Comparison of solvent extraction and LEM extraction in static mixer for recovery of Mo(VI) from dilute aqueous solution

被引:7
作者
Das, Diptendu [1 ]
Juvekar, V. A. [1 ]
Ramprasad, K. [2 ]
Bhattacharya, R. [2 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Bombay 400076, Maharashtra, India
[2] Atom Energy Regulatory Board, Bombay, Maharashtra, India
关键词
Liquid emulsion extraction (LEM); Static mixer; Mo(VI); TBP; Height of transfer units (HTU); LIQUID-LIQUID-EXTRACTION; MASS-TRANSFER; MOLYBDENUM; ACID; TBP;
D O I
10.1016/j.cep.2015.07.012
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this paper, the liquid emulsion membrane extraction of molybdenum(VI) has been conducted in static mixer. The performance in LEM mode is compared to a conventional solvent extraction mode. The rate of extraction in LEM mode is found to be significantly higher than conventional solvent extraction. Study reveals that the optimum residence time, height of the static mixer and optimum surfactant concentration are the deciding parameters of the performance of static mixer. The effect of various parameters such as superficial velocity of aqueous phase and organic phase, residence time, initial Mo(VI) concentration in feed phase, height of column, and surfactant concentration on rate of extraction has been investigated. A mathematical model is developed to predict volumetric mass transfer coefficient (k(L)a) in a static mixer. The k(L)a value is reduced from 0.045 s(-1) to 0.015 s-1 when height of the mixer was increased from 31 cm to 93 cm respectively under the same hydrodynamic conditions. This anomalous decrease of k(L)a with increase in height is due to acid extraction by TBP which reduces driving force for extraction of Mo(VI). HTU for solvent extraction and LEM extraction are estimated as 0.67 m and 0.15 m respectively which indicates less mass transfer resistance in LEM. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:372 / 382
页数:11
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