US2010223839A1PendingUtilityA1

Systems and processes for producing bio-fuels from lignocellulosic materials

Assignee: UNIV WASHINGTON STATEPriority: Mar 4, 2009Filed: Mar 4, 2010Published: Sep 9, 2010
Est. expiryMar 4, 2029(~2.6 yrs left)· nominal 20-yr term from priority
C10J 3/66C01B 2203/0233C10L 9/083C10J 2300/1846C10K 3/006C10B 57/02C01B 3/34C12M 21/12Y02E50/30C10J 2300/1681Y02E50/10C10J 2300/0909C10B 47/44F02C 3/28C10J 2300/165C10J 2300/094C10J 2300/0956C12P 7/06C13K 1/02C12M 43/00C10J 2300/1671C10B 53/02C12M 45/20
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Claims

Abstract

A selective pyrolysis process for the production of bio-oils enriched in pyrolytic sugars and phenols and conversion of these compounds into second generation bio-fuels is disclosed herein. One embodiment of the process comprises pre-treating a biomass with superheated steam or gases in a selected range of temperatures, followed by fast pyrolysis using synthesis gas as a carrier, and a two-step condensation operation. The aqueous phase from the second condenser can then be reformed to produce hydrogen or can be gasified together with the charcoal to produce syngas.

Claims

exact text as granted — not AI-modified
1 . A process for processing a biomass, comprising:
 treating a biomass by heating the biomass at a first temperature;   thermally converting the treated biomass into a product having an oil portion and an aqueous portion via pyrolysis at a second temperature, the first temperature being lower than the second temperature; and   selecting the first temperature based on a correlation between the first temperature and a desired anhydrosugar content in the oil portion of the product.   
     
     
         2 . The process of  claim 1  wherein thermally converting includes using a synthesis gas as a carrier gas in a pyrolysis reactor. 
     
     
         3 . The process of  claim 1 , further comprising producing an oil phase in a first condenser and producing an aqueous phase in a second condenser, the first and second condensers are in a series. 
     
     
         4 . The process of  claim 1 , further comprising separating sugars from phenols in the oil phase via liquid-liquid extraction with a solvent. 
     
     
         5 . The process of  claim 1 , further comprising converting at least a fraction of sugars in the oil phase to ethanol. 
     
     
         6 . The process of  claim 1  wherein the oil phase contains sugars, and wherein the process further comprising converting at least a fraction of the sugars into lipids. 
     
     
         7 . The process of  claim 1  wherein treating a biomass includes treating a biomass by heating the biomass at a first temperature of about 200° C. to about 300° C. 
     
     
         8 . The process of  claim 1  wherein treating a biomass includes treating a biomass by heating the biomass at a first temperature of about 200° C. to about 300° C. for a period of time of about 3 minutes to about 10 hours. 
     
     
         9 . The process of  claim 1  wherein treating a biomass includes treating a biomass by heating the biomass at a first temperature of about 200° C. to about 300° C. for a period of time of about 1 minutes to about 10 hours, and wherein the first temperature is inversely related to the period of time. 
     
     
         10 . A process for processing a biomass, comprising:
 providing a biomass having a first crystallinity;   modifying a structure of cellulose in the biomass to have a second crystallinity higher than the first crystallinity; and   thermally converting the biomass with the increased crystallinity into a pyrolysis product containing anhydrosugar via pyrolysis.   
     
     
         11 . The process of  claim 10  wherein:
 the first crystallinity of the biomass corresponds to a first anhydrosugar content of the pyrolysis product; and   modifying the structure of cellulose includes modifying the structure of cellulose to have a second crystallinity and/or a degree of polymerization corresponding to a second anhydrosugar content higher than the first anhydrosugar content of the pyrolysis product.   
     
     
         12 . The process of  claim 10  wherein:
 the first crystallinity of the biomass corresponds to an anhydrosugar content of the pyrolysis product; and   modifying the structure of cellulose includes enhancing the anhydrosugar content of the pyrolysis product.   
     
     
         13 . The process of  claim 10  wherein modifying the structure of cellulose includes heating the biomass at a first temperature of about 200° C. to about 300° C. 
     
     
         14 . The process of  claim 10  wherein modifying the structure of cellulose includes heating the biomass at a first temperature of about 200° C. to about 300° C. for a period of time of about 1 minute to about 10 hours. 
     
     
         15 . The process of  claim 10  wherein modifying the structure of cellulose includes heating the biomass at a first temperature of about 200° C. to about 300° C. for a period of time of about 3 minutes to about 10 hours, and wherein the first temperature is inversely related to the period of time. 
     
     
         16 . A process for processing a biomass, comprising:
 heating a biomass at a first temperature;   thermally converting the heated biomass into a product via pyrolysis at a second temperature, the first temperature being lower than the second temperature; and   wherein the first temperature is selected to enhance an anhydrosugar content in the product from thermally converting the heated biomass.   
     
     
         17 . The process of  claim 16  wherein the first temperature is selected to be about 200° C. to about 300° C. 
     
     
         18 . The process of  claim 16  wherein the first temperature is selected to be about 200° C. to about 300° C., and wherein a heating period of time is also selected to enhance the anhydrosugar content in the product from thermally converting the heated biomass. 
     
     
         19 . The process of  claim 16  wherein the first temperature is selected to be about 200° C. to about 300° C., and wherein a heating period of time is also selected to enhance the anhydrosugar content in the product from thermally converting the heated biomass, the heating period of time being about 1 minute to about 10 hours. 
     
     
         20 . The process of  claim 16  wherein the first temperature is selected to be about 200° C. to about 300° C., and wherein a heating period of time is also selected to enhance the anhydrosugar content in the product from thermally converting the heated biomass, the heating period of time being about 1 minutes to about 10 hours and inversely related to the first temperature.

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