scholarly journals Ion exchange treatment of solution produced in acid leaching of uranium ore from Amalgamated Rare Earth Mines Limited, Bancroft, Ontario. Ref. No. 7/57-7

1958 ◽  
Author(s):  
E Kornelsen ◽  
V M McNamara
2016 ◽  
Vol 5 (1) ◽  
pp. 48-55
Author(s):  
Сеник ◽  
E. Senik ◽  
Виноградов ◽  
M. Vinogradov ◽  
Таранов ◽  
...  

Problems related to rare earth metals leaching from coal ash and theirs ion-exchange concentration from sulfuric solutions, in particular the characteristics of scandium, yttrium and lanthanum sorption by different ion exchange resins have been considered in this work. It has been shown that the best way to leach rare earth metals from coal ash is a complex acid and biological treatment of ash waste. Kinetics related to the process of scandium, yttrium and lanthanum acid leaching from ash and slag waste of CHPP in Kumertau has been investigated. Subsequent metal solutions concentration was achieved using ion exchange resins. The results of experimental studies related to the processes of rare-earth metals (in particularly scandium) ion exchange concentration by cation exchange resin in the Naform PC-100 have been presented, as well as the results of experimental studies related to rare earth metals (scandium including) sedimentation process, using special sedimentators. Dependences of rare earth metals (in particular scandium) sedimentation efficiency against pH value have been constructed, and recommendations for pH values, that are optimal for rare earth metals sedimentation, have been given. Based on obtained experimental results it was created and tested an experimental laboratory prototype of plant for rare earth metals (scandium, yttrium and lanthanum including) extraction from located near Moscow brown coal basin’s slag heaps, and from ash dumps of Russian Federation’s energy enterprises. This plant’s process flow diagram as well as its operation description has been presented. The created plant was tested in modes previously fulfilled in laboratory conditions. At the same time, carried out integrated exploration have showed the prospects for implementation of developed technical solutions for processing of ash dumps of Russian Federation’s various energy enterprises.


2016 ◽  
Vol 3 (1) ◽  
pp. 6-17 ◽  
Author(s):  
Peter L. Rozelle ◽  
Aditi B. Khadilkar ◽  
Nuerxida Pulati ◽  
Nari Soundarrajan ◽  
Mark S. Klima ◽  
...  

2017 ◽  
Vol 35 (12) ◽  
pp. 1255-1260 ◽  
Author(s):  
Genghong Shuai ◽  
Longsheng Zhao ◽  
Liangshi Wang ◽  
Zhiqi Long ◽  
Dali Cui

2015 ◽  
Vol 5 (2) ◽  
pp. 33-38
Author(s):  
Quang Thai Le ◽  
Minh Tuan Pham ◽  
Nguyen Quynh Trinh ◽  
Khac Tuan Vu ◽  
Hong Ha Nguyen ◽  
...  

Ion exchange is one of the most popular techniques for recovery and purification of uranium from sulfuric acid leaching solution, especially for recovery of uranium from a low uranium containing solutions. Resins commonly used are strong base or weak base anion resins with amine functional group. The anionic form of resins may be NO3-, Cl- , SO­42- or OH-. The selection of  a resin depends on the uranium total exchange capacity, selectivity and the cost. The previous studies often use Amberlite IRA-420 for concentration and purification of uranium solution from Pa Lua sandstone ores. This is a good and suitable resin but high price. To diversify the resins and reduce the costs, instead of IRA-420, the authors tested two commercial resins Indion GS300 (India) and Purolite A400 (UK) in the processing of uranium solution from sandstone ores. The results showed that the uranium total exchange capacity of  these resins is only about 80 - 85% over  Amberlite IRA-420, but these resins should be able to be used instead of Amberlite IRA-420 due to their low cost and availability in Vietnam.


Author(s):  
Zeinab Chour ◽  
Baptiste Laubie ◽  
Jean Louis Morel ◽  
Yetao Tang ◽  
Rongliang Qiu ◽  
...  

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