Process of generating a renewable biofuel from a hydrotreated stream of condensed oxygenates

1. A process for producing a renewable biofuel from liquid bio-oil, the process comprising:

(a) subjecting a liquid bio-oil feedstream containing carbonyl oxygenates to a carbon-carbon bond forming condensation reaction to form C 6 + enriched condensates, wherein the oxygenates are selected from the group consisting of C 3 oxygenates, C 4 oxygenates, C 5 oxygenates and mixtures thereof, and further wherein the C 3 , C 4 and C 5 oxygenates are selected from the group consisting of carboxylic acids, carboxylic acid esters, ketones and aldehydes;

(b) contacting the bio-oil containing condensates of step (a) with hydrogen and hydrotreating the condensates to form a hydrotreated bio-oil comprising C 6 + hydrocarbons; and

(c) fractionating the hydrotreated bio-oil to obtain a C 6 + renewable biofuel,

wherein the condensation reaction in step (a) and the hydrotreating in step (b) occurs in the same reactor.

2. The process of claim 1 , wherein the feedstream containing carbonyl oxygenates originates from an aqueous stream removed from a solids separator.

3. The process of claim 1 , wherein condensation occurs in the presence of a heterogeneous acid catalyst.

4. The process of claim 3 , wherein the heterogeneous acid catalyst is selected from the group consisting of organic sulfonic acids; perfluoroalkylsulfonic acids; zeolites; sulfated transition metal oxides, and perfluorinated ion exchange polymers containing pendant sulfonic acid, carboxylic acid, or sulfonic acid groups; sulfonated copolymers of styrene and divinylbenzene; sulfated silicas, aluminas, titania and/or zirconia; and amorphous SiAl and mixtures thereof.

5. The process of claim 4 , wherein the heterogeneous acid catalyst is selected from the group consisting of ZSM-type zeolites, zeolite beta, sulfonated fluoropolymers or copolymers, sulfated zirconia and amorphous SiAl.

6. The process of claim 3 , wherein the heterogeneous catalyst is a zeolite beta.

7. The process of claim 1 , wherein condensation occurs in the presence of a basic catalyst selected from the group consisting of alkaline oxides, alkaline earth metal oxides, Group IIB oxides and Groups IIIB oxides and mixtures thereof.

8. The process of claim 7 , wherein the basic catalyst is selected from the group consisting of MgO, CaO, SrO, BaO, ZrO 2 , TiO 2 , CeO and mixtures thereof.

9. The process of claim 8 , wherein the basic catalyst is a supported catalyst.

10. The process of claim 1 , wherein the carbon-carbon bond forming condensation reaction is a Diels-Alder reaction.

11. The process of claim 1 , wherein the condensates of step (a) are prepared through a Michael addition reaction.

12. The process of claim 1 , wherein the condensates of step (a) are prepared through a Robinson annulations reaction.

13. The process of claim 1 , wherein the ketones are methyl vinyl ketone and ethyl vinyl ketone.

14. A process for producing a renewable biofuel from biomass, the process comprising:

(a) converting biomass in a biomass conversion reactor into gaseous, liquid and solid components;

(b) separating gaseous components from liquid and solid components;

(c) separating solids from the liquid components in a solids separator and separating the liquid components into an aqueous phase and an organic stream;

(d) fractionating the organic stream into two or more distillates, wherein one of the distillates has the boiling point of naphtha;

(e) feeding into a single reactor an organic phase containing carbonyl-containing oxygenates and condensing and hydrotreating the organic phase in the single reactor to produce a hydrotreated C 6 + enriched stream, wherein the oxygenates are selected from the group consisting of C 3 oxygenates, C 4 oxygenates, C 5 oxygenates and mixtures thereof, and further wherein the C 3 , C 4 and C 5 oxygenates are selected from the group consisting of carboxylic acids, carboxylic acid esters, ketones and aldehydes; and

(f) fractionating the hydrotreated C 6 + enriched stream to obtain a renewable biofuel;

wherein the organic phase fed into the single reactor originates from at least one of the following streams:

(i) the gaseous component from the biomass conversion reactor, wherein the gaseous components are compressed into a liquid stream;

(ii) the distillate having the boiling point of naphtha; or

(iii) the aqueous phase of step (c).

