EP0332000B1 - Use of selected acrylic and/or methacrylic acid ester copolymer versions as flow enhancers in paraffin-rich mineral oils and mineral-oil fractions (I) - Google Patents
Use of selected acrylic and/or methacrylic acid ester copolymer versions as flow enhancers in paraffin-rich mineral oils and mineral-oil fractions (I) Download PDFInfo
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- EP0332000B1 EP0332000B1 EP89103383A EP89103383A EP0332000B1 EP 0332000 B1 EP0332000 B1 EP 0332000B1 EP 89103383 A EP89103383 A EP 89103383A EP 89103383 A EP89103383 A EP 89103383A EP 0332000 B1 EP0332000 B1 EP 0332000B1
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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
- C10L1/18—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
- C10L1/1966—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 poly-carboxylic
Definitions
- auxiliaries which are also referred to as paraffin inhibitors are and are usually prepared by polymerizing olefinically unsaturated compounds which contain at least partially unbranched saturated hydrocarbon chains with at least 18 carbon atoms.
- DE-PS 30 31 900 describes copolymers of n-alkyl acrylates with at least 16 carbon atoms in the alcohol residue and maleic anhydride with molar ratios of n-alkyl acrylate to maleic anhydride from 20: 1 to 1:10. Compounds of this type are said to be used as crystallization inhibitors for paraffin-containing crude oils. Examples shown numerically relate to the use of corresponding copolymers in the molar ratio of the acrylic acid ester to maleic anhydride in the range from 1: 1 to 8: 1. Crude oils with intrinsic pour points below 20 ° C. are predominantly used.
- a table of values deals with India crude oil, which is known to be a particularly paraffin-rich starting material (disruptive paraffin content 15%) and has its own pour point of 33 ° C.
- the optimum effectiveness of the copolymers used in this publication with regard to lowering the pour point on this starting material is at the molar ratio of acrylic acid ester / maleic anhydride of 4: 1.
- the lowest pour points set here are at 12 ° C. If the proportion of maleic anhydride in the copolymer is further reduced, then the pour points of the India crude oil thus added rise again with the addition of the same amount (cf. in particular Table 2 of the cited literature reference).
- Comparative Example 5 of this publication describes a binary copolymer of n-alkyl acrylate with an average chain length C 20 to C 22 and maleic anhydride with a MAH content of 1.9% in the polymer molecule.
- the use of the flow improver of Comparative Example 5 in crude oils with their own pour points above 25 ° C does not lead to a reduction in the pour points to values below 15 ° C in any of the cases shown in the publication.
- the teaching of the present invention is based on the surprising finding that a particularly effective lowering of the solidification temperatures determines According to the known methods of pour point and / or pour point determination - with starting materials with a high paraffin content and correspondingly particularly high self-solidification temperatures can be effectively obtained if selected types of copolymers of the type described below are used as flow aids. It has surprisingly been found that selected copolymers with extremely low maleic anhydride contents can be particularly suitable for effectively lowering the limit temperatures of the flowability of crude oils containing high paraffin or corresponding petroleum fractions.
- the invention accordingly relates to the use of copolymers consisting of acrylic and / or methacrylic acid esters of higher alcohols or alcohol cuts with at least 16 carbon atoms in the alcohol residue, the content of C 22 - and optionally higher alcohols - based on that for the preparation of the acrylate or methacrylate components used alcohol mixture - is at least 45 wt .-%, and not more than 5 wt .-%, preferably 0.5 to 2.5 wt .-% maleic anhydride - wt .-% based on copolymer weight - as a flow improver in paraffin-rich crude oils and / or petroleum fractions with their own pour points above 25 ° C to lower their pour points to values below 15 ° C, preferably below 10 ° C.
- Copolymers of the type mentioned whose content of maleic anhydride is in the range from approximately 0.5 to 2.5% by weight and in particular in the range from approximately 1 to 2% by weight are particularly suitable for the inventive action.
- the percentages by weight relate to the proportion of total monomer.
- the pour point improvers in the sense of Invention it is possible, for example, by adding conventional amounts of the pour point improvers in the sense of Invention to come to pour points of the extremely paraffin-rich starting materials in the range of about 0 to 8 ° C. This ensures trouble-free handling of these crude oils and oil fractions under normal everyday conditions. In particular, it is ensured that lines, distributors and the like which are guided under water can be operated without problems.
- copolymers containing maleic anhydride based on the esters of acrylic acid are particularly suitable for teaching the invention.
- the further particularly preferred acrylic acid esters contain comparatively long-chain alcohol residues, which can be at least predominantly n-alkyl residues and have preferred chain lengths in the range from C 18 to C 24 .
- Proportions of alcohols with a higher carbon number, in particular up to about C 30 and / or alcohols with a lower carbon number up to about C 16 can also be used.
- the dissolution behavior of the copolymers in customary solvents, for example toluene and the like is promoted by the use of appropriate alcohol cuts in the production of the acrylic acid esters and their subsequent copolymerization with maleic anhydride.
- the application concentration of the pour point improvers according to the invention is in the conventional range and is, for example, 20 to 1000 ppm, with amounts in the range from 100 to 500 ppm being preferred.
- the pour point improvers are expediently used in suitable solvents. Details on this and on the preparation of the copolymers can be found in the relevant prior art, for example in DE-PS 30 31 900 already cited.
- the alcohols or alcohol cuts used for the production of the acrylate components can be of native or synthetic origin. Alcohol cuts with a predominant proportion of components with at least 22 carbon atoms, but at the same time also minor amounts of alcohol components in the range C 16 to C 20 , are the preferred starting materials.
- acrylates or methacrylates selected in this way are copolymerized with maleic anhydride in such mixing ratios that the molar ratio of alkyl acrylate or methacrylate to maleic anhydride is greater than 20: 1.
- the two acrylate ester mixtures A and B are used to prepare the maleic anhydride copolymers Distinguish by the C chain distribution of the fatty alcohol mixture used for the acrylic acid esterification.
- the two types of acrylate are characterized as follows: Table 1 C chain distribution of fatty alcohol /% C 16 C 18 C 20 C 22 Acrylate A 16.3 22.9 10.7 46.9 Acrylate B 1.5 8.6 15.2 68.8
- the monomers, initiator and solvent are weighed into a three-necked flask.
