IP Library Granted Patent US 12703895
Granted Patent B2
US 12703895 · App. 16/462,040 · Granted Aug 11, 2026

Processing methods and processing apparatus

Inventors: Alan Peel (Chesterfield, GB); Andrew Gibbs (Chesterfield, GB)
Assignee: Altek Europe Limited
C22B21/0069C22B7/04C22B21/0007Y02P10/20
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Quick Facts
Patent No.
US 12703895
App. No.
16/462,040
Granted
Aug 11, 2026
Kind
B2
Abstract

Methods and apparatus for processing a material, the material being the upper layer from a metal melting process, the material containing one or more salts, the material containing one or metals, are provided. The method includes feeding the material to a size reduction step; feeding the material from the size reduction step to a density based separation step; feeding the material from the density based separation step to a leaching step. The size reduction stage is optimised to provide exposure of material for a ferrous and non-ferrous metal separation. The ferrous separation is preferably provided by an eddy current separator. The non-ferrous separation is preferably provided by a cyclone.

Claims (22)

1 . A method of processing a material from a metal melting process, the material comprising one or more salts and one or more metals, the method including:

feeding the material to a size reduction step;

feeding the material from the size reduction step to a density based separation step;

forming a cleaned salt stream at the density based separation step; and

feeding the cleaned salt stream from the density based separation step to a leaching step.

2 . The method of claim 1 , wherein the size reduction step includes a jaw crushing step, a rolling step, or both.

3 . The method of claim 1 , comprising feeding a treatment chemical to the leaching step, the treatment chemical being distinct from the cleaned salt stream.

4 . The method of claim 1 , wherein the size reduction step provides an output as a flat bed of material to expose a ferrous metal to separation.

5 . The method of claim 1 , comprising:

forming a leached salt stream, at the leaching step; and

feeding the leached salt stream from the leaching step to a spray dryer.

6 . The method of claim 1 , wherein the size reduction step is followed by a ferrous metal separation step and then a non-ferrous metal separation step.

7 . The method of claim 6 , wherein a residence time of the leaching step is less than 10 minutes.

8 . The method of claim 6 , wherein aluminium extracted by the density based separation step is returned to a furnace.

9 . The method of claim 1 , wherein the density based separation step uses a cyclone or an air based cyclone.

10 . The method of claim 1 , comprising removing, at the density based separation step, one or more gas generating components from the material to form the cleaned salt stream.

11 . The method of claim 1 , wherein the density based separation step separates aluminium and/or aluminium containing components from salt containing components.

12 . The method of claim 1 , comprising

producing, at the leaching step, a dissolved salt stream and a suspended solid stream; and

feeding the dissolved salt stream and the suspended solid stream to a filter step.

13 . The method of claim 12 , wherein the filter step includes feeding the dissolved salt stream and the suspended solid stream to a vacuum belt filter.

14 . The method of claim 12 , feeding the dissolved salt stream from the filter step to a spray dryer.