2020
DOI: 10.1016/j.jcou.2019.10.008
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Extraction of neodymium from hard disk drives using supercritical CO2 with organic acids solutions acting as cosolvents

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Cited by 14 publications
(3 citation statements)
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“…The impact of various factors on the chelation of metals with TTA-TBP exhibits the dependence of temperature, pressure and contact time [97]. Reisdo ¨rfer et al [100] reported the use of supercritical CO 2 with organic acids as cosolvents for the recovery of Nd from the hard disk drives. The extraction of the unroasted powder with supercritical CO 2 , at 90 °C and 120 bar gave rise to 50.5 % and 99.4 % Nd recovery efficiency after 30 min, using citric and malic acid, respectively.…”
Section: Pyrometallurgymentioning
confidence: 99%
See 1 more Smart Citation
“…The impact of various factors on the chelation of metals with TTA-TBP exhibits the dependence of temperature, pressure and contact time [97]. Reisdo ¨rfer et al [100] reported the use of supercritical CO 2 with organic acids as cosolvents for the recovery of Nd from the hard disk drives. The extraction of the unroasted powder with supercritical CO 2 , at 90 °C and 120 bar gave rise to 50.5 % and 99.4 % Nd recovery efficiency after 30 min, using citric and malic acid, respectively.…”
Section: Pyrometallurgymentioning
confidence: 99%
“…Supercritical CO 2 was extremely helpful to recover Nd from the unroasted powder using malic acid, reducing the extraction time from 360 min to 30 min. For the roasted NdFeB powder, it was possible to extract 99.5 % of the Nd after 120 min with the use of supercritical CO 2 and malic acid, while maximum recovery was achieved with atmospheric leaching was only 21.0 % even after 360 min [100]. The static and dynamic extraction of Nd from Nd 2 O 3 were investigated with the TBP-HNO 3 complex in sc-CO 2 .Static extraction was 94.69 % with 4.54 M acid at 323.15 K and 15 MPa after 2 h while in case of dynamic extraction efficiency was 97.68 % at 323.15 K and 21 MPa after 3 h with 2.52 M acidity.…”
Section: Pyrometallurgymentioning
confidence: 99%
“…If, however, more purification or elemental separation must be performed, additional process steps are required such as: (i) chlorination using safer agents such as NH 4 Cl [220,221]; (ii) advanced leaching [222][223][224][225][226][227][228][229][230][231][232][233][234][235][236]; (iii) or even bioleaching using bacteria which avoids the use of strong acids [237]; (iv) hydrometallurgy (solid-liquid or liquid-liquid extraction) [15,210,[238][239][240][241][242][243][244]; as well as (v) electrodeposition at the reduction step, including in ionic liquids [245][246][247][248][249][250][251][252][253] and molten salts [254][255][256][257][258][259], with their wide electrochemical stability [260].…”
Section: Rare-earth Elementsmentioning
confidence: 99%