- the batch is evacuated for 10 ⁇ 1 min and the vacuum is released again with 99.999% nitrogen.
- the batch is heated to 90 ° C. and kept at this temperature.
- the entire reaction is carried out under inert conditions.
- the start of the reaction manifests itself in a temperature rise to 93 to 96 ° C.
- the mixture is kept at 90 ° C ⁇ 1 ° C for 3 h. After this time, the mixture is cooled to room temperature within 45 minutes and the product is filled.
- Toluene is used as the solvent here and in the subsequent feed process.
- the polymerization initiator used is dibenzoyl peroxide or azoisobutyronitrile as indicated below.
- the mixing ratio of solvent to monomer mixture is 1: 1 (parts by weight).
- the monomers are dissolved in toluene in the desired mixing ratio at 45 to 50 ° C. and the solution is then cooled to 25 ° C.
- the initiator is also used in solution in toluene. About 20% of the monomer solution determined per batch is placed in a reactor. The reactor is flushed three times with nitrogen and heated to 90 ° C. while stirring under a gentle stream of N 2 . The initiator solution is now metered in so that the total metering time is 2.5 hours.
- a temperature increase occurs 20 minutes after the initiator has been added.
- the temperature is kept at 90 ⁇ 3 ° C by cooling the reactor jacket.
- the remaining monomer solution is metered into the reactor in such a way that the total metering time is 2 h.
- the temperature is kept at 90 ⁇ 3 ° C throughout the reaction time.
- the reaction mixture is then kept at the same temperature for a further 60 min.
- the reaction product is then cooled and filled at 30 ° C.
- Examples 1 to 10 according to the invention are summarized in Table 2 below.
- the type of acrylate monomers A or B used is used in the respective example assigned and the percentage (wt .-%) of maleic anhydride in the monomer mixture for the preparation of the pour point depressant stated.
- the flow improver was produced by the batch process and in Examples 3 to 10 by the feed process.
- Table 2 finally shows the specific viscosity of the copolymer solutions prepared in each case.
- the viscosity is measured using an Ubbelohde viscometer capillary I, ⁇ 0.63 mm.
- the measured toluene solutions are 3% solutions in toluene. The measurement is carried out at 20 ° C after a temperature adjustment of 10 min.
- Table 2 contains the pour point values which were obtained when the pour point improvers according to the invention were added to an India crude (Bombay crude oil) in accordance with the following working instructions.
- the pour point was determined in accordance with ASTM D 97-66 and DIN 51597 as follows:
- the pour point of the untreated Bombay crude oil is 30 ° C according to this determination method.
- Table 2 E.g. Acrylic type % By weight of MAH in the copolymer Specific viscosity Pour point in Bombay crude oil (° C) 1 A 1.25 0.657 6 2nd A 5 1.17 9 3rd A 0.25 0.56 12th 4th A 0.5 0.65 12-15 5 A 1.25 0.65 6 6 B 1.25 0.64 3rd 7 A 1.25 0.37 9 8th A 2.5 0.83 9 9 A 2.5 0.61 9 10th B 5 0.52 12th
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Description
Es ist bekannt, die Fließeigenschaften von Rohölen und/oder Erdölfraktionen durch Mitverwendung beschränkter Mengen synthetischer Fließhilfsmittel zu verbessern. Aufgabe dieser Fließhilfsmittel ist bekanntlich die Absenkung der jeweiligen Temperatur unterhalb derer im flüssigen Kohlenwasserstoffgemisch Festbestandteile - insbesondere höhere Paraffine gegebenenfalls in Kombination mit Asphaltenen oder anderen schwer löslichen Bestandteilen - in solchen Mengen auskristallisieren, daß die Fließfähigkeit der Kohlenwasserstoffgemische nachhaltig beeinträchtigt wird. Der hier angesprochene Temperaturbereich wird durch die bekannten Methoden der Bestimmung von Fließpunkt bzw. Stockpunkt ermittelt. Jedem Rohöl bzw. den daraus gewonnenen Erdölfraktionen kommt aufgrund seiner spezifischen Zusammensetzung ein Eigenfließpunkt zu, der bei vielen Rohölen jedoch so niedrig liegt, daß keine Beeinträchtigung bei der Förderung und beim Pipelinetransport eintritt. Es gibt aber auch eine ganze Reihe von Erdölqualitäten, deren Stockpunkt oberhalb von 10 °C liegt. Schon hier kann für die Praxis die Mitverwendung von Fließhilfsmitteln auf Basis unterschiedlicher synthetischer Homopolymer- und/oder Copolymertypen ratsam sein.It is known to improve the flow properties of crude oils and / or petroleum fractions by using limited amounts of synthetic flow aids. As is known, the task of these flow aids is to lower the respective temperature below those in the liquid hydrocarbon mixture of solid constituents - in particular higher paraffins, if appropriate in combination with asphaltenes or other poorly soluble constituents - in such amounts that the flowability of the hydrocarbon mixtures is permanently impaired. The temperature range mentioned here is determined by the known methods of determining the pour point or pour point. Due to its specific composition, each crude oil or the petroleum fractions obtained from it has its own pour point, which, however, is so low for many crude oils that there is no impairment in production and pipeline transport. But there is also a whole range of petroleum qualities with a pour point above 10 ° C. In practice, the use of flow aids based on different synthetic homopolymer and / or copolymer types can be advisable.
Es besteht ein umfangreicher Stand der Technik zu solchen Hilfsmitteln, die auch als Paraffininhibitoren bezeichnet werden und in der Regel durch Polymerisation von olefinisch ungesättigten Verbindungen, die wenigstens anteilweise unverzweigte gesättigte Kohlenwasserstoffketten mit mindestens 18 C-Atomen enthalten, hergestellt werden. Verwiesen wird beispielsweise auf die DE-AS 22 10 431 sowie die DE-OSen 26 12 757, 22 64 328, 20 62 023, 23 30 232, 19 42 504 und 20 47 448.There is extensive prior art for such auxiliaries, which are also referred to as paraffin inhibitors are and are usually prepared by polymerizing olefinically unsaturated compounds which contain at least partially unbranched saturated hydrocarbon chains with at least 18 carbon atoms. Reference is made, for example, to DE-AS 22 10 431 and DE-OSs 26 12 757, 22 64 328, 20 62 023, 23 30 232, 19 42 504 and 20 47 448.
