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CN102260553A - Oxidation stabilized fuels having enhanced corrosion resistance - Google Patents

Oxidation stabilized fuels having enhanced corrosion resistance Download PDF

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Publication number
CN102260553A
CN102260553A CN2011101335403A CN201110133540A CN102260553A CN 102260553 A CN102260553 A CN 102260553A CN 2011101335403 A CN2011101335403 A CN 2011101335403A CN 201110133540 A CN201110133540 A CN 201110133540A CN 102260553 A CN102260553 A CN 102260553A
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fuel
mixture
composition
alkyl
average molecular
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C.D.马比勒
J.本内特
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Afton Chemical Ltd
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/04Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/08Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/221Organic compounds containing nitrogen compounds of uncertain formula; reaction products where mixtures of compounds are obtained
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/232Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
    • C10L1/2387Polyoxyalkyleneamines (poly)oxyalkylene amines and derivatives thereof (substituted by a macromolecular group containing 30C)
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/08Inhibitors
    • C10L2230/081Anti-oxidants
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Powder Metallurgy (AREA)

Abstract

A method of improving oxidation properties of biodiesel-containing fuel composition is provided. The method provides combining a major amount of middle distillate fuel containing more than about 5 volume percent biodiesel components with a minor amount of a synergistic mixture of (A) a hydrocarbyl-substituted succinimide dispersant and (B) a compound of the formula: and tautomers and enantiomers thereof. In the formula, R2 is a hydrocarbyl group having a number average molecular weight ranging from 100 to 5000. The synergistic mixture has a weight ratio of A:B ranging from 2:1 to 10:1.

Description

Oxidation-stabilized fuel with erosion resistance of raising
Technical field
The present invention relates to some diesel fuel additive and relate to diesel oil fuel and the diesel fuel additive enriched material that comprises this additive.Concrete, the present invention relates to and be used to improve the oxidative stability of diesel oil and biodiesel fuel and/or the method for erosion resistance.
Background of invention and summary of the invention
In order to protect valuable resource and to reduce the environmentally hazardous discharging of possibility, reproducible fuel (for example rape, soybean, oil palm, sugarcane or corn are made by crop for they) is joined in the fuel.A target using such fuel composition is to make eco-friendly day by day transport fuel, and does not change the mode of operation of vehicle motor on such fuel.
The biofuel composition that is used for fuel can be produced by straight chain vegetables oil, animal oil/fat, tallow oil and waste oil.Most biofuel composition is to use the transesterification reaction of base catalysis to produce, because it is most economical method, only needs low temperature and pressure, and has produced 98% conversion yield.Grape, oil palm and soybean oil are the prevailing crops that is used for the production biofuel.The most common commercially available biodiesel fuel is actually biodiesel blend, and its suitable title is a letter b, and one or two numerals are followed in the back, this digitized representation with the mixture of petroleum diesel fuel in the per-cent of biofuel.Pure biofuel sometimes is called " only " biofuel, and is also referred to as B100.Prevailing biodiesel blend is B2, B5, B7, B10, B20 and B50.Rest part is the petroleum base diesel oil fuel, and it often is called petroleum diesel.
Vegetables oil and fatty acid methyl ester have relative short storage life, this owing to them by the aerial oxygen slow oxidation.Formed oxidation products can be insoluble in fuel, and therefore can damage the engine of vehicle.Reason for this reason, the fuel oxidation stability that contains biofuel is an important quality standard.Up to now, use relatively costly fuel dope to become branch to require to satisfy the fuel oxidation stability criterion that contains biofuel, this standard is measured by ASTM D-2274.Therefore, need a kind of like this method, it can effectively reduce or eliminate the needs for relatively costly fuel composition, keeps containing the fuel oxidation stability of biofuel simultaneously.
