Abstract
The preparation, modification and application of green polymers such as poly-lactic acid (PLA), chitosan (CS), and cellulose acetate (CA) for oily wastewater treatment is summed up in this review. Due to the low environmental pollution, good chemical resistivity, high hydrophobicity, and good capacity for water-oil emulsion separation of the presented polymers, it then highlights the various membrane production methods and their role in producing effective membranes, with a focus on recent advances in improving membrane properties through the addition of various Nano materials. As a result, the hydrophilic/hydrophobic properties that are critical in the oil separation mechanism are highlighted. Finally, it looks at the predictions and challenges in oil/water separation and recovery. These ideas are discussed with a focus on modern production methods and oil separation proficiency.
HIGHLIGHTS
Recently, eco-friendly membranes play an important role in the positive environmental impact and environmental conservation. This review provides insights into understand of eco-friendly membrane applications for water–oil processing, where nanofiltration and ultrafiltration eco-friendly membrane systems are mostly applied to the treatment of oily-wastewater effluent.
Graphical Abstract
NOMENCLATURES
- Ag NPs
Silver nanoparticles
- Alg
Alginate
- ALG
Sodium alginate
- CA
Cellulose acetate
- CaCO3
Calcium carbonate
- CM
Cellulose membrane
- CMC
Carboxymethylcellulose
- CNF
Cellulose nanofiber
- CNTs
Carbon nanotubes
- CS
Chitosan
- CST
Chitosan–TiO2
- CT
Chitin
- DMAc
Dimethylacetamide
- DPA
Dopamine
- DSD
Droplet size distribution
- ER
Epoxy resin
- Fe3O4
Iron oxide
- FeCl3
Ferric chloride
- FP
Filter paper
- GA
Glutaraldehyde
- GO
Graphene oxide
- HDTMS
Hexadecyltrimethoxysilane
- LDH
Layered double hydroxides
- MCA
Modified cellulose acetate
- MCE
Mixed cellulose membrane
- MCS
Modified chitosan
- MF
Microfiltration
- MTS
Methyltrichlorosilane
- NaCl
Sodium chloride
- NaClO2
Sodium chlorite
- NaOH
Sodium hydroxide
- NBKP
Cellulose needle-leaf bleached kraft pulp
- N-CQDs
Amino-functionalized carbon quantum dots
- NF
Nanofiltration
- OCA
Oil contact angle
- PAN
Polyacrylonitrile
- PBE
Propylene-based elastomer
- PBS
Poly (butylene succinate)
- PCL
Poly (ε-caprolactone)
- PDA
Polydopamine
- PDLA
Poly (D-lactic acid)
- PEG
Poly (ethylene glycol)
- PET
Polyethylene terephthalate
- PHAs
Polyhydroxyalkanoates
- PHB
Polyhydroxybutyrate
- PLA
Poly lactic acid
- PLGA
Poly (lactide-co-glycolide)
- PPC
Polypropylene carbonate
- PPF
Poly (propylene fumarate)
- PPS
Polyphenylene sulfide
- PPy
Polypyrrole
- PS
Polystyrene
- PSf
Polysulfone
- PVA
Polyvinylpyrrolidone
- PVDF
Polyvinylidene fluoride
- PVDF-HFP
Poly (vinylidene fluoride-co-hexafluoropro-pylene)
- RHs
Relative humidity
- RO
Reverse osmosis
- SeP
Sepiolite
- SiO2
Silicon dioxide
- SMPLA
Superhydrophobic and magnetic poly (lactic acid)
- SNPs
Silica nanoparticles
- SOCM
Superhydrophobic cellulose membrane
- TA
Tannic acid
- TEOS
Tetraethyl orthosilicate
- TiO2
Titanium dioxide
- UF
Ultrafiltration
- UOCA
Underwater oil contact angle
- USEPA
United States Environmental Protection Agency
- WCA
Water contact angle
- WO3
Tungsten oxide
- XPS
X-ray photoelectron spectrometer
- ZIF-8
Zeolite imidazole framework
INTRODUCTION
Oily wastewater refers to wastewater that contains fats, greases, and oils in high concentrations, together with a variety of dissolved components (organic and/or inorganic) (Adetunji & Olaniran 2018; Wei et al. 2020). There are four types of oil-contaminated water (also known as ‘oily wastewater’): free oil, dispersed oil, emulsified oil, and dissolved oil (Saththasivam et al. 2016). These types are based on physical and chemical properties, with the droplet size distribution (DSD) being a major parameter (El-Naas et al. 2014). Free oil separates from water with ease and floats to the surface in calm conditions due to its lower specific gravity than water. The size of oil droplets in wastewater ranges between micron-sized particles and larger droplets (Al-Ani et al. 2020). The DSD of dispersed oil is normally in the range of a hundred to several hundred microns, and it is characterized such that it takes the form of droplets of oil in water (Li et al. 2015). While oil–water mixtures move through pipes or pumps, oiled wastewater or natural occurrences like agitation and wave action or operations which break up free oil droplets and distribute them generate dispersed oils. (Abdulredha et al. 2020). Emulsions can be formed by stabilizing the oil droplets in the dispersion or by coalescing them to produce free oil over time. Either mechanical or chemical stabilized emulsions are oil emulsions generated by dispersing oil droplets in water (Nikovska 2012; Loh et al. 2020). Conditions and relative proportions of oil and water components can produce various emulsions, including simple emulsions like o/w and w/o, as well as more complex emulsions like o/w/o. Simple emulsifiers, like oil–water and water–oil, are more widely used in petroleum, drug, and food industries than complex emulsions (Haghighat et al. 2020). There are no droplets of oil in the water when the oil dissolves in the water. Hydrocarbons that have one or more rings (benzene, for example), as well as aromatic hydrocarbons (naphthalene and organic acids) are the most common components of dissolved oil (Fakhru'l-Razi et al. 2009).
