Rotary torrefaction reactor
US-9150790-B2 · Oct 6, 2015 · US
US10414994B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10414994-B2 |
| Application number | US-201514861786-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 22, 2015 |
| Priority date | May 3, 2010 |
| Publication date | Sep 17, 2019 |
| Grant date | Sep 17, 2019 |
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A device includes a rotary drum and a fluid conduit. The rotary drum has a horizontal rotation axis and the drum has a sealed inlet end and a sealed outlet end. The drum is configured to receive biomass proximate the inlet end and has a discharge port proximate an outlet end. The fluid conduit is disposed along an inner surface of the drum. The fluid conduit is configured to carry heated fluid and has a coupling external to the drum.
Opening claim text (preview).
The claimed invention is: 1. A method comprising: introducing biomass into an interior of a rotary drum, the rotary drum having a center axis; passing thermal fluid through a first passage of a rotary joint into a conduit disposed on an interior of the rotary drum, the conduit configured to heat the biomass to form torrefied biomass; passing thermal fluid out of the conduit through a second passage of the rotary joint; rotating the rotary drum about the center axis; promoting movement of the biomass in the rotary drum; supporting the conduit within the rotary drum with a plurality of lifting flights that extend circumferentially with respect to the center axis and are spaced from one another along a length of the interior of the rotary drum, wherein each of the plurality of lifting flights includes one or more apertures through which the conduit passes; and discharging the torrefied biomass from an outlet port of the rotary drum. 2. The method of claim 1 wherein introducing includes supplying through an airlock. 3. The method of claim 1 wherein passing thermal fluid includes pumping oil. 4. The method of claim 1 wherein passing thermal fluid includes pumping fluid at a rate in the range of from approximately 100 to 2000 gallons per minute. 5. The method of claim 1 wherein passing thermal fluid includes pumping fluid having a temperature of approximately 350 to 700 degrees Fahrenheit. 6. The method of claim 1 wherein passing thermal fluid includes pumping having a temperature of approximately 600 degrees Fahrenheit. 7. The method of claim 1 wherein discharging includes dropping through an aperture on a wall of the drum. 8. The method of claim 1 , wherein passing thermal fluid includes pumping water. 9. The method of claim 1 , wherein passing thermal fluid includes pumping glycol. 10. A method comprising: introducing biomass into an interior of a rotary drum, the rotary drum having a center axis; passing thermal fluid through a first passage of a rotary joint into a conduit disposed on an interior of the rotary drum, the conduit configured to heat the biomass to form torrefied biomass; passing the thermal fluid through the conduit along a length of the rotary drum including through apertures in a plurality of lifting flights, the plurality of lifting flights extending circumferentially within the interior of the rotary drum with respect to the center axis; passing thermal fluid out of the conduit through a second passage of the rotary joint; rotating the rotary drum about the center axis; promoting movement of the biomass in the rotary drum; and discharging the torrefied biomass from an outlet port of the rotary drum. 11. The method of claim 10 , wherein passing thermal fluid includes pumping water. 12. The method of claim 10 , wherein passing thermal fluid includes pumping glycol. 13. The method of claim 10 , wherein passing thermal fluid includes pumping oil.
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