Lubricating Composition for Hydrocarbonated Mixtures and Products Obtained

Information

  • Patent Application
  • 20080184617
  • Publication Number
    20080184617
  • Date Filed
    July 04, 2006
    18 years ago
  • Date Published
    August 07, 2008
    16 years ago
Abstract
A subject of the present invention is an anti-corrosive and antistatic lubricating composition for a hydrocarbonated mixture comprising: a) at least a compound A of Formula (I) below:
Description

The present invention relates to a composition for hydrocarbonated mixtures, in particular with a low sulphur content, intended to improve their lubricity, but also concomitantly limit their corrosive character vis a vis metal parts with which they are brought into contact and increase their antistatic character by raising their conductivity. A composition of this type is applicable to any hydrocarbonated mixture, entirely or partially synthetic, capable of providing the energy required for moving land vehicles or aircraft, more particularly diesel fuel, kerosene or gasoline for internal combustion engines, these hydrocarbons having a low sulphur content of less than 500 ppm, below 50 ppm and even below 10 ppm.


Whatever the hydrocarbonated mixture usable as an energy source for moving these vehicles, it is well known that it must have lubrication capabilities for protecting the pumps, injection systems and all the moving parts with which these mixtures can come into contact. As regulations in many countries have imposed an upper limit on the acceptable sulphur content of fuels of less than 0.05% by weight, then less than 50 ppm and even less than 10 ppm in order to reduce the emissions of pollutants from cars, lorries or buses, in particular in built-up urban areas, the refinery industry has increasingly been led to improve its treatment processes for the removal of sulphur compounds. Increasingly, fuels have become clean and non-polluting products, free from sulphur and the often associated aromatic and polar compounds. However, all these compounds gave the fuels their lubricity. Other negative effects have arisen concomitantly with the loss of the lubricating character, such as increased problems of static electricity, in particular during all the operations of handling hydrocarbons but also during storage. It has thus become necessary to replace these compounds which confer a lubricating character on hydrocarbons, whether distilled or not, with other compounds which do not pollute the environment but have a sufficient lubricating power to avoid the risks of engine wear, and also to mitigate the harmful effects of static electricity and corrosion which are inherent in gas oils.


The prior art includes many solutions to improve the lubricity and/or the corrosion or the lubricity and/or the antistatic effect of additives, but no document has sought to solve the problems of lubricity as a whole, while still limiting the corrosion and the conductivity of the hydrocarbons used in engines, maintaining and even reducing the levels of additives incorporated for an equal efficiency.


In order to improve the lubricity of a fuel, whether gasoline, kerosene or gas oil, several types of additives have already been proposed. These are primarily anti-wear additives, known in the field of lubricants, of the following types, unsaturated fatty acid esters and dimeric fatty acids, aliphatic amines, fatty-acid and diethanolamine esters and long-chain aliphatic monocarboxylic acids as described in patents U.S. Pat. No. 2,252,889, U.S. Pat. No. 4,185,594, U.S. Pat. No. 4,204,481, U.S. Pat. No. 4,208,190, U.S. Pat. No. 4,428,182. Most of these additives have a sufficient lubricating capability, but at concentrations that are certainly too high, which is very disadvantageous in economic terms. Moreover, the additives containing dimeric acids cannot be used in high concentrations in fuels supplying vehicles in which the fuel can be in contact with the lubricating oil, as these acids react chemically to form deposits which are sometimes insoluble in oil, but are primarily incompatible with the detergent additives customarily used.


U.S. Pat. No. 4,609,376 advocates the use of anti-wear additives obtained from esters of mono- and polycarboxylic acids and polyhydroxyl alcohols in fuels containing alcohols in their composition.


Another route of choice is to introduce vegetable oil esters or the vegetable oils themselves into these fuels to improve their lubricity or their smoothness. These include the esters derived from rapeseed, flax, soya, sunflower oils or the oils themselves (see patents EP 635,558 and EP 605,857). One of the major drawbacks of these esters is their low lubricating capability at a concentration of less than 0.5% by weight in the fuels.


