P. S.
Nandamol
a and
Mintu
Porel
*ab
aDepartment of Chemistry, Indian Institute of Technology Palakkad, Kerala 678577, India. E-mail: mintu@iitpkd.ac.in
bEnvironmental Sciences and Sustainable Engineering Center, Indian Institute of Technology Palakkad, Kerala 678577, India
First published on 18th December 2024
Metal-based oxo anions are major contributors towards freshwater contamination. Bioaccumulation and biomagnification through food chains pose threats to the sustainability of the environment. We introduced a novel guanidinium-based cationic porous organic polymer (POP) designed for the rapid and efficient removal of permanganate via electrostatic interaction between a cationic polymer and the anionic pollutant permanganate. The polymer had exceptionally high uptake of 9.4 g g−1 for permanganate ions. This is far superior than that reported in the literature. The material exhibited rapid sorption kinetics and a removal efficiency of 100%. Moreover, selectivity, pH and recyclability experiments were evaluated to confirm the practical applicability of the material. In addition, we employed two distinct strategies for the synthesis of a guanidinium-based cationic POP: solvothermal and mechanochemical. Both polymers were characterized using CPMAS 13C NMR, FT-IR, powder-XRD, N2 sorption analysis, TGA and FE-SEM. The physicochemical properties of both polymers were compared. The polymers showed 100% removal efficiency for permanganate from aqueous solution. The mechanochemical method did not involve energy consumption, long-time duration or involvement of toxic organic solvents, so the process was environmentally benign and economically viable. The solvothermal method consumed more energy and time. Hence, the mechanochemical method was found to be more efficient, cost-effective and environmentally sustainable for the fabrication of a highly efficient guanidinium-based polymeric adsorbent material for permanganate removal from aqueous solutions.
Potassium permanganate is one of the most common chemical reagents. It is widely used as an oxidizing agent in laboratories and chemical industries. Being a powerful oxidizing agent, it is highly exploited in chemical manufacture, tanning, processing of paper, wood and metals, as well as oxidation of chlorinated solvents and compounds. Advanced oxidation processes employing permanganate as the oxidant have gained paramount importance for the extraction of dyes, cyanide, phenolic compounds and other heavy metal pollutants. The National Institute of Occupational Safety and Health has confirmed that permanganate is hazardous and harmful to human health.6 Large-scale discharge of permanganate ions from industrial effluents causes bioaccumulation and biomagnification through food chains and, hence, it is considered to be a significant contributor towards freshwater contamination. Direct exposure can cause shortness of breath, irritation to skin and eyes, whereas the long-term exposure may lead to DNA damage, and disruption to the central nervous system.7 Therefore, decontamination of water bodies from permanganate ions is crucial for the sustainability and wellbeing of aquatic life.
Potassium permanganate contaminates freshwater sources through its use as an oxidant in chemical and water-treatment plants. In addition, 99Tc is a hazardous radionuclide from the nuclear industry with a long half-life of 2.13 × 105 years and exists primarily as a pertechnetate ion [TcO4−]. It is a great challenge to carry out environmental restoration of TcO4− contamination due to its high solubility in water and strong mobility. Considering its radioactivity and operational difficulties, permanganate [MnO4−] anions have been employed as nonradioactive surrogates for TcO4−.8,9
A number of physical and chemical methods, including ion exchange, adsorption, electrodialysis, nanofiltration, chemical precipitation and membrane filtration, have been employed for the removal of toxic permanganate. Among them, adsorption is one of the most favorable because it is safe, efficient and cost-effective. The development of porous adsorbent materials from inexpensive and readily available raw materials has become a research focus. Activated carbon of coconut shells, bone and corn cob10,11 have been explored as adsorbent materials, and one concern was the high cost of production involved. Later on, cheaper materials such as the modified powder of Nitraria retusa, neem and sage leaves were found to be more economical.12–17 Metallic oxides as well as nanoparticles18–22 have also been found to be useful for removal purposes. However, the uptake performance reported for this type of material has been much lower. Thus, poor selectivity, adsorption kinetics and uptake performance have necessitated the development of new materials for the efficient capture of oxo anions from water. Later on, wide attention was drawn towards porous cationic framework materials. Porous organic polymers (POPs) are an emerging class of polymers noted for their porous nature, high chemical and thermal stability, and functional tunability. Ionic porous organic polymers have gained paramount importance as materials capable of both ion exchange and adsorption. POPs with predesigned tunable structure, porosity, diverse functionality, chemical and thermal stability have been widely studied in terms of adsorption and gas storage. Introducing ionic structures into the framework endows them with interesting properties with respect to their electrostatic nature, which further extends their application. Moreover, a combination of microporosity and extended π conjugation provides them with exciting features.23,24 Besides, cationic POPs have been found to be highly efficient for the sequestration of toxic oxo anions from water. Samanta et al. developed a chemically stable ionic viologen-organic network, and adsorption performance towards permanganate was evaluated to be 297.3 mg g−1.4 Nayak et al. synthesized a pyridinium-functionalized POP which showed adsorption of 333 mg g−1 for permanganate ions.25 Jiao et al. reported targeted synthesis of a novel ionic POP with exchangeable chloride and bromide ions in the framework, which showed a total removal of 514.7 mg g−1 for permanganate ions.26 Sarkar et al. reported a bifunctional imidazolium-functionalized ionic POP which showed an exceptionally high intake of 5372 mg g−1 of permanganate.27
