Assessment of Environmental Performance of TiO2 Nanoparticles Coated Self-Cleaning Float Glass
Abstract
:1. Introduction
2. Materials and Methods
2.1. Ecodesign of an Industrial Scale Process
- There might be changes due to scale up in process yield as well as in energy efficiency of the process; these can influence the environmental burdens, as these affect the material and energy use as well as the amount of emissions and waste.
- There might be changes in technology and in the material or energy supplies.
- In LCA analysis of pilot/laboratory plants, processes are often seen as isolated or independent from each other. The effects due to changes in plant utilization are not considered sufficiently.
2.2. Goal and Scope Definition
- HEPAs (high efficiency particulate air filters), possessing 99.97% efficiency, were installed during cutting, soaking in acetic acid and coating steps.
- Use of PPE (personal protective equipment), particularly the face mask with its 95% efficiency [44] in protecting workers from dust and nanoparticles inhalation during coating, installation, use and end-of-life steps was implemented.
- A closed manufacturing system was designed.
- Use of specific packaging to limit the release of nanoparticle emissions during transportation was used.
- Transport distances of facilities, raw material, chemicals, materials for packaging from supplier to the production site have been assumed equal to 100 km, as required by the environmental product declaration (EPD) certification [45].
- Italian mixed-electric energy obtained by non-renewable sources (the electricity type mainly used in Italy) and created by ecoinvent was assumed. Obviously, adopting renewable energy such as photovoltaic energy, would enhance the environmental performance. In particular, environmental damage associated with the use of renewable sources can decrease by more than 87%. Nevertheless, this study is part of a regional Italian project, so its production must be located in the Italian territory.
2.3. Impact Assessment
2.4. Life Cycle Inventory
2.4.1. Production
2.4.2. Installation and Use Phase
2.4.3. End of Life
3. Life Cycle Impact Assessment
3.1. The Modified IMPACT 2002+ Method
Effects of Different Electricity Sources
3.2. The Modified USEtox™ Method
3.3. Comparison between the Environmental Performance NanoTiO2 Functionalized Float Glass and the Conventional Ones
- In the Non-renewable energy impact category, case B determines the higher impact (28.7 mPt on the total damage) mainly due to gas, natural, in-ground emission generated by electric energy manufacture in the production process of nanoTiO2 self-cleaning coated float glass;
- In Global warming, case B determines the higher impact (26.09 mPt on the total damage) mainly due to carbon dioxide, fossil emission generated by natural gas production used in the use phase for air conditioning.
- In Respiratory inorganics impact category, case B determines the higher impact (12.2 mPt on the total damage) mainly due to particulates <2.5 μm emission generated by the lapping process in the production stage. For innovative nanomaterials (case studies B and C), nitrogen oxide emissions in the air reduced by the photocatalytic activity of nanoTiO2 coating generated a reduction of environmental load in this category.
4. Conclusions
Supplementary Materials
Acknowledgments
Author Contributions
Conflicts of Interest
References
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Category | Components | Quantity | Unit | Source |
---|---|---|---|---|
Energy input | Electricity consumption | 244.4 | kWh | Energetic process I/O data derived from ecoinvent database. Energy consumptions were supplied by the chemical lab and scaled up with linear rate |
