Gasoline fuel

1. A method for operating an automotive vehicle having a spark-induced, internal combustion engine and a catalytic converter to yield a reduced amount of NOx, CO, or unburned hydrocarbons as compared to combusting fuel A/O AVE in said engine, the method comprising:

(1) introducing into the engine an unleaded gasoline, suitable for combustion in an automotive engine, having a Reid Vapor Pressure less than 7.5 psi, an octane value of at least 87, a 10% D-86 distillation point no greater than 158.degree. F. a 50% D-86 distillation point no greater than 210.degree. F. and an olefin content less than 10 volume percent; and thereafter

(2) combusting the unleaded gasoline in said engine;

(3) introducing at least some of the resultant engine exhaust emissions into the catalytic converter; and

(4) discharging emissions from the catalytic converter to the atmosphere.

2. A method for aiding in minimizing air pollution caused at least in part by exhaust emissions from gasoline-powered automobiles equipped with catalytic converters and operating within a geographical area defined by a city and its contiguous area populated by at least 500,000 persons, the geographical area also encompassing a plurality of automotive gasoline service stations,

the operation of said automobiles contributing to air pollution in said geographical area,

the method, performed by a gasoline supplier delivering at least 100,000 gallons per day of unleaded gasoline as defined below for automotive combustion in the geographical area during a one week time period, comprising:

delivering to at least 25% of the automotive gasoline service stations supplied by said supplier in said geographical area during said one week time period unleaded gasoline yielding, upon combustion, a reduced amount of NOx, CO, and unburned hydrocarbons as compared to Fuel A/O AVE, said unleaded gasoline being suitable for combustion in an automotive engine and having a Reid Vapor Pressure less than 7.5 psi, an octane value of at least 87, a 10% D-86 distillation point no greater than 158.degree. F., a 50% D-86 distillation point no greater than 210.degree. F., and an olefin content less than 10 volume percent.

3. A method for aiding in minimizing air pollution caused at least in part by exhaust emissions from gasoline-powered automobiles equipped with catalytic converters and operating within a contiguous geographical area having significant air pollution, the geographical area also encompassing a plurality of automotive gasoline service stations,

the operation of said automobiles contributing to air pollution in said geographical area,

the method, performed by a gasoline supplier delivering at least 100,000 gallons per day of unleaded gasoline as defined below for automotive combustion in the geographical area during a one week time period, comprising:

delivering to at least 25% of the automotive gasoline service stations supplied by said supplier in said geographical area during said one week time period unleaded gasoline yielding, upon combustion, a reduced amount of NOx, CO, and unburned hydrocarbons as compared to Fuel A/O AVE, said unleaded gasoline being suitable for combustion in an automotive engine and having a Reid Vapor Pressure less than 7.5 psi, an octane value of at least 87, a 10% D-86 distillation point no greater than 158.degree. F., a 50% D-86 distillation point no greater than 210.degree. F., and an olefin content less than 10 volume percent.

4. A method comprising

(1) supplying unleaded gasoline to a fuel tank of an automobile equipped with an engine and a catalytic converter, said unleaded gasoline yielding, upon combustion, reduced emissions of NOx, CO, or unburned hydrocarbons in comparison to fuel A/O AVE, said unleaded gasoline further being suitable for combustion in an automotive engine and having a Reid Vapor Pressure less than 7.5 psi, an octane value of at least 87, a 10% D-86 distillation point no greater than 158.degree. F., a 50% D-86 distillation point no greater than 210.degree. F., and an olefin content less than 10 volume percent;

(2) combusting in said engine fuel drawn from said fuel tank; and

(3) passing exhaust gases from said engine through said catalytic converter and thence to the atmosphere.

5. A method as defined in claim 4 wherein said unleaded gasoline has a 90% D-86 distillation point no greater than 315.degree. F.

6. A method as defined in claim 5 wherein said unleaded gasoline has an olefin content less than 8 volume percent.

7. A method as defined in claim 6 wherein said unleaded gasoline has a 50% D-86 distillation point less than 195.degree. F.

8. A method as defined in claim 6 wherein said unleaded gasoline has a 50% D-86 distillation point less than 198.degree. F.

9. A method as defined in claim 6 wherein said unleaded gasoline has a 30% D-86 distillation point less than 200.degree. F.

10. A method as defined in claim 6 wherein said unleaded gasoline has a 50% D-86 distillation point less than 203.degree. F.

11. A method as defined in claim 10 wherein said unleaded gasoline has a 90% D-86 distillation point less than 300.degree. F.

12. A method as defined in claim 6 wherein said unleaded gasoline has a 50% D-86 distillation point no greater than 205.degree. F.

13. A method as defined in claim 6 wherein said unleaded gasoline has a 50% D-86 distillation point less than 208.degree. F.

14. A method as defined in claim 10 wherein said unleaded gasoline has a 90% D-86 distillation point less than 300.degree. F.

15. A method as defined in claim 4 wherein said unleaded gasoline has an olefin content less than 6 volume percent.

16. A method as defined in claim 15 wherein said unleaded gasoline has a 90% D-86 distillation point no greater than 315.degree. F.

17. A method as defined in claim 15 wherein said unleaded gasoline has a 50% D-86 distillation point less than 195.degree. F.

18. A method as defined in claim 17 wherein said unleaded gasoline has a 90% D-86 distillation point less than 300.degree. F.

