Photocatalysis for Water Treatment J Anthony Byrne Nanotechnology and Integrated BioEngineering Centre Engineering Research Institute SUNSNOGUIDENANO Sustainable Nanotechnology Conference 2015 ulster.ac.uk
Basic mechanism of photocatalysis with TiO 2 in presence of O 2 h e- O - 2, O 2 H, H 2 O 2, OH O 2 H 2 O organic OH OH ad oxidised organic h+ Rates are low ( typically 1% quantum efficiency) TiO 2 requires UV (only 5% of sunlight) Excellent for contaminants of emerging concern & persistent organic pollutants Nanomaterials give very high surface area for photocatalysis In some cases size quantisation effects may be observed Nano-engineering can give increased efficiencies TiO 2 most common photocatalyst due to stability and non-toxicity
Titanium dioxide (TiO 2 )
Photocatalysis has been shown to be effective for the degradation of a wide range of problematic pollutants in water including EDCs, pharmaceuticals, pesticides, dyes, etc. effective for the inactivation of disinfection resistant microorganisms including viruses, bacteria (including spores), fungi (including spores), protozoan parasites (including oocysts). Puralytics solar bag
Solar Photocatalytic Disinfection of Water
The Millennium Project commissioned by the United Nations in 2002 Millennium Development Goal Target 10: by 2015, reduce by half, the 1.1 billion people lacking access to safe drinking water and basic sanitation. The MDG water target of 88% coverage was met in 2010 748 million people still do not have access to an improved water source for drinking 1.5 million children die each year due to unsafe water Progress on drinking water and sanitation, 2014 update, World Health Organisation and UNICEF, 2014
Improved water source does not mean safe! Non-compliance with microbiological water quality guideline values by improved drinking water source type. Proportion refers to percentage (from UNICEF and World Health Organization, Drinking Water Equity, safety and sustainability, JMP Thematic Report on Drinking Water 2011)
Solar disinfection of water (SODIS) SODIS is used by more than 5 million people and in more than 30 countries around the globe
Solar Photocatalytic Disinfection h Reactive oxygen species e- O - 2, O 2 H, H 2 O 2, OH O 2 H 2 O organic OH OH ad h+ We don t like ROS oxidised organic < 387 nm for anatase TiO 2 http://www.dreamstime.com/
Continuous flow photocatalytic SODIS reactor with add on CPC. TiO 2 (Evonik Aeroxide) coated borosilicate glass tubes (0.4 mg/cm 2 ) were incorporated into the CPC-SODIS reactors used at PSA and used as a 7 L re-circulating batch system with E. coli K12 in saline (1x10 6 CFU/mL) as a model test organism.
E. coli concentration (CFU/mL) UVA radiation (W/m 2 ) E.coli concentration (CFU 10 Continuous 4 flow photocatalytic SODIS reactor 30 with add on CPC. E.coli E.coli concentration (CFU/mL) U/mL) 10 10 3 10 2 UV Data 29-04-08 Local time (HH:MM) 10 1 UV Data 07-05-08 Local time (HH:MM) 15 10:30 11:15 12:00 12:45 13:30 14:15 15:00 15:45 10:30 11:15 12:00 12:45 13:30 14:15 15:00 15:45 50 07-05-08, 01-04-08, Coated external Uncoated coated external internal uncoated internal 50 10 6 07-05-08, 10 6 29-04-08, Coated external coated internal 07-05-08, Coated