According to the present invention, exemplary embodiment provides the method for the oxidative stability of the fuel composition that a kind of raising comprises biofuel.This method provides the mainly midbarrel fuel and a spot of Synergistic mixture that contain greater than at least a biofuel composition of about 5 volume % of amount is merged, and this Synergistic mixture is the succinimide dispersants that replaces of (A) alkyl and (B) compound of following formula and the mixture of tautomer and enantiomer thereof:
Figure 2011101335403100002DEST_PATH_IMAGE001
In the formula, R 2Be that number-average molecular weight is the alkyl of 100-5000.The A:B weight ratio of this Synergistic mixture is 2:1-10:1.
It is a kind of by containing the method for moving engine greater than the midbarrel fuel of at least a biofuel composition of about 5 volume % that another embodiment of the present invention provides.This method comprises with a spot of Synergistic mixture prepares this fuel, a kind of sludge proof fuel composition is provided, and described Synergistic mixture is the succinimide dispersants that replaces of (A) alkyl and (B) compound of following formula and the mixture of tautomer and enantiomer thereof:
Figure 725241DEST_PATH_IMAGE001
R wherein 2Be that number-average molecular weight is the alkyl of 100-5000.The A:B weight ratio of this Synergistic mixture is 2:1-10:1.This engine moves by this fuel composition.
Another embodiment of the present invention provides a kind of purposes of Synergistic mixture, and this mixture is the succinimide dispersants that replaces of (A) alkyl and (B) compound of following formula and the mixture of tautomer and enantiomer thereof:
Figure 54591DEST_PATH_IMAGE001
R wherein 2Be that number-average molecular weight is the alkyl of 100-5000.The A:B weight ratio of this Synergistic mixture is 2:1-10:1, and this mixture is used for containing the midbarrel fuel of at least a biofuel composition of at least 7 volume %, improves the oxidative stability of this fuel according to ASTM D-2274.
A kind of unexpected advantage of above-mentioned A and the Synergistic mixture of B is that the midbarrel fuel that contains greater than the biofuel composition of about 5 volume % can not need to use relatively costly metal passivator, come to satisfy or surpass in the presence of the copper that adds, by ASTM D-2274 measured be used for such fuel oxidation stability criterion.
Other embodiments of the present invention and advantage will partly be illustrated in detailed description subsequently, and/or can understand by practice of the present invention.The two all only is exemplary with illustrative to be to be understood that aforesaid general remark and following detailed description, is not the present invention of requirement for restriction protection.
Embodiment
According to embodiment of the present invention, provide a kind of synergy fuel dope mixture.This Synergistic mixture comprises: (A) succinimide dispersants of alkyl replacement and (B) compound and the tautomer and the enantiomer of following formula:
Figure 253491DEST_PATH_IMAGE001
R wherein 2Be that number-average molecular weight is the alkyl of 100-5000.The A:B weight ratio of this Synergistic mixture can be the about 10:1 of about 2:1-, for example about about 6:1 of 3:1-, more particularly about 3.5:1-5:1.
As what use herein, term " hydrocarbyl group " or " alkyl " are to use with its common implication, and it is well known to a person skilled in the art.Clear and definite, it refers to such group, and this group has the carbon atom that is directly connected on the molecule rest part (the remainder of a molecular), and has main hydrocarbon performance.The example of alkyl comprises:
(1) hydrocarbon substituent, promptly, aliphatic (for example alkyl or alkenyl), alicyclic (cycloalkyl for example, cycloalkenyl) substituting group, with aromatic-, aliphatic-and the aromatic substituents of alicyclic replacement, and ring substituents, wherein this ring is (for example, two substituting groups forms alicyclic group together) that the other part by molecule realizes;
(2) hydrocarbon substituent of Qu Daiing, promptly, the substituting group that contains non-hydrocarbyl group in its described herein context, does not change the hydrocarbon substituent (for example halogen (particularly chlorine and fluorine), hydroxyl, alkoxyl group, sulfydryl, alkyl thiol, nitro, nitroso-group and sulphur oxygen base) that is dominant;
(3) assorted substituting group, that is, such substituting group though it has the hydrocarbon characteristic that is dominant, in the context of the present specification, has comprised other atoms except that carbon atom in ring that was made of carbon atom originally or chain.Heteroatoms comprises sulphur, oxygen, nitrogen, and comprises substituting group for example pyridyl, furyl, thienyl and imidazolyl.Usually,, exist and be not more than two, perhaps as a further example, exist and be not more than one non-hydrocarbon substituent for per 10 carbon atoms in the alkyl; In some embodiments, in alkyl, there is not non-hydrocarbon substituent.