Motivated by such studies, we synthesized a guanidinium-based ionic POP.28–30 The cationic charge in the framework showed better interaction with anionic pollutants, and was responsible for the high ion-exchange ability.31 The polymer was found to be stable, insoluble in water and most organic solvents. The material exhibited exceptionally high uptake capacity of 9.4 g g−1 and fast sorption kinetics for the removal of permanganate ions from aqueous solution. Our POP outperformed other POPs in the literature [Table S1†]. Furthermore, two methods were employed for the synthesis: solvothermal and mechanochemical.32 The synthesized polymers from both methods were characterized by Fourier transform infrared (FT-IR) spectroscopy, cross-polarization magic angle spinning 13C NMR spectroscopy (CPMAS 13C NMR), powder X-ray diffraction (pXRD), field emission scanning electron microscopy (FE-SEM), N2 sorption analysis and thermogravimetric analysis (TGA). A “green” mechanochemical method was found to be as efficient as a solvothermal method, and exhibited similar uptake capacity, as well as structural and physicochemical properties. The removal efficiency, kinetic studies and maximum uptake for permanganate removal were estimated further.33–42
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Scheme 1 Synthetic scheme for [a] TGDM, [b] TMB and [c] guanidinium-based ionic porous organic polymer gn-ipop-cl. |
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Fig. 1 [a] FT-IR spectra for TGDM, and TMB. [b] FT-IR spectra for gn-ipop-cl. [c] CPMAS 13C NMR spectra of gn-ipop-cl. |
The mechanochemical synthesis was found to be advantageous in several aspects: saving time [the polymerization was completed in 45 min whereas it took 72 h for the solvothermal process], lower energy consumption, no harsh experimental conditions and, more importantly, the synthesis was devoid of toxic organic solvents. The FT-IR spectra of TGDM showed the characteristic vibration of the amine group around 3200 cm−1 [Fig. 1a]. TMB showed strong carbonyl stretching around 1700 cm−1 [Fig. 1a]. The strong absorption at 1500–1400 cm−1 for gn-ipop-cl [Fig. 1b] suggested the formation of an imine linkage through Schiff base condensation. The absence of carbonyl and amine peaks in the spectra of gn-ipop-cl further confirmed complete conversion of the monomers. The solid-state 13C NMR spectra of gn-ipop-cl also confirmed the formation of an imine linkage [Fig. 1c]. The peaks observed around 140–150 ppm corresponded to imine carbon.
The powder X-ray diffraction pattern of gn-ipop-cl(MC) [“MC” denoting “mechanochemically synthesized polymer”] exhibited several intense peaks at 2θ 20 to 40, indicating the crystallinity of the sample. This observation could be attributed to molecular confinement in the crystal lattice of the monomer, offering precise control over the packing and crystallinity of the polymer. This effect occurred under the stimuli of heat and pressure. gn-ipop-cl(ST) [“ST” denoting “solvothermally synthesized polymer”] showed a broad diffraction peak suggestive of the amorphous nature of the polymer [Fig. 2a and b]. The thermal stability of the sample was analyzed using TGA, and found to be stable up to 300 °C [Fig. 2c and d].
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Fig. 2 pXRD pattern of [a] gn-ipop-cl(ST) and [b] gn-ipop-cl(MC). TGA profile of [c] gn-ipop-cl(ST) and [d] gn-ipop-cl(MC). BET surface area for [e] gn-ipop-cl(ST) and [f] gn-ipop-cl(MC). |
Nitrogen-sorption analyses performed at 77 K indicated a Brunauer–Emmett–Teller (BET) surface area of 28 m2 g−1 and 34 m2 g−1 for gn-ipop-cl(ST) and gn-ipop-cl(MC), respectively [Fig. 2e and f]. The pore volume obtained was 26 and 33 cc g−1 for gn-ipop-cl(ST) and gn-ipop-cl(MC), respectively. These values were nearly identical for the mechanochemical method as well as the solvothermal method. Furthermore, the morphological characterization of the polymer was performed using field-emission scanning electron microscopy (FE-SEM). Results indicated that the synthetic method had a great influence on the morphology of the polymer because the solvothermal and mechanochemical synthesis resulted in entirely different morphologies of the material [Fig. 3]. Elemental analyses of gn-ipop-cl [Fig. S6†] showed the presence of 50–60% C, 15–20% N, 25–35% O and 6–8% Cl atoms in the framework. The chemical robustness of gn-ipop-cl(ST) and gn-ipop(MC) was evaluated by incubating the material in acidic condition (2 N HCl) and basic condition (2 N NaOH) for 7 days. The structural integrity was evident from the unchanged FTIR spectra before and after treatment (Fig. S7†). The crystallinity of the polymer created by the mechanochemical method remained intact after incubation according to the pXRD pattern (Fig. S8†). The superior quality with respect to the crystallinity and environmentally benign nature of the synthesis prompted selection of gn-ipop-cl(MC) as an adsorbent material, and was further explored for studies on permanganate adsorption.
