TRACK AUV-AOP 3
An innovative Solution to secure safe Water with O3/H2O2 and UV
Ludwig Dinkloh, Xylem Services GmbH An innovative Solution to secure safe Water with O3/H2O2 and UVLudwig Dinkloh, Xylem Services GmbH The Dunea Water Company provides drinking water to over 1.3 Mio customers with an average flow rate of ~ 9,000 m3/h (57 MGD). The water source is the River Meuse. In a dead end side stream of the Meuse River, iron sulfate is dosed for coagulation. This side stream is used as a natural reservoir for self-purification. Dunea abstracts the water from the river and micro sieve it, and then it is transported to the pretreatment. The water is filtered over dual layer rapid sand filtration, and is now clean enough to infiltrate it and it is transported to the dune area. After a residence time of 3 months in the dunes the water is recovered and at three post treatment locations drinking water is produced.
Treatment of algal organic matter in drinking water with UV/Cl2 and UV/H2O2 advanced oxidation: Assessment of disinfection byproduct formation
Fateme Barancheshme, University of North Carolina at Charlotte Treatment of algal organic matter in drinking water with UV/Cl2 and UV/H2O2 advanced oxidation: Assessment of disinfection byproduct formationFateme Barancheshme, University of North Carolina at Charlotte The aim of this study is to assess the change in molecular weight (MW) distribution of natural organic matter (NOM), including that of algal origin, during advanced oxidation processes (AOPs) and determine the correlation between molecular size and disinfection byproducts (DBPs) formation. High performance size exclusion chromatography (HPSEC) equipped with Sievers M9 dissolved organic carbon (DOC) detector was used to assess the MW distributions of organic matter in drinking water samples before and after UV/Cl2 and UV/H2O2 treatment. By doing so, the effect of AOPs on MW distribution of organic matter was assessed, and the study investigated which organic matter fractions are likely responsible for DBPs formation. Drinking water samples were collected with no background algal organic matter. AOPs were conducted on bench-scale and samples were exposed to UV doses up to 2000 mJ/cm2 to simulate full-scale UV dose range in AOPs. Some samples were spiked with extracted algal organic matter. The MW distribution of organic matter in the water samples at different levels of treatment was assessed to determine any correlations with DBP formation. Formation of trihalomethanes and haloacetic acids was measured using EPA methods 551.1 and 552.3 after a uniform formation conditions test.
Innovative UV AOP control strategy for combined Mycrocystin, Taste and Odor, and Virus inactivation
Keith Bircher, Calgon Carbon Corporation Innovative UV AOP control strategy for combined Mycrocystin, Taste and Odor, and Virus inactivationKeith Bircher, Calgon Carbon Corporation The methodology for the validation of full scale UV disinfection reactors using bioassay techniques incorporating surrogates of different UV sensitivity is well understood. The destruction of organic contaminants in water by hydroxyl radicals generated by UV and hydrogen peroxide is more complex in that the water itself exhibits a scavenging demand where other constituents in the water and the concentration of peroxide affect performance. | TRACK BUV LEDs 4
UVC -LED and Wastewater- A marriage whose time has Come
Gary Hunter, Black & Veatch UVC -LED and Wastewater- A marriage whose time has ComeGary Hunter, Black & Veatch UVC LED system have been developed for point of use application as well as for use in the potable drinking water market. Literature indicates that UVC LED systems have been relatively successful at smaller flows with high water quality requirements. LEDs use in wastewater provides some challenges that limit the overall throughput capacity. These challenges relate to not only water quality, design of the reactor, cooling of LEDs and hydraulics. Recent testing indicates that an understanding of the materials of the reactor construction may also play a role in the design of the system. This presentation provides results of modeling work conducted to enhance the efficiency of the UVC-LED system for wastewater. Modeling was conducted using FLUENT to ensure that the hydraulic design was optimized before the radiation model was incorporated into the design. Prototype reactors were developed and tested based on the results. The findings and recommendations of the modeling approach will be presented.
Not All Water Is Created Equal: The Type of Water Used Can Affect Measured Log Inactivation of MS2
Shawn Verhoeven, GAP EnviroMicrobial Services Ltd. Not All Water Is Created Equal: The Type of Water Used Can Affect Measured Log Inactivation of MS2Shawn Verhoeven, GAP EnviroMicrobial Services Ltd. We have seen that the type of water used, whether de-chlorinated tap, ground, ultrafiltered, de-ionized, distilled or waste water, or certain water types mixed with UVT modifiers, can have a dramatic effect on the log reductions of MS2, and other bacteriophage, measured through ultraviolet (UV) reactors, in collimated beam experiments and in ultrafiltration (UF) flow through tests. This impact is important to understand while performing a validation of a water disinfection technology, including UV systems and ultrafilters, as enhanced inactivation of a surrogate microbe will result in in over stating the performance when compared to a real-life installation. Essentially, a flow through validation is an experiment to prove that a certain disinfection technology is effective in reducing harmful contaminates, and quality control is important to any experiment. Validation protocols do have quality control procedures in place such as prescribed in the UVDGM, NWRI, and NSF guidance, but the water used for testing is often not scrutinized enough. This is particularly concerning when looking at the 2019 revision of NSF 55 for UV LED systems where no collimated beam test is required, and the current NWRI guidance where a standard curve is used for stating a dose with wide QC bounds.
