Although the excellent metal-binding capacities of aminopolycarboxylate chelants (APCs) facilitate their extensive use, pre-and post-toxicity of APCs and their high persistence in aquatic environments evoke concerns. Several treatment techniques with a principal focus on the degradation of APCs at the pre-release step have been proposed. Here, we report a technique for the separation of metal ions from waste solution containing excess APCs using a solid phase extraction system with an ion-selective immobilized macrocyclic material, commonly known as a molecular recognition technology (MRT) gel. Synthetic metal solutions with 100-fold chelant content housed in H 2 O matrices were used as samples.The MRT gel showed a higher recovery rate compared with other SPE materials at 20 °C using a flow rate of 0.2 mL min -1 . The effects of solution pH, metal-chelant stability constants and ionic radii were assessed for 32 metals. Compared to the conventional treatment options for such waste solutions, our proposed technique has the advantage of nondestructive separation of both metal ions and chelants. (Ayres, 1970; Bell, 1977; Grasso, 1993;Roundhill, 2001 APCs have been introduced into the natural environment, the aqueous transport of metals, which characteristically form stable complexes with chelates, can be expected to occur (Means et al., 1980;Nowack and VanBriesen, 2005). Residence time of the metals is thus extended, as they are remobilized from soils and sediments into the water phase. EDTA and its homologs are poorly photo-, chemo-and biodegradable in the environment (Means et al., 1980; Bolton Jr. et al., 1993;Kari and Giger, 1995; Egli, 2001;Nowack, 2002;Nörtemann, 2005) and, in most cases, metal complexation raises the threshold values for toxic effects (Sillanpää and Oikari, 1996;Sorvari and Sillanpää, 1996;Sillanpää, 2005).Excess chelant also increases the total nitrogen content and the phosphate solubility in interstitial waters (Norvell, 1984; Horstmann and Gelpke, 1991; Erel and Morgan, 1992;Li and Shuman, 1996; Hering and Morel, 2002).Wastewater with excess APCs entails subsequent separation or degradation treatment before it can be safely discharged. In Europe, treatment of EDTA-containing wastewaters is increasingly required because of the increasingly stringent environmental regulations (Grundler et al., 2005; van Ginkel and Geerts, 2005). Several processes have been proposed for the degradation of APCs to restrict their intrusion to the environment (Sillanpää and Oikari, 1996; Kagaya et al., 1997;Madden et al., 1997;Krapfenbauer and Getoff, 1999;Muñoz and von Sonntag, 2000;Rämö et al., 2000; Bucheli-Witschel and Egli, 2001;Rämö and Sillanpää, 2001;Sillanpää and Pirkanniemi, 2001;Sillanpää and Rämö, 2001;Pirkanniemi et al., 2007). The cost of chelants is also an important issue surrounding their use in metal ion sequestration. Methods that recycle not only the processed water, but also the chelant, may therefore be economically feasible (Lim et al., 2005;Leštan et al., 2008).Separation and pre-conce...