Fuel composition and method for producing a fuel composition

1. A method for producing a multipurpose fuel composition having a freezing point of 40° C. or below, and a cetane number more than 40, wherein the method comprises:

mixing petroleum derived jet fuel and renewable jet fuel,

wherein the renewable jet fuel has a distillation range from 145° C. to 315° C.,

wherein the petroleum derived jet fuel has a freezing point between 47° C. and −60° C.,

wherein a difference between a freezing point of the renewable jet fuel and the freezing point of the petroleum derived jet fuel is less than 25° C.,

such that the multipurpose fuel composition is usable as diesel fuel and as jet fuel,

wherein the renewable jet fuel has an iso-paraffin content of more than 70 wt-%,

wherein the renewable jet fuel contains at least one of:

more than about 70 wt-% of C15 to C18 paraffins,

less than about 20 wt-% of paraffins smaller than C15 paraffins,

less than about 10 wt-% of paraffins larger than C18 paraffins, and

wherein the renewable jet fuel is a jet fuel produced from biological sources and/or waste fat by means of hydrogenation, hydrodeoxygenation, hydrodesulferization, hydrodenitrification, hydrodemetallization, hydrocracking and/or isomerization;

wherein the composition comprises at least 1 vol-% of renewable jet fuel.

2. A method as claimed in claim 1 , wherein the freezing point of the composition is less than −47° C.

3. A method as claimed in claim 1 , wherein the freezing point of the composition is selected to be −55° C. or below.

4. A method as claimed in claim 1 , comprising:

producing the renewable jet fuel from vegetable oil, animal fat, fish fat, palm oil, rapeseed oil, cooking oil, waste fat from the food industry, biogas, algae oil, jatropha oil, soybean oil, and/or microbial oil.

5. A method as claimed in claim 1 , wherein the multipurpose fuel composition has a cetane number more than 45.

6. A method as claimed in claim 1 , wherein the multipurpose fuel composition has a cetane number more than 50.

7. A method as claimed in claim 1 , wherein the renewable jet fuel distillation range is from 145° C. to 280° C.

8. A method as claimed in claim 1 , wherein the renewable jet fuel distillation range is from 180° C. to 315° C.

9. A method as claimed in claim 1 , wherein the renewable jet fuel iso-paraffin content is more than 80 wt-%.

10. A method as claimed in claim 1 , wherein the renewable jet fuel iso-paraffin content is more than 90 wt-%.

11. A method as claimed in claim 1 , where:

the renewable jet fuel contains at least one of:

more than about 85 wt-% of C15 to C18 paraffins,

less than about 10 wt-% of paraffins smaller than C15, and

less than about 5 wt-% paraffins larger than C18.

12. A method as claimed in claim 1 , where:

the renewable jet fuel contains at least one of:

more than about 90 wt-% of C15 to C18 paraffins,

less than about 7 wt-% of paraffins smaller than C15, and

less than about 3 wt-% paraffins larger than C18.

13. A method as claimed in claim 1 , wherein the freezing point of the composition is selected to be −55.2° C. or below.

14. A method as claimed in claim 1 , wherein the freezing point of the composition is selected to be −55.6° C. or below.

15. A method as claimed in claim 1 , wherein the freezing point of the composition is selected to be −55.9° C. or below.

16. A method as claimed in claim 1 , wherein the freezing point of the composition is selected to be −57.4° C. or below.

17. A method as claimed in claim 1 , wherein the freezing point of the composition is selected to be −58.2° C. or below.

18. A method as claimed in claim 1 , wherein the composition comprises:

at least 5 vol-% renewable jet fuel.

19. A method as claimed in claim 1 , wherein the composition comprises:

at least 10 vol-% renewable jet fuel.

20. A method as claimed in claim 1 , wherein the composition comprises:

at least 15 vol-% renewable jet fuel.

21. A method as claimed in claim 1 , wherein the composition comprises:

at least 50 vol-% renewable jet fuel.