Dissolution of Calcareous Phosphate Rock from Gafsa (Tunisia) Using Dilute Phosphoric Acid Solution

In the present study, porous structure of raw and calcined phosphate ore particles was examined. The specific surface area and the pore volume were determined by nitrogen adsorption. Raw particles and calcined ores were leached using dilute phosphoric acid solution (4% P2O5). In all cases, the ESEM (Environmental Scanning Electron Microscopy) observations show that the grain of phosphate holds its shape ovoidale. The sample heated at 780?C presented the lowest specific surface area 0.6 m2/g at each reaction time, and the unreacted phases were analysed using XRD, FT-IR, Nitrogen adsorption and ESEM observations. The selective leaching curves were evaluated in order to test the validity of kinetics models. A mathematical model in the following form was applied. The dissolution of the two samples (raw and calcined phosphate) has been observed to take place in two steps: the first being fast and the second being slow.

[1]  K. L. Elmore,et al.  Solubility of Phosphates, Rates of Solution of Calcium Phosphates in Phosphoric Acid Solutions , 1957 .

[2]  E. E. Ouardia Étude de la calcination du phosphate clair de youssoufia (Maroc) , 2010 .

[3]  Z. Zafar,et al.  Selective leaching kinetics and upgrading of low-grade calcareous phosphate rock in succinic acid , 2005 .

[4]  M. Noaparast,et al.  Selective leaching kinetics of low-grade calcareous phosphate ore in acetic acid , 2009 .

[5]  M. Kocakerim,et al.  Dissolution Kinetics of Phosphate Ore in SO2-Saturated Water , 1994 .

[6]  Z. Zafar,et al.  Selective leaching kinetics of calcareous phosphate rock in lactic acid , 2007 .

[7]  B. Gumgum,et al.  The Enrichment of Low-Grade Mazidagi Phosphates by Calcination and Extraction Methods , 1987 .

[8]  A. Nzihou,et al.  Chemical and Structural Changes of Raw Phosphate during Heat Treatment , 2004 .

[9]  S. I. Abu-eishah,et al.  Beneficiation of calcareous phosphate rocks using dilute acetic acid solutions: optimisation of operating conditions for Ruseifa (Jordan) phosphate , 1991 .

[10]  A. Mgaidi,et al.  Exploration of mesoporous structure of tunisian raw and acid‐leached phosphate ore particles , 1997 .

[11]  Dissolution kinetics of phosphate rock with Cl2 gas in water , 1997 .

[12]  P. Blazy,et al.  Calcination du phosphate sédimentaire à gangue carbonatée d'Akashat (Irak) en four rotatif et en four éclair (Flash) , 1997 .

[13]  A. Özer,et al.  Beneficiation of Mardin-Mazıdaği (Turkey) calcareous phosphate rock using dilute acetic acid solutions , 2006 .

[14]  T. Vaimakis,et al.  The kinetics of dissolution of the carbonate minerals of phosphate ores using dilute acetic acid solutions: the case of pH range from 3.96 to 6.40. , 2002, Journal of colloid and interface science.