To solve these problems, the Applicant has proposed to introduce into fuels with low sulphur contents, below 500 ppm, compositions obtained by mixing fatty monocarboxylic acids and polyaromatic monocarboxylic acids, preferably of vegetable origin, in the form of acids, esters or amine salts (EP 915944, EP 1310547 and EP 1340801).


Industrial producers currently seek to improve lubricity and conductivity or the lubricity and corrosion properties, by using a selection of mixtures which can be introduced into hydrocarbons at reasonable rates and have an efficiency identical to, if not better than, that of the products previously used on their own but sometimes at much higher concentrations.


Thus, to improve lubricity and limit the risks of accumulation of static electricity during the production, handling and use of hydrocarbons with low sulphur contents, below 500 ppm, application WO 01/88064 claims a fuel composition comprising a liquid fuel containing less than 500 ppm sulphur, 0.001 to 1 ppm of at least one monoamine or an N-substituted polyamine and 10 to 500 ppm of at least one fatty acid containing 8 to 24 carbon atoms or its equivalent ester with an alcohol or polyalcohol of at most of eight carbon atoms.


To improve lubricity, application WO 97/45507 proposes to introduce into the hydrocarbons, compounds of the type derived from esterified alkenyl anhydrides, in proportions varying from 5-5000 ppm. The applicants found that by adding certain of these compounds, the anti-corrosive properties of these fuels were greatly improved.


Notwithstanding these improvements, an aim of the present invention is to simultaneously improve the lubricity and the antistatic and anticorrosive properties of hydrocarbonated mixtures with low sulphur contents, while still limiting their quantity with an equal efficiency. It aims more particularly to improve the characteristics of the fuels, gasoline, gas oil and kerosenes with low sulphur contents, whether in the form of an emulsion in water or not, and even of certain lubricants.


A subject of the present invention is a lubricating, anti-corrosive and antistatic composition for a hydrocarbonated mixture comprising:


a) at least a compound A of Formula (I) below:







in which R1 and R2 are hydrogen or a linear or branched alkyl group of 1-40 carbon atoms, possibly comprising at least one double bond, R1 and R2 together being able to form an aromatic or aliphatic ring of 5-6 carbon atoms, said ring being capable of substitution by one to three linear or branched alkyl group(s) of 1-40 carbon atoms, in which R1 and R2 cannot be hydrogen at the same time,


and in which R3 and R4, identical or different, are chosen from the OH groups, wherein R3 and R4 cannot be the OH group at the same time, or deriving from a linear or branched monol or polyol group containing 1-20 carbon atoms having a functionality of 2 to 5 inclusive;


b) and at least one B compound corresponding to a fatty acid of 16-24 carbon atoms, unsaturated or not, possibly in a mixture with a carboxylic acid comprising at least aromatic and/or olefinic polycycle or ring and/or their ester, amide or corresponding amine salts derivatives, taken alone or in a mixture.


Notwithstanding the inherent effects of the compounds A or B, it was noted that the combination of these compounds unexpectedly improved the lubricity of the hydrocarbonated mixtures which contained them, but also increased their conductivity, while still reducing their corrosivity vis-à-vis the metal parts with which these mixtures were able to be placed in contact. Moreover, it was noted that this composition was compatible with all the hydrocarbonated mixtures which can be used as a fuel and/or a lubricant, required for the propulsion of land vehicles or aircraft.


In order to have an optimum efficiency with regard to lubricity, anti-corrosive effect and antistatic effect in the hydrocarbonated mixtures, the composition of additives according to the invention will preferably comprise from 40 to 70% by weight of at least a compound A and from 60 to 30% by weight of at least a compound B.


This efficiency can be improved if this composition also comprises at least 0.1% by weight of a compound C chosen from the C5-C30 mono- and/or polycarboxylic acid esters. The addition of such esters to the concentrations of the invention makes it possible to improve the viscosity of the mixture of additives which can thus be better dispersed in the hydrocarbonated mixture.


