WO2012084906A1 - Composition d'additif carburant à base d'une dispersion de particules de fer et d'un détergent - Google Patents
Composition d'additif carburant à base d'une dispersion de particules de fer et d'un détergent Download PDFInfo
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- WO2012084906A1 WO2012084906A1 PCT/EP2011/073348 EP2011073348W WO2012084906A1 WO 2012084906 A1 WO2012084906 A1 WO 2012084906A1 EP 2011073348 W EP2011073348 W EP 2011073348W WO 2012084906 A1 WO2012084906 A1 WO 2012084906A1
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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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0026—Preparation of sols containing a liquid organic phase
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0034—Additives, e.g. in view of promoting stabilisation or peptisation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0047—Preparation of sols containing a metal oxide
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- 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
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- C10L1/12—Inorganic compounds
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
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- 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
- C10L10/06—Use of additives to fuels or fires for particular purposes for facilitating soot removal
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- 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
- C10L10/18—Use of additives to fuels or fires for particular purposes use of detergents or dispersants for purposes not provided for in groups C10L10/02 - C10L10/16
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1233—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
- C10L1/1608—Well defined compounds, e.g. hexane, benzene
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- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
- C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
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- 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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- 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
- C10L1/192—Macromolecular compounds
- C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
- C10L1/2222—(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/234—Macromolecular compounds
- C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
- C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
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- C10L1/234—Macromolecular compounds
- C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
- C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
- C10L1/2387—Polyoxyalkyleneamines (poly)oxyalkylene amines and derivatives thereof (substituted by a macromolecular group containing 30C)
Definitions
- Fuel additive composition based on a dispersion of iron particles and a detergent
- the present invention relates to the combination of an organic dispersion of iron particles and a detergent in a composition especially useful as a fuel additive for internal combustion engines.
- soot carbonaceous particles
- a satisfactory solution is to introduce into the exhaust line a particulate filter (or FAP in the following text) that will block the soot in its channels to let escape a gas free of soot.
- FAP particulate filter
- the soot is burned to release the FAP channels.
- This step of regeneration of the FAP is usually done at temperatures above the gas temperature during a normal engine operation, the soot usually burning under air at temperatures above 650 ° C.
- a catalyst is generally employed which is intended to facilitate the oxidation of soot directly or indirectly.
- facilitating the oxidation of soot is meant to allow their oxidation at a lower temperature so that this temperature is more frequently reached during a normal engine operation. Part of the soot can be burned continuously during operation of the engine.
- the catalyst also makes it possible to lower the temperature required to regenerate the FAP so that the regeneration temperature is lower than the soot combustion temperature without the presence of said catalyst.
- the catalyst also makes it possible to accelerate the rate of oxidation of the soot, which makes it possible to reduce the time necessary for the regeneration of the FAP.
- New engine technologies such as diesel engines with common-rail and direct injection high-pressure fuel systems, are efficient but sensitive to fuel quality.
- deposits can form in particular in the injectors of diesel engines during their operation.
- the amount of deposit and their formation rate depend on the quality of the fuel used in the engine but also the nature of the fuel additives present therein.
- fuel additive herein means any additive that makes it possible to improve the distribution of fuel in the engine and / or to improve the operating performance of the engine and / or to improve the stability of the operation of the engine in the engine. time. Fuels that contain unstable components, such as the methyl esters of fatty acids typically found in biofuels, tend to form more deposits than mineral fuels do not contain.
- metals in fuels such as copper or zinc can lead to increased deposition quantities and thus levels of fouling of the injectors exacerbated.
- Metals in fuels come from different sources such as fuel and fuel distribution network or other contamination. Metals can also be deliberately introduced into the fuel as in the case of metal additives to aid the regeneration of FAP. Although these additives are beneficial for the regeneration of FAP and are thus desirable, some may promote deposition formation in the fuel system and particularly in fuel injectors.
- Deposits can lead to engine power loss and can eventually damage the engine. These deposits can also degrade the quality of combustion in the cylinders and lead to an increase in polluting emissions and fuel consumption of the engine. It is known that detergent additives reduce or eliminate the formation of deposits in the injectors.
- dispersions of rare earths in particular based on cerium, and / or iron, are known to be effective for the regeneration of FAP and contribute to the reduction of the temperature of FAP. oxidation of soot. These dispersions must have good dispersibility in the fuel in which they are introduced, high stability over time and sufficient catalytic activity at a relatively low concentration.
- Dispersions known to date do not always meet all these criteria. They may have, for example, good dispersibility but insufficient stability, especially when they are introduced into fuels containing fatty acid methyl esters or other readily oxidizable plant-based fuels. These dispersions may be sufficiently stable but have catalytic activity at metal concentrations that are too high to be economically attractive. Moreover, as indicated above, all these dispersions must have a limited impact on the operation of the fuel injectors, in particular lead to a limited fouling thereof, even in the presence of a fuel containing biofuel or a fuel containing metals. In addition, the presence of a BCF in the fuel can lead to reduce the fuel resistance to oxidation, especially when it contains biofuels.
- compositions comprising a FAP regeneration aid additive with good stability and which lead to a low fouling of the injectors and a limited reduction in the resistance to oxidation of the fuel, particularly in the presence of biofuel. .
- compositions comprising an additive having sufficient catalytic activity at a relatively low concentration.
- An object of the invention is to provide a composition well suited to this type of use.
- the invention provides a composition containing an additive to aid the regeneration of FAP in the form of an organic dispersion of iron particles in crystallized form and a detergent comprising a quaternary ammonium salt.
- the dispersion comprises particles of a crystallized iron compound of small size and at least one amphiphilic agent.
- the detergent may further include an oxygenated detergent.
- the invention also provides an additive fuel comprising a fuel and the composition previously described. More specifically, the invention relates to a composition comprising a dispersion and a detergent comprising a quaternary ammonium salt, said dispersion comprising:
- solid objects dispersed in the organic phase in the form of individualized particles or aggregates of particles, consisting of a compound of iron in crystallized form, such that said particles have an average size D DRX less than or equal to 12 nm measured by X-ray diffraction (XRD).
- XRD X-ray diffraction
- the dispersion of the composition according to the invention may be prepared according to a process comprising the following steps:
- the solid objects dispersed in the dispersions of the invention are individualized solid particles or aggregates of such particles. Said particles may, in addition, optionally contain residual amounts of bound or adsorbed ions such as, for example, sodium ions or ammonium ions.
- the dispersion of the composition of the invention has the advantage of being very stable. The particles of the dispersion of the invention do not sediment, and the dispersions do not decant, even after several months. In addition, it can have good compatibility with diesel fuels, including biofuels.
- the dispersion of the composition of the invention is a dispersion in the organic phase.
- the organic phase consists of at least 80%, preferably at least 90%, preferably at least 95% by weight of an organic solvent or a mixture of organic solvents, for example relative to the total mass of the organic phase.
- the organic phase optionally consists solely of an organic solvent or a mixture of organic solvents.
- This organic phase is chosen in particular according to the use of the dispersion.
- organic phase examples include aliphatic hydrocarbons such as hexane, heptane, octane, nonane, cycloaliphatic hydrocarbons such as cyclohexane, cyclopentane, cycloheptane, aromatic hydrocarbons such as benzene, toluene, ethylbenzene, xylenes, liquid naphthenes.
- aliphatic hydrocarbons such as hexane, heptane, octane, nonane
- cycloaliphatic hydrocarbons such as cyclohexane, cyclopentane, cycloheptane
- aromatic hydrocarbons such as benzene, toluene, ethylbenzene, xylenes, liquid naphthenes.
- oil cuts of the Isopar or Solvesso type (trademark registered by the company EXXON), in particular Isopar L or Solvesso 100 which essentially contains a mixture of methylethyl- and trimethylbenzene, Solvesso 150 which contains a mixture of alkylbenzenes in particular of dimethylbenzene and tetramethylbenzene.
- the organic phase can also consist of a petroleum cut.
- polar chlorinated hydrocarbons such as chloro- or dichlorobenzene, chlorotoluene.
- aliphatic and cycloaliphatic ethers as well as ketones, for example diisopropyl ether, dibutyl ether, methyl isobutyl ketone, diisobutyl ketone and mesityl oxide, may be envisaged.
- the organic phase may also advantageously be based on an apolar hydrocarbon, especially as the aliphatic hydrocarbons.
- Isopar-type petroleum fractions essentially containing isoparaffinic and parra-raffinic hydrocarbons at C-11 and C-12.
- the dispersion according to the invention comprises at least one amphiphilic agent.
- This amphiphilic agent has the effect of stabilizing the dispersion of particles. It also serves as a phase transfer agent during the preparation of the dispersions (between the aqueous phase and the organic phase).
- the amphiphilic agent is a carboxylic acid which generally comprises from 10 to 50 carbon atoms, preferably from 10 to 25 carbon atoms.
- This acid can be linear or branched. It can be chosen from aryl, aliphatic or arylaliphatic acids, optionally carrying other functions provided that these functions are stable in the environments where it is desired to use the dispersions according to the present invention.
- tall oil fatty acids such as tall oil fatty acids, soya oil, tallow, linseed oil, oleic acid, linoleic acid, stearic acid and its isomers, pelargonic acid, capric acid, lauric acid, myristic acid, dodecylbenzenesulfonic acid, 2-ethylhexanoic acid, naphthenic acid, hexoic acid.
- amphiphilic agent mention may be made of stearic acid and its isomers, for example a mixture of acids or products which contain chain length distributions such as Prisorine 3501 from Croda.
- This amphiphilic agent may also be composed of one or more polyacids such as succinic acids substituted with polybutenyl groups. These polyacids can be used alone or in combination with one or more aliphatic monocarboxylic acids containing between 10 and 20 carbon atoms on average.
- the oleic acid mixture with one or more succinic acids substituted with polybutenyl groups in which the polybutenyl groups have a mean molecular weight (measured by gas chromatography) of between 500 and 1300 and more. especially between 700 and 1000 g. mol "1 .
- the particles of the dispersion of the invention are based on an iron compound in crystallized form.
- This crystallized form which can be obtained by the implementation of the steps of the aforementioned method, can in particular be observed by the X-ray diffraction technique (XRD) which reveals peaks characteristic of at least one defined crystallized structure of the iron.
- XRD X-ray diffraction technique
- the solid objects of the dispersion of the invention are in the form of particles, or aggregates of particles, of an iron compound whose composition essentially corresponds to an iron oxide in crystallized form.
- the crystallized forms of the iron oxide constituting the particles according to the invention are typically Fe (III) oxides of the maghemite type (Y-Fe 2 O 3 ) and / or Fe (II) and Fe (III) oxides. ) of magnetite type (Fe 3 O 4 ).
- the aforementioned method generally makes it possible to obtain particles based on Fe (III) oxide of maghemite type and / or of Fe (III) and Fe (III) oxide of the magnetite type, the magnetite then being able to oxidize. in Fe (III) oxide of the maghemite type, for example in contact with oxygen.
- the particles of size greater than or equal to 4 nm in the dispersion are, for at least 90% of them, in the form of an iron compound in crystallized form, advantageously at least 95%, preferably at least 99%.
- XRD of the particles of the dispersion is less than or equal to 12 nm.
- the average particle size D DRX measured by XRD of the particles of the dispersion is less than or equal to 8 nm, preferably less than or equal to 7 nm, preferably less than or equal to 6 nm and advantageously less than or equal to 5 nm.
- this size is at least 4 nm.
- the crystalline nature of the particles according to the invention can in particular be demonstrated by XRD analysis.
- the DRX diagram defines two characteristics of these particles:
- the nature of the crystalline phase the position of the measured diffraction peaks and their relative intensity are characteristic of the magnetite or maghemite phase, the crystalline phase then corresponding to the ICDD sheet 01 -088-0315; and the average size D DRX of crystallites (or crystallized domains): this size is calculated from the width at mid-height of the diffraction peak of the crystallographic plane (440) of the maghemite / magnetite: with:
- ⁇ total width at mid-height of the line under consideration, expressed in degrees
- ⁇ diffraction angle (in radian) of the diffraction peak (440) of the magnetite and / or maghemite 0.547 rad.
- the DRX analysis can be carried out, for example, on a commercial apparatus of the X'Pert PRO MPD PANalytical type comprising in particular a g- ⁇ goniometer, enabling the characterization of liquid samples.
- the sample remains horizontal during the acquisition and it is the source and the detector that move.
- the bulk of the particles namely at least 80% in number, have a D MET size of less than or equal to 12 nm, more particularly less than or equal to 8 nm, preferably less than or equal to 7 nm, preferably less than or equal to 6 nm.
- At least 90% and more particularly at least 95% of the particles have a size D MET less than or equal to the above values.
- This size D MET can be demonstrated by analysis of the dispersion by transmission electron microscopy (TEM), used in an imaging mode to visualize at high magnification particles and to measure their size.
- TEM transmission electron microscopy
- the dispersion according to the invention is previously diluted with its solvent so as to reach a mass content of iron of approximately 0.035%.
- the dispersion thus diluted is then placed on an observation grid (like a carbon-based polymer membrane supported on a copper grid), and the solvent is evaporated.
- the principle of the method is to examine under different microscope regions (about 10) and to measure the dimensions of 250 particles, considering these particles as spherical particles.
- a particle is considered identifiable when at least half of its perimeter can be defined.
- the size D MET then corresponds to the diameter of the circle reproducing correctly the circumference of the particle.
- the identification of exploitable particles can be done using software such as: ImageJ, Adobe Photoshop or Analysis.
- the particles of the dispersion of the invention preferably have a fine particle size as observed by MET.
- They have a median diameter ⁇ 50 preferably between 3 nm and 12 nm, more particularly between 4 nm and 10 nm.
