aggressive standards for metals and rubber present in brake systems. Other objectives and benefits will be apparent to those skilled in the art from the following description.

斜上の目的は、驚くべきことに、はう素含量0〜1重量
%範囲にして、はう素がグリコールはう酸エステル形状
をなす特定の液状組成物により達成されることがわかっ
た。
It has now been found that the object of slanting is surprisingly achieved by a particular liquid composition with a borosine content in the range 0-1% by weight, in which the borosene is in the form of a glycol ester.

更に特定するに、本発明の液圧流体は、(a) アルキ
レングリコール 2〜4oi量%fbJ アルキレング
リコールモノアルキルエーテル少くとも18 15〜6
5重景% (装置式 %式% を有するポリアルキレングリコールモノアルキルエーテ
ル少くとも11 15〜55重量% および (d) 上記(a)のほう酸エステル少くとも1種0〜
54重量% よりなる組成物である。(但し、全ての重量%は本液圧
流体組成物の総重量に関する)。
More particularly, the hydraulic fluid of the present invention comprises: (a) alkylene glycol 2-4 oi amount % fbJ alkylene glycol monoalkyl ether at least 18 15-6
Polyalkylene glycol monoalkyl ether having the following formula: at least 11 15 to 55% by weight; and (d) at least one boric acid ester of (a) above: 0 to
The composition consists of 54% by weight. (However, all weight percentages refer to the total weight of the hydraulic fluid composition).

適当なアルキレングリコール(alはモノメチレンクリ
コール、ジエチレングリコール、トリエチレングリコー
ル、モノプロピレングリコール、ジエチレングリコール
およびトリプロピレンクリコールである。取分け、ジエ
チレングリコールおよびトリエチレングリコールが好ま
しい。
Suitable alkylene glycols (al are monomethylene glycol, diethylene glycol, triethylene glycol, monopropylene glycol, diethylene glycol and tripropylene glycol; in particular diethylene glycol and triethylene glycol are preferred.

J 当fxアルキレングリコールモノアルキルエーテル
(b)はアルキレングリコール(a)のC1〜C4モノ
アルキルエーテルである。このうち、トリエチレングリ
コールモノエチルエーテルが好ましい。
J This fx alkylene glycol monoalkyl ether (b) is a C1-C4 monoalkyl ether of alkylene glycol (a). Among these, triethylene glycol monoethyl ether is preferred.

適当なポリアルキレングリコールモノアルキルエーテル
(C)は、上記式中RがC1〜C4アルキルであり、R
1がH又はCH3であり、nが、本化合物の分子量を2
08〜1oooH囲とする如き整数である化合物である
。好ま“しくは、R’=Hの化合物である。
Suitable polyalkylene glycol monoalkyl ethers (C) are those in the above formula in which R is C1-C4 alkyl;
1 is H or CH3, and n is the molecular weight of the compound 2
It is a compound that is an integer such as 08 to 1oooH. Preferably, it is a compound where R'=H.

適当なほう酸エステル(d)はほう素化合物とアルキレ
ングリコール(alとの反応生成物である。好ましいの
は、はう酸とジエチレングリコールとの反応生成物であ
る。
Suitable boric acid esters (d) are the reaction products of boron compounds and alkylene glycols (al). Preferred are the reaction products of boronic acid and diethylene glycol.

本発明の方法によって取得される液状組成物は155°
C(DOT−4の下限)より高い踵T PER,T、1
500cSt (DOT−3の上限)より低い粘度(−
40℃)および約250℃以上のPERT値を示す。
The liquid composition obtained by the method of the invention is
Heel T higher than C (lower limit of DOT-4) PER,T,1
Viscosity lower than 500cSt (upper limit of DOT-3) (-
40°C) and a PERT value of about 250°C or higher.

更に、本液状組成物は、ブレーキ系統に存在する種々の
金属およびゴムに対する攻撃性がほとんど若しくは全く
ない(これはブレーキ系統の寿命にかなり有利である)
ことを特徴とし、加・えて品質の最も高い慣用製品の代
表的特質全てを有する。
Additionally, the present liquid composition has little or no aggressiveness towards the various metals and rubbers present in brake systems (which is of considerable benefit to the service life of brake systems).
In addition, it has all the typical characteristics of a conventional product of the highest quality.

