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
  • C10L1/18—Organic compounds containing oxygen
  • C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
  • C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
  • C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
• • 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
  • C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
  • C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only 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 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
  • C10L1/1608—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 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
  • C10L1/1616—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 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
  • C10L1/22—Organic compounds containing nitrogen
  • C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
  • C10L1/223—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond having at least one amino group bound to an aromatic carbon atom
• • 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
  • C10L10/00—Use of additives to fuels or fires for particular purposes
  • C10L10/10—Use of additives to fuels or fires for particular purposes for improving the octane number
• • 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
  • C10L2200/00—Components of fuel compositions
  • C10L2200/02—Inorganic or organic compounds containing atoms other than C, H or O, e.g. organic compounds containing heteroatoms or metal organic complexes
  • C10L2200/0259—Nitrogen containing compounds
• • 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
  • C10L2200/00—Components of fuel compositions
  • C10L2200/04—Organic compounds
  • C10L2200/0407—Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
  • C10L2200/0415—Light distillates, e.g. LPG, naphtha
• • 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
  • C10L2200/00—Components of fuel compositions
  • C10L2200/04—Organic compounds
  • C10L2200/0407—Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
  • C10L2200/0453—Petroleum or natural waxes, e.g. paraffin waxes, asphaltenes
• • 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
  • C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
  • C10L2230/22—Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency
• • 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
  • C10L2270/00—Specifically adapted fuels
  • C10L2270/02—Specifically adapted fuels for internal combustion engines
  • C10L2270/023—Specifically adapted fuels for internal combustion engines for gasoline engines

Definitions

• Aromatic hydrocarbons are manufactured from hydrogen rich paraffins and naphthenic molecules found in naphtha by a catalytic reforming process.
• the catalytic reforming process yields a product commonly referred to as “reformate” which has a significantly higher anti-knock index (AKI) value (R+M/2).
• AKI anti-knock index
• Use of catalytic reformers contribute to carbon dioxide emission in four fundamental ways. First, it raises the carbon intensity of the fuel by removing hydrogen from the paraffins and naphthenic molecules to produce the aromatics.
• the blended gasoline composition comprises: • an aromatic amine selected from the group consisting of m-toluidine, p-toluidine, o- toluidine and aniline as well as mixtures of the identified compounds in concentrations ranging from about 0.1% to about 5% by volume;
• blended gasoline composition formulated to reduce emissions of carbon.
• the blended gasoline composition comprises:
• an aromatic amine selected from the group consisting of m-toluidine, p-toluidine, o- toluidine and aniline as well as mixtures of the identified compounds in concentrations ranging from about 0.1% to about 5% by volume;
• the disclosed blended gasoline composition is substantially free of aromatic compounds.
• the following disclosure provides a blended gasoline composition suitable for use in over the road vehicles and off road vehicles.
• the disclosed blended gasoline composition is compatible with all current versions of gasoline intended for use in over the road vehicles and off road vehicles. Additionally, the disclosed blended gasoline composition can be distributed without significant modification to the current fuel distribution system. As will be described in more detail below, the disclosed blended gasoline composition produces significantly lower carbon dioxide emissions than currently available versions of gasoline. As a further benefit, the disclosed blended gasoline composition, when compared to currently used gasoline compositions, has energy values equal to or better than the current gasoline compositions due to their higher paraffinic content.
• the disclosed blended gasoline composition achieves the reduction in carbon dioxide emissions by substantially eliminating aromatic compounds from the formulation of the blended gasoline composition.
• the target maximum concentration of aromatic compositions within the blended gasoline composition is less than 15% by volume, not including aromatic amines. More typically, the blended gasoline composition will have less than 10% aromatic content, not including aromatic amines. Even more typically, the blended gasoline composition will have less than 5% aromatic content, not including aromatic amines. Preferably, the blended gasoline composition will have 0% aromatic content, not including aromatic amines.
• the disclosed blended gasoline composition also reduces emissions by limiting the amount of olefins, also known as alkenes, in the composition.
