Biodiesel containing non-phenolic additives and thereby possessing enhanced oxidative stability and low acid number

Information

  • Patent Application
  • 20120023811
  • Publication Number
    20120023811
  • Date Filed
    July 08, 2009
    15 years ago
  • Date Published
    February 02, 2012
    12 years ago
Abstract
Biodiesel compositions are provided, containing non-phenolic additives that improve the oxidative stability and lower the acid number. The invention further provides non-phenolic additive concentrate compositions and diesel fuel compositions containing the above biodiesel compositions.
Description
FIELD OF THE INVENTION

This invention relates to improved biodiesel fuel. It is more particularly concerned with biodiesel fuel containing non-phenolic additives that enhance the oxidative stability and simultaneously decrease the acid number.


BACKGROUND OF THE INVENTION

Carbon dioxide emissions from fuel usage are generally considered a major contributor to global warming. As a means to alleviate the problem, an increased use of biomass derived fuel components (biofuels) in gasoline and diesel fuel is being pursued in many parts of the world. A significant portion of the total amount of biofuels used in the transportation sector is taken by biodiesel, whose consumption in the European Union is already in the millions of tons. The accepted source of biodiesel are various types of vegetable or animal fats and oils, which are generally transesterified to a mixture of fatty acid methyl or ethyl esters so as to reduce viscosity and improve combustion behavior. The resulting biodiesel is quite similar to conventional diesel fuel in many of its properties, such as viscosity, density and ignition quality. Biodiesel is also very compatible with conventional diesel and the two can be blended in any proportion.


In order for biodiesel to be acceptable as a fuel for diesel engines, either alone or mixed with conventional petrodiesel, it has to meet a number of quality criteria irrespective of the raw material that was used for its production. To this end, a number of specifications have been developed, such as EN 14214 in Europe and ASTM D-6751 in the United States, which strictly control the properties and characteristics of biodiesel fuels. The difference in chemical structure between biodiesel (a mixture of liquid carboxylic esters) and the conventional, petroleum derived diesel fuel or petrodiesel (a mixture of liquid hydrocarbons) leads to some notable differences in chemical behavior. Among the most important such differences are the lower stability of biodiesel towards oxidation and also its higher acidity in comparison to petrodiesel. Recognizing this, the European Standard EN 14214 places strict limits both as to the oxidative stability and as to the acidity of biodiesel. It is also noteworthy that the newest version of the European Standard EN 590 for road diesel, which allows the addition of up to 7% of biodiesel, also mandates that the final fuel blend meet specific new requirements as to its oxidative stability.


DESCRIPTION OF THE PRIOR ART

The oxidative stability of biodiesel has been the subject of extensive research in recent years. The consensus is that unsaturation in the fatty acid alkyl chain, particularly as it appears in polyunsaturated fatty acids, is the major cause of oxidative instability. One remedy for this situation is the careful selection of the raw materials used for biodiesel production so as to minimize the content of unsaturated fatty acids. The disadvantage of this approach is that large quantities of vegetable oils would be labeled as unfit for biodiesel production in the face of a constantly increasing demand for this renewable fuel. The alternative solution that has been widely adopted is the addition of small quantities of antioxidant additives that greatly enhance the oxidative stability of biodiesel. The vast majority of antioxidant additives that are used for this purpose are of the phenolic type, so named because they possess at least one hydroxyl group directly attached to an aromatic ring. Among the most common phenolic antioxidants are 2,6-di-tert-butyl-4-cresol, commonly known as BHT (butylated hydroxytoluene), 2,6-di-tert-butyl-4-methoxyphenol, commonly known as BHA (butylated hydroxyanisol), propyl gallate, 1,2,3-trihydroxybenzene (pyrogallol), and tert-butyl-hydroquinone (TBHQ). The chemical structures of these materials are drawn below, plainly displaying their common feature of one or more phenolic hydroxyls.




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These and many other phenolic antioxidants have appeared in the technical literature (cf. Gerhard Knothe, “Some aspects of biodiesel oxidative stability”, Fuel Processing Technology, vol. 88, pp. 669-677, 2007; Southwest Research Institute, “Characterization of biodiesel oxidation and oxidation products”, CRC Project No. AVFL-2b, 2005; and references therein) and are also the subjects of various patents (e.g. German Patent DE 10 252 714 A1, 2002; German Patent DE 10 2005 015 474 A1, 2006; European Patent EP 1989275, 2007).