In a preferred version of the invention, the composition comprises from 40 to 70% by weight of at least a compound A, from 60 to 30% of at least a compound B and from 0.1 to 20% of at least a compound C. This composition will be even more effective in terms of antistatic and lubricating efficiency if it comprises from 30 to 60% by weight of at least a compound A, from 60 to 30% of at least a compound B and from 5 to 20% of at least a compound C.


In order to achieve this efficiency, the compounds A, B and C will be described more precisely below by defining the radicals R1 and R2, and R3 and R4.


Thus, the compounds A will be described in relation to the radicals R1 and R2 on the one hand, and R3 and R4 on the other hand. Any compound exhibiting any one of these characteristics will be considered as forming part of the compounds A of the invention.


In the compounds A of formula (I), the radicals R1 and R2 can be identical or different. In a first version, R1 is an alkenyl group of 1-22 carbon atoms, and R2 is hydrogen or vice-versa.


In a second version, R1 and R2 together form a ring with 5 or 6 aromatic or aliphatic carbons, possibly substituted by one to three alkyl group(s) of 1-3 carbons.


For each of these possibilities for the radicals R1 and R2 defined above, the radicals R3 and R4 of compound A of Formula (I) can also vary.


In a first scenario, R3 and R4, identical or different, are OR5 with R5 a group chosen from —[(CH2)n—O]m—H with n varying from 1-4 and m varying from 1-5; —[CH2—CHOH]p—CH2—OH, with p varying from 1-3; —CH2—CR6R7—OH, with R6 and R7 which can each be hydrogen, a methyl radical or a —CH2OH radical.


In a second scenario, R3 is OR5 with R5 a C1-C10 linear or branched alkyl group, possibly substituted by at least one OH group, and R4 is OH or vice-versa.


In a third scenario, R3 and R4 are identical or different OR5 groups, with R4 a C1-C10 linear or branched alkyl group, possibly substituted by at least one OH group.


In a fourth scenario, R3 is OH or an OR5 group with R5 a C1-C10 linear or branched alkyl group, possibly substituted by at least one OH group, and R4 is OR5 with R5 a —[(CH2)n—O]m—H group with n varying from 1-4 and m varying from 1-5; —[CH2—CHOH]p—CH2—OH, with p varying from 1-3; —CH2—CR6R7—OH, with R6 and R7 which can each be hydrogen, a methyl radical or a —CH2OH radical.


Preferably, the OR5 groups are the groups —O—CH2—CH2—OH or —O—CH2—CHOH—CH2—OH or —O—CH2—C(CH3)(CH2OH)—CH2—OH or —O—CH2—C(CH2OH)—(CH2OH)—CH2—OH.


Of course, the scope of the invention would not be exceeded if mixtures of compounds A were used.


In parallel, the compound B required for the invention is preferably chosen as comprising at least one linear saturated or unsaturated carboxylic acid comprising 10-24 atoms and/or their esters, amides or amine salts derivatives. Among these acids, oleic, linoleic, linolenic, palmitic, stearic, isostearic and lauric acids are preferred, as well as their esters, amides and amine salts derivatives, taken alone or in a mixture.


More precisely, the majority of compound B will comprise a mixture of oleic acid and linoleic acid, and/or their esters, amides and amine salts derivatives. Preferably, compound B will comprise a mixture of linear fatty acids of vegetable origin, rape, ricin, sunflower, maize, copra, pine or flax, and/or their esters, amides or amine salts derivatives, these products generally being commercial products.


Compound B will preferentially be constituted by a mixture of linear fatty acids originating from the distillation of the pine oils and/or their esters, amides or amine salts derivatives, regardless of their origins.


In another embodiment of the invention, compound B could comprise resin acids, including abietic acid, dihydroabietic acid, tetrahydroabietic acid, dehydroabietic acid, neoabietic acid, pimaric acid, levopimaric acid and parastinic acid, and/or their esters, amides or amine salts derivatives.


In this latter scenario, compound B is constituted by a mixture of fatty acids and resin acids corresponding to a heavier distillate of the distillation of oil of vegetable origin. The distillates obtained by distillation of pine oil and/or their esters, amides or amine salts derivatives are preferred.


