Biochar aggregate particles
US-2017197192-A1 · Jul 13, 2017 · US
US12103892B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12103892-B2 |
| Application number | US-202217982697-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 8, 2022 |
| Priority date | Nov 12, 2021 |
| Publication date | Oct 1, 2024 |
| Grant date | Oct 1, 2024 |
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In some variations, the disclosure provides a renewable biocarbon composition comprising from 50 wt % to 99 wt % total carbon, wherein the biocarbon composition is characterized by a base-acid ratio selected from 0.1 to 10, an iron-calcium ratio selected from 0.05 to 5, iron-plus-calcium parameter selected from 5 to 50 wt %, a slagging factor selected from 0.001 to 1, and/or a fouling factor or modified fouling factor selected from 0.1 to 10. Some variations provide a process comprising: providing a biomass feedstock; pyrolyzing the biomass feedstock to generate an intermediate biocarbon stream; washing or treating the intermediate biocarbon stream with an acid, a base, a salt, a metal, H 2 , H 2 O, CO, CO 2 , or a combination thereof, and/or introducing an additive in the process, to adjust a base-acid ratio or other compositional parameter; and recovering a biocarbon composition comprising from 50 wt % to 99 wt % total carbon and optimized for a compositional parameter.
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What is claimed is: 1. A process for producing a biocarbon composition with an optimized base-acid ratio, the process comprising: (a) providing a starting feedstock comprising biomass, wherein the starting feedstock is optionally dried; (b) pyrolyzing the starting feedstock to generate an intermediate biocarbon stream and a pyrolysis vapor, wherein the intermediate biocarbon stream is characterized by a base-acid ratio defined by the following formula: Base - Acid Ratio = Fe 2 O 3 + CaO + MgO + K 2 O + Na 2 O SiO 2 + Al 2 O 3 + TiO 2 wherein each of the Fe 2 O 3 , CaO, MgO, K 2 O, Na 2 O, SiO 2 , Al 2 O 3 , and TiO 2 correspond to weight percentages pursuant to ASTM D4326; (c) washing or treating the intermediate biocarbon stream with an acid, a base, a salt, a metal, H 2 , H 2 O, CO, CO 2 , or a combination thereof, to adjust the base-acid ratio; and/or introducing an additive during step (a) or step (b), to adjust the base-acid ratio; and (d) recovering a biocarbon composition comprising from about 50 wt % to about 99 wt % total carbon, wherein the total carbon is at least 50% renewable as determined from a measurement of the 14 C/ 12 C isotopic ratio of the total carbon, and wherein the base-acid ratio of the biocarbon composition is selected from about 0.1 to about 10; wherein step (c) utilizes acidic water that is obtained from step (a), step (b), or another process step that is conducted prior to step (c). 2. The process of claim 1 , wherein the acidic water is obtained from condensation of the pyrolysis vapor to generate a condensed liquid having a pH from about 1 to about 7. 3. A process for producing a biocarbon composition with an optimized base-acid ratio, the process comprising: (a) providing a starting feedstock comprising biomass, wherein the starting feedstock is optionally dried; (b) pyrolyzing the starting feedstock to generate an intermediate biocarbon stream and a pyrolysis vapor, wherein the intermediate biocarbon stream is characterized by a base-acid ratio defined by the following formula: Base - Acid Ratio = Fe 2 O 3 + CaO + MgO + K 2 O + Na 2 O SiO 2 + Al 2 O 3 + TiO 2 wherein each of the Fe 2 O 3 , CaO, MgO, K 2 O, Na 2 O, SiO 2 , Al 2 O 3 , and TiO 2 correspond to weight percentages pursuant to ASTM D4326; (c) washing or treating the intermediate biocarbon stream with an acid, a base, a salt, a metal, H 2 , H 2 O, CO, CO 2 , or a combination thereof, to adjust the base-acid ratio; and/or introducing an additive during step (a) or step (b), to adjust the base-acid ratio; and (d) recovering a biocarbon composition comprising from about 50 wt % to about 99 wt % total carbon, wherein the total carbon is at least 50% renewable as determined from a measurement of the 14 C/ 12 C isotopic ratio of the total carbon, and wherein the base-acid ratio of the biocarbon composition is selected from about 0.1 to about 10; wherein step (c) utilizes alkaline water that is obtained from step (a), step (b), or another process step that is conducted prior to step (c). 4. A process for producing a biocarbon composition with an optimized expanded base-acid ratio, the process comprising: (a) providing a starting feedstock comprising biomass, wherein the starting feedstock is optionally dried; (b) pyrolyzing the starting feedstock to generate an intermediate biocarbon stream and a pyrolysis vapor, wherein the intermediate biocarbon stream is characterized by an expanded base-acid ratio defined by the following formula: Expanded Base - Acid Ratio = Fe 2 O 3 + CaO + MgO + K 2 O +
containing additives · CPC title
of cellulose-containing material (production of pyroligneous acid C10C5/00) · CPC title
Cutting, disintegrating, shredding or grinding · CPC title
Combustion or pyrolysis · CPC title
by heat treatments, e.g. calcining · CPC title
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