References to other types of antioxidant additives for biodiesel are scant; a recent world patent (WO 2008 121526 A1) discloses antioxidant blends of aromatic diamines with phenolic antioxidants for biodiesel.


Phenolic antioxidants are generally effective in improving the oxidative stability of biodiesel. However, because of the acidic character of the phenolic hydroxyl, they tend to have a negative impact on the acid number of biodiesel. This behavior was reported in a recent study, where it was observed that phenolic antioxidants of various types generally increased the acid number of biodiesel and sometimes brought it above the specification limit, thus making the biodiesel unfit for purpose (Sigurd Schober and Martin Mittelbach, “The impact of antioxidants on biodiesel oxidation stability”, Eur. J. Lipid Sci. Technol., vol. 106, pp. 382-389, 2004).


The acid number is a measure of the amount of acidic components that exist in biodiesel or any other fuel. Since the acidic components are unwanted (they can lead to corrosion of the fuel system and general instability of the fuel itself) the acid number of biodiesel is strictly controlled both in Europe (EN 14214) and the United States (ASTM D-6751). Up to now no additives have been mentioned that would act as acid number depressants.


From the above considerations it becomes obvious that there is a need for antioxidant additives for biodiesel that will possess the same or higher antioxidant activity as the phenolic antioxidants without their negative impact on the acid number. The present invention offers an answer to this need.







DESCRIPTION OF THE INVENTION

The basis of the invention is the discovery that the reaction product of a carboxylic acid and a polyamine, when added to biodiesel in small amounts, is capable of greatly improving the oxidative stability of the biodiesel and simultaneously lowering its acidity, as determined by measuring the acid number.


It is known in the art that when a carboxylic acid (I) is reacted with a 1,2-diamine (II) a 5-membered heterocyclic ring, imidazoline (III) is eventually formed by loss of water, as shown by reaction scheme (1):




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In a similar fashion, if a 1,3-diamine (IV) is reacted with a carboxylic acid, a 6-membered heterocyclic ring, tetrahydropyrimidine (V) is formed, as in reaction scheme (2):




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As mentioned above, the unexpected discovery was made that certain preparations containing the imidazoline (formal name: 4,5-dihydro-1H-imidazole) or tetrahydropyrimidine (formal name: 1,4,5,6-tetrahydro-pyrimidine) moieties (III) and (V) are very effective antioxidants and acid number reducers for biodiesel and its mixtures with petrodiesel. Imidazoline and tetrahydropyrimidine derivatives have been mentioned in the patent literature as components in pharmaceutical preparations (e.g. U.S. Pat. Nos. 5,470,856; 5,925,665; 6,294,566; 6,410,562; 6,875,788; 6,884,801; 7,173,044; 7,482,358), corrosion inhibitors (e.g. U.S. Pat. Nos. 7,057,050; 4,518,782), fuel detergents (e.g. U.S. Pat. Nos. 4,247,300; 2,961,308) etc. To our knowledge the use of imidazoline and tetrahydropyrimidine derivatives as improvers for biodiesel and biodiesel/petrodiesel blends has not been reported up to know and is novel.


For the purposes of this invention, the carboxylic acid portion in reactions (1) and (2) can be either a free acid or a lower ester (preferably a methyl or ethyl ester); in the latter case one mole of water and one mole of alcohol are evolved with the formation of the heterocyclic ring. The desired structure of the carboxylic moiety for the above reactions is shown in formula (VI):




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Where:

    • R1 is a straight or branched alkyl or hydroxyalkyl group having the formula CmH2m−x−k+1(OH)k (m being an integer from 1 to 30, x being 0, 2, 4, or 6 but always fulfilling the relation x<m, and k being 0 or 1), a cyclohexyl group, a phenyl group, or a substituted phenyl group bearing a C1 to C12 alkyl substituent.
    • R2 is hydrogen, methyl, or ethyl.


Based on formula (VI), the carboxylic moiety can be, but is not limited to, any linear monocarboxylic acid from acetic to melissic; a branched carboxylic acid such as isovaleric or isooctanoic; an unsaturated carboxylic acid such as oleic, linoleic, or linolenic; a hydroxyacid such as ricinoleic; a carbocyclic acid such as cyclohexanoic; an aromatic acid such as benzoic or toluic; and the like. The methyl or ethyl esters of the above acids are also desirable. Mixtures of acids and/or esters, such as those derived from fats and oils by saponification or transesterification are particularly desirable because of their low cost.


