Removal Efficiency and Kinetics of Fe3+ from Phosphoric Medium by Solvent Extraction

Haifeng Liu, Chao Hu, Lei Guo, Yanru Jin, Ting Jiang, Zhiye Zhang, Lin Yang
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Abstract

The application of wet-process phosphoric acid in fertilizer is limited due to the excessive Fe3+ concentration. In this paper, a fundamental investigation on the removal of Fe3+ from phosphoric acid with P-15 extractant is conducted. First, effects of several parameters on the extraction rate such as extraction temperature, P-15 concentration, phase ratio O/A on Fe3+ extraction are carefully investigated. The composition of the extract was verified by slope method and saturation capacity method. Then, the kinetic and control mechanism of the extraction reaction is studied by constant interface cell. The extraction reaction rate equation was obtained by the initial rate method. The calculated activation energy of overall reaction is 15.4 kJ·mol−1 and the change of enthalpy ∆H = −4.19 kJ·mol−1 of Fe3+ is measured by automatic calorimeter.

用溶剂萃取法去除磷酸盐介质中的 Fe3+ 的效率和动力学特性
由于 Fe3+ 浓度过高,湿法磷酸在肥料中的应用受到限制。本文对 P-15 萃取剂去除磷酸中的 Fe3+ 进行了基础研究。首先,仔细研究了萃取温度、P-15 浓度、相比 O/A 等几个参数对萃取率的影响。通过斜率法和饱和容量法验证了萃取物的组成。然后,利用恒定界面池研究了萃取反应的动力学和控制机理。通过初始速率法得到了萃取反应速率方程。用自动量热计测量了整个反应的活化能为 15.4 kJ-mol-1,Fe3+的焓变 ∆H = -4.19 kJ-mol-1。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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