Submitted:
18 February 2024
Posted:
19 February 2024
You are already at the latest version
Abstract
Keywords:
1. Introduction
2. Generation Process and Characteristics of MNBs in Water
2.1. The Generation Process of MNBs in Water
2.2. Characteristics of MNBs in Water
3. Characteristics of MNBs Collapse and Influencing Factors of Hydroxyl Radical Generation in MNBW
3.1. Characteristics of MNBs Collapse
3.2. Influencing Factors of ·OH Generation in MNBW
4. Effect Mechanism of MNBs on Pollutants and Biofilms in Water
4.1. MNBs Remove Pollutants from Water
4.2. Control Mechanism of MNBs on Pipe Biofilm Growth
5. Application Prospect of MNBs in Drinking Water
6. Limitations and Prospects of MNBs
- The long-term stable existence of MNBs in water and the ·OH generation mechanism are highly controversial. Existing studies on the above two aspects remain at the surface and speculation level; hence, further discussion is needed.
- The relationship between synergistic and antagonistic effects of MNBs on microorganisms remains unclear. Because the MNBs can generate substantial oxidizing ·OH to destroy microorganisms and provide great potential for water disinfection. Moreover, due to high mass transfer efficiency, MNBs have good biological activity and can promote the biological purification function of water. These two statements are contradictory. Therefore, to better apply MNBs technology, it is required to explore under what circumstances, which side of the synergistic and antagonistic effects of MNBs on microorganisms is more dominant.
- It is difficult to quantitatively determine ·OH generated by MNBs. Recently, the detection methods of ·OH are all indirect methods, which are complicated in operation, and are inevitably interfered by many factors in the detection process, resulting in considerable errors. Future research should focus on direct detection of ·OH to reduce unnecessary interference items.
- MNBs generates a limited amount of ·OH. The ability of MNBs to generate free radicals is only one of its many outstanding properties, and the ·OH generated is only one of the many free radical products. At present, studies on the influence of various factors on the generation of ·OH by MNBs are relatively simple. It should continue to explore how to promote the generation of ·OH by MNBs, and simultaneously control the factors that affect ·OH generation under optimal conditions.
- NBs generation devices are expensive. NBs are superior to MBs in all aspects, but due to the high energy consumption and high price of NB generation devices, the application of NBs in various fields is limited to a certain extent. Hence, developing practical NB generation devices with low energy consumption, low cost, excellent performance and easy promotion is also a new direction of current research.
- The study of MNBs characteristics is not comprehensive enough. At present, the research on the characteristics of MNBs mainly focuses on the well-known aspects of free radical generation and high mass transfer efficiency. Other characteristics of MNBs, such as heat transfer and viscosity, are unknown and require more analysis.
7. Conclusions
Acknowledgments
References
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| Treatment Methods | Pollutants Removed from Drinking Water | Advantages | Disadvantages | References | |
|---|---|---|---|---|---|
| Physico- chemical methods |
Adsorption | Organic pollutants (Bisphenol A) |
Simple and effective. | Adsorbent regeneration, high cost; The adsorption capacity of regenerated adsorbent decreases and the service life is short. | Kim et al., 2015 |
| Membrane separation technology | Particles, Sediments, Algae, Bacteria, Protozoa, Small colloid, Virus, Dissolved organics, Divalent ions Monovalent ions, COD |
No secondary pollution. | High energy consumption, complex equipment, high intake water quality requirements; Membrane fouling. | Yüksel et al., 2013 | |