必要に応じて、本発明の組成物に、ブレーキ流体の性能
を強化する添加剤を加えることができる。
If desired, additives can be added to the composition of the invention to enhance the performance of the brake fluid.

かかる添加剤として、緩衝剤、腐蝕抑制剤、抗酸化剤、
多湿酸化環境での鉄金属に関する保護力を高める物質、
安定剤、染料等さまざまな種類が挙げられる。
Such additives include buffering agents, corrosion inhibitors, antioxidants,
Substances that increase protection for ferrous metals in humid oxidizing environments,
There are various types such as stabilizers and dyes.

一般に、液状組成物に編入されうる添加剤の量は、組成
物の総量に関し0〜10X範囲である。
Generally, the amount of additive that can be incorporated into the liquid composition ranges from 0 to 10X with respect to the total amount of the composition.

は52エステル(a)の製造は大気圧下(好ましくは共
沸溶剤の存在で)又は減圧下(溶剤不在で)50°C〜
200℃範囲の温度で遂行される。
The preparation of the 52 ester (a) is carried out at 50° C. under atmospheric pressure (preferably in the presence of an azeotropic solvent) or under reduced pressure (in the absence of a solvent).
It is carried out at temperatures in the range of 200°C.

本発明に従った液圧流体は、ミキサー内で、成分(al
、(b)、(C1−および(d)並びに添加漬1を一緒
に、十分且つ完全な均質化が達成されるまで混合するこ
とによつズ取得される。一般に、この混合は、大気圧下
室温で好ましくは湿り気のない状態で実施される。
The hydraulic fluid according to the invention is produced in a mixer with a component (al
, (b), (C1- and (d)) and Addition 1 together until sufficient and complete homogenization is achieved. Generally, this mixing is carried out at atmospheric pressure. It is carried out at lower room temperature, preferably in dry conditions.

本発明を下記の非制限的例によって説示する。The invention is illustrated by the following non-limiting examples.

例1 ブレーキ流体を、下記成分を一緒に混合することによっ
て調製した: 56.20 成分(C) : テトラエチレングリコールモノメチル
エーテル Z20 成分(d) : ペンタエチレングリコールモノメチル
エーテル00 計: 100.00 このブレーキ流体は下記特性を示したニー 全還流時沸
点(PERT) 250℃−加湿後沸点(WE’l’ 
PiT) 161℃−粘度(−40°C)1276C8
t −粘度(+100℃) 24 cSt −蒸気閉そく温度(VLT) )250℃−蒸気閉そく
温度+0.5%H20223℃−pH,10,7 〜 高温安定性 テスト合格 −化学安定性 “ −腐蝕(重量変化、m9/ ctrt2) :錫化鉄 
−0,01 策 −0,01 アルミニウム −〇、01 鋳鉄 +0.06 銅 −0,10 黄@ −0,13 −50℃で6時間 −水に対する許容量 −蒸発(蒸発せしめられる物質の重量 に対する重量X) 77 − 相容性 テスト合格 −抗酸化性(重量変化、m9/(:IrL2):鋳鉄 
±001 アルミニウム −0,01 −ゴムに対する影響 テスト合格 −模擬サービステスト 〃 (註二 上記および下記例の特性値は、・SAE J1
703、FMVSS 11(S オ、J: v CUN
A NC95(S−01規格の方法に従って測定した。
Example 1 A brake fluid was prepared by mixing together the following components: 56.20 Component (C): Tetraethylene glycol monomethyl ether Z20 Component (d): Pentaethylene glycol monomethyl ether 00 Total: 100.00 This brake The fluid has the following properties: Boiling point at total reflux (PERT) Boiling point after humidification (WE'l') at 250°C
PiT) 161℃ - Viscosity (-40℃) 1276C8
t - Viscosity (+100°C) 24 cSt - Vapor containment temperature (VLT) ) 250°C - Vapor containment temperature + 0.5% H20223°C - pH, 10,7 ~ High temperature stability Test passed - Chemical stability " - Corrosion (weight) Change, m9/ctrt2): iron stanride
−0,01 Measures −0,01 Aluminum −〇,01 Cast iron +0.06 Copper −0,10 Yellow @ −0,13 −6 hours at 50°C − Allowance for water − Evaporation (relative to the weight of the substance to be evaporated) Weight
±001 Aluminum -0,01 - Effect on rubber Test passed - Simulated service test (Note 2) The characteristic values of the above and the following examples are:
703, FMVSS 11 (S O, J: v CUN
A NC95 (measured according to the method of S-01 standard.

