EP0236844B1 - Use of additives for mineral oils with modified pour- point characteristics - Google Patents
Use of additives for mineral oils with modified pour- point characteristics Download PDFInfo
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- EP0236844B1 EP0236844B1 EP87102629A EP87102629A EP0236844B1 EP 0236844 B1 EP0236844 B1 EP 0236844B1 EP 87102629 A EP87102629 A EP 87102629A EP 87102629 A EP87102629 A EP 87102629A EP 0236844 B1 EP0236844 B1 EP 0236844B1
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- unbranched
- methacrylic acid
- alkoholgemisches
- tert
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/14—Use of additives to fuels or fires for particular purposes for improving low temperature properties
- C10L10/16—Pour-point depressants
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/192—Macromolecular compounds
- C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
- C10L1/196—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
- C10L1/1963—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof mono-carboxylic
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/234—Macromolecular compounds
- C10L1/236—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
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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
- C10M145/00—Lubricating compositions characterised by the additive being a macromolecular compound containing oxygen
- C10M145/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M145/10—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate
- C10M145/12—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate monocarboxylic
- C10M145/14—Acrylate; Methacrylate
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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
- C10M149/00—Lubricating compositions characterised by the additive being a macromolecular compound containing nitrogen
- C10M149/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
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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
- C10M149/00—Lubricating compositions characterised by the additive being a macromolecular compound containing nitrogen
- C10M149/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M149/06—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an amido or imido group
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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
- C10M149/00—Lubricating compositions characterised by the additive being a macromolecular compound containing nitrogen
- C10M149/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M149/10—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a nitrogen-containing hetero ring
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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
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/08—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type
- C10M2209/084—Acrylate; Methacrylate
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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
- C10M2217/00—Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2217/02—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds
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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
- C10M2217/00—Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2217/02—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2217/022—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an amino group
- C10M2217/023—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an amino group the amino group containing an ester bond
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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
- C10M2217/00—Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2217/02—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2217/024—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to an amido or imido group
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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
- C10M2217/00—Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2217/02—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2217/028—Macromolecular compounds obtained from nitrogen containing monomers by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a nitrogen-containing hetero ring
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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
- C10M2217/00—Organic macromolecular compounds containing nitrogen as ingredients in lubricant compositions
- C10M2217/06—Macromolecular compounds obtained by functionalisation op polymers with a nitrogen containing compound
Description
Die Erfindung betrifft die Verwendung von Additiven für Mineralöle, insbesondere für Destillatöle mit stockpunktverbessernder Wirkung auf Basis von Alkylmethacrylaten.The invention relates to the use of additives for mineral oils, in particular for distillate oils with a pour point-improving effect based on alkyl methacrylates.
Mineralöle, wie z.B. handelsübliche Destillatöle, enthalten in der Regel n-Paraffinkohlenwasserstoffe, die sich zwar einerseits auf die Einstellung eines guten Viskositäts-/Temperaturverhaltens günstig auswirken, andererseits aber beim Abkühlen in kristalliner Form ausfallen und dadurch das Fließen der Öle beeinträchtigen oder völlig verhindern ("Stocken"). Eine Verbesserung der Tieftemperatur-Fließeigenschaften kann durch Entparaffinierung erreicht werden. Da die Kosten erheblich ansteigen, wenn man den "Pour point" über bestimmte Werte hinweg herabsetzen will, führt man im allgemeinen nur eine partielle Entparaffinierung der Öle bis zu einem Pour point im Bereich von minus 15 Grad Celsius durch und bedient sich zur weiteren Herabsetzung des Pour point (bis etwa minus 40 Grad Celsius) sogenannter Pour point-Erniedriger, die den Pour point bereits in Konzentrationen zwischen 0,05 und 1 % wirksam herabsetzen. Dabei ist in etwa folgende Vorstellung maßgeblich:Mineral oils, e.g. Commercial distillate oils generally contain n-paraffin hydrocarbons, which on the one hand have a favorable effect on the setting of a good viscosity / temperature behavior, but on the other hand fail in crystalline form on cooling and thereby impair the flow of the oils or completely prevent them ("stagnation") . An improvement in the low-temperature flow properties can be achieved by dewaxing. Since the costs increase considerably if one wants to lower the "pour point" beyond certain values, one generally only partially dewaxes the oils to a pour point in the range of minus 15 degrees Celsius and uses the further reduction Pour point (up to about minus 40 degrees Celsius) so-called pour point depressants, which effectively reduce the pour point in concentrations between 0.05 and 1%. The following idea is decisive:
Paraffinähnliche Verbindungen werden in die wachsenden Paraffinkristallflächen eingebaut und verhindern so das Weiterwachsen der Kristalle und die Bildung ausgedehnter Kristallverbände.Paraffin-like compounds are built into the growing paraffin crystal surfaces and thus prevent the crystals from growing further and the formation of extensive crystal groups.
Für die Wirkungsweise derartiger Pour-Point-Verbesserer gilt, daß sie bestimmte Strukturelemente aufweisen, nämlich hinreichend lange Alkylgruppen, um von der Keimbildung ab in die wachsenden Paraffinkristalle eingebaut zu werden und in größeren Abständen Seitenketten bzw. Seitengruppen um das Kristallwachstum zu stören. (Vgl. Ullmanns, Encyklopädie der technischen Chemie, 4. Auflage, Band 20, Verlag Chemie, 1981, S. 548). Von technisch anwendbaren Pour-point-Erniedrigern muß andererseits verlangt werden, daß sie gute thermische, oxidative und chemische Stabilität, Scherfestigkeit u.ä. besitzen.For the mode of operation of such pour point improvers, it applies that they have certain structural elements, namely sufficiently long alkyl groups to be incorporated into the growing paraffin crystals from the nucleation and side chains or side groups at greater intervals to disrupt the crystal growth. (See Ullmanns, Encyklopedia of technical chemistry, 4th edition, volume 20, Verlag Chemie, 1981, p. 548). Technically applicable pour point depressants, on the other hand, must be required to have good thermal, oxidative and chemical stability, shear strength and the like. have.