- the median diameter in number ⁇ 50 is the diameter such that 50% of the particles counted on TEM plates have a smaller diameter than this value, and 50% of the particles counted have a diameter greater than this value.
- the particles according to the invention preferably have a polydispersity index P n of 0.1 to 0.5.
- This polydispersity index P n is calculated from the particle size distribution determined by MET according to the following formula:
- the state of dispersion of solid objects can be characterized by dynamic light scattering (DDL), also called quasi-elastic light scattering (DQEL), or photon correlation spectroscopy.
- DDL dynamic light scattering
- DQEL quasi-elastic light scattering
- photon correlation spectroscopy This technique makes it possible to measure a hydrodynamic diameter D h of solid objects whose value is very strongly affected by the presence of particle aggregates.
- the solid objects of the invention have a hydrodynamic diameter D h of less than or equal to 50 nm, preferably less than or equal to 30 nm, preferably less than or equal to 20 nm, advantageously less than or equal to at 16 nm, measured by dynamic light scattering (DDL).
- DDL dynamic light scattering
- the hydrodynamic diameter D h of the solid objects of a dispersion according to the invention can be measured on the dispersion of the invention, after dilution thereof with its solvent so as to reach an iron concentration of 1 to 4 gL. "1 .
- An ALV CGS 3 (Malvern) light scattering apparatus with an ALV series 5000 correlator and ALV Correlator V3.0 software or higher can be used.
- This apparatus uses the so-called "Koppel cumulants" data processing method, which makes it possible to access the value of the hydrodynamic diameter D h .
- the experimental data are validated if the scattered intensity is stable and if the autocorrelation function is devoid of anomalies. Finally, the scattered intensity must be within defined limits for each device.
- This preferred feature of the objects of the dispersion increases its stability.
- the individualized nature of the particles also increases the overall contact surface available between them and the soot and thus contributes to the improvement of the catalytic activity of the dispersion according to the invention.
- the dispersions according to the invention may further comprise, in the organic phase, particles of an iron compound in amorphous form, in particular particles whose size is greater than or equal to 4 nm.
- the amorphous character of an iron compound can be demonstrated by XRD analysis of this compound, when no characteristic peak of any crystalline phase of iron is observed.
- the particles of an iron compound in amorphous form are at most 75% by number of the total amount of iron particles of the dispersion.
- the particles of an iron compound in amorphous form represent at most 50% by number of the total amount of iron particle of size greater than or equal to 4 nm, and so preferred at most 40% by number.
- the solid objects dispersed in the dispersion (DSP1) of the composition according to the invention are in the form of individualized particles or aggregates of particles, consisting of an iron compound in crystallized form, such as :
- said particles have a mean size D DRX less than or equal to 7 nm measured by X-ray diffraction (XRD);
- At least 80% by number of said particles have a D MET size less than or equal to 7 nm measured by transmission electron microscopy (TEM).
- the solid objects of this dispersion may preferably have a hydrodynamic diameter D h of less than or equal to 30 nm measured by dynamic light scattering (DDL).
- the organic phase of the dispersion (DSP2) of the composition according to the invention is an apolar organic phase and the solid objects dispersed in the dispersion of the composition according to the invention are in the form of individualized particles or aggregates of particles, consisting of an iron compound in crystallized form, such as:
- said solid objects have a hydrodynamic diameter D h of less than or equal to 30 nm measured by dynamic light scattering (DDL);
- said particles have a mean size D DRX less than or equal to 7 nm measured by X-ray diffraction (XRD);
- At least 80% by number of said particles have a D MET size less than or equal to 7 nm measured by transmission electron microscopy (TEM).
- TEM transmission electron microscopy
- the preferred or more particular values of the parameters D DRX , D h , D MET as well as the diameter ⁇ 50 and the index P n given above apply likewise here for the dispersions DSP 1 and DSP 2 insofar as these values also satisfy the limits given above in the statement of the characteristics of DSP 1 and DSP 2.
- the dispersions according to the invention have a mass concentration of iron compound which may be at least 2%, more particularly of at least 5%, this concentration being expressed as mass of metal iron relative to the total mass of the dispersion.
- This concentration can generally be up to 20%.
- the iron content can be determined by any technique known to those skilled in the art as by measurement by X-ray fluorescence spectroscopy applied directly to the dispersion according to the invention.
- the present invention also relates to a process for preparing the dispersions according to the invention.
- step a) of the process a base and a mixture comprising a salt of Fe (II) and a salt of Fe (III) are brought into contact in a molar ratio of Fe (II) / Fe (III) inclusive of 0.45 to 0.55, preferably about 0.5, preferably 0.5, in an aqueous phase, typically an aqueous solution of the base and iron salts.
- a base it is possible to use, in particular, compounds of the hydroxide type. There may be mentioned alkali or alkaline earth hydroxides and ammonia. It is also possible to use secondary, tertiary or quaternary amines.
- iron salt any water soluble salt can be used.
- the salt of Fe (II) mention may be made of ferric chloride FeCl 2 .
- the salt of Fe (III) mention may be made of ferric nitrate Fe (NO 3 ) 3 .
- step a) the reaction taking place between the Fe (II) salt, the Fe (III) salt and the base is generally carried out under conditions such that the pH of the reaction mixture formed remains greater than or equal to 8 when contacting the iron salts and the base in the reaction medium.
- the pH of the reaction mixture is maintained at a value greater than or equal to 8.
- This pH value is typically between 9 and 13.
- the iron salts and the base are brought into contact in the aqueous phase by introducing a solution of the iron salts into a solution containing the base, the pH of which is at least 8. It is also possible to introduce the iron salts and the base in a solution containing salts, at a concentration typically less than or equal to 3 mol.L "1 , such as for example sodium nitrate, and whose pH is previously adjusted to a value greater than or equal to 8. It is possible to carry out the contact continuously, the pH condition being achieved by adjusting the respective flow rates of the solution of the iron salts and the solution containing the base.
- the size of the particles can be modulated according to the pH at which the aqueous phase is maintained. Typically, and without wishing to be bound to a particular theory, the size of the particles is all the lower as the pH of the aqueous phase is high.
- the reaction of step a) is generally carried out at room temperature. This reaction can advantageously be carried out under an air or nitrogen atmosphere or a nitrogen-air mixture.
- a precipitate is obtained. It may be possible to ripen the precipitate by maintaining it for a certain time, for example a few hours, in the aqueous phase.
- the precipitate is not separated from the aqueous phase at the end of step a) and is left in suspension in the aqueous phase of the reaction of step a ).
- the process comprises, after step a) and before step b), a step a) of separation of the precipitate formed at the end of step a) of the aqueous phase.
- This step a) of separation is carried out by any known means.
- the separated precipitate can then be washed with water for example.
- the precipitate is not subjected to any drying or lyophilization step or any such operation.
- the precipitate may optionally be resuspended in a second aqueous phase.
- step b) In order to obtain a dispersion in the organic phase, during step b), the precipitate obtained at the end of step a), whether separated from the aqueous phase or not, is brought into contact with the organic phase. in which it is desired to obtain the dispersion.
- This organic phase is of the type described above.
- step b) is done in the presence of the aforementioned amphiphilic agent, optionally after neutralization of the suspension obtained at the end of step a).
- the molar ratio between the number of moles of amphiphilic agent and the number of moles of iron is between 0.2 and 1, preferably between 0.2 and 0.8.
- the amount of organic phase to be incorporated is adjusted so as to obtain an oxide concentration as mentioned above.
- the order of introduction during step b) of the different elements of the dispersion is indifferent.
- the precipitate obtained, the amphiphilic agent and the organic phase can be brought into contact simultaneously.
- the contacting between the precipitate and the organic phase can be carried out in a reactor which is under an atmosphere of air, nitrogen or an air-nitrogen mixture.
- the contacting between the precipitate and the organic phase can be carried out at ambient temperature, approximately 20 ° C., it is preferable to operate at a temperature chosen within a range of from 30 ° C. to ⁇ ⁇ ' ⁇ , advantageously between 40 ° C and 100 ° C.
- reaction mixture resulting from the precipitate, the organic phase and the amphiphilic agent is stirred for the duration of the heating.
- step a when the heating is stopped, there are two new phases: one phase organic containing the dispersion of particles, and a residual aqueous phase.
- the organic phase containing the dispersion of particles and the residual aqueous phase is then separated according to standard separation techniques, for example decantation or centrifugation.
- step b organic dispersions having the abovementioned characteristics are obtained.
- Dispersions further comprising particles of an iron compound in amorphous form can be obtained by mixing a first dispersion of particles of an iron compound in amorphous form in an organic phase with a second dispersion of particles of a composed of iron in crystallized form, this second dispersion being of the type according to the first embodiment of the invention.
- Dispersions whose organic phases are identical are preferably mixed.
- composition of the present invention comprises a detergent composition comprising a quaternary ammonium salt.
- the quaternary ammonium salt may be the reaction product:
- the quaternizing agent may comprise dialkyl sulfates, benzyl halides, hydrocarbon-substituted carbonates; hydrocarbon-substituted epoxides in combination with an acid or mixtures thereof.
- the compounds of components (i) (a), (i) (b) and (i) (c), described in more detail below, contain at least one tertiary amine function and cover compounds that can be alkylated to contain at least one tertiary amine function after an alkylation step.
- the quaternary ammonium salts can be prepared in the presence of a solvent, which may or may not be removed once the complete reaction.
- Suitable solvents include, but are not limited to, diluent oil, petroleum naphtha and certain alcohols.
- these alcohols contain at least 2 carbon atoms, and in other embodiments at least 4, at least 6 or at least 8 carbon atoms.
- the solvent of the present invention contains 2 to 20 carbon atoms, 4 to 16 carbon atoms, 6 to 12 carbon atoms, 8 to 10 carbon atoms, or only 8 carbon atoms.
- These alcohols normally carry a 2-alkyl C1-C4 substituent, namely methyl, ethyl, or any isomer of propyl or butyl.
- suitable alcohols include 2-methylheptanol, 2-methyldecanol, 2-ethylpentanol, 2-ethylhexanol, 2-ethylnonanol, 2-propylheptanol, 2-butylheptanol, 2-butyloctanol, isooctanol, dodecanol, cyclohexanol, methanol, ethanol, propan-1-ol, 2-methylpropan-2-ol, 2-methylpropan-1-ol, butan-1-ol, butan-2-ol, pentanol and its isomers, and mixtures thereof.
- the solvent of the present invention is 2-ethylhexanol, 2-ethylnonanol, 2-methylheptanol, or combinations thereof.
- the solvent of the present invention comprises 2-ethylhexanol. Quaternary ammonium salts of succinimide
- the quaternary ammonium salt detergent comprises the reaction product:
- Hydrocarbon-substituted acylating agents useful in the present invention include the reaction product of a long-chain hydrocarbon, generally a polyolefin, with a monounsaturated carboxylic acid or a derivative thereof.
- Suitable long-chain hydrocarbons for use in the preparation of the hydrocarbon-substituted acylating agents are any compound containing an olefinic bond, represented by the following general formula (I):
- each of R 1 , R 2 , R 3 , R 4 and R 5 independently represents a hydrogen atom or a hydrocarbon group.
- At least one of R 3 , R 4 or R 5 represents a hydrocarbon group containing at least 20 carbon atoms.
- long chain hydrocarbons which may also be described as polyolefins or olefin polymers, are reacted with the monounsaturated carboxylic acids and the derivatives described above to form the hydrocarbon-substituted acylating agents. used to prepare the nitrogenous detergent of the present invention.
- olefin polymers there may be mentioned polymers comprising a majority in moles of C 2 -C 20 or C 2 -C 5 mono-olefins.
- these olefins mention may be made of ethylene, propylene, butylene, isobutylene, pentene, octene-1 or styrene.
- the polymers may be homopolymers, such as polyisobutylene, as well as copolymers of two or more of these olefins.
- Suitable copolymers include copolymers of ethylene and propylene, butylene and isobutylene, and propylene and isobutylene.
- copolymers include those in which a minority by moles of the copolymer monomers, e.g., 1 to 10 mol%, a diolefin are C 4 to C 8.
- a copolymer of isobutylene and butadiene and a copolymer of ethylene, propylene and 1,4-hexadiene.
- At least one of the -R groups of the formula (I) indicated above is derived from polybutene, that is to say polymers of C 4 olefins, especially 1-butene, 2-butene and isobutylene.
- C 4 polymers that may be mentioned include polyisobutylene.
- At least one of the -R groups of the formula (I) is derived from polymers of ethylene and alpha-olefin, especially ethylene-propylene-diene polymers.
- polymers of ethylene and alpha-olefin especially ethylene-propylene-diene polymers.
- ethylene-propylene-diene polymers especially ethylene-propylene-diene polymers.
- the olefinic bonds of formula (I) are predominantly vinylidene groups, represented by the following formula (II):
- each R is a hydrocarbon group, which in some embodiments may be:
- R represents a hydrocarbon group
- the vinylidene content of formula (I) may be at least 30 mole percent vinylidene, at least 50 mole percent vinylidene, or at least 70 mole percent vinylidene.
- Such products and methods of preparation are described in US Patents 5,071,919, 5,137,978,
- the hydrocarbon-substituted acylating agent may be made by reacting a compound represented by the formula (I) with at least one carboxylic reactant represented by the following formulas (IV) and (V) :
- each of R 6 , R 8 and R 9 is independently H or a hydrocarbon group
- R 7 is a divalent hydrocarbon group
- n is 0 or 1.
- the hydrocarbon-substituted acylating agent can be made by reacting any compound represented by the formula (I) with any compound represented by the formula (IV) or the formula (V), the reaction being carried out in the presence of at least one aldehyde or at least one ketone.
- Suitable aldehydes include formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, isobutyraldehyde, pentanal, hexanal, heptaldehyde, octanal, benzaldehyde, as well as higher aldehydes.