) 比較のため、下記組成を有す・る混合物の調製を開示し
たフランス国特許第2、j58,525号の例1を反復
した。
) For comparison, Example 1 of French Patent No. 2, J58,525, which discloses the preparation of a mixture having the following composition, was repeated.

部数 テトラエチレングリコール 3o7゜ トリエチレングリコールモノメチルエーテル 55.0
ジエチレングリコール 150 ジプチルアミン 06 JAge Rite Re5in D J O,1硝酸
ナトリウム 0.02 計: 100.42部 か(して得た流体に関し、次の特性値が測定されたニ ー 全還流沸点 248℃ −加湿後沸点 1565℃ −粘度(−40°C) 1585 cSt例2 液圧流体を、下記成分を一緒に混合することにより調製
した: 成分(a):)ジエチレングリコール 60.0%成分
(bl: トリエチレングリコールモノメチルエーテル
 6乙0% 成分(C): テトラエチレングリコールモノメチルエ
ーテル 3!1.OX 成分(d): ヘンタエチレンクリコールモノメチルエ
ーテル 4.0X 計: 1(10,00% この流体は下記特性を示したニ ー 全還流沸点 266℃ −加湿後沸点 159℃ −粘度(−40℃) 1192 cst−低温流動性お
よび様相 テスト合格 例3 液圧流体を、下記成分を一緒に混合することにより調製
した: 成分(a):゛ジエチレングリコール 25.0%成分
(b)ニトリエチレングリコール モノメチルエーテル 30.0% 成分(C): テトラエチレングリコールモノメチルエ
ーテル 16.0% 成分(C):ヘンタメチレンクリコールモノメチルエー
テル 2.ON 計: 1oo、oo% この流体は下記特性値を示したニ ー 全還流沸点 249°C −加湿後沸点 158℃ −粘度(−40℃) 1178 cst−蒸気閉そく温
度 〉250℃ −蒸気閉そく温度+0.5%H20219℃−蒸発(X
部/部)65 例4 液圧流体を、下記成分を混合することにより調製した: 成分(a): ジエチレングリコール 30.0%成分
(bl: )リエチレングリコールモノメチルエーテル
 30.0% 計: 1oo、oo% この流体は下記特性値を示したニ ー 全還流沸点 246°C −加湿後沸点 160℃ −粘度(−40℃) 1264 cst−低温流動性お
よび様相 テスト合格 例5 液圧流体を、下記成分を一緒に混合することにより調製
した: 成分(a): ジエチレングリコール 30.0%成分
(b)ニトリエチレングリコール 43.0%計: 1
00.00X この流体は下記特性値を示したニ ー 全還流沸点 2466C −加湿後沸点 159°C −粘度(−40℃) 1227 cSt−蒸気閉そく温
度 〉250℃ −蒸気閉そ(温度+0.5%H20219℃−低温流動
性および様相・ テスト合格例6 はう素含量0.1%の液圧流体を、下記成分を一緒に混
合することにより調製した: 重量% 成分(a): ジエチレングリコール 22.00X計
: 1oo、oo% この流体は下記特性値を示したニ ー 全還流神意 249°C −加湿後沸点 161℃ −粘度(−40℃) 11415 cSt比較のため、
フランス国特許第2,158,524号の例3に記載の
ものに知似した、等量(約0.1%)のほう素を含み、
また下記組成からなる流体を調製した: 部% − テトラエチレンクリコール 37−2−トリエチレ
ングリコールモノブチルエーテ/l/20.0− トリ
エチレングリコールモノメチルエーテル 67.8− 
Age Rite Re5in D Q、1− 硝酸ナ
トリウム 0.02 計: 1oo、oo部% かくして得た流体に関し下記特性値が測定されたニー 
全還流沸点 246℃ −加湿後沸点 156°C −粘度(−40℃) 1360 cst例7 はう素含量0.46%の液圧流体を、下記成分を一緒に
混合することにより調製した: 成分(a): ジエチレングリコ−# 8.2%成分(
b)ニトリエチレンクリコール モノメチルエーテル 53.0% 成分(C): テトラエチレングリコールモノメチルエ
ーテル 20.0% 成分(d) : HBOとジエチレングリコール(シル
’Ih 1:3)との反応生成物 13.8%計: 1
oo、oo% この流体は下記特性値を示したニ ー 全還流沸点 252℃ −加湿後沸点 167°C −粘度(−40°C) 1096cSt比較のため、フ
ランス国特許第2.158.522号の例1に従って、
等量の0.46%はう素を含み而して下記成分よりなる
流体を調製したニー’)!、l−1−チレングリコール
モノメチルエーテル 75部%かくして得た流体に関し
下記特性値が測定されたニー 全還流沸点 264℃ −加湿後沸点 159℃ −粘度(−40℃) 1030 cst例8 はう素含量0.5Xの液圧流体を、下記成分を一緒に混
合することにより調製した: 成分(a)ニジエチレンクリコール 8.0%成分(b
): )ジエチレングリコールモノメチルエーテル 5
2.0% 成分(C) : テトラエチレングリコールモノメチル
エーテル 20部% 成分(C):ヘンタエチレングリ・コールモZメチルエ
ーテル 5.0% 成分(d) : HBOとジエチレングリコール(3E
−ルb 1:3)との反応生成物 15.0X100.
00% この流体は下記特性値を示したニ ー 全還流沸点 253℃ −加湿後沸点・ 169℃ −粘度(−40℃) 1143 cSt例? はう素含量0.7Xの液圧流体を、下記成分を一緒に混
合することにより調製した: 成分(a): ジエチレングリコール 2.0%成分(
b): )ジエチレングリコールモノメチルエーテル 
