2022
DOI: 10.1016/j.jre.2020.11.021
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Leaching recovery of rare earth elements from the calcination product of a coal coarse refuse using organic acids

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Cited by 45 publications
(9 citation statements)
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References 38 publications
(49 reference statements)
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“…The introduction of organic matter leads to a sharp acceleration of the process of the transition of REE into the solution. Similar results were obtained in [ 75 , 76 ], where the studied materials—tailings, ore containing REE—were leached with separate organic acids. The total increase in the mass of dissolved REE is proportional to the increase in the introduced organic matter.…”
Section: Resultssupporting
confidence: 85%
“…The introduction of organic matter leads to a sharp acceleration of the process of the transition of REE into the solution. Similar results were obtained in [ 75 , 76 ], where the studied materials—tailings, ore containing REE—were leached with separate organic acids. The total increase in the mass of dissolved REE is proportional to the increase in the introduced organic matter.…”
Section: Resultssupporting
confidence: 85%
“…Acid leaching is an efficient, economical, and widely used process in the rare metal metallurgical industry and has an absolutely necessary role in rare earth recovery from coal fly ash. Hence, the leachability of rare earth in the three samples was evaluated using mineral acid (HCl acid) and organic acid (citric acid) at the specific conditions verified in previous research [ 22 , 23 , 24 , 45 ]. On the whole, the recovery of REY using HCl acid is higher than that using citric acid from Figure 8 .…”
Section: Resultsmentioning
confidence: 99%
“…Acid leaching is a process for metal extraction from primary and secondary resources and is also used for the identification of metal leaching ability at specific conditions. The REY leaching ability was defined by hydrochloric acid and citric acid (as a proxy for mineral and organic acid leaching) under measurable conditions based on the reported literature [ 22 , 23 , 24 ]. The hydrochloride acid leaching was performed in the beaker with the conditions: T = 60 °C, the concentration of 3 M, the liquid–solid ratio of 10 (volume/mass, v / m ), leaching time of 120 min, and magnetic stirring speed of 200 rpm.…”
Section: Methodsmentioning
confidence: 99%
“…The reaction temperature was controlled using a water bath, while solid/ liquid mixing was achieved using a magnetic stirrer. Detailed descriptions of the leaching apparatus have been published previously [19,22]. For each test, 2.5-g solid was mixed with 250-mL HCl solution of 1.2 M, and the reaction temperature was fixed at 75 • C. The leaching conditions were consistent with those used in the authors' prior studies on REE recovery from coal refuse [18,19,23].…”
Section: Acid Leaching Testsmentioning
confidence: 99%