Compound C, when it is added to the composition, is a vegetable oil ester from the group constituted by rapeseed, ricin, sunflower, maize, copra, pine or flax oil, the methyl ester of rapeseed being preferred.


A second subject of the invention is a hydrocarbonated mixture with a low sulphur content below 50 ppm, which can be used as a fuel and/or a lubricant required for the movement of land vehicles or aircraft, this mixture comprising at least 50 ppm of the lubricating composition, having additional antistatic and anti-corrosive properties, containing the compounds A and B, and optionally C. The composition gives particularly good performance for hydrocarbonated mixtures having a sulphur content below 10 ppm.


A hydrocarbonated mixture according to the invention will advantageously comprise between 50 and 350 ppm of said composition. This hydrocarbonated mixture is constituted mostly of hydrocarbons originating from the distillation of crude oil, a gasoline, a gas oil, a kerosene or a lubricant, optionally in a mixture with biofuels and/or synthetic fuels originating from the treatment of the gas, this mixture being able to form a stable emulsion in water. By biofuels is meant all essentially hydrocarbonated products originating from the processing of plants, in particular compounds such as compound C, the concentration of which can vary from 0.5 to 100% by weight in the hydrocarbonated mixture. Among synthetic fuels are included the fuels and lubricants obtained by any method of treatment of the gas, in particular by distillation of the products originating from this treatment.


More particularly, the invention relates to hydrocarbonated mixtures, in particular comprising from 50 to 350 ppm of the composition according to the invention, which are:


a gasoline comprising at least one additive chosen from the group consisting of anti-knock, antifreeze, detergent, de-emulsifying, antioxidant, friction modifying, deposit reduction additives and their mixtures;


a diesel fuel comprising at least one additive chosen from the group consisting of filterability, anti-foam, detergent, de-emulsifying additives, procetane and their mixtures;


a domestic heating oil comprising at least one additive chosen from the group consisting of combustion-promoting additives, low-temperature resistance additives, flow, anti-corrosion, antioxidant, biocide, reodorant additives and their mixtures;


kerosene comprising at least one additive chosen from the group consisting of anti-static, antioxidant additives and their mixtures;


lubricant comprising at least one additive chosen from the group consisting of dispersant, de-emulsifiying, detergent, anti-foam, antioxidant, low temperature resistance for improving in particular the flow point, reodorant additives and their mixtures.


The advantages of this composition in a hydrocarbonated mixture in its different applications are described in the examples below, these results being given only for the purposes of illustrating the invention and not limiting it.







EXAMPLE I

The present example describes the preparation of different compounds A according to the invention.


The reaction consists of a mono- or di-esterification of the anhydride function with a polyol or mono alcohol without a catalyst, according to the reagents used.


Thus, an alkylated diacid compound in an acid or anhydride form can be reacted with an alcohol or polyol in a tetracol reactor equipped with an ascending coolant, a thermometer, a dropping funnel and a nitrogen intake.


By means of a dropping funnel and accompanied by mechanical stirring, the alcohol or the polyol is poured dropwise onto the previously heated acid or the anhydride and kept at 70° C.


At the end of the addition, the sample is brought to the reflux temperature of the alcohol. The reactor is kept at this temperature and under nitrogen sweeping for a period of approximately five hours.


At the end of the reaction, the compound A thus obtained is distilled under vacuum in order to eliminate the water produced and/or the excess alcohol.


Different compounds A were prepared. The products obtained by reaction of polyol are in the form of diesters. The products obtained by reaction of mono alcohol are in the form of hemiesters. The compounds A are listed in Table 1 below.












TABLE I








Anhydride/





alcohol


Product
Anhydride
Alcohol
ratio







A1
ODSA
Ethylene glycol
1:3


A2
ODSA
Ethanol
1:2


A4
ODSA
Butanol
1:2


A6
ODSA
Step 1: ethanol
1:2




Step 2: ethylene glycol
1:2


A7
ODSA
Ethanol/
1:2




Diethylene glycol - 50/50
1:3


A8
OSA
Ethylene glycol
1:3





ODSA = octadecenyl succinic anhydride


OSA = octenyl succinic anhydride






EXAMPLE II

The purpose of the present example is to describe the lubricity performance values of the compounds Ai in a mixture with a compound Bi according to the invention, then in a mixture with a third compound Ci.


