Method for controlling the suspension in a suspension smelting furnace

Patent metadata

Field	Value
Publication number	US-10852065-B2
Application number	US-201715593593-A
Country	US
Kind code	B2
Filing date	May 12, 2017
Priority date	Nov 29, 2011
Publication date	Dec 1, 2020
Grant date	Dec 1, 2020

Abstract

The invention relates to a method for controlling suspension in a suspension smelting furnace. The method comprises feeding additionally to pulverous solid matter and additionally to reaction gas reducing agent into the suspension smelting furnace, wherein reducing agent is fed in the form of a concentrated stream of reducing agent through the suspension in the reaction shaft onto the surface of the melt to form a reducing zone containing reducing agent within the collection zone of the melt.

First claim

The invention claimed is:

1. A suspension smelting furnace for suspension smelting of pulverous solid matter, wherein the suspension smelting furnace comprises:
a reaction shaft having an elongated vertical configuration and ending in a lower end,
a lower furnace having an elongated horizontal configuration and that is in communication with and adjoins the lower end of the reaction shaft and
a concentrate burner at the top of the reaction shaft,
the concentrate burner comprises a pulverous solid matter supply device for feeding pulverous solid matter into the reaction shaft and comprises a gas supply device for feeding reaction gas into the reaction shaft,
the concentrate burner being configured to feed pulverous solid matter and reaction gas into the reaction shaft to produce a suspension of pulverous solid matter and reaction gas in the reaction shaft,
the lower furnace being configured to collect suspension on the surface of a melt in the lower furnace so that suspension that lands on the surface creates a collection zone at the surface of the melt in the lower furnace,
the lower furnace further having a roof structure with a feed opening adjoining an open lower end of the reaction shaft,
the suspension smelting furnace being configured to receive additionally to pulverous solid matter and additionally to reaction gas reducing agent from a reducing agent feeder,
the reaction shaft being configured to receive fed pulverous solid matter and reaction gas into the reaction shaft by means of the concentrate burner so that suspension produced by pulverous solid matter and reaction gas forms a suspension jet in a suspension shaft, wherein the suspension jet widens in the reaction shaft in the direction of the lower furnace and wherein the suspension jet has an imaginary vertical central axis, and
the suspension smelting furnace is capable of receiving the reducing agent in the form of a concentrated stream of reducing agent fed from the reducing agent feeder through the suspension in the suspension smelting furnace onto the surface of the melt to form a reducing zone containing the reducing agent within the collection zone of the melt, and wherein the reducing agent is fed at an initial velocity that is at least the feeding velocity of the reaction gas,
the reducing agent feeder being configured so that a concentrated stream of reducing agent is directed from the reducing agent feeder essentially in the direction of an imaginary vertical central axis of the suspension jet and in the vicinity to the imaginary vertical central axis of the suspension jet to prevent reducing agent of the concentrated stream of reducing agent from reacting with reaction gas prior landing on the surface of the melt,
wherein the reducing agent feeder is configured to feed the concentrated stream of reducing agent from the inside the lower furnace of the suspension smelting furnace.

2. The suspension smelting furnace according to claim 1 , wherein the concentrate burner comprising a pulverous solid matter supply device comprising a feeder pipe for feeding pulverous solid matter into the reaction shaft, wherein the feeder pipe has an orifice that opens to the reaction shaft,
a dispersing device, which is arranged concentrically inside the feeder pipe and which extends to a distance beyond the orifice of the feeder pipe into the reaction shaft and which comprises dispersion gas openings for directing dispersion gas around the dispersing device and to pulverous solid matter that flows around the dispersing device; and
a gas supply device for feeding reaction gas into the reaction shaft, wherein the gas supply device opening to the reaction shaft through an annular discharge orifice that concentrically surrounds the feeder pipe for mixing reaction gas that discharges from the annular discharge orifice with pulverous solid matter, which discharges from the orifice of the feeder pipe and which is directed to the side by means of dispersion gas to produce suspension of pulverous solid matter and reaction gas in the reaction shaft.

3. The suspension smelting furnace according to claim 1 , including a controller configured to control the amount of fed reaction gas to the amount of fed reducing agent to form sub-stoichiometric conditions in the middle of the suspension of the suspension smelting furnace.

4. The suspension smelting furnace according to claim 1 , including a controller configured to control the amount of fed reaction gas to the amount of fed reducing agent to form stoichiometric or over-stoichiometric conditions in the middle of the suspension of the suspension smelting furnace.

Assignees

• Outotec Finland Oy

Inventors

• Lahtinen Markku
• Pesonen Lauri P
• Ahokainen Tapio
• Bjorklund Peter

Classifications

• F27D3/14

  Charging or discharging liquid or molten material · CPC title

• F27D19/00 Primary

  Arrangements of controlling devices · CPC title

• F27D2019/0068

  Regulation involving a measured inflow of a particular gas in the enclosure · CPC title

• F27B1/20

  Arrangements of devices for charging · CPC title

• F27D3/0033

  charging of particulate material · CPC title