Classifications

• • 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
  • C10L1/16—Hydrocarbons
• • 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
  • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
  • C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
• • 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
  • C10L1/16—Hydrocarbons
  • C10L1/1608—Well defined compounds, e.g. hexane, benzene
• • 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
  • C10L1/16—Hydrocarbons
  • C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
• • 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
  • C10L1/16—Hydrocarbons
  • C10L1/1625—Hydrocarbons macromolecular compounds
  • C10L1/1633—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
  • C10L1/1641—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
• • 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
  • C10L1/1817—Compounds of uncertain formula; reaction products where mixtures of compounds are obtained

Definitions

• the present invention provides a method of operating a four-stroke spark-ignition internal combustion engine fueled by gasoline compositions.
• base oils as carrier fluids for fuel additives.
• WO 97/41092 A1 discloses alkoxy acetic acid derivatives and their incorporation in additive concentrates and fuel compositions for internal combustion engines.
• the carrier fluids disclosed in WO 97/41092 A1 include hydrocarbon based materials such as polyisobutylenes (PIB's), polypropylenes (PP's) and polyalphaolefins (PAO's), all of which may be hydrogenated or unhydrogenated but are preferably hydrogenated; polyether based materials such as polybutylene oxides (poly BO's), polypropylene oxides (poly PO's), polyhexadecene oxides (poly HO's) and mixtures thereof (i.e.
• a particularly prepared carrier fluid disclosed in WO 97/41092 A1 comprises a combination of a polyalphaolefin having a viscosity at 100° C. in the range 2 ⁇ 10 ⁇ 6 to 2 ⁇ 10 ⁇ 5 m 2 /s (2 to 20 cSt) being a hydrogenated oligomer containing 18 to 80 carbon atoms derived from at least one alphaolefinic monomer containing from 8 to 16 carbon atoms, and a polyoxyalkylene compound selected from glycols, mono- and diethers thereof, having number average molecular weight (M n ) in the range 400 to 3000, the weight ratio polyalphaolefin:polyoxyalkylene compound being in the range 1:10 to 10:1.
• M n number average molecular weight
• the carrier concentration in the final fuel composition of WO 97/41092 A1 is described as up to about 1000 ppm weight, with a stated preference for concentrations of from about 50 ppm by weight to about 400 ppm by weight, based on the total weight of the fuel composition.
• WO 97/41092 A1 does not disclose any beneficial effects, in particularly in terms of improved acceleration response, associated with any of the carrier fluids disclosed therein.
• WO 03/068895 A1 discloses a gasoline composition comprising a major amount of a gasoline suitable for use in a spark ignition engine; 5 to 1000 ppmw, based on total composition, of a fatty acid salt of an alkoxylated oligoamine of general formula I
• each moiety A independently represents an alkylene group of 2 to 8 carbon atoms
• each moiety R independently represents a C 7-23 alkyl or singly or multiply-unsaturated C 7 to C 23 alkenyl group, optionally substituted by one or more —OH groups
• each moiety Z independently represents a C 1-8 alkylene group, a C 3-8 cycloalkylene group, or a C 6-12 arylene or arylalkylene group
• m represents 0 or an integer in the range 1 to 5
• the total of all variables x has a value of 50% to 300% of (m+3)
• 600 to 2000 ppmw based on total composition, of a co-additive selected from the group consisting of (a) a nitrogen-containing detergent containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000, (b) a polyalphaolefin having a viscosity at 100° C.
• the fatty acid salt of an alkoxylated oligoamine incorporated in the gasoline composition disclosed in WO 03/068895 A1 is described as a friction modifier.
• WO 03/068895 A1 discloses enhanced acceleration performance of a spark-ignition engine from the use of fatty acid salt of an alkoxylated oligoamine in combination with a co-additive incorporated in a gasoline composition, however, WO 03/068895 A1 does not disclose any beneficial effects, in particularly in terms of improved acceleration response, associated with the use of any of the co-additives disclosed therein.
• the present invention provides a method of operating a four-stroke spark-ignition internal combustion engine comprising introducing into a combustion chamber of said engine a gasoline composition comprising:
• the gasoline composition for use in a four-stroke spark-ignition internal combustion engine used in the present invention comprises:
• the gasoline may be any gasoline suitable for use in an internal combustion engine of the spark-ignition (petrol) type known in the art.
