Calculation of Light to Medium Rare Earth Solvent Extraction Processes Optimal Extraction Ratio Theory

2018 ◽  
Vol 23 (2) ◽  
pp. 65-72
Author(s):  
Seong-Hoon Moon ◽  
2013 ◽  
Vol 30 (10) ◽  
pp. 1946-1953 ◽  
Author(s):  
Kyung Hwan Ryu ◽  
Changkyu Lee ◽  
Go-Gi Lee ◽  
Sungkoo Jo ◽  
Su Whan Sung

2017 ◽  
Vol 50 (9) ◽  
pp. 716-726
Author(s):  
Chan Yeong Yun ◽  
Kyung Hwan Ryu ◽  
Changkyu Lee ◽  
Go-Gi Lee ◽  
Sungkoo Jo ◽  
...  

2016 ◽  
Vol 159 ◽  
pp. 40-45 ◽  
Author(s):  
Chan Yeong Yun ◽  
Changkyu Lee ◽  
Go-Gi Lee ◽  
Sungkoo Jo ◽  
Su Whan Sung

1998 ◽  
Vol 275-277 ◽  
pp. 940-943 ◽  
Author(s):  
Chunhua Yan ◽  
Jiangtao Jia ◽  
Chunsheng Liao ◽  
Biaoguo Li ◽  
Wenli Li ◽  
...  

Minerals ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 61
Author(s):  
Wenjie Zhang ◽  
Xian Xie ◽  
Xiong Tong ◽  
Yunpeng Du ◽  
Qiang Song ◽  
...  

Solvent extraction is the most widely used method for separation and purification of rare earth elements, and organic extractants such as di(2-ethylhexyl) phosphoric acid (P204) and di(1-methyl-heptyl) methyl phosphonate (P350) are most commonly used for industrial applications. However, the presence of impurity ions in the feed liquid during extraction can easily emulsify the extractant and affect the quality of rare earth products. Aluminum ion is the most common impurity ion in the feed liquid, and it is an important cause of emulsification of the extractant. In this study, the influence of aluminum ion was investigated on the extraction of light rare earth elements by the P204-P350 system in hydrochloric acid medium. The results show that Al3+ competes with light rare earths in the extraction process, reducing the overall extraction rate. In addition, the Al3+ stripping rate is low and there is continuous accumulation of Al3+ in the organic phase during the stripping process, affecting the extraction efficiency and even causing emulsification. The slope method and infrared detection were utilized to explore the formation of an extraction compound of Al3+ and the extractant P204-P350 that entered the organic phase as AlCl[(HA)2]2P350(o).


Minerals ◽  
2021 ◽  
Vol 11 (4) ◽  
pp. 388
Author(s):  
Silvester Jürjo ◽  
Liis Siinor ◽  
Carolin Siimenson ◽  
Päärn Paiste ◽  
Enn Lust

Estonian phosphorite ore contains trace amounts of rare earth elements (REEs), many other d-metals, and some radioactive elements. Rare earth elements, Mo, V, etc. might be economically exploitable, while some radioactive and toxic elements should be removed before any other downstream processing for environmental and nutritional safety reasons. All untreated hazardous elements remain in landfilled waste in much higher concentration than they occur naturally. To resolve this problem U, Th, and Tl were removed from phosphorite ore at first using liquid extraction. In the next step, REE were isolated from raffinate. Nitrated Aliquat 336 (A336[NO3]) and Bis(2-ethylhexyl) Phosphate (D2EHPA) were used in liquid extraction for comparison. An improved method for exclusive separation of radioactive elements and REEs from phosphorite ore in 2-steps has been developed, exploiting liquid extraction at different pH values.


2021 ◽  
Vol 50 (5) ◽  
pp. 1620-1630
Author(s):  
Alexiane Thevenet ◽  
Ana Miljkovic ◽  
Sonia La Cognata ◽  
Cécile Marie ◽  
Christelle Tamain ◽  
...  

New azacryptands with the addition of hydrophilic groups were synthesized to bind selectively the pertechnetate anion in nitric acid medium, and avoid its extraction in the separation process.


1948 ◽  
Vol 20 (8) ◽  
pp. 740-743 ◽  
Author(s):  
H. A. Bewick ◽  
J. E. Currah ◽  
F. E. Beamish

1997 ◽  
Vol 17 (1-4) ◽  
pp. 205-226 ◽  
Author(s):  
GEOFFREY W. STEVENS ◽  
JILSKA M. PERERA

Sign in / Sign up

Export Citation Format

Share Document