2023
DOI: 10.3390/met13020356
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Application of the Microwave and Ultrasonic Combined Technique in the Extraction of Refractory Complex Zinc Ore

Abstract: This paper proposes a combined microwave and ultrasonic technique that aims to extract the refractory mineralogical properties of complex zinc ore. This technique consists of two steps: microwave-assisted phase transformation and ultrasonic-assisted complexation leaching. During the microwave-assisted phase transformation step, the refractory zinc phases transform into manageable phases using doping oxidation agents. In the ultrasonic-assisted complexation leaching step, the effect of NTA3 on Zn2+ species dist… Show more

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Cited by 3 publications
(1 citation statement)
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“…The technology for extracting zinc from clinker comprises three main stages: grinding the clinker to 90% of the -0.071 + 0 mm size fraction, microwave phase transformation, and leaching with H 2 SO 4 . The steps, depicted in Figure 1, include sample preparation; firing of the clinker in the high-temperature microwave reactor of the "ENERGY K-50" unit (Ust-Kamenogorsk, Kazakhstan) (915 MHz, 25 kW), which is advantageous for its high power, stable operation [25][26][27][28][29], and increased efficiency; and the subsequent leaching of the clinker (Figure 2). The leaching of the clinker was conducted in an H 2 SO 4 solution with a concentration of 100 g/dm 3 for 6 h at a stirring speed of 300 rpm, a solid to liquid ratio of 1:5, and a temperature of 293 K. solution with a concentration of 100 g/dm³ for 6 h at a stirring speed of 300 rpm, a solid to liquid ratio of 1:5, and a temperature of 293 K.…”
Section: Methodsmentioning
confidence: 99%
“…The technology for extracting zinc from clinker comprises three main stages: grinding the clinker to 90% of the -0.071 + 0 mm size fraction, microwave phase transformation, and leaching with H 2 SO 4 . The steps, depicted in Figure 1, include sample preparation; firing of the clinker in the high-temperature microwave reactor of the "ENERGY K-50" unit (Ust-Kamenogorsk, Kazakhstan) (915 MHz, 25 kW), which is advantageous for its high power, stable operation [25][26][27][28][29], and increased efficiency; and the subsequent leaching of the clinker (Figure 2). The leaching of the clinker was conducted in an H 2 SO 4 solution with a concentration of 100 g/dm 3 for 6 h at a stirring speed of 300 rpm, a solid to liquid ratio of 1:5, and a temperature of 293 K. solution with a concentration of 100 g/dm³ for 6 h at a stirring speed of 300 rpm, a solid to liquid ratio of 1:5, and a temperature of 293 K.…”
Section: Methodsmentioning
confidence: 99%