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NO129635B
NO129635B NO04199/70*[A NO419970A NO129635B NO 129635 B NO129635 B NO 129635B NO 419970 A NO419970 A NO 419970A NO 129635 B NO129635 B NO 129635B
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fuel
polymer
polyamine
hydrocarbon
stated
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NO04199/70*[A
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Norwegian (no)
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H Morris
P Dorn
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Texaco Development Corp
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/146Macromolecular compounds according to different macromolecular groups, mixtures thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1625Hydrocarbons macromolecular compounds
    • C10L1/1633Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
    • C10L1/1641Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Lubricants (AREA)

Description

Drivstoffsammensetning. Fuel composition.

Foreliggende oppfinnelse angår en drivstoffsammensetning. The present invention relates to a fuel composition.

Forbrenningsmotorer, særlig med toppventiler, er utsatt Internal combustion engines, especially with overhead valves, are exposed

for oppbygning av betydelige hårde og seige avleiringer på inn-løps ventilene og ventilsetene. Disse avsetninger har uhelig innvirkning på motorens gang. Når mengdene av disse avleiringer vokser, utsettes motoren for effekttap, ujevn tolmgang og. enkelte ganger ventilbrenning. Når avsetningene blir svært store, brytes deler av dem av og trekkes inn i forbrenningskammeret. Man har sett tilfeller .av mekanisk ødeleggelse av stempel og stempelringer forårsaket av slike avsetninger. for the build-up of significant hard and tough deposits on the inlet valves and valve seats. These deposits have an unholy effect on the running of the engine. When the amounts of these deposits grow, the engine is exposed to loss of power, uneven idling and. sometimes valve burning. When the deposits become very large, parts of them break off and are drawn into the combustion chamber. Cases have been seen of mechanical destruction of pistons and piston rings caused by such deposits.

Man har gjort et betydelig arbeide for å finne årsaken og Considerable work has been done to find the cause and

arten av disse avsetninger på innløpsventilene. Avsetningene selv består i det vesentlige av biprodukter fra. drivstoff-forbrenningen og nedbrytningen av smøreoljen. Analyse av avsetningene typer på the nature of these deposits on the inlet valves. The provisions themselves essentially consist of by-products from the fuel combustion and the breakdown of the lubricating oil. Analysis of the deposits types on

at de viskositets-forbedrende tilsetninger som tilsettes smøre-oljen virker som bindemidler for avsetningene. Polymetakrylat-viskositetsforbedrere er som et eksempel en klasse slike stoffer som synes å bidra sterkt til oppbygging av disse avsetninger.''that the viscosity-improving additives that are added to the lubricating oil act as binders for the deposits. Polymethacrylate viscosity improvers are, as an example, a class of such substances which seem to contribute strongly to the build-up of these deposits.''

Ved å betrakte motorens drift vil. man se hvorledes ned- '■' brytning av smøreoljen kan føre til avsetninger i brennstoffinn-takssystemet . Forbrenningsmotorer.med elektrisk tenning inneholder et reservoir av smøreolje -i bunnpannen.-'Når motoren kjøres, gjennomføres hovedsmøringen ved at bunnpanneoljen sprutes og kastes opp på motorens bevegelige deler og sylinderveggene. En del av, denne olj en. blir imidlertid pumpet under trykk til motorens øvre deler for å smøre de* bevegelige deler her. I motorer med hengende ventiler føres en liten strøm av den olje som pumpes til motorens overdel hele tiden nedover innløps- og exhaust-ventil^-stammene for å sikre at disse blir konstant smurt i deres lågere ved kjøring. Den olje som renner ned innløpsventilstammen, ventil-hodet og omkring ventilsetet for innløpsventilen•blir etter hva man tror pyrolysert under de herskende temperaturer og fører til dannelse og oppbygning av nevnte avsetninger. By considering the engine operation will. you can see how breakdown of the lubricating oil can lead to deposits in the fuel intake system. Combustion engines with electric ignition contain a reservoir of lubricating oil -in the sump.-'When the engine is running, the main lubrication is carried out by the sump oil being sprayed and thrown up onto the engine's moving parts and the cylinder walls. Part of, this oil one. however, is pumped under pressure to the upper parts of the engine to lubricate the* moving parts here. In engines with hanging valves, a small stream of the oil pumped to the top of the engine is constantly passed down the inlet and exhaust valve^ stems to ensure that these are constantly lubricated in their bearings when driving. The oil that flows down the inlet valve stem, the valve head and around the valve seat for the inlet valve•is believed to be pyrolysed under the prevailing temperatures and leads to the formation and build-up of the aforementioned deposits.