Die zur Zeit bevorzugten Pour-point-Erniedriger sind Polymethacrylate, die bereits in Konzentrationen von 0,1 - 0,5 % den Fließpunkt von Schmierölen hinreichend erniedrigen (vgl. US-PS 2 091 627, US-PS 2 100 993, US-PS 2 114 233). Die Kohlenstoffzahl der Alkylreste liegt dabei zwischen 12 und 18, der Verzweigungsgrad zwischen 10 und 30 Mol-%. Zur Verfügung stehen Polymethacrylate im Bereich
Bekanntlich haben sich auch Olefincopolymerisate (OCP's) unter verschiedenen Anwendungs-Gesichtspunkten als Mineralöladditive in der Praxis bewährt. (Vgl. DE-AS 1 235 491).The currently preferred pour point depressants are polymethacrylates, which lower the pour point of lubricating oils sufficiently in concentrations of 0.1-0.5% (cf. US Pat. No. 2,091,627, US Pat. No. 2,100,993, US Pat. PS 2 114 233). The carbon number of the alkyl radicals is between 12 and 18, the degree of branching between 10 and 30 mol%. Polymethacrylates are available in the area
As is known, olefin copolymers (OCP's) have also proven themselves in practice as mineral oil additives from various application points of view. (See DE-AS 1 235 491).
Relativ viel Beachtung fanden daher Copolymerisate aus diesen beiden Polymerklassen. So beschreibt die DE-OS 21 02 469 unter anderem niedermolekulare Copolymere des Ethylens mit Methylmethacrylat oder 2-Ethylhexylacrylat (M
In der europ. Patentanmeldung 113 591 werden als Schmieröl- und Treibstoffadditive hydrierte Emulsionscopolymere aus 1,3-Butadien und Alkyl(meth)acrylat beschrieben, die als VI-Verbesserer und Stockpunktsverbesserer angewendet werden können. Dispergierende Wirkung erhalten diese Polymere, wenn man sie mit polaren, stickstoffhaltigen Monomeren pfropft.
In der DE-OS 26 12 232 wird eine Kombination eines Ethylen-Isobutylacrylat-Copolymeren und eines Polytetradecylacrylat- oder Hexadecylmethacrylat-Methylmethacrylat-Copolymeren als Additiv für Petroleum-Destillate (b.p. 120 - 480 Grad Celsius) zur Regulierung der Wachskristallbildung im Niedertemperaturbereich empfohlen.
Als Viskositätsindex-Verbesserer mit dispergierender Wirkung werden die Umsetzungsprodukte aus einem langkettigen Alkylacrylat bzw. -methacrylat, einem C1-C4-Alkylacrylat oder -methacrylat und Acrylsäure, die mit 1-Hydroxy-2-alkyl- oder alkylidenimidazolin neutralisiert wurde, in der US-PS 3 397 146 empfohlen.In the European Patent application 113,591 are described as lubricating oil and fuel additives, hydrogenated emulsion copolymers of 1,3-butadiene and alkyl (meth) acrylate, which can be used as VI improvers and pour point improvers. These polymers have a dispersing effect if they are grafted with polar, nitrogen-containing monomers.
DE-OS 26 12 232 recommends a combination of an ethylene-isobutyl acrylate copolymer and a polytetradecyl acrylate or hexadecyl methacrylate-methyl methacrylate copolymer as an additive for petroleum distillates (bp 120-480 degrees Celsius) to regulate wax crystal formation in the low temperature range.
The reaction products of a long-chain alkyl acrylate or methacrylate, a C1-C4-alkyl acrylate or methacrylate and acrylic acid, which has been neutralized with 1-hydroxy-2-alkyl- or alkylidene imidazoline, are described as viscosity index improvers with dispersing action in the US PS 3 397 146 recommended.
Auch die Lehre der FR-A 1 235 693 betrifft polymere VI-Verbesserer auf Basis von Poly(meth)acrylsäureestern mit Vinylpyridin als Co-monomer, wobei die praktisch verwendeten Anwendungskonzentrationen bei ≥ 1,5 % liegen im Einklang mit der üblichen Praxis bei VI-Verbesserern.The teaching of FR-A 1 235 693 also relates to polymeric VI improvers based on poly (meth) acrylic esters with vinylpyridine as a co-monomer, the practical application concentrations being ≥ 1.5% being in line with VI's usual practice -Improve.
In der DE-OS 21 45 249 werden unter Verwendung von Aminen als Initiator hergestellte Polymethacrylate als Schmieröladditive empfohlen. Beispielhaft ausgeführt wurde die Herstellung von Polybutylmethacrylat mit einem Molgewicht von 455 000.
