US2015159105A1PendingUtilityA1

Method of drying biomass

Assignee: SETHI VIJAYPriority: Apr 20, 2010Filed: Feb 17, 2015Published: Jun 11, 2015
Est. expiryApr 20, 2030(~3.7 yrs left)· nominal 20-yr term from priority
Y02P20/145C10L 2290/145Y02E50/30Y02E50/10C10B 53/02C10B 49/10C10L 2290/52C10L 2290/06C10L 2290/10C10L 5/44C10L 5/363C10L 2290/30F26B 3/084C10L 9/083C10L 5/447F26B 2200/02C10L 5/361C10L 2290/50C10L 2290/08C10L 5/30C10L 5/445C10L 2200/0469C10L 5/40C10L 5/442
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Claims

Abstract

A process for torrefaction of biomass is provided in which biomass are passed into a fluidized bed reactor and heated to a predetermined temperature in an oxidizing environment. The dried biomass is then fed to a cooler where the temperature of the product is reduced to approximately 100 degrees Fahrenheit.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A process for drying a biomass, comprising:
 directing said biomass to a fluidized bed reactor;   heating said biomass in said fluidized bed reactor with a first heat source, which provides heat energy into said fluidized bed reactor, to a temperature sufficient to evaporate water and convert a portion of said biomass to vaporized organic compounds, such that a dry biomass is produced that contains less than about 10 wt % moisture; and   further heating said biomass with said first heat source and with a second heat source that is associated with a combustion of said vaporized organic compounds, heat from said first heat source and said second heat source each intermingling to directly provide heat energy to said biomass.   
     
     
         2 . The process of  claim 1 , further comprising adding air to said fluidized bed reactor to adjust an oxygen content of the first heat source and the second heat source within said fluidized bed reactor. 
     
     
         3 . The process of  claim 1 , wherein said biomass is combined with a coal, and wherein the coal and biomass are directed to said fluidized bed reactor. 
     
     
         4 . The process of  claim 1 , wherein said fluidized bed reactor has an aspect ratio is no greater than about 2. 
     
     
         5 . The process of  claim 1 , further comprising directing heated air to said fluidized bed reactor with a startup heater. 
     
     
         6 . The process of  claim 1 , wherein said temperature does not initiate a torrefaction reaction. 
     
     
         7 . The process of  claim 1 , wherein dried biomass is cooled in a mixer or a hollow flight screw cooler. 
     
     
         8 . The process of  claim 1 , wherein dried biomass is consolidated into pellets or briquettes before cooling.

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