All the additive tests were carried out in two types of gas oils GO1 and GO2, the caracteristics of which are given in Table II below.













TABLE II







Characteristics
GO1
GO2




















MV15 (kg/m3)
818.4
835.4



Sulphur content (mg/kg)
8
6



Viscosity 40° C. (mm2/s)
2.13
2.45



Monoaromatics
19.5
25.5



content



Diaromatics
1.7
2.3



content



Polyaromatics content
0
0.1



ASTM D86



Initial boiling point ° C.
168.2
178.2



Point 5% v
190.2
198.7



Point 10% v
196.8
204



Point 20% v
210.7
216.2



Point 30% v
223.6
228.6



Point 40% v
235.8
241.5



Point 50% v
247
255



Point 60% v
257.6
268.2



Point 70% v
269.1
282.1



Point 80% v
282.7
299.4



Point 90% v
303.1
325.9



Point 95% v
320.4
348.9



Final boiling point
335.7
352.5



V.distillate
98.5 mL 
96.8 mL 



Residue
1.4 mL
2.8 mL



Losses
0.1 mL
0.4 mL










Among the compounds Bi of the invention, B1 is a mixture of long-chain fatty acids containing 2% of a mixture of resin acids derived from pine oil, commonly known as tail oil fatty acid.


The lubricity of the Ai/Bi mixtures was tested in two different gas oils, GO1 and GO2 according to standard ISO 12156-1 for each concentration in the gas oil of 100, 150 and 200 ppm.


The results showing the efficiency of the compounds Ai and Bi are given in Table III below.












TABLE III





Compound or mixture
100 ppm
150 ppm
200 ppm















GO1










B1
445 μm
427 μm
407 μm


A1 (75%-wt in Solvarex 10)
609 μm
472 μm
394 μm


B1/A1 - 80/20
496 μm
439 μm
410 μm


B1/A1 - 60/40
504 μm
399 μm
363 μm


B1/A1 - 50/50
458 μm
392 μm
361 μm


B1/A1 - 45/55
407 μm
330 μm
299 μm


B1/A1 - 40/60
515 μm
364 μm
322 μm


B1/A1 - 35/65
416 μm
306 μm
286 μm


B1/A1 - 30/70
384 μm
318 μm
325 μm







GO2










B1
454 μm
428 4 μm  
426 μm


B1/A1 - 50/50
336 μm
 36 μm
249 μm









As A1 is solid at ambient temperature, it is placed in an oven at 60° C. before formulation. For proportions above 50% of A1, it is necessary to place the mixture for a few minutes in the oven at 60° C. in order to homogenize it.


Thus, the maximum level of A1 in B1 is limited by the state of the mixture at ambient temperature. In fact it seems that the maximum acceptable level of A1 for a binary mixture which is liquid at ambient temperature is comprised between 80% (pasty mixture) and 60% (fluid but viscous).


Nevertheless, the results of Table III show a good lubricity efficiency of the mixtures A1/B1.


The best results are obtained with 50/50 A1/B1 mixtures the best compromise between the HFRR efficiency and the homogenization ability of the mixture.


However, in order to improve the viscosity of the mixture A1/B1, a compound C1 was introduced into these compositions.


The lubricity of the mixtures Ai/Bi/Ci was tested in a gas oil GO1 for a concentration in the gas oil of 200 ppm. Among the potential Cis, C1 is a methyl ester of rapeseed or EMC. The results relating to the A1/B1/C1 mixtures are given in Table IV below.














