Process requirements for achieving full-flow disinfection of recirculating water using ozonation and UV irradiation

Требования к процессу для достижения полного проточного обеззараживания циркулирующей воды с помощью озонирования и УФ-облучения
Mark J. Sharrer, Steven T. Summerfelt, Scott Tsukuda, Michael Gearheart, Michael Gearheart
2008-10-31

dissolved ozone (20 ppb)oxidative reduction potential (ORP) controlozonation and UV irradiationproportional-integral (PI) feedback controlrecirculating aquaculture systems (RAS)
A continuous water disinfection process can be used to prevent the introduction and accumulation of obligate and opportunistic fish pathogens in recirculating aquaculture systems (RAS), especially during a disease outbreak when the causative agent would otherwise proliferate within the system. To proactively prevent the accumulation of fish pathogens, ozonation and ultraviolet (UV) irradiation processes have been used separately or in combination to treat water in RAS before it returns to the fish culture tanks. The objective of the present study was to determine the process requirements necessary to disinfect the full RAS flow, using ozonation followed by UV irradiation, just before the flow was returned to the fish culture tank(s). We found that a proportional-integral (PI) feed-back control loop was able to automatically adjust the concentration of ozone (O3) generated in the oxygen feed gas (and thus added in the low head oxygenator) in order to maintain the dissolved O3 residual or ORP at a pre-selected set-point. We determined that it was easier and effective to continuously monitor and automatically control O3 dose using an oxidative reduction potential (ORP) probe (in comparison to a dissolved ozone probe) that was located at the outlet of the O3 contact chamber and immediately before water entered the UV irradiation unit. PI control at an ORP set-point of 450 and 525 mv and a dissolved O3 set-point of 20 ppb provided almost complete full-flow inactivation of heterotrophic bacteria plate counts (i.e., producing <1 cfu/mL) and improved water quality (especially color and %UVT) in a full-scale recirculating system. Achieving this level of treatment required adding a mean dose of approximately 29 ± 3 g O3 per kg feed. However, because water is treated and reused repeatedly in a water reuse system, the mean daily O3 demand required to maintain an ORP of 375–525 mV (or at 20 ppb dissolved O3) was 0.34–0.39 mg/L, which is nearly 10 times lower than what is typically required to disinfect surface water in a single pass treatment. These findings can be used to improve biosecurity and product quality planning by providing a means for continuous water disinfection in controlled intensive RAS.
1
A PI feedback control loop can automatically adjust ozone generation to maintain a pre-selected dissolved O3 residual or ORP set-point for continuous full-flow disinfection.
2
Achieving this treatment level required a mean ozone dose of approximately 29 ± 3 g O3 per kg feed.
3
Mean daily O3 demand to maintain ORP 375–525 mV (or 20 ppb dissolved O3) was 0.34–0.39 mg/L, nearly ten times lower than single-pass surface water disinfection requirements.
4
Monitoring and controlling O3 dose using an ORP probe at the O3 contact chamber outlet (before UV) is easier and more effective than using a dissolved ozone probe.
5
PI control at ORP set-points of 450–525 mV or dissolved O3 of 20 ppb achieved almost complete full-flow inactivation of heterotrophic bacteria (<1 cfu/mL) and improved water color and %UVT in a full-scale RAS.

Full-flow recirculating aquaculture system (RAS) water treated by ozonation followed by UV irradiation

Process requirements and control (ORP/PI feedback, O3 dosing, dissolved O3 levels) needed to achieve full-flow disinfection (inactivation of heterotrophic bacteria, improved water quality) in RAS

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2008-10-31
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Mark J. Sharrer
Steven T. Summerfelt
Scott Tsukuda
Michael Gearheart
Michael Gearheart
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