- aldehydes such as dialdehydes, especially glyoxal, are useful, although monoaldehydes are generally preferred.
- the aldehyde is formaldehyde, which can be supplied in aqueous solution, often called formalin, but which is more often used in the polymeric form that is called paraformaldehyde.
- Paraformaldehyde is considered to be a reactive equivalent and / or a source of formaldehyde.
- Other reactive equivalents include cyclic hydrates or trimers.
- Suitable ketones include acetone, butanone, methyl ethyl ketone and other ketones.
- one of the two hydrocarbon groups of the ketone is a methyl group. Mixtures of two or more aldehydes and / or ketones are also useful. Such hydrocarbon-substituted acylating agents and methods for making them are disclosed in US Patents 5,840,920, 6,147,036 and 6,207,839.
- the hydrocarbon-substituted acylating agent may comprise methylene bisphenol-alkanoic acid compounds. Such compounds may be the condensation product
- each R independently represents a hydrocarbon group
- n is 0 or represents an integer from 1 to 6, with the proviso that m does not exceed the number of valencies of the corresponding Ar group available for substitution;
- Ar represents an aromatic group or group containing from 5 to 30 carbon atoms and from 0 to 3 optional substituents such as amino, hydroxy- or alkyl-polyoxyalkyl, nitro, aminoalkyl and carboxy groups, or combinations of two or more of two of said optional substituents;
- Z is independently -OH, -O, a lower alkoxy group or - (OR 10 ) b OR 11 wherein each R 10 independently represents a divalent hydrocarbyl group, b is a number from 1 to 30, and R 11 represents -H or a hydrocarbyl group; and
- - c is a number that ranges from 1 to 3.
- At least one hydrocarbon group on the aromatic group is derived from polybutene.
- the source of the hydrocarbon groups described above comes from polybutenes obtained by polymerization of isobutylene in the presence of a Lewis acid catalyst such as aluminum trichloride or boron trifluoride.
- a Lewis acid catalyst such as aluminum trichloride or boron trifluoride.
- reaction of (i) with (ii), optionally in the presence of an acid catalyst such as organic sulfonic acids, heteropolyacids and mineral acids may be carried out in the presence of at least one aldehyde or at least one ketone.
- an acid catalyst such as organic sulfonic acids, heteropolyacids and mineral acids.
- the quaternary ammonium salt detergents of succinimide are obtained by reacting the hydrocarbon-substituted acylating agent described above with a compound having an oxygen or nitrogen atom capable of condensing with the agent. acylation.
- the appropriate compounds contain at least one tertiary amine function.
- this compound may be represented by one of the following formulas (VII) and (VIII): HR
- each X independently represents an alkylene group containing 1 to 4 carbon atoms, and each R independently represents a hydrocarbon group.
- Suitable compounds include, but are not limited to: 1-aminopiperidine, 1- (2-aminoethyl) piperidine, 1- (3-aminopropyl) -2-pipecoline, 1-methyl- (4-methylamino) piperidine, 1-amino-2,6-dimethylpiperidine, 4- (1-pyrrolidinyl) piperidine, 1- (2-aminoethyl) pyrrolidine, 2- (2-aminoethyl) -1-methylpyrrolidine, ⁇ , ⁇ diethylethylenediamine, ⁇ , ⁇ -dimethylethylenediamine, N, N-dibutylethylenediamine, ⁇ , ⁇ , ⁇ '-trimethylethylenediamine, ⁇ , ⁇ -dimethyl-N'-ethylethylenediamine, ⁇ , ⁇ -diethyl-N'-methylethylenediamine , ⁇ , ⁇ , ⁇ '-triethylethylenediamine, 3-dimethyl
- the amine used is 3-dimethylaminopropylamine, 3-diethylamino-propylamine, 1- (2-aminoethyl) pyrrolidine, ⁇ , ⁇ -dimethylethylenediamine, or combinations thereof.
- aminoalkyl-substituted heterocyclic compounds such as 1- (3-aminopropyl) imidazole and 4- (3-aminopropyl) morpholine, 1- (2-aminoethyl) piperidine, 3, 3-diamino-N-methyldipropylamine, 3 ', 3-aminobis (N, N-dimethylpropylamine). These have been cited in the list above.
- alkanolamines including but not limited to triethanolamine, trimethanolamine, ⁇ , ⁇ -dimethylaminopropanol, N, N-diethylaminopropanol, ⁇ , ⁇ -diethylaminobutanol, N, N, N- tris (hydroxyethyl) amine and ⁇ , ⁇ , ⁇ -tris (hydroxymethyl) amine.
- the succinimide quaternary ammonium salt detergents of the present invention are formed by combining the reaction product described above (the reaction product of a hydrocarbon-substituted acylating agent and a compound having an atom). oxygen or nitrogen capable of condensing with said acylating agent and further comprising at least one tertiary amine function) with a quaternizing agent suitable for converting the tertiary amine function to quaternary nitrogen.
- Suitable quaternizing agents are detailed below.
- these preparations may be carried out without a solvent or in the presence of a solvent, as described above.
- preparations of quaternary ammonium salts of succinimide are given below.
- the polyisobutylene succinic anhydride (100 parts by weight), which is prepared by reaction of high vinylidene polyisobutylene of number average molecular weight 1000 and maleic anhydride, is heated to 80 ° C and is charged in a jacketed reactor equipped with a stirrer, a condenser, a feed pump attached to a sub-addition tube (adding under the surface of the reaction mixture), a nitrogen line and a thermocouple / temperature controller.
- the reactor is heated to 100 ° C.
- Dimethylaminopropylamine (10.9 parts by weight) is charged to the reaction, keeping the batch temperature below 120% within 8 hours.
- the reaction mixture is then heated to ⁇ ⁇ ' ⁇ and maintained at this temperature for 4 hours, to give a non-quaternized succinimide detergent.
- a non-quaternized succinimide detergent is prepared from a mixture of polyisobutylene succinic anhydride, as described above (100 parts by weight), and diluent oil - Pilot 900 (17.6 parts by weight) - which The mixture is heated with stirring at 1 ° C. under a nitrogen atmosphere. Dimethylaminopropylamine (DMAPA, 10.8 parts by weight) is added slowly over 45 minutes maintaining the batch temperature below 115 ° C. The reaction temperature is brought to ⁇ ⁇ ' ⁇ and maintained at this value for 3 more hours. The resulting compound is a non-quaternized succinimide detergent DMAPA.
- DMAPA Dimethylaminopropylamine
- this non-quaternized succinimide detergent (100 parts by weight) is heated with stirring to 90 ° C.
- Dimethyl sulfate (6.8 parts by weight) is charged to the reactor and stirring is resumed at 300 rpm under a blanket of nitrogen.
- the exothermic reaction that occurs raises the batch temperature to approximately ⁇ ⁇ ' ⁇ .
- the reaction is maintained at ⁇ ⁇ ' ⁇ for 3 hours before cooling and decantation.
- the resulting product contains a quaternary ammonium salt of dimethyl sulfate.
- the quaternary ammonium salt is the reaction product:
- Suitable polyalkene-substituted amines can be derived from an olefin polymer and an amine, such as ammonia, monoamines, polyamines or mixtures of these amines. They can be prepared by all kinds of processes. Suitable polyalkene-substituted amines or amines from which they are derived contain a tertiary amine function or may be alkylated until they contain a tertiary amine function, as long as the polyalkene-substituted amine has at least one amine function tertiary when it is reacted with the quaternization agent.
- One method for preparing a polyalkene-substituted amine is to react a halogenated olefin polymer with an amine, as disclosed in US Pat. Nos. 3,275,554, 3,438,757, 3,454,555, 3,565,804, 3,755,433 and US Pat. and 3,822,289.
- Another method of preparing a polyalkene-substituted amine is to react a hydro-formylated olefin with a polyamine and to hydrogenate the reaction product, as disclosed in US 5,567,845 and 5,496,383.
- Another method for preparing a polyalkene-substituted amine is to convert a polyalkene, using a conventional epoxidation reagent, with or without a catalyst, to the corresponding epoxide and to convert the epoxide to the polyalkene-substituted amine by reaction. with ammonia or an amine under reductive amination conditions, as disclosed in US 5,350,429.
- Another method of preparing a polyalkene-substituted amine is to hydrogenate a ⁇ -aminonitrile, prepared by reacting an amine with a nitrile, as disclosed in US Patent 5,492,641.
- Yet another method for preparing a polyalkene-substituted amine is to hydroformylate polybutene or polyisobutylene with a catalyst, such as rhodium or cobalt, in the presence of CO, H 2 and NH 3 at pressures and elevated temperatures, as disclosed in U.S. Patents 4,832,702, 5,496,383 and 5,567,845.
- a catalyst such as rhodium or cobalt
- the polyalkene-substituted amine can be derived from olefin polymers.
- the olefin polymers suitable for preparing the polyalkene-substituted amines of the invention are the same as those described above.
- the polyalkene-substituted amine may be derived from ammonia, monoamines, polyamines, or mixtures thereof, including mixtures of different monoamines, mixtures of different polyamines, and mixtures of monomamines and polyamines (which include diamines).
- Suitable amines include aliphatic, aromatic, heterocyclic and carbocyclic amines.
- the amines can be characterized by the formula:
- R 12 and R 13 each independently represent a hydrogen atom, a hydrocarbon group, an amino-substituted hydrocarbon group, a hydroxy-substituted hydrocarbon group, an alkoxy-substituted hydrocarbon group, or acylimidoyl groups, provided that not more than one of the radicals R 12 and R 13 represents a hydrogen atom.
- the amine can be characterized by the presence of at least one primary (H 2 N-) or secondary (HN ⁇ ) amino group.
- These amines, or the polyalkene-substituted amines they serve to prepare, may be alkylated if necessary to ensure that they contain at least one tertiary amine function.
- suitable monoamines include ethylamine, dimethylamine, diethylamine, n-butylamine, dibutylamine, allylamine, isobutylamine, cocoamine, stearylamine, laurylamine, methyllaurylamine, oleylamine, and the like. , N-methyloctylamine, dodecylamine, diethanolamine, morpholine and octadecylamine.
- alkyleneamines most of which correspond to the formula:
- n is an integer typically less than 10
- each R 14 independently represents a hydrogen atom or a hydrocarbon group typically having up to 30 carbon atoms
- the Alkylene group is typically an alkylene group having less than 8 atoms of carbon.
- alkyleneamines mention may be made mainly of ethyleneamines, hexyleneamines, heptyleneamines, octyleneamines and other polymethyleneamines. Specific examples of these are: ethylenediamine, diethylenetriamine, triethylenetetramine, propylenediamine, decamethylenediamine, octamethylenediamine, di (heptamethylene) triamine, tripropylenetetramine, tetraethylenepentamine, trimethylenediamine, pentaethylenehexamine, di (trimethylene) triamine, aminopropylmorpholine and dimethylaminopropylamine. Higher homologues such as those obtained by condensation of two or more of the alkyleneamines mentioned above are also useful. Tetraethylenepentamine is particularly useful.
- Ethylene amines also known as polyethylenepolyamines, are especially useful. They are described in detail in the "Ethylene Amines” section in Encyclopedia of Chemical Technology, Kirk and Othmer, Vol. 5, pp. 898-905, Interscience
- All polyalkene-substituted amines above, or the amines from which they are derived, which are secondary or primary amines, can be alkylated to amines Tertiary by means of alkylating agents before being reacted with the quaternizing agents to form the quaternary ammonium salt additives of the present invention.
- Suitable alkylating agents include the quaternizing agents listed below.
- the quaternary ammonium salts of polyalkene-substituted amines of the present invention are formed by combining the reaction product described above (the polyalkene-substituted amine having at least one tertiary amine function) with a suitable quaternizing agent. to convert the tertiary amine function to quaternary nitrogen.
- suitable quaternizing agents are detailed below.
- a preparation of a polyalkene-substituted amine quaternary ammonium salt is presented below.
- An apparatus suitable for the handling of chlorine and gaseous hydrogen chloride (glass reactor, glass stirrer, PTFE gaskets, thermocouple glass thermowells) is connected to sodium hydroxide scrubbers.
- the glass vessel is loaded with Mn 1000 low vinylidene polyisobutylene (PIB, 100 grams) and is heated to 110-120 ° C. Chlorine (70 grams) was bubbled into the reactor over a period of 7 hours. The reaction mixture is then flushed with nitrogen at 110-120 ° C overnight to remove HCl.
- PIB low vinylidene polyisobutylene
- PIB chloride is transferred to an autoclave and the autoclave is sealed.
- 1 mole of gaseous dimethylamine (DMA, 45 g) is added and the reaction is heated to 160-170 ° C and maintained at this temperature for 8 hours, or until that we no longer observe a drop in pressure.
- the reaction is cooled to room temperature and the pressure is released.
- Solvesso TM 150 solvent is added to obtain a 70% by weight solution of active ingredients and the reaction is stirred until it is homogeneous.
- the resulting polyisobutene dimethylamine solution (PIB-DMA) is transferred to a dropping funnel and washed twice with 2M sodium hydroxide solution to remove HCI and NaCl. After separation, the product is dried over MgSO 4 and filtered through a layer of Celite TM (diatomaceous earth).
- the resulting PIB-DMA solution (41 grams of 70% active substance solution) is charged to a glass reactor and stirred at room temperature.
- Dimethyl sulfate (3.3 grams) is added dropwise over one minute to give the quaternary ammonium salt.
- the mixture is stirred at room temperature for 1 hour under a blanket of nitrogen and is sampled and titrated with a green indicator of bromcresol.
- the resulting compound is a quaternary ammonium salt detergent of a polyalkene-substituted amine.
- the quaternary ammonium salt is the reaction product
- Suitable Mannich reaction products have at least one tertiary amine function and are prepared by reaction of a hydrocarbon-substituted phenol, an aldehyde and an amine.
