# US 8,771,397 B2 · Steelmaking facility comprising a direct reduction plant and an electric-arc furnace > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 8,771,397 B2 - Document ID: US8771397B2 - Status: Granted - Kind: B2 - Application number: 12/988,489 - Filed: 2008-04-17 - Published: 2011-04-28 - Granted: 2014-07-08 - Earliest claimed: 2008-04-17 - Assignees: Hyl Technologies, S.A. De C.V.; Danieli & C. Officine Meccaniche SpA - Applicants: Gilberto Garza-Rodriguez; Andrea Tavano; Octavio Jorge Becerra-Novoa - Inventors: Gilberto Garza-Rodriguez; Andrea Tavano; Octavio Jorge Becerra-Novoa - Web page: https://patentgrep.com/patent/US8771397B2 ## CPC - C21B 13/143: {Injection of partially reduced ore into a molten bath} - C21B 13/0086: {Conditioning, transformation of reduced iron ores} - C21B 13/14: Multi-stage processes {processes carried out in different vessels or furnaces} - C21C 5/527: {Charging of the electric furnace} - C21C 5/5294: {General arrangement or layout of the electric melt shop} - F27B 3/18: Arrangements of devices for charging - F27D 3/10: Charging directly from hoppers or shoots - Y02P 10/134: by avoiding CO2, e.g. using hydrogen - Y02P 10/20: Recycling - C21B: MANUFACTURE OF IRON OR STEEL (preliminary treatment of ferrous ores or scrap C22B1/00) - C21C: PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS - F27B: FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS - F27D: DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE - Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS ## Abstract A steelmaking plant including a pressurized direct reduction reactor for continuous production of hot direct reduced iron with a batch-melting furnace and a standby cooler, all three being capable of being situated side-by-side, with such DRI being able to be alternatively fed to the furnace or to the cooler. The furnace is selectively charged through a diverter valve by a pneumatic transport system with the hot DRI being entrained in a carrier gas fed into a receiving bin (having an upper DRI/gas disengagement space and a lower DRI buffer portion). A pressurized charge of the DRI accumulated in such disengaging/buffer bin is periodically fed down into a dosing/depressurization bin which in turn depressurizes the DRI and feeds a batch of DRI down into the furnace. Upon sensing that the buffer portion is full, the DRI is then pneumatically diverted to the cooler, such as during furnace maintenance shut down. ## Claims ### Claim 1 A steelmaking plant comprising: a direct reduction reactor for continuously producing hot direct reduced iron, DRI, with a discharge at its lower end; a DRI melting furnace; a separate DRI cooler positioned aside from said reactor; a pressurized disengagement buffer bin located above said melting furnace; a dosing depressurizing bin located in series between said disengagement buffer bin and said melting furnace and having a capacity to hold a charge of DRI of at least one heat size for said furnace; a pneumatic transport apparatus for conducting said hot DRI with a carrier gas from said reactor discharge to feed selectively, at a level above the discharge of said reactor, either said furnace via said bins or said cooler; said disengagement buffer bin having an upper portion, with space sufficient to disengage DRI from the carrier gas, and also having as its lower portion a buffering capacity to receive a continuing influx of DRI in sufficient excess of one heat size for said furnace to accommodate delays in the melting furnace until the buffering capacity is full; a first conduit means for conveying hot DRI from said reduction reactor to said disengagement buffer bin as part of the pneumatic transport apparatus; a second conduit means for conveying hot DRI from said disengagement buffer bin to said dosing depressurizing bin; a third conduit means for conveying hot DRI from said dosing depressurizing bin to said melting furnace; a fourth conduit means for conveying said hot DRI from said reduction reactor to said DRI cooler as part of the pneumatic transport apparatus; and a diverter valve for selectively directing a continuous flow of DRI from the reactor to one at least said first or fourth conduits. ### Claim 2 (depends on 1) A steelmaking plant according to claim 1, wherein said melting furnace is an electric-arc furnace. ### Claim 3 (depends on 2) A steelmaking plant according to claim 2, further comprising a sensor for determining that the DRI has filled the buffering capacity of said lower portion of disengagement buffer bin and for controlling the diverter valve to switch the DRI flow over to feed the cooler. ### Claim 4 (depends on 3) A steelmaking plant according to claim 3, wherein said dosing depressurizing bin is subject to an ambient atmosphere; and further comprising gas sealing valves for isolating said dosing depressurizing bin from the ambient atmosphere and for maintaining the pressure of the pneumatic transport apparatus in said disengagement buffer bin. ### Claim 5 (depends on 4) A steelmaking plant according to claim 4, wherein said series of bins are aligned such that hot DRI flows by gravity through said second and third conduit means. ### Claim 6 (depends on 5) A steelmaking plant according to claim 5 wherein said DRI cooler includes a disengagement bin. ### Claim 7 (depends on 6) A steelmaking plant according to claim 6, further comprising at least one pressure-lock bin and gas sealing valves at the inlet and outlet of said pressure-lock bin for isolating said pressure-lock bin from the ambient atmosphere and for discharging cooled DRI from said DRI cooler. ### Claim 8 (depends on 7) A steelmaking plant according to claim 7, wherein said disengagement buffer bin has a capacity of at least about 1.3 times the heat size of said melting furnace. ### Claim 9 (depends on 8) A steelmaking plant according to claim 8, wherein said