scholarly journals RECOVERY OF NI2+ BY DI-(2-ETHYLHEXYL) PHOSPHORIC ACID (HDEHP)

2009 ◽  
Vol 12 (3) ◽  
pp. 40-50
Author(s):  
Phuong Mai Tran ◽  
Canh Huy Nguyen ◽  
Thang Manh Ngo

This paper dealts with solvent and bulk liquid membrane extraction of Ni2+ from its chloride solutions by HDEHP in n-heptane. Effects of extraction time, initial pH and Ni2+ concentration in the feed as well as HDEHP concentration in the organic phase were investigated. Solvent extraction equilibrium was established within 10 minutes. Ni2+ showed to be extracted into the organic phase preferentially as Ni(DEHP), complexes. The Ni2+ extraction yield decreased with increasing initial Ni2+ concentration, with decreasing pH and/or HDEHP concentration. The later is not only due to shifting equilibrium of Nils extraction reaction, but also due to concurent extraction of HCI. Results of bulk liquid membrane extraction could be described by the kinetics of interfacial pseudo-first order reactions. Observed rate constants were determined ⁓ 2,30.10-2 ⁒ 2,68.10-2 min-1 for concentration range [Ni2+]0 ⁓ 10-3 ⁒ 10-2 mol/l.

2016 ◽  
Vol 73 (12) ◽  
pp. 2888-2895 ◽  
Author(s):  
Guoping Li ◽  
Juanqin Xue ◽  
Nina Liu ◽  
Lihua Yu

Abstract The transport of cyanide from wastewater through a bulk liquid membrane (BLM) containing tricaprylamine (TOA) as a carrier was studied. The effect of cyanide concentration in the feed solution, TOA concentration in the organic phase, the stirring speed, NaOH concentration in the stripping solution and temperature on cyanide transport was determined through BLM. Mass transfer of cyanide through BLM was analyzed by following the kinetic laws of two consecutive irreversible first-order reactions, and the kinetic parameters (k1, k2, Rmmax, tmax, Jamax, Jdmax) were also calculated. Apparently, increase in membrane entrance (k1) and exit rate (k2) constants was accompanied by a rise in temperature. The values of activation energies were obtained as 35.6 kJ/mol and 18.2 kJ/mol for removal and recovery, respectively. These values showed that both removal and recovery steps in cyanide transport is controlled by the rate of the chemical complexation reaction. The optimal reaction conditions were determined by BLM using trioctylamine as the carrier: feed phase: pH 4, carrier TOA possession ratio in organic phase: 2% (V/V), stripping phase concentration of NaOH: 1% (W/V), reaction time: 60 min, stirring speed: 250 r/min. Under the above conditions, the removal rate was up to 92.96%. The experiments demonstrated that TOA was a good carrier for cyanide transport through BLM in this study.


2005 ◽  
Vol 42 (5) ◽  
pp. 577-586 ◽  
Author(s):  
H. Korkmaz Alpoguz ◽  
Ahmet Kaya ◽  
Aydan Yilmaz ◽  
Mustafa Yilmaz

2003 ◽  
Vol 38 (7) ◽  
pp. 1649-1664 ◽  
Author(s):  
H. Korkmaz Alpoguz ◽  
Shahabuddin Memon ◽  
Mustafa Ersoz ◽  
Mustafa Yilmaz

2004 ◽  
Vol 234 (1-2) ◽  
pp. 101-109 ◽  
Author(s):  
Ming Ma ◽  
Bo Chen ◽  
Xubiao Luo ◽  
Hao Tan ◽  
Dingsheng He ◽  
...  

2005 ◽  
Vol 39 (4) ◽  
pp. 799-810 ◽  
Author(s):  
H. Korkmaz Alpoguz ◽  
Shahabuddin Memon ◽  
Mustafa Ersoz ◽  
Mustafa Yilmaz

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