| Coagulation/flocculation | Refractory organics | Economical and practical. | Produce secondary pollution. | Zhang et al., 2021 | |
| Ultrasonic decomposition | Particles, Organic pollutants | Short reaction time, simple process facilities. | Relatively low efficiency. | Zhang,2013 | |
| Photocatalytic technology | Dissolved organic carbon (DOC), Bacteria | Semiconductors are cheap, can mineralize refractory compounds, clean and safe. | Still in the development stage and immature. | Pera-Titus et al., 2004 | |
| Chemical methods | Electrochemical advanced oxidation processes (EAOPs) |
Organic micro-pollutants | Has the environmental compatibility, versatility, high efficiency, safety. | Relatively low efficiency. Formation of stable by-products. |
Brillas et al., 2009; Moreira et al., 2013 |
| O3 based oxidation process | Organic pollutants (chlorophenols), Bacteria | Economical and efficient, harmless to most organisms, no harmful by-products generation. | Harmful to human health; High energy demand. | Pera-Titus et al., 2004; Baig et al., 2001 | |
| H2O2 based oxidation process | Organic pollutants (chlorophenols), Bacteria | Safe, efficient and easy to use; Widely used to prevent pollution and improve biodegradability. | The reaction process is affected by many factors, and the reaction time is long. | Pera-Titus et al., 2004 | |
| Chlorine based oxidation process | Organic matter, Bacteria Micropollutants, Viruses |
Chlorine remains in the water as residual chlorine, and the activity is persistent. High yield of active species, broad-spectrum, safe and effective. |
Taste and smell are not ideal, forming more than 40 DBPs. Disinfection effect is not ideal, used for secondary disinfection. |
Zhai et al., 2017; Li et al., 2022; Xu et al., 2022; Subramanian et al., 2021 |
|
| Biological methods | Biological sand filtration (BSF) |
Viruses, Bacteria, Heavy metals, Nitrogenous compounds, Pesticides, Organic chemicals, Dissolved organic carbon (DOC), NOM, etc. | Easy operation, efficient and reliable operation, low cost. | (ⅰ) Microorganisms have high selectivity to pollutants, and the biodegradation time is long and the equipment is complex. (ⅱ) The uncontrolled growth of microorganisms may lead to health problems. (ⅲ) The application of biological sand filtration has high requirements on terrain and limited application scenarios. |
Pokhrel et al., 2009; Schijven et al., 2013; Hedegaard et al., 2014; Cai et al., 2014; Pramanik et al., 2015 |
| Biological activated carbon (BAC) | Nitrogenous compounds, Organic carbon, Micropollutants. |
The dual functions of adsorption and biodegradation improve the effectiveness of drinking water. | Li et al., 2012; Yapsakli et al., 2010; Zhang et al., 2010; McKie et al., 2016; Akcay et al., 2016 | ||
| Trickling filter (TF) | NH3-N, Fe, Mn. | No external air supply required. | Tekerlekopoulou et al.,2007 | ||
| Biological aerated filter (BAF) | COD, NH4+-N, Fe, Mn, Diclofenac. | Economical and effective. | Hasan et al., 2011; Han et al., 2013, 2016; He et al., 2014; Marsidi et al., 2018 | ||
| Membrane bioreactor (MBR) |
Nitrate, Total organic carbon (TOC), Deamination, Macro pollutants, Anionic micropollutants (perchlorate, bromate, nitrate) | Overcomes the problem of microbial contamination and supports the growth of selected microorganisms. | Buttiglieri et al., 2005; Li et al., 2003; Ricardo et al., 2012; Matos et al., 2008 |
||
| Fluidized bed biofilm reactor (FBBR) | TOC, THM, Ammonia. | No backwash required, easy to manage. | Xie et al., 2006 | ||
| Integrated/ combining technologies |
Microorganism, Particle, Nitrate, Phosphate, Organic matter, Ammonium | Higher treatment efficiency. Improve the quality of treated water and reduce membrane pollution. |
Tian et al., 2008; Tian et al., 2009 |
||
