IP Library Granted Patent US 12,649,959
Granted Patent B2
US 12,649,959 · App. 17/530,765 · Granted Jun 9, 2026

Biomass pyrolysis integrated with bio-reduction of metal ores, hydrogen production, and/or activated-carbon production

Inventors: James A Mennell (Brighton, UT); Daren Daugaard (Newburg, MO); Dustin Slack (Gwinn, MI)
Assignee: Carbon Technology Holdings, LLC
C22B5/12B01D53/0462B01D53/047B01D53/229C01B3/12C01B3/323C01B3/503C01B3/506C01B3/56C01B32/324C01B32/336C10B53/02C21B13/00F23G5/0273B01D53/02B01D2256/16C01B2203/0233C01B2203/0255C01B2203/0283C01B2203/0405C01B2203/042C01B2203/046C01B2203/06C01B2203/0811F23G2201/302F25J3/0252
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Quick Facts
Patent No.
US 12,649,959
App. No.
17/530,765
Granted
Jun 9, 2026
Kind
B2
Abstract

Improved processes and systems are disclosed for producing renewable hydrogen suitable for reducing metal ores, as well as for producing activated carbon. Some variations provide a process comprising: pyrolyzing biomass to generate a biogenic reagent comprising carbon and a pyrolysis off-gas; converting the pyrolysis off-gas to additional reducing gas and/or heat; reacting at least some of the biogenic reagent with a reactant to generate a reducing gas; and chemically reducing a metal oxide in the presence of the reducing gas. Some variations provide a process for producing renewable hydrogen by biomass pyrolysis to generate a biogenic reagent, conversion of the biogenic reagent to a reducing gas, and separation and recovery of hydrogen from the reducing gas. A reducing-gas composition for reducing a metal oxide is provided, comprising renewable hydrogen according to a hydrogen-isotope analysis. Reacted biogenic reagent may also be recovered as an activated carbon product. Many variations are disclosed.

Claims (26)

1 . A process for producing a metal product, the process comprising:

(a) providing a biomass feedstock;

(b) pyrolyzing the biomass feedstock, thereby generating a biogenic reagent, wherein the biogenic reagent comprises carbon, and a pyrolysis off-gas;

(c) optionally, oxidizing the pyrolysis off-gas, thereby generating heat;

(d) reacting the biogenic reagent with a selected reactant, thereby generating a reducing gas, wherein the reducing gas comprises at least about 10 mol % hydrogen;

(e) chemically reducing a selected metal oxide in the presence of the reducing gas from step (d), wherein the reducing is achieved utilizing the hydrogen, thereby generating a reduced form of the selected metal oxide;

(f) recovering a metal product comprising the reduced form of the selected metal oxide; and

(g) recovering the biogenic reagent continuously or periodically during step (d), or ultimately after step (d), thereby generating a recovered biogenic reagent, wherein the recovered biogenic reagent is an activated carbon,

wherein the process further comprises increasing hydrogen content of the reducing gas via the water-gas shift reaction.

2 . The process of claim 1 , wherein step (e) is conducted at a reduction temperature of at least about 500° C. to at most about 2000° C.

3 . The process of claim 1 , wherein the reduction temperature of at least about 700° C. to at most about 1800° C.

4 . The process of claim 1 , wherein step (e) is conducted for a reduction time of at least about 30 minutes to at most about 48 hours.

5 . The process of claim 1 , wherein the selected metal oxide comprises iron oxide, copper oxide, nickel oxide, magnesium oxide, manganese oxide, aluminum oxide, tin oxide, zinc oxide, cobalt oxide, chromium oxide, tungsten oxide, molybdenum oxide, or a combination thereof.

6 . The process of claim 1 , wherein the selected metal oxide is iron ore.

7 . The process of claim 6 , wherein the iron ore is selected from hematite, magnetite, limonite, taconite, or a combination thereof.

8 . The process of claim 1 , wherein the reduced form of the selected metal oxide is a fully reduced metal.

9 . The process of claim 1 , wherein the reduced form of the selected metal oxide is a second metal oxide having a lower oxidation state than the selected metal oxide.

10 . The process of claim 1 , wherein the selected reactant in step (d) is water.

11 . The process of claim 1 , wherein the selected reactant in step (d) is oxygen, and wherein the oxygen is comprised within air, pure oxygen, enriched oxygen, ozone, or a combination thereof.

12 . The process of claim 1 , wherein the selected reactant in step (d) comprises a combination of water and oxygen.

13 . The process of claim 1 , wherein the reducing gas comprises at least about 25 mol % hydrogen.

14 . The process of claim 1 , wherein the reducing gas comprises at least about 10 mol % carbon monoxide.

15 . The process of claim 1 , wherein the reducing gas comprises at least about 25 mol % carbon monoxide.

16 . The process of claim 1 , wherein the process further comprises partially oxidizing the pyrolysis off-gas, thereby generating a second reducing gas and heat.

17 . The process of claim 16 , wherein step (e) further comprises chemically reducing the selected metal oxide in the presence of the additional reducing gas.

18 . The process of claim 1 , wherein the metal product comprises iron, copper, nickel, magnesium, manganese, aluminum, tin, zinc, cobalt, chromium, tungsten, molybdenum, or a combination thereof.

Assignments (4)
SECURITY INTEREST Recorded Feb 5, 2025
From: CARBON TECHNOLOGY HOLDINGS, LLC
To: ALTER DOMUS (US) LLC
Reel/Frame 070114/0775 →
RELEASE OF SECURITY INTEREST Recorded Feb 4, 2025
From: FORTRESS CREDIT CORP.
To: CARBON TECHNOLOGY HOLDINGS, LLC
Reel/Frame 070608/0239 →
SECURITY INTEREST Recorded Feb 12, 2024
From: CARBON TECHNOLOGY HOLDINGS, LLC
To: FORTRESS CREDIT CORP.
Reel/Frame 066552/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 18, 2022
From: MENNELL, JAMES A.; DAUGAARD, DAREN; SLACK, DUSTIN
To: CARBON TECHNOLOGY HOLDINGS, LLC
Reel/Frame 058674/0528 →
Continuity (3)
Provisional Application 63130460 · Dec 24, 2020
Provisional Application 63116403 · Nov 20, 2020
Related Publication 20220162725A1 · May 26, 2022
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