Besondere Schwierigkeiten treten für die Praxis dann auf, wenn der Eigenfließpunkt des Rohöls bzw. der zu bearbeitenden Erdölfraktion extrem hohe Werte erreicht, die insbesondere wenigstens 25 °C ausmachen und dabei bei 30 °C und darüber liegen können. Erdölmaterialien dieser Art neigen schon bei Umgebungstemperatur zu rascher Verfestigung. Werden beispielsweise Pumpvorgänge auch nur kurzfristig unterbrochen oder werden im Transport Temperaturbereiche - beispielsweise durch Leitungen im Meerwasserbereich - mit verhältinsmäßig niedrigen Temperaturen durchschritten, so tritt die rasche Verfestigung des Kohlenwasserstoffguts zu einer nicht mehr pumpfähigen Masse und damit die Blockade von Leitungen, Pumpen und dergleichen ein. Erschwert wird der Sachverhalt dadurch, daß zum sicheren Ausschluß von Störungen der geschilderten Art von der Praxis häufig gefordert wird, die Fließpunkte der Öle bzw. Ölfraktionen auf Werte unterhalb 15 °C und insbesondere auf Werte unter 12 °C oder gar unter 10 °C abzusenken. Es leuchtet sofort ein, daß technologische Schwierigkeiten ganz besonderer Art dann vorliegen, wenn es beispielsweise gilt, einen Eigenfließpunkt des Rohöls von etwa 33 °C auf Werte deutlich unterhalb 10 °C abzusenken. Als zusätzliche Schwierigkeit ist dabei zu berücksichtigen, daß die einfache Erhöhung der Zusatzmenge beliebiger Fließpunktsverbesserer im allgemeinen nicht zu entsprechend erhöhter Abnahme des Fließpunktes führt. Im einzelnen nicht aufgeklärte Interaktionen zwischen Fließhilfsmittel und den sich verfestigenden Bestandteilen des Rohöls sind wohl etwa im Sinne eines Thresh-hold-Effektes für das angestrebte Ziel verantwortlich zu machen, wobei der bestimmten Konstitution des Fließhilfsmittels entscheidende Bedeutung für seine Wirksamkeit zukommt.In practice, particular difficulties arise when the intrinsic pour point of the crude oil or the petroleum fraction to be processed reaches extremely high values, which in particular can be at least 25 ° C and can be 30 ° C and above. Petroleum materials of this type tend to solidify rapidly even at ambient temperature. If, for example, pumping processes are interrupted even for a short time or if temperature ranges - for example through pipes in the seawater area - are crossed with relatively low temperatures, the rapid solidification of the hydrocarbon material to a mass that is no longer pumpable and thus blockage of pipes, pumps and the like. The situation is made more difficult by the fact that, in order to reliably rule out malfunctions of the type described, practice is often required to lower the pour points of the oils or oil fractions to values below 15 ° C and in particular to values below 12 ° C or even below 10 ° C . It is immediately apparent that there are very special technological difficulties when, for example, it is necessary to lower the crude oil's own pour point from around 33 ° C to values well below 10 ° C. An additional difficulty to be taken into account here is that simply increasing the amount of any pour point improver generally does not lead to a correspondingly increased decrease in the pour point. Interactions between flow aids and the solidifying that have not yet been elucidated Components of the crude oil are probably responsible for the desired goal in the sense of a thresh-hold effect, with the specific constitution of the flow aid being of decisive importance for its effectiveness.
In der DE-PS 30 31 900 werden Mischpolymerisate aus n-Alkylacrylaten mit mindestens 16 C-Atomen im Alkoholrest und Maleinsäureanhydrid mit Molverhältnissen von n-Alkylacrylat zu Maleinsäureanhydrid von 20 : 1 bis 1 : 10 beschrieben. Verbindungen dieser Art sollen als Kristallisationsinhibitoren für paraffinhaltige Rohöle eingesetzt werden. Zahlenmäßig dargestellte Beispiele betreffen die Verwendung entsprechender Copolymere im Molverhältnis des Acrylsäureesters zum Maleinsäureanhydrid im Bereich von 1 : 1 bis 8 : 1. Überwiegend werden dabei Rohöle mit Eigenstockpunkten unterhalb 20 °C eingesetzt. Eine Wertetabelle beschäftigt sich mit dem India-Rohöl, das bekanntlich ein besonders paraffinreiches Ausgangsmaterial ist (störender Paraffingehalt 15 %) und einen Eigenstockpunkt von 33 °C besitzt. Die optimale Wirksamkeit der in dieser Druckschrift verwendeten Mischpolymerisate bezüglich der Stockpunkterniedrigung an diesem Ausgangsmaterial liegt beim Molverhältnis Acrylsäureester/Maleinsäureanhydrid von 4 : 1. Die niedrigsten hier eingestellten Stockpunkte liegen bei 12 °C. Wird der Maleinsäureanhydrid-Anteil im Copolymerisat weiter abgesenkt, dann steigen die Stockpunkte des damit versetzten India-Rohöls bei mengengleicher Zugabe wieder an (vgl. hierzu insbesondere die Tabelle 2 der genannten Literaturstelle).DE-PS 30 31 900 describes copolymers of n-alkyl acrylates with at least 16 carbon atoms in the alcohol residue and maleic anhydride with molar ratios of n-alkyl acrylate to maleic anhydride from 20: 1 to 1:10. Compounds of this type are said to be used as crystallization inhibitors for paraffin-containing crude oils. Examples shown numerically relate to the use of corresponding copolymers in the molar ratio of the acrylic acid ester to maleic anhydride in the range from 1: 1 to 8: 1. Crude oils with intrinsic pour points below 20 ° C. are predominantly used. A table of values deals with India crude oil, which is known to be a particularly paraffin-rich starting material (disruptive paraffin content 15%) and has its own pour point of 33 ° C. The optimum effectiveness of the copolymers used in this publication with regard to lowering the pour point on this starting material is at the molar ratio of acrylic acid ester / maleic anhydride of 4: 1. The lowest pour points set here are at 12 ° C. If the proportion of maleic anhydride in the copolymer is further reduced, then the pour points of the India crude oil thus added rise again with the addition of the same amount (cf. in particular Table 2 of the cited literature reference).
