System and method for preparation of solid biomass by torrefaction

• US 8,276,289 B2
• Filed: 03/25/2010
• Issued: 10/02/2012
• Est. Priority Date: 03/27/2009
• Status: Expired due to Fees

• Current Assignee: Terra Green Energy LLC
• Original Assignee: Terra Green Energy LLC
• Inventors: Causer, Thomas P.
• Primary Examiner(s): GRAVINI, STEPHEN MICHAEL
• Application Number:
  US12/731,253
• Publication Number:
  US 20100242351A1
• Time in Patent Office: 922 Days
• Field of Search: 343/80, 343/81, 344/13, 344/97, 345/24, 34/90, 341/38, 342/10, 423/445.R, 202/95, 202/117, 446/05, 446/06
• US Class Current: 34/90
• CPC Class Codes: C10B 49/02 with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
• CPC Class Codes: C10B 53/02 of cellulose-containing material production of pyroligneous acid C10C5/00
• CPC Class Codes: C10B 57/14 Features of low-temperature carbonising processes
• CPC Class Codes: C10L 5/44 on vegetable substances
• CPC Class Codes: C10L 9/083 Torrefaction
• CPC Class Codes: F23G 5/027 pyrolising or gasifying stage pyrolisation of sludge C02F11/00; destructive distillation of carbonaceous materials C10B53/00
• CPC Class Codes: F23G 5/04 drying
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

Methods and systems for preparing a torrefied biomass fuel are disclosed. Moisture is initially extracted from relatively wet biomass fuel to produce a relatively dry biomass fuel. Remaining moisture is then extracted from the relatively dry biomass fuel in a final drying stage, using steam at a temperature of about 900° F. The resulting dried biomass fuel is conveyed downward using gravity and undergoes torrefaction, which produces torrefied biomass fuel and torrefaction gases. A gaseous mixture of steam and torrefaction gases is vented to a heat exchanger, where the gaseous mixture is heated by a flue gas, and the heated gaseous mixture is used to support the extraction of the remaining moisture in the final drying stage and to support the torrefaction of the dried biomass fuel. Embodiments disclosed herein efficiently use available energy resources to the benefit of manufacturers, consumers, and the environment.

Claims

1. A torrefaction system comprising:

a dryer configured to dry a relatively wet biomass fuel and provide a relatively dry biomass fuel;

a torrefaction reactor comprising;

an upper chamber configured to remove all moisture from the relatively dry biomass fuel in an environment containing steam, and

a lower chamber configured to torrefy dried biomass produced by the upper chamber at a temperature between about 250°

C.-300°

C. (482°

F.-572°

F.);

a combustion unit configured to combust a portion of a gaseous mixture of steam and torrefaction gases vented by the torrefaction reactor to produce a flue gas; and

a heat exchanger configured to exchange heat from the flue gas to the gaseous mixture to provide a heated gaseous mixture for provision to the torrefaction reactor.

2. The torrefaction system of claim 1, wherein the torrefaction reactor further includes a segregation barrier configured to maintain different thermal profiles in the upper chamber and the lower chamber.

3. The torrefaction system of claim 2, wherein the segregation barrier is further configured to enable co-current flow of gases from the upper chamber of the torrefaction reactor to the lower chamber.

4. The torrefaction system of claim 1, wherein the torrefaction reactor further comprises entry ports coupled to a damper system, the damper system configured to supply and maintain a gas mixture temperature in the upper chamber with the temperature in the lower chamber between about 250°

C.-300°

C. (482°

F.-572°

F.).

5. The torrefaction system of claim 1, wherein the combustion unit comprises:

an upper chamber configured to combust the gaseous mixture and a supplemental fuel to produce the flue gas; and

a lower chamber configured to combust a portion of the relatively wet biomass fuel to support production of the flue gas in the upper chamber.

6. The torrefaction system of claim 1, wherein the dryer is a triple pass rotary drum dryer.

7. The torrefaction system of claim 6, wherein the dryer is configured to remove about 80% of the moisture from the relatively wet biomass fuel.