2024
DOI: 10.1016/j.cjche.2024.01.006
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Facile molybdenum and aluminum recovery from spent hydrogenation catalyst

Zhenhui Lv,
Jianan Li,
Dong Xue
et al.
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Cited by 2 publications
(2 citation statements)
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“…Since the leaching paths of NaAlO 2 and NiO in the roasting product overlap with that of molybdenum, which also occurs in pyrometallurgical and biometallurgical recovery routes, further means for separating Mo are necessary. 7,8 Solvent extraction, ion exchange, and adsorption are feasible approaches. Based on the fact that Mo exists as anions (MoO , and H 2 Mo 7 O 24 4− ) in weakly acidic to alkaline solutions, primary-/tertiary-/quaternary-amine, organo-phosphoric, amine resins, and bifunctional ionic liquids have effectively extracted Mo.…”
Section: ■ Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Since the leaching paths of NaAlO 2 and NiO in the roasting product overlap with that of molybdenum, which also occurs in pyrometallurgical and biometallurgical recovery routes, further means for separating Mo are necessary. 7,8 Solvent extraction, ion exchange, and adsorption are feasible approaches. Based on the fact that Mo exists as anions (MoO , and H 2 Mo 7 O 24 4− ) in weakly acidic to alkaline solutions, primary-/tertiary-/quaternary-amine, organo-phosphoric, amine resins, and bifunctional ionic liquids have effectively extracted Mo.…”
Section: ■ Introductionmentioning
confidence: 99%
“…Among hydrometallurgical routes, to drive the Mo present as MoS 2 /MoO x in spent HDS catalysts into the aqueous phase maximally, roasting assisted by sodium salts becomes an enabler for reconstruction of Mo phase into a soluble salt. Since the leaching paths of NaAlO 2 and NiO in the roasting product overlap with that of molybdenum, which also occurs in pyrometallurgical and biometallurgical recovery routes, further means for separating Mo are necessary. , Solvent extraction, ion exchange, and adsorption are feasible approaches. Based on the fact that Mo exists as anions (MoO 4 2– , Mo 7 O 24 6– , HMo 7 O 24 5– , and H 2 Mo 7 O 24 4– ) in weakly acidic to alkaline solutions, primary-/tertiary-/quaternary-amine, organo-phosphoric, amine resins, and bifunctional ionic liquids have effectively extracted Mo. Subsequently, stripping/elution and evaporation-crystallization processes are indispensable for recovery.…”
Section: Introductionmentioning
confidence: 99%