Comparative study of the application of chelating resins for rare earth recovery

Author:

Page Michael J.,Soldenhoff Karin,Ogden Mark D.

Publisher

Elsevier BV

Subject

Materials Chemistry,Metals and Alloys,Industrial and Manufacturing Engineering

Reference40 articles.

1. In-line extraction of REE from dihydrate (DH) and hemidihydrate (HDH) wet processes;Al-Thyabat;Hydrometallurgy,2015

2. Anon (n.d.) For the adsorption of any trivalent metal ion where the resin capacity occupied is small D=K.[H+]−3, where K is the adsorption constant. Using the values at 50% adsorption we can substitute for K to yield D=D50.[H+]503.[H+]−3. Therefore the separation factor for two trivalent metal ions may be calculated as the cube of the ratio of their [H+]50 values (note D50, which is only proportional to the aqueous:resin ratio, and [H+] is equivalent for both ions).

3. Recycling of rare earths: a critical review;Binnemans;J. Clean. Prod.,2013

4. Process for Recovering Rare Earth Oxides From Phosphors, Fluorescent Lamps and Light Bulbs, Cathode Ray Tubes and Other Industrial Wastes. WO2014071510A1;Cardarelli,2014

5. Global rare earth resources and scenarios of future rare earth industry;Chen;J. Rare Earths,2011

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