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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
  • 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

Definitions

• This invention relates to hydrocarbon fuels and more particularly to hydrocarbon fuels having a reduced tendency to form an explosive mist when subjected to shock.
• Patent 3,996,02 issued to Osmond et al discloses the use of copolymers of ethylenically unsaturated hydrocarbons such as isobutylene, butadiene, isoprene and mixtures of ethylene and propylene. This patent also discloses that higher olefins such as pentene, hexene and higher homologs may be included in the polymer but relies that these olefins tend to reduce the chain length to weight ratio.
• Patent 4,356,003 issued to Brooks et al, discloses the use of terpolymers of tertiary butylstyrene, methacrylic acid and a third monomer selected from acrylic and methacrylic esters of aliphatic monohydric alcohols, acrylonitrile, vinyl acetate, styrene and vinyl toluene.
• European Patent Application publication number 0,019,390 issued to Brooks et al, also discloses a terpolymer of tertiary butylstyrene, acrylic and methacrylic esters of aliphatic monohydric alcohols and methacrylic acid as a polymeric additive for aviation fuels.
• Patent 4,289,679 issued to Mack, discloses the preparation of homopolymers and copolymers of alpha-monoolefins. This patent states that these polymers are useful as antimist agents for fuels. These patents show the considerable effort that has been put into research to find additives for fuels which will reduce or eliminate the tendency of the fuel to form a mist when subjected to a shock, and yet will not adversely effect the other desirable properties of a fuel, such as low temperature pumpability. Although some of the above described polymeric materials are effective in reducing the misting tendency of fuels, none of them is completely satisfactory from an overall standpoint. There is a continuing need for improved fuel antimisting agents.
• the present invention discloses high molecular weight polymeric fuel antimist additives which have superior antimisting properties. Accordingly, it is an object of the invention to present novel antimisting agents for hydrocarbon fuels. It is another object of the invention to present high molecular weight polymeric materials which effectively reduce the tendency of hydrocarbon fuels to form an explosive mist upon impact. It is another object of the invention to present a method of reducing the tendency of hydrocarbon fuels to form explosive mists upon impact. It is another object of the invention to present aircraft fuels which resist the tendency to form explosive mists when subjected to shock.
• the benefits of the invention are realized by incorporating into a hydrocarbon fuel small amounts of a high molecular weight copolymer of butene-1 and at least one other alpha-monoolefin having 5 or more carbon atoms.
• the molecular weight of the copolymer is at least 500,000 and most pre- ferrably is in the range of about 1 to 20 million.
• concentration of the copolymer in the hydrocarbon fuel is in the range of about 0.001 to 5 percent and more preferably about 0.01 to 2 percent based on the total.weight of hydrocarbon fuel composition.
• Preferred copolymers are those of butene-1 and at least one alpha-monoolefin having 5 to 20 carbon atoms and most pre- ferrably 6 to 14 carbon atoms.
• copolymers of the invention are comprised of butene-1 and at least one other alpha-monoolefin having 5 or more carbon atoms.
• Preferred copolymers are those of butene-1 and at least one other alpha-monoolefin having 5 to 20 carbon atoms.
• alpha-monoolefins having more than about 20 carbon atoms can be used in the invention, those having 20 or fewer carbon atoms are preferred due to their commercial availability.
• the polymeric compositions of the invention are prepared from butene-1 and one or more higher alpha-monoolefins.
• a two alpha-monoolefin component system When a two alpha-monoolefin component system is employed the butene-1 and the other alpha-monoolefin component are usually present in the reaction mixture in an amount sufficient to produce a copolymer containing at least 10 mole percent of each component. In the preferred embodiments of the two alpha-monoolefin component system each component is present in an amount sufficient to produce copolymers containing 25 or more mole percent of each component.
• the maximum content of any one monomer is 90 mole percent and most preferably 75 mole percent, based on the total number of moles of butene-1 and the other alpha-monoolefin monomers present in the reaction mixture.
• Typical copolymers which are usable in the invention are those prepared from butene-1 and one or more of hexene-1, octene-1, decene-1, dodecene-1, hexadecene-1, eicosene-1, etc.
• Preferred copolymers are those prepared from butene-1 and one or more of hexene-1, octene-1, decene-1, dodecene-1, tetradecene-1, etc.
