In this thesis, a novel, low-energy process route for primary production of copper that utilises synergies between hydro-and pyro-metallurgical processes is proposed. The process involves precipitating copper from an acidic leach solution by pH adjustment. This precipitation step separates and concentrates the copper from the leach solution. The concentrated copper precipitate is then fed to a pyrometallurgical copper smelter or converter. Research on this process focused on four areas:• The copper phases produced by pH adjusted chemical precipitation from acidic solutions.• Factors affecting the kinetics of the copper precipitation step.• The thermal properties of the precipitated copper phases.• The mass and energy balance implications of feeding the precipitated copper product into a copper converter.The solubility of copper phases were determined by precipitating copper from solution and providing sufficient time for equilibrium to be established. In this study, the stabilities of precipitated copper oxide and basic copper sulphate, nitrate and chloride salts were determined over a pH range of 3 to 13 in solutions with ionic strength up to 3.5 M. The solubility products for the precipitated salts were calculated after taking into account the solution speciation, solution species activity coefficients and the surface energy associated with the fine particles. The standard Gibbs energy of formation of CuO tenorite, CuSO 4 .3Cu(OH) 2 brochantite, CuCl 2 .3Cu(OH) 2 clinoatacamite and Cu(NO ) 2 .3Cu(OH) 2 rouaite were estimated to be -124.9, -1,814.1, -1,341.6 and -1,278.5 kJ/mol respectively at 25°C.The copper precipitation kinetics and reaction mechanisms were then studied in the aqueous sulphate system, focusing on the use of limestone as the precipitation reagent. A range of precipitation conditions and reactor configurations were examined to determine which factors had significant effect on the rate of copper precipitation in this complex heterogeneous reaction system where limestone dissolution and co-crystallisation of brochantite and gypsum occur simultaneously. The rate of copper precipitation was initially limited by nucleation of the copper solid after which limestone dissolution was the limiting factor. The dissolution of limestone was dependent on the surface area of limestone, the concentration of copper and the hydrodynamic conditions within the reactor.