| Literature DB >> 25609931 |
Ilka Gehrke1, Andreas Geiser1, Annette Somborn-Schulz1.
Abstract
Important challenges in the global water situation, mainly resulting from worldwide population growth and climate change, require novel innovative water technologies in order to ensure a supply of drinking water and reduce global water pollution. Against this background, the adaptation of highly advanced nanotechnology to traditional process engineering offers new opportunities in technological developments for advanced water and wastewater technology processes. Here, an overview of recent advances in nanotechnologies for water and wastewater treatment processes is provided, including nanobased materials, such as nanoadsorbents, nanometals, nanomembranes, and photocatalysts. The beneficial properties of these materials as well as technical barriers when compared with conventional processes are reported. The state of commercialization is presented and an outlook on further research opportunities is given for each type of nanobased material and process. In addition to the promising technological enhancements, the limitations of nanotechnology for water applications, such as laws and regulations as well as potential health risks, are summarized. The legal framework according to nanoengineered materials and processes that are used for water and wastewater treatment is considered for European countries and for the USA.Entities:
Keywords: nanoadsorbents; nanomembranes; nanometals; nanotechnology; photocatalysis; water technology
Year: 2015 PMID: 25609931 PMCID: PMC4294021 DOI: 10.2147/NSA.S43773
Source DB: PubMed Journal: Nanotechnol Sci Appl ISSN: 1177-8903
Overview of types of nanomaterials applied for water and wastewater technologies
| Nanomaterial | Properties | Applications |
|---|---|---|
| Nanoadsorbents | + high specific surface, higher adsorption rates, small footprint | Point-of-use, removal of organics, heavy metals, bacteria |
| − high production costs | ||
| Nanometals and nanometal oxides | + short intraparticle diffusion distance compressible, abrasion-resistant, magnetic | Removal of heavy metals (arsenic) and radionuclides, media filters, slurry reactors, powders, pellets |
| + photocatalytic (WO3, TiO2) | ||
| − less reusable | ||
| Membranes and membrane processes | + reliable, largely automated process | All fields of water and wastewater treatment processes |
| − relative high energy demand |
Properties, applications, and innovative approaches of nanoadsorbents
| Nanoadsorbents | Properties
| Applications | Novel approaches | |
|---|---|---|---|---|
| Positive | Negative | |||
| Carbon nanotubes | Highly assessable sorption sides, bactericidal, reusable | High production costs, possibly health risk | Point-of-use, heavily degradable contaminants (pharmaceuticals, antibiotics) | Ultralong carbon nanotubes with extremely high specific salt adsorption |
| Polymeric nanoadsorbents (dendrimers) | Bifunctional (inner shell adsorbs organics, outer branches adsorb heavy metals), reusable | Complex multistage production process | Removal of organics and heavy metals | Biodegradable, biocompatible, nontoxic bioadsorbent (combination of chitosan and dendrites) |
| Zeolites | Controlled release of nanosilver, bactericidal | Reduced active surface through immobilization of nanosilver particles | Disinfection processes | Nanozeolites by laser induced fragmentation |
Properties, applications, and innovative approaches for nanometals and nanometal oxides
| Nanometals and nanometal oxides | Properties
| Applications | Novel approaches | |
|---|---|---|---|---|
| Positive | Negative | |||
| Nanosilver and nano-TiO2 | Bactericidal, low human toxicity | Nanosilver, limited durability | Point-of-use water disinfection, antibiofouling surfaces, decontamination of organic compounds, remote areas | TiO2 modification for activation by visible light, TiO2 nanotubes |
| Magnetic nanoparticles | Simple recovery by magnetic field | Stabilization is required | Groundwater remediation | Forward osmosis |
| Nano zero-valent iron | Highly reactive | Stabilization is required (surface modification) | Groundwater remediation (chlorinated hydrocarbon, perchlorates) | Entrapment in polymeric matrices for stabilization |
Properties, applications, and innovative approaches for nanomembranes
| Nanomembranes | Properties
| Applications | Novel approaches | |
|---|---|---|---|---|
| Positive | Negative | |||
| Nanofiltration membranes | Charge-based repulsion, relative low pressure, high selectivity | Membrane blocking (concentration polarization) | Reduction of hardness, color, odor, heavy metals | Sea water desalination |
| Nanocomposite membranes | Increased hydrophilicity, water permeability, fouling resistance and thermal/mechanical robustness | Resistant bulk material required when using oxidizing nanomaterial, possibly release of nanoparticles | Highly dependent on type of composite, eg, reverse osmosis, removal of micropollutants | Bionanocomposite membranes |
| Self-assembling membranes | Homogeneous nanopores, tailor-made membranes | Small quantities available (laboratory scale) | Ultrafiltration | Process scale up |
| Nanofiber membranes | High porosity, tailor-made, higher permeate efficiency, bactericidal | Pore blocking, possibly release of nanofibers | Filter cartridge, ultrafiltration, prefiltration, water treatment, standalone filtration device | Composite nanofiber membranes, bionanofiber membranes |
| Aquaporin-based membranes | High ionic selectivity and permeability | Mechanical weakness | Low pressure desalination | Stabilization processes (surface imprinting, embedding in polymers) |
Figure 1Multibarrier effect of photocatalytic titanium dioxide particles in combination with microfiltration.
