Mechanism and rate of butyl phosphinate formation from reaction of phosphinic acid (Cyanex 272) and tributyl phosphate

被引:6
作者
Barnard, K. R. [1 ]
Shiers, D. W. [1 ]
机构
[1] CSIRO Minerals Natl Res Flagship, Parker Ctr, CSIRO Proc Sci & Engn, Karawara, WA 6152, Australia
关键词
Cyanex; 272; Bis(2,4,4-trimethylpentyl)phosphinic acid; Butyl phosphinate; Butyl bis(2,4,4-trimethylpentyl)phosphinate; Tributyl phosphate; TBP; Murrin Murrin; EXTRACTION; RECOVERY;
D O I
10.1016/j.hydromet.2010.12.001
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
An impurity species, butylbis(2,4,4-trimethylpentyl)phosphinate ('butyl phosphinate'), has recently been identified in the Murrin Murrin solvent extraction (SX) circuits. The present work established that this species is formed via direct reaction between tributyl phosphate (TBP) and the phosphinic acid extractant found in Cyanex 272 and that the reaction is first order relative to the concentration of each reactant. The observations are consistent with the reaction progressing via a bimolecular nucleophilic substitution (S(N)2) mechanism whereby nucleophilic attack of substrate TBP by the phosphinic acid anion occurs, resulting in cleavage of the C-O bond and ejection of dibutyl phosphate anion. The butyl phosphinate formation rate has been determined under synthetic extract, strip and aqueous-free conditions, the latter at temperatures between 40 and 75 degrees C. In the absence of an aqueous phase, the rate coefficient was found to be 0.43 +/- 0.02 M(-1) per annum (95% confidence interval) at 70 degrees C with an activation energy of 122 kJ/mol. Based on the present data and historical SX plant operating information, a model to estimate annual butyl phosphinate generation and its build-up in the Murrin Murrin SX circuits over the last decade was developed. The estimated accrued level of 31 g/L butyl phosphinate by June 2009 is comparable to the measured 32-35 g/L (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:76 / 83
页数:8
相关论文
共 9 条
[1]   Identification and characterisation of a Cyanex 272 degradation product formed in the Murrin Murrin solvent extraction circuit [J].
Barnard, K. R. .
HYDROMETALLURGY, 2010, 103 (1-4) :190-195
[2]  
Bel'skii V.E., 1977, Russ. Chem. Rev, V46, P828
[3]  
Flett D., 2004, Chemistry for sustainable development Journal, V12, P81
[4]   A comparison between TEHA and Cyanex 923 on the separation and the recovery of sulfuric acid from aqueous solutions [J].
Haghshenas, D. Fatmehsari ;
Darvishi, D. ;
Rafieipour, H. ;
Alamdari, E. Keshavarz ;
Salardini, A. A. .
HYDROMETALLURGY, 2009, 97 (3-4) :173-179
[5]  
KOCIENSKI PJ, 2005, PROTECTING GROUPS, P454
[6]   Removal/recovery of hydrochloric acid using Alamine 336, Aliquat 336, TBP and Cyanex 923 [J].
Sarangi, K. ;
Padhan, E. ;
Sarma, P. V. R. B. ;
Park, K. H. ;
Das, R. P. .
HYDROMETALLURGY, 2006, 84 (3-4) :125-129
[7]   DECOMPOSITION OF SOLVENT-EXTRACTION MEDIA DURING NUCLEAR REPROCESSING - LITERATURE-REVIEW [J].
TAHRAOUI, A ;
MORRIS, JH .
SEPARATION SCIENCE AND TECHNOLOGY, 1995, 30 (13) :2603-2630
[8]   RECOVERY OF METAL VALUES FROM SPENT HYDRODESULFURIZATION CATALYSTS BY LIQUID-LIQUID-EXTRACTION [J].
ZHANG, PW ;
INOUE, K ;
TSUYAMA, H .
ENERGY & FUELS, 1995, 9 (02) :231-239
[9]  
2005, 1 BUTANOL MSDS FOUND