The amine portion in reactions (1) and (2) must fulfill certain structural requirements. It must contain at least one primary amine nitrogen atom which is separated by two or three carbon atoms from a second amine nitrogen atom that is primary or secondary. More amine nitrogen atoms may be present and are desirable. Aromatic amines are not preferred because of their high toxicity. Thus the desired structure of the amine moiety is as shown in formula (VII):




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Where:

    • n is 0 or 1.
    • R3 and R4 are hydrogen, methyl, or taken together are part of a cyclohexane ring.
    • R5 is hydrogen, or methyl.
    • R6 is hydrogen, a straight or branched alkyl group having the formula CmH2m−x+1 (m being an integer from 1 to 22 and x being 0, 2, 4, or 6 but always fulfilling the relation x<m), or an amine moiety having the formula —CH2CH2(CH2)pNH[CH2CH2(CH2)pNH]qH with p being 0 or 1 and q being 0, 1, 2, 3, or 4.


Based on formula (VII), the amine moiety can be a diamine, such as 1,2-diaminoethane, 1,2-diaminopropane, 1,3-diaminopropane, 1,2-diaminocyclohexane, and the like; commercially available mixtures of diamines, such as the various substituted 1,3-propanediamines with the trade name DUOMEEN, can also serve as the amine moiety. Polyamines, such as diethylene triamine (DETA), triethylene tetramine (TETA), tetraethylene pentamine (TEPA), dipropylene triamine, and the like are also desirable forms of the amine moiety. The commercially available polyamines such as TETA, TEPA, and their higher homologues are not pure compounds but mixtures of linear, branched, and cyclic polyamines. It is evident that the reaction products of these mixed polyamines with the carboxylic moieties of formula (VI) are not in their turn pure imidazolines or tetrahydropyrimidines; they were found, nevertheless, to be very effective antioxidants and acid number reducers for biodiesel and are therefore among the preferred embodiments of the present invention.


All the reaction products that are useful for the purposes of this invention, as described above, are obtained as solids or viscous liquids. In many instances it is convenient for handling purposes to employ them in the form of concentrated solutions. These solutions may contain from 5% to 95% by weight of the active ingredient dissolved in a suitable solvent, such as a liquid hydrocarbon mixture of high flash point, a biodiesel suitable for use in a compression ignition engine, or a mixture of the two:


The common structural feature of all the products arising from the reaction between a carboxylic acid (VI) and an amine (VII) is that of the imine group (VIII):




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However, the imine group by itself is not sufficient to impart antioxidant activity. It was found that an open chain imine such as that in tetramethylguanidine (IX) is totally ineffective. Similarly, an imine such as that in an oxazoline (X) is of very low effectiveness.




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Thus it appears that for good antioxidant effectiveness the desired structural feature is that of a cyclic carboxamidine, where the imine group and an amine group are attached to the same carbon atom of a 5-membered or a 6-membered heterocyclic ring, thus forming either an imidazoline of structure (III) or a tetrahydropyrimidine of structure (V).




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The methods for preparing imidazolines and tetrahydropyrimidines are simple and well known in the art and have been reported in the patent literature since the 1930's (cf. U.S. Pat. No. 2,155,877). However, particularly in the cases where the starting amine is of the polyamine type, the published preparation procedures, despite their simplicity, require heating of the reactants at temperatures up to 300° C. for long periods of time. It was found that addition to the reaction mixture of a small amount of a strong organic base (e.g. tetramethylguanidine) can speed up the reaction and permit its completion at lower temperatures.


Having described the invention in general terms, we will proceed with specific examples that illustrate its implementation and efficacy.


SPECIFIC EXAMPLES

Examples 1 to 10 were pure chemical entities, produced by the reaction of a single carboxylic moiety of formula (VI) with either 1,2-diaminoethane (II) or 1,3-diaminopropane (IV); thus their chemical structure was that of either a substituted imidazoline (III) or a substituted tetrahydropyrimidine (V). Comparison examples 11 and 12 had the oxazoline structure (X), whereas comparison example 13 was tetramethylguanidine (IX), obtained from a chemical supply house. Experimental details are provided for the preparation of examples 1, 5, and 11 which are typical for the three classes of compounds (III), (V), and (X). Table 1 lists details of all the above examples.