disengagement buffer bin has a capacity of at least about 1.8 times the heat size of said melting furnace. ### Claim 10 (depends on 1) A steelmaking plant according to claim 1, wherein said direct reduction reactor is pressurized. ### Claim 11 (depends on 10) A steelmaking plant according to claim 10, wherein said melting furnace is an electric-arc furnace. ### Claim 12 (depends on 11) A steelmaking plant according to claim 11, further comprising a sensor for determining that the DRI has filled the buffering capacity of said lower portion of disengagement buffer bin and for controlling the diverter valve to switch the DRI flow over to feed the cooler; wherein said dosing depressurizing bin is subject to an ambient atmosphere; and further comprising gas sealing valves for isolating said dosing depressurizing bin from the ambient atmosphere; wherein said series of bins are aligned such that hot DRI flows by gravity through said second and third conduit means; wherein said DRI cooler includes a disengagement bin; and further comprising at least one pressure-lock bin and gas sealing valves at the inlet and outlet of said pressure-lock bin for isolating said pressure-lock bin from the ambient atmosphere and for discharging cooled DRI from said DRI cooler. ### Claim 13 (depends on 12) A steelmaking plant according to claim 12, wherein said disengagement buffer bin has a capacity of at least about 1.3 times the heat size of said melting furnace. ### Claim 14 (depends on 13) A steelmaking plant according to claim 13, wherein said disengagement buffer bin has a capacity of at least about 1.8 times the heat size of said melting furnace. ### Claim 15 (depends on 1) A steelmaking plant according to claim 1, further comprising a direct discharging and depressurizing bin and a diversion fifth conduit means for selectively conveying, via said diverter valve, DRI from said reduction reactor to said direct discharging and depressurizing bin. ### Claim 16 A method of making steel in a mini-mill plant comprising a direct reduction reactor for producing hot direct reduced iron, DRI; a DRI melting furnace; a DRI cooler; a pressurized disengagement buffer bin located above said melting furnace; a dosing depressurizing bin located in series between said disengagement buffer bin and said melting furnace, said disengagement buffer bin having an upper portion, with space sufficient to disengage DRI from the carrier gas, and also having as its lower portion a buffering capacity to receive a continuing influx of DRI in sufficient excess of one heat size for said furnace to accommodate delays in the melting furnace until the buffering capacity is full; a diverter valve; and suitable conduits for transferring said hot DRI from said reduction reactor to said disengagement buffer bin and successively from said disengagement buffer bin to said dosing depressurizing bin and then to said melting furnace and/or for selectively conveying a portion of said hot DRI from said reduction reactor to said DRI cooler; which method comprises the steps of: 1. producing hot DRI in said reduction reactor; 2. selectively and continuously pneumatically conveying by means of a carrier gas said hot DRI to the disengagement buffer bin; 3. determining the amount of hot DRI which will be charged to said melting furnace according to the heat size; 4. determining at what level the DRI is in said dosing depressurizing bin; 5. conveying hot DRI from said disengagement buffer bin to said dosing depressurizing bin to at least match said amount to be charged to the melting furnace; 6. thereafter isolating said dosing depressurizing bin from said disengagement buffer bin: 7. depressurizing said dosing depressurizing bin and dosing the DRI now isolated in the dosing depressurizing bin into the furnace by said amount to be charged; 8. thereafter re-pressurizing and reconnecting said dosing depressurizing bin to said disengagement buffer bin; continuing the cycle of foregoing steps 1-8; except that upon determining that the level of DRI in said disengagement buffer bin has reached its buffering capacity then the pneumatic conveying by means of a carrier gas of said hot DRI is diverted to the cooler. ### Claim 17 (depends on 16) A method according to claim 16, wherein said dosing from said dosing depressurizing bin is into an electric arc steel making furnace, and wherein said disengagement buffer bin has a capacity of at least about 1.3 times the heat size of said melting furnace. ### Claim 18 (depends on 17) A method according to claim 17, further comprising sensing when DRI has filled the buffering capacity of said lower portion of disengagement buffer bin and then controlling the diverter valve to switch the carrier gas conveying the hot DRI over to feed the cooler. ### Claim 19 (depends on 16) A method according to claim 16, wherein said direct reduction reactor is pressurized. ### Claim 20 (depends on 19) A method according to claim 19, wherein said dosing from said dosing depressurizing bin is into an electric arc steel making furnace, and wherein said disengagement buffer bin has a capacity of at least about 1.3 times the heat size of said melting furnace. ### Claim 21 (depends on 20) A method according to claim 20, further comprising sensing when DRI has filled the buffering capacity of said lower portion of disengagement buffer bin and then controlling the diverter valve to switch the carrier gas conveying the hot DRI over to feed the cooler. ### Claim 22 (depends on 16) A method according to claim 16, wherein said mini-mill plant further comprises a pneumatic transport apparatus for conducting said hot DRI with said carrier gas from said reactor to feed selectively, at a level above the discharge from said reactor, either said furnace via said bins or said cooler; and maintaining, in said disengagement buffer bin, pressure from the pneumatic transport apparatus.