| Application fields | Main function | Gas type | Bubble size(nm) | Bubble concentration(one/mL) | Characteristics of applied MNBs | References |
|---|---|---|---|---|---|---|
| Biochemical process | Promote the growth of microalgae and increase the output of many high-value products. | air | <200 | / | ④ | Zhu and Wakisaka, 2019; Choi et al., 2014 |
| Improve biofilm structure and promote aerobic metabolism; Improve COD and ammonia removal rate and reduce aeration. | air | <225 | / | ④ | Xiao et al., 2021; Xiao and Xu, 2020 |
|
| Improve the production efficiency of probiotics through fermentation, mainly in the lag stage and logarithmic stage of strain growth. | air | 180~220 | (3.59±1.14)×107 | ⑥ | Guo et al.,2019 | |
| Improve the production efficiency and recovery rate of yeast. | air | ≈3×105 | / | ④ | Hanotu et al., 2016 | |
| Groundwater remediation | Improve the mass transfer efficiency of O3 and the in-situ remediation efficiency of organically contaminated groundwater. | O3 | 10~1000 | (1~1000)×106 | ③,④ | Hu and Xia., 2018 |
| Surface cleaning | Prevent and remove protein adsorbed on solid surface. | air | 25~35 | / | ⑦ | Wu et al., 2006; Wu et al., 2007 |
| Remove oil stain on metal surface. | air | (2~6)×104 | / | ①,② | Tan et al., 2020 | |
| Agronomy | Improve irrigation water use efficiency, crop yield and quality. | air | 124~148 | (6~7)×108 | ④ | Liu et al., 2019 |
| Improve plant growth; Purifying blue-green algae pollution. | air | 200~2200 | / | ④ | Nakashima et al., 2010 | |
| Soil environment | Change the redox conditions of submerged paddy soil to reduce methane emission. | O2 | 128~242 | (6~8)×107 | ④ | Minamikawa et al., 2020 |
| Remove metal pollutants from soil. | O2 | <103 | / | ④ | Minamikawa et al., 2015 | |
| Improve the availability of oxygen in clay or sandy soil and improve the soil anoxic environment. | O2 | 190~210 | (0.5~1.5)×109 | ④ | Baram et al., 2022 | |
| Marine animals and food | Significantly promote the growth of plants, fish and mice. | O2 | <200 | / | ④ | Ebina et al., 2013 |
| air | / | |||||
| Water pollution treatment | Aeration to improve oxygen mass transfer efficiency. | air | 102~105 | / | ④ | Li et al., 2014 |
| Disinfect and can effectively remove bacteria and viruses. | O3 | (3~6)×104 | / | ⑤ | Sumikura et al., 2007 | |
| Flotation to improve the treatment effect of printing and dyeing wastewater. | air | <6×104 | / | ②,③,④,⑤ | Liu et al., 2010 | |
| Degradation of organic pollutants (see Table 4) | ||||||
| Generation methods | Generation process | Influence factor | Advantages | Disadvantages | References |
|---|---|---|---|---|---|
| Hydrodynamic cavitation | When a large pressure difference is generated in the moving fluid, hydrodynamic cavitation will be observed, resulting in MNBs. | Pressure difference. | High efficiency and low energy consumption. | Bubble size is not easy to control. | Etchepare et al., 2017; Maeda et al., 2015; Huang et al., 2022; Sakr et al.,2022 |
| Ultrasonic cavitation | Apply sound field to make the liquid generate tensile stress and negative pressure. If the pressure is too saturated, MBs will be generated. | Ultrasonic time, frequency. | The bubble size is small and uniform. | Complex operation for large-scale treatment. | |
| Optic cavitation | A certain wavelength of light is irradiated on the photocatalysis material, which makes the electrons transit, and MNBs precipitate. | Wavelength of light. | No secondary pollution. | High cost, not conducive to mass production. | |
| Jet dispersion method | The air-liquid mixture is formed after the air compressor is injected or inhaled by itself, and then injected at high speed, relying on the turbulence between the air and liquid to generate MNBs. | Air intake. | Rapid generation of MNBs with uniform size. | The air intake is difficult to control. | |