Problemet med slike avsetninger oppstår ikke i vesentlig grad på eller omkring exhaustventilene og ventilsetene. Man antar at dette skyldes de høye temperaturer som hersker ved og på exhaustventilen under utblåsningsperioden og virkningen av exhaust-gassene som føres ut med stor hastighet og ikke muliggjør avsetning av avleiringer eller kontinuerlig brenner disse av og transporterer potensielle avsetninger bort. Imidlertid, man får i henhold til oppfinnelsen en vesentlig og uventet økning av innløpsventilens levetid av grunner som man ikke helt forstår. The problem with such deposits does not occur to a significant extent on or around the exhaust valves and valve seats. It is assumed that this is due to the high temperatures that prevail at and on the exhaust valve during the blow-out period and the effect of the exhaust gases which are carried out at high speed and do not enable the deposition of deposits or continuously burn them off and transport potential deposits away. However, according to the invention, one gets a significant and unexpected increase in the service life of the inlet valve for reasons that are not fully understood.

US-patent nr. 3.502.451 vedrører en drivstoffsammensetning for bensin-forbrenningsmotor som inneholder en polymer, kopolymer eller hydrogenert polymer. Spesielt brukes en polymer av - Cg umettet hydrokarbon,, en kopolymer av umettede - Cg-hydrokarboner eller en hydrogenert polymer eller kopolymer av umettede - Cg-hydrokarboner med molekylvekter mellom ca. 500 og 3500 i konsentrasjoner på mellom 0,01 og 0,20 volum-%•i motordrivstoff for forbrenningsmotor med elektrisk tenning. Dette brennstoff er effektivt til å hindre eller nedsette dannelsen av avsetninger på innløpsventilene og innløpsdélene i motoren. US Patent No. 3,502,451 relates to a gasoline internal combustion engine fuel composition containing a polymer, copolymer or hydrogenated polymer. In particular, a polymer of -Cg unsaturated hydrocarbon, a copolymer of unsaturated -Cg hydrocarbons or a hydrogenated polymer or copolymer of unsaturated -Cg hydrocarbons with molecular weights between approx. 500 and 3500 in concentrations of between 0.01 and 0.20% by volume•in motor fuel for internal combustion engines with electric ignition. This fuel is effective in preventing or reducing the formation of deposits on the inlet valves and inlet parts of the engine.

Ifølge foreliggende oppfinnelse er det tilveiebragt en drivstoffsammensetning med forbedrede driftsegenskaper inneholdende N-polyaminsubstituerte alkenylsuccinimider, og denne sammensetning er kjennetegnet ved A) et hydrokarbonbasis-drivstoff bestående av en blanding av hydrokarboner med kokepunkt i bensinområdet, According to the present invention, a fuel composition with improved operating properties containing N-polyamine-substituted alkenylsuccinimides is provided, and this composition is characterized by A) a hydrocarbon-based fuel consisting of a mixture of hydrocarbons with a boiling point in the petrol range,

B) 0,000*4 - 0,1 vek. t-%, basert på sammensetningens vekt, av et N-polyaminsubstituert alkenylsuccinimid fremstilt ved omsetning av en alkenylravsyre eller et alkenylravsyrearihydrid med formelen: hvor R* betegner en hydrokarbongruppe med molekylvekt fra 400 til 3Q0O, med 0,5 - 2 ekvivalenter polyamin med formelen: B) 0.000*4 - 0.1 wk. t-%, based on the weight of the composition, of an N-polyamine substituted alkenyl succinimide prepared by reacting an alkenyl succinic acid or an alkenyl succinic acid arihydride of the formula: where R* denotes a hydrocarbon group with molecular weight from 400 to 3Q00, with 0.5 - 2 equivalents of polyamine with the formula:

hvor x er 1-b og R betegner hydrogen eller en lavere alkylgruppe, og C.) 0,003 - 0,20 volum-? av 1) en polymer av et umettet t^-til Gg-hydrokarbon, 2) en kopolymer av et -umettet C^- til Cg-hydrokarbon eller 3) den tilsvarende hydrogenerte polymer eller kopolymer, hvilken polymer, kopolymer eller hydrogenerte derivater derav har en molekylvekt på 500 3500. where x is 1-b and R denotes hydrogen or a lower alkyl group, and C.) 0.003 - 0.20 volume-? of 1) a polymer of an unsaturated t^- to Gg hydrocarbon, 2) a copolymer of an -unsaturated C^- to Cg hydrocarbon or 3) the corresponding hydrogenated polymer or copolymer, which polymer, copolymer or hydrogenated derivatives thereof have a molecular weight of 500 3500.