Considerations in Treatment of Ultra-Low UV Transmittance liquids using UV-C LED Technology
Jennifer Pagan, AquiSense Technologies Considerations in Treatment of Ultra-Low UV Transmittance liquids using UV-C LED TechnologyJennifer Pagan, AquiSense Technologies Historically, liquids with low ultraviolet transmittance (UVT) have been treated using chemical or thermal disinfection processes. Numerous concerns, from chemical byproducts to consumables reduction and heat induced nutrient degradation, have increased interest in the use of alternative methods. Particularly in beverage processing, further considerations related to wavelength selectivity and the risk of heavy metal contamination have generated interest in UV technology employing UV-C LED light sources. |
Break & Exhibits
TRACK AUV-AOP 4
Quenching of H2O2 after advanced oxidation processes using granular iron (III) oxide
Olya Keen, UNC Charlotte Quenching of H2O2 after advanced oxidation processes using granular iron (III) oxideOlya Keen, UNC Charlotte Quenching of residual hydrogen peroxide (H2O2) after advanced oxidation processes is one of the biggest operational challenges, especially for UV/H2O2 processes where high concentrations of H2O2 are necessary due to its low UV absorbance. Effective quenching is particularly important for drinking water treatment, as residual H2O2 has a high chlorine demand
Photochemical degradation of antioxidants: kinetics and molecular end products
Sofia Semitsoglou-Tsiapou, Biology Centre CAS Photochemical degradation of antioxidants: kinetics and molecular end productsSofia Semitsoglou-Tsiapou, Biology Centre CAS Organic molecules in the ocean store as much carbon (C) as exists in the atmosphere, thus their reactivity has important implications for the global C budget. Studies suggest that a substantial fraction of the complex, presumably recalcitrant, marine dissolved organic carbon (DOC) comprises of molecules rich in highly oxygenated, aliphatic functionalities. Although there may be multiple pathways by which these molecules are produced, we propose that photochemical degradation of algal metabolites via solar light in the presence of reactive radicals is a crucial source. Such abiotic formation of recalcitrant DOC can be tested using carotenoids and related structures as model compounds. This work aimed to characterize radical-assisted, solar degradation of known antioxidants as well as carotenoid-like compounds produced by a variety of organisms, including fungi and algae. The antioxidant activity of molecules harvested from culture media of five species of Ascomycota was assessed via the ABTS radical scavenging assay, exhibiting up to 45 mM Trolox equivalent, roughly 20-fold higher than that of b-carotene. A preliminary screening of both biomass and medium samples via liquid chromatography-mass spectrometry (LC-MS) revealed known antioxidants, such as semiquinones, carotenoids (canthaxanthin), and b-carotene degradation products (beta-apo-4'-carotenal and retinal). Consequently, five representative antioxidant standards were selected and their organic solvent-water aggregates were irradiated under solar light assisted by a constant dose of H2O2, mimicking OH-radical formation in the ocean’s euphotic zone. Degradation kinetics determined via UV-Vis spectroscopy revealed orders of magnitude differences in the reaction rate constants (fucoxanthin > b-carotene > astaxanthin > coenzyme Q10 > vitamin K2), suggesting that heterogeneity in the aliphatic chain and headgroup linkage play important roles in reactivity and may yield distinct oxidation products. LC-QTOF (Quadrupole Time-of-Flight)-MS protocols were applied to identify the structures of reaction products, which were hypothesized to represent short-chain, water-soluble, hydroxylated, alicyclic, putative biomarkers of recalcitrant DOC.
Nitrite formation during the Vacuum UV Photolysis of Nitrate-contaminated Water: Could a pinch of salt help?