Ausgehend von den Problemen insbesondere bei der Herstellung von Inhibitoren der zuletzt geschilderten Art mit höheren Gehalten an Dicarbonsäure-Resten im Polymermolekül will die Lehre der GB 2 160 536 verbesserte Kristallisationsinhibitoren durch den Aufbau ternärer Copolymerisate zur Verfügung stellen. Zum Aufbau des Polymermoleküls wird hier vorgeschlagen, als dritte Monomerkomponente ethylenisch ungesättigte Verbindungen der Formel CH2= CZ1Z2 mitzuverwenden, wobei die Reste Z1 und Z2 gleich oder verschieden sind und für Wasserstoff, Halogen, gesättigte, ungesättigte oder aromatische C1-30-Kohlenwasserstoffreste, Esterreste oder Etherreste stehen. Das Vergleichsbeispiel 5 dieser Druckschrift beschreibt ein binäres Copolymer aus n-Alkylacrylat einer mittleren Kettenlänge C20 bis C22 und Maleinsäureanhydrid mit einem MAH-Gehalt von 1,9% im Polymermolekül. Der Einsatz des Fließverbesserers des Vergleichsbeispiels 5 in Rohölen mit Eigenfließpunkten oberhalb 25°C führt in keinem der in der Druckschrift aufgezeigten Fälle zu einer Absenkung der Fließpunkte auf Werte unterhalb 15°C.Starting from the problems, in particular in the production of inhibitors of the type described above, with higher contents of dicarboxylic acid residues in the polymer molecule, the teaching of GB 2 160 536 aims to provide improved crystallization inhibitors by building up ternary copolymers. To build up the polymer molecule, it is proposed here to use, as the third monomer component, ethylenically unsaturated compounds of the formula CH 2 = CZ 1 Z 2 , where the radicals Z 1 and Z 2 are the same or different and are hydrogen, halogen, saturated, unsaturated or aromatic C 1 -30- hydrocarbon residues, ester residues or ether residues. Comparative Example 5 of this publication describes a binary copolymer of n-alkyl acrylate with an average chain length C 20 to C 22 and maleic anhydride with a MAH content of 1.9% in the polymer molecule. The use of the flow improver of Comparative Example 5 in crude oils with their own pour points above 25 ° C does not lead to a reduction in the pour points to values below 15 ° C in any of the cases shown in the publication.
Die Lehre der vorliegenden Erfindung geht demgegenüber von der überraschenden Erkenntnis aus, daß eine besonders wirkungsvolle Absenkung der Verfestigungstemperaturen - bestimmt nach den bekannten Methoden der Fließpunkt- und/oder Stockpunktermittlung - bei Ausgangsmaterialien hohen Paraffingehalts und dementsprechend besonders hoher Eigen-Verfestigungstemperaturen gerade dann wirkungsvoll erhalten werden kann, wenn ausgewählte Copolymertypen der nachfolgend geschilderten Art als Fließhilfsmittel eingesetzt werden. Es hat sich überraschenderweise gezeigt, daß ausgewählte Copolymerisate mit extrem geringen Maleinsäureanhydrid-Gehalten besonders geeignet sein können, gerade wirkungsvoll die Grenztemperaturen der Fließfähigkeit hochparaffinhaltiger Rohöle bzw. entsprechender Erdölfraktionen abzusenken.In contrast, the teaching of the present invention is based on the surprising finding that a particularly effective lowering of the solidification temperatures determines According to the known methods of pour point and / or pour point determination - with starting materials with a high paraffin content and correspondingly particularly high self-solidification temperatures can be effectively obtained if selected types of copolymers of the type described below are used as flow aids. It has surprisingly been found that selected copolymers with extremely low maleic anhydride contents can be particularly suitable for effectively lowering the limit temperatures of the flowability of crude oils containing high paraffin or corresponding petroleum fractions.
Gegenstand der Erfindung ist dementsprechend die Verwendung von Copolymeren bestehend aus Acryl- und/oder Methacrylsäureestern höherer Alkohole bzw. Alkoholschnitte mit wenigstens 16 C-Atomen im Alkoholrest, deren Gehalt an C22- und gegebenenfalls höheren Alkoholen - bezogen auf das zur Herstellung der Acrylat- bzw. Methacrylatkomponenten eingesetzte Alkoholgemisch - wenigstens 45 Gew.-% beträgt, und nicht mehr als 5 Gew.-%, bevorzugt 0,5 bis 2,5 Gew.-% Maleinsäureanhydrid - Gew.-% hier bezogen auf Copolymergewicht - als Fließverbesserer in paraffinreichen Rohölen und/oder Erdölfraktionen mit Eigenfließpunkten oberhalb 25°C zur Absenkung deren Fließpunkte auf Werte unterhalb 15°C, bevorzugt unter 10°C.The invention accordingly relates to the use of copolymers consisting of acrylic and / or methacrylic acid esters of higher alcohols or alcohol cuts with at least 16 carbon atoms in the alcohol residue, the content of C 22 - and optionally higher alcohols - based on that for the preparation of the acrylate or methacrylate components used alcohol mixture - is at least 45 wt .-%, and not more than 5 wt .-%, preferably 0.5 to 2.5 wt .-% maleic anhydride - wt .-% based on copolymer weight - as a flow improver in paraffin-rich crude oils and / or petroleum fractions with their own pour points above 25 ° C to lower their pour points to values below 15 ° C, preferably below 10 ° C.
