2016
DOI: 10.1016/j.minpro.2016.02.011
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Rare earths concentration from phosphogypsum waste by two-step leaching method

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Cited by 76 publications
(30 citation statements)
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“…Except for the time of leaching, the other reaction parameters have not been studied over continuous intervals (in general, fixing three arbitrary values to be tested for each parameter), which is one of the major gaps that we have avoided by the adoption of RSM [19,20]. Figure 6 of the 3D response surface curves shows that the main parameters having a significant influence on the rare earth leaching process adopted are the following: acid percentage, temperature, and S/L ratio.…”
Section: Ree-dimensional (3d) Response Surface and Isoresponse Curvesmentioning
confidence: 99%
See 1 more Smart Citation
“…Except for the time of leaching, the other reaction parameters have not been studied over continuous intervals (in general, fixing three arbitrary values to be tested for each parameter), which is one of the major gaps that we have avoided by the adoption of RSM [19,20]. Figure 6 of the 3D response surface curves shows that the main parameters having a significant influence on the rare earth leaching process adopted are the following: acid percentage, temperature, and S/L ratio.…”
Section: Ree-dimensional (3d) Response Surface and Isoresponse Curvesmentioning
confidence: 99%
“…e global desirability function D, which is taking into account both the requirements on all the responses Y i , is the geometric mean of the individual desirability d i . e desirability function varies in the interval [0, 1]; the value 1 corresponds to the maximum satisfaction (desired value) and 0 corresponds to an unacceptable response [19,21]. e maximum of the function D gives the best global compromise for all the responses in the studied domains and corresponds to optimal experimental conditions.…”
Section: Optimizationmentioning
confidence: 99%
“…The studies above showed that HCl and HNO 3 were more efficient agencies than H 2 SO 4 for leaching REEs from PG, but H 2 SO 4 was still industrially preferred because of economical reasons. A two-step leaching method was introduced with H 2 SO 4 as the lixiviant using a Tunisian PG [25]. The PG sample was firstly washed with distilled water and after solid-liquid separation underwent a double leaching with 10% H 2 SO 4 solution at 60˚C, for 1 -2 h of continuous stirring at L/S ratio of 1.3.…”
Section: Acid Leaching Of Rees From Pgmentioning
confidence: 99%
“…Because these wastes have very fine grain sizes and complex mineralogical compositions, the reprocessing of them for economic recovery of REEs becomes very challenging [3]. Research was carried out to verify whether the wastes might be useful as a raw material for REEs recovery [4][5][6][7][8][9][10][11][12] and the manufacture of building materials [1]. However, the extraction of REEs and other valuable elements from these wastes in phosphate processing has not been industrially realized, while trace elements are considered one of the main environmental concerns of direct use [13].…”
Section: Introductionmentioning
confidence: 99%