Starting a smelting process

Patent metadata

Field	Value
Publication number	US-9551044-B2
Application number	US-201214363227-A
Country	US
Kind code	B2
Filing date	Dec 6, 2012
Priority date	Dec 6, 2011
Publication date	Jan 24, 2017
Grant date	Jan 24, 2017

Abstract

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.

First claim

The invention claimed is:

1. A method of starting a molten-bath based process for smelting a metalliferous feed material in a smelting apparatus, with the apparatus including a smelting vessel that includes a main chamber for containing a molten bath, a forehearth for discharging molten metal from the main chamber during a smelting campaign, and a forehearth connection that connects the main chamber and the forehearth, and with the method including the steps of:
(a) preheating the main chamber, the forehearth, and the forehearth connection;
(b) pouring a charge of hot metal into the main chamber via the forehearth;
(c) commencing supplying cold oxygen-containing gas and cold carbonaceous material into the main chamber within at most 3 hours after completing the hot metal charge before an insulating layer of crusty slag forms on the metal charge to an extent that it prevents molten metal igniting carbonaceous material and igniting the carbonaceous material and heating the main chamber and molten metal in the main chamber;
(d) continuing supplying oxygen-containing gas and carbonaceous material into the main chamber and combusting carbonaceous material and heating the main chamber and molten metal in the main chamber for a period of at least 10 minutes; and
(e) commencing feeding a metalliferous material into the main chamber in order to initiate metal production.

2. The method defined in claim 1 includes verifying ignition of oxygen-containing gas and carbonaceous material in the main chamber.

3. The method defined in claim 1 wherein step (a) includes preheating a hearth of the vessel, the forehearth, and the forehearth connection such that an average surface temperature of the hearth, the forehearth, and the forehearth connection is above 1000° C.

4. The method defined in claim 3 wherein step (a) includes preheating the hearth of the vessel, the forehearth, and the forehearth connection such that an average surface temperature of the hearth, the forehearth, and the forehearth connection is above 1200° C.

5. The method defined in claim 1 wherein step (b) includes selecting the amount of the charge of hot metal into the main chamber via the forehearth such that the metal level in the main chamber is at least 100 mm above the top of the forehearth connection.

6. The method defined in claim 5 wherein step (b) includes selecting the amount of the charge of hot metal into the main chamber via the forehearth such that the metal level in the main chamber is at least 200 mm above the top of the forehearth connection.

7. The method defined in claim 1 wherein step (c) includes commencing supplying oxygen-containing gas and carbonaceous material into the main chamber within 2 hours after completion of the hot metal charge into the main chamber.

8. The method defined in claim 7 wherein step (c) includes commencing supplying oxygen-containing gas and carbonaceous material into the main chamber within 1 hour after completion of the hot metal charge into the main chamber.

9. The method defined in claim 1 wherein step (d) includes heating the main chamber for a period of 30-60 minutes by combusting carbonaceous material and oxygen-containing gas in the main chamber.

10. The method defined in claim 1 wherein the initial feed rates of oxygen-containing gas and carbonaceous material into the main chamber in step (c) are calculated such that there is sufficient oxygen to fully combust the carbonaceous material.

11. The method defined in claim 10 wherein, once this initial ignition step (c) is complete, the rates of oxygen-containing gas and carbonaceous material are adjusted in step (d) from step (c) rates such that there is at least 40% the amount of oxygen for complete combustion of the carbonaceous material.

12. The method defined in claim 1 includes, following step (d) and before step (e), feeding slag or slag-forming agents into the main chamber in order to establish a suitable slag inventory for smelting metalliferous material in the main chamber.

13. The method defined in claim 1 wherein the molten bath-based smelting process includes the steps of:
(a) supplying carbonaceous material and solid or molten metalliferous material into the molten bath and generating reaction gas and smelting metalliferous material and producing molten metal in the bath,
(b) supplying oxygen-containing gas into the main chamber for above-bath combustion of combustible gas released from the bath and generating heat for in-bath smelting reactions; and
(c) producing significant upward movement of molten material from the bath by gas upwelling in order to create heat-carrying droplets and splashes of molten material which are heated when projected into the combustion region in the top space of the main chamber and thereafter fall back into the bath, whereby the droplets and splashes carry heat downwards into the bath where it is used for smelting of the metalliferous material.

14. A method of starting a molten-bath based process for smelting a metalliferous feed material in a smelting apparatus, with the apparatus including a smelting vessel that includes a main chamber for containing a molten bath, a forehearth for discharging molten metal from the main chamber during a smelting campaign, and a forehearth connection that connects the main chamber and the forehearth, and with the method including the steps of:
(a) preheating the main chamber, the forehearth, and the forehearth connection;
(b) pouring a charge of hot metal into the main chamber via the forehearth;
(c) commencing supplying cold oxygen-containing gas and cold carbonaceous material into the main chamber and igniting carbonaceous material and heating the main chamber and molten metal in the main chamber within a time period before an insulating layer of crusty slag forms on the metal charge to an extent that it prevents molten metal igniting carbonaceous material;
(d) continuing supplying oxygen-containing gas and carbonaceous material into the main chamber and combusting carbonaceous material and oxygen-containing gas and heating the main chamber and molten metal in the main chamber for a period of at least 10 minutes; and
commencing feeding a metalliferous material into the main chamber in order to initiate metal production.

Assignees

• Tech Resources Pty Ltd

Inventors

• Dry Rodney James
• Meijer Hendrikus Koenraad Albertus

Classifications

• Y02P10/122

  by capturing or storing CO2 · CPC title

• F27D3/18

  Charging particulate material using a fluid carrier · CPC title

• C21C5/567

  operating in a continuous way · CPC title

• F27D3/16

  Introducing a fluid jet or current into the charge (F27D3/18 takes precedence) · CPC title

• C21B2100/42

  Sulphur removal · CPC title