The United States Environmental Protection Agency (USEPA) classifies (oil-contaminated) wastewater as among the most toxic and harmful wastewaters in the environment. When oily wastewater is incorrectly released, it pollutes the air and contaminates groundwater and surface waters, posing a serious threat to the surrounding environment and human health (Poulton et al. 2002; Robertson et al. 2007; Hejnfelt & Angelidaki 2009; Ibrahim et al. 2016; Mearns et al. 2020; Yazdan et al. 2020).
Though it's possible to completely clean out the oil from the water, this is made more difficult by oil–water emulsions, which are more stable because of various components in the oil or the water that act as emulsion binders such as asphalting and resin, as well as clay particles, mineral salts and so on (Victorovna 2001). To address this issue, a variety of ways have been developed to break down oil–water emulsions: biological and chemical as well as mechanical (settling tanks, cyclones, centrifuges, and separators), thermal, and electrical, microwave, ultrasonic, and membrane separation techniques (Padaki et al. 2015). To separate oil droplets smaller than 10 m, membrane filtration is a promising mechanism (Tanudjaja et al. 2019). As a result, ultrafiltration (UF) and tighter microfiltration (MF) are the better options for separating oil droplets in the 1–10 μm size range from water (Ghadhban et al. 2020; Lee & Patel 2020; Yahya et al. 2021).
Because of ongoing research and development in both academia and the private sector, the membrane technology market has experienced probably much higher growth. It is also becoming increasingly popular as a separation and purification technique because of the advantages of membrane technology, including its low energy consumption, high efficiency, simplicity of continuous operation, and little environmental impact (Lee & Darling 2016). Wastewater treatment, desalination, food processing, chemicals, and pharmaceuticals have all used membrane separation technology effectively for several decades, showing both its technical and economic virtues (Fane et al. 2015; Abbas et al. 2022).
Polymer membranes are semi-permeable polymer filter media being used pressure-driven treated water. Polyvinylidene fluoride, polysulfone, polycarbonate, polyethersulfone, cellulose acetate, and polyamide are all examples of polymeric materials that can be used in the manufacturing of plastic products. Additionally, in polymeric membranes, the pore size of the membrane can be easily controlled during the manufacturing of the membrane. The installation necessitates a high degree of flexibility and a smaller area (Alsalhy et al. 2018). The membrane separation industry prefers polymeric membranes because of their low cost and wide range of potential uses. Polymer membranes, which are also known as organic membranes, are commonly referred to as such. Polymer membranes are part of a larger family of membranes. Polymer membranes can be replaced by ceramic membranes, which are also called inorganic membranes (Chen et al. 2016; Zhu et al. 2016; Chen et al. 2019; Zhong et al. 2021a).
Enhancing the sustainability of membrane production is an important goal for the field of membrane technology. Despite the many potential uses for membrane technology, our focus was on polymeric membranes and their effect on solvents over the long term. Numerous of the research included in this research concentrated on identifying greener alternatives. The term ‘green’ membrane encompasses two distinct but related concepts. However, the use of renewable resources in place of oil-derived plastics is a good option. On the other side, other chemicals like modifiers, solvents, and additives used in the membrane manufacturing process should present the least degree of hazard as feasible and should be sourced from renewable sources, non-toxic to the environment, and reusable from waste (Capello et al. 2007; Figoli et al. 2014; Hadi et al. 2020).
However, the manufacturing of the membrane itself should not include the use of hazardous chemicals. The benefits of a greener and environmental preparation method are immeasurable; therefore, an excellent toxicity profile and specific physical properties, like solubility in water, a low molecular weight, and a high boiling point make this alternative to hazardous solvents the best solution for replacing them without affecting membrane performance (Al-Ani et al. 2019; Kadhim et al. 2020).
Previous reviews highlighted a general topic on membrane synthesis, preparation, and modification, as they looked at membrane formation, installation techniques, fouling membranes, or manufacturing procedures (Jiang et al. 2021; Mamah et al. 2021; Shi et al. 2021; Singh et al. 2021). Without the specialization and focus in studying of the green membranes and their positive influence on the environment on the one hand, and the possibility of their recycling and the economic value of preparation and applications on the other hand (Wang et al. 2017; Xiong et al. 2019; Bandehali et al. 2021). The aim of this review is to illustrate researchers' and scientists' efforts to develop and apply greener synthesizing pathways, as well as chemical processes which progressively have been more sustainable and greener in order to avoid ecological impacts. In addition, give some suggestions, prior strategies, and future studies of prospects for achieving significant enhancements in membrane development. There is also research on the use of membranes in wastewater treatment and oil–water emulsion separation and a variety of membrane-modification techniques are investigated.