Oppdagelsen av et forbedret drivstoff med en slik sammensetning var høyst overraskende og uventet fordi N-polyamin-substituerte alkenylsuccinimider i motordrivstoff ikke har noen innvirkning når det gjelder å hindre avsetninger på innløps-ventilene og -ventilsetene i forbrenningsmotorer med gnisttenning. The discovery of an improved fuel with such a composition was highly surprising and unexpected because N-polyamine-substituted alkenylsuccinimides in motor fuels have no effect in preventing deposits on the inlet valves and valve seats of spark-ignition internal combustion engines.

R'-gruppen i ovenstående formel er et hydrokarbonradikal fortrinnsvis avledet fra et olefin med fra 2 til 5 C-atomer. Egnede olefiner et etylen, propylen, 1-buten, 2-buten, isobutylen og amylener. Gruppen R<1> har som nevnt en molekylvekt fra 400 til 3000, hvilket tilsvarer ca. 30 til 200 C-atomer, med en foretrukket molekylvekt på ca. b00 til 1200, x er fortrinnsvis et tall fra 2 til 1 og R er fortrinnsvis hydrogen. Egnede polyaminer og polyalkylenpolyaminer med ovenstående formel er etylendiamin, propylendiamin, butylendiamin, dietylentriamin, triétylentetramin, tetraetylenpentamin, pentaetylenheksamin, dipropylentriamin, tripropylentetramin. Dialkylaminoalkylenaminer som dimetylamino-metylamin, dimetylaminopropylamin, dietylaminopropyiamin og lignende kan også brukes. The R' group in the above formula is a hydrocarbon radical preferably derived from an olefin having from 2 to 5 C atoms. Suitable olefins are ethylene, propylene, 1-butene, 2-butene, isobutylene and amylenes. As mentioned, the group R<1> has a molecular weight from 400 to 3000, which corresponds to approx. 30 to 200 C atoms, with a preferred molecular weight of approx. b00 to 1200, x is preferably a number from 2 to 1 and R is preferably hydrogen. Suitable polyamines and polyalkylene polyamines of the above formula are ethylenediamine, propylenediamine, butylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, dipropylenetriamine, tripropylenetetramine. Dialkylaminoalkyleneamines such as dimethylaminomethylamine, dimethylaminopropylamine, diethylaminopropylamine and the like can also be used.

En halv til to ekvivalenter polyamin omsettes med alkenylravsyre >eller -ravsyreanhydridet til reaksjonsproduktet. Bereg-ningene av ekvivalentmengden polyaminreaktant baseres på nitrogen-innholdet, idet etylendiamin har to ekvivalenter pr. mol. Det foretrekkes å omsette ca. en ekvivalent alkenylravsyre :eller One half to two equivalents of polyamine is reacted with alkenyl succinic acid >or -succinic anhydride to the reaction product. The calculations of the equivalent quantity of polyamine reactant are based on the nitrogen content, as ethylenediamine has two equivalents per mol. It is preferred to sell approx. an equivalent alkenyl succinic acid :or

-ravsyreanhydrid med ca. en ekvivalent polyamin. -succinic anhydride with approx. one equivalent polyamine.

Ved en typisk fremstilling fremstilles et polyisobutylen-ravsyreanhydrid ved å omsette et mol polybutylen med molekylvekt ca. 1000 med 196 g (2 mol) maleinsyreanhydrid ved 200°C i 21 timer. Reaksjonsblandingen avkjøles og 750 ml heksan tilsettes. Opp-løsningen filtreres for å fjerne faste forurensninger og avdampes i vakuum for å fjerne heksanet. Temperaturen økes deretter til ca. 200°C for å fjerne alle spor av overskudd av maleinsyreanhydrid. In a typical preparation, a polyisobutylene-succinic anhydride is produced by reacting a mole of polybutylene with a molecular weight of approx. 1000 with 196 g (2 mol) of maleic anhydride at 200°C for 21 hours. The reaction mixture is cooled and 750 ml of hexane are added. The solution is filtered to remove solid impurities and evaporated in vacuo to remove the hexane. The temperature is then increased to approx. 200°C to remove all traces of excess maleic anhydride.

