C10L9/083

Solid fuel burner-gasifier methods and apparatus
09541285 · 2017-01-10 ·

A system for thermally processing solid fuel to produce pyrolysis gases, syngas, tar, char, and/or torrefied products, which includes a bulk solids pump having a curved passage to move a feedstock therein and wherein the pump includes a spool supported for rotational movement. A sleeve shaped chamber or chambers surround all or a portion of at least an axial extent of said curved passage to permit containment of heated gases to heat solid fuel within the curved passage to thermally process the feedstock within the pump.

Method for providing raw material for an industrial process

A method for providing raw material for an industrial process, in particular for steel production, the method including torrefying a torrefaction material, which contains biomass, in a reactor by thermochemically treating the torrefaction material at 200 C. to 600 C., to obtain bio coal, extracting the bio coal from the reactor at a first temperature of up to 600 C., providing bulk materials at a second temperature between 0 C. and 100 C., mixing bio coal with bulk material, thereby cooling down the bio coal with the bulk material and obtaining a mixture of bulk material and bio coal at a third temperature, below the self-ignition temperature of the mixture, and using the mixture to provide the raw material for the industrial process.

Mobile biomass thermochemical energy conversion unit and related methods

A thermochemical energy conversion unit includes a heat expansion assembly including a reactor configured to receive a biomass and convert the biomass into a burnable gas having undesirable materials therein and a biochar. The heat expansion assembly also includes a heat expansion discharge pipe configured to discharge the burnable gas from the heat expansion assembly. The thermochemical energy conversion unit also includes a gas scrubber assembly operatively connected to the heat expansion assembly and configured to receive the burnable gas therefrom and to remove the undesirable materials from the burnable gas. The gas scrubber assembly includes a scrubber discharge pipe configured to discharge the burnable gas from the gas scrubber assembly. The heat expansion assembly and the gas scrubber assembly are configured to be continuously fluidly connected from the heat expansion discharge pipe to the scrubber discharge pipe for generating a continuous flow of the burnable gas therealong.

MOBILE BIOMASS THERMOCHEMICAL ENERGY CONVERSION UNIT AND RELATED METHODS

A thermochemical energy conversion unit includes a heat expansion assembly including a reactor configured to receive a biomass and convert the biomass into a burnable gas having undesirable materials therein and a biochar. The heat expansion assembly also includes a heat expansion discharge pipe configured to discharge the burnable gas from the heat expansion assembly. The thermochemical energy conversion unit also includes a gas scrubber assembly operatively connected to the heat expansion assembly and configured to receive the burnable gas therefrom and to remove the undesirable materials from the burnable gas. The gas scrubber assembly includes a scrubber discharge pipe configured to discharge the burnable gas from the gas scrubber assembly. The heat expansion assembly and the gas scrubber assembly are configured to be continuously fluidly connected from the heat expansion discharge pipe to the scrubber discharge pipe for generating a continuous flow of the burnable gas therealong.

Torrefaction reactor and process

The invention is directed to a configuration comprising of more than one torrefaction batch reactors. A torrefaction batch reactor of the configuration comprises of a closed housing (2) having a gas inlet (4), a gas outlet (5) and a gas permeable biomass holding structure (6) positioned within the housing (2) defining a biomass holding space (7). The gas inlet (4) and the gas outlet (5) of the torrefaction batch reactor are alternatively fluidly connected to the following gas loops, (i) an air drying gas loop (20), (ii) a torrefaction gas loop (25), and (iii) a cooling gas loop (26). One or more batch reactors of the configuration are fluidly connected to the air drying gas loop (20) and one or more other batch reactors are fluidly connected to the torrefaction gas loop (25).