Madjid Mohseni, University of British Columbia Nitrite formation during the Vacuum UV Photolysis of Nitrate-contaminated Water: Could a pinch of salt help?Madjid Mohseni, University of British Columbia Vacuum UV (VUV), as one of the UV-based advanced oxidation processes (AOPs), has shown great promises for degradation of micropollutants in drinking water. Early research demonstrated that hydroxyl radicals generated by VUV can effectively degrade a range of micropollutants under different water matrices and operating conditions. A commonly found solute that might have significant impact on the process is nitrate. Irradiation of nitrate with lower wavelength UV and VUV may result in the formation of nitrite. Given that nitrate and in particular nitrite are potentially harmful compounds, their presence and formation are important sources of concern during the VUV process, and warrant further research. | TRACK BUV LEDs 5
Integrated thermal technology for maximizing UV LED performance
Pao Chen, Violumas Integrated thermal technology for maximizing UV LED performancePao Chen, Violumas UVC LEDs: How heat dissipation influences reliability & optical output More Speakers Announced Soon! | Exhibit Theatre10:15 - 11:00 & 11:15 - 12:00
IUVA Young Professionals Ask Me Anything
11:15am - 12:00pm IUVA Young Professionals Ask Me Anything11:15am - 12:00pm Panelists:
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Lunch & Exhibits
1:30 - 3:00 PM |
TRACK AUV for Food Safety
Challenges of Commercial Adaptation of UVC Preservation Processes of Opaque Beverages and Ingredients
Tatiana Koutchma, AgriFood Canada Challenges of Commercial Adaptation of UVC Preservation Processes of Opaque Beverages and IngredientsTatiana Koutchma, AgriFood Canada Ultraviolet (UVC) technology for treatment of beverages has an advantage of continuous mode, lowers investment, and offers instant energy savings and packaging flexibility. The effectiveness of UVC light at 253.7 nm was demonstrated against food borne pathogens, natural micro-biota, moulds and yeasts but mainly in bench and pilot scale studies. Also, better product quality, higher nutritional content and fresh-like sensory attributes of juices, milk and other soft drinks were shown compare to thermal processing. Despite these obvious benefits and successful application of UVC for municipal and wastewater treatment, commercialization of UVC for opaque beverages and ingredients has been slow. Very limited microbiological, quality sensory data has been reported and validation studies conducted in commercial scale. Food processors who are interested in using UVC technology have to not only select the most appropriate system for their application but also establish processing conditions and UV dose to achieve their safety, shelf-life and quality objectives and properly integrate UVC system in the existing processing line. Product overdosing with UVC light can potentially adversely affect quality of food products due to a variety of organic photochemical reactions and result in off-flavors.
UV treatment efficacy and bacterial cell aggregation
Eirini Vitzilaiou, University of Copenhagen UV treatment efficacy and bacterial cell aggregationEirini Vitzilaiou, University of Copenhagen The Food Industry aims to reduce drinking water intake and wastewater discharge by reconditioning the food processing water for reuse. Membrane filtration and UV-irradiation are commonly employed. Some studies have indicated that UV-irradiation may lead to increased microbial cell aggregation, which would decrease the efficiency of the UV-treatment. The objective of this study was to assess if cell aggregation increased in bacterial strains, isolated after UV-C treatment of a slaughterhouse water sidestream, after exposure for 2, 4, 10, 20 and 30 minutes at 255nm. The UV-LED device PearlBeam (Aquisense Technologies) was used, according to the protocol of Bolton and Linden (2003). Inocula of 10^8 cells/mL were prepared in Saline Peptone Solution (8.5g salt and 1g peptone/L distilled water). Control samples were stirred in a similar set-up without UV-exposure. CFU/mL determination was conducted, and phase-contrast microscopy performed, using the IC Capture 2.4 software to capture images of the UV-treated and untreated samples. Particle number/size distribution was analysed, using Image J and R studio software. In this set-up, UV-C treatment caused a substantial decrease to the non-aggregating Gram-negative bacterial population within the first 2 minutes of exposure (~25mJ/cm2) with limited further reduction. The naturally aggregating Gram-positive bacterial strain displayed increased robustness with ≤3log reduction after 30min. of UV-exposure. The tailing phenomenon was observed, but no UV-induced aggregation. There is a need to investigate further the parameters influencing the inactivation kinetics of relevant microorganisms to ensure safe fit-for-purpose water reuse in the Food Industry.