56.9% 成分(C): テトラエチレングリコールモノメチルエ
ーテル 20部% 成分”’ ” ”:%C,C七’>’b”;4’Q”a
e、L 2 t I Xこの流体は下記特性値を示した
ニ ー 全還流沸点 250°C −加湿後沸点 175℃ −粘度(−40°C) 1409 cStS引例 はう素含量046%の液圧流体を、下記成分を一緒に混
合することにより調製した: 成分(a)ニジエチレングリコール 7.2%成分(b
) : ) IJエチレンクリコールモノメチルエーテ
ル 54.0% 成分(C): テトラエチレングリコールモノメチルエ
ーテル 20.0% 成分(“)” 1jぜ♀Lへ91.−F−VあΩ量論 
13.8X計: 100.00X この流体は下記特性値を示したニ ー 全還流沸点 252℃ −加湿後沸点 162℃ −粘度(−40℃) 1096 cst−流動性および
様相(−50℃): テスト合格例11 はう素含量0.5%の液圧流体を、下記成分を一緒に混
合することにより調製゛した: 成分(a): )ジエチレングリコール 6.0%成分
(b)ニトリエチレンクリコール モノメチルエーテル 50.8% 成分(C): テトラエチレングリコールモノメチルエ
ーテA/20.0% 計: 1oo、oo% この流体は下記特性値を示したニ ー 全還流沸点 265℃ −加湿後沸点 167℃ −粘度(−P40℃) 1546cst−流動性および
様相(−50℃) テスト合格例12 はう素含量0.43%の液圧流体を、下記成分を一緒に
混合することにより調製した: lff1分(a): ジエチレングリコール 9.00
%成分(d) : 83H(J3とジエチレングリコー
ル(モル比1:3)との反応生成物 12.96%io
o、oo% この流体は下記特性値を示したニ ー 全還流沸点 249℃ −加湿後沸点 167℃ −粘度(−40℃) 1092 cst−流動性および
様相(−50℃) テスト合格比較のため、米国特許第
3.711.410号の例68に記載のものに類似せる
、はう素含量0.43%の、下記基本成分よりなる流体
を調製したニー トリエチレングリコールモノメチルエ
ーテル 7s、o1g%−テトラエチレングリコールモ
ノメチルエーテル 4.70部%計: 99.71部% この流体は下記特性値を示したニ ー 全還流沸点 2439C −加湿後沸点 162℃
Parts Tetraethylene glycol 3o7゜Triethylene glycol monomethyl ether 55.0
Diethylene glycol 150 Diptylamine 06 JAge Rite Re5in D J O,1 Sodium nitrate 0.02 Total: 100.42 parts 1565°C - Viscosity (-40°C) 1585 cSt Example 2 A hydraulic fluid was prepared by mixing together the following components: Component (a):) Diethylene glycol 60.0% component (bl: Triethylene glycol monomethyl Ether 600% Component (C): Tetraethylene glycol monomethyl ether 3!1.OX Component (d): Hentaethylene glycol monomethyl ether 4.0X Total: 1 (10,00%) This fluid showed the following characteristics Total reflux boiling point 266°C - Boiling point after humidification 159°C - Viscosity (-40°C) 1192 cst - Cold flow properties and appearance Test Passing Example 3 A hydraulic fluid was prepared by mixing together the following components: Components ( a): Diethylene glycol 25.0% Component (b) Nitriethylene glycol monomethyl ether 30.0% Component (C): Tetraethylene glycol monomethyl ether 16.0% Component (C): Hentamethylene glycol monomethyl ether 2.ON Total: 1oo, oo% This fluid showed the following characteristic values: Total reflux boiling point 249°C - Boiling point after humidification 158°C - Viscosity (-40°C) 1178 cst - Steam confinement temperature 〉250°C - Vapor confinement temperature +0. 5% H20219℃-evaporation (X