internal Coated uncoated external coated external 45 internal 29-04-08, Coated internal uncoated external 45 10 5 40 10 5 40 35 10 4 35 10 4 30 30 10 3 10 3 25 25 10 2 10 2 20 UV Data 29-04-08 UV 20 UV Data Data 01-04-08 29-04-08 10 1 UV Data 07-05-08 15 10 1 UV UV Data Data 07-05-08 15 50 0 10 20 07-05-08, 30 Coated 40 external 50coated internal 60 7050 10 6 07-05-08, Coated external coated internal 10 6 Normalized 29-04-08, time Coated (min) external uncoated internal 45 29-04-08, Coated external uncoated internal 45 10 5 40 10 5 40 35 10 4 35 10 4 30 10 3 30 10 3 25 25 10 2 10 2 20 UV Data 29-04-08 20 UV Data 29-04-08 Local time (HH:MM) 10 1 UV Data 07-05-08 10:30 10 1 UV 11:15 15 Data 07-05-08 12:00 12:45 13:30 14:15 15:00 15:45 15 50 50 07-05-08, Coated external coated internal 01-04-08, Uncoated external uncoated internal 50 10 10 6 6 29-04-08, 01-04-08, Coated Uncoated internal uncoated external external uncoated internal 45 10 6 07-05-08, Coated external coated internal 45 07-05-08, Coated external coated internal 45 10 10 5 5 40 40 10 5 40 35 10 35 10 4 4 35 10 4 30 30 10 10 3 3 30 10 3 25 25 10 25 10 2 2 20 10 2 UV Data 29-04-08 20 UV Data 01-04-08 20 10 10 1 1 UV Data 07-05-08 UV UV Data Data 01-04-08 15 07-05-08 15 10 1 UV Data 07-05-08 Local time (HH:MM) 15 50 10:30 11:15 12:00 12:45 13:30 14:15 15:00 15:45 0 10 20 07-05-08, 30 Coated 40 external 50coated internal 60 70 10 6 0 10 20 30 40 50 60 70 45 Normalized 29-04-08, time Coated (min) external uncoated internal 50 07-05-08, Coated external coated internal 10 6 Normalized time (min) 10 5 29-04-08, Coated internal uncoated external 4540 35 25 20 UV Irradiance (W/m UV UV Irradiance (W/m (W/m 2 ) 2 ) m 2 )
Titania-graphene composites TEM of TiO 2 -RGO following photocatalytic reduction Fernández-Ibáñez et al (2014) Chem Eng J, DOI: 10.1016/j.cej.2014.06.089.
E. coli inactivation at several TiO 2 -RGO concentrations: ( ) 0 mg/l; ( ) 10 mg/l; ( ) 20 mg/l; ( ) 50 mg/l; ( ) 100 mg/l; ( ) 300 mg/l; ( ) 500 mg/l. DL (detection limit) = 2 CFU/mL. Inset shows the TiO 2 -RGO ( ) versus P25 ( ) efficiency on the E. coli inactivation at 500 mg/l of catalyst concentration. DL (detection limit) = 2 CFU/mL. Exposure time (min) 0 15 30 45 60 75 90 105 120 Exposure time (min) 0 2 4 6 8 10 12 14 16 18 20 E. coli (CFU/mL) 10 6 10 5 10 4 10 3 10 2 10 1 E. coli (CFU/mL) 10 6 10 5 10 4 10 3 10 2 10 1 10 0 DL = 2 CFU/mL TiO 2 -RGO versus TiO 2 -P25 500 mg/l 0 5 10 15 20 25 Solar UV-Dose (kj/m 2 ) DL 10 0 0 20 40 60 80 100 120 140 160 Solar UV-Dose (kj/m 2 )
Exposure time (min) 0 30 60 90 120 150 180 210 Exposure time (min) 0 5 10 15 20 25 30 35 40 F. solani (CFU/mL) 10 3 10 2 10 1 F. solani (CFU/mL) 10 3 10 2 10 1 10 0 DL = 2 CFU/mL 0 10 20 30 40 50 Solar UV Dose (kj/m 2 ) TiO 2 -RGO versus TiO 2 -P25 DL 10 0 0 50 100 150 200 250 300 350 Solar UV-Dose (kj/m 2 ) F. solani spore inactivation at several TiO 2 -RGO concentrations: ( ) 0 mg/l; ( ) 10 mg/l; ( ) 35 mg/l; ( ) 50 mg/l; ( ) 100 mg/l; ( ) 300 mg/l; ( ) 500 mg/l. DL (detection limit) = 2 CFU/mL. Figure insert shows the efficiency of TiO 2 -RGO ( ) with 10 mg/l versus TiO 2 -P25 ( ) with 35 mg/l on the F. solani spores inactivation. DL (detection limit) = 2 CFU/mL.