OIL–WATER EMULSIONS SEPARATION MECHANISM
GREEN (BIODEGRADABLE) POLYMER MEMBRANE
Synthesis of a green biodegradable membrane for use in a variety of separation processes is an eco-friendly approach that shows a new method of thinking in chemistry that aims to get rid of toxic waste, decrease energy consumption, and make use of environmental solvents. Effective separations of emulsions are a growing issue due to the increasing amount of oily wastewater and the oil spills caused by the sinking of oil tankers, industrial accidents and other ships. Many studies in recent years have concentrated on creating various membranes to improve the mechanical separation of emulsions. Several polymers were used to prepare membranes for o/w separation. In response to the growing demand for sustainable and cost-effective membrane production methods, many studies have focused on creating and synthesizing a membrane from green basic material (Figoli et al. 2014). As a consequence, bioplastics, such as bio-based and petroleum-based biodegradable polymers, gained a lot of interest in recent years (Hamad et al. 2014). Bio-based and petroleum-based polymers refer to bioplastics derived from both biological and fossil sources. There are two types of biopolymers: those that degrade and those that don't degrade. Biodegradable bioplastics are those that can be broken down by microorganisms in the natural environment. Polymers that degrade in the environment come in three varieties: plants, animals, and synthetically created. Polylactic acid (PLA), poly (lactide-co-glycolide) (PLGA), cellulose acetate (CA), polyhydroxyalkanoates (PHAs), collagen and sericin, chitosan/chitin (CS/CT), poly (vinyl alcohol) (PVA), lignin, alginate (Alg), starch, poly (butylene succinate) (PBS), poly (propylene fumarate) (PPF), poly (ε-caprolactone) (PCL), and other infrequently utilized polymeric materials polymers that degrade in the environment. PHAs, PLA, PLGA, lignin, starch, Alg, and CA acetate are all polymers derived from plants or vegetables. Collagen and sericin are both derived from animals. Chitosan/chitin may be acquired from both plant and animal sources. PBS, PPF, and PCL are synthetic biodegradable polymers. Table 1 provides some advantages and disadvantages of the investigated green material with other options. It has been shown that the use of these substances is increasing at a rate of roughly 10% to 20% every year (Kumar & Maiti 2016; Chang et al. 2021). Since their first use in the packaging sector, the uses of biodegradable polymers have been expanded to include a variety of industries, including membrane separation technologies (Safi et al. 2020; Rashid et al. 2022). In nature, polymers can be either biodegradable or not; this implies that several natural polymers might not have been biodegradable. It is critical that plastic supply be renewable, both environmentally and economically, as well as that its disposal in the natural environment be done without concern or made of recycled (Credou & Berthelot 2014; Lee et al. 2021). Lastly, a great number of used membranes ought to be recycled and reused again. This review therefore investigates the membrane industry's transformation requirements in the context of recycling and reuse.
Polymer Type . | Advantage . | Disadvantage . | Ref. . |
---|---|---|---|
PLA | Biodegradable, biocompatibility, eco-friendly material, good physical and mechanical properties, safe, non-toxic | Hydrophobicity | Zaaba & Jaafar (2020); Amini et al. (2021) |
CS | Biodegradable, biocompatibility, good solubility, bioactivity, non-toxic | Low mechanical, may contract. | Nunes et al. (2021) |
CA | Biodegradable, easy processing, raw material from renewable resource, non-toxic | Low chemical resistances, low mechanical strength | Zaaba & Jaafar (2020); Kamal et al. 2014) |
PEG | Biocompatibility, stable dissolution, good substrate for restore physiological functions | Hydrophilicity | Amini et al. (2021) |
PSf | High mechanical properties, high chemical, and thermal stability | Hydrophobic | Ali et al. (2014); Dmitrieva et al. (2022) |
PVDF | Good chemical, mechanical, thermal stability | Hydrophobicity | Dmitrieva et al. (2022); Dumitrescu et al. (2020) |
Polymer Type . | Advantage . | Disadvantage . | Ref. . |
---|---|---|---|
PLA | Biodegradable, biocompatibility, eco-friendly material, good physical and mechanical properties, safe, non-toxic | Hydrophobicity | Zaaba & Jaafar (2020); Amini et al. (2021) |
CS | Biodegradable, biocompatibility, good solubility, bioactivity, non-toxic | Low mechanical, may contract. | Nunes et al. (2021) |
CA | Biodegradable, easy processing, raw material from renewable resource, non-toxic | Low chemical resistances, low mechanical strength | Zaaba & Jaafar (2020); Kamal et al. 2014) |
PEG | Biocompatibility, stable dissolution, good substrate for restore physiological functions | Hydrophilicity | Amini et al. (2021) |
PSf | High mechanical properties, high chemical, and thermal stability | Hydrophobic | Ali et al. (2014); Dmitrieva et al. (2022) |
PVDF | Good chemical, mechanical, thermal stability | Hydrophobicity | Dmitrieva et al. (2022); Dumitrescu et al. (2020) |
Poly lactic acid (PLA)
PLA is a biodegradable polymer generated from renewable sources such as sugarcane, corn, and cellulose. It has biodegradable thermoplastic with good biocompatibility and absorbability. PLA has been used mostly in clinical uses such as implant devices, tissues scaffold, and internal sutures up until the last decade due to its high cost, scarce availability, and restricted molecular weight (Galiano et al. 2019). New methods for producing high-molecular-weight PLA polymers at a lower cost have emerged, expanding the material's potential applications (Huang et al. 2016). As a biodegradable and renewable resource, PLA has been proposed as a reasonable solution to society's mounting solid waste disposal issues (Ummartyotin & Pechyen 2016). PLA is a member of a class of aliphatic polyesters that are generated from hydroxy acids. Lactic acid (2-hydroxy propionic acid), a PLA building block, can be found in both optically activated- and l-enantiomers. PLA with varying material qualities can be made based on the number of enantiomers. This enables the manufacture of a broad range of PLA polymers to meet a variety of performance needs. In comparison to existing petroleum-based polymers, PLA possesses reasonable physical, optical, barrier and mechanical properties (Naffakh et al. 2014).
