Direct reduced iron system and method using synthetic combustion air
AssigneeNucor Corporation
InventorMirmohammadyousef Motamedhashemi
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Abstract
A system and method of direct reduction of iron (DRI) is disclosed, having a reduction unit configured to reduce iron oxides to metallic iron; a process gas heater coupled to the reduction unit, the process gas heater configured to supply the reduction unit directly with a source of heated reducing gas, where the process gas heater is further configured to receive a synthetic combustion air stream for heating the reducing gas, the synthetic combustion air stream comprising a source of oxygen with essentially no nitrogen. A method of carbon dioxide emission reduction from a direct reduction of iron (DRI) process is also disclosed.
Claims17
A method of direct reduction of iron (DRI) in a reduction unit configured to reduce iron oxides to metalized iron, the method comprising:
- providing to a reduction unit a source of heated reducing gas from a process gas heater;
- producing a top gas stream comprising process carbon dioxide, unreacted reducing gas, unreacted hydrocarbon fuel, and water;
- providing a synthetic combustion air stream to the process gas heater, the synthetic combustion air stream comprising a source of oxygen with essentially no nitrogen;
- and
- reducing iron oxides present in the reduction unit to iron metal.
A method of carbon dioxide emission reduction from a direct reduction of iron (DRI) process, the method comprising:
- reducing iron oxides present in a reduction unit to iron metal;
- producing a top gas stream in the reduction unit comprising process carbon dioxide, water, unreacted reducing gas, and unreacted hydrocarbon fuel;
- introducing the top gas stream to a top gas scrubber coupled to the reduction unit, wherein the top gas scrubber provides a scrubbed gas stream comprising the process carbon dioxide, the unreacted reducing gas, and the unreacted hydrocarbon fuel;
- introducing the scrubbed gas stream to a top gas separator coupled to the top gas scrubber, wherein the top gas separator provides:
- a first stream from at least two streams, the first stream comprising the unreacted reducing gas and the unreacted hydrocarbon fuel with essentially no process carbon dioxide;
- and a second stream from the at least two streams, the second stream comprising essentially the process carbon dioxide;
- providing the first gas stream directly or indirectly to a process gas heater, alone or in combination with additional hydrocarbon fuel and/or a portion of the scrubbed gas stream;
- providing synthetic combustion air to the process gas heater, the synthetic combustion air comprising a mixture of the second stream and a source of oxygen with essentially no nitrogen, the process gas heater producing a flue gas stream comprising flue gas carbon dioxide and the process carbon dioxide;
- introducing the flue gas stream to a flue gas scrubber and providing a carbon dioxide rich stream;
- sequestering the carbon dioxide rich stream and reducing carbon dioxide emission from the reduction unit.
Dependencies are inferred from the claim text.