A dilute copper metal composition includes 57-85% wt Cu, 3.0% wt Ni, 0.8% wt Fe, 7-25% wt Sn and 3-15% wt Pb. A process includes the steps of partially oxidizing a black copper composition to obtain a first copper refining slag and a first enriched copper metal, partially oxidizing the first enriched copper metal to obtain a second copper refining slag, whereby at least 37.0% wt of the amount of tin and lead processed is retrieved in the first and second copper refining slags together; and partially reducing the first copper refining slag to form a first lead-tin based metal composition and a first spent slag. The process further includes the steps of adding the second copper refining slag to the first lead-tin based metal composition, thereby forming a first liquid bath; and partially oxidizing the first liquid bath, thereby obtaining the dilute copper metal composition.

A method for producing briquettes made of a waste material includes provisioning of at least one metal and at least one organic material. The waste material is mechanically prepared in a single or multiple stages and at least one first fraction of the waste material is separated. A briquette mixture containing the at least one first fraction is produced, wherein the at least one first fraction has a calorific value of 0 MJ/kg to 30 MJ/kg. A calorific value of the briquette mixture is adjusted by varying at least the first fraction. The briquette mixture is introduced into a briquetting device and pressed into briquettes. Briquettes with a calorific value of 5 MJ/kg to 30 MJ/kg and with a maximum copper content of 0.1 wt % to 20 wt % are produced.

A method for recovering metals, such as noble metals or copper, from secondary materials and other materials having organic constituents, wherein the organic components are extracted from the secondary materials and other material by thermal treatment in a process chamber and the secondary materials and other materials having organic constituents are prepared for the recovery process.

According to the present invention there is provided a method for treating a zinc leach residue comprising the steps of: adding the zinc leach residue and a sulfide material comprising copper and flux to a furnace having a molten bath therein; operating the furnace to produce a matte comprising copper and a slag comprising zinc; separating the matte from the slag; and recovering zinc from the slag. The method preferably comprises the additional step of recovering the copper and/or other precious metals such as silver and gold, from the matte.

According to the present invention there is provided a method for smelting a zinc sulfide concentrate, the method comprising the steps of: feeding the zinc sulfide concentrate to a reduction furnace at a known mass flow rate of sulfur; feeding copper metal to the reduction furnace at a mass flow rate of copper approximately three-times the mass flow rate of sulfur; reducing the zinc sulfide to zinc according to the equation ZnS.sub.(l)+2Cu.sub.(l).fwdarw.Cu.sub.2S.sub.(l)+Zn.sub.(g); and fuming the zinc; wherein sulfur is absorbed into the copper metal in the reduction furnace to form a copper sulfide molten matte. The partial pressure of SO.sub.2 in the furnace is maintained below about 10.sup.3 atm and the reduction furnace is operated at a temperature of between about 1240 and about 1300 C.

A method for obtaining metals of the 8th to 14th groups, in particular raw copper, comprises the following steps: i) providing and melting down a mixed feed comprising electronic waste in a smelting reactor, so that a first melt with a first metallic phase and a first slag phase is formed; ii) separating out the first slag phase from the smelting reactor; iii) refining the remaining first metallic phase by means of an oxygen-containing gas, possibly with the addition of copper-containing residual materials, so that a second, copper-enriched slag phase is formed; iv) possibly separating off the second slag phase and repeating the step; v) separating off the refined first metallic phase from the smelting reactor; and vi) adding a further mixed feed comprising electronic waste to the remaining second, copper-enriched slag phase and repeating process steps i) to vi).