Weiter sind Additive für n-paraffinhaltige Schmieröle entwickelt worden, die auf Mischungen von verschiedenen Acrylatpolymeren beruhen (DE-OS 33 39 103). Diese Mischungen bestehen
- I. aus 10 - 99 Gew.-% an Polymeren P1, die
- a) aus (Meth)acrylsäureestern von geradkettigen, unverzweigten C6-C15-Alkoholen mit 6 bis 15 Kohlenstoffatomen und
- b) aus (Meth)acrylsäureestern von geradkettigen unverzweigten C16-C30-Alkoholen und
- c) aus (Meth)acrylsäureestern mit verzweigten C8-C40-Alkoholen,
- d) aus (Meth)acrylsäureestern von C1-C5-Kohlenstoffatomen,
- e) aus Monomeren, mit funktionellen Gruppen aufgebaut sind,
- II. aus 90 - 1 Gew.-% an Polymeren P2, die
- a') aus (Meth)acrylsäureestern von geradkettigen unverzweigten C6-C15-Alkoholen und
- b') aus (Meth)acrylsäureestern von geradkettigen, unverzweigten C16-C30-Alkoholen und
- c') aus (Meth)acrylsäureestern von verzweigten C8-C40-Alkoholen und
- d') aus (Meth)acrylsäureestern von C1-C5-Alkoholen aufgebaut sind,
- e') aus Monomeren mit funktionellen Gruppen
Furthermore, additives have been developed for lubricating oils containing n-paraffin, which are based on mixtures of different acrylate polymers (DE-OS 33 39 103). These mixtures exist
- I. from 10 - 99 wt .-% of polymers P1, the
- a) from (meth) acrylic acid esters of straight-chain, unbranched C6-C15 alcohols with 6 to 15 carbon atoms and
- b) from (meth) acrylic acid esters of straight-chain unbranched C16-C30 alcohols and
- c) from (meth) acrylic acid esters with branched C8-C40 alcohols,
- d) from (meth) acrylic acid esters of C1-C5 carbon atoms,
- e) are composed of monomers with functional groups,
- II. From 90-1% by weight of polymers P2, the
- a ') from (meth) acrylic acid esters of straight-chain unbranched C6-C15 alcohols and
- b ') from (meth) acrylic acid esters of straight-chain, unbranched C16-C30 alcohols and
- c ') from (meth) acrylic acid esters of branched C8-C40 alcohols and
- d ') are composed of (meth) acrylic acid esters of C1-C5 alcohols,
- e ') from monomers with functional groups
In der DE-A-1 444 884 werden in Öl gelöste Mischpolymerisate auf Basis von Acrylestern beansprucht, wobei das Polymerisat ein Pfropfmischpolymerisat aus mindestens einem Alkylacrylat oder -methacrylat darstellt, dessen Alkylrest Öllöslichkeit gewährleistet. Diesem Polymerisat sind Einheiten von Maleamin- oder Itaconaminsäuren aufgepfropft, die 1-22 Gew-% des Pfropfmischpolymerisats ausmachen. Soweit diese Pfropfmischpolymerisate zur Erniedrigung des "Gießpunktes" eingesetzt wurden, werden sie in Zusatzmengen von 1 Gew.-% angewendet.DE-A-1 444 884 claims copolymers dissolved in oil based on acrylic esters, the polymer being a graft copolymer made from at least one alkyl acrylate or methacrylate, the alkyl radical of which ensures oil solubility. Units of maleamic or itaconamic acids, which make up 1-22% by weight of the graft copolymer, are grafted onto this polymer. To the extent that these graft copolymers have been used to lower the "pour point", they are used in additional amounts of 1% by weight.
Es erscheint bemerkenswert, daß methylmethacrylat-haltige Stockpunktverbesserer bislang keinen Eingang in die Praxis gefunden haben. Dabei dürfte die an sich berechtigte Erwartung eine Rolle gespielt haben, daß Produkte die Methylmethacrylat in substantiellen Anteilen enthalten, erst bei höheren Zusatzmengen eine zufriedenstellende Wirkung entfalten.It appears remarkable that pour point improvers containing methyl methacrylate have so far not been used in practice. The justified one should be Expectations have played a role that products that contain methyl methacrylate in substantial proportions only develop a satisfactory effect with higher additions.
Es bestand nach wie vor die Aufgabe, stockpunktverbessernde Additive für Mineralöle, insbesondere Destillatöle auf paraffinischer Basis zur Verfügung zu stellen, die bei unverminderter Effizienz, d.h. in etwa gleichen Anwendungskonzentrationen wirkend, möglichst kostengünstig herstellbar sein sollten. Insbesondere war an den Ersatz der relativ teuren höheren Alkylester zu denken.It was still the task to provide pour point improving additives for mineral oils, in particular distillate oils on a paraffinic basis, which with undiminished efficiency, i.e. acting in approximately the same application concentrations, should be able to be produced as inexpensively as possible. In particular, the replacement of the relatively expensive higher alkyl esters was to be considered.
Es wurde nun gefunden, daß die vorstenend genannte Aufgabe in besonders günstiger Weise gelöst werden kann mittels der erfindungsgemäßen Verwendung definierter Additive als Stockpunktverbesserer in Mineralölen. Die erfindungsgemäß zu verwendenden Additive mit stockpunktverbessernder Wirkung bestehen aus einem Polymethacrylat P in Form statis aufgebaut aus
- a) 10 - 30 Molprozent, vorzugsweise 10 - 20 Molprozent Methylmethacrylat
- b) 10 - 70 Molprozent, vorzugsweise 10 - 50 Molprozent Alkylmethacrylaten mit unverzweigten Alkylestern mit 16 - 30 Kohlenstoffatomen im Alkylrest und
- c) 80 - 0 Molprozent, vorzugsweise 80 - 30 Molprozent, insbesondere 80 - 50 Molprozent Alkylmethacrylaten mit unverzweigten Alkylresten mit 4 - 15, vorzugsweise 6 - 15 Kohlenstoffatomen und/oder verzweigten Alkylresten mit 4 - 40, vorzugsweise 8 - 30, Kohlenstoffatomen im Alkylrest und als Monomerkomponente
daß die Monomerkomponente b) aus mehreren unter sich verschiedenden Alkylmethacrylaten besteht, als Öladditive, wobei die Polyalkylmethacrylate P in Mengen zwischen 0.05 und 1 Gew.-% als Stockpunkt-Verbesserer in Mineralölen eingesetzt werden.It has now been found that the above-mentioned object can be achieved in a particularly favorable manner by means of the use of defined additives according to the invention as pour point improvers in mineral oils. The additives to be used according to the invention with a pour point-improving effect consist of a polymethacrylate P in the form of statis
- a) 10-30 mole percent, preferably 10-20 mole percent methyl methacrylate
- b) 10-70 mol percent, preferably 10-50 mol percent of alkyl methacrylates with unbranched alkyl esters with 16-30 carbon atoms in the alkyl radical and
- c) 80-0 mol percent, preferably 80-30 mol percent, in particular 80-50 mol percent, of alkyl methacrylates with unbranched alkyl radicals having 4-15, preferably 6-15 carbon atoms and / or branched alkyl radicals with 4-40, preferably 8-30, carbon atoms in the alkyl radical and as a monomer component
that the monomer component b) consists of several different alkyl methacrylates, as oil additives, the polyalkyl methacrylates P being used in amounts between 0.05 and 1% by weight as pour point improvers in mineral oils.
Die Natur der Polymerisate P als statistische Copolymerisate ergibt sich u.a. aus der im weiteren gegebenen, allgemeinen Herstellungsvorschrift.The nature of the polymers P as statistical copolymers results, inter alia, from the general preparation instructions given below.
