Development of a Spiral-Type Flowing Liquid Membrane Module with High Stability and Its Application to the Recovery of Chromium and Zinc

Effect of supporting membrane on removal of cadmium by the hybrid liquid membrane process

A hybrid liquid membrane process was used to remove cadmium cation from a solution using bis-(2-ethylhexyl) phosphoric acid as the carrier for the first time. Different polyethersulphone supporting membranes were prepared by a phase inversion technique. The prepared membrane could be efficiently used as the supporting membranes for the proposed process. The effects of porosity and pore size of the supporting membrane on removal efficiency were investigated. In addition, the effects of various operating parameters such as carrier concentration in organic phase, pH of feed phase, acid concentration, and temperature on the performance of the process were also investigated. It was found that the maximum flux of cadmium is obtained using the supporting membrane with 84.5% porosity and the pore size of 132 nm. The optimum carrier concentration is 0.2 M, the optimum pH of the feed phase is 6, and the optimum concentration of acid in the stripping phase is 0.6 M.

Study on removal of cadmium by hybrid liquid membrane process

Removal of cadmium as a hazardous heavy metal is studied by applying a new design of hybrid cell for liquid membrane process. Tri-iso-octyl amine (TIOA) is used as the carrier in the organic phase. The concentration of cadmium in the samples is measured by atomic absorption spectroscopy. The effect of various parameters including type of supporting membrane, pH of feed and stripping phases, initial concentration of cadmium, carrier concentration, solvent nature, and also organic film resistance on mass transfer rate and removal efficiency are studied. The effect of temperature on mass transfer flux is studied by proposing a prediction model. The optimum carrier concentration is found to be about 0.05 M. The appropriate values of pH for feed and stripping phases are about 3 and 13, respectively.

Arsenic(V) removal with polymer inclusion membranes from sulfuric acid media using DBBP as carrier

Polymer inclusion membranes (PIMs) based on cellulose triacetate (CTA) and dibutyl butyl phosphonate (DBBP) were tested for arsenic(V) separation from H2SO4 for its recovery from copper electrolytes. Solvent extraction experiments allowed the determination of the As(V)-DBBP and H2SO4-DBBP complexes formed in the organic phase. Application of a transient model to membrane transport experiments in solutions containing only arsenic or H2SO4 indicated that it occurred under a kinetically controlled regime by formation of H3AsO4[DBBP]2 and H2SO4[DBBP] species, respectively. When arsenic and H2SO4 are simultaneously present, the existence of a third species, H3AsO4[DBBP][H2SO4], explains well the fact that As(V) flux decreases and that H2SO4 flux increases. In both cases, a limiting 50% recovery value was obtained. However, active arsenic transport (>50%) is achieved if the H2SO4 concentration gradient is assured (e.g., using a triple-cell configuration). In this way, high arsenic recovery factors (90% in 800 min) were obtained with initial concentrations of 5000 mg/L As(V) and 220 g/L H2SO4. In all membrane systems tested, good As(V) selectivity over copper (up to 30000 mg/L) was attained.

Preparation of magnetic dye affinity adsorbent and its use in the removal of aluminium ions

Aluminium has recently been considered as a causative agent in dialysis encephalopathy, osteodystrophy, and anemia occuring in hemodialysis patients. The aim of this study is to prepare magnetic poly(2-hydroxyethylmethacrylate) (mPHEMA) adsorbent and to investigate it's useability for the removal of Al(III) ions from drinking and dialysis water. Magnetic PHEMA beads in a size range 80-120 microm were produced by a dispersion polymerization technique. Then Alizarin Red was covalenlty attached onto the mPHEMA beads. Al(III) adsorption from aqueous solutions was examined by batch system. mPHEMA beads were characterized by swelling tests, electron spin resonance (ESR), scanning electron microscopy (SEM), and elemental analysis. Important results obtained in this study are as follows: the swelling ratio of mPHEMA beads was 34%. The presence of magnetite in the polymeric structure was confirmed by ESR. The mPHEMA beads have a spherical shape and porous structure. Alizarin Red loading was 135.8 micromol g(-1) polymer. The maximum Al(III) adsorption was 722 micromol g(-1) polymer at pH 5.0. Non-specific Al(III) adsorption was about 23 micromol g(-1) polymer under the same conditions. High desorption ratios (98%) were achieved by using 0.1 M HNO3. It was possible to reuse the beads without significant loss of Al(III) adsorption capacity.