Phase behaviors and properties of certain triacylglycerols and fatty acid methyl esters
This application relates to phase behaviors of certain triacylglycerols and fatty acid methyl esters, and how the phase behaviors of these individual components in a biodiesel fuel, as well as their combined mixtures, helps understand the fundamental mechanisms of their crystallization so as to design biodiesel fuels with improved low temperature characteristics.
1. A method for reducing the cloud point temperature of a biodiesel fuel, the method comprising:
(a) mixing the biodiesel fuel with a biodiesel crystallization depressant composition consisting essentially of a triacylglycerol having (a) an unsaturated fatty acid in the sn-1 and sn-3 positions, and (b) a saturated fatty acid in the sn-2 position; and
(b) obtaining the biodiesel fuel with a reduced cloud point temperature,
wherein the triacylglycerol is 1,3-dioleoyl-2-palmitoyl glycerol or 2-stearoyl diolein (OSO).
2. The method of claim 1 , wherein the triacylglycerol is mixed with a biodiesel fuel comprising at least one saturated, monounsaturated, or polyunsaturated fatty acid methyl ester.
3. The method of claim 2 , wherein the at least one saturated, monounsaturated, or polyunsaturated fatty acid methyl ester is selected from the group consisting of methyl palmitate, methyl laurate, methyl myristate, methyl caprate, methyl linoleate, methyl linolenate, methyl oleate, methyl stearate, methyl arachidate, and methyl behenate, individually or in combinations thereof.
4. The method of claim 3 , wherein the at least one saturated, monounsaturated, or polyunsaturated fatty acid methyl ester comprises methyl palmitate.
5. The method of claim 4 , wherein the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl palmitate are mixed to a desired molar fraction, X OPO , where X ranges from greater than 0 to 1.0.
6. The method of claim 2 , wherein the mixture of the at least one saturated, monounsaturated, or polyunsaturated fatty acid methyl ester and the triacylglycerol exhibit a binary phase behavior comprising one or more eutectics.
7. The method of claim 5 , wherein the mixture of the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl palmitate comprises two DSC cooling end/or heating cycle eutectics at molar fraction 0.45 OPO and 0.80 OPO .
8. The method of claim 5 , wherein the mixture of the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl palmitate has a calculated liquidus line comprising (i) a non-ideality of mixing parameter of between about −62.54 kJ/mol to about 0.68 kJ/mol, (ii) an enthalpy of melting of between about 24 kJ/mol to about 161 kJ/mol, and (iii) a melting temperature of between about 293 K to about 303 K.
9. The method of claim 3 , wherein the at least one saturated, monounsaturated, or polyunsaturated fatty acid methyl ester comprises methyl stearate and wherein the triacylglycerol comprises 1,3-dioleoyl-2-palmitoyl glycerol.
10. The method of claim 9 , wherein the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl stearate are mixed to a desired molar fraction, X OPO , where X ranges from greater than 0 to 1.0.
11. The method of claim 10 , wherein the mixture of the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl stearate comprises a singularity at 0.65 OPO and 0.90 OPO .
12. The method of claim 10 , wherein the mixture of the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl stearate comprises a DSC heating cycle eutectic at molar fraction 0.90 OPO .
13. The method of claim 10 , wherein the mixture of the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl stearate comprises a DSC heating cycle peritectic at molar fraction 0.65.sub.OPO, with a DSC heating cycle peritectic line spanning from molar fraction 0.11 OPO to molar fraction 0.65 OPO .
14. The method of claim 10 , wherein the mixture of the 1,3-dioleoyl-2-palmitoyl glycerol and the methyl stearate has a calculated liquidus line comprising (i) a non-ideality of mixing parameter of between about −97.1 kJ/mol to about −3.5 kJ/mol, (ii) an enthalpy of melting of between about 72.89 kJ/mol to about 195.69 kJ/mol, and (iii) a melting temperature of between about 19° C. to about 38° C.
15. The method of claim 3 , wherein the at least one saturated, monounsaturated, or polyunsaturated fatty acid methyl ester comprises methyl stearate, and wherein the triacylglycerol comprises 2-stearoyl diolein, and wherein the 2-stearoyl diolein and the methyl stearate are mixed to a desired molar fraction, X OSO , where X ranges from greater than 0 to 1.0.
16. The method of claim 15 , wherein when the mixture of the 2-stearoyl diolein and the methyl stearate comprises a molar fraction of 0.0 OSO to 0.65 OSO , and wherein the mixture comprises a crystallization primarily in a triclinic form and a monoclinic form.
17. The method of claim 15 , wherein the mixture of the 2-stearoyl diolein and the methyl stearate has two DSC heating cycle eutectics at molar fraction 0.50 OSO and 0.80 OSO .
18. The method of claim 15 , wherein the mixture of the 2-stearoyl diolein and the methyl stearate has a calculated liquidus line comprising (i) a non-ideality of mixing parameter of between about −49.5 kJ/mol to about −7.0 kJ/mol, (ii) an enthalpy of melting of between about 53.22 kJ/mol to about 76.14 kJ/mol, and (iii) a melting temperature of between about 294 K to about 310 K.