Die Polymeren P besitzen vorzugsweise einen Molekulargewichtsbereich 10 000 bis 800 000. Die Bestimmung des Molekulargewichts kann in an sich bekannter Weise mittels Gelpermeationschromatographie vorgenommen werden. (Vgl. Vieweg-Braun, Kunststoff-Handbuch, Band I, Carl Hanser Verlag, 1975). Üblicherweise liegen die Uneinheitlichkeiten (
Der Staudinger-Index beträgt 10 - 150 ml/g in Chloroform bei 20 Grad Celsius.The polymers P preferably have a molecular weight range of 10,000 to 800,000. The molecular weight can be determined in a manner known per se by means of gel permeation chromatography. (See Vieweg-Braun, Kunststoff-Handbuch, Volume I, Carl Hanser Verlag, 1975). The inconsistencies are usually (
The Staudinger index is 10 - 150 ml / g in chloroform at 20 degrees Celsius.
Eine bevorzugte Ausführungsart der Erfindung sieht als Maßgabe vor, daß sofern der Anteil der unverzweigten Alkylmethacrylate mit 4 bis 15 Kohlenstoffatomen im Alkylrest im Bereich 35 - 45 Mol-% bezogen auf das Polymerisat P liegt, der Anteil der Komponente b) am Polymerisat P 20 bis 30 Mol-% betragen soll.
Weiter soll als eine bevorzugte Ausführungsart der Erfindung die Maßgabe gelten, daß schon der Anteil der unverzweigten Alkylmethacrylate mit 4 bis 15 Kohlenstoffatomen im Alkylrest im Bereich 15 - 30 Mol-% liegt, der Anteil der Komponente b) am Polymerisat P 25 bis 40 Mol-% betragen soll. Desweiteren sieht eine ebenfalls bevorzugte Ausführungsart der Erfindung vor, daß sofern der Anteil der unverzweigten Alkylmethacrylate mit 4 bis 15 Kohlenstoffatomen im Alkylrest null Mol-% beträgt, der Anteil der Komponente b) am Polymerisat P 30 bis 50 Mol-% ausmacht.A preferred embodiment of the invention provides that, provided that the proportion of unbranched alkyl methacrylates having 4 to 15 carbon atoms in the alkyl radical is in the range 35-45 mol% based on the polymer P, the proportion of component b) in the polymer P 20 to 30 mol% should be.
A further preferred embodiment of the invention is that the proportion of unbranched alkyl methacrylates having 4 to 15 carbon atoms in the alkyl radical is in the range 15-30 mol%, and the proportion of component b) in the polymer P is 25 to 40 mol%. % should be. Furthermore, a likewise preferred embodiment of the invention provides that if the proportion of unbranched alkyl methacrylates having 4 to 15 carbon atoms in the alkyl radical is zero mol%, the proportion of component b) in the polymer P is 30 to 50 mol%.
Die Monomeren für die Komponenten a) - c) der Polymerisate P sind an sich bekannt.
Als Monomere der Komponente b) kommen die Methacrylsäureester der geradkettigen, unverzweigten C16-C30-Alkanole, insbesondere von unverzweigten C16-C24-Alkanole, speziell von C18-C22-Alkoholen in Frage. Genannt seien insbesondere Handelsprodukte wie die Talgfettalkohole sowie die unter dem Namen Alfole R (Produkt der Fa. Condea, Hamburg) im Handel befindlichen. Es können somit auch unter sich verschiedene Ester die Monomeren vom Typ b) bilden. Solche Mischungen können als vorteilhaft betrachtet werden.
Als Monomere der Komponente c) kommen einerseits die Methacrylsäureester der geradkettigen, unverzweigten C4-C15-Alkanole in Frage. Genannt seien z.B. die geradkettigen, unverzweigten C10-C14-Alkohole, insbesondere die nach dem Ziegler-Verfahren durch Hydrolyse von Aluminiumalkoxiden gewonnenen.
Erwähnt seien z.B. als Produkte die Lorole R der Fa. Henkel KG, Düsseldorf und die Alfole R der Fa. Condea, Hamburg.
Andererseits kommen als Monomere der Komponente c) die Methacrylsäureester verzweigter Alkanole mit 4 bis 40 Kohlenstoffatomen im Molekül, insbesondere der verzweigten C8-C20-Alkoholen des Iso-Alkanol-Typs, speziell des Isodecyl, Isotridecyl- und Isooctodecylalkohols in Frage.The monomers for components a) - c) of the polymers P are known per se.
Suitable monomers for component b) are the methacrylic acid esters of straight-chain, unbranched C16-C30 alkanols, in particular unbranched C16-C24 alkanols, especially C18-C22 alcohols. Commercial products such as tallow fatty alcohols and those sold under the name Alfole R (product from Condea, Hamburg) are particularly worth mentioning. Different esters can thus also form the monomers of type b). Such mixtures can be considered advantageous.
The monomers of component c) are, on the one hand, the methacrylic acid esters of the straight-chain, unbranched C4-C15 alkanols. Examples include the straight-chain, unbranched C10-C14 alcohols, particularly those obtained by the Ziegler process by hydrolysis of aluminum alkoxides.
Examples include the Lorole R from Henkel KG, Düsseldorf and the Alfole R from Condea, Hamburg.
On the other hand, the monomers of component c) are the methacrylic acid esters of branched alkanols having 4 to 40 carbon atoms in the molecule, in particular the branched C8-C20 alcohols of the isoalkanol type, especially isodecyl, isotridecyl and isooctodecyl alcohol.
Die Molgewichte
Die Herstellung der Polymerisate P kann nach den üblichen radikalischen Polymerisationsverfahren vorgenommen werden. (Vgl. H. Rauch-Puntigam, Th. Völker: Acryl- und Methacrylverbindungen, Springer-Verlag, Berlin, 1967).The polymers P can be prepared by the customary free-radical polymerization processes. (See H. Rauch-Puntigam, Th. Völker: Acryl- und Methacrylverbindungen, Springer-Verlag, Berlin, 1967).