• the gasoline used in the gasoline composition of the present invention i.e. component (a) above
• base gasoline may conveniently also be referred to as ‘base gasoline’.
• Gasolines typically comprise mixtures of hydrocarbons boiling in the range from 25 to 230° C. (EN-ISO 3405), the optimal ranges and distillation curves typically varying according to climate and season of the year.
• the hydrocarbons in a gasoline may be derived by any means known in the art, conveniently the hydrocarbons may be derived in any known manner from straight-run gasoline, synthetically-produced aromatic hydrocarbon mixtures, thermally or catalytically cracked hydrocarbons, hydro-cracked petroleum fractions, catalytically reformed hydrocarbons or mixtures of these.
• the specific distillation curve, hydrocarbon composition, research octane number (RON) and motor octane number (MON) of the gasoline are not critical.
• the research octane number (RON) of the gasoline may be in the range of from 80 to 110, preferably from 90 to 105, more preferably from 93 to 102, most preferably from 94 to 100 (EN 25164);
• the motor octane number (MON) of the gasoline may suitably be in the range of from 70 to 110, preferably from 75 to 105, more preferably from 80 to 100, most preferably from 84 to 95 (EN 25163).
• gasolines comprise components selected from one or more of the following groups; saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and oxygenated hydrocarbons.
• the gasoline may comprise a mixture of saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and, optionally, oxygenated hydrocarbons.
• the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 40 percent by volume based on the gasoline; preferably, the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 30 percent by volume based on the gasoline.
• the aromatic hydrocarbon content of the gasoline is in the range of from 0 to 70 percent by volume based on the gasoline; preferably, the aromatic hydrocarbon content of the gasoline is in the range of from 10 to 60 percent by volume based on the gasoline.
• the benzene content of the gasoline is at most 10 percent by volume, more preferably at most 5 percent by volume, especially at most 1 percent by volume based on the gasoline.
• the saturated hydrocarbon content of the gasoline is at least 40 percent by volume based on the gasoline; preferably, the saturated hydrocarbon content of the gasoline is in the range of from 40 to 80 percent by volume based on the gasoline.
• the gasoline preferably has a low or ultra low sulphur content, for instance at most 1000 ppmw (parts per million by weight), preferably no more than 500 ppmw, more preferably no more than 100, even more preferably no more than 50 and most preferably no more than even 10 ppmw.
• the gasoline also preferably has a low total lead content, such as at most 0.005 g/l, most preferably being lead free—having no lead compounds added thereto (i.e. unleaded).
• the gasoline comprises oxygenated hydrocarbons
• at least a portion of non-oxygenated hydrocarbons will be substituted for oxygenated hydrocarbons.
• the oxygen content of the gasoline may be up to 35 percent by weight (e.g. ethanol per se) based on the gasoline.
• the oxygen content of the gasoline may be up to 25 percent by weight, preferably up to 10 percent by weight.
• suitable ranges of oxygen content of the gasoline are from 0 to 5 percent by weight, preferably from 1.0 to 3.5 percent by weight, and more preferably from 1.2 to 2.7 percent by weight.
• oxygenated hydrocarbons examples include alcohols, ethers, esters, ketones, aldehydes, carboxylic acids and their derivatives, and oxygen containing heterocyclic compounds.
• the oxygenated hydrocarbons that may be incorporated into gasolines are selected from alcohols (such as methanol, ethanol, propanol, iso-propanol, butanol, tert-butanol and iso-butanol) and ethers (preferably ethers containing 5 or more carbon atoms per molecule, e.g., methyl tert-butyl ether), a particularly preferred oxygenated hydrocarbon is ethanol.
• the amount of oxygenated hydrocarbons in gasoline may vary over a wide range.
• gasolines comprising a major proportion of oxygenated hydrocarbons are currently commercially available in countries such as Brazil and U.S.A, e.g. ethanol per se and E85, as well as gasolines comprising a minor proportion of oxygenated hydrocarbons, e.g. E10.
• Gasolines may contain up to 100 percent by volume oxygenated hydrocarbons.
