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Complexes metal-extractant

Liquid-liquid extractions using ammonium pyrrolidine dithiocarbamate (APDC) as a metal chelating agent are commonly encountered in the analysis of metal ions in aqueous samples. The sample and APDC are mixed together, and the resulting metal-ligand complexes are extracted into methyl isobutyl ketone before analysis. [Pg.223]

Extraction, a unit operation, is a complex and rapidly developing subject area (1,2). The chemistry of extraction and extractants has been comprehensively described (3,4). The main advantage of solvent extraction as an industrial process Hes in its versatiHty because of the enormous potential choice of solvents and extractants. The industrial appHcation of solvent extraction, including equipment design and operation, is a subject in itself (5). The fundamentals and technology of metal extraction processes have been described (6,7), as has the role of solvent extraction in relation to the overall development and feasibiHty of processes (8). The control of extraction columns has also been discussed (9). [Pg.60]

Other Metals. Because of the large number of chemical extractants available, virtually any metal can be extracted from its aqueous solution. In many cases extraction has been developed to form part of a viable process (275). A review of more recent developments in metal extraction including those for precious metals and rare earths is also available (262). In China a complex extraction process employing a cascade of 600 mixer—settlers has been developed to treat leach Hquor containing a mixture of rare earths (131). [Pg.81]

The distribution ratio, i.e. the ratio of the amount of metal extracted as complex into the organic phase to that remaining in all forms in the aqueous phase, is given by... [Pg.165]

To examine the effect of ultrasound on the decomposition of Zn-dithizone complex, 0.2264 g Zn metal was treated with 10 ml of 5 M NaOH and sonicated for 30 min for maximum dissolution of Zn metal. After treating with ultrasound, 0.5 ml of 1 % dithizone was added to form Zn-dithizone red coloured complex. This red colour Zn-dithizone complex was extracted in chloroform and made upto to the mark in 50 ml volumetric flask with chloroform. 10 ml of this complex was sonicated for different duration of time (10, 20 and 30 min) and UV-vis spectro-photometric analysis was carried out. [Pg.243]

The presence in dyehouse effluents of typical dye-complexing metal ions is an environmentally sensitive issue, such metallic contamination arising mostly from the decomposition of metal-complex dyes [26]. The synthetic complexing agent cucurbituril (section 10.3.2) can be used to selectively extract such metal ions from the effluent. [Pg.355]

Nakamura H., Takagi M., Ueno K., Complexation and extraction of alkali metal ions by 4 -picrylaminobenzo-18-crown-6 derivatives, Anal. Chem. 1980 52 1668. [Pg.42]

An extractive spectrophotometric procedure based on the complexation of reduced Iron(II) with 5-Chloro-7-iodo-8-hydroxyquinoline (CIHQ) for the estimation of micro amounts of vitamin C. The resulting brown colored complex was extracted into chloroform to give a reddish brown extract which shows an absorption band at 485 nm. This chelate was formed immediately and the apparent molar absorptivity and Sandell s sensitivity for vitamin C was found to be 8.5 x 105 dm3 mol"1 cm 1 and 2.072xl0 4g cm 2. Linear relationship between absorbance and concentration of ascorbic acid is observed up to 0.8 pg ml"1. Interference studies of different substances including sugars, vitamins and amino acids, metal ions and organic acids were carried out. The utility of the method was tested by analysing some of the marketed products of vitamin C... [Pg.117]

The previous chapters have demonstrated that liquid-liquid extraction is a mass transfer unit operation involving two liquid phases, the raffinate and the extract phase, which have very small mutual solubihty. Let us assume that the raffinate phase is wastewater from a coke plant polluted with phenol. To separate the phenol from the water, there must be close contact with the extract phase, toluene in this case. Water and toluene are not mutually soluble, but toluene is a better solvent for phenol and can extract it from water. Thus, toluene and phenol together are the extract phase. If the solvent reacts with the extracted substance during the extraction, the whole process is called reactive extraction. The reaction is usually used to alter the properties of inorganic cations and anions so they can be extracted from an aqueous solution into the nonpolar organic phase. The mechanisms for these reactions involve ion pah-formation, solvation of an ionic compound, or formation of covalent metal-extractant complexes (see Chapters 3 and 4). Often formation of these new species is a slow process and, in many cases, it is not possible to use columns for this type of extraction mixer-settlers are used instead (Chapter 8). [Pg.370]

Both carboxylic (e.g., Versatic acid) and organophosphorus acids have been used commercially to extract the lanthanides. The extraction follows the formation of the metal-extractant complex [Eq. (11.21)] and so depends on the pH of the feed. [Pg.499]

One important point regarding microemulsion extraction is that the complexity of the system with its three phases, two interfaces, and usually unknown phase morphology makes the prediction of its performance quite difficult, particularly when dealing with solutes of diverse properties. The literature indicates that it does not always improve metal extraction, and in cases it may even hinder it due to the effect of the emulsifying additives. [Pg.663]


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See also in sourсe #XX -- [ Pg.410 , Pg.416 ]




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Complex Formation and Metal Extraction

Complexing extractants

Ether complexes, solvent extraction metals

Extractable Metal-Organic Complexes

Halide complexes, solvent extraction metals

Metal complexation/supercritical fluid extraction

Metal-organic complexes extraction

Metals extraction

Oxime complexes, solvent extraction metals

Solvent extraction of metal complexes

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