US20150027035A1 - Compositions for use in internal-combustion engines and methods of forming and using such compositions - Google Patents
Compositions for use in internal-combustion engines and methods of forming and using such compositions Download PDFInfo
- Publication number
- US20150027035A1 US20150027035A1 US14/216,852 US201414216852A US2015027035A1 US 20150027035 A1 US20150027035 A1 US 20150027035A1 US 201414216852 A US201414216852 A US 201414216852A US 2015027035 A1 US2015027035 A1 US 2015027035A1
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- United States
- Prior art keywords
- fuel composition
- microemulsion
- fuel
- component
- diesel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000000203 mixture Substances 0.000 title claims abstract description 84
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims description 46
- 239000000446 fuel Substances 0.000 claims abstract description 103
- 239000004530 micro-emulsion Substances 0.000 claims abstract description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000000654 additive Substances 0.000 claims abstract description 4
- 238000005260 corrosion Methods 0.000 claims abstract description 4
- 230000007797 corrosion Effects 0.000 claims abstract description 4
- 239000003112 inhibitor Substances 0.000 claims abstract description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 23
- 238000002156 mixing Methods 0.000 claims description 15
- 239000003623 enhancer Substances 0.000 claims description 9
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000000356 contaminant Substances 0.000 claims description 4
- 229910052698 phosphorus Inorganic materials 0.000 claims description 4
- 239000011574 phosphorus Substances 0.000 claims description 4
- 229910052717 sulfur Inorganic materials 0.000 claims description 4
- 239000011593 sulfur Substances 0.000 claims description 4
- 239000003225 biodiesel Substances 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 claims description 3
- 239000013618 particulate matter Substances 0.000 claims description 3
- 231100000719 pollutant Toxicity 0.000 claims description 3
- 238000010257 thawing Methods 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims description 2
- -1 polyol fatty acid esters Chemical class 0.000 description 13
- 239000003995 emulsifying agent Substances 0.000 description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- 229920005862 polyol Polymers 0.000 description 8
- OGBUMNBNEWYMNJ-UHFFFAOYSA-N batilol Chemical class CCCCCCCCCCCCCCCCCCOCC(O)CO OGBUMNBNEWYMNJ-UHFFFAOYSA-N 0.000 description 7
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 5
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 5
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 5
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 5
- 239000005642 Oleic acid Substances 0.000 description 5
- 229940053200 antiepileptics fatty acid derivative Drugs 0.000 description 5
- 235000014113 dietary fatty acids Nutrition 0.000 description 5
- 239000000194 fatty acid Substances 0.000 description 5
- 229930195729 fatty acid Natural products 0.000 description 5
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 5
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- 230000002194 synthesizing effect Effects 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 3
- NKRVGWFEFKCZAP-UHFFFAOYSA-N 2-ethylhexyl nitrate Chemical compound CCCCC(CC)CO[N+]([O-])=O NKRVGWFEFKCZAP-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 238000005809 transesterification reaction Methods 0.000 description 2
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 102000004882 Lipase Human genes 0.000 description 1
- 108090001060 Lipase Proteins 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000001246 colloidal dispersion Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- 239000002816 fuel additive Substances 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 239000001788 mono and diglycerides of fatty acids Substances 0.000 description 1
- 235000019960 monoglycerides of fatty acid Nutrition 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 150000003626 triacylglycerols Chemical class 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/328—Oil emulsions containing water or any other hydrophilic phase
-
- 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
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression 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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/08—Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
-
- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/12—Use of additives to fuels or fires for particular purposes for improving the cetane 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, 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
- C10L1/12—Inorganic compounds
- C10L1/1266—Inorganic compounds nitrogen containing compounds, (e.g. NH3)
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1881—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
- C10L1/191—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polyhydroxyalcohols
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
- C10L1/231—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2200/00—Components of fuel compositions
- C10L2200/04—Organic compounds
- C10L2200/0407—Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
- C10L2200/0438—Middle or heavy distillates, heating oil, gasoil, marine fuels, residua
- C10L2200/0446—Diesel
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2250/00—Structural features of fuel components or fuel compositions, either in solid, liquid or gaseous state
- C10L2250/08—Emulsion details
- C10L2250/084—Water in oil (w/o) emulsion
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2250/00—Structural features of fuel components or fuel compositions, either in solid, liquid or gaseous state
- C10L2250/08—Emulsion details
- C10L2250/086—Microemulsion or nanoemulsion
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2270/00—Specifically adapted fuels
- C10L2270/02—Specifically adapted fuels for internal combustion engines
- C10L2270/026—Specifically adapted fuels for internal combustion engines for diesel engines, e.g. automobiles, stationary, marine
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/60—Measuring or analysing fractions, components or impurities or process conditions during preparation or upgrading of a fuel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Definitions
- the disclosure relates to the field of fuel compositions. More particularly, the disclosure relates to fuel compositions and fuel additives for internal combustion engines.