Til en blanding av 1100 g (1 mol) polyisobutenylravsyreanhydrid og 400 ml toluen settes langsomt ved romtemperatur 52 g (0,5 mol) dietylentriamin. Blandingen oppvarmes og vann-toluen-azeotropen oppsamles i en vannfelle. Reaksjonen er avsluttet når det ikke lenger går over vann. Blandingen oppvarmes til 100°C under nedsatt trykk for å fjerne toluenet og man har et produkt som vesentlig består av bispolyisobutenylsuccinimid. To a mixture of 1100 g (1 mol) of polyisobutenylsuccinic anhydride and 400 ml of toluene, 52 g (0.5 mol) of diethylenetriamine are added slowly at room temperature. The mixture is heated and the water-toluene azeotrope is collected in a water trap. The reaction is finished when no more water passes over it. The mixture is heated to 100°C under reduced pressure to remove the toluene and a product is obtained which essentially consists of bispolyisobutenyl succinimide.

Ved en annen typisk fremstilling fremstilte man polyiso-buty lenravsyreanhydrid ved omsetning av 1 mol polybuten med mol-vekt ca. 1300 med 196 g (2 mol) maleinsyreanhydrid ved 200°C i 24 timer. Reaksjonsblandingen ble avkjølt og 750 ml heksan til- , satt. Oppløsningen ble filtrert for å fjerne faste stoffer og inndampet i fullt vakuum for å fjerne heksanet. Temperaturen ble øket til ca. 200°C for å fjerne alle spor av maleinsyreanhydrid-overskudd. In another typical preparation, polyisobutylene succinic anhydride was produced by reacting 1 mol of polybutene with a molar weight of approx. 1300 with 196 g (2 mol) of maleic anhydride at 200°C for 24 hours. The reaction mixture was cooled and 750 ml of hexane was added. The solution was filtered to remove solids and evaporated in full vacuum to remove the hexane. The temperature was increased to approx. 200°C to remove all traces of excess maleic anhydride.

Til en blanding av 1 mol polyisobutenylravsyreanhydrid og 400 ml toluen settes langsomt ved romtemperatur 0,5 mol etylendiamin. Blandingen oppvarmes og azeotropen av vann og toluen opp-fanges i en vannfelle. Reaksjonen er fullstendig når det ikke To a mixture of 1 mol of polyisobutenylsuccinic anhydride and 400 ml of toluene, 0.5 mol of ethylenediamine is added slowly at room temperature. The mixture is heated and the azeotrope of water and toluene is collected in a water trap. The reaction is complete when it is not

lenger går over noe vann. Blandingen oppvarmes til ca. 100 C further goes over some water. The mixture is heated to approx. 100 C

under redusert trykk for å fjerne toluenet og gir et produkt som består i det vesentlige av bispolyisobutenylravsyreimid. under reduced pressure to remove the toluene to give a product consisting essentially of bispolyisobutenyl succinimide.

Den polymer som brukes i drivstoffet ifølge oppfinnelsen, The polymer used in the fuel according to the invention,

er en polymer som fremstilles fra et umettet hydrokarbon, dvs. et mono-olefin, diolefin eller en kopolymer av disse, med en antallsmidlere molekylvekt på 500 til 35°0. Blandinger av olefinpolymere med antallsmidlere molekylvekt 4'om faller innenfor dette område er også effektive. Olefiner som kan brukes for fremstilling av polydlefinpolymere omfatter etylen, propylen, 1-buten, 2-buten, isobiitylen, amylen, heksylen, butadien og isopren. Generelt har de olefinmonomere som brukes for fremstilling av umettede poly-olefinhydrokarboner med fra 2 til 6 C-atomer. Polyolefinpolymere oppbygget av C^- og C^-olefiner, som propylen og isobutylen, er særlig foretrukket i henhold til oppfinnelsen. Andre polyolefiner som kan brukes, er fremstilt ved krakking av polyolefinpolymere eller av kopolymere med høy molekylvekt til polymere som faller innenfor ovenstående molekylvektområde. Derivater av de anførte polymere fremstilt ved metning av disse polymere ved hydrogenering er også effektive og omfattes av oppfinnelsen. Uttrykket "polymere" skal omfatte polyolefinpolymere og deres tilsvarende hydrogenerte derivater. is a polymer produced from an unsaturated hydrocarbon, i.e. a mono-olefin, diolefin or a copolymer thereof, with a number average molecular weight of 500 to 35°0. Blends of olefin polymers with number average molecular weight 4' if falling within this range are also effective. Olefins that can be used to make polyolefin polymers include ethylene, propylene, 1-butene, 2-butene, isobiethylene, amylene, hexylene, butadiene and isoprene. In general, the olefin monomers used for the preparation of unsaturated polyolefin hydrocarbons have from 2 to 6 C atoms. Polyolefin polymers made up of C 1 and C 2 olefins, such as propylene and isobutylene, are particularly preferred according to the invention. Other polyolefins that can be used are prepared by cracking polyolefin polymers or high molecular weight copolymers to polymers falling within the above molecular weight range. Derivatives of the listed polymers produced by saturating these polymers by hydrogenation are also effective and are covered by the invention. The term "polymers" shall include polyolefin polymers and their corresponding hydrogenated derivatives.