Part/Part) 65 Example 4 A hydraulic fluid was prepared by mixing the following components: Component (a): Diethylene glycol 30.0% Component (bl: )Lyethylene glycol monomethyl ether 30.0% Total: 1oo, oo % This fluid showed the following characteristic values: Total reflux boiling point 246°C - Boiling point after humidification 160°C - Viscosity (-40°C) 1264 cst - Low temperature fluidity and appearance Test passing example 5 Hydraulic fluid was prepared with the following components. Prepared by mixing together: Component (a): Diethylene glycol 30.0% Component (b) Nitriethylene glycol 43.0% Total: 1
0.00 H202 19°C - Low Temperature Flowability and Appearance - Test Pass Example 6 A hydraulic fluid with 0.1% boron content was prepared by mixing together the following components: Weight % Component (a): Diethylene glycol 22.00X Total: 1oo, oo% This fluid showed the following characteristic values Total reflux 249°C - Boiling point after humidification 161°C - Viscosity (-40°C) 11415 cSt For comparison,
containing an equal amount (approximately 0.1%) of boron, similar to that described in Example 3 of French Patent No. 2,158,524;
A fluid having the following composition was also prepared: Part % - Tetraethylene glycol 37 - 2-Triethylene glycol monobutyl ether/l/20.0 - Triethylene glycol monomethyl ether 67.8 -
Age Rite Re5in D Q, 1- Sodium Nitrate 0.02 Total: 1oo, oo parts% The following characteristic values were measured for the fluid thus obtained.
Total reflux boiling point 246°C - Boiling point after humidification 156°C - Viscosity (-40°C) 1360 cst Example 7 A hydraulic fluid with a 0.46% borosine content was prepared by mixing together the following components: Ingredients (a): Diethylene glyco-# 8.2% component (
b) Nitriethylene glycol monomethyl ether 53.0% Component (C): Tetraethylene glycol monomethyl ether 20.0% Component (d): Reaction product of HBO and diethylene glycol (Syl'Ih 1:3) 13.8 % total: 1
oo, oo% This fluid showed the following characteristic values: Total reflux boiling point 252°C - Boiling point after humidification 167°C - Viscosity (-40°C) 1096 cSt For comparison, French Patent No. 2.158.522 According to example 1,
An equal amount of 0.46% of borine was prepared by preparing a fluid consisting of the following components. , l-1-ethylene glycol monomethyl ether 75 parts% The following characteristic values were measured for the fluid thus obtained: Total reflux boiling point 264°C - Boiling point after humidification 159°C - Viscosity (-40°C) 1030 cst Example 8 Boron A hydraulic fluid with a content of 0.5X was prepared by mixing together the following components: Component (a) Nidiethylene glycol 8.0% Component (b
): ) Diethylene glycol monomethyl ether 5
