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 (CO.sub.2), may be isolated using carbon capture and sequestration (CCS) for reducing associated greenhouse gas emissions.

Disclosed herein, in some aspects, are systems and methods for producing a material comprising iron through self-reduction of iron ore using bio-oil and/or other reducing agents (e.g., bio-based reducing agents), such as biocrude, ethanol, or other bio-based liquids or biologically sourced liquids. The bio-oil and/or other reducing agents can be mixed with the iron ore to form a furnace mixture, which can be heated, such that the components of the bio-oil and/or other reducing agents in the furnace mixture reduce the iron ore to form an iron product (e.g., a material that includes metallic iron). In some cases, the pre-formed furnace mixture allows for the reducing agents to interact with the iron more readily, thereby providing for quicker reaction rates, and thereby quicker reduction of iron ore, as compared to direct reduction iron production.

A method of ironmaking using full-oxygen hydrogen-rich gas which includes hot transferring and hot charging the high-temperature coke, sinter and pellet into the ironmaking furnace through transferring and charging device, and injecting oxygen and hydrogen-rich combustible gas at a predetermined temperature into the ironmaking furnace through the oxygen tuyere and the gas tuyere disposed at the ironmaking furnace, respectively. It also provides an apparatus for ironmaking using full-oxygen hydrogen-rich gas which includes a raw material system, a furnace roof gas system, a coke oven gas injecting system, a dust injecting system, a slag dry-granulation and residual heat recovering system and an oxygen system. Additionally an apparatus and method for hot transferring and hot charging of ironmaking raw material is disclosed.

A method of starting a molten-bath based melting process includes commencing supplying cold oxygen-containing gas and cold carbonaceous material into a main chamber of a smelting vessel within at most 3 hours after completing a hot metal charge into the vessel and igniting the carbonaceous material and heating the main chamber and molten metal in the main chamber.

A system for energy optimization in a plant (3) for producing direct-reduced metal ores (3). The plant (3) has at least one reduction unit (12), a device for separating gas mixtures (7, 7a, 7b) having an associated compressing device (4, 4a, 4b), and a gas-heating device (10) upstream of the reduction unit (12). Part of the process gases (2, 2a, 2b) is fed by a feed line from a smelting reduction plant to the plant for producing direct-reduced metal ores (3). A turbine (8, 8a, 8b) is fit between the device for separating gas mixtures (7, 7a, 7b) and the gas-heating device (10) upstream of the reduction unit (12) such that a pressure drop between the device for separating gas mixtures (7, 7a, 7b) and the reduction unit (12) is converted into forms of energy that can be used to operate additional components (4, 4a, 4b, 15, 15a, 15b) of the plant (3), in particular electrical energy and/or mechanical energy. Energy consumption of the plant (3) is reduced.

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 (CO.sub.2), may be isolated using carbon capture and sequestration (CCS) for reducing associated greenhouse gas emissions.

A cooling assembly for cooling exhaust gases emitted from a steel-making furnace includes a body having a cross-sectional shape with a thickness defined between an outer surface and an inner surface thereof. The body includes a first mounting end having a first length and a second mounting end having a second length, the second length being different from the first length. The body is arcuately-shaped with a concave inner surface and convex outer surface, and the second mounting end is spaced from the first mounting end. A fluid conduit is defined between the inner surface and the surface for a cooling fluid to flow therethrough.

The present invention provides a reduction system and method that can be operated with any proportion of gaseous hydrogen-containing gases and gaseous hydrocarbon-containing gases having the possibility of continuing its operation, ensuring an high process availability and negligible loss of production, when the gaseous hydrogen-containing gas for any reason is not available and allow the substitution of the gaseous hydrogen-containing gas with a gaseous hydrocarbon-containing gas with minor adjustments in the plant operation. The reduction system of the invention is designed to be implemented in new and already built direct reduction plants to operate efficiently and has lower capital and operation costs.

A direct reduction plant, system, and/or method utilizing gas that is injected between a reduction gas injection level and a top gas offtake level in a shaft furnace to modulate (or moderate) the reduction speed and temperature in the upper portion of the shaft furnace, above the reduction gas injection level, where the initial reduction of iron oxide from Fe2O3 to Fe3O4 or FeO takes place. This gas injected above the reduction gas injection level in the shaft furnace may be quenched process gas, quenched reformed gas, quenched mixed gas (including both quenched process gas and quenched reformed gas), and/or cold process gas. The length of the shaft furnace can also be extended to offset the initial slower reduction or enlarged overall reduction zone so that the productivity can be maintained.

The present invention relates to a metal material production configuration (1) and to a method of direct reduction of a metal oxide material (5) holding a first thermal energy into a reduced metal material (16). The method comprises the steps of charging the metal oxide material (5) holding the first thermal energy into a direct reduction facility (7) via a metal oxide material charging inlet device (A), introducing a pre-heated hydrogen containing reducing agent (H), holding a second thermal energy, into the direct reduction facility (7) via a reducing agent inlet device (B).

The metal oxide material (5) id direct reduced by using the first thermal energy of the metal oxide material (5) to heat or further heat the introduced pre-heated hydrogen containing reducing agent (H) for providing a chemical reaction between the introduced pre-heated hydrogen containing reducing agent (H) and the metal oxide material (5); exposing the reduced metal material to a required heat treatment temperature for providing heat treatment of the reduced metal material to obtain a densified reduced metal material; and upholding the required heat treatment temperature by the introduction of the pre-heated hydrogen containing reducing agent (H) by means of a heat treatment providing device (17).