Besonders geeignet sind für das erfindungsgemäße Handeln Copolymere der genannten Art, deren Gehalt an Maleinsäureanhydrid im Bereich von etwa 0,5 bis 2,5 Gew.-% und insbesondere im Bereich von etwa 1 bis 2 Gew.-% liegt. Auch hier beziehen sich die Angaben zu Gew.-% jeweils auf den Anteil am Gesamtmonomer. Es ist Bestandteil der erfindungsgemäßen Lehre, die Fließpunkte der eingesetzten Rohöle und/oder Erdölfraktionen mit ihren Ausgangs- bzw. Eigenfließpunkten oberhalb 25°C und insbesondere oberhalb 30°C durch den Zusatz der erfindungsgemäß definierten Fließverbesserer auf Werte unterhalb 15°C und bevorzugt unter 10°C einzustellen. Erfindungsgemäß wird es beispielsweise möglich, durch Zugabe konventioneller Mengen der Fließpunktverbesserer im Sinne der Erfindung auf Fließpunkte der extrem paraffinreichen Ausgangsmaterialien im Bereich von etwa 0 bis 8°C zu kommen. Damit ist die störungsfreie Handhabung auch dieser Rohöle bzw. Ölfraktionen unter den normalen Alltagsbedingungen gewährleistet. Insbesondere ist sichergestellt, daß unter Wasser geführte Leitungen, Verteiler und dergleichen störungsfrei betrieben werden können.Copolymers of the type mentioned whose content of maleic anhydride is in the range from approximately 0.5 to 2.5% by weight and in particular in the range from approximately 1 to 2% by weight are particularly suitable for the inventive action. Here, too, the percentages by weight relate to the proportion of total monomer. It is part of the teaching according to the invention that the pour points of the crude oils and / or petroleum fractions used with their starting or intrinsic pour points above 25 ° C. and in particular above 30 ° C. by adding the flow improvers defined according to the invention to values below 15 ° C. and preferably below 10 ° C. According to the invention it is possible, for example, by adding conventional amounts of the pour point improvers in the sense of Invention to come to pour points of the extremely paraffin-rich starting materials in the range of about 0 to 8 ° C. This ensures trouble-free handling of these crude oils and oil fractions under normal everyday conditions. In particular, it is ensured that lines, distributors and the like which are guided under water can be operated without problems.
Besonders geeignet sind für die Lehre der Erfindung geringe Mengen an Maleinsäureanhydrid enthaltende Copolymere auf Basis der Ester von Acrylsäure. Die weiterhin besonders bevorzugten Acrylsäurester enthalten vergleichsweise langkettige Alkoholreste, die wenigstens überwiegend n-Alkylreste sein können und bevorzugte Kettenlängen im Bereich von C18 bis C24 aufweisen. Anteilsweise können Alkohole mit höherer Kohlenstoffzahl, insbesondere bis etwa C30 und/oder Alkohole mit niedrigerer Kohlenstoffzahl bis etwa C16, mitverwendet werden. Insbesondere das Lösungsverhalten der Copolymerisate in üblichen Lösungsmitteln, beispielsweise Toluol und dergleichen, wird durch den Einsatz von entsprechenden Alkoholschnitten bei der Herstellung der Acrylsäureester und deren nachfolgende Copolymerisation mit Maleinsäureanhydrid gefördert.Small quantities of copolymers containing maleic anhydride based on the esters of acrylic acid are particularly suitable for teaching the invention. The further particularly preferred acrylic acid esters contain comparatively long-chain alcohol residues, which can be at least predominantly n-alkyl residues and have preferred chain lengths in the range from C 18 to C 24 . Proportions of alcohols with a higher carbon number, in particular up to about C 30 and / or alcohols with a lower carbon number up to about C 16 , can also be used. In particular, the dissolution behavior of the copolymers in customary solvents, for example toluene and the like, is promoted by the use of appropriate alcohol cuts in the production of the acrylic acid esters and their subsequent copolymerization with maleic anhydride.
Es hat sich weiterhin gezeigt, daß bei der Mitverwendung von nur geringen Mengen an Maleinsäureanhydrid als Comonomeres im Sinne der erfindungsgemäßen Lehre in den Fließpunktverbesserern dann besonders wirkungsvolle Copolymere erhalten werden, wenn vergleichsweise hohe Gehalte an Alkoholresten mit wenigstens 22 C-Atomen in der Acrylat- bzw. Methacrylatkomponente vorliegen. So sieht die Lehre der Erfindung vor, Alkoholschnitte für die Herstellung der Acrylatkomponente(n) einzusetzen, deren Gehalt an C22-Alkohol wenigstens 45 Gew.-% ausmacht. Besonders gute Fließpunktverbesserer werden dann erhalten, wenn diese langkettigen Alkoholkomponenten in den zur Herstellung der (Meth)-Acrylatkomponente eingesetzten Alkoholschnitten oberhalb von 50 Gew.-% liegen. Die hier angegebenen Gewichtsprozent-Zahlen beziehen sich auf den Gehalt an C22-Alkohol - und gegebenenfalls höheren Alkoholen - im Alkoholgemisch, das für die Herstellung der Acrylat- bzw. Methacrylatkomponenten verwendet worden ist.It has further been shown that when only small amounts of maleic anhydride are used as comonomers in the sense of the teaching according to the invention, particularly effective copolymers are obtained in the pour point improvers if comparatively high contents of alcohol residues with at least 22 carbon atoms in the acrylate or Methacrylate component are present. The teaching of the invention thus provides for the use of alcohol cuts for the production of the acrylate component (s) whose content of C 22 alcohol makes up at least 45% by weight. Particularly good pour point improvers are obtained if these long-chain alcohol components in the alcohol cuts used to produce the (meth) acrylate component are above 50% by weight. The weight percentages given here relate to the content of C 22 alcohol - and possibly higher alcohols - in the alcohol mixture which was used for the production of the acrylate or methacrylate components.
Die Anwendungskonzentration der erfindungsgemäßen Fließpunktverbesserer liegt im konventionellen Bereich und beträgt beispielsweise 20 bis 1 000 ppm, wobei Mengen im Bereich von 100 bis 500 ppm bevorzugt werden. Die Fließpunktverbesserer werden dabei zweckmäßigerweise in geeigneten Lösungsmitteln eingesetzt. Einzelheiten hierzu sowie zur Herstellung der Copolymerisate finden sich im einschlägigen Stand der Technik, beispielsweise in der bereits zitierten DE-PS 30 31 900.The application concentration of the pour point improvers according to the invention is in the conventional range and is, for example, 20 to 1000 ppm, with amounts in the range from 100 to 500 ppm being preferred. The pour point improvers are expediently used in suitable solvents. Details on this and on the preparation of the copolymers can be found in the relevant prior art, for example in DE-PS 30 31 900 already cited.
