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Metal-Organic Frameworks (MOFs) Incorporated Polymeric Membranes for the Removal of Hazardous Materials from Wastewater

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Abstract
Rapid industrial development, urbanization, and population growth have given rise to an immense responsibility to address increasing water scarcity and environmental pollution issues. Currently, the volume of textile wastewater discharged into the aquatic environment is rising enormously. The purification of harmful textile dyeing wastewater has unveiled several challenges since it comprises a complex mixture, counting dyestuff, additives, microplastics, salts, etc. Moreover, these large quantities of textile wastewater with colored chemicals are non-biodegradable and highly harm humans and creatures living in aqueous environments. Therefore, it is essential to remove the contaminants from textile wastewater. Many conventional techniques, including adsorption, advanced oxidation processing, distillation, flocculation, and membrane separation, have been extensively used for textile wastewater treatment.
Recently, membrane separation has attracted extensive interest for wastewater treatment owing to its excellent benefits of low energy consumption yet higher separation efficiency combined with a convenient operating procedure. Several membrane separation techniques were established, such as microfiltration, ultrafiltration, nanofiltration, and reverse osmosis. Specifically, nanofiltration (NF) technologies offer the highest potential as the most potent candidate for separating organic molecules and inorganic salts. However, developing an innovative NF membrane capable of rejecting almost 100 % of contaminants with high water flux is highly desirable. Numerous studies have focused on fabricating novel composite NF membranes composed of nanofillers and a polymer matrix for selective contaminant removal from wastewater. More recently, synthetic and natural polymers have become the dominant raw materials for fabricating separation membranes. However, polymeric membranes facing several disadvantages, including lack of hydrophilicity, low anti-fouling ability, limited mechanical stability, and insufficient chemical stability. Therefore, they significantly restrict their use in wide-reaching applications.
Membrane modification is a superior technique to overcome these obstacles. Incorporating novel nanomaterials into polymers has impressively contributed to developing renewable composite membranes for wastewater treatment. Metal-organic frameworks (MOFs) have been widely utilized as novel candidates to fabricate futuristic composite membranes due to their high porosity, superior surface area, tunable pore structure, suitable polymers affinity, an abundance of functional groups, and high adsorption capacity. Consequently, in this work, the fabricated PES/MOF-5 membrane was primarily studied to remove hazardous indigo carmine (IC) and methylene blue (MB) dyes. MOF-5 incorporation enhances the permeability and hydrophilicity of the PES membrane with the values of pure water flux (PWF) of 20.5 to 77.1 L/m2 h and contact angle of 73.1 to 60.3°, respectively, even though PES/MOF-5 membrane sustained 97% and 89% rejection of MB and IC, respectively.
Likewise, an Eco-friendly MOF membrane was fabricated with hazardous free MOFs (MIL-100 (Fe)) incorporated into the chitosan (CS) biopolymer. MIL-100 (Fe) incorporation enhances the CS membrane properties, including pore size, surface charge, structural morphology, and hydrophilicity. The CS/MIL-100 (Fe) membrane exhibited the improved pure water flux from 5 to 52 L/m2 h and 99% rejection of cationic methylene blue and anionic methyl orange. The CS/MIL-100 (Fe) membrane rejects the salts in the following trend of MgSO4 (Rreal - 67% and Ractual - 64.2%) > Na2SO4 (Rreal - 59.4% and Ractual - 58.1%) > CaCl2 (Rreal - 49.1% and Ractual - 48.3%) > NaCl (Rreal - 32.6% and Ractual - 32.1%). The CS/MIL-100 (Fe) membrane exhibited excellent rejection and anti-fouling performances with outstanding recycling stability.
Moreover, the removal of harmful dye adsorbed microplastics (MPs) was studied by the PSF/MIL-100 (Fe) membrane. Compared to the pristine PSF membrane (M0), incorporation of the hydrophilic MIL-100 (Fe) nanoparticles significantly modified the morphology, hydrophilicity (water contact angle reduced to 63.2º ±1.2 from 83.6º ±1), porosity, and pore size. Incorporating a 0.5 wt% loading of MIL-100 (Fe) particles into the PSF matrix (M0.5) was initiated to deliver the highest performance relative to the membranes with other loadings. M0.5 membrane includes superior pure water flux (10.3 times higher than M0) with a high methylene blue (MB) rejection rate of more than 99% and excellent anti-fouling properties of MB dye, microplastics (MPs)+MB dye feed solutions. Besides, the M0.5 membrane was sustained with outstanding performances at various concentrations of MB dye, MPs, and a range of transmembrane pressures (TMPs). Furthermore, the membrane exhibited good salt rejection capability and reusability for as many as six cycles of MB dye rejection without compromising the permeability and anti-fouling performance. This study highlights MOFs incorporated polymeric composite membrane offers excellent potential for efficiently removing contaminants from the actual textile wastewater.