A biodegradable PLA-based hierarchical functionalized electrospun nanofibrous membrane was successfully fabricated. Nanoscale Ag-NPs on the PLA nanofibers were used to create the hierarchical rough structure by adhering them to the PDA layer by (Liu & Yuan 2018). Fluorinated thiols were then added to the surface to create the super hydrophobic/superoleophilic properties. The super hydrophobicity (θ water = 158.6°) of the produced nanofibrous membrane was found to be stable in a variety of solutions, including alkali, salt, and acid. As a result, the membranes were shown to have a high penetration flux (2,664 Lm−2h−1) for a wide range of oils and an acceptable separation performance (more than 95%) separation efficiency for both various oil–water solutions and surfactant stabilized water–oil emulsions). This nanofiber's hydrophobicity (θ water = 142.3°) and hierarchical rough structure were able to hold up after 20 times of repeated use due to the durability of the Ag NPs fixed on the nanofibers and show better recyclability.
Table 2 summarizes the evolution of modern PLA membrane types, where a good rejection rate of more than 90% can be achieved due to an improved membrane structure. Such as improving contact angle, porosity, and pore size, this is done by improving the membrane characteristics by adding the appropriate additives to the polymer casting solution through the membrane preparation.
Membrane . | Oils . | Additives/component Used . | Performance/efficiency . | Pore size . | Porosity . | Contact angle . | Ref. . |
---|---|---|---|---|---|---|---|
PLA nonwoven filter | soybean oil, N-hexane, styrene, diesel oil, N-heptane, silicone oil | chloroform ethanol | more than 95% | 10–100 μm | high | WCA 151° | Fan et al. (2020) |
SMPLA nonwoven fabric | n-hexane, toluene, carbon tetrachloride, cyclohexane, ethanol, and diethyl ether | DPA PVDF-HFP | up to 99.5% | / | 6.78–9.91% | WCA 151.7° | Zeng et al. (2020) |
PLA foam | different oils and organic solvents | dioxane | 98% | / | >90% | WCA 151° | Wang et al. (2019) |
PLA filtration films | petroleum ether, gasoline, diesel oil, and vegetable oil | NaCl | more than 97% | 500 nm–10 μm | WCA 153.5 ± 1.7° | Xue et al. (2013) | |
PLA@TiO2@MTS nanofibrous membrane | soybean oil, toluene, carbon tetrachloride, petroleum ether and n-hexane | TiO2 MTS | more than 95% | / | / | WCA 157.4 ± 0.9° | Zhou et al. (2019a) |
Nano-PLA nonwoven fabric | castor oil, petroleum ether, n-hexane, silicone oil, lubricating oil | ER KH-560 | 96% | 100 μm | / | WCA 152.1° | Lu et al. (2022) |
ZIF-8@PLA composite aerogel | cyclohexane, petroleum ether, vegetable oils, n-heptane, CCl4 | ZIF-8 | close to 100% | 10–30 nm | / | WCA 145° | Li et al. (2021a) |
PLA/WO3/N-CQDs fiber | hexadecane n-hexane, and n-heptane | WO3/N-CQDs | 91.80% | 1.848 ± 0.328 μm | / | WCA 132.37° | Nugraha et al. (2021) |
PLA/PPC PLA/PHB PLA/PBS PLA/TEC | oil and grease | PBS, PPC, PHB, SNPs | more than 98% | 18.3–28.55 nm | good | / | Ghorbani et al. (2021) |
PLLA films | petroleum ether | chloroform | 99.1% | / | 69.5–87.5% | WCA 152.1° | Sun et al. (2021) |
PLA/PBE micro-nanofiber fabrics | soybean oil | PBE | excellent | / | / | WCA 134° | Li et al. (2022) |
PLLA/SiO2 nanocomposite membrane | oil (red) | SiO2 | effective | / | / | WCA 167.1° | Zhong et al. (2021b) |
Modified PLLA nonwoven fabric | hexane, toluene, and tetrachloromethane | PDLA | more than 97% | / | / | WCA 130.8 ± 1.5° | Zhu et al. (2020) |
PLA fiber membrane | n-hexane, olive oil, and lubricant oil | chloroform N, N dimethylformamide | more than 99.98% | 500 nm–1 μm | 92 ± 4.1% | WCA 150.3° | Liu et al. (2019a) |
Janus PLA fibrous membrane | carbon tetrachloride, n-hexane, and petroleum ether | SiO2 CNTs | more than 99% | / | / | WCA is more than 142° | Qin et al. (2020) |
PLA/γ-Fe2O3 composite membranes | motor oil, silicone oil, castor oil, corn oil, lubricating oil, sunflower oil, n-hexane, olives oil, cedar oil | γ-Fe2O3 | high separation | / | >90% | WCA 148° | Zhang et al. (2019) |
PLA packing | n-hexane | PS | 95% | 4–200 μm | / | WCA 150° | Xing et al. (2019) |
PLA porous membrane | n-hexane | PS | 99.4% | ∼25 μm | / | WCA 151.7° | Xing et al. (2018) |
Advanced PLA non-woven fabric | n-hexane and tetrachloromethane | TiO2 | 86.9% | / | / | WCA 150° | Shi et al. (2018) |
Nanofibrous PLA membrane | toluene | PDA | 98.4 ± 1.0% | / | high | WCA 158.6° ± 1.2° | Liu & Yuan (2018) |
SiO2/PS/PLA non-woven fabric | hexane, soybean oil, toluene, pump oil, tetrachloromethane, and vegetable oil | SiO2 PS | efficient | / | / | WCA 152.0 ± 2.1° | Gu et al. (2017) |