- FIG. 1 is a schematic block diagram showing a new method for synthesizing and formulating a fuel composition for use in internal-combustion engines in accordance with the present invention.
- FIG. 2 is a schematic diagram that shows a method for formulating a fuel composition on large scale in accordance with the present invention.
- the invention provides fuel compositions for use in internal-combustion engines, and methods of forming and using such compositions.
- the fuel compositions generally comprise (1) a hydrocarbon fuel, such as diesel, (2) a polar fluid, such as alcohol, water, and/or other oxygen rich fluids, (3) an emulsifier present in an amount effective for the hydrocarbon fuel, polar fluid, and emulsifier to form an emulsion; and (4) a cetane enhancer, such as 2-ethylhexyl nitrate.
- the emulsifier may be selected from a group consisting of noncyclic polyol fatty acid esters and noncyclic polyol fatty alcohol ethers. In some embodiments, at least about half of the emulsifier is selected from this group. In other embodiments, at least about half of this group is mono-substituted.
- the emulsifier also may consist essentially of a single molecular species having both polar and nonpolar portions.
- the methods generally include methods of forming and using the fuel compositions, including components thereof.
- the invention provides methods of forming the emulsifier, by synthesizing and/or purifying components of the emulsifier. These components may include noncyclic polyol fatty acid esters and noncyclic polyol fatty alcohol ethers.
- Monoglycerides of fatty acids have been used for years as surfactants in a variety of food, cosmetic, and other formulated products. In most applications, industrial-grade monoglyceride compositions having 40-55% monoglyceride content have proven suitable. However, the present application in fuel formulations requires high-purity monoglycerides to yield optimal performance, and inexpensive monoglycerides to be economically practical.
- Monoglycerides have been synthesized by a variety of methods. Unfortunately, these methods generally yield products that must be further distilled or extracted to obtain high-purity monoglycerides. Moreover, these methods generally are unsuitable for forming monoglycerides of unsaturated fatty acids, such as oleic acid, because of oxidative decomposition at the point of unsaturation.
- U.S. Pat. No. 2,022,493 to Christensen et al. discloses the conventional method for synthesizing monoglycerides, which involves the transesterification of triglycerides with glycerol and sodium hydroxide to form the monoglycerides.
- the product of this method is a mixture of 40-55% monoglyceride, 20-30% diglyceride, and a remainder of unreacted triglyceride.
- U.S. Pat. No. 2,132,437 to Richardson et al. and U.S. Pat. No. 2,073,797 to Hilditch et al. disclose two methods of increasing monoglyceride selectivity by converting the triglyceride to free fatty acid before esterification. However, the products of these methods are still contaminated with at least 20% di- and triglyceride, and the methods are considerably more complex than the conventional method.
- U.S. Pat. No. 5,153,126 to Schroder et al. discloses a method for making additional gains in selectivity by using a lipase enzyme as the transesterification catalyst. However, this method is very costly and difficult to scale up.
- a fuel composition for use in internal-combustion engines has a fuel component, an alcohol component, a water component, a microemulsion, and a cetane-enhancer component.
- the microemulsion includes at least one of lower grade fatty acid derivatives being present in an amount effective for the fuel, alcohol, and water components to form a microemulsion.
- the emulsifier is present in an amount effective for the biodiesel fuel, alcohol, water, and emulsifier to form an emulsion.
- FIG. 1 shows a new method 100 for synthesizing and formulating a fuel composition for use in internal-combustion engines.
- a lower grade fuel is provided, the fuel is non-renewable content in the fuel composition.