- the hydrocarbon substituent of the hydrocarbon-substituted phenol may have 10 to 400 carbon atoms, in another case 30 to 180 carbon atoms, and in another case 10 to 40 to 10 carbon atoms.
- This hydrocarbon substituent may be derived from an olefin or a polyolefin.
- Useful olefins include alpha-olefins, such as 1-decene, which are commercially available.
- Suitable polyolefins include those described in the foregoing paragraphs.
- the hydrocarbon-substituted phenol can be prepared by alkylating a phenol with one of these suitable olefins or polyolefins, such as polyisobutylene or polypropylene, by well-known alkylation methods.
- the aldehyde used to form the Mannich detergent may have 1 to 10 carbon atoms, and is generally formaldehyde or a reactive equivalent thereof, such as formalin or paraformaldehyde.
- the amine used to form the Mannich detergent may be a monoamine or a polyamine.
- Suitable amines for preparing the Mannich reaction product of the invention are the same as those described in the foregoing paragraphs.
- the Mannich detergent is prepared by reaction of a hydrocarbon-substituted phenol, an aldehyde and an amine as described in US Patent 5,697,988.
- the Mannich reaction product is prepared from an alkylphenol derived from a polyisobutylene, formaldehyde and a primary monoamine, a secondary monoamine or an alkylenediamine.
- the amine is ethylenediamine or dimethylamine.
- Other suitable methods of preparing Mannich reaction products are found in US Pat. Nos. 5,876,468 and 5,876,468. As indicated above, it may be necessary, with some of the amines, to subsequently react the Mannich reaction product with an epoxide or carbonate, or other alkylating agent, to obtain the tertiary amine function.
- the Mannich quaternary ammonium salts of the present invention are formed by combining the reaction product described above (the Mannich reaction product having at least one tertiary amine function) with a quaternizing agent suitable for converting the amino function. Tertiary nitrogen in quaternary nitrogen. Suitable quaternizing agents are detailed below. By way of nonlimiting example, a preparation of a quaternary ammonium salt of Mannich is presented below.
- Alkylated phenol (800 g), which in turn is prepared from Mn 1000 polyisobutylene, and SO-44 diluent oil (240 g) are charged to a reactor as described above. A blanket of nitrogen is applied to the tank and the mixture is stirred at 100 rpm. To this mixture was added (dropwise) formalin (55.9 g) for 50 minutes. After that, dimethylamine (DMA, 73.3 g) was added dropwise (dropwise) over the next 50 minutes. The mixture is heated to 68 ° C and held for one hour at this temperature. The mixture is then heated to 106 ° C and held for another 2 hours at this temperature. The temperature of the mixture is then raised to 130 ° C. and maintained for 30 minutes at this temperature before allowing the mixture to come to room temperature. The mixture is purified by vacuum distillation (at 130 ° and -0.9 bar) to remove any remaining water to give a Mannich DMA.
- DMA dimethylamine
- the Mannich DMA (1700 g) is introduced into a reactor.
- Styrene oxide (1700 g) is introduced into a reactor.
- quaternizing agents suitable for preparing any of the quaternary ammonium salt detergents described above mention may be made of dialkyl sulphates, benzyl halides, substituted carbonates and the like. hydrocarbon, hydrocarbon-substituted epoxides used in combination with an acid, or mixtures thereof.
- the quaternizing agent comprises: halides such as chloride, iodide or bromide; hydroxides; sulfonates; alkyl sulfates such as dimethyl sulfate; sultones; phosphates; alkyl phosphates in CM 2, di-alkyl phosphates in CM 2; borates; C 1 -C 12 alkylborates; nitrites; nitrates; carbonates, bicarbonates, alkanoates, O-di-alkyl (d- 12 ) dithiophosphates, or mixtures thereof.
- the quaternizing agent may be: a dialkyl sulfate such as dimethyl sulfate, N-oxides, sultones such as propane or butane-sultone, alkyl halides, acyl or aralkyl such as methyl or ethyl chloride, bromide or iodide or benzyl chloride, hydrocarbyl (or alkyl) substituted carbonates, or combinations thereof. If the alkyl halide is benzyl chloride, the aromatic ring is optionally further substituted with alkyl or alkenyl groups.
- hydrocarbon (or alkyl) groups of the hydrocarbon-substituted carbonates may contain 1 to 50, 1 to 20, 1 to 10 or 1 to 5 carbon atoms per group.
- the hydrocarbon-substituted carbonates contain two hydrocarbon groups that may be the same or different.
- suitable hydrocarbon-substituted carbonates include dimethyl or diethyl carbonate.
- the quaternizing agent may be a hydrocarbon-substituted epoxide, having the following formula: (IX)
- R 15, R 16, R 17 and R 18 may independently represent H or a hydrocarbon group -C 50.
- suitable hydrocarbon-substituted epoxides include: styrene oxide, ethylene oxide, propylene oxide, butylene oxide, stilbene oxide, C 2 epoxides - 5 o, or combinations thereof.
- Suitable acids include carboxylic acids, such as acetic acid, propionic acid, butyric acid, and the like.
- the hydrocarbon-substituted acylating agent is polyisobutylene succinic anhydride and the compound comprising an oxygen or nitrogen atom capable of condensing said acylating agent is chosen from dimethylaminopropylamine, N-methyl- 1,3-diaminopropane, N, N-dimethylaminopropylamine, ⁇ , ⁇ -diethylaminopropylamine, N, N-dimethylaminoethylamine, diethylenetriamine, dipropylenetriamine, dibutylenetriamine, triethylenetetraamine, tetraethylenepentaamine, pentaethylenehexaamine, hexamethylenetetraamine, and bis (hexamethylene) triamine.
- Oxygenated detergent is polyisobutylene succinic anhydride and the compound comprising an oxygen or nitrogen atom capable of condensing said acylating agent.
- compositions of the present invention further comprise an oxygenated detergent additive.
- the oxygenated detergent additive may comprise a hydrocarbon compound bearing at least two substituents which are carboxy functions in the form of acids or at least one carboxy function in the form of anhydride.
- the oxygenated detergent additive is a hydrocarbon compound bearing at least two substituents which are carboxy functions in the form of acids or anhydrides.
- the oxygenated detergent additive is a hydrocarbon-substituted succinic acylating agent.
- the hydrocarbon-substituted oxygenated detergent additive is a dimeric acid compound.
- the hydrocarbon-substituted oxygenated detergent additive of the present invention comprises a combination of two or more of the oxygenated detergents described in this section.
- Suitable oxygen-containing hydrocarbon-substituted detergent additives include dimer acids.
- Dimer acids are a type of diacid polymer derived from fatty acids and / or polyolefins, especially the polyalkenes described herein, which contain an acid function.
- the dimer acid used in the present invention has been derived from polyolefins Cio to C 2 o, by d 2 to C 8 and / or of 6 to C 8.
- hydrocarbon-substituted oxygenated detergent additives mention may be made of acids, halides, succinic anhydrides, and combinations thereof.
- the agents are acids or anhydrides, and in other embodiments the agents are anhydrides, and in others Still further embodiments the agents are hydrolyzed anhydrides.
- the hydrocarbon compound of the substituted hydrocarbon additive and / or the primary hydrocarbon group of the hydrocarbon-substituted succinic acylating agent generally contains an average of at least 8, or 30, or 35 up to 350, or up to at 200, or up to 100 carbon atoms.
- the hydrocarbon group is derived from a polyalkene.
- Suitable polyalkenes include homopolymers and interpolymers of polymerizable olefin monomers of 2 to 16 or 6 or 4 carbon atoms.
- Suitable olefins and polyolefins include all those described in the foregoing headings.
- the olefin is a monoolefin such as ethylene, propylene, 1-butene, isobutene, and 1-octene, or a polyolefinic monomer, such as a diolefinic monomer, such as 1,3-butadiene and isoprene.
- the interpolymer is a homopolymer.
- An example of a polymer is polybutene.
- 50% of the polybutene comes from isobutylene.
- Polyalkenes are prepared by standard procedures.
- the hydrocarbon groups are derived from polyalkenes whose Mn value is at least 1300, or 1500, or 1600 to 5000, or up to 3000, or up to 2500, or up to at 2000, or up to 1800, and the Mw / Mn ratio is 1, 5 or 1, 8, or 2, or up to 2.5 to 3.6, or up to 3.2.
- the polyalkene is a polyisobutylene having a molecular weight of 800 to 1200.
- the substituted hydrocarbon substituted and / or substituted succinic acylating agents are prepared by reacting the polyalkene described above with an excess of maleic anhydride to give substituted succinic acylating agents in which the number of succinic groups for each equivalent weight of substituent group is at least 1, 3, or up to 1, 5, or up to 1, 7, or up to 1.8. The maximum number will generally not exceed 4.5, or up to 2.5, or up to 2.1, or up to 2.0.
- the polyalkene may here be any of those described above.
- the hydrocarbon and / or hydrocarbon group contains an average of 8, or 10, or 12 up to 40, or up to 30, or up to 24, or up to 20 atoms. of carbon.
- the hydrocarbon group contains an average of 16 to 18 carbon atoms.
- the olefin, olefin oligomer or polyalkene may be reacted with the carboxylic reagent such that there is at least one mole of carboxylic reagent per mole of olefin, olefin oligomer or polyalkene that reacts.
- the hydrocarbon-substituted oxygenated detergents and / or the hydrocarbon-substituted succinic acylating agents contain a diacid function.
- the hydrocarbon group of the hydrocarbon-substituted succinic acylating agent is derived from polyisobutylene and the diacid function of the agent is derived from carboxylic acid groups, such as a hydrocarbon-substituted succinic acid.
- the hydrocarbon-substituted acylating agent comprises one or more hydrocarbon-substituted succinic anhydride groups.
- the hydrocarbon-substituted acylating agent comprises one or more hydrolyzed hydrocarbon-substituted succinic anhydride groups.
- the oxygenated detergent is a polyisobutylene compound having a succinic anhydride or succinic acid headgroup.
- the oxygenated detergent may be a polyisobutylene succinic anhydride and / or a hydrolysed version thereof.
- the preparation of suitable oxygenated detergents is described in International Patent Application WO 2006/063161 A2.
- Example 0-1 Glissopal TM 1000 (18.18 kg) is loaded into a sealed vessel at 100 ° C and stirred. The vessel is heated to ⁇ ⁇ 67 ° C and a vacuum is applied. The vessel is then pressurized with a nitrogen atmosphere (1 bar) while it is heated to M5 ° C. Once the product has reached M5 ° C, maleic anhydride (2.32 kg) is added using a heated double-jacketed syringe pump (ISCO pump) in approximately 9 hours. hours. The reaction temperature is raised slowly, throughout the maleic anhydride feed, from 175 ° C. to 225 ° C. at the end of the reaction time. load. The reaction is then maintained at 225 ° C for a further 10 hours.
- ISCO pump heated double-jacketed syringe pump
- the resulting polyisobutylene succinic anhydride has a kinematic viscosity at ⁇ ⁇ ' ⁇ of 570 cSt (mm / s) and a total acid number (TAN) of 127 mg KOH / g.
- PIBSA polyisobutylene succinic anhydride
- the PIBSA of Example 0-1 (340 g) was charged to a reactor and mixed with Pilot TM 900 (60 g). The contents of the tank are stirred at 400 rpm for 1 hour and then heated to 90 ° C. The vessel is then charged with nitrogen to provide an inert atmosphere. Water (5.9 g) is added to the mixture over 10 minutes. The mixture is then stirred for 2 hours.
- the resulting hydrolysed PIBSA has a total acid number of 163 mg / KOH and a kinematic viscosity at ⁇ ⁇ ' ⁇ of 500 mm / s (cSt).
- the product formed contains 85% by weight of hydrolysed product and 15% by weight of Pilot® 900.
- the carbonyl / water ratio is 0.5 / 1.
- the weight ratio of the quaternary ammonium salt detergent to the oxygenated detergent may be from 1/10 to 10 1, 1/8 to 8/1, 1/1 to 8/1 or 3/1 to 7/1, all weight ratios being calculated on a non-solvent basis. In other embodiments, the weight ratio can be from 2/1 to 4/1.
- hydrocarbon substituent or "hydrocarbon group” is used in its ordinary sense, which is well known to those skilled in the art. To be more precise, it denotes a group comprising a carbon atom attached directly to the rest of the molecule and having a predominantly hydrocarbon character.
- hydrocarbon groups examples include: hydrocarbon substituents, that is to say aliphatic (for example alkyl or alkenyl), alicyclic (for example cycloalkyl, cycloalkenyl) substituents and aromatic, aliphatic and aromatic-substituted aromatic substituents; alicyclic, as well as cyclic substituents in which the ring is supplemented by another part of the molecule (for example two substituents together form a ring); substituted hydrocarbon substituents, i.e., substituents containing non-hydrocarbon groups which, in the context of this invention, do not alter the predominantly hydrocarbon nature of the substituent (e.g.
- hetero-substituents that is, substituents which, while having a predominantly hydrocarbon character, in the context of this invention, contain something other than carbon in a ring or chain which is otherwise composed of carbon atoms .
- heteroatoms mention may be made of sulfur, oxygen and nitrogen, and this covers substituents such as pyridyl, furyl, thienyl and imidazolyl.
- no more than two, preferably no more than one, non-hydrocarbon substituent will be present per group of 10 carbon atoms in the hydrocarbon group, and typically there will be no non-hydrocarbon substituents in the group. hydrocarbon.
- the present invention also relates to a process for preparing the composition according to the invention, said process comprising a step of contacting and mixing a detergent and a dispersion according to the invention, whereby the composition is obtained. .