• copolymers examples include butene-l-hexene-1 copolymer, butene-l-octene-1 copolymer, butene-1-decene-1 copolymer, butene-1-dodecene-1 copolymer and butene-1-tetradecene copolymer.
• Preferred terpolymers include butene-l-hexene-l-decene-1 terpolymer, butene-1-octene-1-dodecene-1 terpolymer, etc.
• the copolymers of the invention desirably have a weight average molecular weight of at least 500,000 and are generally in the range of 500,000 to 20 million. There is no upper molecular weight limit and polymers having any weight average molecular weight above about 500,000 are usable. At the lower end of the scale polymers having weight average molecular weight significantly below about 500,000 are not as desirable as those having weight average molecular weight of at least 500,000. In a preferred embodiment the weight average molecular weight is in the range of about 1 to 20 million.
• the method of polymerization of the monomers is not a part of the invention.
• any of the several well known methods for polymerizing alpha-monoolefins can be employed.
• a particularly suitable method is the Z iegler process using catalyst systems comprising combinations of a compound of a metal of Groups IV-B, V-B, VI- B or VIII of the Periodic Chart of the Elements found on pages 392-393 of the Handbook of Chemistry and Physics, 37th Edition with an organometal compound of a rare earth or metal from Groups I-A, II-A, or III-A of the Periodic Chart of the Elements.
• Particularly suitable catalyst systems are those comprising titanium halides and organoaluminium compounds.
• a typical polymerization procedure is to contact the monomeric mixture with the catalyst in a suitable inert hydrocarbon solvent for the monomers and the catalyst in a closed reaction vessel at reduced temperatures and autogenous pressure and in a nitrogen atmosphere. Further details of the Ziegler process are set forth in U.S. Patent 3,692,676, which is incorporated herein by reference.
• the hydrocarbon fuels in which the copolymer of the invention may be used include kerosene, jet fuel, naphtha, gasoline, etc.
• the copolymers are particularly effective in jet aviation fuels such as grade JP-8, specified in U.S. Military Specification MIL-T-83133, grade JP-5 (flash point 140°F minimum) as specified in U.S. Military Specification MIL-T-5624G, grades Jet A and Jet A-1 (flash point 110°F minimum) as specified in U.S. Military Specification MIL-T-D1655/66T, etc.
• the copolymer is added to the hydrocarbon fuel at a concentration which is effective to eliminate or substantially reduce the tendency of the hydrocarbon fuel* to form a highly explosive mist upon being subjected to shock. In general, this is accomplished by incorporating the copolymer into the hydrocarbon fuel at a concentration of about .001 to 5 percent based on the total weight of hydrocarbon fuel composition.
• the preferred concentration of copolymer in the hydrocarbon fuel composition is in the range of about .01 to 2 percent based on the total weight of the hydrocarbon fuel composition.
• the concentration of copolymer in the hydrocarbon fuel which produces the optimum result will vary depending on the particular comonomers from which the copolymer is prepared, the molecular weight of the copolymer and the hydrocarbon fuel being treated.
• Other fuel additives can be used in combination with the copolymers in the invention. For example, corrosion inhibitors, antioxidants, etc. can be added to the hydrocarbon fuel formulation, as desired.
• the copolymer in the desired concentration is dissolved in the hydrocarbon fuel. This can be accomplished by adding the copolymer directly to the fuel or by adding a solution of the copolymer and a compatible hydrocarbon solvent to the hydrocarbon fuel. Upon addition of the copolymer to the hydrocarbon fuel, the mixture is agitated sufficiently to completely dissolve the copolymer in the hydrocarbon fuel. This can be easily accomplished, as the copolymers are readily soluble in hydrocarbon fuels.
• Untreated Jet A fuel was tested according to the above procedure at a fuel spillage rate of 20 gallons per second and at a relative air velocity of 130 knots. A huge fireball formed and propagated against the flow of air to the most forward point in the fuel stream.
• Example I The test of Example I was repeated using Jet A fuel containing 0.1 weight percent of a butene-l-dodecene-1 copolymer having an inherent viscosity of 13.0 dl/g.
• the modified fuel did form an ignitable mist. Small fire- balls formed but self-extinguished before contacting the ground. There was little or no tendency of the ignited fuel to propagate toward the ignition source..
• Example II The procedure of Example II was repeated except that the air speed was 120 knots. The fuel had no propensity to ignite.

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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)
• Liquid Carbonaceous Fuels (AREA)

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Citations (2)

• 1984
  • 1984-10-09 EP EP84306890A patent/EP0177649A1/fr not_active Withdrawn

Patent Citations (2)

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