Membrane . | Oils . | Additives/component Used . | Performance/efficiency . | Pore size . | Porosity . | Contact angle . | Ref. . |
---|---|---|---|---|---|---|---|
PLA nonwoven filter | soybean oil, N-hexane, styrene, diesel oil, N-heptane, silicone oil | chloroform ethanol | more than 95% | 10–100 μm | high | WCA 151° | Fan et al. (2020) |
SMPLA nonwoven fabric | n-hexane, toluene, carbon tetrachloride, cyclohexane, ethanol, and diethyl ether | DPA PVDF-HFP | up to 99.5% | / | 6.78–9.91% | WCA 151.7° | Zeng et al. (2020) |
PLA foam | different oils and organic solvents | dioxane | 98% | / | >90% | WCA 151° | Wang et al. (2019) |
PLA filtration films | petroleum ether, gasoline, diesel oil, and vegetable oil | NaCl | more than 97% | 500 nm–10 μm | WCA 153.5 ± 1.7° | Xue et al. (2013) | |
PLA@TiO2@MTS nanofibrous membrane | soybean oil, toluene, carbon tetrachloride, petroleum ether and n-hexane | TiO2 MTS | more than 95% | / | / | WCA 157.4 ± 0.9° | Zhou et al. (2019a) |
Nano-PLA nonwoven fabric | castor oil, petroleum ether, n-hexane, silicone oil, lubricating oil | ER KH-560 | 96% | 100 μm | / | WCA 152.1° | Lu et al. (2022) |
ZIF-8@PLA composite aerogel | cyclohexane, petroleum ether, vegetable oils, n-heptane, CCl4 | ZIF-8 | close to 100% | 10–30 nm | / | WCA 145° | Li et al. (2021a) |
PLA/WO3/N-CQDs fiber | hexadecane n-hexane, and n-heptane | WO3/N-CQDs | 91.80% | 1.848 ± 0.328 μm | / | WCA 132.37° | Nugraha et al. (2021) |
PLA/PPC PLA/PHB PLA/PBS PLA/TEC | oil and grease | PBS, PPC, PHB, SNPs | more than 98% | 18.3–28.55 nm | good | / | Ghorbani et al. (2021) |
PLLA films | petroleum ether | chloroform | 99.1% | / | 69.5–87.5% | WCA 152.1° | Sun et al. (2021) |
PLA/PBE micro-nanofiber fabrics | soybean oil | PBE | excellent | / | / | WCA 134° | Li et al. (2022) |
PLLA/SiO2 nanocomposite membrane | oil (red) | SiO2 | effective | / | / | WCA 167.1° | Zhong et al. (2021b) |
Modified PLLA nonwoven fabric | hexane, toluene, and tetrachloromethane | PDLA | more than 97% | / | / | WCA 130.8 ± 1.5° | Zhu et al. (2020) |
PLA fiber membrane | n-hexane, olive oil, and lubricant oil | chloroform N, N dimethylformamide | more than 99.98% | 500 nm–1 μm | 92 ± 4.1% | WCA 150.3° | Liu et al. (2019a) |
Janus PLA fibrous membrane | carbon tetrachloride, n-hexane, and petroleum ether | SiO2 CNTs | more than 99% | / | / | WCA is more than 142° | Qin et al. (2020) |
PLA/γ-Fe2O3 composite membranes | motor oil, silicone oil, castor oil, corn oil, lubricating oil, sunflower oil, n-hexane, olives oil, cedar oil | γ-Fe2O3 | high separation | / | >90% | WCA 148° | Zhang et al. (2019) |
PLA packing | n-hexane | PS | 95% | 4–200 μm | / | WCA 150° | Xing et al. (2019) |
PLA porous membrane | n-hexane | PS | 99.4% | ∼25 μm | / | WCA 151.7° | Xing et al. (2018) |
Advanced PLA non-woven fabric | n-hexane and tetrachloromethane | TiO2 | 86.9% | / | / | WCA 150° | Shi et al. (2018) |
Nanofibrous PLA membrane | toluene | PDA | 98.4 ± 1.0% | / | high | WCA 158.6° ± 1.2° | Liu & Yuan (2018) |
SiO2/PS/PLA non-woven fabric | hexane, soybean oil, toluene, pump oil, tetrachloromethane, and vegetable oil | SiO2 PS | efficient | / | / | WCA 152.0 ± 2.1° | Gu et al. (2017) |
Chitosan (CS)
As the second most prevalent biopolymer in nature, chitosan (CS) can be observed in shells of crustaceans and insect pests, molluscan organs, and fungal structures. In most cases, it's produced by chitin deacetylation (CT) (Anitha et al. 2014; Antony et al. 2019; Liu et al. 2019b). Chitosan is a biopolymer with strong hydrophilicity and antibacterial characteristics that is affordable and harmless. (Abu-Saied et al. 2017). Co-polymerization of β (1, 4)-linked 2-amino-deoxy-D-glucopyranose and N acetylglucosamine results in its chemical structure. The hydroxyl and amino groups (which provide electrons) are both present. Despite this, it is soluble in dilute organic acids such as formic, acetic, and lactic acids and insoluble in a variety of organic solvents, water, and alkalis. With only a modest amount of acid, chitosan can achieve high levels of water solubility because of the presence of the acid-soluble polar ether (COC), hydroxyl (OH), and amino (NH2) groups (Ma & Sahai 2013; Cao et al. 2018). Because of the availability of amino groups and hydroxyl groups, CS-based materials have been extensively explored for decontamination of minerals from effluents, and they are widely employed in the pharmaceutical, chemical, and paper industries, and protection of the environment sectors. Many chemical alterations have been made to chitosan in order to increase its adsorption capacity (Losev et al. 2017; Jiang et al. 2018; Behr & Ganesan 2022).