- composition of the invention that is to say the composition containing the additive to aid the regeneration of FAP in the form of a dispersion of particles of an iron compound in crystallized form and the detergent, can be obtained by mixing the detergent composition and the dispersion by any conventional means for mixing, which mixture is generally obtained by stirring at a temperature close to room temperature (from 15 to 30 ° C).
- the weight ratio between the dispersion and the detergent composition can vary greatly depending on various parameters such as the characteristics of the engine and its equipment including fuel injectors, its polluting emissions, including the amount of soot emitted, the architecture of the line of exhaust and depollution, including the use of a FAP or Catalyzed Filter containing a catalyst and its promixity of the collector of the engine, the means for increasing the temperature to trigger regeneration or the geographical area in which the vehicle will circulate, the latter defining the quality of the fuel that the vehicle will use.
- This weight ratio between the dispersion and the detergent composition can typically vary between 10/90 and 90/10, in some cases between 20/80 and 80/20, and in some cases even more accurate between 30/70 and 70/30.
- the ratio can be advantageously chosen above 50/50, that is to say with a greater proportion of dispersion than detergent.
- the iron content may be between 0.05% and 25%, more particularly between 2% and 15%, this concentration being expressed in% by weight of iron metal relative to the total weight of the composition.
- the organic dispersions according to the invention have the particularity, once added to the fuel, of not significantly reducing the stability of said fuel, particularly when it contains unstable fractions such as biofuel fractions such as methyl esters of dicarboxylic acid. 'vegetal oils. Fuel stability can be measured through its resistance to oxidation.
- Another type of test consists in quantifying, by chemical dosing (as per ISO 6619), the increase in acidity of the fuel heated following the bubbling of oxygen (aging test EN ISO 12205 (petroleum products - Determination of the oxidation stability of middle distillates of oil (1996))
- the evolution of the acidity is expressed as a function of the difference in acidity or ⁇ between aged and unaged fuel The higher the ⁇ , the more the fuel has been oxidized.
- the invention also relates to an additive fuel comprising a fuel and a composition according to the invention.
- the invention also relates to a method for preparing an additive fuel according to the invention, comprising a step of contacting and mixing a fuel and a composition according to the invention, whereby the fuel is obtained. additive.
- compositions according to the invention can be used as a fuel additive for internal combustion engines, more particularly as a fuel additive.
- diesel fuel oils or other engines such as certain gasoline engines emitting soot or carbonaceous particles, and for example as biofuel additives.
- They can more generally be used as combustion additives in fuels or liquid fuels of energy generators such as internal combustion engines (combustion engines), generators, oil burners, or jet engines.
- energy generators such as internal combustion engines (combustion engines), generators, oil burners, or jet engines.
- the fuels with additives according to the invention can be used in combination with a FAP containing no catalyst, or with a FAP containing a catalyst, such as a CSF.
- the nature of the catalyst component CSF can be of any type including precious metals such as platinum or palladium associated with various support materials or binder such as alumina. Reducible materials such as rare earth oxides, such as cerium oxide or manganese-based oxides may also be associated.
- compositions according to the invention may be additive to fuels according to any means known to those skilled in the art, both by a vectorization device on board the vehicle but also directly additive in the fuel before it is introduced into the vehicle. This last case can be advantageously used in the case of fleets of vehicles equipped with FAP and having their own service station to refill the full of fuel.
- FBC Fuel Borne Catalyst
- the devices on board the vehicle may in particular be devices comprising a tank, for loading a volume of the composition according to the invention and to cover a certain autonomy, and a means of vectorization of the composition to the fuel as a metering pump injecting a defined amount of the composition into the fuel tank of the vehicle and a steering tool of the vectorization means.
- the engine can be fed continuously with a fuel additive FBC, the concentration can be stable or variable over time.
- the engine can also be fed alternately with a fuel additive and non-additive.
- the amount of BCF to add to the fuel can vary greatly depending on various parameters such as the characteristics of the engine and its equipment, its polluting emissions, including the amount of soot emitted, the architecture of the exhaust and depollution line, in particular the use of a FAP or CSF containing a catalyst and its promixity of the engine manifold, the means for increasing the temperature to trigger the regeneration or the geographical area in which the vehicle will circulate, the latter defining the quality of the fuel that the vehicle will use.
- the BCF can also be injected into the exhaust line upstream of the FAP, preferably by a means for finally dispersing the particles in the soot bed.
- This case is particularly suitable in the case where the regeneration of the FAP is done by direct injection of fuel in the exhaust line upstream of the FAP, that this fuel is burned on an oxidation catalyst upstream of the FAP or by a burner or by any other means.
- the fuel included in the fuel additive is selected from the group consisting of gas oils and biofuels.
- Suitable fuels for the preparation of an additive fuel according to the present invention include, in particular, commercially available fuels and, in some embodiments, all commercially available diesel fuels and / or biofuels.
- Diesel fuels can also be called diesel fuels.
- Biofuels are also called biofuels.
- Appropriate fuels in the implementation of the present invention are not limited too, and are usually liquid at room temperature, for example 20 to 30 ⁇ €.
- the liquid fuel may be a hydrocarbon fuel, a fuel other than a hydrocarbon, or a mixture thereof.
- the hydrocarbon-type fuel may be a petroleum distillate, such as a gasoline as defined by ASTM D4814, or a diesel fuel, as defined by ASTM D975 or European Standard EN590 + A1.
- the liquid fuel is a gasoline, and in another embodiment the liquid fuel is unleaded gasoline.
- the liquid fuel is a diesel fuel.
- the hydrocarbon fuel may be a hydrocarbon prepared by a process of converting a gas to a liquid to include, for example, hydrocarbons made by a process such as the Fischer-Tropsch process.
- the fuel used in the present invention is a diesel fuel, a diesel fuel, or combinations thereof.
- the non-hydrocarbon fuel may be an oxygen-containing composition, often referred to as an oxygenation product, which comprises an alcohol, an ether, a ketone, an ester of a carboxylic acid , a nitroalkane, or a mixture thereof.
- the fuel other than a hydrocarbon may comprise, for example, methanol, ethanol, methyl t-butyl ether, methyl ethyl ketone, trans-esterified oils and / or fats of plant or animal origin, such as rapeseed methyl ester and soy methyl ester, and nitromethane.
- Mixtures of hydrocarbon and non-hydrocarbon type fuels may include, for example, gasoline and methanol and / or ethanol, diesel fuel and ethanol, and diesel fuel and a trans-esterified vegetable oil such as rapeseed methyl ester and other bio-derived fuels.
- the liquid fuel is a water emulsion in a hydrocarbon type fuel, a fuel other than a hydrocarbon, or a mixture thereof.
- the liquid fuel may have a sulfur content, on a weight basis, of 5000 ppm or less, 1000 ppm or less, 300 ppm or less, 200 ppm or less. less, 30 ppm or less, or 10 ppm or less.
- the liquid fuel of the invention is present in an additive fuel according to the invention in a predominant amount, that is to say generally greater than 95% by weight, and in other embodiments it is present in a larger quantity. at 97% by weight, greater than 99.5% by weight, or greater than 99.9% by weight.
- Suitable fuels for carrying out the present invention optionally include one or more additional performance additives, solvents or diluents. These performance additives can be of any type and make it possible, for example, to improve the fuel distribution in the engine and / or to improve the performance of the engine operation and / or to improve the stability of the operation of the engine.
- antioxidants such as sterically hindered phenol, detergent and / or dispersant additives such as nitrogen detergents or succinimides or cold flow improvers such as a copolymer of maleic anhydride and esterified styrene.
- the compositions of the present invention may further comprise one or more additional performance additives, solvents or diluents.
- Additional performance additives may include: an antioxidant such as a hindered phenol or a derivative thereof and / or a diarylamine or a derivative thereof; a corrosion inhibitor; and / or a detergent / dispersant additive, other than the fuel additive of the present invention, such as a polyetheramine or a nitrogen detergent, including, but not limited to, PIB-amine detergents / dispersants and succinimide detergents / dispersants .
- an antioxidant such as a hindered phenol or a derivative thereof and / or a diarylamine or a derivative thereof
- a corrosion inhibitor such as a corrosion inhibitor
- / or a detergent / dispersant additive other than the fuel additive of the present invention, such as a polyetheramine or a nitrogen detergent, including, but not limited to, PIB-amine detergents / dispersants and succinimide detergents / dispersants .
- the additional performance additives may also include: a cold flow improver such as a copolymer of maleic anhydride and esterified styrene and / or a copolymer of ethylene and vinyl acetate; a foam inhibitor and / or an antifoam agent such as silicone oil; a demulsifier such as a polyalkoxylated alcohol; a lubricity agent such as a carboxylic fatty acid; a metal deactivator such as an aromatic triazole or a derivative thereof, including but not limited to benzotriazole; and / or an additive against recession of the valve seats such as an alkali metal sulfosuccinate salt.
- a cold flow improver such as a copolymer of maleic anhydride and esterified styrene and / or a copolymer of ethylene and vinyl acetate
- a foam inhibitor and / or an antifoam agent such as silicone oil
- a demulsifier such as a
- the combined total amount of additional performance additive compounds present, on a solvent / oil-free basis, may range from 0 or 0.01% by weight to 65, 50 or even 25% by weight, or 0.01% by weight to 20% by weight of the composition. Although one or more of the other performance additives may be present, it is common for the other performance additives to be present in different amounts relative to each other.
- the invention also relates to a method of implementing an internal combustion engine comprising a step of conveying to said engine a fuel and a composition according to the invention.
- composition of the invention is combined with the direct addition fuel and the additive fuel is used to operate an engine equipped with an exhaust system with a FAP or CSF.
- the additive fuel containing the composition of the invention can be contained in a fuel tank, transmitted to the engine where it is burned, and the iron oxide particles reduce the oxidation temperature of the soot collected in the FAP.
- the above procedure is used except that the composition of the invention is kept on board the engine-driven apparatus. (eg an automobile, a bus, a truck, etc.) in a tank with a separate fuel composition.
- the composition is combined or mixed with the fuel during engine operation.
- composition of the invention may be added to the fuel in an amount such that the mass content of iron in the additive fuel is from 1 ppm to 50 ppm, more particularly from 2 ppm to 20 ppm, to iron metal relative to the mass. total fuel.
- suitable internal combustion engines include spark ignition engines and compression ignition engines; 2-cycle or 4-stroke cycles; a liquid fuel obtained by direct injection, indirect injection, jet injection and carburettor; current rail injector and pump injector systems; engines for light vehicles (eg passenger car) and heavy vehicles (eg commercial truck); and engines that operate with hydrocarbon and non-hydrocarbon fuels and mixtures thereof.
- Engines may be part of integrated emission systems containing elements such as EGR systems; aftertreatment including a three-way catalyst, an oxidation catalyst, NOx absorbers and catalysts, catalyzed and uncatalyzed particle traps; a variable distribution; and injection timing and flow configuration.
- One liter of solution is prepared in the following manner: 576 g of Fe (NO 3 ) 3 are mixed with 99.4 g of FeCl 2 , 4 H 2 O. The mixture is supplemented with distilled water to obtain a liter of solution. The final concentration of this iron precursor solution is 1.5 mol.L -1 in Fe.
- a solution of NaOH 6 mol.L "1 is prepared in the following manner: 240 g of sodium hydroxide pellets are diluted in distilled water to obtain a liter of solution.
- a stock solution composed of 400 ml of sodium nitrate solution NaN0 3 to 3 mol.L "1 is introduced .
- the pH of the solution is adjusted to 1 1 with the aid of a few drops of soda at 6 mol / L.
- the formation of the precipitate is carried out by simultaneous addition of the iron precursor solution and the sodium hydroxide solution prepared previously. reagents are adjusted so that the pH is kept constant and equal to 1 1 at room temperature.
- This organic dispersion has a mass content of iron of 10%, expressed as mass of metal iron relative to the total mass of the dispersion collected.
- the iron content is determined by X-ray fluorescence analysis directly on the dispersion. This same technique is used in the following examples to control the iron content.
- One liter of solution is prepared in the following manner: 576 g of Fe (NO 3 ) 3 are mixed with 99.4 g of FeCl 2 , 4 H 2 O. The mixture is supplemented with distilled water to obtain a liter of solution. The final concentration of this iron precursor solution is 1.5 mol.L -1 in Fe.
- a solution of NaOH 6 mol.L "1 is prepared in the following manner: 240 g of sodium hydroxide pellets are diluted in distilled water to obtain a liter of solution.
- a stock solution composed of 400 ml of sodium nitrate solution NaN0 3 to 3 mol.L "1 is introduced .
- the pH of the solution is adjusted to 13 with the aid of a few drops of soda at 6 mol / L.
- the formation of the precipitate is carried out by simultaneous addition of the iron precursor solution and the sodium hydroxide solution prepared previously, the introduction rates of these two reagents. are adjusted so that the pH is kept constant and equal to 13 at room temperature.
- This organic dispersion has a mass content of iron of 10%, expressed as mass of metal iron relative to the total mass of the dispersion collected. Characterization by X-ray diffraction (XRD)
- the XRD analysis of the dispersions of Example 1 was carried out according to the indications given in the description. It can be seen that the diffractogram peaks of the dispersion 1A and of the dispersion 1B correspond to the diffraction peaks characteristic of the crystallized magnetite and / or maghemite crystalline phase (sheet ICDD 01 -088-0315).
- the TEM analysis was performed according to the indications given in the description.
- a detergent composition consisting of a quaternary ammonium salt of succinimide derived from succinimide dimethylaminopropylamine, alcohol 2-ethylhexyl and acetic acid, and quaternized with propylene oxide and prepared by a method substantially similar to that described in Example Q-1 above.
- a detergent composition is prepared by mixing 50 parts by weight of the quaternary ammonium succinimide salt of Example 2A with 18 parts by weight of oxygenated detergent, all parts by weight being calculated on a solvent-free basis. The mixture of constituents is carried out under ambient conditions.