As what use herein, term " main amount " is understood that expression is greater than or equal to 50wt%, and the about amount of the about 98wt% of 80-for example is with respect to the gross weight of said composition.In addition, as what use herein, term " on a small quantity " is understood that to represent the amount less than 50wt%, with respect to the gross weight of said composition.
As what use herein, " biological reproducible fuel ", " biodiesel fuel " and " biofuel composition " are understood that to represent any fuel that derives from non-oil resource.Such resource includes but not limited to cereal, corn, soybean and other crops; Grass, for example switchgrass, spire awns and weeds; Algae, sea grass, vegetables oil; Natural fat; And composition thereof.On the one hand, the reproducible fuel of this biology can comprise single hydroxyl alcohol, for example has these alcohol of about 5 carbon atoms of 1-.The example of the indefiniteness of suitable single hydroxyl alcohol comprises methyl alcohol, ethanol, propyl alcohol, propyl carbinol, isopropylcarbinol, the trimethyl carbinol, amylalcohol and primary isoamyl alcohol.
As what use herein, " midbarrel fuel " can be for example petroleum naphtha, kerosene or diesel fuel composition.It can be domestic fuel oil, industrial diesel oil, boring oil, motor vehicle diesel fuel, distillatory bunker fuel or kerosene stock for example aviation fuel or domestic kerosene.It specifically can be a diesel fuel composition.More specifically, midbarrel fuel is such fuel, and it is suitable for and/or is adapted to and/or is intended for use in the oil engine; Automobile fuel composition for example, and/or be adapted to and/or be intended for use in motor vehicle diesel (ignition) engine.Such midbarrel fuel can be organically or synthesize the source, diesel oil for example the oil source or the fischer-tropsch source.The boiling point of midbarrel fuel can be in 125 or 150 to 400 or 550 ℃ conventional diesel range, and this depends on grade and purposes.This midbarrel fuel can be 0.75-1.0g/cm 15 ℃ density 3, 0.8-0.86g/cm for example 3(IP365) and measured cetane value (ASTM D613) be 35-80, suitable is 40-75 or 70.The initial boiling point of midbarrel fuel can be suitable be 150-230 ℃, and the final boiling point of this fuel can be 290-400 ℃.This midbarrel fuel 40 ℃ dynamic viscosity (ASTM D445) can be suitable be 1.5-4.5mm 2/ s (centistokes(cst)).
The composition A of this Synergistic mixture can be a dispersion agent, for example contains the dispersion agent of amine.Suitable contain the succinimide dispersants that the amine dispersion agent can comprise that alkyl replaces.The number-average molecular weight of the hydrocarbyl substituent of this dispersion agent can be that about 100-is about 5000, and for example about about 5000 dalton of 500-measure by GPC.
As what use herein; term " succinimide " expression has comprised the complete reaction product that reacts between amine and hydrocarbyl substituted succinic or the acid anhydrides (perhaps for example succinic acylating agent); and plan comprises such compound; wherein said product is except being reacted with anhydride moiety by amine or contacting the formed imide connection type; can also have acid amides, and/or salt connects.
Suitable hydrocarbyl substituted succinic acid anhydride can form by at first the alkylene unsaturated hydrocarbons of desired molecular weight and maleic anhydride being reacted.Operable temperature of reaction is about 100 ℃-about 250 ℃.
Use the alkylene unsaturated hydrocarbons of higher, can obtain good result at about 200 ℃-about 250 ℃.This reaction can promote by adding chlorine.