TABLE IV









HFRR
Viscosity


Mixture
A1
B1
C1
(μm)
40° C. (mm2/s)




















M1
40%
60%
0%
363 μm
89.65


M2
40%
60%
0%
355 μm
99.54


M3
40%
40%
20%
330 μm
71.28


M4
70%
30%
0%
291 μm
564.14


M5
50%
30%
20%
352 μm
115.96


M6
40%
50%
10%
282 μm
100


M7
55%
45%
0%
299 μm
373.76


M8
55%
45%
0%
315 μm
222.53


M9
60%
30%
10%
287 μm
251.18


M10
50%
40%
10%
239 μm
142.15


M11
45%
50%
5%
275 μm
175


M12
60%
35%
5%
280 μm
288.34









The best compromises between viscosity (between 70 and 120 mm2/s at 40° C.) and lubricity (<350 μm) are obtained for the mixtures M7 and M11, the viscosity of M8 being insufficient.


EXAMPLE III

The present example aims to illustrate the lubricity efficiency of the other compounds Ai according to the invention, alone or in combination with Bi and C1. Among the other compounds Bi, B2 is an ester resulting from the reaction of B1 with glycerol in a ratio 1:1 and B3 is the product of the reaction of B1 with diethanolamine in a ratio 1:1. The results are given in Table V below.














TABLE V







Compound
100 ppm
150 ppm
200 ppm
















GO1












B1
445 μm
427 μm
407 μm



A2
595 μm
409 μm
438 μm



B1/A2 - 50/50
455 μm
403 μm
327 μm



A4
560 μm
488 μm
374 μm



B1/A4 - 50/50
457 μm
426 μm
327 μm



A6
581 μm
494 μm
313 μm



B1/A6 - 50/50
476 μm
379 μm
340 μm



A7
595 μm
553 μm
330 μm



B1/A7 - 50/50
555 μm
468 μm
345 μm



A8
537 μm
525 μm
333 μm



B1/A8 - 50/50
415 μm
420 μm
287 μm



B1/A8/C1 - 42/43/15
481 μm
348 μm
312 μm



B2


320 μm



B3


382 μm



B2/A2 - 55/45


290 μm



B3/A2 - 55/45


310 μm



B3/A1/C1 - 42/43/15


379 μm



B2/A1/C1 - 42/43/15


380 μm







GO2












B1
454 μm
428 μm
426 μm



A2
488 μm
385 μm
385 μm



B1/A2 - 50/50
459 μm
377 μm
369 μm










As for A1, a synergic effect is noted between the compounds B1 and Ai, the addition of C1 improving the viscosity of the mixture if necessary.


EXAMPLE V

The present example aims to illustrate the significant effect of the mixture Ai/Bi on conductivity and corrosion.


200 ppm of the mixture Ai/Bi is introduced into the gas oil GO1. The conductivity measurements were carried out according to standard ASTM D2624-2, and those for corrosion according to standard ASTM D 655.


The results are given in Tables VI and VII below.












TABLE VI







Tested products
Conductivity




















GO1
44
pS/m



GO1 + 200 ppm A1(75% Solvarex)
367
pS/m



GO1 + 100 ppm A1(75% Solvarex)
204
pS/m



GO1 + 200 ppm B1
45
pS/m



GO1 + 200 ppm B2
47
pS/m



GO1 + 200 ppm B3
40
pS/m



GO1 + 200 ppm C1
70
pS/m



GO1 + 200 ppm B1/A1 - 50/50
163
pS/m



GO1 + 200 ppm B1/A1/C1 - 42/43/15
145
pS/m



GO1 + 200 ppm B2/A1/C1 - 42/43/15
104
pS/m



GO1 + 200 ppm B3/A1/C1 - 42/43/15
182
pS/m




















TABLE VII







Corrosion Test
Fresh water









GO1
E



GO1 + 200 ppm A1
A



GO1 + 200 ppm B1
A



GO1 + 200 ppm B1/A1 - 50/50
A



GO1 + 200 ppm B1/A1/C1 - 42/43/15
A



GO1 + 200 ppm B2/A1/C1 - 42/43/15
A



GO1 + 200 ppm B3/A1/C1 - 42/43/15
A







E = corroded,



A = no corrosion






Even if there is good conductivity efficiency and no corrosion with A1 alone, the same cannot be said for lubricity (cf. table III of Example II).


On the other hand, the Bis contribute only a low conductivity but a high lubricity.