- the oxygenated detergent is a polyisobutylene succinic polyisobutylene anhydride of high vinylidene content having a number average molecular weight of 1000 and maleic anhydride and is prepared by a method substantially similar to that described in Example 0-1.
- a detergent composition is prepared according to the procedures of Example 2B except that 35 parts by weight of the quaternary ammonium salt of succinimide is used with 9 parts by weight of the oxygenated detergent, all parts by weight being calculated on a base without solvent.
- a detergent composition is prepared according to the procedures of Example 2B except that the oxygenated detergent is hydrolyzed by reaction with water to form a polyisobutylene succinic acid prepared by a method substantially similar to that described in Example 0 -2.
- a detergent composition is prepared according to the procedures of Example 2A, except that the quaternary ammonium salt of succinimide is derived from dimethylaminopropylamine succinimide and dimethyl sulfate and is prepared by a process substantially similar to that described in US Pat.
- Example Q-2 except that more solvent is present to give a mixture having a level of active substances of 65% by weight in petroleum naphtha solvent.
- a detergent composition is prepared according to the procedures of Example 2C except that the oxygenated detergent is hydrolysed by reaction with water to form a polyisobutylene succinic acid prepared by a method substantially similar to that described in Example 0-2.
- Eight fuel additive compositions (3A to 31) consisting of mixtures of the dispersions 1A or 1B of Example 1 and detergents of Examples 2A or 2F are prepared by mixing at room temperature each liquid in controlled proportions.
- composition 3B contains 4.3% by weight of iron metal.
- compositions are prepared in the same manner using controlled amounts of 1A or 1B dispersions, detergents of Example 2A or 2F and any solvent.
- Table 3 shows the amounts of each component for the various compositions as well as their iron content.
- Table 3 Composition of additives and iron content% solvent detergent dispersion
- An additive fuel is prepared to measure the stability of the compositions according to the invention with said fuel. For this, a certain amount of composition is added to the fuel in order to reach a mass concentration of 7 ppm of iron metal in the fuel. The additive fuel is then continuously heated to 70 ° C. and the stability period of the additive composition is quantified.
- the additive composition is considered stable when the iron content in the fuel has not decreased by more than 10%.
- the fuel used here is a fuel containing approximately 1% by weight of biofuel (fatty acid methyl ester or FAME) (Table 4).
- a precise quantity of each of the additive compositions is added to 250 ml of fuel so as to obtain, after homogenization, 7 ppm of iron metal in the fuel and the possible presence of one or more detergent molecules according to the composition added:
- composition 20.2 mg.
- the evolution of the iron content in the fuel is quantified by means of a regular sampling of a volume of 20 ml of fuel in the upper part of the fuel. This volume, once filtered at 0.2 ⁇ , is analyzed by X Fluorescence to determine the iron content.
- compositions 3B to 31 according to US Pat.
- the invention has a significantly increased stability over the composition 3A without detergent, since no decrease in the iron content is measured after 50 days of continuous heating at 70 ° C of the fuels with additives.
- the stability of the compositions according to the invention is therefore greater than 50 days at 70 ° C.
- the compatibility of the type B10 fuel used in Example 4 is measured with addition of the additive compositions of Example 3 (3A, 3B, 3C, 3D, 3E, 3F, and 3G).
- compositions 3B to 31 show that in the presence of compositions containing a detergent containing at least one quaternary ammonium salt (compositions 3B to 31), the induction time of the additive fuel is higher than for the additive fuel of the composition 3A alone. (not containing a quaternary ammonium detergent), which reflects a lower oxidation of the fuel and thus a better compatibility.
- the downstream exhaust line is a commercial line composed of an oxidation catalyst containing a platinum-alumina washcoat followed by a silicon carbide FAP (FAP total volume 2.52 L, diameter 5.66 inches, length 5.87 inches).
- the fuel used is a commercial fuel meeting the EN590 DIN 51628 standard containing less than 10 ppm of sulfur and containing 7% by volume of EMAG.
- the fuel is additive of the various compositions 3B and 3E of Example 3.
- the content of the added composition is adjusted so as to add to the fuel a quantity of composition corresponding to 7 ppm by weight (composition 3B) or 5 ppm weight (composition 3E) of iron expressed in the form of metal iron relative to the total mass of fuel.
- composition 3B 7 ppm by weight
- composition 3E 5 ppm weight
- the test is performed in two successive steps: a step of loading the FAP, followed by a step of regeneration thereof.
- the conditions of these two stages are strictly identical for the three tests, apart from the fuel used (additive or not).
- the loading phase is carried out by operating the engine at a speed of 3000 rpm and using a torque of 45 Nm for approximately 6 hours. This loading phase is stopped when 12 g of particulate phases are loaded into the FAP. During this phase the temperature of the gases upstream of the FAP is from 230 to 235 ° C. Under these conditions the particle emissions are about 2 g / h.
- the FAP is disassembled and weighed in order to control the mass of charged particles during this phase (amount of particulate phase in the FAP after loading Table 7).
- the FAP is then reassembled on the bench and warmed by the engine which is reset for 30 minutes in the operating conditions of the load (3000 rpm / 45 Nm).
- the engine conditions are then modified (torque 80 Nm / 2000 rpm) and a post-injection is requested from the engine's electronic central unit (ECU), which makes it possible to raise the temperature upstream of the FAP to 450 ° C and to start the regeneration of the FAP. These conditions are maintained for 35 minutes (2100 seconds), this time being counted from the start of the post-injection.
- ECU electronic central unit
- the regeneration efficiency of the FAP is measured through two parameters: the% burned soot, which corresponds to the soot combustion rate calculated at each instant t as a function of the reduction of the pressure drop AP (t):
- AP start of regeneration 100% burned soot corresponding to the stabilization of the pressure drop at the lowest level observed under these conditions with a DPF containing no soot.
- start of regeneration 100% burned soot corresponding to the stabilization of the pressure drop at the lowest level observed under these conditions with a DPF containing no soot.
- the pressure drop stabilizes before the end of the regeneration test, which makes it possible to calculate this criterion.
- the pressure drop remains high and unstable, which does not allow this criterion to be calculated.
- compositions 3B and 3E When the compositions 3B and 3E are compared, it is found that these two compositions lead to similar kinetics of combustion if we observe the evolution of the pressure drop at different times through the calculation of burnt soot (5, 10, 15, 20 or 35 minutes) of the regeneration at 450 ° C. However, this efficiency is obtained with a smaller amount of additive (in this case 5 ppm of iron metal) for the additive prepared from the dispersion containing crystallites of magnetite and / or maghemite type of smaller size (here 4 nm). for composition 3E). When the crystallite size is 9 nm (composition 3B), the amount to be introduced corresponds to a metal iron content of 7 ppm by weight.
- the set of examples illustrates that the compositions containing crystallites of the magnetite and / or small maghemite type (typically 4 nm) can be very effective at low dosage while not significantly degrading the fuel.
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- Dispersion Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Detergent Compositions (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
Claims
Priority Applications (12)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201180062508.9A CN103429717B (zh) | 2010-12-22 | 2011-12-20 | 基于铁颗粒分散体和清净剂的燃料添加剂组合物 |
MX2013006996A MX356137B (es) | 2010-12-22 | 2011-12-20 | Composicion de aditivo combustible a base de dispersion de particulas de fierro y detergente. |
EP18158906.0A EP3348626B1 (fr) | 2010-12-22 | 2011-12-20 | Utilisation d'une composition d'additif carburant à base d'une dispersion de particules de fer et d'un détergent |
CA2821983A CA2821983C (fr) | 2010-12-22 | 2011-12-20 | Composition d'additif carburant a base d'une dispersion de particules de fer et d'un detergent |
US13/996,587 US9914892B2 (en) | 2010-12-22 | 2011-12-20 | Fuel additive composition containing a dispersion of iron particles and a detergent |
EP11802920.6A EP2655575B1 (fr) | 2010-12-22 | 2011-12-20 | Composition d'additif carburant à base d'une dispersion de particules de fer et d'un détergent |
KR1020137019427A KR101922895B1 (ko) | 2010-12-22 | 2011-12-20 | 철 입자 분산제 및 세제에 기반을 둔 연료 첨가제 조성물 |
AU2011347510A AU2011347510B2 (en) | 2010-12-22 | 2011-12-20 | Fuel additive composition containing a dispersion of iron particles and a detergent |
JP2013545294A JP5959531B2 (ja) | 2010-12-22 | 2011-12-20 | 鉄粒子の分散体及び洗浄剤をベースとする燃料添加剤組成物 |
ES11802920.6T ES2675122T3 (es) | 2010-12-22 | 2011-12-20 | Composición de aditivo de combustible a base de una dispersión de partículas de hierro y de un detergente |
SG2013048590A SG191321A1 (en) | 2010-12-22 | 2011-12-20 | Fuel additive composition containing a dispersion of iron particles and a detergent |
BR112013016068-3A BR112013016068B1 (pt) | 2010-12-22 | 2011-12-20 | Composição, uso de uma composição, carburante aditivado e método de implementação de um motor de combustão interna |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1061065A FR2969654B1 (fr) | 2010-12-22 | 2010-12-22 | Composition d'additif carburant a base d'une dispersion de particules de fer et d'un detergent |
FR1061065 | 2010-12-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2012084906A1 true WO2012084906A1 (fr) | 2012-06-28 |
Family
ID=44034247
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2011/073348 WO2012084906A1 (fr) | 2010-12-22 | 2011-12-20 | Composition d'additif carburant à base d'une dispersion de particules de fer et d'un détergent |
Country Status (13)
Country | Link |
---|---|
US (1) | US9914892B2 (fr) |
EP (2) | EP2655575B1 (fr) |
JP (1) | JP5959531B2 (fr) |
KR (1) | KR101922895B1 (fr) |
CN (1) | CN103429717B (fr) |
AU (1) | AU2011347510B2 (fr) |
BR (1) | BR112013016068B1 (fr) |
CA (1) | CA2821983C (fr) |
ES (2) | ES2748524T3 (fr) |
FR (1) | FR2969654B1 (fr) |
MX (1) | MX356137B (fr) |
SG (1) | SG191321A1 (fr) |
WO (1) | WO2012084906A1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2015086995A1 (fr) | 2013-12-12 | 2015-06-18 | Filtrauto | Filtre à carburant et cartouche pour un tel filtre avec réservoir d'additif embarqué. |
WO2015086996A1 (fr) | 2013-12-12 | 2015-06-18 | Filtrauto | Filtre à carburant avec dispositif de libération d'additif |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2969655B1 (fr) * | 2010-12-22 | 2014-01-10 | Rhodia Operations | Composition d'additif carburant a base d'une dispersion de particules de fer et d'un detergent de type sel d'ammonium quaternaire de polyester |
CN104640960B (zh) * | 2012-07-26 | 2019-02-12 | 高效燃料解决方案有限责任公司 | 分子尺寸燃料添加剂主体 |
MX2015016343A (es) * | 2013-05-28 | 2016-03-01 | Lubrizol Corp | Inhibicion de asfaltenos. |
WO2014203459A1 (fr) * | 2013-06-18 | 2014-12-24 | パナソニック インテレクチュアル プロパティ コーポレーション オブ アメリカ | Dispositif d'entrée et procédé d'entrée de requête d'opération |
WO2017190239A1 (fr) * | 2016-05-05 | 2017-11-09 | Nfluids Inc. | Transfert de phase destiné à la préparation d'organosols nanométriques stables |
Citations (72)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3087436A (en) | 1960-12-02 | 1963-04-30 | Ross Gear And Tool Company Inc | Hydraulic pump |
US3172892A (en) | 1959-03-30 | 1965-03-09 | Reaction product of high molecular weight succinic acids and succinic anhydrides with an ethylene poly- amine | |
US3215707A (en) | 1960-06-07 | 1965-11-02 | Lubrizol Corp | Lubricant |
US3231587A (en) | 1960-06-07 | 1966-01-25 | Lubrizol Corp | Process for the preparation of substituted succinic acid compounds |
US3272746A (en) | 1965-11-22 | 1966-09-13 | Lubrizol Corp | Lubricating composition containing an acylated nitrogen compound |