- the fuel can be diesel.
- a non-renewable content including lower grade fatty acid derivatives (or surfactant) and/or other surfactants may be selected.
- an alcohol component such as, but not limited to, lower grade ethanol (i.e. hydrous ethanol, and so forth) may be selected or provided.
- a microemulsion having at least one of lower grade fatty acid derivatives is provided.
- the steps 102 to steps 106 can be performed in any order.
- the microemulsion is considered to be extremely fine colloidal dispersions consisting of micelles, or “bubbles,” of water and alcohol coated with a layer of surfactant.
- the fuel composition is formed or formulated by adding to the fuel, a microemulsion having at least one of hydrous component, renewable component, and polar component being present in an amount effective for forming the fuel composition.
- the microemulsion may include a mixture of oleic acid, ethanol, ammonia, water, and a cetane enhancer, such as 2-ethylhexyl nitrate.
- steps may be performed under conditions that would tend not to substantially reduce an unsaturated fatty acid or fatty chloride. Such conditions may include performing one or more of the steps in an inert atmosphere, such as a nitrogen atmosphere, or performing one or more of the steps in the absence of light.
- an inert atmosphere such as a nitrogen atmosphere
- FIG. 2 shows a method 200 for formulating a fuel composition on large scale.
- the method 200 may include refining crude oil 202 and through one or more refining process fuel is derived.
- the fuel can be straight run diesel 204 .
- lower grade fatty acid derivatives such as, oleic acid, ethanol, and bi products of crude oil such as ammonia, water, along with cetane enhancer are blended to form microemulsion 206 .
- the microemulsion 206 may include at least one of lower grade fatty acid derivatives that may be present in an amount effective for the fuel 204 , alcohol, and water components to form a microemulsion 206 .
- the fatty acid can be oleic acid.
- the method 200 may also include assessing the quality of the microemulsion 206 that can be done by analyzing at least one of an oxidative stability and contaminates in the microemulsion 206 .
- the diesel 204 can be a straight run diesel or an unadditized diesel.
- the microemulsion 206 may be blended with fuel, water, ammonia, cetane enhancer, and alcohol to form the fuel composition 208 (final product).
- the microemulsion 206 may be blended in different volumes with the fuel 204 (or diesel) which can be 5%, 6%, 12%, and so forth. Further, the microemulsion 206 for formulating fuel composition may include a mixture of oleic acid, ethanol, ammonia, water, and a cetane enhancer.
- the microemulsion 206 can be blended with lower grade diesel or fuel 204 by using inline blending process at a petroleum terminal.
- the inline blending process includes blending of the microemulsion 206 at the petroleum terminal(s) within one or more pipelines.
- the microemulsion 206 can be blended with lower grade diesel/fuel 204 by performing splash blending at the petroleum terminal.
- the splash blending may include blending the microemulsion 206 in a storage container (not shown) and then blending with the diesel 204 in distribution vehicle to splash blend in a transportation tank (not shown).
- the microemulsion 206 may also be blended with the fuel 204 by performing splash blending at a distributor i.e. by blending microemulsion 206 when blending the diesel (or fuel) 204 to have the fuel composition 208 for distribution.
- the present disclosure provides a fuel composition for use in internal-combustion engines; the fuel composition may include a lower grade fuel component 204 , and a microemulsion having at least one of hydrous component, a renewable component, and a polar component, which are present in an amount effective for forming the fuel composition.
- the fuel composition may enhance lubricity, corrosion, and water stability without the use of other additives and inhibitors.
- the microemulsion 206 is blended with lower grade diesel/fuel 204 , water component, a cetane enhancer, an alcohol component to form the fuel composition.
- the disclosed method forms a new improved fuel composition that includes increased concentration of renewable contents. Further, the new improved fuel composition is formed such that it may reduce carbon intensity in the internal combustion engines.
- the new improved fuel composition can also dilute contents of aromatics, sulfur, phosphorus, and other contaminants.
- the new improved fuel composition may also reduce emissions of NOx, particulate matter, and other criteria pollutants.
- the improved fuel composition allows a flashpoint to stay below 38C for microemulsion concentrations greater than 1% but the flashpoint increases for microemulsion concentrations that are below 1%.