In order to achieve the aims of the invention, it is therefore necessary to establish the best compromise between Ai, Bi and Ci, promoting both lubricity and conductivity, with no corrosion. The best compromise is obtained with a ratio A1/B1/C1 corresponding to 43/42/15, lubricity ranging from 300 μm to 350 μm.


EXAMPLE VI

The present example aims to illustrate the significant effect of the mixture Ai/Bi on lubricity, conductivity and corrosion in a kerosene containing less than 3000 ppm sulphur The results are given in Table VIII below.












TABLE VIII







Conductivity
HFRR


Test
WSIM
ASTM D2624
(μm)



















Kero
98
50
pS/m
808 μm


Kero + A1 (200 ppm)
99
356
pS/m
440 μm


Kero + A1 (100 ppm)
98
2046
pS/m
660 μm


Kero + B1 (200 ppm)
95
56
pS/m
435 μm


Kero + B1 (100 ppm)

<56
pS/m
516 μm


Kero + A1/B1/C1 - (200 ppm)
48
164
pS/m
386 μm


42/43/15









The effects of the composition according to the invention can also be clearly seen for the kerosenes.

Claims
  • 1. A lubricating, anti-corrosive and antistatic composition for hydrocarbon mixtures comprising: a) at least a compound A of Formula (I) below:
  • 2. Composition according to claim 1, characterized in that the composition comprises from 40 to 70% by weight of at least a compound A and from 60 to 30% by weight of at least a compound B.
  • 3. Composition according to claim 1, characterized in that it comprises at least 0.1% by weight of a compound C chosen from C5-C30 mono- and/or polycarboxylic acid esters.
  • 4. Composition according to claim 3, characterized in that it comprises from 30 to 70% by weight of at least a compound A, from 60 to 30% of at least a compound B and from 0.1 to 20% of at least a compound C.
  • 5. Composition according to claim 3, characterized in that it comprises from 30 to 60% by weight of at least a compound A, from 60 to 30% of at least a compound B and from 5 to 20% of at least a compound C.
  • 6. Composition according to claim 1, characterized in that, in Formula (I) of compound A, R1 is an alkenyl group of 1-22 carbon atoms, and R2 is hydrogen, or vice-versa.
  • 7. Composition according to claim 1, characterized in that, in Formula (I) of compound A, R1 and R2 together form a ring with 5 or 6 aromatic or aliphatic carbons, optionally substituted by one to three alkyl group(s) of 1-3 carbons.
  • 8. Composition according to claim 1, characterized in that, in Formula (I) of compound A, R3 and R4, identical or different, are OR5 with R5 a group chosen from —[(CH2)n—O]m—H with n varying from 1-4 and m varying from 1-5; —[CH2—CHOH]p—CH2—OH, with p varying from 1-3; —CH2—CR6R7-OH, with R6 and R7 which can each be hydrogen, a methyl radical or a —CH2OH radical.
  • 9. Composition according to claim 1, characterized in that, in Formula (I) of compound A, R3 is OR5 with R5 a C1-C10 linear or branched alkyl group, possibly substituted by at least one OH group, and R4 is OH or vice-versa.
  • 10. Composition according to claim 1, characterized in that, in Formula (I) of compound A, R3 and R4 are OR5 groups, identical or different, with R5 a C1-C10 linear or branched alkyl group, possibly substituted by at least one OH group.
  • 11. Composition according to claim 1, characterized in that, in Formula (I) of compound A, R3 is OH or an OR5 group with R5 a C1-C10 linear or branched alkyl group, optionally substituted by at least one OH group, and R1 is OR5 with R5 a —[(CH2)n—O]m—H group with n varying from 1 to 4 and m varying from 1 to 5; —[CH2—CHOH]p—CH2—OH, with p varying from 1 to 3; —CH2-CR6R7—OH, with R6 and R7 which can each be hydrogen, a methyl radical or a —CH2OH radical.
  • 12. Composition according to claim 1, characterized in that, in Formula (I) of compound A, the OR5 groups are the groups —O—CH2—CH2—OH or O—CH2—CHOH—CH2—OH or —O—CH2—C(CH3)(CH2OH)—CH2—OH or —O—CH2—C(CH2OH)(CH2OH)—CH2—OH.
  • 13. Composition according to claim 1, characterized in that compound B comprises at least one saturated or unsaturated linear carboxylic acid comprising 10-24 atoms and/or their esters, amide or amine salts derivatives, taken alone or in a mixture.