• the amount of oxygenated hydrocarbons present in gasoline is selected from one of the following amounts: up to 85 percent by volume; up to 65 percent by volume; up to 30 percent by volume; up to 20 percent by volume; up to 15 percent by volume; and, up to 10 percent by volume, depending upon the desired final formulation of the gasoline.
• the gasoline may contain at least 0.5, 1.0 or 2.0 percent by volume oxygenated hydrocarbons.
• gasolines which have an olefinic hydrocarbon content of from 0 to 20 percent by volume (ASTM D1319), an oxygen content of from 0 to 5 percent by weight (EN 1601), an aromatic hydrocarbon content of from 0 to 50 percent by volume (ASTM D1319) and a benzene content of at most 1 percent by volume.
• the base oil admixed with the gasoline in the present invention can be any base oil, or mixture of base oils, having a kinematic viscosity at 100° C. of at least 1 cSt.
• the base oil admixed with the gasoline in the present invention is a liquid hydrocarbon base oil.
• liquid hydrocarbon base oil it is meant a base oil which is comprised essentially of compounds consisting of carbon and hydrogen.
• the liquid hydrocarbon base oil will contain less than 10 wt % of compounds containing elements other than carbon and hydrogen, more typically less than 5 wt %, most typically less than 3 wt % of compounds containing elements other than carbon and hydrogen.
• the kinematic viscosity at 100° C. of the base oil admixed with the gasoline in the present invention accords with one of parameters (i) to (ix) below, or a combination of one of parameters (i) to (v) and one of parameters (vi) to (ix):—
• Ranges having a combination of any feature selected from (i) through (v) above and any feature selected from (vi) through (ix) above are particularly applicable in the present invention.
• Examples of specific combinations of the above features include (i) and (vi), (ii) and (vii), (iii) and (viii), (iv) and (ix), and (v) and (ix), respectively being progressively more preferred.
• the base oil having a kinematic viscosity at 100° C. of at least 1 cSt will have a viscosity index (VI) (ASTM D 2270) of at least 80. More typically, the base oil having a kinematic viscosity at 100° C. of at least 1 cSt will have a VI of at least 85, conveniently the base oil will have a VI of at least 90 or even at least 95.
• the VI of the base oil may be at least 100, for instance at least 110 or even at least 120.
• the VI of the base oil will be at most 300, more typically at most 250; conveniently, the VI of the base oil may be at most 200.
• the boiling point of the base oil is not critical, however, typically the boiling point will be at least 260° C., more typically at least 300° C.
• Any base oil or mixture of base oils having a kinematic viscosity at 100° C. of at least 1 cSt known in the art may be used in the gasoline composition of the present invention.
• conventional known mineral oils and synthetic oils or mixtures of one or more mineral oils and/or one or more synthetic oils may be used.
• Mineral oils include liquid petroleum oils and solvent-treated or acid-treated mineral lubricating oil of the paraffinic, naphthenic, or mixed paraffinic/naphthenic type which may be further refined by hydrofinishing processes and/or dewaxing.
• Naphthenic base oils have low viscosity index (VI) (generally 40-80) and a low pour point. Such base oils are produced from feedstocks rich in naphthenes and low in wax content.
• Paraffinic base oils have higher VI (generally >95) and a high pour point. Said base oils are produced from feedstocks rich in paraffins.
• Synthetic processes enable molecules to be built from simpler substances or to have their structures modified to give the precise properties required.
• Synthetic base oils include hydrocarbon oils such as olefin oligomers, and dewaxed waxy raffinate, and may also include non-hydrocarbon oils such as dibasic acid esters and polyol esters.
• An example of synthetic base oils that may be used are the synthetic hydrocarbon base oils sold by the Shell Group under the designation “XHVI” (trade mark).
• Base oils or mixtures of base oils derived from the product of a Fischer-Tropsch synthesis process may also be conveniently used as the base oil in the present invention; mixtures of base oils derived from the product of a Fischer-Tropsch synthesis process and one or more mineral oils and/or one or more synthetic oils may also be used in the present invention.
