Exploring the novel PES/malachite mixed matrix membrane to remove organic matter for water purification
Graphical abstract
Introduction
Urbanization, climate change, and overpopulation have driven water reclamation to be the core of sustainable alternatives to address global water scarcity. Recycled water can be utilized in an array of fields, including agricultural irrigation, toilet flushing, industrial processing, as well as replenishing sources for drinking water (Michael-Kordatou et al., 2015). The accomplishment of desired water quality requires a certain degree of removal of contaminants from the water sources. Of the water treatment technologies, polymeric membranes have soared as a most effective and reliable practice widely used in biological and chemical wastewater/water treatment and/or pretreatment for the nanofiltration and reverse osmosis modes (Ahmad et al., 2013, Ly et al., 2018b, Zhang et al., 2017), due to the absolute separation of impurities, stable water filtration, compact design and low chemical addition (Ahmad et al., 2013).
Interest in polymeric ultrafiltration (UF) membrane materials continues to rise in using polyethersulfone (PES), accredited to its excellent physical and chemical properties (Shen et al., 2012). However, the hydrophobic nature of PES leads to easy fouling, and hinders the permeability with increasing chemical and energy consumption, and shorten membrane lifespan (Sutzkover-Gutman et al., 2010). In recent decades, the incorporation of inorganic nanoparticles (NPs) in polymer matrices has developed beyond expectation, most notably for titanium (Ti) (Li et al., 2009, Razmjou et al., 2011, Vatanpour et al., 2012, Wu et al., 2008, Yang and Wang, 2006), silica (Si) (Yu et al., 2009), silver (Ag) (Basri et al., 2011, Li et al., 2013), and zirconium (Zr) (Rajabi et al., 2015, Shen et al., 2012). Such synthesis has been reported to be a promising route to enhance permeability, selectivity, physicochemical and mechanical stability of the pristine membranes (Dlamini et al., 2019). For example, Li et al. (2009) stated that introducing TiO2 NPs into the PES membrane can either make the hybrid membrane more water permeable or increase the tensile strength using the optimal dose of 1–2 wt.%. Noted in other literature when using Zr-based NPs it was found that much smaller weights of approximately 0.2–0.4 wt.% is required to obtain exceptional performance of the nanocomposite PES membrane (Shen et al., 2012).
In this context, the incorporation of copper (Cu) NPs into membranes has also attracted much attention (Akar et al., 2013, Ben-Sasson et al., 2014, García et al., 2018, Nasrollahi et al., 2018). A very recent study fabricated the PES/CuO membrane and reported that a nanocomposite membrane blended with 0.2 wt.% CuO NPs approximately doubled the flux in comparison to the pristine PES membrane (Nasrollahi et al., 2019). The Cu NPs can be synthesized from the chemical reduction of Cu-based inorganic salts using a basic reduction procedure. Cu-based salts are essential materials for a myriad of industrial, agricultural, or mining applications (Bilal et al., 2013, Jančula and Maršálek, 2011). CuSO4, for instance, is considered to be the most known algaecide and herbicide used in agriculture (Jančula and Maršálek, 2011). As such, their existence in the waste solid or wastewater effluent is inevitable and problematic, because exposure to excessive Cu2+ cation is well documented to cause severe detrimental health effects such as nausea, respiratory impairment, liver and kidney failure (Bilal et al., 2013). Another copper compound, malachite Cu2(OH)2CO3 (MLC) is a natural mineral, extensively applicable in jewelry, artwork, fertilizer, wood preservative and electronic devices (Molchan et al., 2008, Saha and Das, 2009, Srivastava et al., 2015). Besides, MLC and its nano-sized forms have been proven to be far less toxic than the CuSO4 (Arnold et al., 2003, Lee et al., 2016, Wang et al., 2014). As such, this merit suggests the possibility of being capable of recovering the potential toxic Cu ion waste into more useful MLC NPs that can be incorporated into the PES polymer matrix. To date, the physicochemical characteristics of the mixed matrix Cu-based nanocomposite membranes have not been fully explored as yet, and thus, deserve further investigation.
Aside from the matrix structure, the successful membrane application is mostly dependent upon the degree of fouling. Among these reported fouling factors, organic constituents in water are highlighted as critical components responsible for membrane fouling (Ly and Hur, 2018, Sutzkover-Gutman et al., 2010). Additionally, the removal of natural organic matter (NOM) is of great importance because of its catastrophic reservoir for carcinogenic disinfection byproducts (DBP) upon chlorination (Yang et al., 2008). Dissolved organic carbon (DOC) is widely adopted as a foremost parameter to determine the rejection and fouling potential of organic matters quantitatively. The major drawback of this technique lies in the fact that it is not sensitive and provides no information on chemical compositions (Ly et al., 2019). Recently, special attention has been paid to optical methods, such as ultraviolet–visible absorbance (UV–Vis) and fluorescence spectroscopy, of which the powerful credits are rapid, highly sensitive and robust (Henderson et al., 2009) and yet to the best of our knowledge their applications on evaluation of NOM rejection using different tailored nanocomposite membranes have not been explored. Consequently, this study is directed by having two primary objectives, that are: (1) to fabricate and to examine the nanocomposite PES/MLC MMMs properties, and (2) to evaluate the fouling potential, adsorption, and rejection of organic matter by the novel MMMs.
Section snippets
Materials
PES with MW of 62,000 g/mol was acquired from Solvay Advanced Polymer (Belgium). PEG (MW = 1000 g/mol) was purchased from Tianjin Kermel Chemical Reagent Co. Ltd. Both were dried in the oven at 70 °C for 4 h before being used. The solvent DMAc (N, N-dimethylacetamide) was supplied by BASF (Germany). All the chemical reagents (NaCl, CaCl2, NaHCO3, CuSO4·5H2O, Na2CO3, and ethylene glycol (EG)) were purchased from Tianjin Kermel Chemical Reagent Co. Ltd. The standard Suwannee River NOM (SRNOM, 2R101N)
MLC NPs and PES/MLC MMMs characterized by FTIR, XRD and Raman analyses
The FTIR spectra of the MLC NPs and the nanocomposite membranes are shown in Fig. 1a. FTIR of MLC NPs indicated the broad band at around 3000–3500 cm−1 representing the stretching vibration of –OH group, intensive peaks at 1500 and 1384 cm−1 were attributed to ν3 asymmetric carboxylate (CO3−) stretching modes (Fig. 1a). The ν1 symmetric CO3− vibration was observed referring to the sharp peak at 1096 cm−1. Finally, some absorption peaks at 700, and 800 cm−1 were correspondingly assigned to ν2 and ν4
Conclusions
The PES/MLC membranes were successfully fabricated by vapor and non-solvent induced phase separation and interaction of MLC NPs with the polymer solution posed greatly influence on the morphology of the membrane. The results demonstrated that adding MLC NPs to the PES membrane decreased the contact angle, making the membrane more hydrophilic. At the optimal amount of 0.1 wt.% (M3), the membrane displayed the best water flux of 931.1 LMH and revealed the highest tension strength of 5.06 ± 0.33 MPa.
Conflicts of interest
None declared.
Acknowledgments
We gratefully acknowledge the financial supports for this work from National Natural Science Foundation of China (Grant No. 21878230) and Tianjin Science and Technology Planning Project (Grant No. 18PTZWHZ00210), and Postdoctoral International Exchange Program project as well as the Chang-jiang Scholars and Innovative Research Team in the University of Ministry of Education, China (Grant No. IRT-17R80). The Program of Introducing Talents of Discipline to Universities of China (111 Program)
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