期刊文献+

反胶团萃取磷酸溶液中镁的动力学 被引量:12

Kinetics of Reverse Micelles Extraction of Magnesium from Phosphoric Acid Solution
在线阅读 下载PDF
导出
摘要 采用恒界面池研究了二壬基萘磺酸(DNNSA)-煤油-磷酸体系萃取镁离子的动力学。考察了搅拌转速和传质界面积对萃取速率的影响,实验结果表明:磷酸中镁离子的萃取速率在200r?min?1时出现与搅拌强度无关的化学反应动力学"坪区",此时萃取速率正比于两相接触面积,说明萃取过程为界面化学反应控制过程。在动力学"坪区",镁离子萃取速率正比于萃取剂浓度和水相镁离子浓度,随着温度升高萃取速率增加;萃取反应活化能为70.01kJ?mol?1,并得到了DNNSA萃取磷酸中镁离子的萃取动力学方程。 The kinetic studies of Mg (Ⅱ) extraction from phosphoric acid solution by dinonylnaphthalene sulfonic acid (DNNSA) in kerosene were investigated with a Lewis Cell. The effects of stirring rate and interfacial area were studied. When stirring speed is more than 200 r·min^-1, there is a chemical reaction kinetic region where the extraction rate of Mg (Ⅱ) is independent of the stirring speed. The experimental results demonstrate that the extraction rate of Mg (Ⅱ) is apparently proportional to the interfacial area between the aqueous phase and the organic phase, and it indicates that the Ng (Ⅱ) extraction rate is controlled by a chemical reaction at the interface. In the kinetic region, the rate of Mg (Ⅱ) extraction is direct proportional to the concentration of Mg (Ⅱ) and DNNSA. Moreover, the extraction rate also increases with the increase of extraction temperature. The activation energy of extraction was calculated to be 70.01 kJ·mol^-1m and the kinetic equation ofMg ( Ⅱ ) extraction from phosphoric acid by DNNSA was put forward.
作者 余静 刘代俊
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2009年第6期939-944,共6页 Journal of Chemical Engineering of Chinese Universities
基金 国家自然科学基金资助项目(20676048)
关键词 动力学 萃取 反胶团 磷酸 二壬基萘磺酸(DNNSA) kinetics extraction reverse micelles magnesium phosphoric acid dinonylnaphthalene sulfonic acid(DNNSA)
  • 相关文献

参考文献9

二级参考文献30

  • 1朱屯.有机磷(膦)酸萃取钴和镍的动力学行为比较[J].化工学报,1993,44(3):343-349. 被引量:4
  • 2GUO Yin-cheng(郭诚),XU Jin-ming(徐进明),SONG Yao-zhu(宋耀祖) et al.Simulation of flow and combustion process in a phosphoric column reactor(热法磷酸塔内流动与燃烧过程数值模拟)[J].J Chem Eng of Chinese Univ(高校化学工程学报),2001,15(4):357-362.
  • 3[3]Murugaiya P.Parasuramaiyer H,Venkateswarlu Ch.Separation of trace metal impurities from phosphoric acid on Chelex-100[J].Indian J Chem Technol,1988,26(4):194-196.
  • 4[4]Touajbia D,Kerdjoudj H.Concentration and purification of wet industrial phosphoric acid by electro-electrodialysis[J].J Appl Electrochem,1996,26(10):1071-1073.
  • 5[5]Habashi F,Naito K,Awadalla F T.Crystallization of impurities from black phosphoric acid at high temperature[J].J Chem Technol Biotechnol,1983.33A(5):261-265.
  • 6TIAN Heng-shui(田恒水),TANG Song-qian(唐嵩千),SU Yuan-fh(苏元复).Fluorine removal from wet phosphoric acid by solvent extraction to produce cattle feed additive(液-液萃取法从湿法磷酸中脱氟制饲料磷酸氢钙)[J].Journal of East China Institute of Chemical Technology(华东化工学院学报),1988,14(5):551-557.
  • 7[8]Mc Culloulgh J F Phosphoric acid purification:comparing the process choices[J].Chem Eng,1976,3(26):01-103.
  • 8[9]Lo T C,Baird M H,Hanson C (Eds).Handbook of Solvent Extraction[M]New York:Wiley,1983.
  • 9[10]Williams K A,Stem D R.Liquid-liquid extraction procedure for the purification of phosphoric acid[J].US Patent:3 694 153,1972-09-26.
  • 10[11]Bradford J L,Ore F B.Extraction process for the purification of phosphoric acid[P]US Patent:No.4 053 564,1977-10-11.

共引文献51

同被引文献98

引证文献12

二级引证文献30

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部