Modular direct reduction systems and associated methods

Patent metadata

Field	Value
Publication number	US-12319975-B2
Application number	US-202217697850-A
Country	US
Kind code	B2
Filing date	Mar 17, 2022
Priority date	Mar 17, 2022
Publication date	Jun 3, 2025
Grant date	Jun 3, 2025

Abstract

A modular direct reduction system for producing direct reduced iron (DRI) includes a reformer system which receives a flow of feed gas and which discharges a flow of reducing gas, the reformer system including a plurality of separate reformer modules connected together and wherein each reformer module includes a reformer vessel including an internal chamber, a reactor tube extending through the internal chamber of the reformer vessel and containing a catalyst configured to react with the feed gas received by the reactor tube to form the reducing gas, and a burner to burn a fuel gas to heat the reactor tube, and a furnace system connected to the reformer system and including a furnace having a first inlet which receives an iron ore, a second inlet which receives the reducing gas from the reformer system to form the DRI, and an outlet which discharges the DRI.

First claim

What is claimed is:

1. A modular direct reduction system for producing direct reduced iron (DRI), the system comprising:
a reformer system which receives a flow of feed gas along a feed gas flowpath and which discharges a flow of reducing gas along a reducing gas flowpath, the reformer system comprising a plurality of separate reformer modules connected together and wherein each reformer module comprises:
a reformer vessel comprising an internal chamber;
a reactor tube extending through the internal chamber of the reformer vessel and containing a catalyst configured to react with the feed gas received by the reactor tube to form the reducing gas; and
a burner which receives a flow of fuel gas along a fuel gas flowpath and is configured to burn the fuel gas to heat the reactor tube;

a furnace system connected to the reformer system and comprising a furnace having a first inlet which receives an iron ore, a second inlet which receives the reducing gas from the reformer system to react with the iron ore and form the DRI, and an outlet which discharges the DRI.

2. The system of claim 1 , wherein each of the plurality of separate reformer modules are truckable.

3. The system of claim 1 , wherein each of the plurality of separate reformer modules has a size equal to or less than an intermodal standardized shipping container.

4. The system of claim 1 , further comprising:
a feed gas header connected to each of the plurality of separate reformer modules, wherein the feed gas flowpath extends through the feed gas header; and
a reducing gas header connected to each of the plurality of separate reformer modules, wherein the reducing gas flowpath extends through the reducing gas header.

5. The system of claim 1 , wherein:
the feed gas comprises a pre-heated feed gas and the feed gas flowpath comprises a pre-heated feed gas flowpath; and
the system further comprises:
a heat recovery system which receives a flow of raw feed gas along a raw feed gas flowpath and which discharges a flow of the pre-heated feed gas along the pre-heated feed gas flowpath, the heat recovery system comprising a plurality of separate heat recovery modules connected together and wherein each heat recovery module comprises:
a heat recovery vessel comprising an internal chamber;
a first fluid conduit extending through the internal chamber of the heat recovery vessel, wherein the first fluid conduit receives the flow of raw feed gas and discharges the flow of pre-heated feed gas; and
a second fluid conduit extending through the internal chamber of the heat recovery vessel, wherein the second fluid conduit receives a flow of flue gas from the reformer system to heat the raw feed gas received by the first fluid conduit.

6. The system of claim 5 , wherein each of the plurality of separate heat recovery modules are truckable.

7. The system of claim 5 , wherein each of the plurality of separate heat recovery modules has a size equal to or less than an intermodal standardized shipping container.

8. The system of claim 5 , further comprising:
a raw feed gas header connected to each of the plurality of separate heat recovery modules, wherein a raw feed gas flowpath extends through the raw feed gas header; and
a pre-heated feed gas header connected to each of the plurality of separate heat recovery modules, wherein a pre-heated feed gas flowpath extends through the pre-heated feed gas header.

9. A method for providing a direct reduction system to produce direct reduced iron (DRI), the method comprising:
(a) determining a number of pre-fabricated reformer modules of the direct reduction system required to provide the direct reduction system with a desired DRI output capacity;
(b) transporting the determined number of pre-fabricated reformer modules from an off-site location to a site of the direct reduction system;
(c) connecting the determined number of pre-fabricated reformer modules together to form a reformer system of the direct reduction system, wherein the reformer system is configured to convert a feed gas received by the reformer system into a reducing gas discharged by the reformer system; and
(d) connecting the reformer system to a furnace system of the direct reduction system at the site of the direct reduction system, wherein the furnace system is configured to convert an iron ore received by the furnace system into the DRI using the reducing gas discharged by the reformer system.

10. The method of claim 9 , wherein (b) comprises road-transporting the determined number of pre-fabricated reformer modules to the site of the direct reduction system.

11. The method of claim 9 , wherein (b) comprises water-transporting the determined number of pre-fabricated reformer modules to the site of the direct reduction system.

12. The method of claim 9 , wherein each of the pre-fabricated reformer modules comprises:
a vessel comprising an internal chamber;
a reactor tube extending through the internal chamber of the vessel and containing a catalyst configured to react with the feed gas received by the reactor tube to form the reducing gas; and
a burner which receives a flow of fuel gas along a fuel gas flowpath and is configured to burn the fuel gas to heat the reactor tube.

13. The method of claim 9 , wherein at least some of the determined number of pre-fabricated reformer modules are connected together to form a reformer very large module (VLM) prior to transporting the reformer VLM to the site of the direct reduction system.

14. The method of claim 9 , further comprising:
(e) determining a number of pre-fabricated heat recovery modules of the direct reduction system required to provide the direct reduction system with the desired DRI output capacity;
(f) transporting the determined number of pre-fabricated heat recovery modules to the site of the direct reduction system; and
(g) connecting the determined number of pre-fabricated heat recovery modules together to form a heat recovery system of the direct reduction system, wherein the heat recovery system is configured to heat the feed gas using a flue gas discharged by the reformer system before the feed gas is received by the reformer system.

15. The method of claim 14 , wherein (f) comprises road-transporting the determined number of pre-fabricated heat recovery modules to the site of the direct reduction system.

16. The method of claim 14 , wherein each of the pre-fabricated reformer modules comprises:
a heat recovery vessel comprising an internal chamber;
a first fluid conduit extending through the internal chamber of the heat recovery vessel, wherein the first fluid conduit receives the feed gas heated by the heat recovery module; and
a second fluid conduit extending through the internal chamber of the heat recovery vessel, wherein the second fluid conduit receives a flue gas from the reformer system to heat the feed gas received by the first fluid conduit.

17. A method for providing a direct reduction system to produce direct reduced iron (DRI), the method comprising:
(a) fabricating a plurality of separate reformer modules at an off-site location, each of the plurality of separate reformer modules comprising:
a vessel comprising an internal chamber;
a reactor tube extending through the internal chamber of the vessel and containing a catalyst configured to react with a feed gas received by the reactor tube to form a reducing gas; and
a burner which receives a flow of fuel gas along a fuel gas flowpath and is configured to burn the fuel gas to heat the reactor tube;

(b) transporting at least some of the fabricated reformer mod

Assignees

• Fluor Tech Corp

Inventors

• Dailey Jonathan M
• Corradi Ray A
• Ubbens Menko H

Classifications

• C21B2300/02

  Particular sequence of the process steps · CPC title

• C21B13/14

  Multi-stage processes {processes carried out in different vessels or furnaces} · CPC title

• C21B13/02

  in shaft furnaces · CPC title

• C21B13/0073

  Selection or treatment of the reducing gases · CPC title

• C01B2203/0227

  containing a catalytic reforming step · CPC title