Die Herstellung der Polymerisate schließt an die Polymerisationsverfahren des Standes der Technik an. In einem Reaktionsgefäß, das zweckmäßig mit Rührer, Thermometer, Rückflußkühler und Dosierleitung ausgestattet ist, wird eine Mischung aus Mineralöl und einer Monomerenmischung aus a), b) und c) vorgelegt, soweit die letzteren zum Einsatz kommen. Unter C02-Atmosphäre und Rühren wird auf ca. 90 - 100 Grad Celsius erhitzt. Nach Erreichen dieser Temperatur und Zugabe von Initiator (vorzugsweise Perverbindungen wie Perester, Peroxiden oder Azoverbindungen) wird eine Mischung aus den Monomeren a), b) und c), sowie weiterer Initiator zudosiert; ca. 2 Stunden nach Ende des Zulaufs wird weiterer Initiator nachgefüttert. Die Gesamtinitiatormenge liegt in der Regel bei 1 - 3 Gew.-%, bezogen auf die Gesamtmenge der Monomeren. Die Gesamtpolymerisationszeit beträgt im allgemeinen 8 - 9 Stunden. Man erhält eine viskose Lösung mit einem Polymerisatgehalt von im allgemeinen 40 - 70 Gew.-%.The preparation of the polymers follows the polymerization processes of the prior art. A mixture of mineral oil and a monomer mixture of a), b) and c) is placed in a reaction vessel which is expediently equipped with a stirrer, thermometer, reflux condenser and metering line, insofar as the latter are used. The mixture is heated to approx. 90 - 100 degrees Celsius under a C02 atmosphere and stirring. After this temperature has been reached and initiator (preferably per compounds such as peresters, peroxides or azo compounds) has been added, a mixture of the monomers a), b) and c) and further initiator is metered in; approx. 2 hours after the end of the feed, another initiator becomes replenished. The total amount of initiator is usually 1-3% by weight, based on the total amount of monomers. The total polymerization time is generally 8-9 hours. A viscous solution with a polymer content of generally 40-70% by weight is obtained.
Ölaufmischung zur Messung des Pour points, der Tieftemperaturviskosität und des "Stable Pour Points"Oil mixture for measuring the pour point, the low-temperature viscosity and the "stable pour point"
Das Additive wird, eventuell zusammen mit weiteren Zusatzstoffen, wie DI-Paket und OCP-VI-Verbesserern, bei 50 - 60 Grad Celsius unter Rühren im Grundöl gelöst.The additive, possibly together with other additives such as DI package and OCP-VI improvers, is dissolved in the base oil at 50 - 60 degrees Celsius while stirring.
Die erfindungsgemäßen Additive können den Mineralölen in an sich bekannter Weise zugesetzt werden. Für Stockpunktverbesserer ist erfindungsgemäß ein Zusatz von 0,1 bis 1,0 Gew.-% vorgesehen. Auf die zur Verfügung stehenden Mineralöle wurde bereits vorstehend (vgl. Stand der Technik) eingegangen. Allgemeine Angaben finden sich im Ullmann, Bd. 20, loc.cit., pg. 457-503.The additives according to the invention can be added to the mineral oils in a manner known per se. According to the invention, an addition of 0.1 to 1.0% by weight is provided for pour point improvers. The mineral oils available have already been discussed above (cf. prior art). General information can be found in Ullmann, Vol. 20, loc.cit., Pg. 457-503.
Vorteilhafte Wirkungen der Erfindung liegen in einer verbesserten Wirksamkeit in bestimmten Mineralölen und einem breiteren Wirkungsspektrum in Mineralölen unterschiedlicher Viskosität.Advantageous effects of the invention lie in an improved effectiveness in certain mineral oils and a broader spectrum of activity in mineral oils of different viscosity.
Ölformulierungen, die die erfindungsgemäßen Additive enthalten, zeigen neben den erforderlichen Viskositätsdaten bei 100 Grad Celsius sehr günstige Werte für Pour-point und Stable Pour-point sowie ausgezeichnete Viskositätsdaten bei minus 15 Grad Celsius bis minus 40 Grad Celsius.Oil formulations containing the additives according to the invention, in addition to the required viscosity data at 100 degrees Celsius, show very favorable values for pour point and stable pour point as well as excellent viscosity data at minus 15 degrees Celsius to minus 40 degrees Celsius.
Die Charakterisierung kann durch folgende Meßgrößen erfolgen:
In einem 2 l-Vierhalskolben mit Rührer, Thermometer, Rückflußkühler und Dosierleitung wird folgende Mischung vorgelegt:
- 300 g
- Mineralöl (η100 Grad Celsius = 3,9 qmm/s)
- 21,00 g
- Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
- 8,97 g
- Methacrylsäureester eines unverzweigten C16-C18 Alkoholgemisches
- 3,33 g
- Methylmethacrylat
- 0,13 g
- Dodecylmercaptan
- 0,36 g
- tert.-Butylperoctoat
- 420,62 g
- Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
- 179,41 g
- Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
- 66,67 g
- Methylmethacrylat
- 2,67 g
- Dodecylmercaptan
- 2,0 g
- tert.-Butylperoctoat
Gesamtpolymerisationszeit 8 Stunden. Es wird eine klare, viskose Lösung erhalten.The following mixture is placed in a 2 l four-necked flask with stirrer, thermometer, reflux condenser and metering line:
- 300 g
- Mineral oil (η 100 degrees Celsius = 3.9 qmm / s)
- 21.00 g
- Methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
- 8.97 g
- Methacrylic acid ester of an unbranched C16-C18 alcohol mixture
- 3.33 g
- Methyl methacrylate
- 0.13 g
- Dodecyl mercaptan
- 0.36 g
- tert-butyl peroctoate
- 420.62 g
- Methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
- 179.41 g
- Methacrylic acid ester of an unbranched C16-C18 alcohol mixture
- 66.67 g
- Methyl methacrylate
- 2.67 g
- Dodecyl mercaptan
- 2.0 g
- tert-butyl peroctoate
Total polymerization time 8 hours. A clear, viscous solution is obtained.
Polymerisatgehalt = 70 Gew.-%.Polymer content = 70% by weight.