Molekylvekten for de polymere eller polymerderivatene er viktig for fremstilling av et effektivt drivstoff i henhold til oppfinnelsen. Virkningsfulle drivstoffsammensetninger i henhold til oppfinnelsen krever en polymer eller hydrogenert polymer-derivat med antallsmidlere molekylvekt på mellom 500 og 3500 The molecular weight of the polymer or polymer derivatives is important for the production of an efficient fuel according to the invention. Effective fuel compositions according to the invention require a polymer or hydrogenated polymer derivative with a number average molecular weight of between 500 and 3500

målt ved osmometrimetoden. Meget effektive drivstoffsammensetninger fremstilles ut fra polymere og derivater derav med molekylvekter innenfor de foretrukne området 650 til 2600. Meget effektive drivstoffsammensetninger kan fremstilles inneholdende polymere med relativt lav molekylvekt, dvs. polymere med molekylvekter på mellom 650 og 995• measured by the osmometry method. Highly efficient fuel compositions are produced from polymers and derivatives thereof with molecular weights within the preferred range of 650 to 2600. Highly efficient fuel compositions can be produced containing polymers with a relatively low molecular weight, i.e. polymers with molecular weights of between 650 and 995•

Fremgangsmåten for fremstilling av disse olefinpolymere, kopolymere, hydrogenerte polymere eller kopolymere er velkjent. Bestemmelsen av den antallsmidlere molekylvekt for de polymere skjer i henhold til ASTM osmometrimetoden med betegnelsen ASTM D-2503"67. Eksempler på polymere som er'effektive i drivstoffsammensetninger i henhold til oppfinnelsen^ angitt sammen med deres antallsmidlere molekylvekt^ er som følger: polypropylen 800, polypropylen 975, polypropylen 1120, polypropylen 1150, polypropylen 1370, polypropylen- 2560, polybuten-I 800, polybuten-1 1200, polyisobutylen 850, polyisobutylen 1000,.polyisobutylen 1200, polyisobutylen 1575, hydrogenert polybuten 1100, - C^-etylen-butylen-kopolymer (1:1) 810. The process for producing these olefin polymers, copolymers, hydrogenated polymers or copolymers is well known. The determination of the number average molecular weight of the polymers takes place in accordance with the ASTM osmometry method with the designation ASTM D-2503"67. Examples of polymers which are effective in fuel compositions according to the invention^ indicated together with their number average molecular weight^ are as follows: polypropylene 800 , polypropylene 975, polypropylene 1120, polypropylene 1150, polypropylene 1370, polypropylene- 2560, polybutene-I 800, polybutene-1 1200, polyisobutylene 850, polyisobutylene 1000,.polyisobutylene 1200, polyisobutylene 1575, hydrogenated polybutene 1100, - C^-ethylene- butylene copolymer (1:1) 810.

Fremgangsmåten for fremstilling av N-polyamin-substituerte alkenylsuccinimider er også kjent. Det skal fremheves at egnede N-polyamin-substituerte alkenylsuccinimider eller blandinger av disse kan råes i handelen. Det er hensiktsmessig å bruke reaksjonsproduktet oppløst i en mineralolje. The process for preparing N-polyamine-substituted alkenylsuccinimides is also known. It should be emphasized that suitable N-polyamine-substituted alkenylsuccinimides or mixtures thereof can be obtained commercially. It is appropriate to use the reaction product dissolved in a mineral oil.