| Compressed air passing through diffusion plate method | The pressurized air enters the liquid phase through the micropores with a certain size on the special diffusion plate, and the gas forms MNBs under the shear of the micropores. | Size of micropore. | Relatively simple operation, easy to form MNBs. | Expensive device, pores are easy to block. | |
| Mechanical force high-speed shearing air method | The larger bubbles in the liquid are divided into MNBs by using the shear effect generated by the high-speed rotating impeller. | Impeller rotation. | Rapid generation of a large number of MNBs. | Unstable bubble size, high energy consumption. | |
| Dissolved gas release method | First, pressurize the gas to make it supersaturated and dissolved, and then decompress the gas to release, thus producing MNBs. | Pressure and nozzle cavitation mode. | Simple operation and low energy consumption. | Discontinuous gas dissolution and release, low efficiency. | |
| Aeration method | Directly use various micro nano bubble generators to aerate in water, producing MNBs. | MNBs generator type. | Easy to operate, non-toxic and residue free. | The instrument is expensive. | |
| Chemical reaction method | Add chemical reagents to the solution to make it react violently, producing MNBs. | Type of reactant. | High bubble generation efficiency. | Bring secondary pollution | |
| Electro-chemical method | Electrolyze water through electrode to form MNBs on the positive and negative plates. | Voltage size, electrolytic time . | The size of bubbles can be controlled. | High energy consumption and low efficiency. |
| Bubble type | T | P | Reference |
|---|---|---|---|
| MNBs | >5000K | / | Takahashi et al., 2007b |
| Air NBs | 3000K | 5GPa | Yasui et al., 2019 |
| Oxygen NBs | 2800K | 4.5GPa | |
| MNBs | 500~15000 K | 100~5000 Pa | Wang et al., 2021 |
| MNBs | 2000–6000 K | / | Sun et al., 2018 |
| Pollutants | Generation of MNBs | Type of air source | Reaction time(min) | Initial concentration/(mg/L) | pH | Temperature | Degradation rate constant/degradation rate/lnc/c0 | References |
|---|---|---|---|---|---|---|---|---|
| Alachlor | Swirling jet-induced cavitation. | air | 100 | 50 | 5.9 | 40℃ | 4.90×10−2min-1 | Wang and Zhang, 2009 |
| Rhodamine B | Swirling jet-induced cavitation. | air | 180 | 5 | 5.4 | 40℃ | 62%/5.13×10−3min-1 | Wang et al., 2008 |
| Diethyl phthalate | Aeration method | O3 | 30 | 222 | 9 | 25℃ | 98% | Jabesa et al., 2016 |
| Phenol | Dissolved gas release method. | O2 | 120 | 18.8 | 2.3 | 35℃ | 83%/2.67×10−2min-1 | Li et al., 2009b |
| Dissolved gas release method. | air | 180 | / | <7 | <50℃ | 30% | Takahashi et al., 2007 | |
| Micro bubble ozonation reactor. | O3+Ga(OH)2 | 40 | 450 | / | 25℃ | 99% | Cheng et al., 2018 | |
| Methyl orange | Spiral liquid flow coupled pressurized dissolution | O3 | 30 | 10 | / | 20℃ | 96% | Xia and Hu, 2016 |
| Aeration method | O3 | 30 | 50 | 3~11 | 20℃ | >90% | Xia and Hu., 2018 | |
| Spiral liquid flow-type. | O3 | 30 | 10 | / | / | 98% | Hu and Xia, 2018 | |
| Photoresist | Dissolved gas release method. | O3 | 9.6 | / | / | 22℃ | 100% | Takahashi et al., 2012 |
| Butylated hydroxytoluene | Aeration method | O3 | 0.5 | <2 | 7 | / | 97% | Achar et al., 2020 |
| Dimethyl Sulfoxide | Aeration method | O3 | / | / | / | / | 7.0×10-4-1.9×10-3s-1 | Li et al., 2009c |
| P-chlorophenol | Ultrasonic cavitation. | air | 120 | / | / | 38℃ | 0.00899min-1/-0.83 | Teo et al., 2001 |
| P-nitrophenol | Jet cavitation reactor. | air | 90 | 8 | 3.5 | / | 50% | Kalumuck and Chahine, 2000 |
| Trichloroethylene | Aeration method | O3 | 20 | 14 | / | / | 100% | Xia et al., 2018 |
| Polyvinyl alcohol | Dissolved gas release method. | O3 | 120 | / | <7 | <35℃ | 30% | Takahashi et al., 2007 |
| Benzothiophene | Ultrasonic cavitation. | air | 60 | / | 5 | 25℃ | 0.0492min-1 | Kim et al., 2005 |
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