A study on transport, kinetic selectivity and stability in SLM operations using a new carrier, the molecule 2-hydroxy-5-dodecylbenzaldehyde (2H5DBA) in kerosene, is described. A simple transport model is derived to evaluate the mass transfer coefficient in the membrane. Finally a comparison with the di (2-ethylhexyl) phosphoric acid (D2EHPA) carrier in kerosene is made. The SLM system was employed and tested in the removal of Cu2+ from wastewater by using the operating conditions obtained from L-L extraction tests. Studies on the kinetics of copper extraction by using the 2H5DBA showed that complexation reaction is very fast. Transport tests were performed at different carrier concentrations (10%, 30%, 50% v/v) showing the improvement of SLM performance with increasing its concentration. Operating the SLM at optimum conditions (50% v/v 2H5DBA concentration in kerosene, feed pH = 5, strip pH = 2.2) final copper concentrations in the feed and strip phases were, respectively, 2.0 mg•L-1 and 47.0 mg•L-1, starting from 50 mg∙L-1 in the feed, meaning a significant up-hill transport. The fluxes (J) were calculated by fitting the experimental data of copper concentration in the feed by an exponential equation. They were used to calculate the transport (kinetic) selectivities of Cu2+ SLM separation over Ni2+, Zn2+ and Mn2+, given by the ratio J0 (Cu) / J0 (M), where M = Ni, Zn and Mn. The values were 37.4, 48.2 and 42.1, respectively. Transport and stability tests at the optimal carrier concentration by using the 2H5DBA and the D2EHPA in kerosene were carried out to compare them in terms of flux, lifetime and mass transfer coefficients. Experimental data evidenced for 2H5DBA a lower copper flux (8.67 mmol•h-1•m-2 vs. 36.71 mmol•h-1•m-2), a lower lifetime (20 h vs 57 h) and lower mass transfer coefficient in the membrane (3.00∙10-7 m∙s-1 vs 2.00∙10-6 m∙s-1) but the selectivity of the separation process can overcome the disadvantages.
Selective removal of Cu2+ versus Ni2+, Zn2+ and Mn2+ by using a new carrier in a supported liquid membrane
MOLINARI, Raffaele;ARGURIO, Pietro
2006-01-01
Abstract
A study on transport, kinetic selectivity and stability in SLM operations using a new carrier, the molecule 2-hydroxy-5-dodecylbenzaldehyde (2H5DBA) in kerosene, is described. A simple transport model is derived to evaluate the mass transfer coefficient in the membrane. Finally a comparison with the di (2-ethylhexyl) phosphoric acid (D2EHPA) carrier in kerosene is made. The SLM system was employed and tested in the removal of Cu2+ from wastewater by using the operating conditions obtained from L-L extraction tests. Studies on the kinetics of copper extraction by using the 2H5DBA showed that complexation reaction is very fast. Transport tests were performed at different carrier concentrations (10%, 30%, 50% v/v) showing the improvement of SLM performance with increasing its concentration. Operating the SLM at optimum conditions (50% v/v 2H5DBA concentration in kerosene, feed pH = 5, strip pH = 2.2) final copper concentrations in the feed and strip phases were, respectively, 2.0 mg•L-1 and 47.0 mg•L-1, starting from 50 mg∙L-1 in the feed, meaning a significant up-hill transport. The fluxes (J) were calculated by fitting the experimental data of copper concentration in the feed by an exponential equation. They were used to calculate the transport (kinetic) selectivities of Cu2+ SLM separation over Ni2+, Zn2+ and Mn2+, given by the ratio J0 (Cu) / J0 (M), where M = Ni, Zn and Mn. The values were 37.4, 48.2 and 42.1, respectively. Transport and stability tests at the optimal carrier concentration by using the 2H5DBA and the D2EHPA in kerosene were carried out to compare them in terms of flux, lifetime and mass transfer coefficients. Experimental data evidenced for 2H5DBA a lower copper flux (8.67 mmol•h-1•m-2 vs. 36.71 mmol•h-1•m-2), a lower lifetime (20 h vs 57 h) and lower mass transfer coefficient in the membrane (3.00∙10-7 m∙s-1 vs 2.00∙10-6 m∙s-1) but the selectivity of the separation process can overcome the disadvantages.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.