Basisdrivstoffet i henhold til oppfinnelsen består av en blanding av hydrokarboner som koker i bensinkokepun.ktområdet Dette basisdrivstoff kan bestå av rettkjedede eller forgrenede paraffiner, cykloparaffiner, olefiner og aromatiske hydrokarboner, eller blandinger av disse. Drivstoffet kan være avledet fra direkte destillert lettbensin, polymerbensin, naturlig bensin eller fra katalytisk krakket eller termisk krakket hydrokarbon og katalytisk behandlede og raffinerte oljer,, og koker mellom ca. 32 og 230°C. Sammensetningen av selve basisdrivstoffet er ikke avgjørende og heller ikke har drivstoffet oktantall noen merkbar innvirkning på oppfinnelsen. Alle de vanlige bensintyper kan brukes for utførelse av oppfinnelsen. The base fuel according to the invention consists of a mixture of hydrocarbons that boil in the petrol boiling point range. This base fuel can consist of straight-chain or branched paraffins, cycloparaffins, olefins and aromatic hydrocarbons, or mixtures of these. The fuel can be derived from directly distilled light petrol, polymer petrol, natural petrol or from catalytically cracked or thermally cracked hydrocarbon and catalytically treated and refined oils,, and boils between approx. 32 and 230°C. The composition of the base fuel itself is not decisive, nor does the fuel's octane number have any noticeable impact on the invention. All the usual types of petrol can be used for carrying out the invention.

Drivstoffsammensetningen ifølge oppfinnelsen kan inneholde alle de additiver som vanligvis tilsettes motordrivstoff. F.eks. kan basisbrennstoffet blandes med en anti-banke-forbindelse, som tetraalkylbly, bl.a. tetraetylbly, tetrametylbly, tetrabutylbly og blandinger av disse, generelt i konsentrasjoner på fra ca. 0,1-1 ml pr. liter bensin. Den blanding av tetraetylbly som fåes i handelen for tilsetning til bensin, inneholder en blanding av etylenklorid og etylenbromid som brukes som avdriver for å fjerne blyet fra forbrenningskammeret i form av flyktig blyhalogenid. Brennstoffet kan også inneholde alle de vanlige typer antikondens-tilsetninger, korrosjonsinhibitorer, fargestoffer og lignende som f.eks. anført i US-patenter 2.632.695, 2.844.449, 3-325.260, 3.232,724, 2.622.018 og 2.922.708. The fuel composition according to the invention can contain all the additives that are usually added to motor fuel. E.g. can the base fuel be mixed with an anti-knock compound, such as tetraalkyl lead, i.a. tetraethyl lead, tetramethyl lead, tetrabutyl lead and mixtures thereof, generally in concentrations of from approx. 0.1-1 ml per liter of petrol. The mixture of tetraethyl lead which is commercially available for addition to petrol contains a mixture of ethylene chloride and ethylene bromide which is used as a drifter to remove the lead from the combustion chamber in the form of volatile lead halide. The fuel can also contain all the usual types of anti-condensation additives, corrosion inhibitors, dyes and the like such as e.g. disclosed in US Patents 2,632,695, 2,844,449, 3-325,260, 3,232,724, 2,622,018 and 2,922,708.

De nye drivstoffsammensetninger ifølge oppfinnelsen fremstilles ved å blande passende mengder nevnte N-polyamin-substituerte alkenylsuccinimider og polymeradditiver til utgangsbensinen. Additivene er lett oppløselige og kan tilsettes r ønsket rekkefølge og på ønsket måte. The new fuel compositions according to the invention are produced by mixing appropriate amounts of said N-polyamine-substituted alkenylsuccinimides and polymer additives to the starting gasoline. The additives are easily soluble and can be added in the desired order and in the desired manner.

De forsøksmetoder som har vært brukt for å prøve drivstoff-sammensetningene var "Buick Induction System Deposits Test<*> gjennom-ført med en 1964 Buick 425 CID V-8 motor. Drivstoffene som ble underkastet disse forsøk ble bedømt med hensyn til avsetningsmengde på motorens innløpsventiler og -ventilseter, hvilket fremgår mer detaljert nedenfor^The test methods that have been used to test the fuel compositions were the "Buick Induction System Deposits Test<*> conducted with a 1964 Buick 425 CID V-8 engine. The fuels subjected to these tests were rated for the amount of deposits on the engine's inlet valves and valve seats, which appears in more detail below^

Forsøket ble utført med ovenfor nevnte motor forsynt med The experiment was carried out with the above-mentioned engine supplied with

en PCV-ventil ("Positive Crankcase Ventilation" = positiv bunn-panneventilasjon) ag tilkoblet dynamometer og utstyr for regulering av hastighet, belastning og mtortemperatur. Forsøket krever ca. 1300 1 bensin og 15 1 smøreolje pr. forsøk. a PCV valve ("Positive Crankcase Ventilation" = positive bottom pan ventilation) and connected dynamometer and equipment for regulating speed, load and mtor temperature. The experiment requires approx. 1300 1 petrol and 15 1 lubricating oil per attempt.

