# US 4,391,632 A · Process for the separation of lead from a sulfidic concentrate

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- Number: US 4,391,632 A
- Document ID: US4391632A
- Status: Granted
- Kind: A
- Application number: 06/254,211
- Filed: 1981-04-15
- Granted: 1983-07-05
- Earliest claimed: 1980-04-16
- Assignees: Outokumpu Oy
- Inventors: Olavi A. Aaltonen; Rolf E. Malmstrom; Esko O. Nermes; Tapio K. Tuominen
- Web page: https://patentgrep.com/patent/US4391632A

## CPC

- C22B 13/02: by dry processes
- C22B: PRODUCTION AND REFINING OF METALS (electrolytic C25); PRETREATMENT OF RAW MATERIALS

## Abstract

Lead in separated from a sulfidic concentrate by feeding a finely-divided concentrate, a silicate-high slagging agent, and air or oxygen-enriched air into the upper section of a suspension reaction shaft of a flash-smelting furnace in order to form a suspension and to oxidize the lead to lead oxide, by removing the gases via a riser pipe of the furnace and by discharging melt from a lower furnace of the flash-smelting furnace for further treatment. The slagging agent is fed at such a rate that substantially all of the melt is of the slag type and that all of the melt withdrawn from the lower furnace is directed to a reduction stage in order to reduce the lead silicate and to separate it as raw lead. The transversal cross section of the lower furnace is preferably substantially circular.

## Claims

### Claim 1

A process for the separation of lead from a sulfidic concentrate using a flash-smelting furnace which has a lower furnace, a riser pipe connected to the lower furnace for removing gas from the lower furnace, and a reaction shaft connected to the lower furnace, said reaction shaft having an upper section with means for feeding said concentrate into said upper section, comprising the steps of feeding a finely-divided concentrate, a silicate-high slagging agent, and air or oxygen-enriched air into said upper section of said reaction shaft in order to form a suspension and to oxidize the lead to lead oxide, removing gases via said riser pipe, and withdrawing melt from said lower furnace for further treatment which process further comprises feeding the slagging agent at such a rate that substantially all of the lead oxide reacts with the slagging agent to produce lead silicate, resulting in a melt in the form of a slag containing substantially all of the lead silicate in said lower furnace, withdrawing melt from the lower furnace; and directing all of the melt withdrawn from the lower furnace to a reduction furnace in order to reduce the lead silicate to produce raw lead and a slag low in lead and high in silicate and separating raw lead from the slag.

### Claim 2 (depends on 1)

The process of claim 1, in which slagging agent is also fed into the lower furnace or the riser pipe or both and to a point at which there prevails a relatively strong gas turbulence.

### Claim 3 (depends on 1)

The process of claim 1, in which the slagging agent is fed into a lower section of the riser pipe.

### Claim 4 (depends on 1)

The process of claim 1, in which the slagging agent used is the lead-low, silicate-high slag obtained from reduction of the lead silicate and separation of raw lead.

### Claim 5 (depends on 1)

The process of claim 1, in which the slagging agent used is a finely-divided quartz sand.

### Claim 6 (depends on 1)

The process of claim 1, in which the feed is controlled in such a manner that the gas flow velocity in the lower furnace is relatively high, at minimum about 10-20 m/s.

### Claim 7 (depends on 1)

The process of claim 1, in which the temperature of the suspension is at minimum 1373 K. and its oxygen pressure is higher than 5.multidot.10.sup.-10 atm, and the temperature of the suspension is at maximum 1873 K. at an oxygen pressure which is higher than 6.multidot.10.sup.-6 atm.