• Non-limiting examples of Fischer-Tropsch derived base oils are disclosed in EP-A-0776959, EP-A-0668342, WO-A-97/21788, WO-A-00/15736, WO-A-00/14188, WO-A-00/14187, WO-A-00/14183, WO-A-00/14179, WO-A-00/08115, WO-A-99/41332, EP-A-1029029, WO-A-01/18156 and WO-A-01/57166.
• the base oil admixed with the gasoline in the present invention is a base oil selected from a Group I to Group IV base oil (or base stock), or mixture thereof, having a kinematic viscosity at 100° C. of at least 1 cSt.
• Group I base oil base oil, “Group II” base oil, “Group III” base oil and “Group IV” base oil in the present invention are meant base oils according to the definitions of American Petroleum Institute (API) categories I, II, III and IV. Such API categories are defined in API Publication 1509, 15 th Edition, Appendix E, April 2002.
• API American Petroleum Institute
• Group I base oils contain less than 90% saturates (according to ASTM D2007) and/or greater than 0.03% sulphur (according to ASTM D2622, D4294, D4927 or D3120) and have a viscosity index of greater than or equal to 80 and less than 120 (according to ASTM D2270).
• Group II base oils contain greater than or equal to 90% saturates and less than or equal to 0.03% sulphur and have a viscosity index of greater than or equal to 80 and less than 120, according to the aforementioned ASTM methods.
• Group III base oils contain greater than or equal to 90% saturates and less than or equal to 0.03% sulphur and have a viscosity index of greater than 120, according to the aforementioned ASTM methods.
• Group IV base oils are polyalphaolefins (PAO).
• Group I to IV base oils used, and various conventional known Group I to IV base oils selected from mineral oils and synthetic lubricating oils may be conveniently used.
• the base oil admixed with the gasoline in the present invention can conveniently be a liquid hydrocarbon base oil derived from a mineral oil.
• the base oil, or at least part of the base oil, admixed with the gasoline in the present invention can also conveniently be a synthetically derived base oil, preferably a synthetically derived liquid hydrocarbon base oil. If at least part of the base oil admixed with the gasoline in the present invention is a synthetically derived base oil, the concentration of synthetically derived base oil in the base oil admixed with the gasoline is preferably selected from one of the following proportions: at least 50 wt %; at least 70 wt %; at least 90 wt %; at least 95 wt %; at least 98 wt %; at least 99 wt %; and, 100 wt %. Examples of “synthetically derived liquid hydrocarbon base oils” include polyalphaolefin (PAO) compositions and polyinternalolefin (PIO) compositions.
• PAO polyalphaolefin
• PIO polyinternalolefin
• the base oil admixed with the gasoline in the gasoline composition of the present invention is a synthetically derived base oil having a kinematic viscosity at 100° C. of at least 1 cSt per se.
• the volumetric balance of the base oil may conveniently be made up using any base oil or mixture of base oils known in the art, provided that the overall base oil has a kinematic viscosity at 100° C. of at least 1 cSt.
• conventional known mineral oils and base oils derived from the product of a Fischer-Tropsch synthesis process or mixtures of one or more mineral oils and/or one or more base oils derived from the product of a Fischer-Tropsch synthesis process may be used to make up the volumetric balance of the base oil.
• the base oil, or at least part of the base oil, admixed with the gasoline in the present invention can also be a base oil derived from the product of a Fischer-Tropsch synthesis process; preferably, when the base oil, or at least part of the base oil, admixed with the gasoline is a base oil derived from the product of a Fischer-Tropsch synthesis process, the base oil is a liquid hydrocarbon base oil.
• the concentration of the product of a Fischer-Tropsch synthesis process in the base oil admixed with the gasoline is preferably selected from one of the following proportions: at least 50 wt %; at least 70 wt %; at least 90 wt %; at least 95 wt %; at least 98 wt %; at least 99 wt %; and, 100 wt %.
• the base oil admixed with the gasoline in the gasoline composition of the present invention is a base oil derived from the product of a Fischer-Tropsch synthesis process having a kinematic viscosity at 100° C. of at least 1 cSt per se.
• the volumetric balance of the base oil may conveniently be made up using any base oil or mixture of base oils known in the art, provided that the overall base oil has a kinematic viscosity at 100° C. of at least 1 cSt.
• conventional known mineral oils and synthetic oils or mixtures of one or more mineral oils and/or one or more synthetic oils may be used to make up the volumetric balance of the base oil.
