Method for wet torrefaction of a biomass

1. A process for wet torrefaction of a wet biomass into a liquid fuel or gas product utilizing a two chamber reactor wherein the two chamber reactor comprises a loading chamber and a reaction chamber containing water, the process comprising:

a) loading the wet biomass into the loading chamber, wherein the loading chamber is designed to be sealed and pressurized and is maintained between about 25° C. and about 180° C. and wherein, the wet biomass is plant material;

b) sealing the loading chamber to maintain wet biomass;

c) prior to introducing the wet biomass into the reaction chamber containing water, increasing temperature to about 275° C., and increasing pressure sufficient to maintain water in liquid state within the reaction chamber so that the reaction temperature is maintained at about 260° C. thereby increasing the energy density of a reacted biomass by at least about 40%;

d) introducing the wet biomass into the reaction chamber containing water such that the desired reaction temperature is maintained at about 260° C. or equilibrates thereto; e) quenching the reaction within the reaction chamber wherein the reacted biomass temperature is lowered below 180° C. so that total time from step d) and e) is for the wet biomass being introduced into the reaction chamber, maintained in the reaction chamber at about 260° C. to the wet biomass being quenched below 180° C. is less than five minutes; wherein being subjected to the reaction condition increases the energy density of the reacted biomass by at least about 40% relative to the wet biomass prior to wet torrefaction; and

f) forming the reacted biomass with an increased energy density of at least 40% into a liquid fuel or gas product.

2. The process of claim 1 further comprising subjecting the wet biomass to the desired reaction condition for an amount of time effective to increase the natural binder concentration of the reacted biomass relative to the biomass prior to reaction.

3. The process of claim 2 wherein the natural binder is lignin or a derivative of lignin.

4. The process of claim 1 wherein the plant material is loblolly pine.

5. The process of claim 4 wherein the wet biomass total time is about 60 seconds.

6. A process for wet torrefaction utilizing a two chamber reactor wherein the two chamber reactor comprises a loading chamber and a reaction chamber containing water, the process comprising:

a) loading a biomass into the loading chamber, wherein the loading chamber is designed to be sealed and pressurized and is maintained between about 25° C. and about 180° C., wherein the biomass is plant material;

b) sealing the loading chamber to minimize pressure loss in the reaction chamber during wet torrefaction;

c) prior to introducing biomass into the reaction chamber containing water, increasing temperature and increasing pressure within the reaction chamber to at or above a desired reaction temperature and a pressure sufficient to maintain water in a liquid state wherein the desired reaction temperature comprises a temperature includes a temperature in a range between about 230° C. and about 260° C. and is sufficient to increase the energy density of a reacted biomass by at least 25%;

d) introducing biomass into the reaction chamber containing water, such that the desired reaction temperature of between about 230° C. and about 260° C. is maintained or equilibrates thereto;

e) subjecting biomass to the desired reaction temperature, wherein the desired reaction temperature includes a temperature in a range between about 230° C. and about 260° C. and compressed water in an inert atmosphere thereby forming a reacted biomass with a water to biomass ratio of between about 5:1 w/w to about 75:1 w/w, and an energy density increased by at least about 25% of the reacted biomass relative to the biomass prior to wet torrefaction; and

f) quenching the reaction occurring in the reaction chamber wherein biomass temperature is lowered below 180° C. so that total time between steps d)-f) is for the biomass being introduced into the reaction chamber, maintained in the reaction chamber between about 230° C. and about 260° C. to the biomass being quenched below 180° C. is less than five minutes and allows energy density of the reacted biomass to be increased by at least about 25% relative to biomass prior to wet torrefaction.

7. The process of claim 6 wherein the temperature of the desired reaction temperature is about 260° C.

8. The process of claim 6 wherein the amount of total time is about 60 seconds.

9. The process of claim 1 wherein the wet biomass is cellulosic.

10. The process of claim 6 wherein the biomass is subjected to the desired reaction temperature for less than two minutes.

11. The process of claim 6 further comprising subjecting the biomass to the desired reaction condition for an amount of time effective to increase the natural binder concentration of the reacted biomass relative to the biomass prior to reaction.

12. The process of claim 6 further comprising forming the reacted biomass into at least one of a solid fuel, a liquid fuel, or a gas product.

13. The process of claim 6 further comprising applying pressure to the reacted biomass in an amount sufficient to form a pellet.

14. The process of claim 1 wherein the plant material comprises cellulose, hemi-cellulose, lignin or a combination thereof.

15. The process of claim 6 wherein the plant material comprises cellulose, hemi-cellulose, lignin or a combination thereof.

16. The process of claim 13 wherein the biomass contains lignin and the reacted biomass has a greater concentration of lignin than prior to treatment and is sufficient to form a pellet from the reacted biomass without addition of exogenous binders.

17. The process of claim 1 , wherein the plant material is rice husks or corn stover.

18. The process of claim 6 , wherein the plant material is loblolly pine.

19. The process of claim 18 , wherein the desired reaction temperature is about 260° C.