2.0% Component (C): Tetraethylene glycol monomethyl ether 20 parts% Component (C): Hentaethylene glycol monomethyl ether 5.0% Component (d): HBO and diethylene glycol (3E
Reaction product with -ru b 1:3) 15.0X100.
00% This fluid showed the following characteristic values Total reflux boiling point 253℃ - Boiling point after humidification 169℃ - Viscosity (-40℃) 1143 cSt Example? A hydraulic fluid with a 0.7X boronate content was prepared by mixing together the following components: Component (a): Diethylene glycol 2.0% component (
b): ) Diethylene glycol monomethyl ether
56.9% Component (C): Tetraethylene glycol monomethyl ether 20 parts% Component "'"": %C, C7'>'b";4'Q"a
e, L 2 t I was prepared by mixing together the following ingredients: Component (a) Nidiethylene glycol 7.2% Component (b)
) : ) IJ Ethylene glycol monomethyl ether 54.0% Component (C): Tetraethylene glycol monomethyl ether 20.0% Component (")" 1j ze♀L 91. -F-VaΩstoichiometry
13.8X Meter: 100.00X This fluid exhibited the following characteristics: Total reflux boiling point 252°C - Boiling point after humidification 162°C - Viscosity (-40°C) 1096 cst - Fluidity and appearance (-50°C): Test Passing Example 11 A hydraulic fluid with a 0.5% borosine content was prepared by mixing together the following components: Component (a): ) Diethylene glycol 6.0% Component (b) Nitriethylene glycol monomethyl Ether 50.8% Component (C): Tetraethylene glycol monomethyl ether A/20.0% Total: 1oo, oo% This fluid showed the following characteristic values: Total reflux boiling point 265℃ - Boiling point after humidification 167℃ - Viscosity (-P40°C) 1546cst - Flowability and Appearance (-50°C) Test Passing Example 12 A hydraulic fluid with a 0.43% boron content was prepared by mixing together the following components: lff1 min (a ): Diethylene glycol 9.00
% component (d): 83H (reaction product of J3 and diethylene glycol (molar ratio 1:3) 12.96% io
o, oo% This fluid showed the following characteristic values: Total reflux boiling point 249°C - Boiling point after humidification 167°C - Viscosity (-40°C) 1092 cst - Fluidity and appearance (-50°C) Test pass For comparison, A fluid similar to that described in Example 68 of U.S. Pat. No. 3,711,410, with a 0.43% borosine content, was prepared consisting of the following basic components: Neat triethylene glycol monomethyl ether 7s, 1 g% - Tetraethylene glycol monomethyl ether 4.70 parts% Total: 99.71 parts% This fluid showed the following characteristic values: Total reflux boiling point 2439C - Boiling point after humidification 162°C