Efficacy of Ultraviolet-C Light Emitting Diodes at 277 NM for Inactivation of Penicillium Expansum Spores on Apples
Tatiana Koutchma, Guelph Research and Development Center, Agriculture and Agri-Food Canada Efficacy of Ultraviolet-C Light Emitting Diodes at 277 NM for Inactivation of Penicillium Expansum Spores on ApplesTatiana Koutchma, Guelph Research and Development Center, Agriculture and Agri-Food Canada A comparative study was performed to assess the efficacy of UV-C light emitting diodes (UV-C LEDs) at 277 nm and low-pressure mercury (LPM) at 253.7 nm to inactivate Penicillium expansum spores on apple skin at 4°C or 25°C. In saline, the D value for the inactivation of P. expansum spores supported at 277 nm was 6.62 mJ/cm2 at 25°C and 7.19 mJ/cm2 at 4°C, which was significantly lower than at 253.7 nm (9.26 mJ/cm2). The UV-mediated inactivation of P. expansum spores on the surface of apple skin followed non-linear kinetics with an initial linear phase followed by tailing. The calculated D values for spores on apple surface were significantly higher compared to within saline (14.49 and/18.80 mJ/cm2 with 277 nm at 25°C and 4°C, respectively, compared to 23.00 mJ/cm2 with 253.7 nm). These higher D values could be due to protective constituents within the peel or more likely the shading effects from the contours on the apple surface. Yet, the log reductions achieved (>2 log CFU) were found to be equivalent to washing in hypochlorite solutions (200 ppm free-chlorine) as current industrial practice. UV-C light at 277 and 253.7 nm (500 mJ/cm2) was shown to prevent spoilage of inoculated and stored apples (28 days) if treated prior to mechanical damage. The same UV-C treatments at fluences corresponding to inactivation of 2 log CFU of P. expansum did not impact apple physico-chemical quality parameters during 12 weeks of storage at 25°C. | TRACK BUV LEDs 6
The expanding potential of biofilm inhibition and disruption by UV-C LEDs
Rich Simons, AquiSense Technologies and Graham Gagnon, Dalhousie University The expanding potential of biofilm inhibition and disruption by UV-C LEDsRich Simons, AquiSense Technologies and Graham Gagnon, Dalhousie University The numerous benefits of UV-C LEDs have led to anticipation of their usage across a range of industries. However, initially low power outputs focused integration efforts on the disinfection of planktonic species in small-scale drinking water systems; early developments in efficient reactor design allowed the technology a foothold in this industry and drove expansion of the market to accommodate its unique characteristics. As UV-C LEDs become simultaneously cheaper and more powerful there is greater interest in fulfilling their potential in a wider range of applications. One such area is in the inhibition and disruption of nuisance biofilms.
UV-LEDs in water scarce settings: Biofouling mitigation during drip irrigation with reclaimed wastewater in Israel.
Tara Randall, University of Colorado Boulder UV-LEDs in water scarce settings: Biofouling mitigation during drip irrigation with reclaimed wastewater in Israel.Tara Randall, University of Colorado Boulder According to the UN, 70% of the world's freshwater is used for irrigation. Water reuse in agriculture has large potential to decrease pressure on the environment for water resources. Drip irrigation with wastewater (WW) has become more common in the last decades. Drip irrigation is advantageous for many reasons, including water efficiency. Unfortunately, emitters often clog due to the formation of biofilms. When treated WW effluent is used for drip-irrigation, chlorination is the most common method for reduction of emitters' bio-clogging. However, chlorine disinfection has many disadvantages, including the formation of disinfection-by-products (DBPs) as well as high capital/ operation costs.
Opportunistic pathogen deterrence in premise plumbing using UVC point-of-use devices: Minimum surface irradiation intensities for biofilm prevention
Hamed Torkzadeh, Clemson University Opportunistic pathogen deterrence in premise plumbing using UVC point-of-use devices: Minimum surface irradiation intensities for biofilm preventionHamed Torkzadeh, Clemson University Multispecies biofilms growing on interior surfaces of showerheads and other premise plumbing components are known reservoirs for opportunistic respiratory pathogens (ORPs) such as Legionella spp., Nontuberculous Mycobacteria (NTM), and Pseudomonas aeruginosa. Several efforts have reported the detection of ORPs in hospital showerheads and faucets. The number of cases of disease caused by Legionella spp. has increased by more than 5 times during 2000-2015 and the number of NTM cases has increased by 95% during 1994-2014. The increase in cases of diseases mandates a substantive public health response. With the emergence of efficient and compact deep-UV light emitting diodes (UV-LEDs), shower heads equipped with internal germicidal irradiation have been proposed as point-of-use ORP prevention tools for hospital dormitories. To advance this technology, we have anticipated performance challenges associated with high UV resistance of ORPs within realistic biological matrices (infected amoebae and detached biofilm flocs), as well as the potential for exacerbated biofilm growth on surfaces exposed to indirect/sublethal UVC intensities. The magnitude of minimum UVC intensities required for complete biofilm prevention on continuously irradiated surfaces is a key unknown parameter, and determination of which presents many experimental challenges. Here we will present the development of laboratory protocol for determining minimum UV intensities for biofilm prevention, including flow cell configuration, irradiation methods, and microscopy characterizations. Results of irradiation studies of OBP-harboring biofilm-formers and minimum UVC intensities required to completely prevent biofilm will also be presented. |
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