Typical alkene can include but not limited to the polymkeric substance and the multipolymer of cracked cerotene hydrocarbon, linear alpha olefin, branched chain alhpa olefin, light alkene.This alkene can be selected from ethene, propylene, butylene for example iso-butylene, 1-octane, 1-hexene, 1-decene or the like.Useful polymkeric substance and/or multipolymer can include but not limited to polypropylene, polybutene, polyisobutene, ethylene-propylene copolymer, ethene-isobutylene copolymers, propylene-isobutylene copolymers, ethene-1-decene multipolymer or the like.
In the one side of disclosed embodiment, the hydrocarbyl substituent of this hydrocarbyl substituted succinic acid anhydride can come from butene polymers, for example the polymkeric substance of iso-butylene.Be used for herein suitable polyisobutene comprise by having about at least 60%, for example approximately the HR-PIB of the end vinylidene content of 70%-about 90% and Geng Gao formed these.Suitable polyisobutene can comprise use BF 3These that catalyzer is prepared.The number-average molecular weight of this hydrocarbyl substituent can change in wide scope, for example is that about 100-is about 5000, and for example approximately 500-is about 5000, passes through gpc measurement.
Can use except the carboxylic acid reaction thing of maleic anhydride for example toxilic acid, the acid of good fortune horse, oxysuccinic acid, tartrate, methylene-succinic acid, itaconic anhydride, citraconic acid, citraconic anhydride, methylfumaric acid, ethyl maleic anhydride, dimethyl maleic anhydride, ethyl toxilic acid, dimethyl maleic acid, hexyl toxilic acid or the like, comprise corresponding sour halogenide and low-grade fatty acid ester.The mol ratio of maleic anhydride and alkene can change widely in reaction mixture.Therefore, this mol ratio can be about 1.5 at about 5:1-, the about range of the about 1:3 of 3:1-for example, and as a further example, this maleic anhydride can use with over-stoichiometric, reacts completely to impel.Unreacted maleic anhydride can be removed by vacuum distilling.
In numerous polyamines any one can be used to prepare the succinimide dispersants that this alkyl replaces.The exemplary polyamines of indefiniteness can comprise aminoguanidine double manganese ester (AGBC), diethylenetriamine (DETA), triethylene tetramine (TETA), tetraethylene pentamine (TEPA), five ethene hexamines (PEHA) and heavy polyamines.Heavy polyamines can comprise the mixture of polyalkylene polyamine, it has a small amount of rudimentary polyamines oligopolymer for example TEPA and PEHA, but main oligopolymer has 7 or more a plurality of nitrogen-atoms, and the polyamine mixture of two or more primary amine per molecules and ratio routine is branching widely.The polyamines of indefiniteness (it can be used for preparing the succinimide dispersants that this alkyl replaces) is disclosed in US patent No.6548458 in addition, and this invention all is incorporated herein by reference with it at this.In one embodiment of the present invention, this polyamines can be selected from tetraethylene pentamine (TEPA).
In one embodiment, this dispersion agent can comprise the compound of formula (IV):
Figure 984687DEST_PATH_IMAGE002
Wherein n represents 0 or the integer of 1-5, R 2It is above-mentioned hydrocarbyl substituent.In one embodiment, n is 3, R 2Be the polyisobutenyl substituting group, for example derive from have about at least 60%, the about polyisobutenyl substituting group of the polyisobutene of the end vinylidene content of 70%-about 90% and Geng Gao for example.The compound of formula (IV) can be the hydrocarbyl substituted succinic acid anhydride, polyisobutenyl succinic anhydride (PIBSA) for example, and with polyamines, the reaction product of tetraethylene pentamine (TEPA) for example.