15. The process of claim 14 , wherein condensation occurs in the presence of a heterogeneous acid catalyst.

16. The process of claim 14 , wherein condensation occurs in the presence of a basic catalyst selected from the group consisting of alkaline oxides, alkaline earth metal oxides, Group IIB oxides and Groups IIIB oxides and mixtures thereof.

17. The process of claim 16 , wherein the basic catalyst is selected from the group consisting of MgO, CaO, SrO, BaO, ZrO 2 , TiO 2 , CeO and mixtures thereof.

18. A process for producing a renewable biofuel from biomass, the process comprising:

(a) subjecting a biomass to catalytic thermolysis and separating liquid products and solid products

(b) separating a bio-oil from the liquid product of step (a), wherein the bio-oil contains C 3 oxygenates, C 4 oxygenates, C 5 oxygenates and mixtures thereof, and further wherein the C 3 , C 4 and C 5 oxygenates are selected from the group consisting of carboxylic acids, carboxylic acid esters, ketones and aldehydes;

(c) subjecting the C 3 oxygenates, C 4 oxygenates, C 5 oxygenates and mixtures thereof in the bio-oil to condensation and forming C 6 + enriched condensates;

(d) hydrotreating the bio-oil containing the C 6 + enriched condensates with hydrogen to form a hydrotreated C 6 + enriched stream; and

(e) fractionating the hydrotreated C 6 + enriched stream to obtain a C 6 + renewable biofuel;

wherein the condensation of the C 3 oxygenates, C 4 oxygenates, C 5 oxygenates and mixtures thereof in step (c) and hydrotreating of the C 6 + enriched condensates in step (d) occurs in the same reactor.

19. The process of claim 18 , wherein the amount of C 3 -C 5 oxygenates in the bio-oil subjected to condensation is from about 1 to about 25 weight percent.

20. The process of claim 18 , wherein the oxygen content of the bio-oil subjected to condensation is between from 10 to 50 weight percent.

21. The process of claim 18 , wherein a light fraction having a boiling point between from about 150° F. to about 180° F., an intermediate fraction having a boiling point between from about 180° F. to about 420° F. and a heavy fraction having a boiling point above 420° F. are separated in the fractionator.

22. A process for producing a renewable biofuel which comprises:

(a) subjecting a biomass feedstream to thermolysis in a biomass conversion unit;

(b) separating solids, a first organic stream containing C 3 -C 5 oxygenates and an aqueous stream from an effluent of the biomass conversion unit;

(c) separating water and a second organic stream from the aqueous stream, wherein the second organic stream further contains C 3 -C 5 oxygenates;

(d) fractionating the first organic stream into two or more distillate streams wherein at least one of the distillate streams has the boiling point of naphtha;

(e) introducing at least a portion of the distillate stream having the boiling point of naphtha and the second organic stream into a reactor and condensing C 3 -C 5 oxygenates into a C 6 + enriched stream in the reactor and then hydrotreating the C 6 + enriched stream in the reactor;

(f) recovering the hydrotreated C 6 + enriched stream from the reactor; and

(g) fractionating the hydrotreated C 6 + enriched stream to obtain a renewable biofuel;

wherein the C 3 -C 5 oxygenates are selected from the group consisting of carboxylic acids, carboxylic acid esters, ketones and aldehydes.

23. The process of claim 22 , further comprising:

(i) producing a gaseous stream in the biomass conversion unit;

(ii) compressing the gaseous stream into a liquid stream containing C 3 -C 5 oxygenates; and

(iii) feeding the liquid stream of step (ii) into the reactor.