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A novel cyclic functional monomer (CFM) was used to develop an As(III)-ion imprinted polymer (As-IIP). CFM possesses a positively charged imidazolium moiety and its specific cyclic size matches that of As(III). Batch adsorption experiments showed that the As-IIP has a maximum As(III) adsorption capacity of 55 mg/g, while that of the control polymer (CP) is only 25 mg As(III)/g. Adsorption isotherms for As(III) agree with the Langmuir model, suggesting monolayer adsorption. Kinetic studies showed that the adsorption process followed pseudo-second-order kinetics. The relative selectivity coefficients of As-IIP compared to CP for Cl − /H 2 AsO 3 − , SO 4 2− /H 2 AsO 3 − , HPO 4 2− /H 2 AsO 3 − , NO 3 − /H 2 AsO 3 − , and Mo 7 O 24 6− /H 2 AsO 3 − are 1.03, 1.95, 2.55, 1.52 and 2.51, respectively. The removal efficiency of As-IIP for As(III) in actual industrial wastewater was nearly 100%, which confirms that As-IIP has a high adsorption capacity as well as selectivity for the removal of As(III) from wastewater. [ABSTRACT FROM AUTHOR]

Enhancing the performance of adsorbents to the utmost extent is an objective but challenging in applying adsorption technology to wastewater treatment. In this work, novel quaternary ammonium polymers (QAPs) with high density adsorption site (i.e., quaternized N, confirmed by FT-IR results) were designed and prepared for rapid selective removal of Cr(VI) from water. The results of EDS analysis indicated the maximum exposure rate of N on the surface of QAPs was as high as 86.1%, which almost doubled comparing to that of Cr(VI) ions imprinted polymers (Cr(VI)-IIP) (46.2%). Interestingly, the maximum adsorption capacity (211.8 mg/g) and initial adsorption rate (h0 , 66.6 mg/ (g·min)) of QAPs (i.e., 5:1(TRIM)) for Cr(VI) are about 3.6 times and 4.9 times those of Cr(VI)-IIP (63.0 mg/g and 13.5 mg/(g·min)), respectively. Impressively, flow-through adsorption experiments demonstrated 5:1(TRIM) can completely remove 5 mg/L of Cr(VI) within five seconds. Additionally, 5:1(TRIM) exhibited a remarkable selectivity for Cr(VI) adsorption, and high purity (100%) of chromium can be readily obtained. The proposed idea of high exposure effect of the adsorption site can provide a valuable guidance for designing rapid selective adsorbents to remove and reclaim Cr(VI) from wastewater. Schematic Diagram for mechanism of Cr(VI) adsorption on QAPs and correlation between exposure rate of N and Q m. [Display omitted] • QAPs is a kind of adsorbent with high density adsorption sites on its surface. • Adsorption capacity (Q m) of QAPs was positively correlated with exposure rate of N. • QAPs exhibit high capacity, rapid adsorption rate for the Cr(VI) adsorption. • QAPs can achieve high purity chromate recovery due to the high selectivity. • QAPs has a good economic benefit in the recovery of chromate from wastewater. [ABSTRACT FROM AUTHOR]

[Display omitted] • UiO-66-Rd i-s and UiO-66-Rd p-m adsorbents were designed for capturing Ag(I) from wastewater. • Rhodanine groups were confirmed to be modified outside of UiO-66-Rd p-m and inside of UiO-66-Rd i-s. • UiO-66-Rd p-m exhibited faster kinetic and higher selectivity for Ag(I) capture than UiO-66-Rd i-s. • Enhanced selectivity was dominated by high-exposure rhodanine sites outside of UiO-66-Rd p-m. Highly efficient capturing of silver from wastewater is critical for environmental and economic sustainability but remains significantly challenging to achieve fast kinetics and precise selectivity. Herein, we present two approaches based on rhodanine (Rd)-modified UiO-66 including post-modified ligand exchange for UiO-66-Rd p-m and in-situ solvothermal for UiO-66-Rd i-s. The resultant UiO-66-Rd p-m and UiO-66-Rd i-s perform maximum adsorption capacity of 120 and 109 mg·g−1, respectively, which are both about 6 times higher than pristine UiO-66. Benefitting from high-exposure Rd groups over the surface, UiO-66-Rd p-m exhibits about 3 times faster kinetic adsorption and nearly 15 times higher maximum selectivity coefficient than UiO-66-Rd i-s. Experiment and calculation demonstrate that the excellent performance of Rd-modified UiO-66 is dominantly owing to S chelation in the Rd group. In addition, site energy distributions of the Dubinin-Ashtakhov isotherm model confirm that UiO-66-Rd p-m has more effective sites for Ag(I) adsorption relative to UiO-66-Rd i-s. While a higher density of Rd outside the UiO-66-Rd p-m provides a larger coordination number of S/Ag (1.41) than UiO-66-Rd i-s (0.59), which is attributed to its sufficient exposed active S sites for multidentate coordination of Ag(I), thus significantly enhancing adsorption rate and selectivity. These findings are exploited to shed new insight into the design of adsorbents for the efficient recycling of noble metals from water. [ABSTRACT FROM AUTHOR]