The composition B of this Synergistic mixture can react by the hydrocarbyl oxycarbonyl based compound with the amine compound of following first formula or its salt and following second formula and make:
Figure 2011101335403100002DEST_PATH_IMAGE003
Wherein R is selected from hydrogen and the alkyl that contains about 15 carbon atoms of about 1-, and R 1Be selected from hydrogen and the alkyl that contains about 20 carbon atoms of about 1-,
Figure 40367DEST_PATH_IMAGE004
R wherein 2Be that number-average molecular weight is the alkyl of about 200-about 3000.Do not wish to be subject to theoretic knowledge, it is believed that the reaction product of described amine and hydrocarbyl oxycarbonyl based compound is an aminotriazole, for example the bis-amino triazole compounds of following formula:
Figure 2011101335403100002DEST_PATH_IMAGE005
Comprise its tautomer and enantiomer, have the number-average molecular weight of about 200-about 3000, and contain about 80 carbon atoms of about 40-.The five-ring of this triazole is considered to aromatic.This aminotriazole is a quite stable for oxygenant, and hydrolysis extremely.Do not determine though it is believed that it, this reaction product be polyalkenyl two-3-amino-1,2, the 4-triazole.Such product has comprised high relatively a nitrogen content, is in a nitrogen content scope of the about 2.9wt% of about 1.8wt%-.
In other aspects of the present invention, disclosedly contain the A of additive and the Synergistic mixture of B can comprise the fuel-soluble carrier.Such carrier can be dissimilar, for example liquid or solid, for example wax.The example of liquid vehicle includes but not limited to mineral oil and oxygenate, for example liquid poly-alkoxylation ether (being also referred to as polyalkylene glycol or polyalkylene ether), liquid poly-alkoxylation phenol, liquid poly-alkoxylation ester, liquid poly-alkoxylation amine, and composition thereof.The example of oxygenate carrier fluid can find in US patent No.5752989, and this carrier all is incorporated herein by reference with it at this.The other example of oxygenate carrier fluid can comprise the aryl poly-alkoxylation thing that alkyl replaces, and its 17 days July in 2003 that is described in people such as Colucci, its explanation all was incorporated herein by reference with it at this among the disclosed US patent disclosure No.2003/0131527.
In other respects, this contains the A of additive and the Synergistic mixture of B can not contain carrier.For example, some compositions can not contain mineral oil or oxygenate, these for example above-mentioned oxygenate.
One or more optional in addition additives may reside in the fuel composition disclosed herein.For example this fuel composition can comprise defoamer, dispersion agent, stain remover, antioxidant, thermo-stabilizer, carrying object, metal passivator, dyestuff, markers, corrosion inhibitor, biocide, anti static additive, flow improver, friction modifiers, demulsifying compound, emulsifying agent, de-misting agent, the freezing additive, antiknock dope, tensio-active agent, the n-Hexadecane improving agent, corrosion inhibitor, cold flow improver, pour point reducer, solvent, demulsifying compound, slip additive, extreme pressure agent, viscosity index improver, the sealing swelling agent, amine stabiliser, combustion improving agent, dispersion agent, the specific conductivity improving agent, labeling dye, the organic nitrate ignition accelerator, manganese tricarbonyl compound and composition thereof.In some aspects, this fuel additive composition described herein can comprise about 10wt% or lower, and perhaps about in other respects 5wt% or one or more lower above-mentioned additives are based on the gross weight of this additive or fuel composition.Similarly, this fuel composition can comprise an amount of fuel mix composition for example methyl alcohol, ethanol, dialkyl ether or the like.
When preparation composition disclosed in this invention, disclosed additive can use with the amount that is enough to improve oxidized stability, described fuel is the midbarrel fuel that for example contains greater than at least a biofuel composition of 5 volume %, for example B7, B10, B20, B50 and B100 diesel oil fuel.In some respects, this fuel can comprise fuel and a spot of above-mentioned synergy compositions of additives of main amount.On the one hand, fuel of the present invention can comprise the amino-triazole compound thing (B) described herein that (based on activeconstituents) measured below: about about 100ppm of 1ppm-, for example about about 70ppm of 20ppm-.On the other hand, fuel composition disclosed in this invention can comprise the dispersion agent described herein (A) that (based on activeconstituents) measured below: about about 500ppm of 50-, for example about about 200ppm of 80ppm-.
