US2005151307A1PendingUtilityA1
Method and apparatus for producing molten iron
Priority: Sep 30, 2003Filed: Sep 29, 2004Published: Jul 14, 2005
Est. expirySep 30, 2023(expired)· nominal 20-yr term from priority
C21B 13/02Y02P10/122C21B 2100/282C21B 13/002C21B 2100/64C21B 2100/22C21B 13/143C21B 2100/44Y02P10/134
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Claims
Abstract
A system for producing molten iron from iron ores, including a direct reduction shaft furnace, a melting zone in a melting furnace having a coke bed in its lower portion and a charging and preheating chamber in its upper portion, and at least one reducing gas generation zone in communication with said melting zone.
Claims
exact text as granted — not AI-modified1 . A system for producing molten iron from iron ores, comprising:
(1) a direct reduction shaft furnace; (2) a melting zone in a melting furnace having a coke bed in its lower portion and a charging and preheating chamber in its upper portion; and (3) at least one reducing gas generation zone communicating with said melting zone, wherein said system:
(a) produces a reduced intermediate product with a predetermined degree of metallization and carburization in said reduction furnace by reaction of said ores with a high-temperature reducing and carburizing gas;
(b) charges said reduced intermediate product into said melting furnace upon said coke bed, whereby said reduced intermediate product is melted by contact with said high-temperature reducing gas;
(c) produces a reducing gas in said reducing gas generation zone by partial combustion of a hydrocarbon fuel with an oxygen-containing gas; and
(d) transfers said reducing gas into said melting furnace preventing any free oxygen from contacting said coke bed in said melting furnace.
2 . The system for producing molten iron from iron ores according to claim 1 , wherein said reducing gas is produced in a partial combustion chamber so that the hydrocarbon fuel, and oxygen-containing gas react an combust to substantially eliminate the presence of any free oxygen before contacting said coke bed.
3 . The system for producing molten iron from iron ores according to claim 2 , wherein said hydrocarbon fuel is natural gas.
4 . The system for producing molten iron from iron ores according to claim 3 , wherein the ratio of the volumetric flow rate of the oxygen-containing gas to the flow rate of said natural gas is in the range from about 0.86 to about 1.04.
5 . The system for producing molten iron from iron ores according to claim 2 , wherein said hydrocarbon fuel is liquid.
6 . A system for producing molten iron from iron ores according to claim 2 , wherein said hydrocarbon fuel is pet-coke.
7 . A system for producing molten iron from iron ores according to claim 2 , wherein said hydrocarbon fuel is coal.
8 . The system for producing molten iron from iron ores according to claim 1 , wherein said system:
(e) withdraws reacted reducing gas from said reduction furnace; (f) regenerates the reducing potential of said withdrawn reducing gas by cooling and removing at least a portion of its water content; (g) heats a portion of said regenerated withdrawn reducing gas to a temperature above 800° C.; and (h) feeds said heated regenerated withdrawn reducing gas to the reduction furnace.
8 . The system for producing molten iron from iron ores according to claim 1 , wherein said reducing gas is produced in a single partial combustion chamber and fed to said PATENT 120194 - 4420 . 1 melting furnace through a plurality of inlet ports formed and located in the refractory lining of said melting furnace.
9 . The system for producing molten iron from iron ores according to claim 1 , wherein said reducing gas being is produced in a plurality of partial combustion chambers connecting to said melting furnace through a plurality of inlet ports formed through the wall of said melting furnace.
10 . The system for producing molten iron from ores according to claim 1 , wherein said inlet ports are located in said melting furnace so that the high-temperature reducing gas is fed to contact said coke and ascend through a portion of said coke bed and through said preheating chamber of said melting furnace.
11 . The system for producing molten iron according to claim 10 , wherein said iron-containing material is DRI produced in a location remote from said melting furnace.
12 . The system for producing molten iron according to claim 11 , wherein said reducing gas effluent from said melting furnace is further used as fuel, power generation or synthesis gas in other chemical processes.
13 . The system for producing molten iron according to claims 8 , wherein the length of said partial combustion chamber is at least about 0.6 m.
14 . The system for producing molten iron according to claims 8 , wherein the length of said partial combustion chamber is at least about 0.8 m.
15 . The system for producing molten iron according to claim 1 , wherein said melting furnace is located at a remote distance from said direct reduction shaft furnace, wherein said system:
(a) withdraws effluent gases from said melting furnace; (b) cools and cleans said effluent gases; (c) separates CO 2 from said cooled effluent gases; (d) heats said cooled effluent gases to a temperature above about 600° C.; and (e) recycles said heated reducing gases to said melting furnace.
16 . The system for producing molten iron according to claim 15 , wherein a portion of said cooled and cleaned effluent gases from said melting furnace are utilized as fuel for heating said recycled gases.Join the waitlist — get patent alerts
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