For hvert forsøk renses sylindertoppen fullstendig og det innsettes nye innløpsventiler. Man påser spesielt at klaringen mellom innløpsventil og ventilføring holdes mellom 0,089 og For each test, the cylinder head is completely cleaned and new inlet valves are inserted. Care is taken in particular that the clearance between the inlet valve and the valve guide is kept between 0.089 and

0,115 mm. Videre sørger man for at ventilsetebreddene ligger mellom 1,2 og 2,0 mm. Motorblokken overhales fullstendig som an-ført i 1964 service håndboken Buick når kompressjonen synker eller oljeforbruket blir for stort. 0.115 mm. Furthermore, it is ensured that the valve seat widths are between 1.2 and 2.0 mm. The engine block is completely overhauled as stated in the 1964 Buick service manual when compression drops or oil consumption becomes excessive.

Motoren påfylles 1 liter olje og renses 15 minutter ved 1500 omdreininger pr. minutt. Oljen tappes og man påfyller på The engine is filled with 1 liter of oil and cleaned for 15 minutes at 1,500 rpm. minute. The oil is drained and topped up

nytt 1 liter olje hvoretter forsøkene begynner. Motoren kjøres i 4 perioder på hver b timer, med ialt 16 perioder, dvs. 96 timer på følgende måte: new 1 liter of oil after which the experiments begin. The engine is run for 4 periods of b hours each, with a total of 16 periods, i.e. 96 hours, as follows:

Etter avsluttet kjøreforsøk tas sylindertoppen- og ventilene ut og ventilene bedømmes visuelt med hensyn til avleiringer på ventilhodeområdetf Avleiringer på innløpsventilen bedømmes etter en verdiskala som går fra 10 til 1.. Karakteren 10 antyder en fullstendig ren, ventil, mens karakteren 1 gis til en ekstremt belagt ventil. Avsetninger omkring ventilsetet bedømmes med karakteren S - spor, L - lett, M - middel, T -tykt. After the test run, the cylinder head and valves are removed and the valves are visually assessed for deposits on the valve head area. coated valve. Deposits around the valve seat are graded S - traces, L - light, M - medium, T - thick.

Følgende eksempler illustrerer utførelse av oppfinnelsen. Den utgangsbensin som ble brukt var en typisk kvalitets-bensin inneholdende 0,8 ml tetraetylbly pr. liter bensin. Basisbrennstoffet inneholdt 25 % aromatiske, 20 % olefiniske og 55 '% alifatiske hydrokarboner bestemt ifølge FIA-analyse. Bensinen hadde et startkokepunkt ifølge ASTM på 30°C og et sluttkokepunkt på 190°C, og et Research oktantall på ca. 100. Når intet annet er angitt, inneholdt utgangsot'ensinen 0,5 volum-% handelsvanlig additiv inneholdende korrosjonsinhibitor i mineralolje. Denne additivblanding hadde ingen vesentlig betydning på avsetningene på innløpsventilen og -ventilsetet. The following examples illustrate implementation of the invention. The starting petrol used was a typical quality petrol containing 0.8 ml of tetraethyl lead per liter of petrol. The base fuel contained 25% aromatic, 20% olefinic and 55% aliphatic hydrocarbons as determined by FIA analysis. The petrol had an initial boiling point according to ASTM of 30°C and a final boiling point of 190°C, and a Research octane number of approx. 100. When nothing else is stated, the starting oil contained 0.5% by volume of commercial additive containing corrosion inhibitor in mineral oil. This additive mixture had no significant effect on the deposits on the inlet valve and valve seat.

En typisk bensin uten tilsetning ifølge oppfinnelsen gir en bedømmelseskarakter på avsetningen på innløpsventilen på ca. 6,0, og en ventilsetekarakter på T=tykt. En forbedring i ventilkarakteren på 0,5 enheter bedre enn basisbensinen og brukbar .ventilseteav-setning, spor eller lett, utgjør en vesentlig forbedring. En forbedring på 1,0 enhet eller mer generelt til 7,0 eller høyere og godtagbar karakter for avsetning på ventilsetet er en meget vesentlig forbedring i motorenhet. A typical petrol without additive according to the invention gives an assessment mark on the deposit on the inlet valve of approx. 6.0, and a valve seat grade of T=thick. An improvement in valve character of 0.5 units better than the base gasoline and usable .valve seat deposition, trace or light, constitutes a significant improvement. An improvement of 1.0 unit or more generally to 7.0 or higher and acceptable grade for deposit on the valve seat is a very significant improvement in engine unit.