Below we will highlight the different types of chitosan membrane fabrication methods used. Some typical examples of chitosan membranes for water–oil separation applications are summarized in Table 3. With a detailed illustration of the prepared membrane characteristics and the membrane performance.
Membrane . | Oils . | Additives/ component used . | Performance/efficiency . | Pore size . | Porosity . | Contact angle . | Ref. . |
---|---|---|---|---|---|---|---|
MCS-MCA-TiO2 membrane | cyclohexane | TiO2 | 99.4% | / | / | WCA 13.7° OCA 157.24° | Yu et al. (2019) |
CS@PCL membranes | hexane and heptane | PCL | more than 99.9% | 42 nm | / | WCA, OCA in the air at 0° | Doan et al. (2021) |
CS/ALG Nanofiber-coated Meshes | toluene, n-hexane, chloroform, kerosene and crude oil | ALG | 99% | 268 nm | / | OCA over 160° | Zhou et al. (2019b) |
UiO-66-NH2/CS/mixed cellulose | dichloromethane, petroleum ether, dodecane and gasoline | UiO-66-NH2 | more than 95%. | 220 nm | high | OCA 150° | Zhu et al. (2021) |
Catechol/Chitosan co-deposited membranes | n-hexadecane, peanut oil, and crude oil | catechol | higher removal efficiencies | / | / | WCA 138° | Zhao et al. (2021) |
Modified Chitosan–Gelatin membrane | cooking oil, light crude oil, and used engine oil | gelatin | more than 98% | 100–200 μm | high | WCA 0° | Zakuwan et al. (2021) |
CTS-PPS microfiber membranes | n-hexane, petroleum ether, and toluene | GA | more than 99% | 1.38–3.52 μm | 50.3–82.4% | OCA 151.89° | Huang et al. (2019) |
SiO2/CT-PVDF Membrane | gasoline | SiO2 | 99% | / | 41–53% | WCA 68.62° | Ardeshiri et al. (2019) |
CST and CS modified membranes | hexadecane, octane, petroleum ether, toluene | TiO2 | more than 97%, | 220 nm | / | OCA 165.7 ± 5.0° | Du et al. (2017) |
GO/CS Membrane | soybean, silicone, and octane | GO | more than 95% | / | / | WCA and OCA 0° | Ponnanikajamideen et al. (2021) |
CS/TiO2 modified nitrocellulose membrane | sixteen alkanes, petroleum ether, and diesel | TiO2 | 98.5% | / | / | OCA 156.2 ± 3.3° | Li et al. (2021b) |
r-PET@ Chitosan. membranes | kerosene, hexane, CTC, and TCE | r-PET | more than 95% | / | / | OCA 168.0 ± 1.9° WCA 168.1 ± 2.5° | Baggio et al. (2021) |
PEG-Chi Hybrid-Coated | vegetable oil | PEG | 98% | / | increased | / | McCloskey et al. (2010) |
Membrane . | Oils . | Additives/ component used . | Performance/efficiency . | Pore size . | Porosity . | Contact angle . | Ref. . |
---|---|---|---|---|---|---|---|
MCS-MCA-TiO2 membrane | cyclohexane | TiO2 | 99.4% | / | / | WCA 13.7° OCA 157.24° | Yu et al. (2019) |
CS@PCL membranes | hexane and heptane | PCL | more than 99.9% | 42 nm | / | WCA, OCA in the air at 0° | Doan et al. (2021) |
CS/ALG Nanofiber-coated Meshes | toluene, n-hexane, chloroform, kerosene and crude oil | ALG | 99% | 268 nm | / | OCA over 160° | Zhou et al. (2019b) |
UiO-66-NH2/CS/mixed cellulose | dichloromethane, petroleum ether, dodecane and gasoline | UiO-66-NH2 | more than 95%. | 220 nm | high | OCA 150° | Zhu et al. (2021) |
Catechol/Chitosan co-deposited membranes | n-hexadecane, peanut oil, and crude oil | catechol | higher removal efficiencies | / | / | WCA 138° | Zhao et al. (2021) |
Modified Chitosan–Gelatin membrane | cooking oil, light crude oil, and used engine oil | gelatin | more than 98% | 100–200 μm | high | WCA 0° | Zakuwan et al. (2021) |
CTS-PPS microfiber membranes | n-hexane, petroleum ether, and toluene | GA | more than 99% | 1.38–3.52 μm | 50.3–82.4% | OCA 151.89° | Huang et al. (2019) |
SiO2/CT-PVDF Membrane | gasoline | SiO2 | 99% | / | 41–53% | WCA 68.62° | Ardeshiri et al. (2019) |
CST and CS modified membranes | hexadecane, octane, petroleum ether, toluene | TiO2 | more than 97%, | 220 nm | / | OCA 165.7 ± 5.0° | Du et al. (2017) |
GO/CS Membrane | soybean, silicone, and octane | GO | more than 95% | / | / | WCA and OCA 0° | Ponnanikajamideen et al. (2021) |
CS/TiO2 modified nitrocellulose membrane | sixteen alkanes, petroleum ether, and diesel | TiO2 | 98.5% | / | / | OCA 156.2 ± 3.3° | Li et al. (2021b) |
r-PET@ Chitosan. membranes | kerosene, hexane, CTC, and TCE | r-PET | more than 95% | / | / | OCA 168.0 ± 1.9° WCA 168.1 ± 2.5° | Baggio et al. (2021) |
PEG-Chi Hybrid-Coated | vegetable oil | PEG | 98% | / | increased | / | McCloskey et al. (2010) |
