Oil/Water Separation Using Waste-Derived Functional Materials with Special Wetting Behavior
Abstract
:1. Introduction
2. Waste Materials with Special Wettability for Oil/Water Separation
2.1. Underwater Superoleophobic-Superhydrophilic Surfaces
2.2. Underoil Superhydrophobic-Superoleophilic Surfaces
3. Summary and Future Work
- (1)
- Most of the studies are still limited to the lab scale only, and are very difficult to apply at the industrial scale. Therefore, it is highly essential to examine their applicability in real case problems with the oil of different viscosities under natural environmental conditions.
- (2)
- The matrix of oily contaminated wastewater is more complex. Therefore, design and development of multi-functional materials should be focused on performing real field applications.
- (3)
- Generally, special wettability waste materials have weak mechanical properties and a very small service life. However, longevity is one of the essential factors during its practical application to treat real field contaminated water at a large scale. Therefore, further research must be focused on the combination of theoretical and experimental investigations to achieve industrialization and large-scale oil/water separation in the real field practical application of special wettability waste materials with a continuous mode of operation.
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Mechanism | Separation Process | Waste Material | Sources of Waste Materials | Other Material for Surface Modification | Coating Method | Contact Angle | Separation Efficacy | Flux/Sorption Capacity | Separated Oils | Comments | Ref. |
---|---|---|---|---|---|---|---|---|---|---|---|
Hydrophobic /oleophilic | Sorption | Waste tissue paper | Cellulose waste | Polyvinyl alcohol, sodium chlorite, sodium hydroxide, tetraethyl orthosilicate | Freeze-drying | WCA 154.93° ± 4.14 | - | 69−168 g g−1 Sorption capacity | Chloroform, motor oil, acetone, DMF, olive oil and toluene | The modified aerogel exhibits sorption efficay greater than 92% even after repeating 20 cycles and 89% up 50 cycles of repeation process. | [72] |
Egg carton material | Cellulose waste | Acetone, candle soot | Dip-coating | WCA = 142.2°, OCA = 43.1° | - | Absorption: 3 g g−1 | Petrol, diesel, refined oil, coconut, engine and mustard oil | The maximum and minium sorption capacity of the modified surfaces were 3.1 and 1.6 g g−1 for mustard oil and petrol, respectively. | [73] | ||
Waste bamboo | Agricultural waste | Methyl trimethoxy silane, Anhydrous Alcohol | Chemical vapor deposition and delignification | WCA = 153°, OCA = 0° | - | Absorption: 18.8 g g−1 | Silicone oil, diesel oil, chloroform, paraffin oil and toluene | The highest oil absorption capacities of the developed surfaces was >40–55%. | [74] | ||
Epoxy resins | Industrial waste | Epoxy oligomer, 4, 4-diaminodiphenyl methane, N-methyl kelopyrrolidide | Dip-coating | WCA = 146.5° | - | Absorption: 116 g g−1. | Soybean oil, colza oil, pump oil, n-hexane, chloroform and silicone oil | The selective oil absorption ability of developed surface stabilized was approximately 53 g g−1 with respect to gasoline even after the 10 successive repetition of separation cycles. | [75] | ||
Skin collagen fiber waste | Industrial waste | Methacrylic acid, glycidyl Methacrylate, sodium dodecyl sulphate, dodecyl Mercaptan | In situ free radical polymerization | WCA 145° | 99.93 ± 0.03% | -- | Soybean oil and motor oil | The developed modified surfcace exhbited high separation efficiency (>99.93%) even after 10 cycles and 3 cycles for surfactant free oil in water emulsion and surfactant-stabilized oil-in-water emulsion respectively. | [76] | ||
Polystyrene foam | Plastic waste | Styrene, Tetraethyl orthosilicate, Ammonia solution and hexadecyltrimethoxysilane | Pickering emulsion (HIPPE) technique | - | - | 20.4–58.1 g g−1 Absorption capacity | Dichloromethane, chloroform, acetone, hexane, dichloromethane, acetic ether, methanol, ethanol, toluene, peanut oil, diesel, pump oil and crude oil | The fabricated foam adsorb oil and revealed the adsorption capacity above 90% even after the 10 consecutive cycles. | [77] | ||
Filtration | Waste polystyrene | Plastic waste | Ethyl acetate, craft polystyrene | Blow spinning | WCA 138° OCA 0° | 97% | - | Diesel oil | After repeating consecutive two cycles the separation efficacy of the modified material was >90%. | [78] | |
Thermosetting resins | Plastic waste | - | Simple Mechanical crushing | WCA 117° | 97% | 15 987 L m−2 h−1 s Separation flux | Toluene, chloroform, n-hexane and gasoline | The prepared surface can easily separate the oil/water mixtures as well as emulsion with the droplet size more than 50 nm. | [79] | ||
