US2003000822A1PendingUtilityA1

Method for thermal transformation of biomass

Priority: Jan 12, 2000Filed: Dec 29, 2000Published: Jan 2, 2003
Est. expiryJan 12, 2020(expired)· nominal 20-yr term from priority
C10B 53/02C10B 53/00Y02E50/10C10G 1/02C10G 1/06F23G 2209/26C01B 32/336F23G 2201/40C10B 49/02
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Claims

Abstract

In the method for thermal biomass processing, comprising charging the material in a converter, pyrolyzing said material at a temperature ranging between 650 and 950° C. in the medium of a reducing gas, feeding of steam after the pyrolysis reaction has been completed, and isolating the resultant solid residue, reducing gas is prepared by combusting a hydrocarbon fuel at an air consumption factor α ranging from 0.85 to 1.1, and by mixing the resultant combustion products together with the biomass pyrolysis gases, the ratio between said gases and said combustion products being (1-3):1. The proposed method for biomass processing makes possible using a biomass as a pollution-free fuel, as well as for simultaneously producing activated charcoal having high specific surface area ranging from 280 to 500 ml/100 g.

Claims

exact text as granted — not AI-modified
1 . A method for thermal biomass processing, comprising charging the material in a converter, pyrolyzing said material at a temperature ranging between 650 and 950° C. in the medium of a reducing gas, feeding of steam after the pyrolysis reaction has been completed, and isolating the resultant solid residue, CHARACTERIZED in that said reducing gas is prepared by combusting a hydrocarbon fuel at an air consumption factor a ranging from 0.85 to 1.1, and by mixing the resultant combustion products together with the biomass pyrolysis gases, the ratio between said gases and said combustion products being (1-3):1.  
     
     
         2 . The method of  claim 1 , CHARACTERIZED in that saturated steam is fed at a temperature ranging from 105 and 140° C., and a weight percentage ratio between said saturated steam and the material being processed is equal to (0.1-0.25):1.

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