Use therein in the aspect of carrier, this fuel composition can comprise the carrier that (based on activeconstituents) measured below: based on every kg fuel be the about 1000mg of about 10mg-carrier, for example carrier that is the about 700mg of about 25mg-based on every kg fuel.The activeconstituents basic weight does not comprise following weight: (i) relevant with the institute disclosed additive producing and use to remaining unreacted composition, (ii) used solvent (if existence) in disclosed additive is made, this solvent is in disclosed additive forming process or afterwards, but carrier (if using carrier) uses before adding.
Fuel dope of the present invention can be independent or be blended in the basic fuel so that different subgroups is incompatible.In some embodiments, additive component of the present invention is blended in the fuel when can use multifunctional additive for lubricating oils, because when being in the multifunctional additive for lubricating oils form, this has utilized by merging common phase capacitive and the convenience that described one-tenth branch provides.Equally, use enriched material can reduce mixing time and the wrong possibility of minimizing mixing.
The diesel oil fuel of disclosed embodiment can be used in the two in service of fixing diesel motor (for example in power generation assembly, the pumping plant etc. used engine) and on-fixed diesel motor (for example as the motive engine in automobile, truck, road sorting equipment, the military vehicle etc.).
In one embodiment, the diesel oil fuel that comprises biofuel of the present invention can be not have basically, does not for example have conventional metal passivation immunomodulator compounds.Term " does not have " to be defined as in this application such concentration basically, and it does not have the influence that can measure according to ASTM D-2274 basically for oxidative stability or insolubles formation.
Metal passivator (it can reduce or cancellation in the fuel that contains biofuel of the present invention) can comprise the condensation product of adjacent aromatic hydroxyl aldehyde and fatty amine.A typical example of such metal passivator is two salicylic aldehyde Alkylenediamines, and it is that condensation by the Alkylenediamine of the salicylic aldehyde of 2mol and 1mol prepares.Such metal passivator comprises for example salicylidene-meta-aminophenol, two inferior salicyl quadrols, two inferior salicyl propylene diamine, and N, N'-two inferior salicyl-1.
Embodiment
The following examples are exemplifying of exemplary embodiment of the present invention.At these embodiment and the application's elsewhere, whole umbers and per-cent are weight unit, unless indication is arranged in addition.The proposition purpose of these embodiment only is illustrative, and purpose and unrestricted scope of the present invention disclosed herein.
Embodiment 1
In the following embodiments, use the copper solutions of copper naphthenate that the copper of B7 diesel oil fuel with 2ppm is mixed, and determine the total insoluble substance in the fuel of 500ml according to ASTM D-2274 oxidation with 8wt% copper.Maximum insolubles according to ASTM D-2274 in the diesel oil fuel is a 2.5mg/100ml fuel.The total insoluble substance that does not contain the basic B7 fuel of the copper that adds to some extent is a 0.6mg/100ml fuel.Add copper, and, determine that this contains the fuel oxidation stability of at least a biofuel composition according to this fuel of ASTM method oxidation.
In whole tests, being used for above-mentioned additive (A) and carrier (B) is the mixture of Aromatic 150 and Aromatic 200.In following table, " MDA " is the metal passivator of aforesaid a kind of routine.Test-results is illustrated in the following table.
Table 1
Figure 2011101335403100002DEST_PATH_IMAGE007
As test 4 and 8-9 shown in, compare with basic fuel (test 1 and 2), the fuel that is combined as the oxidation that contains 2ppm copper of composition A and B provides the collaborative reduction of insolubles amount.Even when half treatment rate of composition A and B (test 10), compare with basic fuel (test 2), in the fuel of oxidation, also exist the collaborative reduction of total insoluble substance amount.The test 3 that contains composition A and MDA shows the raising that obviously is better than testing 1 basic fuel, and MDA is joined (test 11) do not show the test 12 that significantly is better than not containing test 4 and the 8-9 of MDA or contains MDA separately among composition A and the B.Therefore, can from contain fuel, cancel MDA, and when using the Synergistic mixture of composition A and B, still can improve oxidative stability greater than the biofuel composition of 5 volume %.