- the improved fuel composition forms spontaneously upon blending, and maintains clarity at low temperatures, upon freeze-thawing, and for prolonged periods. Further, the improved fuel composition can be biodiesel.
- the disclosed method for formulating the fuel composition further includes optimizing the microemulsion volumes to be blended with a different quality of diesel or fuel.
- the method also includes optimizing the microemulsion 206 to blend with different quality of diesel/fuel.
- the disclosed method also includes optimizing the algorithms for microemulsion optimization based off crude oil contents and diesel refining optimization.
- the present disclosure also provides a method for allowing for the blending of renewable components upstream of distributer blenders.
- the formulated fuel composition results in increased renewable contents in fuel or diesel, and reduced carbon intensity.
- the formulated fuel composition also includes diluted contents of sulfur, phosphorus, and ash.
- the formulated fuel composition when used in internal combustion engines may result in reduced emissions.
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Abstract
A fuel composition for use in internal-combustion engines has a lower grade fuel component, and a microemulsion. The microemulsion includes at least one of hydrous component, renewable component, and polar component being present in an amount effective for forming the fuel composition. The fuel composition may enhance lubricity, corrosion, and water stability without the use of other additives and inhibitors.
Description
- This application claims the benefit under 35 U.S.C. §119(e) of U.S. Provisional Patent Applications, Ser. Nos. 61/798,461 and 61/798,438, each filed Mar. 15, 2013, and each of which is hereby incorporated by reference in its entirety for all purposes. This application is also a continuation of U.S. patent application Ser. No. 13/966,207, filed Aug. 13, 2013 and entitled METHOD OF FORMULATING A FUEL COMPOSITION FOR USE IN INTERNAL-COMBUSTION ENGINES, which application is a continuation-in-part of U.S. patent application Ser. No. 13/217,171, filed Aug. 24, 2011 and entitled METHOD OF FORMULATING A FUEL COMPOSITION FOR USE IN INTERNAL-COMBUSTION ENGINES, which application is a continuation of U.S. patent application Ser. No. 12/105,164, filed Apr. 17, 2008 and entitled METHOD OF FORMULATING A FUEL COMPOSITION FOR USE IN INTERNAL-COMBUSTION ENGINES, which application claims priority to U.S. Provisional Patent Application Ser. No. 60/974,779, filed Sep. 24, 2007 and entitled MICROEMULSION FUEL COMPOSITIONS AND METHODS FOR PRODUCING THE SAME and also claims priority to U.S. Provisional Patent Application Ser. No. 61/036,007, filed Mar. 12, 2008 and entitled FUEL COMPOSITIONS FOR USE IN INTERNAL-COMBUSTION ENGINES AND METHODS OF FORMING USING SUCH COMPOSITIONS, each of which is incorporated herein by reference in its entirety for all purposes.
- The disclosure relates to the field of fuel compositions. More particularly, the disclosure relates to fuel compositions and fuel additives for internal combustion engines.
-
FIG. 1 is a schematic block diagram showing a new method for synthesizing and formulating a fuel composition for use in internal-combustion engines in accordance with the present invention. -
FIG. 2 is a schematic diagram that shows a method for formulating a fuel composition on large scale in accordance with the present invention. - The invention provides fuel compositions for use in internal-combustion engines, and methods of forming and using such compositions.
- The fuel compositions generally comprise (1) a hydrocarbon fuel, such as diesel, (2) a polar fluid, such as alcohol, water, and/or other oxygen rich fluids, (3) an emulsifier present in an amount effective for the hydrocarbon fuel, polar fluid, and emulsifier to form an emulsion; and (4) a cetane enhancer, such as 2-ethylhexyl nitrate. The emulsifier may be selected from a group consisting of noncyclic polyol fatty acid esters and noncyclic polyol fatty alcohol ethers. In some embodiments, at least about half of the emulsifier is selected from this group. In other embodiments, at least about half of this group is mono-substituted. The emulsifier also may consist essentially of a single molecular species having both polar and nonpolar portions.
- The methods generally include methods of forming and using the fuel compositions, including components thereof. For example, the invention provides methods of forming the emulsifier, by synthesizing and/or purifying components of the emulsifier. These components may include noncyclic polyol fatty acid esters and noncyclic polyol fatty alcohol ethers.