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Fig. 3 Field emission scanning electron microscopy images of [a and b] gn-ipop-cl(ST) and [c and d] gn-ipop-cl(MC). |
The decrease in absorbance of permanganate with time [Fig. 4a] clearly indicated the removal of permanganate ions from water. The polymer showed a adsorption kinetics with a removal efficiency of 100%. It was evident from the absorbance spectra that the absorbance decreased to zero after 20 min of contact for gn-ipop-cl(MC) and 30 min for gn-ipop-cl(ST) [Fig. 4c and d]. Each experiment was done in triplicate, and the final kinetic data fitted with a pseudo first-order equation and second-order rate equation. For gn-ipop-cl(ST) as well as gn-ipop-cl(MC), kinetic data fitted well with pseudo second-order kinetics with a high R2 value (>0.99) [Fig. 4e and f]. This finding revealed the dependence of adsorption on the concentration of permanganate as well as the number of available active sites.
In order to calculate the total uptake capacity of the polymers, 1 mg of polymer was treated with a 1 mL solution of varying concentrations of potassium permanganate. The maximum uptake capacity was calculated to be 9.397 and 9.277 g g−1 for gn-ipop-cl(MC) and gn-ipop-cl(ST), respectively [Fig. 5a and b]. Data were evaluated using the Langmuir adsorption model [Fig. 5c and d]. In order to mimic the true situation, selectivity studies were performed in the presence of other competing anions [Fig. 6a and b]. Anions such as Cl−, Br−, NO3−, and SO42− were chosen as competing anions because they are omnipresent in common water sources. An aqueous solution of targeted oxo anion and competing anion in an equimolar ratio was stirred with polymer adsorbent until equilibration, and total uptake of permanganate was evaluated. Studies on this binary mixture revealed that the removal efficiency of permanganate ions remained almost unchanged even in the presence of competing anions in the solution. Moreover, the reusability of the polymer was evaluated for up to five cycles [Fig. 6c and d]. After each cycle, the polymer was collected through centrifugation, and washed with deionized water and organic solvents. It was then incubated with a saturated KCl solution for 1 day, washed and dried and used for the next cycle. The adsorption performance was also evaluated with solutions of different pH [Fig. 6e and f]. The effect of pH on removal efficiency was negligible, indicating the applicability of the material in a broad range of pH. The temperature dependence of adsorption of permanganate over gn-ipop-cl was also evaluated [Fig. S11†]. There was a slight decrease in the adsorption performance upon increasing the temperature from 25° to 45 °C [Fig. S11†]. This observation could be attributed to the physical nature of adsorption. The decrease in adsorption capacity with increasing temperature indicated that adsorption was exothermic in nature. This might have been due to the weakening of adsorptive forces between permanganate and the active sites on the adsorbent surface as a result of increase in temperature.
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Fig. 5 Isotherm analyses of [a] gn-ipop-cl(MC) and [b] gn-ipop-cl(ST). Langmuir adsorption model for [c] gn-ipop-cl(MC) and [d] gn-ipop-cl(ST). |
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Fig. 6 Selectivity studies for [a] gn-ipop-cl(MC) and [b] gn-ipop-cl(ST). Recyclability tests for [c] gn-ipop-cl(MC) and [d] gn-ipop-cl(ST). pH studies for [e] gn-ipop-cl(MC) and [f] gn-ipop-cl(ST). |
The structural integrity of post-treated materials was analyzed using FT-IR, pXRD, FE-SEM as well as EDX analyses. A vibrational stretching frequency around 1000 cm−1 confirmed the presence of MnO4− in the framework [Fig. S12†]. The crystallinity and morphology of the polymer remained unchanged after adsorption [Fig. S13 and S14†]. Elemental analyses confirmed the presence of Mn in the framework [Fig. S15†]. Moreover, the negligible amount of Cl− in the post-treated polymer suggested the possibility of ion exchange.
Thus, the material exhibited exceptionally high uptake for permanganate ions from water (Fig. 7). This finding could be attributed to the strong adsorptive interaction due to electrostatic forces between the anionic pollutant and cationic active sites in the polymer framework.
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Fig. 7 Photographs of permanganate solution and polymer adsorbent before and after adsorption of permanganate. |
gn-ipop-cl(MC) and gn-ipop-cl(ST) showed identical activity in studies for the removal of permanganate ions. The mechanochemically synthesized guanidinium-based ionic POP was easier to synthesize, had a faster process and showed superior properties compared with its solvothermal analogue, and retained similar activity.
We sincerely acknowledge the Central Instrumentation Facility (CIF) at the Indian Institute of Technology, Palakkad, and SAIF Indian Institute of Science, Bangalore, India.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4py01329h |
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