In sum, the present invention relates to following technical scheme:
1. method that is used to improve the oxidative stability of the fuel composition that comprises biofuel, this method comprises: the midbarrel fuel and a spot of Synergistic mixture that contain greater than at least a biofuel composition of about 5 volume % that will mainly measure merge, and the compound of the succinimide dispersants that this Synergistic mixture is replaced by (A) alkyl substantially and (B) following formula and tautomer thereof and enantiomer are formed:
Figure 358478DEST_PATH_IMAGE005
R wherein 2Be number-average molecular weight be the alkyl of 100-5000 and wherein the weight ratio of A:B be 2:1-10:1.
2. the method for scheme 1, wherein this ingredients of a mixture A comprises the reaction product of polyalkenyl succsinic acid or acid anhydrides and tetraethylene pentamine.
3. the method for scheme 2, wherein this polyalkenyl succsinic acid or acid anhydrides are the daltonian polyisobutene of 800-1100 derived from number-average molecular weight.
4. the method for scheme 3, wherein this polyisobutene comprises and has at least 60% or the highly reactive polyisobutenes of the two keys of more terminal olefine.
5. any one method among the scheme 1-4, wherein this midbarrel fuel comprises the A of 200-600ppm weight and the mixture of B.
6. any one method, wherein R among the scheme 1-5 2Be that number-average molecular weight is the daltonian polyolefine group of 200-3000.
7. any one method among the scheme 1-6, wherein this midbarrel fuel does not have two inferior salicyl Diaminoalkane compounds basically.
8. any one method among the scheme 1-7, wherein this total insoluble substance amount that contains the fuel of A and B is not more than 2.5mg/100ml, and this total insoluble substance amount is measured by ASTM D-2274.
9. any one method among the scheme 1-8, wherein this midbarrel fuel does not have metal passivator basically.
10. any one method among the scheme 1-9, wherein the weight ratio of A:B is the about 5:1 of about 3.5:1-in this midbarrel fuel.
11. the compound of the succinimide dispersants that the purposes of a Synergistic mixture, this mixture are replaced by (A) alkyl substantially and (B) following formula and tautomer thereof and enantiomer are formed:
Figure 157807DEST_PATH_IMAGE005
R wherein 2Be that number-average molecular weight is the alkyl of 100-5000, wherein the A:B weight ratio is 2:1-10:1, this mixture is used for containing the midbarrel fuel of at least a biofuel composition of at least 7 volume %, improve the oxidative stability of this fuel according to ASTM D-2274, wherein this fuel according to the oxidative stability of ASTM D-2274 less than the 2.5mg/100ml insolubles, in contrast, do not have the fuel oxidation stability of this Synergistic mixture greater than the 2.5mg/100ml insolubles.
12. the purposes of the mixture of scheme 11, wherein this ingredients of a mixture A comprises the reaction product of polyalkenyl succsinic acid or acid anhydrides and tetraethylene pentamine, and wherein this polyalkenyl succsinic acid or acid anhydrides are the daltonian polyisobutene of 800-1100 derived from number-average molecular weight.
13. the purposes of the mixture of scheme 12, wherein this polyisobutene comprises and has at least 60% or the highly reactive polyisobutenes of the two keys of more terminal olefine.
14. the purposes of any one mixture among the scheme 11-13, wherein this midbarrel fuel comprises the A of 200-600ppm weight and the mixture of B.
15. the purposes of any one mixture among the scheme 11-14, wherein this midbarrel fuel does not have metal passivator basically.