- These and other aspects of the invention are described in the following four sections: (1) synthesis of noncyclic polyol fatty acid esters and noncyclic polyol fatty alcohol ethers, (2) purification of noncyclic polyol fatty acid esters and noncyclic polyol fatty alcohol ethers, (3) fuel compositions, and (4) examples.
- Monoglycerides of fatty acids have been used for years as surfactants in a variety of food, cosmetic, and other formulated products. In most applications, industrial-grade monoglyceride compositions having 40-55% monoglyceride content have proven suitable. However, the present application in fuel formulations requires high-purity monoglycerides to yield optimal performance, and inexpensive monoglycerides to be economically practical.
- Monoglycerides have been synthesized by a variety of methods. Unfortunately, these methods generally yield products that must be further distilled or extracted to obtain high-purity monoglycerides. Moreover, these methods generally are unsuitable for forming monoglycerides of unsaturated fatty acids, such as oleic acid, because of oxidative decomposition at the point of unsaturation. U.S. Pat. No. 2,022,493 to Christensen et al. discloses the conventional method for synthesizing monoglycerides, which involves the transesterification of triglycerides with glycerol and sodium hydroxide to form the monoglycerides. However, the product of this method is a mixture of 40-55% monoglyceride, 20-30% diglyceride, and a remainder of unreacted triglyceride. U.S. Pat. No. 2,132,437 to Richardson et al. and U.S. Pat. No. 2,073,797 to Hilditch et al. disclose two methods of increasing monoglyceride selectivity by converting the triglyceride to free fatty acid before esterification. However, the products of these methods are still contaminated with at least 20% di- and triglyceride, and the methods are considerably more complex than the conventional method. U.S. Pat. No. 5,153,126 to Schroder et al. discloses a method for making additional gains in selectivity by using a lipase enzyme as the transesterification catalyst. However, this method is very costly and difficult to scale up.
- A fuel composition for use in internal-combustion engines has a fuel component, an alcohol component, a water component, a microemulsion, and a cetane-enhancer component. The microemulsion includes at least one of lower grade fatty acid derivatives being present in an amount effective for the fuel, alcohol, and water components to form a microemulsion. The emulsifier is present in an amount effective for the biodiesel fuel, alcohol, water, and emulsifier to form an emulsion.
-
FIG. 1 shows anew method 100 for synthesizing and formulating a fuel composition for use in internal-combustion engines. At step 102 a lower grade fuel is provided, the fuel is non-renewable content in the fuel composition. The fuel can be diesel. A non-renewable content including lower grade fatty acid derivatives (or surfactant) and/or other surfactants may be selected. Atstep 104, an alcohol component such as, but not limited to, lower grade ethanol (i.e. hydrous ethanol, and so forth) may be selected or provided. Then atstep 106, a microemulsion having at least one of lower grade fatty acid derivatives is provided. Thesteps 102 tosteps 106 can be performed in any order. The microemulsion is considered to be extremely fine colloidal dispersions consisting of micelles, or “bubbles,” of water and alcohol coated with a layer of surfactant. - Thereafter, at
step 108, the fuel composition is formed or formulated by adding to the fuel, a microemulsion having at least one of hydrous component, renewable component, and polar component being present in an amount effective for forming the fuel composition. The microemulsion may include a mixture of oleic acid, ethanol, ammonia, water, and a cetane enhancer, such as 2-ethylhexyl nitrate. - These steps may be performed under conditions that would tend not to substantially reduce an unsaturated fatty acid or fatty chloride. Such conditions may include performing one or more of the steps in an inert atmosphere, such as a nitrogen atmosphere, or performing one or more of the steps in the absence of light.
