Process of Producing Biochar From Beneficiated Organic-Carbon-Containing Feedstock
A process for making biochar from a processed organic-carbon-containing feedstock is described. The processed feedstock is introduced into a substantially microwave-transparent reaction chamber. A microwave source emits microwaves which are directed through the microwave-transparent wall of the reaction chamber to impinge on the feedstock within the reaction chamber. The microwave source may be rotated relative to the reaction chamber. The feedstock is subjected to microwaves until the desired reaction occurs to produce a solid processed biochar fuel.
1 . A process of making processed biochar, a solid renewable fuel, composition, comprising:
inputting into a system comprising a first and a second subsystem an unprocessed organic-carbon-containing feedstock that includes free water, intercellular water, intracellular water, intracellular water-soluble salts, and at least some plant cells comprising cell walls that include lignin, hemicellulose, and microfibrils within fibrils;
passing unprocessed organic-carbon-containing feedstock through the first sub-system, a beneficiation sub-system process, to result in processed organic-carbon-containing feedstock having a water content of less than 20 wt % and a salt content that is reduced by at least 60 wt % on a dry basis from that of the unprocessed organic-carbon-containing feedstock; and
passing the processed organic-carbon-containing feedstock through the second sub-system, a microwave sub-system process, to result in a solid renewable fuel composition having an energy density of at least 17 MMBTU/ton (20 GJ/MT) a water content of less than 10 wt %, water-soluble salt that is decreased by at least 60 wt % on a dry basis from that of the unprocessed organic-carbon-containing feedstock.
2 . The process of claim 1 , wherein the beneficiation sub-system process and the microwave sub-system process further comprise:
inputting into a beneficiation sub-system reaction chamber unprocessed organic-carbon-containing feedstock comprising free water, intercellular water, intracellular water, intracellular water-soluble salts, and at least some plant cells comprising cell walls that include lignin, hemicellulose, and microfibrils within fibrils;
exposing the feedstock to hot solvent under pressure for a time at conditions specific to the feedstock to make some regions of the cell walls comprising crystallized cellulosic fibrils, lignin, and hemicellulose more able to be penetrable by water-soluble salts without dissolving more than 25 percent of the lignin and hemicellulose;
removing the pressure so as to penetrate the more penetrable regions to create porous feedstock with open pores in the plant cell walls;
pressing the porous feedstock with conditions that include an adjustable compaction pressure versus time profile and compaction time duration, and between pressure plates to create processed organic-carbon-containing feedstock that has a water content of less than 20 wt % and a water-soluble salt content that is decreased by at least 60 wt % on a dry basis from that of unprocessed organic-carbon-containing feedstock;
inputting processed organic-carbon-containing feedstock into a substantially microwave-transparent reaction chamber containing no externally supplied oxygen and within a microwave reflective enclosure;
directing microwaves from a microwave source through walls of the reaction chamber to impinge on the feedstock;
providing relative motion between the microwave-transparent reaction chamber and the microwave source; and
microwaving the feedstock until the feedstock reacts to produce a solid fuel comprising less than 60 wt % on a dry basis of water-soluble salt from that of unprocessed organic-carbon-containing feedstock, a water content of less than 10 wt %, and pores that have a variance in pore size of less than 10 percent.
3 . The process of claim 1 , wherein the beneficiation sub-system process and the microwave sub-system process further comprise:
inputting into a reaction chamber unprocessed organic-carbon-containing feedstock comprising free water, intercellular water, intracellular water, intracellular water-soluble salts, and at least some plant cells comprising cell walls that include lignin, hemicellulose, and microfibrils within fibrils;
exposing the feedstock to hot solvent under pressure for a time at conditions specific to the feedstock to make some regions of the cell walls comprising crystallized cellulosic fibrils, lignin, and hemicellulose more able to be penetrable by water-soluble salts without dissolving more than 25 percent of the lignin and hemicellulose;
removing the pressure so as to penetrate the more penetrable regions to create porous feedstock with open pores in the plant cell walls;
pressing the porous feedstock with conditions that include an adjustable compaction pressure versus time profile and compaction time duration, and between pressure plates less than 20 wt %, a water-soluble salt content that is decreased by at least 60 wt % on a dry basis over that of unprocessed organic-carbon-containing feedstock, and a cost per weight of removing the water and water-soluble salt that is reduced to less than 60% of the cost per weight of similar water removal from known mechanical, known physiochemical, or known thermal processes;
inputting processed organic-carbon-containing feedstock into a substantially microwave-transparent reaction chamber containing no externally supplied oxygen and within a microwave reflective enclosure;
directing microwaves from a microwave source through walls of the reaction chamber to impinge on the feedstock;
providing relative motion between the microwave-transparent reaction chamber and the microwave source; and
microwaving the feedstock until the feedstock reacts to produce a solid fuel comprising a water-soluble salt content that is a decrease of more than 60 wt % on a dry basis from that of unprocessed organic-carbon-containing feedstock and a water content of less than 10 wt %.