• the Fischer-Tropsch synthesis process converts carbon monoxide and hydrogen into longer chain, usually paraffinic, hydrocarbons:
• the carbon monoxide and hydrogen may themselves be derived from organic or inorganic, natural or synthetic sources, typically either from natural gas or from organically derived methane.
• the gases which are converted into liquid fuel components using such processes can in general include natural gas (methane), LPG (e.g. propane or butane), “condensates” such as ethane, synthesis gas (CO/hydrogen) and gaseous products derived from coal, biomass and other hydrocarbons.
• Typical catalysts for the Fischer-Tropsch synthesis of paraffinic hydrocarbons comprise, as the catalytically active component, a metal from Group VIII of the periodic table, in particular ruthenium, iron, cobalt or nickel. Suitable such catalysts are described for instance in EP-A-0 583 836 (pages 3 and 4).
• Fischer-Tropsch synthesis process from which the base oil may be derived is not critical and any Fischer-Tropsch synthesis process known in the art may be used.
• Fischer-Tropsch synthesis processes which can be used to prepare the above-described Fischer-Tropsch derived base oil are the so-called commercial Slurry Phase Distillate technology of Sasol, the Shell Middle Distillate Synthesis Process (SMDS) and the “AGC-21” Exxon Mobil process. These and other processes are, for example, described in more detail in EP-A-776 959, EP-A-668 342, US-A-4 943 672, US-A-5 059 299, WO-A-99/34917 and WO-A-99/20720.
• these Fischer-Tropsch synthesis products will comprise hydrocarbons having 1 to 100 and even more than 100 carbon atoms.
• the product of the Fischer-Tropsch synthesis process will contain saturated hydrocarbon products (normal, cyclic and/or iso-paraffins) and optionally may also comprise unsaturated hydrocarbon products and oxygenated hydrocarbon products, depending upon the specific Fischer-Tropsch process used.
• the base oil may be obtained directly from the Fischer-Tropsch synthesis process, or indirectly for instance by fractionation of a Fischer-Tropsch synthesis product or from a treated Fischer-Tropsch synthesis product.
• the treatment that may be applied to the Fischer-Tropsch synthesis product can be any hydrocarbon treatment known in the art. Examples of suitable treatments that may be performed on the Fischer-Tropsch synthesis product include hydrotreatment, hydrogenation, hydrocracking, hydroisomerization, polymerisation, alkylation, distillation, cracking-decarboxylation, isomerisation and hydroreforming, as described for instance in GB-2 077 289 B, EP-A-0 147 873, U.S. Pat. No. 4,125,566 and U.S. Pat. No. 4,478,955.
• the base oil derived from a Fischer-Tropsch synthesis process may be a base oil derived from the processes described in WO 2004/007647 A1 and US 2005/0098476 A1.
• a base oil derived from a Fischer-Tropsch synthesis process has essentially no (i.e. undetectable), or very low levels of, sulphur and nitrogen. Compounds containing these heteroatoms tend to act as poisons for Fischer-Tropsch catalysts and are therefore removed from the synthesis gas feed. Further, the process as usually operated produces no or very low levels of aromatic compounds.
• the concentration of the base oil admixed with the gasoline in the present invention will be in the range of from 0.1 to 5 wt %, based on the overall gasoline composition.
• the concentration, based on the overall gasoline composition, of the base oil admixed with the gasoline in the present invention accords with one of parameters (x) to (xix) below, or a combination of one of parameters (x) to (xiv) and one of parameters (xv) to (xix):—
• Ranges having a combination of any feature selected from (x) through (xiv) above and any feature selected from (xv) through (xix) above are particularly applicable in the present invention.
• Examples of specific combinations of the above features include (x) and (xv), (xi) and (xvi), (xii) and (xvii), (xiii) and (xviii), and (xiv) and (xix), respectively being progressively more preferred.
• the concentration, based on the overall gasoline composition, of the base oil admixed with the gasoline in the present invention may be at least 0.5 wt %.
• the concentration of the base oil admixed with the gasoline may be in the range of from 0.5 to 5.0 wt %, from 0.5 to 4.5 wt %, from 0.5 to 4.0 wt %, from 0.5 to 3.5 wt %, from 0.5 to 3.0 wt % or even from 0.5 to 2.5 wt %.