Examples 14 to 30 were prepared from mixtures of carboxylic moieties of formula (VI), mixtures of amine moieties of formula (VII), or both. In these cases it was found advantageous to add a small amount of tetramethylguanidine (IX) as a reaction promoter. Experimental details are provided for the preparation of Examples 14 and 28, which is typical of all the others. Table 2 lists details of examples 14 to 30.


Example 31 demonstrates the effectiveness of examples 1 to 30 as antioxidants in biodiesel, based on experimental measurements. Example 32 deals with the antioxidant effectiveness in blends of biodiesel with conventional petrodiesel, as required by the latest European Standard EN 590. Finally, example 33 addresses the effect on acid number of representative examples.


Example 1

In a round bottom flask equipped with a water separator and a reflux condenser were placed 50 g (0.25 mol) of lauric acid dissolved in 150 mL toluene and then 16.8 g (0.28 mol) of 1,2-diaminoethane were added dropwise and with stirring. The mixture was heated under reflux until water stopped separating and then the toluene was distilled off in vacuo. The solid residue was recrystallized from a mixture of toluene and heptane, thus affording the desired 2-undecyl imidazoline as colorless crystals, m.p. 123-125° C.


Example 5

Lauric acid and 1,3-diaminopropane were reacted in the same fashion as example 1 and afforded 2-undecyl tetrahydropyrimidine, m.p. 66-67° C.


Comparison Example 11

Lauric acid and 2-aminoethanol were reacted in the same fashion as example 1 and afforded 2-undecyl oxazoline, m.p. 71-74° C.













TABLE 1







ENTITY
STRUCTURE
R









EXAMPLE 1
(III)
n-Undecyl



EXAMPLE 2
(III)
n-Pentadecyl



EXAMPLE 3
(V)
n-Butyl



EXAMPLE 4
(V)
n-Heptyl



EXAMPLE 5
(V)
n-Undecyl



EXAMPLE 6
(V)
n-Tridecyl



EXAMPLE 7
(V)
n-Pentadecyl



EXAMPLE 8
(V)
n-Heptadecyl



EXAMPLE 9
(V)
Cyclohexyl



EXAMPLE 10
(V)
Oleyl



COMPARISON EXAMPLE 11
(X)
n-Undecyl



COMPARISON EXAMPLE 12
(X)
Oleyl



COMPARISON EXAMPLE 13
(IX)











Example 14

50 g of commercial tetraethylenepentamine (TEPA) was placed in a 500 mL round bottom flask and 0.25 g of tetramethylguanidine was added. The mixture was brought to a temperature of 100° C. with stirring under a nitrogen atmosphere. Technical oleic acid of 90% purity (141 g) was then added dropwise over a period of 30 minutes with continued stirring. A vacuum of about 50 mm Hg was then applied and the temperature was increased to 170° C. and was kept there for 4 hours. The heating was then discontinued, the vacuum was broken with nitrogen being admitted, and the flask was allowed to cool to room temperature. The product was a light brown viscous oil and its weight revealed the loss of about 1 mol of water.


Example 28

The procedure of example 14 was repeated, except that the oleic acid was replaced by 130 g of a mixture of fatty acids obtained from the saponification of cottonseed oil. The product was a viscous and clear brown oil.











TABLE 2





ENTITY
CARBOXYLIC MOIETY
AMINE MOIETY







EXAMPLE 14
OLEIC ACID
TEPA


EXAMPLE 15
BENZOIC ACID
DUOMEEN C


EXAMPLE 16
OCTANOIC ACID
DUOMEEN C


EXAMPLE 17
VALERIC ACID
DUOMEEN C


EXAMPLE 18
CYCLOHEXANOIC ACID
DUOMEEN C


EXAMPLE 19
LAURIC ACID
DUOMEEN C


EXAMPLE 20
OLEIC ACID
DUOMEEN C


EXAMPLE 21
LAURIC ACID
DUOMEEN O


EXAMPLE 22
LAURIC ACID
DETA


EXAMPLE 23
CYCLOHEXANOIC ACID
DETA


EXAMPLE 24
METHYL OLEATE
TEPA


EXAMPLE 25
METHYL OLEATE
TETA


EXAMPLE 26
LAURIC ACID
TETA


EXAMPLE 27
FFA 1
DETA


EXAMPLE 28
FFA 1
TEPA


EXAMPLE 29
FFA 2
DETA


EXAMPLE 30
FFA 2
TEPA









Because of space limitations in Table 2 certain abbreviations are used, whose meaning is the following:

    • DETA, TETA, and TEPA are common names for the commercially available mixtures of ethylene polyamines, also known as diethylene triamine, triethylene tetramine, and tetraethylene pentamine respectively.
    • DUOMEEN C is the commercial name of a mixture of 1-alkyl-1,3-propanediamines, whose alkyl groups are ultimately derived from coconut oil via an intermediate coco-amine. DUOMEEN O is a similar mixture, ultimately derived from olive oil via an intermediate oleylamine.
    • FFA 1 is a mixture of free fatty acids that was produced by saponification of cottonseed oil. FFA 2 was similarly derived from rapeseed oil.


Example 31

To test the antioxidant activity of the above additives, a biodiesel base fuel was utilized and was designated as Biodiesel A. It was prepared by base catalyzed transesterification with methanol of a vegetable oil blend consisting of 65% rapeseed oil and 35% used frying oil. Two more biodiesel base fuels were used in some of the experiments, designated as Biodiesel B and Biodiesel C; the former was made from a mixture of 36% used frying oil, 20% palm oil, and 44% soybean oil and the latter from a mixture of 32.4% used frying oil, 36% rapeseed oil, and 21.6% soybean oil. Some of the important characteristics of these three biodiesel base fuels are shown in Table 3, along with the respective limits in the European Standard EN 14214 and the methods that were used to measure them.














TABLE 3






Methyl







Ester
Sulfur
Water
Acid
Oxidation


Property
Content
Content
Content
Number
Stability







Unit
% m/m
mg/kg
mg/kg
mg KOH/g
hours


Biodiesel A
96.7
5.0
352
0.47
4.8


Biodiesel B
97.8
5.0
356
0.28
 4.15


Biodiesel C
97.9
5.0
300
0.26
6.5


Limit
96.5 min
10 max
500 max
0.50 max
6 min


Method
EN 14103
EN ISO
EN ISO
EN 14104
EN 14112




20846
12937









The method that was used to measure the oxidation stability in all cases was EN 14112, which is prescribed in the European Standard EN 14214 and is commonly known as the Rancimat test. It measures, under specified conditions, the induction period before the onset of rapid oxidation; the minimum acceptable value is 6 hours according to EN 14214.


Each of the examples 1-10 and 14-30 was separately added to Biodiesel A at a concentration of 1000 ppm (0.1% m/m) and the oxidation stability was measured by the Rancimat test in triplicate. For comparison purposes the same procedure was used with comparison examples 11-13 and also with BHT, one of the most widely used phenolic antioxidant additives for biodiesel. To make comparisons easier, the relative effectiveness of each example in comparison to BHT was computed according to formula (3):






R=(SE−S0)/(SB−S0)  (3)


Where R is the relative effectiveness in comparison to BHT, SE is the induction period of the biodiesel containing the example additive, S0 is the induction period of the neat biodiesel, and SB is the induction period of the biodiesel containing BHT.


Table 4 shows the Rancimat induction period (average of 3 determinations) and the relative performance of all examples.











TABLE 4






INDUCTION PERIOD
RELATIVE


ADDITIVE
(hours)
EFFECTIVENESS

















NONE
4.80



BHT
8.89
1.00


EXAMPLE 1
5.91
0.27


EXAMPLE 2
6.22
0.35


EXAMPLE 3
10.45
1.38


EXAMPLE 4
8.94
1.01


EXAMPLE 5
11.64
1.67


EXAMPLE 6
9.43
1.13


EXAMPLE 7
8.99
1.02


EXAMPLE 8
8.29
0.85


EXAMPLE 9
9.67
1.19


EXAMPLE 10
9.72
1.20


EXAMPLE 14
12.06
1.78


EXAMPLE 15
11.48
1.63


EXAMPLE 16
10.69
1.44


EXAMPLE 17
10.31
1.35


EXAMPLE 18
9.55
1.16


EXAMPLE 19
9.08
1.05


EXAMPLE 20
8.89
1.00


EXAMPLE 21
8.88
1.00


EXAMPLE 22
8.91
1.00


EXAMPLE 23
7.58
0.68


EXAMPLE 24
10.28
1.34


EXAMPLE 25
8.91
1.00


EXAMPLE 26
7.69
0.71


EXAMPLE 27
11.24
1.57


EXAMPLE 28
14.65
2.41


EXAMPLE 29
12.52
1.89


EXAMPLE 30
15.89
2.71


COMPARISON
5.17
0.09


EXAMPLE 11


COMPARISON
5.02
0.05


EXAMPLE 12


COMPARISON
4.79
0.00


EXAMPLE 13









On examining the results shown in Table 4, the following observations can be made:

    • All 27 examples of this invention improved the oxidative stability of the biodiesel base fuel.
    • The oxidation stability improvement in all but one of the examples was enough to bring the off-specification base biodiesel A to within specification.
    • A large majority of the examples (20 out of 27) were more effective than BHT in improving the oxidative stability of biodiesel A, with two of them being more than twice as effective.
    • Comparison examples 11 and 12 (which possessed the oxazoline moiety) showed only a very slight antioxidant activity, whereas the acyclic amidine of comparison example 13 displayed a complete lack of such activity.


Several of the more effective examples in Table 4 were also tested in the more prone to oxidation Biodiesel B and at a lower concentration of 500 ppm (0.05% m/m). The results of the Rancimat test are shown in Table 5.













TABLE 5








INDUCTION PERIOD
RELATIVE



ADDITIVE
(hours)
EFFECTIVENESS




















NONE
4.15




BHT
6.65
1.00



EXAMPLE 3
8.39
1.70



EXAMPLE 5
8.04
1.56



EXAMPLE 9
7.74
1.44



EXAMPLE 14
7.99
1.54



EXAMPLE 15
8.30
1.66



EXAMPLE 16
8.08
1.57



EXAMPLE 17
7.52
1.35



EXAMPLE 24
7.80
1.46



EXAMPLE 27
8.44
1.72



EXAMPLE 28
10.12
2.39



EXAMPLE 29
9.30
2.06



EXAMPLE 30
10.54
2.56










All the examples listed in Table 5 showed high antioxidant activity at the lower concentration of 500 ppm and they were all significantly more effective than the phenolic antioxidant BHT in this respect.


Example 32

Given that the newest European Standard for road diesel EN 590 has a requirement for minimum oxidation stability of the final biodiesel/petrodiesel blend, a series of experiments were run to test the efficacy of the additives of this invention in this respect. Biodiesel C was blended in several concentrations with an ultra low sulfur conventional diesel fuel meeting the current European specifications. Example 29 was used as the antioxidant additive and was compared with the well known phenolic antioxidant TBHQ.


Three batches of Biodiesel C were used for this set of experiments. One was neat, the second contained 1000 ppm of the additive of example 29, and the third contained 1000 ppm of TBHQ. Neat Biodiesel C had an oxidation stability of 6.5 hours, as already mentioned in Table 3; the stability of the second batch was increased to 12.5 hours by the presence of Example 29, whereas the stability of the third batch was brought up to an impressive 21.6 hours by TBHQ, which thus appeared as an extremely effective antioxidant additive for biodiesel.


The three batches were mixed at various proportions with petrodiesel and the oxidation stability of the resulting blends was measured by the modified Rancimat method (EN 15751) as required by EN 590. The specification limit for the induction period in blends is set as 20 hours minimum.


Table 6 contains the results of these tests.










TABLE 6







BIODIESEL
INDUCTION TIME (hours)










IN THE BLEND
NO ANTIOXIDANT
EXAMPLE 29
TBHQ













100%
6.50
12.50
21.60


10% v/v 
22.68
32.61
24.05


7% v/v
28.66
35.43
27.48


5% v/v
31.66
37.79
28.70


4% v/v
33.22
39.58
29.81


3% v/v
34.48
39.55
30.80


2% v/v
37.74
38.34
32.57









The results in Table 6 show that Example 29 of this invention is effective in enhancing the oxidative stability of biodiesel whether it is neat or blended with conventional diesel fuel in various proportions. The situation is completely different with the phenolic antioxidant TBHQ; it is extremely effective in stabilizing neat biodiesel but in the case of blends its effectiveness disappears and it actually behaves as a pro-oxidant when the biodiesel concentration is 7% or less.


Example 33

To measure the effect of additives on biodiesel acidity several samples were prepared, each one being a solution containing 1000 ppm of either a phenolic antioxidant or one of the examples of the present invention in one of the biodiesel base fuels A, B, or C. The acid number of each sample was measured with standard method EN 14104 and the results are shown in Table 7.