Cellulose acetate (CA)
CA is a polymer that is often used in membrane production and has been the subject of much research. CA can be used to create membranes for microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO), and it is typically employed in dialysis applications (Sivakumar et al. 2006; Iwata 2015; Kargarzadeh et al. 2018). CA is biodegradable and sustainable because it is made from cellulose, a naturally occurring substance. Because of its insolubility, cellulose must be treated with acetic anhydride and acetic acid to produce CA (Gopinath et al. 2018). However, it has many disadvantages, including low mechanical strength, thermal resistance, and chemical resistance. As a result, the addition of additives or surface modifications is frequently required to enhance the properties of CA membranes (Alcheikhhamdon & Hoorfar 2017; Mohamed et al. 2017).
What's more, for different purposes, cellulose-based materials (such as filter paper and membranes) can also be chemically changed. Hydrophobic nanoparticles can be applied to filter paper by spin-coating, dipping, or spraying the paper with a solution, emulsion, or suspension (Li et al. 2008; Wang et al. 2008; Huang et al. 2012; Yetisen et al. 2013).
Table 4 summarizes information on the cellulose acetate membrane preparation. It is illustrating the recent development of the performance of the cellulose acetate membranes for water/oil emulsion separation via improving the performance of synthesized membranes, which can be achieved by improving the characteristics of the prepared membranes by using some modern techniques to improve the polymer casting solution.
Membrane . | Oils . | Additives/ component used . | Performance/efficiency . | Pore size . | Porosity . | Contact angle . | Ref. . |
---|---|---|---|---|---|---|---|
Cellulose-TA-PVA-PVDF membrane | diesel oil, lubricant oil, pump oil sunflower oil | TA-PVA TA-PVA-PVDF | 99.99% | / | / | UOCA is more than 150° | Gao et al. (2021) |
Modified cellulose acetate membranes | decane and marcol 52 white oil | GO, LDH and SeP | more than 98% | 0.45 μm | UOCA 151.1 ± 2.1° | Li et al. (2017) | |
Flat-sheet and hollow fiber cellulose membranes | crude oil | ionic liquid | more than 95% | 0.01 and 10 μm | / | / | Kim et al. (2019) |
Bacterial cellulose filter | motor oil | corn steep liquor | 100% | / | 76.12% | WCA 90° | Galdino et al. (2020) |
CNF-PDA-coated cellulose acetate membrane | diesel, cydohexane, toluene, low viscidity crude oil | PDA | more than 99% | 167.7 nm | / | UOCA 157.3° | Yin et al. (2020) |
PPy@FP and PPy@CA-50 membrane | hexadecane, cyclohexane and dimethylbenzene | pyrrole | around 99% | 0.3608 μm | / | WCA 150° | Li et al. (2020) |
Cellulose hollow fiber membranes | machine oil | PEG | more than 99% | / | / | / | Li et al. (2006) |
Cellulose membrane (SOCM) | diesel oil, petroleum ether, toluene, hexane, dichloroethane | TEOS HDTMS | more than 98% | 15–20 μm | / | WCA 164.4° | Xie et al. (2019) |
Cellulose filter membrane | vegetable oil, hexane, crude oil, silicone oil, and PET ether | silane and myrcene | high levels of extractive activity | / | / | WCA 160 ± 4° | Kollarigowda et al. (2017) |
Nanofibrous cellulosic membrane | mineral oil, kerosene, n-hexane, and petroleum ether | DMAc | more than 99% | 1–4 μm | / | OCA more than 150° | Hong et al. (2018) |
Cellulose membrane | n-hexane, trichloromethane, soybean oil, gasoline | NaOH NaClO2 | 98% | / | / | OCA 151.3◦ | Li et al. (2021c) |
Composite cellulose membrane | dichloromethane, kerosene | NBKP | more than 95% | / | 53.99% | WCA 162.3° | Wang et al. (2021) |
Cellulose/LDH membrane | chloroform, toluene, diesel oil, petroleum ether, and heptane | LDH | more than 93% | 15 ∼ 20 μm | / | WCA 154 ± 1.8° | Yue et al. (2017) |
Cellulose membrane (FP@SA/CaCO3) | petroleum ether, soybean oil, hexane, toluene dichloroethane | CaCO3 | more than 99.2% | / | / | OCA 151.1° | Yang et al. (2021) |
Bacterial cellulose membranes (BCMs) | hexane | / | more than 99.7% | / | / | OCA more than 150° | Sai et al. (2020) |
CA-g-PAN membranes | pump oil | PAN | FRR more than 90%, | / | / | WCA 56.9 ± 0.9° | Chen et al. (2009) |
Membrane . | Oils . | Additives/ component used . | Performance/efficiency . | Pore size . | Porosity . | Contact angle . | Ref. . |