• the concentration, based on the overall gasoline composition, of the base oil admixed with the gasoline in the present invention may be at least 1.0 wt %.
• the concentration of the base oil admixed with the gasoline may be in the range of from 1.0 to 5.0 wt %, from 1.0 to 4.5 wt %, from 1.0 to 4.0 wt %, from 1.0 to 3.5 wt %, from 1.0 to 3.0 wt % or even from 1.0 to 2.5 wt %.
• the gasoline composition may conveniently additionally include one or more fuel additive.
• concentration and nature of the fuel additive(s) that may be included in the gasoline composition of the present invention is not critical.
• suitable types of fuel additives that can be included in the gasoline composition include anti-oxidants, corrosion inhibitors, detergents, dehazers, antiknock additives, metal deactivators, valve-seat recession protectant compounds, dyes, friction modifiers, carrier fluids, diluents and markers. Examples of suitable such additives are described generally in U.S. Pat. No. 5,855,629.
• the fuel additives can be blended with one or more diluents or carrier fluids, to form an additive concentrate, the additive concentrate can then be admixed with the gasoline.
• the one or more diluents or carrier fluids used is a base oil, in particular a liquid hydrocarbon base oil, having a kinematic viscosity at 100° C. of at least 1 cSt, the concentration of the base oil admixed with the gasoline to form the gasoline composition will be adjusted accordingly.
• the (active matter) concentration of any additives present in the gasoline or the gasoline composition is preferably up to 1 percent by weight, more preferably in the range from 5 to 1000 ppmw, advantageously in the range of from 75 to 300 ppmw, such as from 95 to 150 ppmw.
• a gasoline composition according to the present invention may be prepared by a process which comprises bringing into admixture with gasoline, from 0.1 wt % to 5 wt %, based on the overall gasoline composition, of a base oil having a kinematic viscosity at 100° C. of at least 1 cSt, and optionally other conventional gasoline components, such as one or more fuel additives.
• said fuel additives when one or more fuel additives are to be incorporated into the gasoline composition of the present invention, said fuel additives may be blended with the base oil having a kinematic viscosity at 100° C. of at least 1 cSt to form an additive concentrate containing the fuel additives at suitable concentrations to result in a gasoline composition having the desired concentration of the fuel additives when from 0.1 wt % to 5 wt %, based on the overall gasoline composition, of this additive concentrate is admixed with gasoline.
• gasoline compositions according to the present invention in a four-stroke spark-ignition internal combustion engine has provided an improvement in the acceleration response of the engine.
• improved in the acceleration response it is meant that a four-stroke spark-ignition internal combustion engine fueled with a gasoline composition according to the present invention takes less time to accelerate between two specific speeds (as determined by the rpm of the engine) than the same engine, operating under the same conditions, fueled using a gasoline composition comprising only the base gasoline (i.e. not containing a base oil having a kinematic viscosity at 100° C. of at least 1 cSt).
• the present invention also encompasses the use of a gasoline composition
• a gasoline composition comprising:
• the present invention provides a method of operating a four-stroke spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition as defined above.
• the base fuel used was an unleaded gasoline (95 ULG) of RON 95.1, MON 86.7, and having sulphur content (ASTM D 2622-94) of 8 ppmw, iso+normal paraffins content of 61.18% v/v, saturated naphthenes content of 6.49%, aromatics content of 28.35% v/v and olefins content of 3.81% v/v (as measured by Gas Chromatography), density at 15° C. (ISO 3675:93/D4052:91) 0.7307 kg/l, distillation (ISO 3405/88) IBP 39.2° C., 10% 56.6° C., 50% 93.2° C., 90% 139.8° C. and FBP 172.2° C.
• the n-hexadecane (99% purity) was supplied by Avocado Organics.
• the measured kinematic viscosity at 100° C. of the n-hexadecane was 1.10 mm 2 /s (ASTM D 445).
• “HVI-60” mineral base oil is a bright and clear high viscosity index mineral base oil having kinematic viscosity at 100° C. of 4.4 to 4.9 mm 2 /s (ASTM D 445), a minimum flashpoint of 204° C. (ASTM D 93) and pour point of ⁇ 12 to ⁇ 15° C. (ASTM D 97).
