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Liquid membrane extraction carrier concentration effect

Facilitated transport of penicilHn-G in a SLM system using tetrabutyl ammonium hydrogen sulfate and various amines as carriers and dichloromethane, butyl acetate, etc., as the solvents has been reported [57,58]. Tertiary and secondary amines were found to be more efficient carriers in view of their easy accessibility for back extraction, the extraction being faciUtated by co-transport of a proton. The effects of flow rates, carrier concentrations, initial penicilHn-G concentration, and pH of feed and stripping phases on transport rate of penicillin-G was investigated. Under optimized pH conditions, i. e., extraction at pH 6.0-6.5 and re-extraction at pH 7.0, no decomposition of peniciUin-G occurred. The same SLM system has been applied for selective separation of penicilHn-G from a mixture containing phenyl acetic acid with a maximum separation factor of 1.8 under a liquid membrane diffusion controlled mechanism [59]. Tsikas et al. [60] studied the combined extraction of peniciUin-G and enzymatic hydrolysis of 6-aminopenicillanic acid (6-APA) in a hollow fiber carrier (Amberlite LA-2) mediated SLM system. [Pg.220]

In Chapter 6, characteristic features of emulsion liquid membrane systems are examined by Yurtov and Koroleva. The effects of surfactant and carrier concentrations and external and internal phase compositions upon the properties of the extracting emulsions are discussed. Several mathematical models for the rheological curves are considered, and regions of applicability for the models are evaluated. An influence of nanodispersion formation on mass transfer through the interface and on the properties of extracting emulsions for cholesterol is demonstrated. [Pg.9]

Effect of Carrier Concentration. The carrier (extractant) also exerts a significant influence on the stability of an extracting emulsion. As a rule, the carrier will be surface-active which will reduce the stability of the emulsion due to competitive adsorption at the interface. However for ELM systems, a high concentration of carrier in the liquid membrane is usually not necessary. For each carrier, the optimal concentration will be determined by the opposing influences of the carrier on the rate of extraction of the target substance and the stability of the extracting emulsion. [Pg.93]

In addition to specific carrier features, a number of external factors may also have marked effects on transport rates. The nature of the membrane phase (in particular for liquid or supported liquid [6.10b] membranes) influences the distribution equilibria as well as the stability and selectivity of the complex in the membrane and the cation exchange rates at the interfaces. The nature of the coextracted anion affects transport via a (cationic complex-anion) pair (Fig. 10) simply by modifying the amount of salt extracted into the membrane this amount decreases with higher hydration energy and lower lipophilicity of the anion (for example, chloride compared with picrate). The concentration of salt in the aqueous phase will, of course, affect the amount extracted into the membrane and therefore the transport rates (for illustrations of these effects see for instance [6.1]). [Pg.73]


See other pages where Liquid membrane extraction carrier concentration effect is mentioned: [Pg.115]    [Pg.202]    [Pg.890]    [Pg.892]    [Pg.900]    [Pg.901]    [Pg.11]    [Pg.842]    [Pg.842]    [Pg.192]    [Pg.200]    [Pg.202]    [Pg.204]    [Pg.214]    [Pg.594]    [Pg.221]    [Pg.1049]    [Pg.1063]   
See also in sourсe #XX -- [ Pg.93 ]




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Carrier concentration

Carrier concentration effect

Carrier effect

Carrier liquid

Carriers, membranes

Extract concentration

Extractants effect

Extraction concentration

Extraction effectiveness

Extraction membranes

Extractive effect

Liquid membrane extraction effect

Membrane effects

Membrane, liquid extraction

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