Die für die Herstellung der Acrylatkomponenten eingesetzten Alkohole oder Alkoholschnitte können nativen oder synthetischen Ursprungs sein. Alkoholschnitte mit einem überwiegenden Anteil an Komponenten mit wenigstens 22 C-Atomen, gleichzeitig aber auch untergeordneten Mengen an Alkoholkomponenten des Bereichs C16 bis C20, sind die bevorzugten Einsatzmaterialien. In einer besonderen Ausführungsform der Erfindung werden derart ausgewählte Acrylate bzw. Methacrylate mit Maleinsäureanhydrid in solchen Mischungsverhältnissen copolymerisiert, daß das Molverhältnis von Alkyl-Acrylat bzw. -Methacrylat zu Maleinsäureanhydrid größer als 20 : 1 ist.The alcohols or alcohol cuts used for the production of the acrylate components can be of native or synthetic origin. Alcohol cuts with a predominant proportion of components with at least 22 carbon atoms, but at the same time also minor amounts of alcohol components in the range C 16 to C 20 , are the preferred starting materials. In a particular embodiment of the invention, acrylates or methacrylates selected in this way are copolymerized with maleic anhydride in such mixing ratios that the molar ratio of alkyl acrylate or methacrylate to maleic anhydride is greater than 20: 1.
Zur Herstellung der Maleinsäureanhydrid-Copolymerisate werden die beiden Acrylatestergemische A und B eingesetzt, die sich durch die C-Kettenverteilung des jeweils zur Acrylsäureveresterung eingesetzten Fettalkoholgemisches unterscheiden. Die beiden Acrylattypen kennzeichnen sich dabei wie folgt:
Zur Herstellung der Acrylat/MAH-Copolymeren werden zwei Verfahrenstypen eingesetzt, das Batch-Verfahren und das Zulaufverfahren.Two types of processes are used to produce the acrylate / MAH copolymers, the batch process and the feed process.
Die Monomeren, Initiator und Lösungsmittel werden in einen Dreihalskolben eingewogen.The monomers, initiator and solvent are weighed into a three-necked flask.
Bei einer Rührerdrehzahl von 70 Upm wird der Ansatz 10 x 1 min lang evakuiert und das Vakuum jeweils mit 99,999 %igem Stickstoff wieder aufgehoben. Bei einer Rührerdrehzahl von 50 Upm und unter leichtem N2-Strom wird der Ansatz auf 90 °C erwärmt und bei dieser Temperatur gehalten. Während der gesamten Reaktion wird unter Inertbedingungen gearbeitet. Das Anspringen der Reaktion äußert sich in einem Temperaturanstieg auf 93 bis 96 °C. Der Ansatz wird 3 h bei 90 °C ± 1 °C gehalten. Nach dieser Zeit wird innerhalb von 45 min auf Raumtemperatur abgekühlt und das Produkt abgefüllt.At a stirrer speed of 70 rpm, the batch is evacuated for 10 × 1 min and the vacuum is released again with 99.999% nitrogen. At a stirrer speed of 50 rpm and under a slight stream of N 2, the batch is heated to 90 ° C. and kept at this temperature. The entire reaction is carried out under inert conditions. The start of the reaction manifests itself in a temperature rise to 93 to 96 ° C. The mixture is kept at 90 ° C ± 1 ° C for 3 h. After this time, the mixture is cooled to room temperature within 45 minutes and the product is filled.
Als Lösungsmittel wird hier und im nachfolgenden Zulaufverfahren Toluol eingesetzt. Der eingesetzte Polymerisationsinitiator ist Dibenzoylperoxid oder Azoisobutyronitril wie nachstehend noch angegeben. Das Mischungsverhältnis von Lösungsmittel zu Monomerengemisch beträgt 1 : 1 (Gew.-Teile).Toluene is used as the solvent here and in the subsequent feed process. The polymerization initiator used is dibenzoyl peroxide or azoisobutyronitrile as indicated below. The mixing ratio of solvent to monomer mixture is 1: 1 (parts by weight).
Die Monomeren werden im jeweils gewünschten Mischungsverhältnis bei 45 bis 50 °C in Toluol gelöst und die Lösung anschließend auf 25 °C abgekühlt. Auch der Initiator wird in Toluol gelöst eingesetzt. Etwa 20 % der pro Ansatz bestimmten Monomerlösung wird in einem Reaktor vorgelegt. Der Reaktor wird dreimal mit Stickstoff gespült und unter leichtem N2-Strom unter Rühren auf 90 °C erwärmt. Die Initiatorlösung wird jetzt so zudosiert, daß die Gesamtdosierzeit 2,5 h beträgt.The monomers are dissolved in toluene in the desired mixing ratio at 45 to 50 ° C. and the solution is then cooled to 25 ° C. The initiator is also used in solution in toluene. About 20% of the monomer solution determined per batch is placed in a reactor. The reactor is flushed three times with nitrogen and heated to 90 ° C. while stirring under a gentle stream of N 2 . The initiator solution is now metered in so that the total metering time is 2.5 hours.
Ca. 20 min nach Beginn der Initiatorzugabe tritt eine Temperaturerhöhung auf. Die Temperatur wird durch Kühlen des Reaktormantels bei 90 ± 3 °C gehalten.Approx. A temperature increase occurs 20 minutes after the initiator has been added. The temperature is kept at 90 ± 3 ° C by cooling the reactor jacket.
30 min nach Beginn der Initiatorzugabe wird die restliche Monomerlösung so in den Reaktor dosiert, daß die Gesamtdosierzeit 2 h beträgt. Während der gesamten Reaktionszeit wird die Temperatur bei 90 ± 3 °C gehalten. Nachfolgend wird das Reaktionsgemisch weitere 60 min bei der gleichen Temperatur gehalten. Anschließend wird das Reaktionsprodukt gekühlt und bei 30 °C abgefüllt.30 minutes after the initiator has been added, the remaining monomer solution is metered into the reactor in such a way that the total metering time is 2 h. The temperature is kept at 90 ± 3 ° C throughout the reaction time. The reaction mixture is then kept at the same temperature for a further 60 min. The reaction product is then cooled and filled at 30 ° C.