Materials I/O | Float glass uncoated | 9.91 | kg | Data supplied by the chemical lab and scaled up with linear rate and Colorobbia Italia SpA. for nanoTiO2 suspension |
Tap water | 52.77 | L | ||
Acetone | 263.33 | kg | ||
Acetic acid | 4.37 | kg | ||
Water deionized | 2.39 | kg | ||
Compressed air | 423.33 | L | ||
nanoTiO2 suspension | 5.84E−03 | kg | ||
Protection film (LDPE) | 1.92E−02 | kg | Data was supplied by one of the company leaders in glass production | |
Viscose fiber cloth | 0.13 | kg | ||
Concrete | 0.24 | m3 | ||
Heat gain in summer season due to nanocoating | 825.2 | kW | Data supplied by the chemical lab and scaled up with linear rate | |
Heat lost in winter season due to nanocoating | 754.13333 | kW | ||
Emissions to air | Particulates <2.5 µm | 1.43E−02 | kg | Data supplied by the chemical lab and scaled up with linear rate |
Particulates >10 µm | 2.61E−02 | kg | ||
Particulates >2.5 µm and <10 µm | 6.53 | kg | ||
Acetic acid | 7.20E−02 | kg | ||
Water | 1.29E−02 | kg | ||
Acetone | 3.31E−06 | kg | ||
Particulates <100 nm in air | 6.67E−03 | kg | ||
Particulates <100 nm inhaled | 0.75 | kg | ||
NOx | 1.17E−01 | kg | ||
Nitric acid | 2.40E−04 | kg | ||
Toluene | 92E−03 | kg | ||
CO2 | 3.92E−02 | kg | ||
Transports | Road | 85.49 | tkm | |
Waste to treatment | Disposal to residual landfill of nanoTiO2 particulates captured by filter | 4.01E−04 | g | Waste quantities were given from the chemical lab while waste treatment statistics were derived from the ecoinvent process |
Acetone wastes captured by filter to residual landfill | 5.05E−03 | cm3 | ||
Acetic acid wastes captured by filter to residual landfill | 4.33 | kg | ||
Wastewater treatment (water used during the maintenance operations of equipment) | 52.77 | L | ||
Disposal of particulates <2.5 µm and >10 µm dust captured by filter to residual landfill | 1248.21 | g | ||
Disposal waste glass (inertization) | 8.04 | kg | End of life of functionalized glass was built ad hoc according to ecodesign approach. Data were appropriately assumed |
Impact Category | Unit | Total | Production | Installation | Use Phase | End of Life |
---|---|---|---|---|---|---|
Carcinogens | kg C2H3Cl eq | 6.35E−01 | 2.33E−03 | 3.37E−01 | 1.99E−02 | 6.35E−01 |
Non-carcinogens | kg C2H3Cl eq | 6.14E−01 | 3.02E−03 | 5.15E−02 | 4.30E−02 | 6.14E−01 |
Respiratory inorganics | kg PM2.5 eq | 4.60E−02 | 3.58E−04 | −8.27E−03 | 3.11E−03 | 4.60E−02 |
Ionizing radiation | Bq C-14 eq | 8.20E+02 | 4.17E+00 | 1.88E+02 | 6.35E+01 | 8.20E+02 |
Ozone layer depletion | kg CFC-11 eq | 7.75E−06 | 1.01E−07 | 6.14E−06 | 3.51E−07 | 7.75E−06 |
Respiratory organics | kg C2H4 eq | 2.13E−02 | 2.78E−04 | −1.86E+00 | 2.69E−03 | 2.13E−02 |
Aquatic ecotoxicity | kg TEG water | 5.46E+03 | 3.58E+01 | 9.13E+02 | 2.31E+02 | 5.46E+03 |
Terrestrial ecotoxicity | kg TEG soil | 5.88E+02 | 8.05E+00 | 1.10E+02 | 6.83E+01 | 5.88E+02 |
Terrestrial acid/nutri | kg SO2 eq | 7.76E−01 | 9.62E−03 | −4.79E−01 | 6.78E−02 | 7.76E−01 |
Land occupation | m2org.arable | 5.31E−01 | 5.64E−03 | 5.08E−01 | 1.84E+00 | 5.31E−01 |
Aquatic acidification | kg SO2 eq | 2.29E−01 | 1.62E−03 | 8.40E−02 | 1.24E−02 | 2.29E−01 |
Aquatic eutrophication | kg PO4 P-lim | 7.15E−03 | 2.69E−05 | 1.58E−03 | 3.43E−04 | 7.15E−03 |
Global warming | kg CO2 eq | 4.26E+01 | 2.43E−01 | 4.03E+01 | 2.97E+00 | 4.26E+01 |
Non-renewable energy | MJ primary | 8.31E+02 | 4.44E+00 | 5.83E+02 | 3.39E+01 | 8.31E+02 |
Mineral extraction | MJ surplus | 2.87E+00 | 5.98E−03 | 1.89E−01 | 8.30E−02 | 2.87E+00 |
Radioactive waste | kg | 3.76E+01 | 1.73E−01 | 7.59E+00 | 6.47E+01 | 3.76E+01 |
Carcinogens inhaled | kg | 1.10E−03 | 3.82E−06 | 2.23E−04 | 8.17E−05 | 1.10E−03 |
