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1.
Studies of the extraction of thallium(I) from aqueous solution into chloroform or MIBK using 6 reagents have been made. Reagent concentration, pH variation, and the addition of adductforming agents to the organic phase have all been investigated. Association constants and distribution coefficients for several of the better reagents have been determined. Theoretical interpretations have permitted the identification, of participating species and the calculation of equilibrium constants in several cases. 相似文献
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The extraction of cobalt(II) from sulfate medium of ionic strength 0.33?mol dm?3 by capric acid dissolved in chloroform has been carried out at 25°C. By using the slope analysis method, the stoichiometry of the organometallic complex extracted was determined. Cobalt(II) complex exists as a mononuclear species CoL2.2HL in the lower concentration region of capric acid and a binuclear ones (CoL2.2HL)2 in the higher concentration region. Extraction constants for each species were given. UV–visible and FTIR spectroscopy have also been used for the investigation of the extractant and their complexes. Electronic spectrum of cobalt(II) caprate species indicates the octahedral structure. 相似文献
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Fourteen different chelating reagents have been investigated, as possible extradants for radioiabelled 10-6M thallium(I) from aqueous solutions into chloroform. The data have beun analyzed theoretically to identify the predominant species involved and to estimate association and distribution constanta. 相似文献
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Studies of the extraction of thallium (I) from aqueous solution into an immiscible organic solvent have been made using 71 chelating reagent-solvent pairs involving 16 reagents and 17 solvents. The data have been analyzed to identify the predominant species involved, and association and partition constants have been estimated in many cases, The best extraction systems seem to be those involving 3phenylpropylxanthate and chloroform, chlorobenzene or methylene chloride. 相似文献
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The effect of diethylamine (S) in the extraction of nickel and cobalt thenoyl-trifluoroacetonates (MT2) was studied. The results showed that quantitative extraction may be carried out, with formation of a single species MT2S2, which is more stable with cobalt than with nickel. An aqueous solution of these two cations may be analysed by liquid-liquid extraction and gas chromatography of the organic phase.
Zusammenfassung
Der Einfluss von Diäthylamin (S) bei der Extraktion von Nickel- und Kobaltthenoyltrifluoracetonat (MT2) wurde untersucht. Die Ergebnisse zeigten, dass eine quantitative Extraktion unter Bildung einer einzigen Spezies MT2S2 ausgeführt werden kann, wobei die Verbindung mit Kobalt stabiler als die mit Nickel ist. Eine wässrige Lösung dieser beiden Kationen kann durch Flüssig-Flüssig-Extraktion und durch Gaschromatographie der organischen Phase analysiert werden. 相似文献
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J. Zsakó G. Pokol Cs. Novák Cs. Várhelyi A. Dobó G. Liptay 《Journal of Thermal Analysis and Calorimetry》2001,64(2):843-856
A number of 30 [Co(en)3 ]Y3 , [Co(en)2 X2 ]Y and [Co(en)2 X(amine)]Y2 type complexes (X =Cl, Br; Y =Cl, Br, I, NCO, NCS, NO3 , ClO4 , etc.; amine =aromatic and alkylamines) were obtained from trans-[Co(en)2 Cl2 ]Cl by double decomposition and by substitution reactions, respectively. The structure of the complexes was proved by means
of far and middle FTIR spectra. The thermal decomposition was studied by TG, DTA and DSC measurements. Mass spectra were also
recorded. In the case of [Co(en)3 ]Y3 complexes the nitrate, perchlorate and dimesoperiodates decompose suddenly, frequently explosion like. The halides and thiocyanates
seem to substitute an ethylenediamine ligand, yielding a rather unstable intermediate. The pyrolysis of [Co(en)2 X2 ]Y type derivatives yields no relatively stable intermediates, but the decomposition temperatures may be correlated with
the nature of Y and with the cis or trans configuration of the compound. With the [Co(en)2 X(amine)]Y2 type complexes one observes the formation of [Co(en)2 XY]Y as intermediate product. From the TG curves kinetic parameters were derived for some dehydration and deamination processes,
by using the nomogram method. The validity of a non-linear kinetic compensation law was observed.
This revised version was published online in July 2006 with corrections to the Cover Date. 相似文献
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Equilibrium distribution coefficients have been determined for the extraction of cobalt(II) with 8-mercaptoquinoline as a function of pH and reagent concentraton at ambient temperature. The extractable complex is a diadduct, i. e. two molecules of the reagent are coordinated to the cobalt(II) chelate. The adduct formation constant in chloroform and the overall formation constant in the aqueous phase have been determined. Pyridine and its methyl derivatives were found to enhance the extraction of Co(II) into chloroform in the presence of 8-mercaptoquinoline. From the extraction equilibrium data, the adduct formation constants of 12 chelate to nitrogen base adducts were evaluated. The special role of steric factors is discussed. 相似文献
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A new method is proposed for the solvent extraction separation of cobalt(II) with hexaacetatocalix(6)arene in toluene. Cobalt(II) was extracted at pH 7.4 with 10 x 10(-4) M hexaacetocalix(6)arene, stripped with 2 M nitric acid, and determined spectrophotometrically at 500 nm as its complex with nitroso-R-salt. Cobalt was separated from any associated elements. The method was extended to the analysis of cobalt(II) in real samples such as vitamin B-12. 相似文献
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Cobalt ions in aqueous thiocyanate solution react with Aliquat-336-xylene solution to form anion-association complex which is easily extracted into the organic phase. A typical extraction procedure involves extracting a solution which is 10 ppm in cobalt and 0.06 M,
Strippant | Cobalt stripped (%) |
Na2S (M) 1.0 | 18.3 |
2.0 | 10.7 |
Na2SO3 (M) 0.1 | 10.7 |
0.5 | 49.6 |
1.0 | 52.9 |
EDA (%) 2.5 | 76.6 |
NaOH (M) 0.1 | 4.1 |
0.5 | 74.1 |
1.0 | 90.8 |
2.0 | 76.8 |
NH4OH (M) 0.1 | 24.1 |
0.5 | 91.8 |
1.0 | 97.5 |
2.0 | 99.9 |
EDTA (M) 0.02 | >99.9 |
0.05 | >99.9 |
0.1 | >99.9 |
EDTA (%) 0.1 | >99.9 |
0.5 | >99.9 |
1.0 | >99.9 |