A process for producing direct reduced iron with a hydrogen rich gas, utilizing a non-fired reducing gas heater such as an electric heater to heat the reducing gas to the temperatures sufficient for iron reduction, includes: providing a shaft furnace to reduce iron oxide with the hydrogen rich reducing gas; removing steam and particulates from the shaft furnace top gas with a scrubber; processing all or a portion of the scrubbed top gas in a gas separation unit such as a membrane and a PSA gas separation unit to create a hydrogen rich stream to be recycled back to the shaft furnace as the reducing agent, so that the hydrogen consumption can be reduced when non-fired reducing gas heater is applied.

Methods and systems for producing steel or similar molten-iron-containing materials in melting or smelting furnaces utilizing pre-reduced iron ore, known also as direct reduced iron (DRI) or sponge iron, wherein the emission of CO.sub.2 and other greenhouse gases is significantly low. Such methods and systems are based on producing DRI in a direct reduction furnace with a reducing gas comprising hydrogen; melting at least a portion of the DRI in a melting furnace in order to generate hot gases; producing steam and/or hot water using the heat contained in the hot gases. From the steam and/or hot water hydrogen is produced by electrolysis, at least a portion of which is fed to the direct reduction furnace as a component of the reducing gas to produce the DRI.

A method of heating direct reduced iron between a direct reduced iron source and processing equipment for the direct reduced iron, comprises providing a conduit heater assembly between the direct reduced iron source and the processing equipment, wherein the conduit heater assembly receives a flow of the direct reduced iron from the direct reduced iron source and heats the direct reduced iron as the direct reduced iron flows through the conduit heater assembly and to the processing equipment.

A method of heating direct reduced iron between a direct reduced iron source and processing equipment for the direct reduced iron, comprises providing a conduit heater assembly between the direct reduced iron source and the processing equipment, wherein the conduit heater assembly receives a flow of the direct reduced iron from the direct reduced iron source and heats the direct reduced iron as the direct reduced iron flows through the conduit heater assembly and to the processing equipment.

The subject of the invention is a method of smelting carbon steels directly from iron ore in one metallurgical reactor, consisting in introducing fine iron ore and fine fluxes into the reactor from the top of the reactor and a gas reducer in the form of hydrogen or a mixture of hydrogen and carbon monoxide from the bottom of the reactor and reducing iron oxides in the liquid phase, while the desired final carbon content in the steel is controlled by introducing an amount of carbon directly into the metal bath which ensures that the desired level of carburisation of the steel is achieved, or by introducing a specific amount of carbon reducer in the form of coke breeze into the iron-bearing charge, characterised in that the thermal energy in the reactor is generated in the process of combustion of natural gas with oxygen in the upper part of the reactor, and the supplied excess of natural gas in relation to the amounts resulting from the stoichiometry of the combustion process is thermally decomposed into carbon and molecular hydrogen providing a reducing atmosphere at the bottom of the reactor.

A method of heating direct reduced iron between a direct reduced iron source and processing equipment for the direct reduced iron, comprises providing a conduit heater assembly between the direct reduced iron source and the processing equipment, wherein the conduit heater assembly receives a flow of the direct reduced iron from the direct reduced iron source and heats the direct reduced iron as the direct reduced iron flows through the conduit heater assembly and to the processing equipment.

An externally heated vertical reactor for reduction of iron ore, the reactor including: (a) a reactor tube positioned vertically adjacent to a furnace; (b) an external furnace positioned vertically adjacent at least one wall of the reactor tube to provide heat to be conducted through the at least one wall; (c) an input port at a base of the reactor tube, wherein the reducing gases are heated and injected into the input port such that the reducing gases rise upward through the reactor tube; (d) a gas exhaust positioned adjacent a top surface of the reactor; (e) a gas filter positioned adjacent an entrance to the gas exhaust; and (f) a bed positioned at the base of the reactor tube, wherein the reduced iron powder product is collected in the bed at the base of the reactor tube.

Processes that generate syngas or reformed gas that have the desired H2/CO ratio, such that they can be used directly for producing higher value liquids, such as using a FT GTL process. The systems and methods of the present invention are simpler and more cost effective than conventional systems and methods. The systems and methods of the present invention generate the required CO2 in a reforming furnace by combusting natural gas with a mixture of O2 from an external source and CO2 that is recirculated from a reforming furnace. A second application of the natural gas combustion with external O2 mixed with recirculated CO2 in the reformer burners can be utilized in a DR process. The reformed gas or syngas containing H2 and CO is used to reduce iron oxide to metallic iron in a shaft furnace, for example.

An apparatus for manufacturing molten metal has a stationary electric furnace, a raw material charging chute, and exhaust duct and a secondary combustion burner in the furnace top, and a shock generator. The raw material charging chute is in one end of the furnace in a width direction and an electric heating region is spaced from the raw material charging chute in the width direction. A raw material layer having a sloping surface extends downward from the one end of the furnace having the raw material charging chute toward the electric heating region, the sloping surface supporting a metal agglomerate raw material layer. The shock generator is provided at least partially within the raw material and extends to the sloping surface, to be in contact with the metal agglomerate raw material layer, and to mechanically overcome hanging of the metal agglomerate raw material layer on the sloping surface.

A direct reduction method and system including an electric heater system adapted to heat a reduction gas and a shaft furnace adapted to receive and utilize the heated reduction gas and one or more of a carbonaceous gas and/or material to produce the direct reduced iron containing carbon, including: providing the reduction gas to an electric heating elements of the electric heater system to heat the reduction gas; stopping the providing the reduction gas; and providing a hydrogen gas or a hydrogen gas with added steam to remove carbon deposition from the electric heating elements of the electric heater system while continuing to heat the reduction gas such that the direct reduced iron production including carbon is not interrupted.