Total | mPt (milli-point) | 2.522E+01 | 1.641E+01 | 1.700E−01 | 7.100E+00 | 1.534E+00 |
Damage Category | Unit | Total | Production | Installation | Use Phase | End of Life |
---|---|---|---|---|---|---|
Human health | DALY | 2.99E−05 | 3.59E−05 | 2.67E−07 | −8.61E−06 | 2.37E−06 |
Ecosystem quality | PDF·m2·year | 9.99E+00 | 6.31E+00 | 8.17E−02 | 9.72E−01 | 2.63E+00 |
Climate change | kg CO2 eq | 8.61E+01 | 4.26E+01 | 2.43E−01 | 4.03E+01 | 2.97E+00 |
Resources | MJ primary | 1.46E+03 | 8.34E+02 | 4.44E+00 | 5.83E+02 | 3.40E+01 |
Radioactive waste | kg | 1.10E+02 | 3.76E+01 | 1.73E−01 | 7.59E+00 | 6.47E+01 |
Carcinogens inhaled | DALY | 1.41E−03 | 1.10E−03 | 3.82E−06 | 2.23E−04 | 8.17E−05 |
Impact Category | Unit | NanoTiO2 Self-Cleaning Coated (Electric Energy Mix) | NanoTiO2 Self-Cleaning Coated (Renewable Energy Source) |
---|---|---|---|
Carcinogens | kg C2H3Cl eq | 9.95E−01 | 7.36E−01 |
Non-carcinogens | kg C2H3Cl eq | 7.11E−01 | 8.78E−01 |
Respiratory inorganics | kg PM2.5 eq | 4.12E−02 | 3.04E−02 |
Ionizing radiation | Bq C-14 eq | 1.08E+03 | 1.08E+03 |
Ozone layer depletion | kg CFC-11 eq | 1.43E−05 | 8.42E−06 |
Respiratory organics | kg C2H4 eq | −1.83E+00 | −1.84E+00 |
Aquatic ecotoxicity | kg TEG water | 6.64E+03 | 6.37E+03 |
Terrestrial ecotoxicity | kg TEG soil | 7.75E+02 | 7.46E+02 |
Terrestrial acid/nutri | kg SO2 eq | 3.74E−01 | 7.79E−02 |
Land occupation | m2org.arable | 2.89E+00 | 2.69E+00 |
Aquatic acidification | kg SO2 eq | 3.27E−01 | 2.40E−01 |
Aquatic eutrophication | kg PO4 P-lim | 9.11E−03 | 1.14E−02 |
Global warming | kg CO2 eq | 8.61E+01 | 4.45E+01 |
Non-renewable energy | MJ primary | 1.45E+03 | 6.76E+02 |
Mineral extraction | MJ surplus | 3.15E+00 | 3.89E+00 |
Renewable energy | MJ | 1.10E+02 | 6.87E+02 |
Radioactive waste | kg | 1.41E−03 | 1.40E−03 |
Carcinogens inhaled | kg | 7.45E−07 | 7.45E−07 |
Total | mPt (milli-point) | 2.522E+01 | 1.475E+01 |
Impact Category | Unit | Total | Production | Installation | Use Phase | End of Life |
---|---|---|---|---|---|---|
Human toxicity, cancer | CTUh # | 4.401E−06 | 3.692E−06 | 1.497E−08 | 5.65E−07 | 1.297E−07 |
Human toxicity, non-cancer | CTUh # | 1.565E−07 | 1.261E−07 | 6.657E−10 | 2.297E−08 | 6.797E−09 |
Ecotoxicity | CTUe § | 46.236702 | 38.666071 | 0.1488913 | 6.0468404 | 1.3748995 |
Human toxicity, cancer, indoor | CTUh # | 1.066E−08 | 6.344E−14 | 1.256E−09 | 2.073E−09 | 7.327E−09 |
Human toxicity, non-cancer, indoor | CTUh # | 4.359E−13 | 2.595E−18 | 5.139E−14 | 8.479E−14 | 2.997E−13 |
© 2017 by the authors; licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC-BY) license (http://creativecommons.org/licenses/by/4.0/).
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Pini, M.; Cedillo González, E.I.; Neri, P.; Siligardi, C.; Ferrari, A.M. Assessment of Environmental Performance of TiO2 Nanoparticles Coated Self-Cleaning Float Glass. Coatings 2017, 7, 8. https://doi.org/10.3390/coatings7010008
Pini M, Cedillo González EI, Neri P, Siligardi C, Ferrari AM. Assessment of Environmental Performance of TiO2 Nanoparticles Coated Self-Cleaning Float Glass. Coatings. 2017; 7(1):8. https://doi.org/10.3390/coatings7010008
Chicago/Turabian StylePini, Martina, Erika Iveth Cedillo González, Paolo Neri, Cristina Siligardi, and Anna Maria Ferrari. 2017. "Assessment of Environmental Performance of TiO2 Nanoparticles Coated Self-Cleaning Float Glass" Coatings 7, no. 1: 8. https://doi.org/10.3390/coatings7010008
APA StylePini, M., Cedillo González, E. I., Neri, P., Siligardi, C., & Ferrari, A. M. (2017). Assessment of Environmental Performance of TiO2 Nanoparticles Coated Self-Cleaning Float Glass. Coatings, 7(1), 8. https://doi.org/10.3390/coatings7010008