  • 14. Composition according to claim 1, characterized in that the majority of compound B comprises a mixture of oleic, linoleic, palmitic, stearic, isostearic and lauric acids and/or their esters, amide or amine salts derivatives, taken alone or in a mixture.
  • 15. Composition according to claim 1, characterized in that compound B comprises a mixture of fatty acids of plant origin, from rapeseed, ricin, sunflower, maize, copra, pine or flax and/or their esters, amide or amine salts derivatives, taken alone or in a mixture.
  • 16. Composition according to claim 1, characterized in that compound B is constituted by a mixture of fatty acids originating from the distillation of pine oils and/or their esters or amine salts derivatives.
  • 17. Composition according to claim 1, characterized in that the compound B comprises resin acids, including abietic acid, dihydroabietic acid, tetrahydroabietic acid, dehydroabietic acid, neoabietic acid, pimaric acid, levopimaric acid and parastinic acid, and/or their esters, amide or amines salt derivatives, taken alone or in a mixture.
  • 18. Composition according to claim 1, characterized in that the compound B is constituted by a mixture of fatty acids and resin acids originating from the distillation of vegetable oil, their esters, amide or amine salts derivatives.
  • 19. Composition according to claim 3, characterized in that the compound C is a vegetable oil ester of rapeseed, ricin, sunflower, maize, copra, pine or flax, preferably methyl ester of rapeseed.
  • 20. Hydrocarbonated mixture comprising at least 50 ppm of a composition according to claim 1, preferably between 50 and 350 ppm of said composition.
  • 21. Hydrocarbonated mixture according to claim 20, with a low sulphur content below 50 ppm, preferably below 10 ppm.
  • 22. Hydrocarbonated mixture according to claim 20, characterized in that it comprises hydrocarbons originating from the distillation of crude oil, gasoline, a gas oil, a kerosene or a lubricant, optionally in a mixture with biofuels and/or synthetic fuels originating from the treatment of the gas, this mixture being able to form a stable emulsion in water.
  • 23. Hydrocarbonated mixture according to claim 20, which is a gasoline comprising at least one additive chosen from the group consisting of anti-knock, antifreeze, detergent, de-emulsifying, antioxidant, friction modifying, deposit reduction additives and their mixtures.
  • 24. Hydrocarbonated mixture according to claim 20, which is a diesel fuel comprising at least one additive chosen from the group consisting of filterability, anti-foam, detergent, de-emulsifying additives, procetane and their mixtures.
  • 25. Hydrocarbonated mixture according to claim 20, which is a domestic heating oil comprising at least one additive chosen from the group consisting of combustion promoting additives, low-temperature resistance additives, flow, anti-corrosion, antioxidant, biocide, reodorant additives and their mixtures.
  • 26. Hydrocarbonated mixture according to claim 20, which is a kerosene comprising at least one additive chosen from the group consisting of anti-static and antioxidant additives and their mixtures.
  • 27. Hydrocarbonated mixture according to claim 20, which is a lubricant comprising at least one additive chosen from the group consisting of dispersant, de-emulsifying, detergent, anti-foam, antioxidant, low-temperature resistance to improve in particular the pour point, reodorant additives and their mixtures.
  • 28. Hydrocarbonated mixture comprising at least 50 ppm of a composition according to claim 19.
  • 29. Hydrocarbonated mixture according to claim 28, with a sulphur content below 50 ppm.
  • 30. Hydrocarbonated mixture according to claim 29, comprising from 50 to 350 ppm of the composition.
  • 31. Hydrocarbonated mixture according to claim 30, wherein the sulphur content is below 10 ppm.
Priority Claims (1)
Number Date Country Kind
05/071128 Jul 2005 FR national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/FR2006/001578 7/4/2006 WO 00 12/17/2007