Viskosität (100 Grad Celsius, 70 Gew.-%ig) = 800 qmm/s Zusammensetzung:
- 24 Mol-% a)
- 20 Mol-% b)
- 56 Mol-% c)
- 24 mol% a)
- 20 mol% b)
- 56 mol% c)
- Vorlage:
-
300 g Mineralöl (η100 Grad Celsius = 3,9 qmm/s)
25,8 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
7,5 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
0,13 g Dodecylmercaptan
0,36 g tert.-Butylperoctoat - Zulauf:
-
517,4 g Methacrylsäure eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
149,3 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
2,67 g Dodecylmercaptan
2,0 g tert.-Butylperoctoat
Viskosität (100 Grad Celsius, 70 Gew.-%ig) = 560 qmm/s Zusammensetzung:
- 0 Mol-% a)
- 20 Mol-% b)
- 79 Mol-% c)
- Template:
-
300 g mineral oil (η 100 degrees Celsius = 3.9 qmm / s)
25.8 g of methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
7.5 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
0.13 g dodecyl mercaptan
0.36 g of tert-butyl peroctoate - Intake:
-
517.4 g methacrylic acid of a C12-C15 alcohol mixture with 23% branched alcohols
149.3 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
2.67 g dodecyl mercaptan
2.0 g of tert-butyl peroctoate
Viscosity (100 degrees Celsius, 70% by weight) = 560 qmm / s Composition:
- 0 mol% a)
- 20 mol% b)
- 79 mol% c)
Herstellung wie Additiv A, aber
- Vorlage:
-
360 g Mineralöl (η100 Grad Celsius = 3,9 qmm/s)
18,56 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
4,0 g Methacrylsäureester eines unverzweigten C12-C14-Alkoholgemisches
15,2 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 60 % verzweigten Alkoholen
2,24 g Methylmethacrylat
1,4 g tert.-Butylperoctoat - Zulauf:
-
371,2 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
80,0 g Methacrylsäureester eines unverzweigten C12-C14-Alkoholgemisches
304,0 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 60 % verzweigten Alkoholen
44,8 g Methylmethacrylat
8,0 g tert.-Butylperoctoat
Viskosität (100 Grad Celsius, 70 Gew.-%ig) = 680 qmm/s Zusammensetzung:
- 15 Mol-% a)
- 38 Mol-% b)
- 47 Mol-% c)
- Template:
-
360 g mineral oil (η 100 degrees Celsius = 3.9 qmm / s)
18.56 g methacrylic acid ester of an unbranched C16-C18 alcohol mixture
4.0 g of methacrylic acid ester of an unbranched C12-C14 alcohol mixture
15.2 g of methacrylic acid ester of a C12-C15 alcohol mixture with 60% branched alcohols
2.24 g methyl methacrylate
1.4 g of tert-butyl peroctoate - Intake:
-
371.2 g methacrylic acid ester of an unbranched C16-C18 alcohol mixture
80.0 g methacrylic acid ester of an unbranched C12-C14 alcohol mixture
304.0 g methacrylic acid ester of a C12-C15 alcohol mixture with 60% branched alcohols
44.8 g methyl methacrylate
8.0 g of tert-butyl peroctoate
Viscosity (100 degrees Celsius, 70% by weight) = 680 qmm / s Composition:
- 15 mol% a)
- 38 mol% b)
- 47 mol% c)
Herstellung wie Additiv A, aber
- Vorlage:
-
360 g Mineralöl (η100 Grad Celsius = 3,9 qmm/s)
17,08 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
22,92 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 60 % verzweigten Alkoholen
1,4 g tert.-Butylperoctoat - Zulauf:
-
341,6 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
458,4 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 60 % verzweigten Alkoholen
8,0 g tert.-Butylperoctoat
Viskosität (100 Grad Celsius, 70 Gew.-%ig) = 560 qmm/s Zusammensetzung:
- 0 Mol-% a)
- 38 Mol-% b)
- 62 Mol-% c)
- Template:
-
360 g mineral oil (η 100 degrees Celsius = 3.9 qmm / s)
17.08 g methacrylic acid ester of an unbranched C16-C18 alcohol mixture
22.92 g of methacrylic acid ester of a C12-C15 alcohol mixture with 60% branched alcohols
1.4 g of tert-butyl peroctoate - Intake:
-
341.6 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
458.4 g of methacrylic acid ester of a C12-C15 alcohol mixture with 60% branched alcohols
8.0 g of tert-butyl peroctoate
Viscosity (100 degrees Celsius, 70% by weight) = 560 qmm / s Composition:
- 0 mol% a)
- 38 mol% b)
- 62 mol% c)
Herstellung wie Additiv A, aber
- Vorlage:
-
300 g Mineralöl (η100 Grad Celsius = 3,9 qmm/s)
19,31 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
10,66 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
3,33 g Methylmethacrylat
0,13 g Dodecylmercaptan
0,36 g tert.-Butylperoctoat - Zulauf:
-
386,69 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
213,34 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
66,67 g Methylmethacrylat
2,67 g Dodecylmercaptan
2,00 g tert.-Butylperoctoat
Viskosität (100 Grad Celsius, 70 Gew.-%ig) = 800 qmm/s Zusammensetzung:
- 24 Mol-% a)
- 24 Mol-% b)
- 52 Mol-% c)
- Template:
-
300 g mineral oil (η 100 degrees Celsius = 3.9 qmm / s)
19.31 g methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
10.66 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
3.33 g methyl methacrylate
0.13 g dodecyl mercaptan
0.36 g of tert-butyl peroctoate - Intake:
-
386.69 g of methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
213.34 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
66.67 g methyl methacrylate
2.67 g dodecyl mercaptan
2.00 g of tert-butyl peroctoate
Viscosity (100 degrees Celsius, 70% by weight) = 800 qmm / s Composition:
- 24 mol% a)
- 24 mol% b)
- 52 mol% c)
Herstellung wie Additiv A, aber
- Vorlage:
-
300 g Mineralöl (η100 Grad Celsius = 3,9 qmm/s)
24,08 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
9,22 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