• the blended gasoline composition will have less than 10% by volume olefins. More typically, the blended gasoline composition will have less than 8% olefin content. More commonly, the blended gasoline composition will have less than 5% olefin content. Preferably, the blended gasoline composition will have 0% olefin content.
• the disclosed blended gasoline composition includes a base fuel blend of hydrocarbons as commonly produced by most refineries.
• the base fuel blend contains hydrocarbons having chain lengths as commonly produced by refinery units such as hydrocrackers, isomerization units, alkylation units, hydrodesulfurization units, and optionally fluid catalytic cracker units and optionally reformers.
• refinery units such as hydrocrackers, isomerization units, alkylation units, hydrodesulfurization units, and optionally fluid catalytic cracker units and optionally reformers.
• alkylate, reformate, FCCU gasoline, isomerate and naphtha may be included in the base fuel blend.
• Such units typically produce hydrocarbons having chains lengths of about four carbon atoms to about 12 carbon atoms (C4 to C12). More typically, the base fuel blend will have from five carbon atoms to 12 carbon atoms (C5 to C12).
• Such hydrocarbons include, but are not limited to, paraffins, olefins, naphthene and aromatic hydrocarbons.
• the olefin and aromatic constituents are preferably of limited concentrations or eliminated.
• the base fuel blend will make up about 70% to about 90% by volume of the total blended gasoline composition.
• CBOB stands for conventional blend stock for oxygenated blending.
• RBOB stands for reformulated blend stock for oxygenated blending.
• CARBOB stands for California reformulated blend stock for oxygenate blending.
• the base fuel blend will have a PONA distribution that is different from current base fuels.
• the ratio of paraffins, olefins, naphthene and aromatics is known as the fuels PONA.
• Typical base fuels have PONA’s as follows:
• the base fuel blend used in the present blended gasoline composition has a distinctly different PONA distribution as follows:
• gasoline compositions frequently add ethanol to the base fuel in order to achieve the desired final AKI value.
• Current fuels utilize 0-10% by volume ethanol in the final blend.
• the blended gasoline composition of the present invention utilizes from about 10% to about 20% by volume ethanol in the final blend.
• the blended gasoline composition further reduces the release of non-renewable carbon into the atmosphere.
• paraffins have the highest energy content per pound.
• maximizing the paraffins in the blended gasoline composition has the effect of decreasing the amount of fuel required to produce the same energy release as currently available gasolines.
• removal of the aromatics and olefin content and increasing the paraffin content advantageously raises the hydrogen to carbon ratio of the blended gasoline composition while also taking advantage of the octane blending synergy of paraffins and ethanol.
• the blended gasoline composition also includes between about 10% and about 20% ethanol. Typically, the blended gasoline composition contains between about 10% and 15% ethanol. Additionally, the blended gasoline composition contains an octane booster in the form of an aromatic amine. Suitable aromatic amines included, but are not limited to: aniline, m-toluidine, o-toluidine, p-toluidine and mixtures thereof. Typically, the blended gasoline composition contains up to 5% by volume of the octane booster. More commonly, the blended gasoline composition contains up to 4% by volume of the octane booster.
• the blended gasoline composition contains about 3% by volume of the octane booster. More typically the blended gasoline composition contains about 2% by volume of the octane booster. In most instances, the octane booster is m-toluidine at a concentration of about 1% to about 4% by volume.
• refineries may blend several feed streams together.
• true octane numbers do not blend linearly.
• some octane boosters have a generally known value when combined with current base fuel blends the octane value of boosters may vary depending on the composition of the selected base fuel blend.
• the final octane value of the resulting blend will be determined by conventional laboratory testing methods.
• the ethanol component will be added following the addition of the aromatic amine.
• the fuel had an octane value of RON 73.3.
• 15% ethanol was added by volume to the fuel having the RON of 73.3 to increase the octane value to a lab tested RON of 84.4.
• the sequence of blending will likely be the initial formulation of a base fuel followed by the addition of an aromatic amine.
• the aromatic amine will likely be added at the refinery to create the CBOB, RBOB and CARBOB base blends.
