Continuous Purification of Wet-Process Phosphoric Acid via Microchannel

被引:0
|
作者
Saba, Mansouri [1 ]
Kambiz, Varmra [2 ]
Babak, Aghel [1 ]
机构
[1] Kermanshah Univ Technol, Fac Energy, Dept Chem Engn, Kermanshah, Iran
[2] Kermanshah Univ Med Sci, Res Ctr Oils & Fats, Kermanshah, Iran
来源
IRANIAN JOURNAL OF CHEMISTRY & CHEMICAL ENGINEERING-INTERNATIONAL ENGLISH EDITION | 2022年 / 41卷 / 01期
关键词
Solvent extraction; Microchannel; Purification; Wet-process phosphoric acid; LIQUID-LIQUID-EXTRACTION; MASS-TRANSFER COEFFICIENT; N-BUTYL PHOSPHATE; SOLVENT-EXTRACTION; SIMULTANEOUS RECOVERY; REMOVAL; PRECIPITATION; CADMIUM; URANIUM; PHASE;
D O I
暂无
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Solvent extraction is an economically efficient method widely used in the purification of wet phosphoric acid. In this study, a microchannel was applied to promote the mixing and purification of phosphoric acid during continuous production. For this aim, solvent extraction was conducted to purify phosphoric acid via methyl isobutyl ketone/tri-butyl phosphate mixtures. Additionally, the Box-Behnken design method was used to survey the solvent extraction process. The effect of various operational parameters such as solvent concentration (45-65 %wt), temperature (18-28 degrees C), and organic/aqueous phase ratio (2:1-6:1) at a constant flow rate of 70 mL/L was examined. Experimental results indicated that the microchannel at the residence time of 6.85 min could promote the extraction percentage of and sulfate removal of more than 98% and 60%, respectively, compared to the batch extractor.
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页码:79 / 87
页数:9
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