Eksemplene 6 og 7 viser anvendelse av foreliggende oppfinnelse og man ser den overraskende økning i renheten for innløps-ventiler og -ventilseter som oppstår ved det uventede samvirke mellom komponentene i tilsetningen ifølge oppfinnelsen. Examples 6 and 7 show the application of the present invention and one sees the surprising increase in the cleanliness of inlet valves and valve seats that occurs due to the unexpected interaction between the components of the additive according to the invention.

Claims (10)

1. Drivstoffsammensetning méd forbedrede driftsegenskaper inneholdende N-polyaminsubstituerte alkenylsuccinimider., karakterisert ved A) et hydrokarbonbasisdrivst<p>ff bestående av en blanding av hydrokarboner med kokepunkt i bensinområdet, B) 0,0004 - 0,1 vekt-%, basert på sammensetningens vekt, av et N-polyamin-substituert alkenylsuccinimid fremstilt ved omsetning av en alkenylravsyre eller et alkenylravsyreanhydrid med formelen: hvor R' betegner en hydrokarbongruppe med molekylvekt fra 100 til 3000, med 0,5-2 ekvivalenter polyamin med formelen: hvor x er 1- 6 og R betegner hydrogen eller en lavere alkylgruppe, og C) 0,003 - t3,20 volum-? av i; en polymer av et umettet C2~ til Cg-hydrokarbon, 2) en kopolymer av et umettet C2~ til Cg-hydrokarbon eller 3) den tilsvarende hydrogenerte polymer eller kopolymer, hvilken polymer, kopolymer eller hydrogenerte derivater derav har en molekylvekt på 500-3500.1. Fuel composition with improved operating properties containing N-polyamine substituted alkenylsuccinimides., characterized by A) a hydrocarbon base fuel<p>ff consisting of a mixture of hydrocarbons with a boiling point in the petrol range, B) 0.0004 - 0.1% by weight, based on the composition's weight, of an N-polyamine-substituted alkenyl succinimide prepared by reacting an alkenyl succinic acid or an alkenyl succinic anhydride with the formula: where R' denotes a hydrocarbon group with molecular weight from 100 to 3000, with 0.5-2 equivalents of polyamine with the formula: where x is 1-6 and R denotes hydrogen or a lower alkyl group, and C) 0.003 - t3.20 volume-? of in; a polymer of an unsaturated C2~ to Cg hydrocarbon, 2) a copolymer of an unsaturated C2~ to Cg hydrocarbon or 3) the corresponding hydrogenated polymer or copolymer, which polymer, copolymer or hydrogenated derivatives thereof have a molecular weight of 500-3500. 2. Drivstoff som angitt i krav 1, karakterisert v e d at R' iiar en molekylvekt fra 800 til 1200.2. Fuel as specified in claim 1, characterized in that R' has a molecular weight of from 800 to 1200. 3. Drivstoff som angitt i krav 1 eller 2, karakterisert ved at R' er avledet fra et olefin med 2 til 5 C-atomer.3. Fuel as stated in claim 1 or 2, characterized in that R' is derived from an olefin with 2 to 5 C atoms. 4. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at R er hydrogen.4. Fuel as specified in one or more of the above requirements, characterized in that R is hydrogen. 5. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at x i nevnte polyamin har verdien 2 til 4.5. Fuel as specified in one or more of the above claims, characterized in that x in said polyamine has the value 2 to 4. 6. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at polyaminet er dietylentriamin.6. Fuel as stated in one or more of the above claims, characterized in that the polyamine is diethylenetriamine. 7. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at nevnte N-polyamin-substituerte alkenylsuccinimid er reaksjonsproduktet mellom polybutenravsyreanhydrid og dietylentriamin. b. 7. Fuel as stated in one or more of the above claims, characterized in that said N-polyamine-substituted alkenylsuccinimide is the reaction product between polybutene succinic anhydride and diethylenetriamine. b. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at nevnte polymer av umettet hydrokarbon har en molekylvekt fra b50 til 2600. Fuel as stated in one or more of the above claims, characterized in that said polymer of unsaturated hydrocarbon has a molecular weight from b50 to 2600. 9. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at nevnte polymer av et umettet hydrokarbon er oppbygget fra C, - C^-olefiner. 9. Fuel as stated in one or more of the above claims, characterized in that said polymer of an unsaturated hydrocarbon is built up from C1 - C2 olefins. 10. Drivstoff som angitt i et eller flere av de ovenstående krav, karakterisert ved at nevnte polymer av umettet hydrokarbon er et polypropylen.10. Fuel as stated in one or more of the above claims, characterized in that said polymer of unsaturated hydrocarbon is a polypropylene.
NO04199/70*[A 1969-11-06 1970-11-04 NO129635B (en)

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