Cellulosic biomass processing for hydorgen extraction

Abstract

Methods are disclosed for extracting hydrogen from a biomass compound comprising carbon, oxygen, and hydrogen. The biomass may include cellulose, lignin, and/or hemicellulose. Water is combined with the compound to produce a wet form of the compound. The wet form of the compound is transferred into a reaction processing chamber. The wet form of the compound is heated within the reaction chamber such that elements of the compound dissociate and react, with one reaction product comprising hydrogen gas. The hydrogen gas is processed to generate electrical power.

1 - 27 . (canceled) 
     
     
         28 . A method for extracting hydrogen from a compound comprising carbon, hydrogen, and oxygen, the method comprising:
 determining an amount of water to combine with the compound;   combining the determined amount of water with the compound to produce a wet form of the compound;   transferring the wet form of the compound into a reaction processing chamber;   heating the wet form of the compound within the reaction processing chamber such that elements comprised by the wet form of the compound dissociate and react with each other through a hydrous pyrolysis process, wherein one reaction product comprises hydrogen gas; and   extracting the hydrogen gas.   
     
     
         29 . The method recited in  claim 28 , wherein determining the amount of water to combine with the compound comprises:
 determining a weight percent water of the compound; and   determining a remaining mass of water to combine with the compound to form the wet form of the compound, wherein the remaining mass of water depends on the determined weight percent water of the compound.   
     
     
         30 . The method recited in  claim 28 , wherein the hydrous pryolysis process comprises C x H y O z +(2x−z)H 2 O=xCO 2 +(2x+y/2−z)H 2  and wherein (2x-z)H 2 O equals the determined amount of water to combine with the compound and C x H y O z  is the compound comprising carbon, hydrogen, and oxygen with x carbon atoms, y hydrogen atoms, and z oxygen atoms. 
     
     
         31 . The method recited in  claim 28 , wherein the determined amount of water to combine with the compound equals M w −W*M T ;
 W equals a weight percent water of the compound; 
 M w  equals a mass water to add per mass of the compound as dry input mass; and 
 M T  equals a total mass of the compound. 
 
     
     
         32 . The method recited in  claim 28 , wherein the compound consists of carbon, hydrogen, and oxygen. 
     
     
         33 . The method recited in  claim 28 , wherein the compound comprises cellulose. 
     
     
         34 . The method recited in  claim 28 , wherein the compound comprises lignin. 
     
     
         35 . The method recited in  claim 28 , wherein the compound comprises hemicellulose. 
     
     
         36 . The method recited in  claim 28 , further comprising providing a flow of an inert gas to the reaction chamber. 
     
     
         37 . The method recited in  claim 36 , wherein the inert gas comprises at least argon or nitrogen. 
     
     
         38 . The method recited in  claim 28 , wherein the extracted hydrogen gas is processed to produce liquid fuels. 
     
     
         39 . The method recited in  claim 28 , wherein the water comprises liquid water. 
     
     
         40 . The method recited in  claim 28 , wherein extracting the hydrogen gas comprises passing reaction-product gases through a water-cooled chamber to remove unreacted water. 
     
     
         41 . The method recited in  claim 28 , wherein heating the wet form of the compound comprises heating the wet form of the compound to a temperature between 700° C. and 1100° C. 
     
     
         42 . The method recited in  claim 41 , wherein heating the wet form the compound comprises heating the wet form of the compound to a temperature between 1000° C. and 1100° C. 
     
     
         43 . The method of  claim 41 , wherein heating the wet form of the compound occurs under atmospheric pressure conditions. 
     
     
         44 . The method recited in  claim 28 , wherein transferring the wet form of the compound into a reaction processing chamber occurs continuously. 
     
     
         45 . The method recited in  claim 44 , wherein the continuous transfer of the wet form of the compound into the reactor utilizes a geometry that reduces a presence of air. 
     
     
         46 . The method recited in  claim 28 , wherein heating the wet form of the compound within the reaction chamber such that the elements comprised by the wet form of the compound dissociate and react with each other through at least the hydrous pyrolysis reaction occurs without an addition of water within the reaction processing chamber. 
     
     
         47 . The method recited in  claim 28 , further comprising extracting one or more other reaction products besides hydrogen gas.