Claims (5)

【特許請求の範囲】[Claims] (1)臭素含量0〜1重量%の本質上下記成分すなわち
、 a)一般式 %式%() (ここでR3は炭素原子2〜3個のアルキレン基であり
、Xは1〜3の整数である)を有するアルキレングリコ
ール2〜40重量%、 b)一般式 %式%() (ここでRaおよびXは既述の意味を有し、社は01〜
C4アルキルである) を有するアルキレングリコールモノアルキルエーテル1
5〜65重量%、 C)一般式 %式%() (ここでRはC4〜C4アルキルであり、R1はH又は
Cd5であり、nは、本化合物の分子量を208〜10
00範囲とする如き整数である) を有するポリアルキレングリコールモノアルキルエーテ
ル少くとも1種15〜55重量%、d)1:1.5〜3
モル比のH5BO,と前記一般式(I)のアルキレ/グ
リコールとの反応生成物0〜54重量%、および e)抑制剤少くとも1種0〜10重量%よりなる液圧流
体(但し、全ての重量%は本液圧流体の総重量に基づく
ものとする)。
(1) bromine content of 0 to 1% by weight, essentially the following components: 2-40% by weight of an alkylene glycol having the general formula % () (where Ra and
C4 alkyl)
5-65% by weight, C) general formula % formula % () (where R is C4-C4 alkyl, R1 is H or Cd5, n represents the molecular weight of the compound from 208 to 10
d) 15-55% by weight of at least one polyalkylene glycol monoalkyl ether having the following integer range: 1:1.5-3
A hydraulic fluid consisting of a molar ratio of 0 to 54% by weight of the reaction product of H5BO and the alkylene/glycol of general formula (I), and e) 0 to 10% by weight of at least one inhibitor (provided that all weight percent shall be based on the total weight of the hydraulic fluid).
(2)式(Iff)を有する化合物C)において、R1
がHであり、nが、該化合物の分子量を208〜340
範囲とする如き整数であることを特徴とする特許請求の
範囲第1項記載の液圧流体。
(2) In compound C) having formula (Iff), R1
is H, and n represents the molecular weight of the compound from 208 to 340.
A hydraulic fluid as claimed in claim 1, characterized in that the range is an integer.
(3)流体が奥歯を含まず而して、 a)ジエチレングリコールおよびトリエチレングリコー
ルより選ばれるアルキレングリコール23〜33重量%
、 b)トリエチレングリコールモノメチルエーテル20〜
45重量%、および C)平均分子量208〜600の、一般式(111)を
有する化合物類よりなる群から選ばれるポリアルキレン
グリコールモノメチルエーテル少くとも1棟20〜50
重量%よりなることを特徴とする特許請求の範囲第1項
記載の液圧流体。
(3) The fluid does not contain back teeth, and a) 23 to 33% by weight of an alkylene glycol selected from diethylene glycol and triethylene glycol.
, b) Triethylene glycol monomethyl ether 20~
45% by weight, and C) at least one polyalkylene glycol monomethyl ether selected from the group consisting of compounds having the general formula (111) with an average molecular weight of 208 to 600.
Hydraulic fluid according to claim 1, characterized in that it consists of % by weight.
(4)流体が臭素を含み而して本質上下記成分すなわち
、 a)ジエチレングリコールおよびトリエチレングリコー
ルよりなる群から選ばれるアルキレングリコール2〜z
s、35<i%、b)トリエチレングリコールモノメチ
ルエーテル40〜60重量%、 C)平均分子量208〜600の、一般式(III)を
有する化合物類よりなる群から選ばれるポリアルキレン
グリコールモノアルキルエーテル少くとも1釉15〜3
5重量%、 d)ジエチレングリコールおよびトリエチレングリコー
ルよりなる群から選ばれるアルキレングリコール3モル
とH5B0.1モルとの反応生成物3〜34重景% 装置なることを特徴とする特許請求の範囲第1項記載の
液圧流体。
(4) The fluid contains bromine and consists essentially of the following components: a) Alkylene glycols selected from the group consisting of diethylene glycol and triethylene glycol 2-z
s, 35<i%, b) 40 to 60% by weight of triethylene glycol monomethyl ether, C) polyalkylene glycol monoalkyl ether selected from the group consisting of compounds having the general formula (III) and having an average molecular weight of 208 to 600. At least 1 glaze 15-3
5% by weight, d) 3-34% by weight of a reaction product of 3 moles of an alkylene glycol selected from the group consisting of diethylene glycol and triethylene glycol and 0.1 mole of H5B. Hydraulic fluids as described in Section.
(5) 成分d)が流体の総重量に対し3〜24重量%
を占め、そして該成分がジエチレングリコール3モルと
H,Bo、 1モルとの反応生成物であることを特徴と
する特許請求の範囲第4項記載の液圧流体。
(5) Component d) is 3 to 24% by weight based on the total weight of the fluid.
Hydraulic fluid according to claim 4, characterized in that the component is the reaction product of 3 moles of diethylene glycol and 1 mole of H, Bo.
JP59123901A 1983-06-21 1984-06-18 Hydraulic fluid Granted JPS6013892A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT21698/83A IT1163547B (en) 1983-06-21 1983-06-21 HYDRAULIC FLUIDS
IT21698A/83 1983-06-21

Publications (2)

Publication Number Publication Date
JPS6013892A true JPS6013892A (en) 1985-01-24
JPH0458520B2 JPH0458520B2 (en) 1992-09-17

Family

ID=11185563

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59123901A Granted JPS6013892A (en) 1983-06-21 1984-06-18 Hydraulic fluid

Country Status (4)

Country Link
EP (1) EP0129240B2 (en)
JP (1) JPS6013892A (en)
DE (1) DE3470176D1 (en)
IT (1) IT1163547B (en)

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IT1163547B (en) 1987-04-08
EP0129240B1 (en) 1988-03-30
IT8321698A0 (en) 1983-06-21
EP0129240A1 (en) 1984-12-27
JPH0458520B2 (en) 1992-09-17
DE3470176D1 (en) 1988-05-05
EP0129240B2 (en) 1994-06-01

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