Production of renewable biofuels

1. A process for producing a renewable fuel, said process comprising:

(a) providing a bio-oil having an oxygen content of less than 15 weight percent;

(b) separating said bio-oil into at least a light fraction and a heavy fraction, wherein the mid-boiling point of said heavy fraction is at least 100° C. greater than the mid-boiling point of said light fraction;

(c) hydrotreating at least a portion of said heavy fraction to thereby provide a hydrotreated product; and

(d) combining at least a portion of said light fraction and at least a portion of said hydrotreated product with a petroleum-derived gasoline to thereby produce a renewable gasoline, wherein said renewable gasoline comprises said petroleum-derived gasoline in an amount of at least 60 weight percent, said light fraction in an amount of at least 0.1 weight percent, and said hydrotreated product in an amount of at least 0.1 weight percent.

2. The process of claim 1 , wherein said bio-oil has not previously been subjected to hydrotreatment.

3. The process of claim 1 , wherein the oxygen content of said bio-oil is less than 10 weight percent.

4. The process of claim 1 , wherein said separating of step (b) is carried out by distillation.

5. The process of claim 1 , wherein said separating of step (b) is carried out by extraction, membrane separation, partial condensation, and/or non-heated fractionation.

6. The process of claim 1 , wherein at least 75 weight percent of said light fraction boils at a temperature below 205° C., wherein at least 75 weight percent of said heavy fraction boils at a temperature above 205° C.

7. The process of claim 1 , wherein at least 5 weight percent of said bio-oil subjected to said separating of step (b) is separated into said light fraction, wherein at least 10 weight percent of said bio-oil subjected to said separating of step (b) is separated into said heavy fraction.

8. The process of claim 1 , wherein said renewable gasoline comprises said petroleum-derived gasoline in an amount of at least 70 weight percent and at most 99 weight percent; wherein said renewable gasoline comprises said light fraction in an amount of at least 0.1 weight percent and at most 20 weight percent, wherein said renewable gasoline comprises said hydrotreated product in an amount of at least 0.1 weight percent and at most 50 weight percent.

9. The process of claim 1 , further comprising recovering a hydrotreated bio-gasoline fraction from said hydrotreated product, wherein at least 75 weight percent of the hydrotreated bio-gasoline fraction has a boiling point less than 205° C., wherein said hydrotreated bio-gasoline fraction is said portion of said hydrotreated product that is combined with said petroleum-derived gasoline in step (d).

10. The process of claim 1 , further comprising separating said hydrotreated product into a hydrotreated bio-gasoline fraction, a hydrotreated bio-diesel fraction, and a hydrotreated bio-fuel oil fraction, wherein at least 75 weight percent of the hydrotreated bio-gasoline fraction has a boiling point less than 205° C., wherein at least 75 weight percent of the hydrotreated bio-diesel fraction has a boiling point between 205° C. to 325° C., wherein at least 75 weight percent of the hydrotreated bio-fuel oil fraction has a boiling point above 325° C.

11. The process of claim 10 , wherein at least 2 weight percent of said hydrotreated product is separated into said hydrotreated bio-gasoline fraction, wherein at least 5 weight percent of said hydrotreated product is separated into said hydrotreated bio-diesel product, wherein at least 5 weight percent of said hydrotreated product is separated into said hydrotreated bio-fuel oil fraction.

12. The process of claim 10 , wherein said hydrotreated bio-gasoline fraction is said portion of said hydrotreated product that is combined with said petroleum-derived gasoline in step (d), further comprising blending at least a portion of said hydrotreated diesel fraction with a petroleum-derived diesel to thereby produce a renewable diesel, further comprising blending at least a portion of said hydrotreated bio-fuel oil fraction with a petroleum-derived fuel oil to thereby produce a renewable fuel oil.

13. The process of claim 1 , wherein said providing of step (a) includes thermochemically converting biomass in the presence of a catalyst, wherein said bio-oil is not subjected to deoxygenation between said thermochemically converting and said separating of step (b).

14. The process of claim 13 , wherein said thermochemically converting comprises fast pyrolysis carried out in a riser reactor.

15. A process for producing a renewable fuel, said process comprising:

(a) thermochemically converting biomass in the presence of a catalyst to thereby produce bio-oil;

(b) separating said bio-oil into a bio-gasoline fraction and a bio-distillate fraction by heated distillation, wherein at least 75 weight percent of the bio-gasoline fraction has a boiling point below 205° C., wherein at least 75 weight percent of the bio-distillate fraction has a boiling point above 205° C., wherein the mid-boiling point of said bio-distillate fraction is at least 100° C. greater than the mid-boiling point of said bio-gasoline fraction;

(c) hydrotreating and fractionating at least a portion of said bio-distillate fraction to thereby provide separate streams of a hydrotreated bio-gasoline, a hydrotreated bio-diesel, and a hydrotreated bio-fuel oil, wherein at least 75 weight percent of said hydrotreated bio-gasoline has a boiling point less than 205° C., wherein at least 75 weight percent of said hydrotreated bio-diesel has a boiling point between 205° C. to 325° C., wherein at least 75 weight percent of the hydrotreated bio-fuel oil has a boiling point above 325° C.; and

(e) combining at least a portion of said bio-gasoline fraction and at least a portion of said hydrotreated bio-gasoline with a petroleum-derived gasoline to thereby produce a renewable gasoline.

16. The process of claim 15 , wherein the oxygen content of said bio-oil is less than 15 weight percent, wherein said bio-oil is not subjected to hydrotreatment prior to said separating of step (b).

17. The process of claim 15 , wherein said hydrotreating of step (c) is carried out prior to said fractionating of step (c).

18. The process of claim 15 , wherein at least 20 weight percent of said bio-oil subjected to said separating of step (b) is separated into said bio-gasoline fraction, wherein at least 10 weight percent of said bio-oil subjected to said separating of step (b) is separated into said bio-distillate fraction.

19. The process of claim 15 , wherein said renewable gasoline comprises said petroleum-derived gasoline in an amount of at least 60 weight percent and at most 99.5 weight percent, wherein said renewable gasoline comprises a blend component selected from the group consisting of said bio-gasoline, said hydrotreated bio-gasoline fraction, and combinations thereof, in an amount of at least 0.1 weight percent and at most 40 weight percent, wherein said renewable gasoline comprises said hydrotreated bio-gasoline in an amount of at least 0.1 weight percent and at most 40 weight percent.

20. The process of claim 15 , further comprising blending at least a portion of said hydrotreated bio-diesel with a petroleum-derived diesel composition to thereby produce a renewable diesel.

21. The process of claim 15 , wherein said thermochemically converting of step (a) converts lignocellulosic biomass by fast pyrolysis in a riser reactor.