High-carbon biogenic reagents and uses thereof

Patent metadata

Field	Value
Publication number	US-12570912-B2
Application number	US-202117357702-A
Country	US
Kind code	B2
Filing date	Jun 24, 2021
Priority date	Apr 15, 2011
Publication date	Mar 10, 2026
Grant date	Mar 10, 2026

Abstract

This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu/lb, 13,000 Btu/lb, 14,000 Btu/lb, or 14,500 Btu/lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and/or strength that derive from the feedstock, heat rate, and additives.

First claim

We claim:

1 . A biogenic syngas-generating feedstock comprising, on a dry basis:
at least about 75 wt % total carbon; at most about 5 wt % hydrogen; at most about 1 wt % nitrogen; at least about 1 wt % and at most about 10 wt % oxygen; at most about 0.5 wt % phosphorus; at most about 0.2 wt % sulfur; and an additive selected from a metal, a metal oxide, a metal hydroxide, a metal halide, or a combination thereof; wherein the biogenic syngas-generating feedstock comprises a biochar, wherein the biochar is a product of pyrolysis.

2 . The biogenic syngas-generating feedstock of claim 1 , wherein the additive is selected from magnesium, manganese, aluminum, nickel, chromium, silicon, boron, cerium, molybdenum, phosphorus, tungsten, vanadium, iron halide, iron chloride, iron bromide, magnesium oxide, dolomite, dolomitic lime, fluorite, fluorospar, bentonite, calcium oxide, lime, or a combination thereof.

3 . The biogenic syngas-generating feedstock of claim 1 , wherein the biogenic syngas-generating feedstock is substantially free of fossil fuel.

4 . The biogenic syngas-generating feedstock of claim 1 , wherein the total carbon consists essentially of biogenic carbon.

5 . A biogenic syngas-generating feedstock comprising, on a dry basis:
at least about 75 wt % total carbon; at most about 5 wt % hydrogen; at most about 1 wt % nitrogen; at least about 1 wt % and at most about 10 wt % oxygen; at most about 0.5 wt % phosphorus; at most about 0.2 wt % sulfur; and an additive selected from an acid or a salt thereof, or a base or a salt thereof; wherein the biogenic syngas-generating feedstock comprises a biochar, wherein the biochar is a product of pyrolysis.

6 . The biogenic syngas-generating feedstock of claim 5 , wherein the additive is selected from sodium hydroxide, potassium hydroxide, magnesium oxide, hydrogen bromide, hydrogen chloride, sodium silicate, potassium permanganate, or a combination thereof.

7 . The biogenic syngas-generating feedstock of claim 5 , wherein the total carbon consists essentially of biogenic carbon.

8 . A process for producing direct-reduced iron from direct reduction of iron ore, the process comprising:
converting a biogenic syngas-generating feedstock into a gas stream, wherein the gas stream comprises CO; reducing iron ore, wherein the reducing is achieved using a reducing gas, wherein the reducing gas is syngas, and wherein the syngas comprises the CO; and wherein the biogenic syngas-generating feedstock comprises:
at least about 75 wt % total carbon;
at most about 5 wt % hydrogen;
at most about 1 wt % nitrogen;
at least about 1 wt % and at most about 10 wt % oxygen;
at most about 0.5 wt % phosphorus;
at most about 0.2 wt % sulfur; and
an additive selected from a metal, a metal oxide, a metal hydroxide, a metal halide, or a combination thereof; wherein the biogenic syngas-generating feedstock comprises a biochar, wherein the biochar is a product of pyrolysis.

9 . A process for producing direct-reduced iron from direct reduction of iron ore, the process comprising:
converting a biogenic syngas-generating feedstock into a gas stream, wherein the gas stream comprises CO; reducing iron ore, wherein the reducing is achieved using a reducing gas, wherein the reducing gas is syngas, and wherein the syngas comprises the CO; and wherein the biogenic syngas-generating feedstock comprises:
at least about 75 wt % total carbon;
at most about 5 wt % hydrogen;
at most about 1 wt % nitrogen;
at least about 1 wt % and at most about 10 wt % oxygen;
at most about 0.5 wt % phosphorus;
at most about 0.2 wt % sulfur; and
an additive selected from an acid or a salt thereof, or a base or a salt thereof; wherein the biogenic syngas-generating feedstock comprises a biochar, wherein the biochar is a product of pyrolysis.

10 . A biogenic syngas-generating feedstock consisting essentially of, on a dry basis, carbon, hydrogen, oxygen, nitrogen, phosphorus, sulfur, non-combustible matter, and an additive selected from the group consisting of magnesium, manganese, aluminum, nickel, chromium, silicon, boron, cerium, molybdenum, phosphorus, tungsten, vanadium, iron halide, iron chloride, iron bromide, magnesium oxide, dolomite, dolomitic lime, fluorite, fluorospar, bentonite, calcium oxide, lime, and combinations thereof;
wherein the biogenic syngas-generating feedstock comprises at least about 75 wt % total carbon on a dry basis; wherein the biogenic syngas-generating feedstock comprises a biochar, wherein the biochar is a product of pyrolysis.

11 . A biogenic syngas-generating feedstock consisting essentially of, on a dry basis, carbon, hydrogen, nitrogen, phosphorus, sulfur, non-combustible matter, and an additive selected from the group consisting of sodium hydroxide, potassium hydroxide, magnesium oxide, hydrogen bromide, hydrogen chloride, sodium silicate, potassium permanganate, and combinations thereof;
wherein the biogenic syngas-generating feedstock comprises at least about 75 wt % total carbon on a dry basis; wherein the biogenic syngas-generating feedstock comprises a biochar, wherein the biochar is a product of pyrolysis.

Assignees

• Carbon Tech Holdings Llc

Inventors

• Despen Daniel J
• Mennell James A
• Filips Steve

Classifications

• C01B32/312

  Preparation · CPC title

• C01B32/318

  characterised by the starting materials · CPC title

• C21C5/52

  Manufacture of steel in electric furnaces {(C21C5/005 takes precedence)} · CPC title

• C10L5/442

  Wood or forestry waste · CPC title

• C10L5/36

  Shape · CPC title