Sugarcane bagasse ash | Agricultural waste | Methyl triethoxysilane, tetraethoxysilane | Sol–gel process | WCA 163.9° | 99.9% | Oil flux: 137.2 L m−2 h−1 s | Crude oil | The separation efficacy of the modified surfaces was examined in consideration of process variables such as grafting time (30 to 60 min), grafting cycle (1–4 cycles), and calcination temperature (400–600 °C) to separation effieciency. | [80] | ||
Underwater super-oleophobic/ hydrophilic | Filtration | Polyurethane foams | Plastic waste | Ferric chloride, dopamine, ammonium hydroxide, polydopamine | Polymerization | Underwater OCA 145.7 ± 2.8 | 98.7% | Water flux higher than 57,796 L h−1 m−2 | Hexane, cyclohexane, liquid paraffin, pump oil and petroleum ether | The oil/water separation effucacy of the developed surface of modfied foam was >97% even after the 100 cycles of the recycling test. | [81] |
Carbon fibers | Industrial waste | Cellulose filter papers, tannic acid, tris(hydroxymethyl)- Aminomethane (Tris), (3-Aminopropyl) triethoxysilane, sodium Dodecyl sulphate, sodium hydroxide, hydrochloric Acid, dichloromethane (DCM) | Pyrolysis method | Underwater OCA 157.2° | 99.8% | - | Dichloromethane (DCM), canola oil, n-hexane, kerosene and silicone oils | The developed surface has high roughness 2.1 times higher than the raw material as well as effective surface area was 1.6 times higher than the control due to development of micro–nanostructured sructured on the surface. | [49] | ||
Coal fly ash | Industrial waste | Coal fly ash, distilled water | - | Underwater OCA 155 ± 2° | 99.9% | - | Kerosene, diesel and hexane | Oil/water separation efficacy was directly proportional to the thickness of the separating membrane. However separating flux was decreases from 1050 L m−2 h−1 to 513 L m−2 h−1 with the increase of thickness. | [82] | ||
Natural shell | Raw materials discarded on the beach | Perfluorooctanoic acid, (3-aminopropyl) triethoxysilane and bis (3-(trimethoxy silyl) propyl) amine, Spray-Mount™ Super 75 | Dip-coating method | Underwater OCA 154° | 99.3% | - | Chloroform, olive oil, decane and hexadecane | The developed surface was capable to separate both oil/water and oil/oil mixtures of different polarity. | [83] | ||
Pomelo Peel fibers | Fruit waste | Anhydrous ethanol, waterborne polyurethane | Spraying method | Underwater OCA | 97.0% | - | Kerosene, motor oil and soybean oil, hexane, liquid paraffin and chloroform | The modified mesh exhbited high separation efficiency (>97.0%) in oil/water mixtures of different pHs. | [84] | ||
Coconut shell waste | Fruit waste | Quartz sand, waterborne polyurethane | Dip-coating method | Underwater OCA 151.2° | 99.92% | - | Hexane, dichloromethane, trichloromethane, anhydrous ethanol and petroleum ether | The developed material exhibits the permeability coefficient of organic solvents such as cyclohexane, petroleum ether, dichloromethane, and trichloromethane were higher than 10 m/h than water 9.37 m/h. | [85] | ||
Waste cigarette filter | Cellulose waste | Trichloromethane, acetone and N, N-dimethylformamide | Electrospinning approach | Underwater OCA | 99.9% | Water flux was about 1000 L m−2 h−1 | Kerosene, diesel, petroleum ether, hexane and trichloromethane | The prepared surface exhibits underwater superoleophobicity and underoil super hydrophobicity. In addition, separation efficiency was >99% even after the 10 repeating cycles of sepration process. | [62] | ||
Waste Paper | Cellulose waste | - | - | Underwater OCA 151 ± 2.5° | 99% | - | Soyabean oil, cyclohexane and hexane | The modified waste papers exhbited very flux of oil/water mixture sepration revealed water flux, i.e., 1126, 1837, 3246, 1273, and 1145 L·m−2·h−1 for stickers, notebook, lens paper, envelopes, and receipts, respectively. | [86] | ||
Bricks Powder | Waste bricks | Distilled water and ethanol | Physical refining process | Underwater OCA 150° | 98.4% | Flux 4384 L m−2 h−1 | Hexane, methylbenzene, trichloromethane and absolute ethyl alcohol and soyabean oil | The fabricated waste bricks granules (100–400 µm) have superhydrophilicity and superoleophilicity in air and under-liquid amphiphobic properties. | [87] |
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Singh, A.K. Oil/Water Separation Using Waste-Derived Functional Materials with Special Wetting Behavior. Resources 2022, 11, 83. https://doi.org/10.3390/resources11100083
Singh AK. Oil/Water Separation Using Waste-Derived Functional Materials with Special Wetting Behavior. Resources. 2022; 11(10):83. https://doi.org/10.3390/resources11100083
Chicago/Turabian StyleSingh, Arun K. 2022. "Oil/Water Separation Using Waste-Derived Functional Materials with Special Wetting Behavior" Resources 11, no. 10: 83. https://doi.org/10.3390/resources11100083
APA StyleSingh, A. K. (2022). Oil/Water Separation Using Waste-Derived Functional Materials with Special Wetting Behavior. Resources, 11(10), 83. https://doi.org/10.3390/resources11100083