Method for pyrolyzing ligneous biomass
AssigneeGroupe Onym
InventorsYvon NADEAU, MUSTAPHA OUYED
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Abstract
A method for pyrolyzing ligneous biomass includes mechanically grinding ligneous biomass into particles with a size of less than 3 cm3 and conveying the ligneous particles to a dryer. The ligneous particles coming from the dryer is heated in a horizontal-trough pyrolysis reactor having an oxygen level of less than 15%. The reactor includes a first inlet for the ligneous particles and a second inlet for heat-transfer beads. The reactor is configured to make the ligneous particles react so as to have a first output of a mixture of heat-transfer beads and pyrolyzed ligneous particles and a second output of the pyrolysis gas. The residence time in the reactor is at least 20 seconds and the heat-transfer beads are heated in a bead regenerator.
Claims11
1-10. (canceled)
A method for pyrolyzing ligneous biomass, comprising:
- mechanically grinding ligneous biomass into ligneous particles of less than 3 cm3;
- conveying the ligneous particles to a dryer operating at a temperature of at least 80° C., the dryer being configured to have a moisture level of the ligneous particles of less than 10% at an outlet;
- heating the ligneous particles coming from the dryer, in a horizontal-trough pyrolysis reactor having an oxygen level of less than 15%, the horizontal-trough pyrolysis reactor comprising a first inlet for the ligneous particles and a second inlet for heat-transfer beads, the heating is configured to establish a temperature inside the horizontal-trough pyrolysis reactor of between 400° C. and 660° C. and configured to make the ligneous particles react so as to have a first output of a mixture of the heat-transfer beads and pyrolyzed ligneous particles, and a second output of a pyrolysis gas, the residence time in the horizontal-trough pyrolysis reactor is at least 20 seconds;
- heating the heat-transfer beads in a bead regenerator, prior to the heat-transfer beads entering the horizontal-through reactor, at a temperature of between 400° C. and 650° C. for at least 40 seconds, the bead regenerator comprising a main cylinder through which cylindrical tubes pass in which the heat-transfer beads pass.
Dependencies are inferred from the claim text.