0,13 g Dodecylmercaptan
0,36 g tert.-Butylperoctoat - Zulauf:
-
482,02 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
184,68 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
2,67 g Dodecylmercaptan
2,00 g tert.-Butylperoctoat
Viskosität (100 Grad Celsius, 70 Gew.-%ig) = 560 qmm/s Zusammensetzung:
- 0 Mol-% a)
- 24 Mol-% b)
- 76 Mol-% c)
- Template:
-
300 g mineral oil (η 100 degrees Celsius = 3.9 qmm / s)
24.08 g of methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
9.22 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
0.13 g dodecyl mercaptan
0.36 g of tert-butyl peroctoate - Intake:
-
482.02 g of methacrylic acid ester of a C12-C15 alcohol mixture with 23% branched alcohols
184.68 g of methacrylic acid ester of an unbranched C16-C18 alcohol mixture
2.67 g dodecyl mercaptan
2.00 g of tert-butyl peroctoate
Viscosity (100 degrees Celsius, 70% by weight) = 560 qmm / s Composition:
- 0 mol% a)
- 24 mol% b)
- 76 mol% c)
Herstellung wie Additiv A, aber
- Vorlage:
-
300 g Mineralöl (η100 Grad C = 3,9 qmm/s)
25,8 g Methacrylsäureester eines C12-C15-Alkoholgemisches mit 23 % verzweigten Alkoholen
7,5 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
0,13 g Dodecylmercaptan
0,36 g tert.-Butylperoctoat - Zulauf:
-
517,4 g Methacrylsäure eines C12-C15-Alkoholgemisches mit verzweigten Alkoholen
149,3 g Methacrylsäureester eines unverzweigten C16-C18-Alkoholgemisches
2,67 g Dodecylmercaptan
2,0 g tert.-Butylperoctoat
Viskosität (100 Grad C, 70 Gew.-%ig) = 560 qmm/s Zusammensetzung:
- 0 Mol-% a)
- 20 Mol-% b)
- 79 Mol-% c)
- Template:
-
300 g mineral oil (η 100 degrees C = 3.9 qmm / s)
25.8 g of methacrylic acid ester of a C 12 -C 15 alcohol mixture with 23% branched alcohols
7.5 g of methacrylic acid ester of an unbranched C 16 -C 18 alcohol mixture
0.13 g dodecyl mercaptan
0.36 g of tert-butyl peroctoate - Intake:
-
517.4 g of methacrylic acid of a C 12 -C 15 alcohol mixture with branched alcohols
149.3 g of methacrylic acid ester of an unbranched C 16 -C 18 alcohol mixture
2.67 g dodecyl mercaptan
2.0 g of tert-butyl peroctoate
Viscosity (100 degrees C, 70% by weight) = 560 qmm / s Composition:
- 0 mol% a)
- 20 mol% b)
- 79 mol% c)
Claims (1)
- Use of polymethacrylates P as oil additives, the polymethacrylates P being in the form of random copolymers and synthesised froma) 10 - 30 mol.% of methyl methacrylateb) 10 - 70 mol.% of alkyl methacrylates with unbranched alkyl groups having 16 to 30 carbon atoms in the alkyl group,c) 80 - 0 mol.% of alkyl methacrylates with unbranched alkyl groups having 4 to 15 carbon atoms and/or branched alkyl groups having 4 to 40 carbon atoms in the alkyl group as the monomer component,characterised in that the polyalkyl methacrylates P are used in amounts between 0.05 and 1 wt.% as pour point improving agent in mineral oils, with the proviso that the monomer component b) comprises several alkyl methacrylates which are different from one another.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3607444 | 1986-03-07 | ||
DE19863607444 DE3607444A1 (en) | 1986-03-07 | 1986-03-07 | ADDITIVES FOR MINERAL OILS WITH IMPROVEMENT EFFECT |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0236844A2 EP0236844A2 (en) | 1987-09-16 |
EP0236844A3 EP0236844A3 (en) | 1988-03-30 |
EP0236844B1 true EP0236844B1 (en) | 1997-09-24 |
Family
ID=6295696
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP87102629A Expired - Lifetime EP0236844B1 (en) | 1986-03-07 | 1987-02-24 | Use of additives for mineral oils with modified pour- point characteristics |
Country Status (4)
Country | Link |
---|---|
US (1) | US4867894A (en) |
EP (1) | EP0236844B1 (en) |
JP (1) | JPS62212497A (en) |
DE (2) | DE3607444A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5955405A (en) * | 1998-08-10 | 1999-09-21 | Ethyl Corporation | (Meth) acrylate copolymers having excellent low temperature properties |
US6255261B1 (en) | 1999-09-22 | 2001-07-03 | Ethyl Corporation | (Meth) acrylate copolymer pour point depressants |
Families Citing this family (49)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3613992C2 (en) * | 1986-04-25 | 2000-05-04 | Roehm Gmbh | Additives for paraffinic lubricating oils |
FR2600071B1 (en) * | 1986-06-13 | 1988-08-26 | Inst Francais Du Petrole | COPOLYMER COMPOSITIONS FOR USE IN PARTICULAR AS ADDITIVES FOR HYDROCARBON OILS |
DE3818438A1 (en) * | 1988-05-31 | 1989-12-07 | Roehm Gmbh | MINERAL OIL WITH IMPROVED FLOW BEHAVIOR |
US5349019A (en) * | 1988-12-24 | 1994-09-20 | Hoechst | New copolymers, mixtures thereof with poly(meth)acrylate esters and the use thereof for improving the cold fluidity of crude oils |
DE3930142A1 (en) * | 1989-09-09 | 1991-03-21 | Roehm Gmbh | DISPERGING VISCOSITY INDEX IMPROVERS |
DE4000753A1 (en) * | 1990-01-12 | 1991-07-18 | Roehm Gmbh | POWER TRANSFER FLUID BASED ON MINERAL OIL |
DE4312715A1 (en) * | 1993-04-20 | 1994-10-27 | Roehm Gmbh | Comb polymers |
US5312884A (en) * | 1993-04-30 | 1994-05-17 | Rohm And Haas Company | Copolymer useful as a pour point depressant for a lubricating oil |
JP2748104B2 (en) * | 1994-03-08 | 1998-05-06 | 三洋化成工業株式会社 | Viscosity index improver and lubricating oil |
US5665685A (en) * | 1994-06-02 | 1997-09-09 | Sanyo Chemical Industries, Ltd. | Gear and transmission lubricant compositions of improved sludge-dispersibility, fluids comprising the same |
