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Mechanism and kinetics study on removal of Iron from phosphoric acid by cation exchange resin

Mechanism and kinetics study on removal of Iron from phosphoric acid by cation exchange resin

作     者:Xinke Leng Yanjun Zhong Dehua Xu Xinlong Wang Lin Yang 

作者机构:School of Chemical Engineering Sichuan University 

出 版 物:《Chinese Journal of Chemical Engineering》 (中国化学工程学报(英文版))

年 卷 期:2019年第27卷第5期

页      面:1050-1057页

核心收录:

学科分类:0710[理学-生物学] 0830[工学-环境科学与工程(可授工学、理学、农学学位)] 0817[工学-化学工程与技术] 08[工学] 0703[理学-化学] 

基  金:Supported by the National Basic Research Program of China(2016YFD0200404) 

主  题:Purification of wet-process phosphoric acid Cation exchange resin Kinetics models Diffusion models 

摘      要:Iron element is one of the main impurities in wet-process phosphoric acid and it has a significant impact on the subsequent phosphorus chemical products. This paper studied the feasibility of using Sinco-430 cation exchange resin for iron removal from phosphoric acid. The specific surface area and the total exchange capacity of resin were 8.91 m2·g-1 and 5.18 mmol·g-1, respectively. The sorption mechanism was determined by FTIR and XPS and the results indicated that iron was combined with-SO3 H in resin. The removal process was studied as a function of temperature, H3 PO4 content and mass ratio between resin and solution. The unit mass of resin to remove iron was 0.058 g·g-1 resin when the operating parameters were T = 50 ℃, H3 PO4 content = 27.61 wt%and S/L = 0.1, respectively. Kinetics study demonstrated that pseudo-second-order reaction model fits this study best and the calculated activation energy of overall reaction is 29.10 kJ·mol-1. The overall reaction process was mainly controlled by pore diffusion.

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