Fuel compositions
A fuel composition exhibiting a reduced acceleration time, the fuel composition comprising a blend comprising a non-Fischer-Tropsch derived diesel base fuel and from about 0.2 v/v % to 3 v/v % Fischer-Tropsch derived kerosene fuel product, the blend exhibiting a reduced acceleration time that is at least 0.20% less than a theoretical acceleration time.
1. A fuel composition exhibiting a reduced acceleration time, the fuel composition comprising
a blend comprising
(a) a non-Fischer-Tropsch derived diesel base fuel having boiling points within the range of from 150 to 400° C., a density of from 0.75 to 0.9 g/cm 3 at 15° C., and a cetane number of from 35 to 80, and
(b) a quantity of from about 0.2 v/v. % to 3 v/v. % Fischer-Tropsch derived kerosene fuel product exhibiting a distillation range of from 140 to 260° C., a density of from 0.73 to 0.76 g/cm 3 at 15° C., and a cetane number of from 63 to 75;
(c) the blend exhibiting a reduced acceleration time that is at least 0.20% less than a theoretical acceleration time calculated based on the relative densities, calorific values, and relative proportions of the components of the fuel composition, assuming a linear relationship between the relevant property and the theoretical acceleration time.
2. The fuel composition of claim 1 wherein the diesel base fuel is petroleum derived.
3. The fuel composition of claim 1 further comprising from 10 to 17% v/v Fischer-Tropsch derived gas oil having boiling points within the range of from 150 to 400° C., a density of from 0.76 to 0.79 at 15° C., and a cetane number of greater than 70 as a blend component.
4. The fuel composition of claim 3 wherein the concentration of the Fischer-Tropsch derived gas oil is about 15% v/v based on the overall composition.
5. The fuel composition of claim 1 wherein the fuel composition produces one or more additional improvements selected from the group consisting of:
(i) reducing emissions of the internal combustion engine;
(ii) improving cold flow performance of the fuel composition; and/or
(iii) increasing cetane number of the fuel composition.
6. The fuel composition of claim 3 wherein the diesel base fuel is petroleum derived.
7. The fuel composition of claim 4 further comprising from 10 to 17% v/v. Fischer-Tropsch derived gas oil having boiling points within the range of from 150 to 400° C., a density of from 0.76 to 0.79 at 15° C., and a octane number of greater than 70 as a blend component.
8. The fuel composition of claim 7 wherein the concentration of the Fischer-Tropsch derived gas oil is about 15% v/v based on the overall composition.
9. The fuel composition of claim 1 comprising 2 v/v % or more of the Fischer-Tropsch derived kerosene fuel product.
10. The fuel composition of claim 3 wherein using the fuel composition produces one or more additional improvements selected from the group consisting of:
(i) reducing emissions of the internal combustion engine;
(ii) improving cold flow performance of the fuel composition; and/or
(iii) increasing cetane number of the fuel composition.
11. A fuel composition exhibiting a reduced acceleration time, the fuel composition comprising a blend comprising
(a) non-Fischer-Tropsch derived diesel base fuel having boiling points within the range of from 150 to 400° C., a density of from 0.75 to 0.9 g/cm 3 at 15° C., and a cetane number of from 35 to 80; and
(b) from about 1 v/v. % to about 3 v/v. % Fischer-Tropsch derived kerosene fuel product exhibiting a distillation range of from 140 to 260° C., a density of from 0.73 to 0.76 g/cm 3 at 15° C., and a cetane number of from 63 to 75;
(c) the blend exhibiting a reduced acceleration time that is at least 0.20% less than a theoretical acceleration time calculated based on the relative densities, calorific values, and relative proportions of the components of the fuel composition assuming a linear relationship between the relevant property and the theoretical acceleration time.
12. The fuel composition of claim 11 wherein the diesel base fuel is petroleum derived.
13. The fuel composition of claim 11 further comprising from 10 to 17% v/v of Fischer-Tropsch derived gas oil having boiling points within the range of from 150 to 400° C., a density of from 0.76 to 0.79 at 15° C., and a cetane number of greater than 70 as a blend component.
14. The fuel composition of claim 4 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 250° C.
15. The fuel composition of claim 4 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 210° C. and a cetane number of from 65 to 69.
16. The fuel composition of claim 11 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 250° C.
17. The fuel composition of claim 11 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 210° C. and a cetane number of from 65 to 69.
18. The fuel composition of claim 1 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 250° C.
19. The fuel composition of claim 1 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 210° C. and a cetane number of from 65 to 69.
20. The fuel composition of claim 3 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 250° C.
21. The fuel composition of claim 3 wherein the Fischer-Tropsch derived kerosene product exhibits a distillation range of from 150 to 210° C. and a cetane number of from 65 to 69.