IT1270673B (en) * | 1994-10-19 | 1997-05-07 | Euron Spa | MULTIFUNCTIONAL ADDITIVE FOR LUBRICANTS COMPATIBLE WITH FLUOROELASTOMERS |
DE19518786A1 (en) * | 1995-05-22 | 1996-11-28 | Roehm Gmbh | Lubricant additives |
US5821313A (en) | 1995-06-19 | 1998-10-13 | The Lubrizol Corporation | Dispersant-viscosity improvers for lubricating oil compositions |
US5969068A (en) | 1995-06-19 | 1999-10-19 | The Lubrizol Corporation | Dispersant-viscosity improvers for lubricating oil compositions |
BR9811959B1 (en) | 1997-08-22 | 2010-03-09 | A method for improving the low temperature flowability of lubricating oils by using mixtures of high and low molecular weight polymer additives, lubricating oil and concentrate compositions for use in said compositions. | |
US5834408A (en) * | 1997-10-24 | 1998-11-10 | Ethyl Corporation | Pour point depressants via anionic polymerization of (meth)acrylic monomers |
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FR2982871A1 (en) | 2011-11-22 | 2013-05-24 | Univ Sud Toulon Var | POLY (N-ALKYL ACRYLATE) POLYMERS AND THEIR USE AS OIL FLOW POINT SIZERS |
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JP2023554452A (en) | 2020-12-18 | 2023-12-27 | エボニック オペレーションズ ゲーエムベーハー | Method for producing homopolymers and copolymers of alkyl (meth)acrylates with low residual monomer content |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2114233A (en) * | 1933-05-22 | 1938-04-12 | Rohm & Haas | Polymeric materials |
US2091627A (en) * | 1934-06-08 | 1937-08-31 | Rohm & Haas | Composition of matter and process |
US2100993A (en) * | 1934-12-14 | 1937-11-30 | Rohm & Haas | Process for preparing esters and products |
BE581079A (en) * | 1958-07-28 | |||
US3238133A (en) * | 1962-07-30 | 1966-03-01 | Shell Oil Co | Lubricating oil compositions containing neutral ashless polymeric detergents |
BE636998A (en) * | 1962-11-14 | 1900-01-01 | ||
US3397146A (en) * | 1966-08-22 | 1968-08-13 | Union Carbide Corp | Lubricating compositions |
US3697644A (en) * | 1966-10-18 | 1972-10-10 | Gillette Co | Cosmetic composition |
US3475321A (en) * | 1966-11-14 | 1969-10-28 | Exxon Research Engineering Co | Solvent dewaxing with a synergistic wax crystal modifier composition |
GB1163807A (en) * | 1967-08-30 | 1969-09-10 | Shell Int Research | Polyalkyl Methacrylates suitable as Luboil Additives |
US3878180A (en) * | 1970-12-14 | 1975-04-15 | Texaco Inc | Polymerization of acrylic acid esters |
DE2102469C2 (en) * | 1971-01-20 | 1989-06-29 | Basf Ag, 6700 Ludwigshafen | Use of ethylene copolymers as an additive to petroleum and petroleum fractions |
GB1347713A (en) * | 1971-05-05 | 1974-02-27 | Shell Int Research | Alkyl methacrylate polymer compositions suitable as luboil additives |
US3904385A (en) * | 1972-05-08 | 1975-09-09 | Texaco Inc | Polyacrylates and waxy residual fuel compositions thereof |
CA1071865A (en) * | 1975-03-28 | 1980-02-19 | Max J. Wisotsky | Polymer combinations useful in distillate hydrocarbon oils to improve cold flow properties |
US4146492A (en) * | 1976-04-02 | 1979-03-27 | Texaco Inc. | Lubricant compositions which exhibit low degree of haze and methods of preparing same |
US4045376A (en) * | 1976-04-23 | 1977-08-30 | Texaco Inc. | Synthetic turbine oils |
US4123368A (en) * | 1977-03-24 | 1978-10-31 | Rohm And Haas Company | Alkaline earth metal salt dispersions in acrylic polymers |
GB1559952A (en) * | 1977-10-26 | 1980-01-30 | Shell Int Research | Lubricating oil compositions |
US4229311A (en) * | 1979-07-18 | 1980-10-21 | Rohm Gmbh | Lubricating oil additives |
FR2497822A1 (en) * | 1981-01-12 | 1982-07-16 | Organo Synthese Ste Fse | ADDITIVES FOR LUBRICATING OILS BASED ON STYRENE AND C12-C20 ALKYL HEAVY METHACRYLATES, MANUFACTURING METHOD AND APPLICATIONS |
US4533482A (en) * | 1982-12-30 | 1985-08-06 | Rohm And Haas Company | Hydrogenated diolefin-lower alkyl acrylate or methacrylate viscosity index improving copolymers for lubricating oils |
DE3317396A1 (en) * | 1983-05-13 | 1984-11-15 | Henkel KGaA, 4000 Düsseldorf | USE OF COLOYERS FROM ESTERS AND AMIDES OF ACRYLIC AND / OR METHACRYLIC ACIDS AS STOCK POINTS LOW FOR PARAFFIN SOLUTIONS |
DE3339103A1 (en) * | 1983-10-28 | 1985-05-09 | Röhm GmbH, 6100 Darmstadt | ADDITIVES FOR LUBRICANTS |
DE3544061A1 (en) * | 1985-12-13 | 1987-06-19 | Roehm Gmbh | HIGHLY STABLE MULTI-RANGE LUBRICANTS WITH IMPROVED VISCOSITY INDEX |
-
1986
- 1986-03-07 DE DE19863607444 patent/DE3607444A1/en not_active Ceased
-
1987
- 1987-02-24 DE DE3752119T patent/DE3752119D1/en not_active Expired - Lifetime
- 1987-02-24 EP EP87102629A patent/EP0236844B1/en not_active Expired - Lifetime
- 1987-03-03 JP JP62046935A patent/JPS62212497A/en active Pending
-
1988
- 1988-04-20 US US07/185,317 patent/US4867894A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5955405A (en) * | 1998-08-10 | 1999-09-21 | Ethyl Corporation | (Meth) acrylate copolymers having excellent low temperature properties |
US6255261B1 (en) | 1999-09-22 | 2001-07-03 | Ethyl Corporation | (Meth) acrylate copolymer pour point depressants |
Also Published As
Publication number | Publication date |
---|---|
US4867894A (en) | 1989-09-19 |
EP0236844A2 (en) | 1987-09-16 |
DE3607444A1 (en) | 1987-09-10 |
EP0236844A3 (en) | 1988-03-30 |
JPS62212497A (en) | 1987-09-18 |
DE3752119D1 (en) | 1997-10-30 |
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