US3275554A (en) | 1963-08-02 | 1966-09-27 | Shell Oil Co | Polyolefin substituted polyamines and lubricants containing them |
US3361673A (en) | 1959-08-24 | 1968-01-02 | Chevron Res | Lubricating oil compositions containing alkenyl succinimides of tetraethylene pentamine |
US3401118A (en) | 1967-09-15 | 1968-09-10 | Chevron Res | Preparation of mixed alkenyl succinimides |
US3438757A (en) | 1965-08-23 | 1969-04-15 | Chevron Res | Hydrocarbyl amines for fuel detergents |
US3454555A (en) | 1965-01-28 | 1969-07-08 | Shell Oil Co | Oil-soluble halogen-containing polyamines and polyethyleneimines |
US3598738A (en) | 1966-09-23 | 1971-08-10 | Du Pont | Oil compositions containing ethylene copolymers |
US3755433A (en) | 1971-12-16 | 1973-08-28 | Texaco Inc | Ashless lubricating oil dispersant |
US3778371A (en) | 1972-05-19 | 1973-12-11 | Ethyl Corp | Lubricant and fuel compositions |
US3822289A (en) | 1972-04-17 | 1974-07-02 | Synthetic Chemicals Ltd | Synthesis of thiophens |
US3912764A (en) | 1972-09-29 | 1975-10-14 | Cooper Edwin Inc | Preparation of alkenyl succinic anhydrides |
US3954808A (en) | 1972-11-02 | 1976-05-04 | Edwin Cooper & Company Limited | Methylene bis-phenol alkanoic acid compounds |
US4026809A (en) | 1974-12-19 | 1977-05-31 | Texaco Inc. | Lubricating compositions containing methacrylate ester graft copolymers as useful viscosity index improvers |
US4032700A (en) | 1973-06-25 | 1977-06-28 | Exxon Research And Engineering Company | Process for the preparation of aminated polymers useful as additives for fuels and lubricants |
US4110349A (en) | 1976-06-11 | 1978-08-29 | The Lubrizol Corporation | Two-step method for the alkenylation of maleic anhydride and related compounds |
US4137185A (en) | 1977-07-28 | 1979-01-30 | Exxon Research & Engineering Co. | Stabilized imide graft of ethylene copolymeric additives for lubricants |
US4156061A (en) | 1974-03-06 | 1979-05-22 | Exxon Research & Engineering Co. | Epoxidized terpolymer or derivatives thereof, and oil and fuel compositions containing same |
US4171959A (en) | 1977-12-14 | 1979-10-23 | Texaco Inc. | Fuel composition containing quaternary ammonium salts of succinimides |
US4234435A (en) | 1979-02-23 | 1980-11-18 | The Lubrizol Corporation | Novel carboxylic acid acylating agents, derivatives thereof, concentrate and lubricant compositions containing the same, and processes for their preparation |
US4253980A (en) | 1979-06-28 | 1981-03-03 | Texaco Inc. | Quaternary ammonium salt of ester-lactone and hydrocarbon oil containing same |
US4320019A (en) | 1978-04-17 | 1982-03-16 | The Lubrizol Corporation | Multi-purpose additive compositions and concentrates containing same |
US4326973A (en) | 1981-01-13 | 1982-04-27 | Texaco Inc. | Quaternary ammonium succinimide salt composition and lubricating oil containing same |
US4338206A (en) | 1981-03-23 | 1982-07-06 | Texaco Inc. | Quaternary ammonium succinimide salt composition and lubricating oil containing same |
US4357250A (en) | 1978-04-17 | 1982-11-02 | The Lubrizol Corporation | Nitrogen-containing terpolymer-based compositions useful as multi-purpose lubricant additives |
US4658078A (en) | 1986-08-15 | 1987-04-14 | Shell Oil Company | Vinylidene olefin process |
US4668834A (en) | 1985-10-16 | 1987-05-26 | Uniroyal Chemical Company, Inc. | Low molecular weight ethylene-alphaolefin copolymer intermediates |
US4832702A (en) | 1986-04-04 | 1989-05-23 | Basf Aktiengesellschaft | Polybutyl-and polyisobutylamines, their preparation, and fuel compositions containing these |
US4937299A (en) | 1983-06-06 | 1990-06-26 | Exxon Research & Engineering Company | Process and catalyst for producing reactor blend polyolefins |
US5071919A (en) | 1990-05-17 | 1991-12-10 | Ethyl Petroleum Additives, Inc. | Substituted acylating agents and their production |
US5137978A (en) | 1990-05-17 | 1992-08-11 | Ethyl Petroleum Additives, Inc. | Substituted acylating agents and their production |
US5137980A (en) | 1990-05-17 | 1992-08-11 | Ethyl Petroleum Additives, Inc. | Ashless dispersants formed from substituted acylating agents and their production and use |
US5254138A (en) | 1991-05-03 | 1993-10-19 | Uop | Fuel composition containing a quaternary ammonium salt |
US5286823A (en) | 1991-06-22 | 1994-02-15 | Basf Aktiengesellschaft | Preparation of highly reactive polyisobutenes |
US5324800A (en) | 1983-06-06 | 1994-06-28 | Exxon Chemical Patents Inc. | Process and catalyst for polyolefin density and molecular weight control |
US5336278A (en) | 1993-05-13 | 1994-08-09 | The Lubrizol Corporation | Fuel composition containing an aromatic amide detergent |
US5350429A (en) | 1992-03-19 | 1994-09-27 | Basf Aktiengesellschaft | Diaminoalkanes, their preparation and fuels and lubricants containing the diaminoalkanes |
US5458793A (en) | 1993-05-13 | 1995-10-17 | The Lubrizol Corporation | Compositions useful as additives for lubricants and liquid fuels |
US5492641A (en) | 1992-05-04 | 1996-02-20 | Basf Aktiengesellschaft | β-aminonitriles and N-alkyl-1,3-propylenediamines and their use as fuel additives and lubricant additives |
US5496383A (en) | 1993-03-23 | 1996-03-05 | Basf Aktiengesellschaft | Fuel additives, their preparation and gasoline engine fuels containing the additives |
US5620949A (en) | 1995-12-13 | 1997-04-15 | The Lubrizol Corporation | Condensation products of alkylphenols and aldehydes, and derivatives thereof |
WO1997019022A1 (fr) * | 1995-11-22 | 1997-05-29 | Rhodia Chimie | Sol organique comportant au moins un compose oxygene de terre(s) rare(s), procede de synthese dudit sol et utilisation dudit sol pour la catalyse |
US5697988A (en) | 1991-11-18 | 1997-12-16 | Ethyl Corporation | Fuel compositions |
US5739356A (en) | 1995-08-22 | 1998-04-14 | The Lubrizol Corporation | Lactones useful as intermediates for preparing lubricating oil and fuel additives |
US5777142A (en) | 1995-08-22 | 1998-07-07 | The Lubrizol Corporation | Unsaturated hydroxycarboxylic compounds useful as intermediates for preparing lubricant and fuel additives |
US5827805A (en) | 1996-02-29 | 1998-10-27 | The Lubrizol Corporation | Condensates of alkyl phenols and glyoxal and products derived therefrom |
US5840920A (en) | 1996-08-08 | 1998-11-24 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives |
US5851966A (en) | 1997-06-05 | 1998-12-22 | The Lubrizol Corporation | Reaction products of substituted carboxylic acylating agents and carboxylic reactants for use in fuels and lubricants |
US5876468A (en) | 1996-09-05 | 1999-03-02 | Lubrizol Adibis Holdings (Uk) Limited | Detergents for hydrocarbon fuels |
US5885944A (en) | 1996-05-21 | 1999-03-23 | The Lubrizol Corporation | Low chlorine polyalkylene substituted carboxylic acylating agent compositions and compounds derived therefrom |
US5912213A (en) | 1997-06-05 | 1999-06-15 | The Lubrizol Corporation | Substituted carboxylic acylating agent compositions and derivatives thereof for use in lubricants and fuels |
US6001781A (en) | 1997-09-10 | 1999-12-14 | The Lubrizol Corporation | Process for preparing condensation product of hydroxy-substituted aromatic compounds and glyoxylic reactants |
US6020500A (en) | 1995-08-22 | 2000-02-01 | The Lubrizol Corporation | Hydroxy-substituted monolactones useful as intermediates for preparing lubricating oil and fuel additives |
US6077909A (en) | 1997-02-13 | 2000-06-20 | The Lubrizol Corporation | Low chlorine content compositions for use in lubricants and fuels |
US6147036A (en) | 1996-08-08 | 2000-11-14 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives and derivatives thereof |
US6165235A (en) | 1997-08-26 | 2000-12-26 | The Lubrizol Corporation | Low chlorine content compositions for use in lubricants and fuels |
FR2797199A1 (fr) * | 1999-08-04 | 2001-02-09 | Rhodia Terres Rares | Dispersion colloidale organique de particules essentiellement monocristallines d'au moins un compose a base d'au moins une terre rare, son procede de preparation et son utilisation |
US6562913B1 (en) | 1999-09-16 | 2003-05-13 | Texas Petrochemicals Lp | Process for producing high vinylidene polyisobutylene |
FR2833862A1 (fr) * | 2001-12-21 | 2003-06-27 | Rhodia Elect & Catalysis | Dispersion colloidale organique de particules de fer, son procede de preparation et son utilisation comme adjuvant de carburant pour moteurs a combustion interne |
US20040176552A1 (en) | 2001-03-28 | 2004-09-09 | Texas Petrochemicals Lp | Process for producing mid-range vinylidene content polyisobutylene polymer products |
FR2860443A1 (fr) * | 2003-10-03 | 2005-04-08 | Rhodia Elect & Catalysis | Dispersion colloidale organique de cerium et d'un element choisi parmi le rhodium et le palladium et son utilisation comme adjuvant de gazoles pour moteurs a combustion interne |
WO2006063161A2 (fr) | 2004-12-09 | 2006-06-15 | The Lubrizol Corporation | Procede de preparation d'un additif et utilisation de celui-ci |
WO2006135881A2 (fr) * | 2005-06-16 | 2006-12-21 | The Lubrizol Corporation | Detergents a base de sel d'ammonium quaternaire utilisables dans des combustibles |
US20070180760A1 (en) * | 2006-02-09 | 2007-08-09 | Headwaters Nanokinetix, Inc. | Crystalline nanocatalysts for improving combustion properties of fuels and fuel compositions incorporating such catalysts |
WO2008116550A1 (fr) * | 2007-03-28 | 2008-10-02 | Infineum International Limited | Procédé d'apport de fer au piège à particules de l'échappement d'un moteur diesel |
WO2008116552A1 (fr) * | 2007-03-28 | 2008-10-02 | Infineum International Limited | Procédé de fabrication d'un colloïde d'oxyde de fer |
WO2009140190A1 (fr) * | 2008-05-15 | 2009-11-19 | The Lubrizol Corporation | Sels quaternaires destinés à être utilisés comme agents tensio-actifs dans des dispersions |
US20100242342A1 (en) * | 2006-09-05 | 2010-09-30 | Cerion Technology, Inc. | Cerium-containing nanoparticles |
WO2010150040A1 (fr) * | 2009-06-23 | 2010-12-29 | Rhodia Operations | Combinaison synergique détergent et composé à métal actif |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007014916A1 (de) | 2007-03-26 | 2008-10-02 | Evonik Degussa Gmbh | Verfahren und Vorrichtung zum Hochdruckdispergieren |
-
2010
- 2010-12-22 FR FR1061065A patent/FR2969654B1/fr not_active Expired - Fee Related
-
2011
- 2011-12-20 US US13/996,587 patent/US9914892B2/en active Active
- 2011-12-20 ES ES18158906T patent/ES2748524T3/es active Active
- 2011-12-20 AU AU2011347510A patent/AU2011347510B2/en not_active Ceased
- 2011-12-20 SG SG2013048590A patent/SG191321A1/en unknown
- 2011-12-20 ES ES11802920.6T patent/ES2675122T3/es active Active
- 2011-12-20 KR KR1020137019427A patent/KR101922895B1/ko active IP Right Grant
- 2011-12-20 CN CN201180062508.9A patent/CN103429717B/zh not_active Expired - Fee Related
- 2011-12-20 WO PCT/EP2011/073348 patent/WO2012084906A1/fr active Application Filing
- 2011-12-20 JP JP2013545294A patent/JP5959531B2/ja not_active Expired - Fee Related
- 2011-12-20 EP EP11802920.6A patent/EP2655575B1/fr not_active Not-in-force
- 2011-12-20 CA CA2821983A patent/CA2821983C/fr not_active Expired - Fee Related
- 2011-12-20 MX MX2013006996A patent/MX356137B/es active IP Right Grant
- 2011-12-20 BR BR112013016068-3A patent/BR112013016068B1/pt not_active IP Right Cessation
- 2011-12-20 EP EP18158906.0A patent/EP3348626B1/fr not_active Not-in-force
Patent Citations (86)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3172892A (en) | 1959-03-30 | 1965-03-09 | Reaction product of high molecular weight succinic acids and succinic anhydrides with an ethylene poly- amine | |
US3219666A (en) | 1959-03-30 | 1965-11-23 | Derivatives of succinic acids and nitrogen compounds | |
US3361673A (en) | 1959-08-24 | 1968-01-02 | Chevron Res | Lubricating oil compositions containing alkenyl succinimides of tetraethylene pentamine |
US3215707A (en) | 1960-06-07 | 1965-11-02 | Lubrizol Corp | Lubricant |
US3231587A (en) | 1960-06-07 | 1966-01-25 | Lubrizol Corp | Process for the preparation of substituted succinic acid compounds |
US3087436A (en) | 1960-12-02 | 1963-04-30 | Ross Gear And Tool Company Inc | Hydraulic pump |
US3275554A (en) | 1963-08-02 | 1966-09-27 | Shell Oil Co | Polyolefin substituted polyamines and lubricants containing them |
US3454555A (en) | 1965-01-28 | 1969-07-08 | Shell Oil Co | Oil-soluble halogen-containing polyamines and polyethyleneimines |
US3565804A (en) | 1965-08-23 | 1971-02-23 | Chevron Res | Lubricating oil additives |
US3438757A (en) | 1965-08-23 | 1969-04-15 | Chevron Res | Hydrocarbyl amines for fuel detergents |
US3272746A (en) | 1965-11-22 | 1966-09-13 | Lubrizol Corp | Lubricating composition containing an acylated nitrogen compound |
US3598738A (en) | 1966-09-23 | 1971-08-10 | Du Pont | Oil compositions containing ethylene copolymers |