In der nachfolgenden Tabelle 2 sind die erfindungsgemäßen Beispiele 1 bis 10 zusammengefaßt. Dabei wird dem jeweiligen Beispiel der Typ des eingesetzten Acrylatmonomeren A bzw. B zugeordnet und der Prozentgehalt (Gew.-%) des Maleinsäureanhydrids im Monomerengemisch zur Herstellung des Fließpunkterniedrigers angegeben. In den Beispielen 1 und 2 ist der Fließverbesserer nach dem Batch-Verfahren und in den Beispielen 3 bis 10 nach dem Zulaufverfahren hergestellt worden.Examples 1 to 10 according to the invention are summarized in Table 2 below. The type of acrylate monomers A or B used is used in the respective example assigned and the percentage (wt .-%) of maleic anhydride in the monomer mixture for the preparation of the pour point depressant stated. In Examples 1 and 2, the flow improver was produced by the batch process and in Examples 3 to 10 by the feed process.
In den Beispielen 1 und 7 ist als Initiator Azoisobutyronitril, in allen anderen Beispielen als Initiator Dibenzoylperoxid verwendet worden.In Examples 1 and 7, azoisobutyronitrile was used as the initiator, and dibenzoyl peroxide was used as the initiator in all other examples.
Die Tabelle 2 zeigt schließlich die spezifische Viskosität der jeweils hergestellten Copolymerlösungen. Die Viskositätsmessung erfolgt dabei mit einem Ubbelohde-Viskosimeter Kapillare I, ⌀ 0,63 mm. Die vermessenen Toluollösungen sind dabei 3 %ige Lösungen in Toluol. Die Messung wird bei 20 °C nach einer Temperaturangleichung von 10 min durchgeführt.Table 2 finally shows the specific viscosity of the copolymer solutions prepared in each case. The viscosity is measured using an Ubbelohde viscometer capillary I, ⌀ 0.63 mm. The measured toluene solutions are 3% solutions in toluene. The measurement is carried out at 20 ° C after a temperature adjustment of 10 min.
Die Tabelle 2 enthält schließlich die Fließpunktwerte (Pourpoint), die bei der Zugabe der erfindungsgemäßen Fließpunktverbesserer zu einem India-Crude (Bombay-Rohöl) gemäß der nachfolgenden Arbeitsanweisung erhalten worden sind.Finally, Table 2 contains the pour point values which were obtained when the pour point improvers according to the invention were added to an India crude (Bombay crude oil) in accordance with the following working instructions.
Der Pourpoint wurde in Anlehnung an ASTM D 97-66 bzw. DIN 51597 wie folgt bestimmt:The pour point was determined in accordance with ASTM D 97-66 and DIN 51597 as follows:
25,0 g Bombay-Rohöl wurden zusammen mit 800 ppm der 50-gewichtsprozentigen Lösung des Fließverbesserers in einem geschlossenen Gefäß 15 min lang auf 50 °C gehalten und dabei 5mal in regelmäßigen Abständen kräftig geschüttelt. Das so gedopte Rohöl wurde rasch in ein zylinderförmiges Glasgefäß mit einem Innendurchmesser von 27 mm umgefüllt und dieses sogleich verschlossene Gefäß ausreichend tief in ein Wasserbad von + 36°C gehängt.25.0 g of Bombay crude oil, together with 800 ppm of the 50% strength by weight solution of the flow improver, were kept in a closed vessel at 50 ° C. for 15 minutes and vigorously shaken 5 times at regular intervals. The crude oil doped in this way was quickly poured into a cylindrical glass vessel with an inside diameter of 27 mm and this immediately sealed vessel was hung sufficiently deep in a water bath at + 36 ° C.
Nach 30 min wurde das Glas leicht zur Seite geneigt und beobachtet, ob der Inhalt fließend war. Die Probe wurde nun schrittweise um je 3 °C gekühlt und die Prüfprozedur jedesmal vollzogen. Zur Temperatur, bei der der Inhalt auch bei Neigung des Prüfglases um 90 ° nicht mehr floß, wurden 3 °C addiert und diese Temperatur als Pourpoint festgelegt.After 30 minutes the glass was tilted slightly to the side and observed whether the contents were flowing. The sample was then gradually cooled by 3 ° C and the test procedure was carried out each time. 3 ° C was added to the temperature at which the contents no longer flowed, even when the test glass was inclined by 90 °, and this temperature was defined as the pour point.
Der Pourpoint des unbehandelten Bombay-Rohöls liegt nach dieser Bestimmungsmethode bei 30 °C.
Claims (4)
- The use of copolymers consisting of acrylates and/or methacrylates of higher alcohols or alcohol cuts containing at least 16 C atoms in the alcohol radical, of which the content of C22 and optionally higher alcohols - based on the alcohol mixture used to produce the acrylate or methacrylate components - is at least 45% by weight, and no more than 5% by weight and preferably 0.5 to 2.5% by weight of maleic anhydride (% by weight here based on the weight of the copolymer) as flow improvers in paraffin-rich crude oils and/or petroleum fractions with self-pour points above 25°C for reducing their pour points to values below 15°C and preferably below 10°C.
- The use claimed in claim 1, characterized in that the flow improvers are used in crude oils or in petroleum fractions with self-pour points of at least 30°C.
- The use claimed in claims 1 and 2, characterized in that maleic anhydride copolymers based on esters of acrylic acid with predominantly C18-24, alcohols are used, corresponding alcohol cuts with a content of C22 and optionally higher alcohols of more than 50% by weight being preferred.