• ethanol will be added at an appropriate point in the distribution system to achieve the final desired AKI value.
• the blended gasoline composition may have the following components:
• an aromatic amine selected from the group consisting of m-toluidine, p-toluidine, o-toluidine and aniline as well as mixtures of the identified compounds in concentrations ranging from 0.1% to 5% by volume;
• CBOB, RBOB or CARBOB type refinery product in concentrations up to 90% provided that the CBOB, RBOB or CARBOB material meets the specifications for aromatics and olefins as defined above.
• a desired formulation will substantially lower or eliminate aromatic and olefin content providing a blended gasoline composition having the following components:
• an aromatic amine selected from the group consisting of m-toluidine, p-toluidine, o-toluidine and aniline as well as mixtures of the identified compounds in concentrations ranging from 0.1% to 5% by volume;
• CBOB, RBOB or CARBOB type refinery product in concentrations up to 86% provided that the CBOB, RBOB or CARBOB material meets the specifications for aromatics and olefins as defined above.
• a particularly desired formulation will eliminate aromatic and olefin content providing a blended gasoline composition having the following components:
• an aromatic amine selected from the group consisting of m-toluidine, p-toluidine, o-toluidine and aniline as well as mixtures of the identified compounds in concentrations ranging from 0.1% to 5% by volume; • ethanol in concentrations between 10% and 20%;
• CBOB, RBOB or CARBOB type refinery product in concentrations up to 86% provided that the CBOB, RBOB or CARBOB material meets the specifications for aromatics and olefins as defined above.
• the blended gasoline composition will contain 2% - 4% m- toluidine and ethanol at concentrations between 10% and 15% while being free of other aromatic compounds and free of olefins.
• Table 1 compares the non-amine aromatic content of a commonly available winter gasoline formulation to the non-amine aromatic content of the disclosed blended gasoline composition.
• Table 1 also demonstrates the reduction of non-amine aromatic content when the disclosed blended gasoline composition is combined in a 50:50 mixture with the same winter gasoline formulation.
• Table 1 also demonstrates that the disclosed blended gasoline composition is miscible with currently available gasolines and the corresponding mixture of currently available winter or summer gasoline can be blended with the disclosed blended gasoline composition for distribution as a final gasoline composition for use by consumers.
• the blended gasoline composition is characterized as having an AKI of at least 87. While an AKI of 87 is the minimum for the blended gasoline composition, manipulation of the base fuel blend, the octane booster and ethanol content may provide higher AKI values up to about 100 when blending 20% ethanol, 5% m-toluidine and 75% CBOB. Additionally, Table 2 reflects the ability of the blended gasoline composition to satisfy the API specific gravity and RVP values for winter and summer blends.
• a further characteristic of the disclosed blended gasoline composition is the ability of this composition to safely blend with current gasoline stocks.
• Table 4 demonstrates the environmental improvements provided by use of the blended gasoline composition in replace of current winter and summer gasoline blends of available gasoline.
• the table provides data based on an annual gasoline consumption (2019) of 150 billion gallons per year.
• gasoline is typically sold in Winter and Summer gasolines.
• Table 4 compares the combined total for the assumed Winter and Summer gasolines to the disclosed blended gasoline composition prepared using paraffinic naphtha.
• Renewable fuels such as ethanol and renewable naphtha are considered carbon neutral.
• Renewable naphtha is obtained as a waste product from the manufacture of renewable diesel and/or renewable jet fuel.
• the biomass e.g . com and sugarcane
• the biomass used in preparation of the renewable fuels absorbs CO2 as it grows. The capture of CO2 during the growth of the biomass may offset the CO2 when the renewable fuel is burned.
• Tables 4-5 reflect the expected CO2 reduction provided by using the blended gasoline composition in lieu of currently available summer/winter gasolines after subtracting out the renewable carbon derived from the use of ethanol.
• the remaining non-ethanol hydrocarbons in the fuel blend are considered to be from fossil fuel, i.e. non-renewable hydrocarbons.