US3401118A (en) | 1967-09-15 | 1968-09-10 | Chevron Res | Preparation of mixed alkenyl succinimides |
US3755433A (en) | 1971-12-16 | 1973-08-28 | Texaco Inc | Ashless lubricating oil dispersant |
US3822289A (en) | 1972-04-17 | 1974-07-02 | Synthetic Chemicals Ltd | Synthesis of thiophens |
US3778371A (en) | 1972-05-19 | 1973-12-11 | Ethyl Corp | Lubricant and fuel compositions |
US3912764A (en) | 1972-09-29 | 1975-10-14 | Cooper Edwin Inc | Preparation of alkenyl succinic anhydrides |
US3954808A (en) | 1972-11-02 | 1976-05-04 | Edwin Cooper & Company Limited | Methylene bis-phenol alkanoic acid compounds |
US4032700A (en) | 1973-06-25 | 1977-06-28 | Exxon Research And Engineering Company | Process for the preparation of aminated polymers useful as additives for fuels and lubricants |
US4156061A (en) | 1974-03-06 | 1979-05-22 | Exxon Research & Engineering Co. | Epoxidized terpolymer or derivatives thereof, and oil and fuel compositions containing same |
US4026809A (en) | 1974-12-19 | 1977-05-31 | Texaco Inc. | Lubricating compositions containing methacrylate ester graft copolymers as useful viscosity index improvers |
US4110349A (en) | 1976-06-11 | 1978-08-29 | The Lubrizol Corporation | Two-step method for the alkenylation of maleic anhydride and related compounds |
US4137185A (en) | 1977-07-28 | 1979-01-30 | Exxon Research & Engineering Co. | Stabilized imide graft of ethylene copolymeric additives for lubricants |
US4171959A (en) | 1977-12-14 | 1979-10-23 | Texaco Inc. | Fuel composition containing quaternary ammonium salts of succinimides |
US4320019A (en) | 1978-04-17 | 1982-03-16 | The Lubrizol Corporation | Multi-purpose additive compositions and concentrates containing same |
US4357250A (en) | 1978-04-17 | 1982-11-02 | The Lubrizol Corporation | Nitrogen-containing terpolymer-based compositions useful as multi-purpose lubricant additives |
US4234435A (en) | 1979-02-23 | 1980-11-18 | The Lubrizol Corporation | Novel carboxylic acid acylating agents, derivatives thereof, concentrate and lubricant compositions containing the same, and processes for their preparation |
US4253980A (en) | 1979-06-28 | 1981-03-03 | Texaco Inc. | Quaternary ammonium salt of ester-lactone and hydrocarbon oil containing same |
US4326973A (en) | 1981-01-13 | 1982-04-27 | Texaco Inc. | Quaternary ammonium succinimide salt composition and lubricating oil containing same |
US4338206A (en) | 1981-03-23 | 1982-07-06 | Texaco Inc. | Quaternary ammonium succinimide salt composition and lubricating oil containing same |
US5324800A (en) | 1983-06-06 | 1994-06-28 | Exxon Chemical Patents Inc. | Process and catalyst for polyolefin density and molecular weight control |
US4937299A (en) | 1983-06-06 | 1990-06-26 | Exxon Research & Engineering Company | Process and catalyst for producing reactor blend polyolefins |
US4668834B1 (en) | 1985-10-16 | 1996-05-07 | Uniroyal Chem Co Inc | Low molecular weight ethylene-alphaolefin copolymer intermediates |
US4668834A (en) | 1985-10-16 | 1987-05-26 | Uniroyal Chemical Company, Inc. | Low molecular weight ethylene-alphaolefin copolymer intermediates |
US4832702A (en) | 1986-04-04 | 1989-05-23 | Basf Aktiengesellschaft | Polybutyl-and polyisobutylamines, their preparation, and fuel compositions containing these |
US4658078A (en) | 1986-08-15 | 1987-04-14 | Shell Oil Company | Vinylidene olefin process |
US5137978A (en) | 1990-05-17 | 1992-08-11 | Ethyl Petroleum Additives, Inc. | Substituted acylating agents and their production |
US5137980A (en) | 1990-05-17 | 1992-08-11 | Ethyl Petroleum Additives, Inc. | Ashless dispersants formed from substituted acylating agents and their production and use |
US5071919A (en) | 1990-05-17 | 1991-12-10 | Ethyl Petroleum Additives, Inc. | Substituted acylating agents and their production |
US5254138A (en) | 1991-05-03 | 1993-10-19 | Uop | Fuel composition containing a quaternary ammonium salt |
US5286823A (en) | 1991-06-22 | 1994-02-15 | Basf Aktiengesellschaft | Preparation of highly reactive polyisobutenes |
US5408018A (en) | 1991-06-22 | 1995-04-18 | Basf Aktiengesellschaft | Preparation of highly reactive polyisobutenes |
US5697988A (en) | 1991-11-18 | 1997-12-16 | Ethyl Corporation | Fuel compositions |
US5350429A (en) | 1992-03-19 | 1994-09-27 | Basf Aktiengesellschaft | Diaminoalkanes, their preparation and fuels and lubricants containing the diaminoalkanes |
US5492641A (en) | 1992-05-04 | 1996-02-20 | Basf Aktiengesellschaft | β-aminonitriles and N-alkyl-1,3-propylenediamines and their use as fuel additives and lubricant additives |
US5567845A (en) | 1993-03-23 | 1996-10-22 | Basf Aktiengesellschaft | Fuel additives, their preparation and gasoline engine fuels containing the additives |
US5496383A (en) | 1993-03-23 | 1996-03-05 | Basf Aktiengesellschaft | Fuel additives, their preparation and gasoline engine fuels containing the additives |
US5336278A (en) | 1993-05-13 | 1994-08-09 | The Lubrizol Corporation | Fuel composition containing an aromatic amide detergent |
US5458793A (en) | 1993-05-13 | 1995-10-17 | The Lubrizol Corporation | Compositions useful as additives for lubricants and liquid fuels |
US5856524A (en) | 1995-08-22 | 1999-01-05 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives |
US5739356A (en) | 1995-08-22 | 1998-04-14 | The Lubrizol Corporation | Lactones useful as intermediates for preparing lubricating oil and fuel additives |
US5777142A (en) | 1995-08-22 | 1998-07-07 | The Lubrizol Corporation | Unsaturated hydroxycarboxylic compounds useful as intermediates for preparing lubricant and fuel additives |
US5786490A (en) | 1995-08-22 | 1998-07-28 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives |
US6114547A (en) | 1995-08-22 | 2000-09-05 | The Lubrizol Corporation | Hydroxy-substituted monolactones and use thereof as intermediates for preparing lubricating oil and fuel additives |
US6020500A (en) | 1995-08-22 | 2000-02-01 | The Lubrizol Corporation | Hydroxy-substituted monolactones useful as intermediates for preparing lubricating oil and fuel additives |
WO1997019022A1 (fr) * | 1995-11-22 | 1997-05-29 | Rhodia Chimie | Sol organique comportant au moins un compose oxygene de terre(s) rare(s), procede de synthese dudit sol et utilisation dudit sol pour la catalyse |
US5620949A (en) | 1995-12-13 | 1997-04-15 | The Lubrizol Corporation | Condensation products of alkylphenols and aldehydes, and derivatives thereof |
US5827805A (en) | 1996-02-29 | 1998-10-27 | The Lubrizol Corporation | Condensates of alkyl phenols and glyoxal and products derived therefrom |
US5885944A (en) | 1996-05-21 | 1999-03-23 | The Lubrizol Corporation | Low chlorine polyalkylene substituted carboxylic acylating agent compositions and compounds derived therefrom |
US5840920A (en) | 1996-08-08 | 1998-11-24 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives |
US6147036A (en) | 1996-08-08 | 2000-11-14 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives and derivatives thereof |
US6207839B1 (en) | 1996-08-08 | 2001-03-27 | The Lubrizol Corporation | Process for preparing compositions useful as intermediates for preparing lubricating oil and fuel additives |
US5876468A (en) | 1996-09-05 | 1999-03-02 | Lubrizol Adibis Holdings (Uk) Limited | Detergents for hydrocarbon fuels |
US6077909A (en) | 1997-02-13 | 2000-06-20 | The Lubrizol Corporation | Low chlorine content compositions for use in lubricants and fuels |
US5912213A (en) | 1997-06-05 | 1999-06-15 | The Lubrizol Corporation | Substituted carboxylic acylating agent compositions and derivatives thereof for use in lubricants and fuels |
US5851966A (en) | 1997-06-05 | 1998-12-22 | The Lubrizol Corporation | Reaction products of substituted carboxylic acylating agents and carboxylic reactants for use in fuels and lubricants |
US6165235A (en) | 1997-08-26 | 2000-12-26 | The Lubrizol Corporation | Low chlorine content compositions for use in lubricants and fuels |
US6001781A (en) | 1997-09-10 | 1999-12-14 | The Lubrizol Corporation | Process for preparing condensation product of hydroxy-substituted aromatic compounds and glyoxylic reactants |
FR2797199A1 (fr) * | 1999-08-04 | 2001-02-09 | Rhodia Terres Rares | Dispersion colloidale organique de particules essentiellement monocristallines d'au moins un compose a base d'au moins une terre rare, son procede de preparation et son utilisation |
US6683138B2 (en) | 1999-09-16 | 2004-01-27 | Texas Petrochemicals Lp | Process for producing high vinylidene polyisobutylene |
US6562913B1 (en) | 1999-09-16 | 2003-05-13 | Texas Petrochemicals Lp | Process for producing high vinylidene polyisobutylene |
US20050137363A1 (en) | 1999-10-19 | 2005-06-23 | Texas Peterochemicals Lp | Process for producing mid-range vinylidene content polyisobutylene polymer products |
US20060079652A1 (en) | 1999-10-19 | 2006-04-13 | Baxter C E Jr | Mid-range vinylidene content polyisobutylene polymer product produced by liquid phase polymerization process |
US20040176552A1 (en) | 2001-03-28 | 2004-09-09 | Texas Petrochemicals Lp | Process for producing mid-range vinylidene content polyisobutylene polymer products |
US7037999B2 (en) | 2001-03-28 | 2006-05-02 | Texas Petrochemicals Lp | Mid-range vinylidene content polyisobutylene polymer product and process for producing the same |
FR2833862A1 (fr) * | 2001-12-21 | 2003-06-27 | Rhodia Elect & Catalysis | Dispersion colloidale organique de particules de fer, son procede de preparation et son utilisation comme adjuvant de carburant pour moteurs a combustion interne |
WO2003053560A1 (fr) | 2001-12-21 | 2003-07-03 | Rhodia Electronics And Catalysis | Dispersion colloidale organique de particules de fer, son procede de preparation et son utilisation comme adjuvant de carburant pour moteurs a combustion interne |
FR2860443A1 (fr) * | 2003-10-03 | 2005-04-08 | Rhodia Elect & Catalysis | Dispersion colloidale organique de cerium et d'un element choisi parmi le rhodium et le palladium et son utilisation comme adjuvant de gazoles pour moteurs a combustion interne |
WO2006063161A2 (fr) | 2004-12-09 | 2006-06-15 | The Lubrizol Corporation | Procede de preparation d'un additif et utilisation de celui-ci |
WO2006135881A2 (fr) * | 2005-06-16 | 2006-12-21 | The Lubrizol Corporation | Detergents a base de sel d'ammonium quaternaire utilisables dans des combustibles |
US20070180760A1 (en) * | 2006-02-09 | 2007-08-09 | Headwaters Nanokinetix, Inc. | Crystalline nanocatalysts for improving combustion properties of fuels and fuel compositions incorporating such catalysts |
US20100242342A1 (en) * | 2006-09-05 | 2010-09-30 | Cerion Technology, Inc. | Cerium-containing nanoparticles |
WO2008116550A1 (fr) * | 2007-03-28 | 2008-10-02 | Infineum International Limited | Procédé d'apport de fer au piège à particules de l'échappement d'un moteur diesel |
WO2008116552A1 (fr) * | 2007-03-28 | 2008-10-02 | Infineum International Limited | Procédé de fabrication d'un colloïde d'oxyde de fer |
WO2009140190A1 (fr) * | 2008-05-15 | 2009-11-19 | The Lubrizol Corporation | Sels quaternaires destinés à être utilisés comme agents tensio-actifs dans des dispersions |
WO2010150040A1 (fr) * | 2009-06-23 | 2010-12-29 | Rhodia Operations | Combinaison synergique détergent et composé à métal actif |
Non-Patent Citations (1)
Title |
---|
KIRK; OTHMER: "Encyclopedia of Chemical Technology", vol. 5, 1950, INTERSCIENCE PUBLISHERS, pages: 898 - 905 |
Cited By (2)
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---|---|---|---|---|
WO2015086995A1 (fr) | 2013-12-12 | 2015-06-18 | Filtrauto | Filtre à carburant et cartouche pour un tel filtre avec réservoir d'additif embarqué. |
WO2015086996A1 (fr) | 2013-12-12 | 2015-06-18 | Filtrauto | Filtre à carburant avec dispositif de libération d'additif |
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US9914892B2 (en) | 2018-03-13 |
ES2748524T3 (es) | 2020-03-17 |
EP3348626A1 (fr) | 2018-07-18 |
JP5959531B2 (ja) | 2016-08-02 |
AU2011347510A8 (en) | 2013-09-05 |
BR112013016068B1 (pt) | 2019-07-02 |
CA2821983C (fr) | 2019-01-15 |
CA2821983A1 (fr) | 2012-06-28 |
KR101922895B1 (ko) | 2018-11-28 |
EP2655575A1 (fr) | 2013-10-30 |
ES2675122T3 (es) | 2018-07-06 |
US20140007494A1 (en) | 2014-01-09 |
EP3348626B1 (fr) | 2019-07-10 |
MX356137B (es) | 2018-05-16 |
JP2014507498A (ja) | 2014-03-27 |
SG191321A1 (en) | 2013-07-31 |
BR112013016068A2 (pt) | 2016-09-20 |
CN103429717B (zh) | 2015-08-12 |
FR2969654B1 (fr) | 2013-02-08 |
EP2655575B1 (fr) | 2018-03-28 |
CN103429717A (zh) | 2013-12-04 |
FR2969654A1 (fr) | 2012-06-29 |
AU2011347510B2 (en) | 2016-11-17 |
MX2013006996A (es) | 2013-11-04 |
KR20140051111A (ko) | 2014-04-30 |
AU2011347510A1 (en) | 2013-08-01 |
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