- The use claimed in claims 1 to 3, characterized in that copolymers with a maleic anhydride content of 1 to 2% by weight are used.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE3807394 | 1988-03-07 | ||
DE3807394A DE3807394A1 (en) | 1988-03-07 | 1988-03-07 | USE OF SELECTED COPOLYMER TYPES OF ACRYLIC AND / OR METHACRYLIC ACID ESTERS AS FLOW-IMPROVERS IN PARAFFIN-LIKE PETROLEUM AND PETROLEUM FRACTIONS (I) |
Publications (3)
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EP0332000A2 EP0332000A2 (en) | 1989-09-13 |
EP0332000A3 EP0332000A3 (en) | 1990-04-18 |
EP0332000B1 true EP0332000B1 (en) | 1997-05-02 |
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EP89103383A Expired - Lifetime EP0332000B1 (en) | 1988-03-07 | 1989-02-27 | Use of selected acrylic and/or methacrylic acid ester copolymer versions as flow enhancers in paraffin-rich mineral oils and mineral-oil fractions (I) |
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EP (1) | EP0332000B1 (en) |
JP (1) | JPH01290892A (en) |
AR (1) | AR247930A1 (en) |
AU (1) | AU610700B2 (en) |
BR (1) | BR8901035A (en) |
CA (1) | CA1334013C (en) |
DE (2) | DE3807394A1 (en) |
DK (1) | DK110689A (en) |
MX (1) | MX172301B (en) |
NO (1) | NO177470C (en) |
TR (1) | TR23834A (en) |
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DE3830913A1 (en) * | 1988-09-10 | 1990-03-15 | Henkel Kgaa | NEW WAFER EMULSION SCOPOLYMERISES, ESPECIALLY A WATER AND OIL DEFINITIVE FORM FOR IMPROVING FLOW PROPERTIES AND POINT POINT LIGHTING OF PETROLEUM AND PETROLEUM FRACTIONS, AND THEIR USE |
FR2710652B1 (en) * | 1993-09-30 | 1995-12-01 | Elf Antar France | Composition of cold operability additives for middle distillates. |
CN104710560B (en) * | 2013-12-13 | 2017-06-06 | 中国石油天然气集团公司 | A kind of dicyclopentadiene and Long Chain Alkyl Acrylate polymer pour point depressant for crude oil |
RU2541680C1 (en) * | 2014-03-21 | 2015-02-20 | Общество с ограниченной ответственностью "Научно-производственное предприятие КВАЛИТЕТ" (ООО "НПП КВАЛИТЕТ") | Inhibitor of asphaltresinparaffin sediments |
CA3015143C (en) | 2016-03-10 | 2023-10-03 | Basf Se | Aqueous polymer dispersions, a method for their preparation and the use thereof as pour-point depressants for crude oil, petroleum, and petroleum products |
LU93040B1 (en) * | 2016-04-21 | 2017-10-27 | Univ Hamburg | Additive for improving the flow properties of paraffinic crude oils |
EP3445837A1 (en) * | 2016-04-21 | 2019-02-27 | Universität Hamburg | Crude oil composition comprising an additive for improving the flow properties of paraffin-containing crude oil |
CN109114426B (en) * | 2017-06-26 | 2020-09-04 | 中国石油天然气集团公司 | Composition for crude oil pour point depressant, preparation method and application |
MX2020002740A (en) | 2017-09-11 | 2020-07-21 | Basf Corp | Aqueous polymer dispersions, a method for their preparation and the use thereof as pour-point depressants for crude oil, petroleum, and petroleum products. |
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GB2160536A (en) * | 1984-06-21 | 1985-12-24 | Elf Aquitaine | Polymeric additives usable for inhibition of the deposit of paraffins in crude oils |
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GB1068401A (en) * | 1965-02-08 | 1967-05-10 | Exxon Research Engineering Co | Improved motor fuel composition |
US3904385A (en) * | 1972-05-08 | 1975-09-09 | Texaco Inc | Polyacrylates and waxy residual fuel compositions thereof |
DE3031900C2 (en) * | 1980-08-23 | 1983-06-09 | Chemische Fabriek Servo B.V., 7491 Delden | Copolymers of n-alkyl acrylates and maleic anhydride and their use as crystallization inhibitors for crude oils containing paraffin |
-
1988
- 1988-03-07 DE DE3807394A patent/DE3807394A1/en not_active Withdrawn
-
1989
- 1989-02-27 EP EP89103383A patent/EP0332000B1/en not_active Expired - Lifetime
- 1989-02-27 DE DE58909795T patent/DE58909795D1/en not_active Expired - Lifetime
- 1989-03-03 TR TR89/0216A patent/TR23834A/en unknown
- 1989-03-03 MX MX015136A patent/MX172301B/en unknown
- 1989-03-06 AU AU31024/89A patent/AU610700B2/en not_active Ceased
- 1989-03-06 NO NO890937A patent/NO177470C/en unknown
- 1989-03-06 JP JP1053610A patent/JPH01290892A/en active Pending
- 1989-03-06 BR BR898901035A patent/BR8901035A/en not_active Application Discontinuation
- 1989-03-07 CA CA000592933A patent/CA1334013C/en not_active Expired - Fee Related
- 1989-03-07 AR AR89313350A patent/AR247930A1/en active
- 1989-03-07 DK DK110689A patent/DK110689A/en not_active Application Discontinuation
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GB2160536A (en) * | 1984-06-21 | 1985-12-24 | Elf Aquitaine | Polymeric additives usable for inhibition of the deposit of paraffins in crude oils |
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NO177470C (en) | 1995-09-20 |
AU3102489A (en) | 1989-09-07 |
DE58909795D1 (en) | 1997-06-05 |
EP0332000A3 (en) | 1990-04-18 |
MX172301B (en) | 1993-12-13 |
BR8901035A (en) | 1989-10-24 |
AR247930A1 (en) | 1995-04-28 |
NO177470B (en) | 1995-06-12 |
AU610700B2 (en) | 1991-05-23 |
DK110689D0 (en) | 1989-03-07 |
NO890937D0 (en) | 1989-03-06 |
TR23834A (en) | 1990-09-25 |
CA1334013C (en) | 1995-01-17 |
EP0332000A2 (en) | 1989-09-13 |
JPH01290892A (en) | 1989-11-22 |
DE3807394A1 (en) | 1989-09-21 |
NO890937L (en) | 1989-09-08 |
DK110689A (en) | 1989-09-08 |
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