---|---|---|---|---|---|---|---|
Cellulose-TA-PVA-PVDF membrane | diesel oil, lubricant oil, pump oil sunflower oil | TA-PVA TA-PVA-PVDF | 99.99% | / | / | UOCA is more than 150° | Gao et al. (2021) |
Modified cellulose acetate membranes | decane and marcol 52 white oil | GO, LDH and SeP | more than 98% | 0.45 μm | UOCA 151.1 ± 2.1° | Li et al. (2017) | |
Flat-sheet and hollow fiber cellulose membranes | crude oil | ionic liquid | more than 95% | 0.01 and 10 μm | / | / | Kim et al. (2019) |
Bacterial cellulose filter | motor oil | corn steep liquor | 100% | / | 76.12% | WCA 90° | Galdino et al. (2020) |
CNF-PDA-coated cellulose acetate membrane | diesel, cydohexane, toluene, low viscidity crude oil | PDA | more than 99% | 167.7 nm | / | UOCA 157.3° | Yin et al. (2020) |
PPy@FP and PPy@CA-50 membrane | hexadecane, cyclohexane and dimethylbenzene | pyrrole | around 99% | 0.3608 μm | / | WCA 150° | Li et al. (2020) |
Cellulose hollow fiber membranes | machine oil | PEG | more than 99% | / | / | / | Li et al. (2006) |
Cellulose membrane (SOCM) | diesel oil, petroleum ether, toluene, hexane, dichloroethane | TEOS HDTMS | more than 98% | 15–20 μm | / | WCA 164.4° | Xie et al. (2019) |
Cellulose filter membrane | vegetable oil, hexane, crude oil, silicone oil, and PET ether | silane and myrcene | high levels of extractive activity | / | / | WCA 160 ± 4° | Kollarigowda et al. (2017) |
Nanofibrous cellulosic membrane | mineral oil, kerosene, n-hexane, and petroleum ether | DMAc | more than 99% | 1–4 μm | / | OCA more than 150° | Hong et al. (2018) |
Cellulose membrane | n-hexane, trichloromethane, soybean oil, gasoline | NaOH NaClO2 | 98% | / | / | OCA 151.3◦ | Li et al. (2021c) |
Composite cellulose membrane | dichloromethane, kerosene | NBKP | more than 95% | / | 53.99% | WCA 162.3° | Wang et al. (2021) |
Cellulose/LDH membrane | chloroform, toluene, diesel oil, petroleum ether, and heptane | LDH | more than 93% | 15 ∼ 20 μm | / | WCA 154 ± 1.8° | Yue et al. (2017) |
Cellulose membrane (FP@SA/CaCO3) | petroleum ether, soybean oil, hexane, toluene dichloroethane | CaCO3 | more than 99.2% | / | / | OCA 151.1° | Yang et al. (2021) |
Bacterial cellulose membranes (BCMs) | hexane | / | more than 99.7% | / | / | OCA more than 150° | Sai et al. (2020) |
CA-g-PAN membranes | pump oil | PAN | FRR more than 90%, | / | / | WCA 56.9 ± 0.9° | Chen et al. (2009) |
CONCLUSION
Green membranes were harnessed to separate oil–water emulsion mixtures, selectively and efficiently, based on their unique structural properties, distinct production methods, and the materials used to enhance their defining characteristics are reviewed in this article. Because membrane oil–water separation/rejection performance is strongly influenced by membrane morphology, several eco-friendly preparations and design options were explored in depth. According to a comprehensive evaluation of membrane preparation processes, several synthesizing active membrane capabilities can be identified. The ecological environment faces a serious threat from oil spills and industrial contamination. Filtration improvements for oily wastewater have been given more attention due to safety concerns. Membrane separation technology, with its low energy consumption, provides a promising and effective choice for treating wastewater. However, finding low-cost, strong, and environmentally friendly composite membranes capable of providing a high level of separation remains a challenge. Most authors agree that there is an urgent, ongoing need to prioritize the use of green composite membrane for oil–water emulsion separation for the reasons stated above. Oily wastewater is a byproduct of several industrial processes and is becoming a growing environmental issue. As a result, researchers are looking for easy, cheap, environmentally friendly, and easily scalable methods of manufacturing novel materials that can efficiently separate oil–water at low cost.
ACKNOWLEDGEMENTS
The support of Department of Chemical Engineering, University of Technology Technology Baghdad, Iraq is gratefully acknowledged.
DATA AVAILABILITY STATEMENT
All relevant data are included in the paper or its Supplementary Information.
CONFLICT OF INTEREST
The authors declare there is no conflict.