SciELO - Scientific Electronic Library Online

 
vol.41 número3Cathodic behaviour of anodized titanium in simulated physiologicalUse of hydrocolloids as edible covers to produce low fat french fries índice de autoresíndice de materiabúsqueda de artículos
Home Pagelista alfabética de revistas  

Servicios Personalizados

Revista

Articulo

Indicadores

  • No hay articulos citadosCitado por SciELO

Links relacionados

  • No hay articulos similaresSimilares en SciELO

Compartir


Latin American applied research

versión impresa ISSN 0327-0793

Resumen

GAMBARRA, M.M.P.; LIMA, C.C.  y  GOIS, L.M.N.. Separation efficiency in a sieve plates extractor. Lat. Am. appl. res. [online]. 2011, vol.41, n.3, pp.205-209. ISSN 0327-0793.

This work analyzes the separation efficiency data involving mass transfer between two immiscible liquid phases in a bench lab extractor without mechanical agitation. The experimental apparatus consisted in a cylindrical glass column containing perforated plates, operating in countercurrent mode. The experimental runs were developed by using butane-acetic acid-water system, following a factorial experimental design involving the variables: dispersed phase velocity, the continuous phase velocity and the number of stages (two and four plates). The collected acid acetic raffinate and extract was analysed by titration with sodium hydroxide. Separation efficiencies were estimated through Murphree (1925) and Kawase (1990) models. The results showed that the higher was the dispersed flow, higher was the separation efficiency. An opposite behavior was observed for the continuous phase flow effect. In relation to the number of plates, higher efficiencies were achieved for 4 plates arrangement. The results provided empirical equations to predict the extraction efficiency, which exhibited good correlation with experimental data.

Palabras clave : Liquid-Liquid Extraction; Efficiency; Mass Transfer.

        · texto en Inglés     · Inglés ( pdf )

 

Creative Commons License Todo el contenido de esta revista, excepto dónde está identificado, está bajo una Licencia Creative Commons