• Table 7 below reflects the formulation of the blended gasoline composition used in the test results of Tables 4-6.
• Table 8 below provides one example of the hydrocarbon distribution of naphtha suitable for use in the disclosed blended gasoline composition.
• a renewable naphtha having the same distribution of hydrocarbons is also suitable for use in the disclosed blended gasoline composition.
• naphtha includes both paraffins and naphthenes having carbon chains from C4 to C12 and traces of C13 and higher as described in Table 8.
• renewable naphtha is a biproduct of the manufacture of renewable diesel and renewable jet fuel/kerosene. Therefore, when using renewable naphtha, the resulting blended gasoline composition may have nearly a net zero carbon emission contribution for the reasons discussed above.
• the blended gasoline composition significantly reduces the release of carbon into the atmosphere. Comparing the carbon release attributed to the Winter Gasoline to that of the blended gasoline composition, the blended gasoline composition reduces carbon dioxide emission by 9.90% on an annual basis. Further, when comparing the Summer Gasoline to that of the blended gasoline composition, the blended gasoline composition reduces carbon dioxide emission by 14.56% on an annual basis. Additionally, the reduced reliance upon use of the catalytic reformer process will further reduce carbon dioxide emission.
• Table 5 provides further data on carbon and CO2 reductions resulting from the use of the blended gasoline composition.
• use of the blended gasoline composition is expected to reduce CO2 emissions by 12.75% simply due to changing the composition of the gasoline burned.
• Row I of Table 5 further demonstrates the savings in CO2 emissions due to use of the blended composition and includes the savings in CO2 emissions resulting from reduced dependency on the use of the catalytic reformation process. According to the data provided, the expected overall reduction in U.S. CO2 emissions is 2.68%.
• Table 6 below provides estimates reflecting the beneficial reduction in refinery operations resulting from use of the disclosed blended gasoline composition.
• Table 6 demonstrates that use of the blended gasoline composition should also lead to an overall reduction in refinery barrels per day processed. The reduction in refinery processing is a result of the overall lower requirement for the base fuel. Additionally, the use of the disclosed blended gasoline composition simplifies the composition of the base fuel as described in Table 8 below.
• the resulting carbon released into the atmosphere due to motor vehicle use of summer and winter current blends of gasoline is over 60 billion moles. This total includes carbon release due to operation of catalytic reformers in the refineries.
• the blended gasoline composition disclosed herein does not rely upon products prepared by the catalytic reformers, e.g. aromatic hydrocarbons.
• the blended gasoline composition contains minimal concentrations of aromatic compounds.
• use of reformate from the catalytic reformer can be eliminated such that the aromatic compounds in the blended gasoline composition result primarily from naturally occurring aromatics in the crude oil.
• Table 9 shows the expected Carbon Release per Unit of Energy in pounds of Carbon per BTU upon burning of the respective gasoline compositions in an internal combustion engine.
• the carbon release per unit of energy for the blended gasoline composition may be as low as 0.0000364 pound per BTU when the blended gasoline composition is burned in an internal combustion engine. See Table 4, the row titled “Carbon release per unit of energy, (lbs. of carbon/BTU) .”

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• Chemical & Material Sciences (AREA)
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• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Combustion & Propulsion (AREA)
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• Liquid Carbonaceous Fuels (AREA)
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• 2021
  • 2021-05-07 US US17/314,579 patent/US11434441B2/en active Active
  • 2021-08-12 EP EP21939963.1A patent/EP4334420A4/en active Pending
  • 2021-08-12 CN CN202180097459.6A patent/CN117255846A/zh active Pending
  • 2021-08-12 KR KR1020237041591A patent/KR20240004872A/ko active Pending
  • 2021-08-12 JP JP2023568432A patent/JP2024516726A/ja not_active Ceased
  • 2021-08-12 CA CA3218344A patent/CA3218344A1/en active Pending
  • 2021-08-12 WO PCT/US2021/045749 patent/WO2022235285A1/en not_active Ceased
• 2023
  • 2023-11-07 SA SA523451453A patent/SA523451453B1/ar unknown

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