2022
DOI: 10.1016/j.chemosphere.2021.132020
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Acid leaching of LiCoO2 enhanced by reducing agent. Model formulation and validation

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Cited by 27 publications
(15 citation statements)
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“…The detailed process is shown in Scheme 1. As reported, 19,40 the mole ratio of Li to Co (Li/Co) is usually higher than unity. In this work, Li/Co for dcPEG is also beyond unity at the relatively low temperature (Figure S8).…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…The detailed process is shown in Scheme 1. As reported, 19,40 the mole ratio of Li to Co (Li/Co) is usually higher than unity. In this work, Li/Co for dcPEG is also beyond unity at the relatively low temperature (Figure S8).…”
Section: ■ Results and Discussionmentioning
confidence: 99%
“…[24][25][26] The leaching process of LCO with H 2 O 2 in the acidic medium can be summarized as follows. 27 LiCoO 2 + 3H + + 1/2H 2 O 2 $ Li + + Co 2+ + 2H 2 O + 1/2O 2 (1) The recovery of cobalt as Co(OH) 2 , CoCO 3 , and LCO during leaching has been the subject of numerous investigations published in the literature. 3,[28][29][30] A new technique for recycling LCO involves cobalt leaching and precipitation as cobalt sulfide, which can be utilized as a supercapacitor electrode material.…”
Section: Introductionmentioning
confidence: 99%
“…24–26 The leaching process of LCO with H 2 O 2 in the acidic medium can be summarized as follows. 27 LiCoO 2 + 3H + + 1/2H 2 O 2 ⇄ Li + + Co 2+ + 2H 2 O + 1/2O 2 …”
Section: Introductionmentioning
confidence: 99%
“…Conventional hydrometallurgical processing involves the leaching of Li and Co in both inorganic , and organic acids, and recently, deep eutectic solvents (DES) are also reported. , A complex layered structure, and high valence of Co (+3) in the LCO substrate require expensive external reductants (such as H 2 O 2 and ascorbic acid), extended leaching time, , followed by solvent extraction or precipitation . Recently, a novel process of simultaneous leaching and precipitation of LCO as cobalt tartrate using tartaric acid and H 2 O 2 reductant has been reported .…”
Section: Introductionmentioning
confidence: 99%
“…Also, the water leaching time (2 h) for the recovery of LiOH was very high, whereas the recovery of Li (43%) and Co (83%) was low. 16 Conventional hydrometallurgical processing involves the leaching of Li and Co in both inorganic 17,18 and organic acids, 19−21 and recently, deep eutectic solvents (DES) are also reported. 22,23 A complex layered structure, and high valence of Co (+3) in the LCO substrate require expensive external reductants (such as H 2 O 2 and ascorbic acid), extended leaching time, 24,25 itation.…”
Section: Introductionmentioning
confidence: 99%