Abbreviations: AOP, advanced oxidation process; UV, ultraviolet.
Effects of various nanomaterials in different aquatic organisms
| Test species | Material | Study outcome | Reference |
|---|---|---|---|
| Algae (green algae, | TiO2: 20.5 nm primary particle, 20% rutile, 80% anatase, BET surface area 45 m2/g; sonicated (Evonik P25) | EC50 32–44 mg/L | |
| Invertebrates ( | TiO2: 20.5 nm primary particle, 20% rutile, 80% anatase, BET surface area 45 m2/g; sonicated (Evonik P25) | LC50 >10 mg/L | |
| Fish (zebrafish, | TiO2: 20.5 nm primary particle, 20% rutile, 80% anatase, BET surface area 45 m2/g, sonicated (Evonik P25) | LC50 >10 mg/L | |
| Algae (green algae, | <75 nm primary particle of TiO2 (Sigma product 643017) | EC50 >100 mg/L | |
| Algae (green algae, | 140 nm in water, 79% rutile, 21% anatase, coated with alumina (ulftrafne TiO2 powder from DuPont with a coating of alumina [DuPont uf-C TiO2]) | EC50 21 mg/L (cell number) | |
| Fish (rainbow trout, | 140 nm in water, 79% rutile, 21% anatase, coated (DuPont uf-C TiO2) | LC50 >100 mg/L | |
| Algae (green algae, | Fine TiO2, 380 nm in water rutile, coated (~99% TiO2, ~1% alumina) | EC50 16 mg/L (cell number) | |
| Invertebrate ( | TiO2: Primary particle <25 nm, anatase, filtered (0.22 μm) | LC50 5.5 mg/L | |
| Frog larvae ( | Mortality by concentrations of double-wall CNTs, different concentrations | 0%–15% (10 mg/L) | |
| Nano TiO2: 25–70 nm | EC50 >20,000 mg/L (TiO2) | ||
| Nano TiO2: 25–70 nm | LC50 ~20,000 mg/L (TiO2) | ||
| Nano-/Micro-Ag | Mortality on different concentrations | ||
| Nano TiO2: 25–70 nm | LC50 >20,000 mg/L (TiO2) | ||
| Zebrafsh ( | Fullerenes | LC50 200 ppb (C60) | |
| Percentage growth inhibition of TiO2 (330 nm), SiO2 (205 nm), ZnO (480 nm) | 75%±6.6% at 1,000 ppm TiO2 | ||
| Percentage growth inhibition of TiO2 (330 nm), SiO2 (205 nm), ZnO (480 nm) | 15%±4.2% at 500 ppm TiO2 |
Abbreviations: EC50, median effective concentration; LC50, median lethal concentration; LOEC, lowest observed effect concentration; NOEC, no observed effect concentration; BET, Brauner-Emmett-Teller.
Figure 2Properties of nanoparticles in water bodies.
Risk quotient for different nanoparticles in surface water and STP effluent in Europe, USA, and Switzerland
| Europe | USA | Switzerland | |
|---|---|---|---|
| Nano-TiO2 | |||
| Surface water | 0.015 | 0.002 | 0.02 |
| STP effluent | 3.5 | 1.8 | 4.3 |
| Nano-ZnO | |||
| Surface water | 0.25 | 0.02 | 0.32 |
| STP effluent | 10.8 | 7.7 | 11 |
| Nanosilver | |||
| Surface water | 1.1 | 0.17 | 1.03 |
| STP effluent | 61.1 | 30.1 | 55.6 |
| CNT | |||
| Surface water | <0.0005 | <0.0005 | <0.0005 |
| STP effluent | <0.0005 | <0.0005 | <0.0005 |
| Fullerenes | |||
| Surface water | <0.0005 | <0.0005 | <0.0005 |
| STP effluent | 0.026 | 0.023 | 0.019 |
Note: Reprinted with permission from Gottschalk F, Sonderer T, Scholz RW, Nowack B. Modeled environmental concentrations of engineered nanomaterials (TiO2, ZnO, Ag, CNT, fullerenes) for different regions. Environ Sci Technol. 2009;43: 9216–9222.105 Copyright © 2009, American Chemical Society.
Abbreviation: STP, sewage treatment plant.