Author(s)
Gnanaselvan Gnanasekaran
Issued Date
2021
Awarded Date
2021. 8
Type
Dissertation
URI
https://dcoll.jejunu.ac.kr/common/orgView/000000010222
Affiliation
제주대학교 대학원
Department
대학원 에너지화학공학전공
Advisor
Young, Sun Mok
Table Of Contents
CHAPTER 1 INTRODUCTION AND LITERATURE REVIEW 1
1.1 Background 1
1.2 Membrane separation 3
1.3 List of polymeric membrane used for wastewater treatment 4
1.3.1 Polyethersulfone 4
1.3.2 Chitosan 5
1.3.3 Polysulfone 6
1.4 Membrane flow configurations 7
1.5 Types of membranes process 8
1.5.1 Microfiltration 8
1.5.2 Ultrafiltration 8
1.5.3 Nanofiltration 9
1.5.4 Reverse osmosis 9
1.6 Metal-organic framework (MOFs) 10
1.6.1 MOFs applications 11
1.7 MOFs incorporated polymeric membranes 11
1.8 Hazardous pollutants 12
1.8.1 Dye 12
1.8.2 Methylene blue dye 12
1.8.3 Methyl Orange 13
1.8.4 Indigo Carmine 13
1.8.5 Salts 13
1.8.6 Microplastics 14
1.9 The scope of this present work 15
1.10 References 17
CHAPTER 2 MATERIALS AND METHODS 26
2.1 Introduction 26
2.2 Materials 26
2.2.1 Chemicals 26
2.3 Apparatus 30
2.4 MOF synthesis 30
2.5 Membrane preparation 31
2.6 Material characterization 31
2.6.1 Fourier transform infrared spectroscopy 31
2.6.2 X-ray diffraction 32
2.6.3 BrunauerEmmettTeller (BET) surface area analysis 32
2.6.4 Field-emission scanning electron microscopy 32
2.6.5 Field-emission transmission electron microscopy 33
2.6.6 Energy dispersive X-ray spectroscopy 33
2.6.7 X-ray photoelectron spectroscopy 33
2.6.8 Zeta potential measurement 33
2.6.9 3D nanoprofiller 34
2.6.10 Contact angle measurement 34
2.7 Nanofiltration 35
2.8 Flux recovery ratio 36
2.9 References 37

CHAPTER 3 PERFORMANCE OF COMPOSITE PES/MOF-5 MEMBRANES FOR THE REMOVAL OF HAZARDOUS TEXTILE DYES 39
3.1 Introduction 39
3.2 Preparation and characterization of MOF-5 41
3.3 Membrane preparation 42
3.4 Permeation studies 43
3.5 Rejection of textile dye 44
3.6 Results and Discussion 44
3.6.1 FTIR characterization of MOF-5 44
3.6.2 XRD analysis of MOF-5 45
3.6.3 Surface Morphology of MOF-5 46
3.6.4 Energy Dispersive X-ray Spectroscopy of MOF-5 47
3.6.5 XRD analysis of membranes 48
3.6.6 Surface morphology of membranes 49
3.6.7 EDX analysis of membranes 50
3.6.8 Contact angle measurement of membranes 51
3.6.9 Porosity and pore size of membranes 52
3.6.10 Permeability of membranes 52
3.6.11 Dye rejection 53
3.6.12 Effect of pH 54
3.7 Conclusion 56
3.8 References 57
CHAPTER 4 EFFICIENT REMOVAL OF ANIONIC, CATIONIC TEXTILE DYES AND SALT MIXTURE USING A NOVEL CHITOSAN/MIL-100 (FE) BASED NANOFILTRATION MEMBRANE 63
4.1 Introduction 63
4.2 Preparation of MIL-100 (Fe) 66
4.3 Preparation of CS/MIL-100 (Fe) membranes 67
4.4 Nanofiltration 69
4.5 Result and discussion 69
4.5.1 MIL-100 (Fe) characterizations 69
4.5.2 Membrane characterization 73
4.5.2.1 XRD and FTIR analysis of membranes 73
4.5.2.2 Morphological analyses of membranes 73
4.5.2.3 Surface roughness of membranes 75
4.5.2.4 Elemental analysis of membranes 77
4.5.2.5 Surface charge of membranes 79
4.5.3 Membrane performances 83
4.5.3.1 Permeability of membranes 83
4.5.3.2 Dye rejection of membranes 84
4.5.3.3 Antifouling performance of membranes 88
4.5.3.4 Salt rejection of membranes 88
4.5.3.5 Dye/salt mixture rejection of membrane 91
4.5.3.6 Reusability of membranes 95
4.6 Conclusion 100
4.7 References 101
CHAPTER 5 NOVEL MIL-100 (FE) INCORPORATED HIGH-FLUX POLYSULFONE NANOFILTRATION MEMBRANE AND ITS EXCELLENT REMOVAL PERFORMANCE OF MICROPLASTIC ADSORBED DYE CONTAMINANT FROM TEXTILE WASTEWATER 113
5.1 Introduction 113
5.2 Preparation of PSF/MIL-100 (Fe) membranes 117
5.3 Characterization of PSF/MIL-100 (Fe) membranes 118
5.4 Nanofiltration 118
5.5 Result and discussion 119
5.5.1 XRD analysis of membranes 119
5.5.2 Cross-sectional view of the membrane 121
5.5.3 EDS analysis of membrane 123
5.5.4 Pure water flux of membranes 123
5.5.5 Porosity and mean pore size of membranes 125
5.5.6 Contact angle of membranes 126
5.5.7 Work of adhesion and wetting energy 127
5.5.8 Filtration performance of membranes 128
5.5.8.1 Effect of pH on the membrane performances 129
5.5.8.1.1 MB rejection 129
5.5.8.1.2 Rejection of MPs adsorbing MB 133
5.5.8.2 Effect of concentration on membrane performances 137
5.5.8.2.1 MB rejection 137
5.5.8.2.2 Rejection of MPs adsorbing MB 139
5.5.8.3 Effect of pressure on the membrane 141
5.5.9 Salt rejection of membranes 143
5.5.10 Cycling performance 145
5.6 Conclusions 147
5.7 References 148
CHAPTER 6 SUMMARY AND RECOMMENDATIONS 156
6.1 Summary 156
6.2 Recommendation 157
Degree
Doctor
Publisher
제주대학교 대학원
Citation
Gnanaselvan Gnanasekaran. (2021). Metal-Organic Frameworks (MOFs) Incorporated Polymeric Membranes for the Removal of Hazardous Materials from Wastewater
Appears in Collections:
Faculty of Applied Energy System > Energy and Chemical Engineering
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