Titania Nanotubes
Comparison of titania nanostructures formed by hydrothermal treatment (a) (b) (c) (d) 50nm 10nm (e) (f) (g) (h) HRTEM images of (a)-(b) as-prepared and samples annealed at (c)-(d) 300ºC (e) 400ºC (f) 500ºC (g) 600ºC (h) 700ºC Wadhwa et al, J. Adv. Oxid. Technol. Vol. 14, No. 1, 2011
HRTEM Crystallinity, BET (m 2 /g) Optimum photoactivity for Observed best material depends on P25 the model pollutant tested As-prepared 400 C 10nm Amorphous, ~401 100% tubes Anatase, ~265 30% tubes formic acid 700 C Anatase, ~48 Phenol 100% hexagonal crystals
Toxicity study of titania nanostructures as compared to MWCNTs Cell viability was determined using A549 human lung adenocarcinoma cell line obtained from ATCC after 1, 3 and 7 days in culture using the standard colorimetric MTT assay. A commercial MTT assay kit (Sigma Aldrich, UK) was used, employing a modification of the Mosmann method No significant cytotoxic effects were observed with titania but significant cytotoxic effects were observed with the MCNTs. Wadhwa et al., Journal of Hazardous Materials 191 (2011) 56 61
Suspension vs Immobilised Photocatalyst In laboratory scale experiments many researchers employ a basic photoreactor system utilising the photocatalyst as a powder suspension (slurry) in water. The main issue with suspension reactors is catalyst recovery following treatment. P25 is widely used. It has a small primary particle size (~ 25 nm) and is hydrophilic in nature forming well dispersed suspensions in water. The particles do tend to agglomerate to some extent giving a particle size between 0.2-0.45 µm.
Post treatment catalyst recovery would add to the overall capital and running costs of any system. Nevertheless, some workers have developed pilot scale and even full scale water treatment systems employing TiO 2 in suspensions. Photocatalytic treatment plant at Plataforma Solar de Almeria, CIEMAT-PSA http://www.psa.es/webesp/instalaciones/aguas.php
Challenges There are few, if any, full scale photocatalytic water or wastewater treatment systems operating. Effective reactor engineering is required to demonstrate photocatalysis can be applied at full scale and to demonstrate the cost-benefits Novel visible light active materials are needed to improve the solar photocatalytic efficiency Photocatalysis, like other AOPs is a degradative (not simply removal) therefore control engineering of the process is difficult New photocatalytic materials must be assessed for toxicity and toxicology before deployment.
Acknowledgements University of Ulster: Photocatalysis Group: Brian Eggins, Patrick Dunlop, Heather Coleman, Jeremy Hamilton, Trudy McMurray, Alison Davidson, Dheaya Alrousan, Conor Sheeran, Shikha Wadhwa, Mukhtar Ahmed, Ashlene Vennard, Emma Magee, Sonja Webber, Louise McNally, Preetam Sharma, Brenda Cruz, Marco Ciavola, Cristina Pablos; project and visiting students; Plataforma Solar de Almeria; Pilar Fernandez-Ibanez, Inma Polo; Sixto Malato; Florida International University: Kevin O Shea; Northwestern University - Kimberly Gray; Tyndall National Research Centre- Michael Nolan; University of Cincinnati- Dion Dionysiou, Changseok Han, Miguel Pelaez; AQUAPULSE Team; PEBCAT Team; COCON Team; PCATIE Team; SODISWATER Team; Rita Dhodapkar NEERI Funding: DELNI for funding two projects under the US-Ireland Collaborative Partnership Initiative (USA NSF, RoI SFI) and RCIF Nanoparticle labs; University of Ulster for PhD student support. European Commission (SFERA - Solar Facilities for the European Research Area), EU-FP4 PCATIE, EU-FP5 PEBCAT and COCON, EU-FP6 SODISWATER, EU-FP7 AQUAPULSE; NATO Science for Peace; British Council; Royal Society for International Exchange with NEERI, India; US-EPA;