-
FIG. 2 shows amethod 200 for formulating a fuel composition on large scale. Themethod 200 may include refiningcrude oil 202 and through one or more refining process fuel is derived. The fuel can be straight rundiesel 204. Similarly, lower grade fatty acid derivatives, such as, oleic acid, ethanol, and bi products of crude oil such as ammonia, water, along with cetane enhancer are blended to formmicroemulsion 206. Themicroemulsion 206 may include at least one of lower grade fatty acid derivatives that may be present in an amount effective for thefuel 204, alcohol, and water components to form amicroemulsion 206. The fatty acid can be oleic acid. Then, at least 57 to 99% offuel 204 i.e. diesel can be blended with 43-1% ofmicroemulsion 206 to formulate afuel composition 208. Themethod 200 may also include assessing the quality of themicroemulsion 206 that can be done by analyzing at least one of an oxidative stability and contaminates in themicroemulsion 206. And thediesel 204 can be a straight run diesel or an unadditized diesel. In one or more blending containers, themicroemulsion 206 may be blended with fuel, water, ammonia, cetane enhancer, and alcohol to form the fuel composition 208 (final product). Themicroemulsion 206 may be blended in different volumes with the fuel 204 (or diesel) which can be 5%, 6%, 12%, and so forth. Further, themicroemulsion 206 for formulating fuel composition may include a mixture of oleic acid, ethanol, ammonia, water, and a cetane enhancer. - The
microemulsion 206 can be blended with lower grade diesel orfuel 204 by using inline blending process at a petroleum terminal. The inline blending process includes blending of themicroemulsion 206 at the petroleum terminal(s) within one or more pipelines. Alternatively, themicroemulsion 206 can be blended with lower grade diesel/fuel 204 by performing splash blending at the petroleum terminal. The splash blending may include blending themicroemulsion 206 in a storage container (not shown) and then blending with thediesel 204 in distribution vehicle to splash blend in a transportation tank (not shown). Themicroemulsion 206 may also be blended with thefuel 204 by performing splash blending at a distributor i.e. by blendingmicroemulsion 206 when blending the diesel (or fuel) 204 to have thefuel composition 208 for distribution. - The present disclosure provides a fuel composition for use in internal-combustion engines; the fuel composition may include a lower
grade fuel component 204, and a microemulsion having at least one of hydrous component, a renewable component, and a polar component, which are present in an amount effective for forming the fuel composition. The fuel composition may enhance lubricity, corrosion, and water stability without the use of other additives and inhibitors. Themicroemulsion 206 is blended with lower grade diesel/fuel 204, water component, a cetane enhancer, an alcohol component to form the fuel composition. The disclosed method forms a new improved fuel composition that includes increased concentration of renewable contents. Further, the new improved fuel composition is formed such that it may reduce carbon intensity in the internal combustion engines. The new improved fuel composition can also dilute contents of aromatics, sulfur, phosphorus, and other contaminants. The new improved fuel composition may also reduce emissions of NOx, particulate matter, and other criteria pollutants. The improved fuel composition allows a flashpoint to stay below 38C for microemulsion concentrations greater than 1% but the flashpoint increases for microemulsion concentrations that are below 1%. The improved fuel composition forms spontaneously upon blending, and maintains clarity at low temperatures, upon freeze-thawing, and for prolonged periods. Further, the improved fuel composition can be biodiesel. - The disclosed method for formulating the fuel composition further includes optimizing the microemulsion volumes to be blended with a different quality of diesel or fuel. The method also includes optimizing the
microemulsion 206 to blend with different quality of diesel/fuel. The disclosed method also includes optimizing the algorithms for microemulsion optimization based off crude oil contents and diesel refining optimization. The present disclosure also provides a method for allowing for the blending of renewable components upstream of distributer blenders. The formulated fuel composition results in increased renewable contents in fuel or diesel, and reduced carbon intensity. The formulated fuel composition also includes diluted contents of sulfur, phosphorus, and ash. The formulated fuel composition when used in internal combustion engines may result in reduced emissions. - In the preceding description, various aspects of claimed subject matter have been described. For purposes of explanation, specific numbers, systems and/or configurations were set forth to provide a thorough understanding of the claimed subject matter. However, it should be apparent to one skilled in the art having the benefit of this disclosure that claimed subject matter may be practiced without the specific details. In other instances, features that would be understood by one of ordinary skill were omitted and/or simplified so as not to obscure claimed subject matter. While certain features have been illustrated and/or described herein, many modifications, substitutions, changes and/or equivalents will now occur to those skilled in the art. It is, therefore, to be understood that the appended claims are intended to cover all such modifications and/or changes as fall within the true spirit of claimed subject matter.