19. A method as defined in claim 15 wherein said unleaded gasoline has a 50% D-86 distillation point less than 198.degree. F.

20. A method as defined in claim 19 wherein said unleaded gasoline has a 90% D-86 distillation point no greater than 315.degree. F.

21. A method as defined in claim 15 wherein said unleaded gasoline has a 50% D-86 distillation point less than 200.degree. F.

22. A method as defined in claim 21 wherein said unleaded gasoline has a 90% D-86 distillation point less than 300.degree. F.

23. A method as defined in claim 15 wherein said unleaded gasoline has a 50% D-86 distillation point less than 203.degree. F.

24. A method as defined in claim 23 wherein said unleaded gasoline has a 90% D-86 distillation point no greater than 315.degree. F.

25. A method as defined in claim 23 wherein said unleaded gasoline has a 90% D-86 distillation point less than 300.degree. F.

26. A method as defined in claim 15 wherein said unleaded gasoline has a 50% D-86 distillation point no greater than 205.degree. F.

27. A method as defined in claim 26 wherein said unleaded gasoline has a 90% D-86 distillation point no greater than 315.degree. F.

28. A method as defined in claim 15 wherein said unleaded gasoline has a 50% D-86 distillation point less than 208.degree. F.

29. A method as defined in claim 28 wherein said unleaded gasoline has a 90% D-86 distillation point no greater than 315.degree. F.

30. A method as defined in claim 1, 3, 4, 5, or 29 wherein said unleaded gasoline has a 50% D-86 distillation point less than 200.degree. F.

31. A method as defined in claim 1, 3, 4, 5 or 29 wherein said unleaded gasoline has a 50% D-86 distillation point less than 195.degree. F.

32. A method as defined in claim 1, 4, 5, 7, 9, 11, 12, 15, or 29 wherein the octane value of the unleaded gasoline is at least 92.

33. A method as defined in claim 32 wherein the Reid Vapor Pressure of the unleaded gasoline is less than 7.0 psi.

34. A method as defined in claim 3, 4, 6, 14, 17, 20, 21, 25, 26, or 29 wherein the paraffin content of the unleaded gasoline is greater than 70 volume percent.

35. A method as defined in claim 34 wherein the Reid Vapor Pressure of the unleaded gasoline is ,less than 7.0 psi.

36. A method as defined in claim 35 wherein the octane value of the unleadeded gasoline is at least 92.

37. A method as defined in claim 36 wherein the 10% D-86 distillation point of the unleaded gasoline is no more than 135.degree. F.

38. A method as defined in claim 28 wherein said unleaded gasoline has a 90% D-86 distillation point less than 300.degree. F.

39. A method as defined in claim 1, 2, 3, 4, 5, or 29 wherein said unleaded gasoline has a 50% D-86 distillation point no greater than 205.degree. F.

40. A method as defined in claim 1, 4, 6, 10, 13, 18, 22, 27, or 38 wherein the 10% D-86 distillation point of the unleaded gasoline is less than 140.degree. F.

41. A method as defined in claim 40 wherein the octane value of the unleaded gasoline is at least 92.

42. A method as defined in claim 1, 2, 3, 4, 5, 10, 16, 18, 20, 21, 27, or 38 wherein the Reid Vapor Pressure of the unleaded gasoline is less than 7.0 psi.

43. A method as defined in claim 42 wherein the 10% D-86 distillation point of the unleaded gasoline is no more than 135.degree. F.

44. A method as defined in claim 43 wherein the octane value of the unleaded gasoline is at least 92.

45. A method as defined in claim 2, 3, 4, 7, 11, 15, 21, 27, or 38 wherein the paraffin content of the unleaded gasoline is greater than 65 volume percent.

46. A method as defined in claim 45 wherein the octane value of the unleaded gasoline is at least 92.

47. A method as defined in claim 45 wherein the Reid Vapor Pressure of the unleaded gasoline is less than 7.0 psi.

48. A method as defined in claim 47 wherein the 10% D-86 distillation point of the unleaded gasoline is less than 140.degree. F.

49. A method as defined in claim 48 wherein the octane value of the unleaded gasoline is at least 92.

50. A method as defined in claim 3, 4, 5, 13, 15, 18, 22, 26, or 38 wherein the paraffin content of the unleaded gasoline is greater than 72 volume percent.

51. A method as defined in claim 50 wherein the octane value of the unleaded gasoline is at least 92.

52. A method as defined in claim 50 wherein the 10% D-86 distillation point of the unleaded gasoline is less than 140.degree. F.

53. A method as defined in claim 50 wherein the Reid Vapor Pressure of the unleaded gasoline is less than 7.0 psi.

54. A method as defined in claim 53 wherein the 10% D-86 distillation point of the unleaded gasoline is no more than 135.degree. F.

55. A method as defined in claim 3, 4, 12, 15, 16, 18, 24, or 38 wherein the paraffin content of the unleaded gasoline is greater than 75 volume percent.

56. A method as defined in claim 55 wherein the Reid Vapor Pressure of the unleaded gasoline is less than 7.0 psi.

57. A method as defined in claim 56 wherein the octane value of the unleaded gasoline is at least 92.

58. A method as defined in ciaim 57 wherein the 10% D-86 distillation point of the unleaded gasoline is no more than 135.degree. F.