Silver extraction by percolation leaching on a pelletized sample of stale tailings with the organic binding agent Alcotac® CB6 is studied. A column 0.5 m high and 56 mm in internal diameter was used for laboratory tests on percolation leaching. Pelletization was carried out in a drum-type granulator with the Alcotac® CB6 reagent (BASF, Germany) consumption of 800 g/t; the moisture content of the granules was 8–10% with a size of 8–10 mm. The composition of the samples was determined based on the data of optical and electron microscopy, X-ray diffraction, local X-ray spectral, X-ray fluorescence, and mass spectrometry with inductively coupled plasma. Stale tailings of the Zhezkazgan enrichment plant (Ulytau region, Republic of Kazakhstan) were examined, in which the main part of copper is represented by oxidized minerals (78.47%); content of sulfide minerals is 21.53%. The results of physicochemical studies with the determination of the material composition of the sample and observations on the percolation leaching of copper and silver from the stale tailings of Zhezkazgan are presented. The copper leaching was studied in two stages using a sulfuric acid solution as a solvent. The next stage was the transfer of silver into the solution by cyanidation. Copper extraction into the solution was 88.55% with a sulfuric acid consumption of 80.0 kg/t of tailings, and that of silver was 75.31% with a sodium cyanide consumption of 0.55 kg/t. The studies of two-stage leaching showed the effectiveness of preliminary pelletizing of stale tailings with the Alcotac® CB6 reagent. In the process of leaching, the pelletized material features sufficient porosity and permeability and provides access of cyanide solutions to the surface of precious metals.
Hot compression tests were conducted on an ultrahigh-alloyed Al–Zn–Mg–Cu alloy within a temperature range of 250 to 450°C and a strain rate range of 0.001 to 1 s–1. The effects of strain rate and temperature on the flow curves were analyzed, along with the relationship between flow stress and microstructural evolution. The results indicate that, except for a strain rate of 1 s–1 across all temperatures, the flow curves following the peak stress do not exhibit monotonic work hardening or dynamic softening. In contrast, continuous work hardening is observed at this strain rate. The diverse shapes of the flow curves are attributed to the various precipitates formed due to the high alloying element content. Dynamic recovery (DRV) is identified as the main flow softening mechanism for the ultrahigh-alloyed Al–Zn–Mg–Cu alloy. While dynamic recrystallization (DRX) contributes to flow softening at a strain rate of 0.001 s–1, the deformed microstructure becomes the predominant softening mechanism at lower temperatures and higher strain rates. Additionally, the low intensity of isotropic texture at higher temperatures and strain rates facilitates DRX, resulting in a decrease in peak stress.
The objective of this work was to investigate the selected properties of particleboard (PB) containing waste rubber – a mixture of carpets and isolators (GWR) and tires (GWT) from discarded automobiles. Mechanical (tensile strength (IB), bending strength (BS), physical (water absorption (WA), thickness swelling (TS) after 2 and 24 h of immersion), chemical (volatile compounds - VOC using GC-MS method), thermo-physical (thermal conductivity and diffusivity, specific heat capacity) and sound absorption coefficient were analyzed. In addition, a density profile and microscopic analysis of the particleboards were performed. The addition of 10% rubber to the PB either maintains the IB or improves the BS of the composite. The best results for WA after 24 h (97.94%) and TS after 24 h (30.74%) were achieved for composites containing tire granulates. For this reason, these PBs are the most suitable for utilization in areas with higher humidity. Adding 20% of GWR to PB decreased the total content of VOC emissions by 85% so it can be stated that the rubber probably acts as a VOC sorbent. Control PBs had significantly lower thermal conductivity and diffusivity, and comparable specific heat capacity values than PBs containing GWR and GWT. The best sound insulation properties were obtained for PBs containing 20% of GWR. Microscopic analysis pointed to greater GWT and GWR contents resulting in higher C content in the PB. All PBs containing GWR have a higher mean density compared to that of control, ranging from 597 kg·m−3 to 615 kg·m−3. On the other hand, PB containing GWT had comparable or lower density values.
The aim is to conduct research in the field of hydrometallurgical refining of metallurgical silicon. The object of research was metallurgical silicon after oxidative refining from AO Kremnii, part of the United Company RUSAL (Shelekhov, Irkutsk oblast, Russia). The chemical composition of the obtained samples was studied by X-ray fluorescence analysis and X-ray spectral microanalysis. According to elemental analysis, metallurgical silicon contains (wt %) 0.53Al, 0.6094Fe, 0.0491Ti, 0.0628Ca, 0.0066V, 0.002Cr, 0.014Mn, 0.003Cu, 0.010P, 0.007Ba, 0.007Ni, 0.002Zn. It is shown that intermetallic compounds of the following composition were recorded in the studied samples: AlFeSi2 (with an admixture of Ca), FeSi2 (with an admixture of Al), FeSi2Ti (with an admixture of Zr). To reduce the content of impurities in silicon, we selected the following acids as solvents: 10% H2SO4, HCl, and HNO3, as well as 4% HF in various ratios. To study the possibility of reactions of interaction of intermetallic compounds with selected solvents, the values of the Gibbs energy change, which had negative values, were calculated. Experimental leaching of impurities was conducted on silicon samples with particle sizes of –200 μm under constant stirring using a magnetic stirrer. The process parameters included a temperature of 60°C, a liquid-to-solid ratio of 5 : 1, and a purification duration of 60 min. It was found that using a solvent mixture of sulfuric and hydrofluoric acids in a 1 : 1 ratio achieved the highest degree of silicon purification, with an impurity removal rate of 86.85%. It is shown that when using a mixture of sulfuric and hydrochloric acids in a ratio of 1 : 3, the degree of purification of metallurgical silicon was 41.48%. In this way, solvents that enable maximum purification of silicon from impurity elements were identified.