Modeling purification of phosphoric acid contaminated with cadmium by liquid-liquid extraction

被引:15
作者
Boulkroune, N. [1 ]
Meniai, A. H. [1 ]
机构
[1] Univ Mentouri Constantine, LIPE, Dept Chim Ind, Constantine, Algeria
来源
TERRAGREEN 2012: CLEAN ENERGY SOLUTIONS FOR SUSTAINABLE ENVIRONMENT (CESSE) | 2012年 / 18卷
关键词
Phosphoric acid; Solvent extraction; Purification; Wet process; Dodecane;
D O I
10.1016/j.egypro.2012.05.134
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Phosphoric acid production is considered as second worldwide after that of sulphuric acid. It is an important and necessary intermediate chemical compound in sensitive industrial fields such as the fertilizers, detergents, food, pharmaceutical industries. Its main production is through the wet process which is responsible for the presence of various impurities like metallic cations such as Pb-2 (+), Cd-2 (+), Mg-2 (+), etc, initially contained in the phosphate rocks. Indeed many techniques for the purification of phosphoric acid have been developed. In this work the modeling of the purification of phosphoric acid by liquid-liquid extraction was considered. The model was tested on Cd-2 (+) as contaminant and di (2ethylhexyl) dithiophosphoric acid diluted in dodecane as complexing agent. The results obtained from a parametric study investigating the effect of the initial concentrations of phosphoric acid and that of the complexing agent, are reported. (C) 2012 Published by Elsevier Ltd. Selection and/or peer review under responsibility of The TerraGreen Society.
引用
收藏
页码:1189 / 1198
页数:10
相关论文
共 8 条
[1]  
Bendada A., 2001, CHEM ENG, V24, P1273
[2]   A SIMPLE NUMERICAL-METHOD FOR SOLVING COMPLEX EQUILIBRIA [J].
DEVORE, JA .
JOURNAL OF CHEMICAL EDUCATION, 1988, 65 (10) :868-870
[3]   Extraction of Al(III) from phosphoric acid by HDDNSA [J].
ElKhaiary, MI .
SEPARATION AND PURIFICATION TECHNOLOGY, 1997, 12 (01) :13-16
[4]  
Mellah A., CHEM ENG PROCESSING, V45, P684
[5]   Elimination of cadmium from wet process phosphoric acid with Alamine 336 [J].
Nazari, K ;
Ghadiri, A ;
Babaie, H .
MINERALS ENGINEERING, 2005, 18 (13-14) :1233-1238
[6]   CALCULATION OF VAPOR-LIQUID-EQUILIBRIA IN NITRIC-ACID WATER NITRATE SALT SYSTEMS USING AN EXTENDED UNIQUAC EQUATION [J].
SANDER, B ;
RASMUSSEN, P ;
FREDENSLUND, A .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (05) :1185-1195
[7]  
STAS J, 1990, B SOC CHIM FR, P360
[8]   Extraction of cadmium (II) from phosphoric acid media using the di(2-ethylhexyl) dithiophosphoric acid (D2EHDTPA): Feasibility of a continuous extraction-stripping process [J].
Touati, M. ;
Benna-Zayani, M. ;
Kbir-Ariguib, N. ;
Trabelsi-Ayadi, M. ;
Buch, A. ;
Grossiord, J. L. ;
Pareau, D. ;
Stambouli, M. .
HYDROMETALLURGY, 2009, 95 (1-2) :135-140