Claims (23)
1. A fuel composition for use in internal-combustion engines, the fuel composition comprising:
a lower grade fuel component;
a microemulsion comprising at least one of a hydrous component, a renewable component, and a polar component being present in an amount effective for forming the fuel composition; and
wherein the fuel composition enhances lubricity, corrosion, and water stability without the use of other additives and inhibitors.
2. The fuel composition of claim 1 , wherein the microemulsion is blended with lower grade diesel, water component, a cetane enhancer, an alcohol component to form the fuel composition.
3. The fuel composition of claim 2 , wherein the lower grade fuel is diesel which is at least one of a straight run diesel or an unadditized diesel.
4. The fuel composition of claim 3 , wherein the microemulsion volumes which are blended with the lower grade diesel component is at least one of 5%, 6%, and 12%.
5. The fuel composition of claim 4 , wherein the fuel composition comprises increased concentration of renewable contents.
6. The fuel composition of claim 5 , wherein the fuel composition is formed such that it reduces carbon intensity in the internal combustion engines.
7. The fuel composition of claim 6 , wherein the fuel composition dilutes contents of aromatics, sulfur, phosphorus, and other contaminants.
8. The fuel composition of claim 7 , wherein the fuel composition reduces emissions of NOx, particulate matter, and other criteria pollutants.
9. The fuel composition of claim 8 , wherein the fuel composition allows a flashpoint to stay below 38C for microemulsion concentrations greater than 1% but the flashpoint increases for microemulsion concentrations that are below 1%.
10. The fuel composition of claim 9 , wherein the fuel composition forms spontaneously upon blending, and maintains clarity at low temperatures, upon freeze-thawing, and for prolonged periods.
11. The fuel composition of claim 10 , wherein the fuel composition is biodiesel.
12. A method of formulating a fuel composition for use in internal-combustion engines, the method comprising:
providing a fuel; and
forming the fuel composition by adding to the fuel, a microemulsion comprising at least one of hydrous component, renewable component, and polar component being present in an amount effective for forming the fuel composition; and
wherein the fuel composition enhances lubricity, corrosion, and water stability without the use of other additives and inhibitors.
13. The method of claim 12 further comprising assessing the quality of the microemulsion.
14. The method of claim 13 , wherein the quality is assessed by analyzing at least one of an oxidative stability and contaminants in the microemulsion.
15. The method of claim 14 further comprising optimizing the microemulsion volumes to be blended with different quality of the diesel.
16. The method of claim 15 , wherein the diesel is at least one of a straight run diesel or an unadditized diesel.
17. The method of claim 16 , wherein the microemulsion volumes which are blended with the lower grade diesel component is at least one of 5%, 6%, and 12%.
18. The method of claim 17 , wherein the microemulsion is blended with lower grade diesel, a water component, a cetane enhancer, an alcohol component to form the fuel composition.
19. The method of claim 18 , wherein the fuel composition is formed such that it reduces carbon intensity in the internal combustion engines.
20. The method of claim 19 , wherein the fuel composition dilutes contents of aromatics, sulfur, phosphorus, and other contaminants.
21. The method of claim 20 , wherein the fuel composition reduces emissions of NOx, particulate matter, and other criteria pollutants.
22. The method of claim 21 , wherein the fuel composition allows a flashpoint to stay below 38C for microemulsion concentrations greater than 1% but flashpoint increases for microemulsion concentrations that are below 1%.
23. The method of claim 22 , wherein the fuel composition forms spontaneously upon blending, and maintains clarity at low temperatures, upon freeze-thawing, and for prolonged periods.
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US6017368A (en) * | 1998-06-22 | 2000-01-25 | Steinmann; Henry W | Microemulsion fuel compositions for the internal combustion engine and for oil furnaces |
WO2000063322A1 (en) * | 1999-04-21 | 2000-10-26 | Pure Fuels Usa, Inc. | Fuel compositions |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2017214493A1 (en) * | 2016-06-09 | 2017-12-14 | Fueltek, Inc. | Hygroscopic fuel blends and processes for producing same |
Also Published As
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US20150020440A1 (en) | 2015-01-22 |
US20160257896A1 (en) | 2016-09-08 |
US20160251586A1 (en) | 2016-09-01 |
US20140041286A1 (en) | 2014-02-13 |
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