• Shell “XHVI-8” (trade mark) base oil is a bright and clear product from the Shell “XHVI” (trade mark) synthesis process, having a kinematic viscosity at 100° C. of 7.8 to 8.5 mm 2 /s (ASTM D 445), a minimum flashpoint of 210° C. (ASTM D 93) and a pour point of ⁇ 15° C. (ASTM D 97).
• “HVI-160” mineral base oil is a bright and clear high viscosity index mineral base oil having kinematic viscosity at 100° C. of 10.7 to 11.8 mm 2 /s (ASTM D 445), a minimum flashpoint of 228° C. (ASTM D 93) and pour point of ⁇ 9° C. (ASTM D 97).
• the High viscosity GtL base oil is a Fischer-Tropsch derived base oil having a kinematic viscosity at 100° C. of 19.0 mm 2 /s (ASTM D 445), a viscosity index of approximately 170, a flashpoint of 247.5° C. (ASTM D 93) and a pour point of ⁇ 30° C. (ASTM D 5950).
• “HVI-650” mineral base oil is a bright and clear high viscosity index mineral base oil having kinematic viscosity at 100° C. of 30.5 to 34.2 mm 2 /s (ASTM D 445), a minimum flashpoint of 267° C. (ASTM D 93) and pour point of ⁇ 6° C. (ASTM D 97).
• PAO-40 synthetic base oil known as Spectrasyn (trade mark) Polyalphaolefin (PAO) 40, was supplied by ExxonMobil Chemical, and has a kinematic viscosity at 100° C. of 39 cSt, a flashpoint of 281° C., and a pour point of ⁇ 36° C.
• V k 100 of the Base Oils Component added to fuel
• V k 100 Hexadecane 1.10 HVI-60 mineral base oil 4.65 Shell XHVI-8 base oil 8 HVI-160 mineral base oil 11.25 High viscosity GtL base oil 19 HVI-650 mineral base oil 32 PAO-40 synthetic base oil 39
• the acceleration benefit of the fuels of Table 1 was measured using a four-stroke bench engine.
• the four-stroke bench engine used was a Ford Zetec 2.0 litre in-line 4 cylinder, 16-valve, multipoint fuel injection, spark-ignition engine and an MT-75 gearbox, with electronic port fuel injection and mapped ignition system (EEC4).
• EEC4 electronic port fuel injection and mapped ignition system
• PAS Power Assisted Steering
• the FM (Friction Modifier) acceleration test comprised a warm-up/stabilization (of dynamometer load, acceleration times, and engine/test cell temperatures) and then an acceleration test stage where a Base (reference) fuel is tested against a candidate fuel.
• the continuous test sequence is divided into distinct phases as follows: “Base run #1”, “Base run #2”, “Test fuel run”, “Base run #3”.
• acceleration cycles are run continuously throughout all the test phases, including fuel changes and flushing.
• Engine oil, coolant and air intake temperatures, together with ambient conditions such as barometric air pressure and humidity are measured and monitored during the test, since these parameters can have an immediate and significant effect on acceleration test, which can be accounted for.
• the details of the testing phase are as follows: The operator will conduct the test, starting the test using the base (reference) fuel and allow a minimum of:
• Test run consists of a minimum of 45 accelerations per fuel. Each candidate test fuel is tested in triplicate. The fuels were tested in a randomised order.
• Tm1 the time taken for the engine to accelerate from 2010 to 4000 rpm
• Tm3 the time taken for the engine to accelerate from 2300 rpm to 4000 rpm
• each test fuel was run through the test three times, and the test order of the different fuels was randomised. If Tm1 and Tm3 are less for the test fuel compared to the base fuel, then the test fuel gives an acceleration benefit.
• Tables 3 and 4 summarise the results from these tests, giving the value of Tm1 and Tm3 for each run of the test fuels, and also gives the average value of these parameters for each of the candidate (test) fuels.
• the results reported in Tables 3 and 4 give the acceleration benefit of the candidate (test) fuels of the present invention in terms of percentage improvement in acceleration performance over the base fuel.

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