Systems and methods for improved carbon capture associated with molten metal production

Patent metadata

Field	Value
Publication number	US-12258640-B2
Application number	US-202418421103-A
Country	US
Kind code	B2
Filing date	Jan 24, 2024
Priority date	Jan 25, 2023
Publication date	Mar 25, 2025
Grant date	Mar 25, 2025

Abstract

The present disclosure relates to systems and methods for the production of molten metals direct oxidative combustion of one or more solid fuels. The systems and methods may be combined with coal gasifiers and related components for reducing overall energy requirements as well as external fuel sources, e.g., through the use of endogenously-generated hydrogen. In beneficial aspects, components of the carbonaceous exhaust produced in accordance with the disclosed systems and methods, such as carbon dioxide (CO2), may be isolated using carbon capture and sequestration (CCS) for reducing associated greenhouse gas emissions.

First claim

The invention claimed is:

1. A method for molten metal production comprising:
combusting a fuel in the presence of a metal ore and a reducing gas in a reactor for producing at least a molten metal product and a top gas including carbon dioxide (CO 2 ) and a combustible component;
passing at least a portion of the top gas to a combustor arranged downstream of the reactor so that the top gas is combusted with an oxidant in the combustor to provide a combustion product stream;
passing at least a portion of the combustion product stream through one or more heat exchangers arranged downstream of the combustor to remove heat therefrom and to provide a cooled combustion product stream;
passing the cooled combustion product stream to one or more processing components arranged downstream of the heat exchanger and configured to capture CO 2 from the cooled combustion product stream; and
recycling at least a portion of the captured CO 2 to the combustor.

2. The method of claim 1 , wherein combusting the fuel is performed at a temperature of about 1,200° C. to about 2,000° C.

3. The method of claim 1 , wherein combusting the fuel is performed at a pressure in a range of about 1 bar to about 10 bars.

4. The method of claim 1 , wherein, prior to combusting the fuel, the method further comprises injecting hydrogen (H 2 ) gas into the reactor.

5. The method of claim 1 , wherein the combustion product stream is cooled to a temperature of about 20° C. to about 200° C.

6. The method of claim 1 , further comprising removing solids from the top gas before passing the top gas to the combustor.

7. The method of claim 1 , wherein recycling the at least the portion of the captured CO 2 to the combustor comprises recycling a first portion of the captured CO 2 .

8. The method of claim 7 , further comprising:
heating a second portion of the captured CO 2 ; and
flowing the second portion of the captured CO 2 through a turbine after the heating to produce electrical power.

9. The method of claim 8 , further comprising combining the first portion of the captured CO 2 with the oxidant upstream of the combustor.

10. The method of claim 8 , further comprising heating the first second portion of the captured CO 2 in at least one of the one or more heat exchangers via the combustion product stream before flowing the second portion of the captured CO 2 through the turbine.

11. The method of claim 1 , further comprising flowing a hydrogen (H 2 ) stream into the reactor as the reducing gas.

12. The method of claim 11 , further comprising generating the H 2 stream via at least a coal gasifier.

13. The method of claim 12 , further comprising:
outputting a treated gas stream from the coal gasifier;
reducing a sulfur content of the treated gas stream with a catalytic shift reactor; and
providing at least a portion of the treated gas stream to a pressure swing adsorption (PSA) unit to produce the H 2 stream.

14. The method of claim 11 , further comprising heating the H 2 stream in at least one of the one or more heat exchangers via the cooled combustion product stream before flowing the H 2 stream into the reactor.

Assignees

• 8 Rivers Capital Llc

Inventors

• Allam Rodney John

Classifications

• C21B2100/282

  of carbon dioxide · CPC title

• C21B2100/66

  Heat exchange · CPC title

• C21B2100/62

  Energy conversion other than by heat exchange, e.g. by use of exhaust gas in energy production · CPC title

• B01D2258/025

  from metallurgy plants · CPC title

• B01D2257/80

  Water · CPC title