IP Library Granted Patent US 7,867,377
Granted Patent B2
US 7,867,377 · App. 11/614,118 · Granted Jan 11, 2011

Fuel composition

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Quick Facts
Patent No.
US 7,867,377
App. No.
11/614,118
Granted
Jan 11, 2011
Kind
B2
Abstract

A composition having a density at 15° C. of between 820 and 845 kg/m 3 and a cetane number of equal or greater than 40, which composition has been obtained by blending the following components: (a) a cracked gas oil, (b) a mineral derived gas oil other than (a), and (c) a Fischer-Tropsch derived kerosene fraction; and the use of this composition as an automotive gas oil fuel composition.

Claims (80)

1. An automotive gas oil fuel composition comprising:

(a) a quantity of from greater than 15 vol % to 60 vol % of a cracked gas oil exhibiting a density at 15° C. of greater than 845 kg/m 3 ;

(b) a mineral derived gas oil other than (a);

(c) a quantity of a Fischer-Tropsch derived kerosene fraction having paraffin content of between 98 and 100 wt % effective to produce the fuel composition comprising:

(i) a density at 15° C. of between 820 and 845 kg/m 3 ;

(ii) a cetane number of equal to or greater than 40;

(iii) a T95 of between 275 and 360° C.; and

(iv) a cold filter plugging point below +5° C.

2. The fuel composition of claim 1 comprising between 10 and 50 vol % of the Fischer-Tropsch derived kerosene fraction (c).

3. The fuel composition of claim 1 comprising 30 vol. % or more of the cracked gas oil component (a).

4. The fuel composition of claim 1 comprising 40 vol. % or more of the cracked gas oil component (a).

5. The fuel composition of claim 1 comprising 50 vol. % or more of the cracked gas oil component (a).

6. The fuel composition of claim 1 exhibiting a cetane number of above 45.

7. The fuel composition of claim 3 exhibiting cetane number of above 45.

8. The fuel composition of claim 5 exhibiting cetane number of above 45.

9. The fuel composition of claim 1 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

10. The fuel composition of claim 3 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

11. A fuel composition comprising:

(a) from greater than 15 vol. % to 60 vol. % of a cracked gas oil having a density at 15° C. of greater than 845 kg/m 3 and a cetane number of less than 45;

(b) an amount of a mineral derived gas oil other than (a), the mineral derived gas oil having a density at 15° C. of between 820 and 845 kg/m 3 and a cetane number of from 51 to 75, and (c) a quantity of a Fischer-Tropsch derived kerosene fraction having paraffin content of between 98 and 100 wt %, a density at 15° C. of from 730 to 760 kg/m 3 and a cetane number of from 63 to 75, the quantity being sufficient to produce the fuel composition comprising:

(i) a density at 15° C. of between 820 and 845 kg/m 3 ;

(ii) a cetane number of equal or greater than 40

(iii) a T95 of between 275 and 360° C.; and

(iv) a cold filter plugging point below +5° C.

12. The fuel composition of claim 11 comprising 30 vol. % or more of the cracked gas oil component (a).

13. The fuel composition of claim 11 comprising 40 vol. % or more of the cracked gas oil component (a).

14. The fuel composition of claim 11 comprising 50 vol. % or more of the cracked gas oil component (a).

15. The fuel composition of claim 11 wherein the quantity of Fischer-Tropsch derived kerosene fraction is sufficient to produce a cetane number of above 45.

16. The fuel composition of claim 12 wherein the quantity of Fischer-Tropsch derived kerosene fraction is sufficient to produce a cetane number of above 45.

17. The fuel composition of claim 14 wherein the quantity of Fischer-Tropsch derived kerosene fraction is sufficient to produce a cetane number of above 45.

18. The fuel composition of claim 11 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

19. The fuel composition of claim 12 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

20. The fuel composition of claim 13 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

21. A process for increasing the amount of cracked gas oil that can be included in an automotive gas oil fuel composition having a density at 15° C. of between 820 and 845 kg/m 3 , a T95 of between 275 and 360° C., a cold filter plugging point below +5° C., and a cetane number of equal or greater than 40, the process comprising:

blending (a) from greater than 15 vol. % to about 60 vol % cracked gas oil having a density at 15° C. of greater than 845 kg/m 3 and a cetane number of less than 45, with (b) mineral derived gas oil other than the cracked gas oil (a), the mineral derived gas oil having a cetane number of from greater than 45 to about 80, and (c) a quantity of Fischer-Tropsch derived kerosene fraction having a density at 15° C. of from 730 to 760 kg/m 3 and a cetane number of from 63 to 75 and paraffin content of between 98 and 100 wt %;

wherein the quantity of the Fischer-Tropsch derived kerosene fraction is sufficient to produce the fuel composition having a density at 15° C. of between 820 and 845 kg/m 3 and a cetane number of equal or greater than 40.

22. The process of claim 21 comprising blending 30 vol. % or more of the cracked gas oil (a).

23. The process of claim 21 comprising blending 40 vol % or more of the cracked gas oil (a).

24. The process of claim 21 comprising blending 50 vol % or more of the cracked gas oil (a).

25. The process of claim 21 wherein the quantity of the Fischer-Tropsch derived kerosene fraction (c) is sufficient to produce the fuel composition having a cetane number of above 45.

26. The process of claim 22 wherein the quantity of the Fischer-Tropsch derived kerosene fraction (c) is sufficient to produce the fuel composition having a cetane number of above 45.

27. The process of claim 23 wherein the quantity of the Fischer-Tropsch derived kerosene fraction (c) is sufficient to produce the fuel composition having a cetane number of above 45.

28. The process of claim 21 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

29. The process of claim 22 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

30. The process of claim 23 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

31. An automotive gas oil fuel composition comprising:

(a) from greater than 15 vol % to about 60 vol % hydrotreated light cycle oil;

(b) ultra low sulfur diesel fuel; and,

(c) a quantity of a Fischer-Tropsch derived kerosene fraction having paraffin content of between 98 and 100 wt % sufficient to produce the fuel composition having a density at 15° C. of between 820 and 845 kg/m 3 and a cetane number of equal to or greater than 40 and T95 of between 275 and 360° C., a cold filter plugging point below +5° C.

32. The fuel composition of claim 31 comprising 30 vol. % or more of the hydrotreated light cycle oil (a).

33. The fuel composition of claim 31 comprising 40 vol. % or more of the hydrotreated light cycle oil (a).

34. The fuel composition of claim 31 comprising 50 vol. % or more of the hydrotreated light cycle oil (a).

35. The fuel composition of claim 31 wherein the fuel composition has a cetane number of above 45.

36. The fuel composition of claim 32 wherein the fuel composition has a cetane number of above 45.

37. The fuel composition of claim 33 wherein the fuel composition has a cetane number of above 45.

38. The fuel composition of claim 31 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

39. The fuel composition of claim 32 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

40. The fuel composition of claim 33 wherein

operating an automotive vehicle using the fuel composition comprising a refinery kerosene fraction in place of the Fischer-Tropsch derived kerosene fraction produces a first acceleration time; and,

operating the automotive vehicle under the same conditions using the fuel composition comprising the Fischer-Tropsch derived kerosene fraction produces an improved acceleration time.

Assignments (1)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →