The effects of temperature and pH on rheological characteristics of coalwater slurry (CWS) were investigated. With regard to effect of temperature, the experiments were carried out using a thermal cup at different temperatures in the range from 100 to 200 F (37.8 to 93.3C). The studied pH range of slurry was from pH 2 to pH 12. The apparent viscosity and non-Newtonian …
WhatsApp: +86 18221755073The kinetics and mechanism of leaching of the key minerals are reviewed together with methods for enhancing nickel recovery. Existing and developing AL processes for …
WhatsApp: +86 182217550731. Introduction. Dairy slurry is an important plant nutrient source on farms, supplying partial or total requirement for grass fertilisation. However, mismanagement, such as high application rate or inappropriate application time during the year, can lead to nutrient losses to the wider environment (Smith and Chambers, 1993).In dairy production systems one of the …
WhatsApp: +86 18221755073Nickel and cobalt extraction from limonite ore will be leached with high-pressure sulfuric acid. Leaching limonite ore with sulfuric acid is selective in temperature and high pressure. The first plant for high-pressure acid leaching (HPAL) of laterite …
WhatsApp: +86 18221755073Methods of processing low-grade laterite ores resulting in high purity leaching products are currently being explored due to the rapid depletion of high-grade ores. In this study, reduction pre-treatment is conducted prior to the atmospheric leaching of limonitic laterite ore to produce a nickel-cobalt-scandium-rich leach solution and iron-rich ...
WhatsApp: +86 18221755073The characteristics of the compound in the extraction process using High Pressure Acid Leaching (HPAL) and Sulfation-Roasting-Leaching (SRL) methods are similar to the dominance of Hematite (Fe 2 O 3) and Fe content > 40%. Atmospheric leaching (AL) residues are dominated by compounds in the form of the mineral Fayalite with a high Si …
WhatsApp: +86 18221755073Leaching temperature, leaching duration, sulfuric acid to ore weight ratio and particle size of the limonitic nickel laterite ore were studied. Optimum parameters determined as 255 o C, 0.30 sulfuric acid to ore weight ratio, a particle size of −850μ, 1 h of leaching duration with 30% w/w. 87.3% of Ni and 88.8% of Co in the ore extracted into the PLS but, …
WhatsApp: +86 18221755073A key step in the hydrometallurgical processing of nickel laterites is the partial neutralisation of the leached slurry or pregnant leach solution (PLS) to neutralise free sulfuric …
WhatsApp: +86 18221755073autothermally, and the temperature of the leach slurry is set by the amount of heat released by the leaching reaction. Heat is not added to the leaching vessel from external sources, and excess heat generated from the oxidation process is removed through humidification of the vessel off gases. 2. Ultrafine Grinding and the IsaMill™ Technology
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WhatsApp: +86 18221755073Metals 2021, 11, 1335 4 of 14 oxygen gas was injected at 2 MPa into the slurry to provide an oxidative environment. The leaching duration was set to 1 h.
WhatsApp: +86 18221755073The pregnant leach solution (PLS) obtained from a nickel laterite heap leach exhibits some significant differences to a HPAL discharge slurry. HPAL produces a hot slurry, at 20-25% …
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WhatsApp: +86 18221755073Precipitation of scandium from pregnant leach solution of high-pressure acid leaching of nickel laterite ore and its re-leaching behavior from the precipitate ... of 99.81, 42.88, 36.66, and 99.88%, respectively. The best condition for Sc re-leaching was obtained at a leaching duration of 90 minutes, temperature 35°C, H 2 SO 4 concentration ...
WhatsApp: +86 18221755073The free acidity of the PLS was determined by titration using 1.0 M sodium hydroxide (NaOH) solution and 0.1% Methyl Orange (C14H14N3NaO3S). Table 2 The changes of slurry pH before and after high‒pressure leaching and the free acidity of pregnant leach solutions under different sulfuric acid concentrations. 2.2.2.
WhatsApp: +86 18221755073The removal of trivalent iron and aluminum was studied from synthetic Li-ion battery leach solution by phosphate and hydroxide precipitation (pH 2.5–4.25, t = 3 h, T = 60 °C).
WhatsApp: +86 18221755073This method can achieve high nickel recovery with low acid consumption compared to atmospheric leaching. The temperature used in the HPAL process is around 250 C with about 4 MPa with the autoclave system. The problem appears with HPAL residue due to the huge quantity of residue, limited space and high maintenance disposal dam.
WhatsApp: +86 18221755073Mixing of H 2 S, H 2 SO 3, etc. in the steam and hot water of a DHR well can easily corrode the pipe materials and the well-stabilization slurry. A high-temperature sulfur-corrosion-resistant slurry system containing HTR2000 (retarder) (density 1.86 g/cm 3, initial consistency 12 Bc, consistency time 252 min, water loss 23 mL in 30 min (API ...
WhatsApp: +86 18221755073The evaluation of engineering and temperature resistance of the cement slurry proves the rationality of the accumulation model, which can be applied to the design of a high temperature cementing ...
WhatsApp: +86 18221755073Feeding laterite nickel slurry into high pressure acidleach (HPAL) autoclaves in an aggressive environment with slurries heated up to 200°C requires a special pump design. For decades the piston diaphragm pumps have been used for autoclave feeding at gold ore pressure oxidation plants with slurries up to l 77°C.
WhatsApp: +86 18221755073Heap Leaching. Heap leaching is a process that grinds gold mine with low grade to certain particles, heap upon the leakage-proof bottom mat that is concreted by pitch, concrete or plastic cloth, spray the low concentration cyanide solution, alkaline solution, nontoxic solvent, dilute sulphuric acid on the stock heap, make the gold dissolve, the solution with gold heap up, then …
WhatsApp: +86 18221755073The leaching experiments were conducted in a 0.5 L digestor coupled with mechanical agitation and a stirring speed of 400 rpm. For each experiment, a pulp with 2.5 to …
WhatsApp: +86 18221755073Temperature Higher temperatures will increase the rate of gold dissolution, however it is not economical to heat the slurry. High temperatures also reduce the capacity of carbon to adsorb gold and lower the solubility of oxygen in the slurry. Therefore leaching and adsorption is conducted at ambient temperatures.
WhatsApp: +86 18221755073The abundant resources of steel slag make it an intriguing prospect for long-term CO 2 storage by mineral carbonation. Herein, the dissolution of steel slag in an acetic acid (HAc) solution and the fixation of CO 2 in the leachate of steel slag to synthesize high-value CaCO 3 were investigated. Results show that the microwave water bath condition is beneficial for …
WhatsApp: +86 18221755073High pressure acid leaching of a refractory lateritic nickel ore S. Kaya, Y.A. Topkaya Department of Metallurgical and Materials Engineering, Middle East Technical University (METU), 06531 Ankara ...
WhatsApp: +86 18221755073After leaching, a solid–liquid separation step, such as countercurrent decantation or filtration with cake washing, is applied to the leach slurry to separate the solid residue from the pregnant …
WhatsApp: +86 18221755073The leaching process may employ one of a variety of chemicals such as dilute sulfuric acid, dilute aqueous cyanide, or other reagents. Methods for contacting ore and solution include agitating ground solids and solution (slurry) in open tanks, agitating slurry at a high temperature in a pressure vessel, or percolating solution through crushed ore that has been piled in a heap
WhatsApp: +86 18221755073The key findings of the IX/SX process are; (1) recovery of copper from pregnant leach solutions with metal concentrations, varying on a broad range; (2) can be operate effectively with very low ...
WhatsApp: +86 18221755073The pregnant leach solution (PLS) obtained from a nickel laterite heap leach exhibits some significant differences to a HPAL discharge slurry. HPAL produces a hot slurry, at 20-25% solids,
WhatsApp: +86 18221755073Abstract: Results of an analysis of the operating data of an ash leaching system show that the sys- tem removed 90% of the chloride (Cl) and 82% of the potassium (K) introduced to the system with ...
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