All phenolic antioxidants increase the acid number of the biodiesel they are dissolved in, which is expected on account of the acidity of the phenolic hydroxyls that they all contain. By contrast, all examples of the present invention reduced the acid number of the biodiesel, a fact that is attributed to the basicity of their chemical structures which can all be classed as amine derivatives.











TABLE 7









ACID NUMBER (mg KOH/g)










ADDITIVE
Biodiesel A
Biodiesel B
Biodiesel C













NONE
0.47
0.28
0.26


BHT*
0.53
0.51
0.29


TBHQ*
0.49
0.44
0.32


PROPYL GALLATE*
0.55
0.52
0.38


EXAMPLE 3
0.35
0.26
0.24


EXAMPLE 5
0.28
0.21
0.20


EXAMPLE 14
0.34
0.23
0.21


EXAMPLE 27
0.29
0.24
0.23


EXAMPLE 29
0.27
0.24
0.22





*phenolic antioxidant






Having described the invention in detail, those skilled in the art will understand that modifications may be made to the various aspects of the invention without departing from the spirit and scope of the invention that is disclosed herein. It is, therefore, not intended that the scope of the invention be limited to the specific embodiments that were described as examples but rather that the scope of the present invention be defined by the appended claims.

Claims
  • 1) A biodiesel composition of improved oxidation stability and low acid number, comprising: a. A major amount of biodiesel fuel suitable for use in a compression ignition engine and consisting of a mixture of methyl or ethyl esters of fatty acids derived from fats and oils of vegetable or animal origin, andb. A minor amount of a substance or mixture of substances which is the product of the chemical reaction between Component 1 and Component 2, wherein:Component 1 is a carboxylic acid, a carboxylic ester or a mixture of carboxylic acids and/or esters having the chemical formula:
  • 2) A biodiesel composition according to claim 1, where Component 2 is N-(2-aminoethyl-1,2-ethanediamine), also known as Diethylene Triamine or DETA.
  • 3) A biodiesel composition according to claim 1, where Component 2 is the mixed polyamine Triethylene Tetramine or TETA.
  • 4) A biodiesel composition according to claim 1, where Component 2 is the mixed polyamine Tetraethylene Pentamine or TEPA.
  • 5) A biodiesel composition according to claim 1, where Component 1 is a mixture of fatty acids obtained by the saponification of a vegetable or animal oil or fat or a mixture of such oils or fats.
  • 6. A biodiesel composition according to claim 1, where the substance or mixture of substances described in paragraph (b) is present at a concentration between 0.01 percent by weight and 1 percent by weight.
  • 7) A biodiesel composition according to claim 1, which also contains an appropriate amount of additives for improving some of its properties such as ignition quality, cold flow characteristics, resistance to microbial degradation, tribological characteristics, and the like.
  • 8) An additive concentrate composition comprising a. at least 5 percent by weight of a substance or mixture of substances which is the product of the chemical reaction between Component 1 and Component 2 according to claim 1, andb. up to 95 percent by weight of a diluent consisting of a liquid mixture of hydrocarbons having a flash point of at least 100° C. and a final boiling point of less than 340° C., a biodiesel fuel suitable for use in a compression ignition engine and consisting of a mixture of methyl or ethyl esters of fatty acids derived from fats and oils of vegetable or animal origin, or a blend of liquid hydrocarbons and biodiesel fuel as defined hereinabove.
  • 9) A diesel fuel composition comprising: Conventional diesel fuel derived from petroleum or other mineral fuels and suitable for use in a compression ignition engine, to the extent of 99 percent or less by volume, andA biodiesel composition according to claim 1, to the extent of one percent or more by volume.
  • 10) A diesel fuel composition according to claim 9, which also contains an appropriate amount of additives for improving some of its properties such as ignition quality, cold flow characteristics, resistance to microbial degradation, tribological characteristics, and the like.
  • 11) A method for the preparation of the substance or mixture of substances according to paragraph (b) of claim 1, consisting of the addition to the reaction mixture of a strong organic base, such as tetramethylguanidine, to the extent of 0.1% to 5% by weight in relation to the weight of Component 2 described in claim 1.
Priority Claims (1)
Number Date Country Kind
20090100113 Feb 2009 GR national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/GR09/00047 7/8/2009 WO 00 8/22/2011