Should be noted in the discussion above that as used in this specification and the appended claims singulative " ", " a kind of " and " being somebody's turn to do " comprise the plural number indication, clearly and clearly are limited to outside the indication unless have in addition.Therefore, comprise the antioxidant that two or more are different when for example, mentioning " antioxidant ".As what use herein, term " comprise " and its grammatical variants purpose right and wrong determinate so that the project in the described tabulation is not got rid of other identical projects that can substitute or be increased to listed project.
In this specification and the appended claims, unless indication is arranged in addition, otherwise used other numerical value in whole numeral of expression amount, per-cent or ratio and specification sheets and the claim, being understood to be in whole situations is with term " approximately " correction.Therefore, unless opposite indication is arranged, the numerical parameter described in specification sheets below and the additional claim is about, and its expected performance that can look for acquisition according to the present invention changes.At least and not plan to limit the application of the theory of the scope that is equivalent to claim, each numerical parameter at least should be according to the significant digital value of being reported with by using common rounding method to explain.
Though described specific embodiment, applicant or others skilled in the art can expect can't expecting at present or the unforeseen option of possibility, change, variation, improvement and basic Equivalent.Therefore, the additional claim of applying date submission and their possible modification purposes are to comprise all such options, change, variation, improvement and basic Equivalent.

Claims (10)

1. method that is used to improve the oxidative stability of the fuel composition that comprises biofuel, this method comprises: the midbarrel fuel and a spot of Synergistic mixture that contain greater than at least a biofuel composition of about 5 volume % that will mainly measure merge, and the compound of the succinimide dispersants that this Synergistic mixture is replaced by (A) alkyl substantially and (B) following formula and tautomer thereof and enantiomer are formed:
R wherein 2Be number-average molecular weight be the alkyl of 100-5000 and wherein the weight ratio of A:B be 2:1-10:1.
2. the process of claim 1 wherein that this ingredients of a mixture A comprises the reaction product of polyalkenyl succsinic acid or acid anhydrides and tetraethylene pentamine.
3. the method for claim 2, wherein this polyisobutene comprises and has at least 60% or the highly reactive polyisobutenes of the two keys of more terminal olefine.
4. the method for any one, wherein R among the claim 1-3 2Be that number-average molecular weight is the daltonian polyolefine group of 200-3000.
5. the method for any one among the claim 1-4, wherein this midbarrel fuel does not have two inferior salicyl Diaminoalkane compounds basically.
6. the method for any one among the claim 1-5, wherein this total insoluble substance amount that contains the fuel of A and B is not more than 2.5mg/100ml, and this total insoluble substance amount is measured by ASTM D-2274.
7. the method for any one among the claim 1-6, wherein this midbarrel fuel does not have metal passivator basically.
8. the compound of the succinimide dispersants that the purposes of a Synergistic mixture, this mixture are replaced by (A) alkyl substantially and (B) following formula and tautomer thereof and enantiomer are formed:
Figure 348607DEST_PATH_IMAGE002
R wherein 2Be that number-average molecular weight is the alkyl of 100-5000, wherein the A:B weight ratio is 2:1-10:1, this mixture is used for containing the midbarrel fuel of at least a biofuel composition of at least 7 volume %, improve the oxidative stability of this fuel according to ASTM D-2274, wherein this fuel according to the oxidative stability of ASTM D-2274 less than the 2.5mg/100ml insolubles, in contrast, do not have the fuel oxidation stability of this Synergistic mixture greater than the 2.5mg/100ml insolubles.
9. the purposes of the mixture of claim 8, wherein this ingredients of a mixture A comprises the reaction product of polyalkenyl succsinic acid or acid anhydrides and tetraethylene pentamine, and wherein this polyalkenyl succsinic acid or acid anhydrides are the daltonian polyisobutene of 800-1100 derived from number-average molecular weight.
10. the purposes of the mixture of any one among the claim 8-9, wherein this midbarrel fuel comprises the A of 200-600ppm weight and the mixture of B.
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