1. 1
Validation Protocol for Performance Testing and Scaling Ballast Water Treatment Systems
Employing UV Disinfection and Filtration
Jim Cosman
Regulatory Affairs Manager
Trojan Technologies
3020 Gore Road
London, Ontario Canada
jcosman@trojanuv.com
Jim Fraser
Product Architect, Ballast Water
Trojan Technologies
Glen Latimer
Engineering Team Leader, Ballast Water
Trojan Technologies
Jennifer Gerardi-Fraser
Product Platform Manager, Ballast Water
Trojan Technologies
Abstract
Several ballast water treatment system vendors are employing UV disinfection and filtration in
systems designed to meet the IMO D2 Ballast Water Performance Standard. A key issue that
has been identified is the application of performance test results for one ballast water
treatment system to an up or down-scaled version of the exact same system so that type
approval can be given to a range of capacities. A proposed validation protocol for performance
testing and scaling ballast water treatment systems employing UV disinfection and filtration is
discussed. In addition, the concepts of UV dose delivery and factors that impact the
performance of UV systems, UV transmittance, and bioassay validation protocol for
performance testing UV systems are discussed. In addition, the factors that impact the scaling
of filtration systems are discussed.
Introduction
Over the past three decades, ultraviolet (UV) systems have gained increasing popularity as a
means of disinfecting wastewaters, drinking water, and industrial process waters. Further,
several ballast water treatment system vendors are also employing UV disinfection in systems
designed to meet the IMO D2 Ballast Water Performance Standard. UV disinfection is
considered a viable technology for ballast water treatment because it is simple to operate, no
additional chemicals are required (no chemical storage or handling), there are no residuals, and
the efficacy of UV is not impacted by salinity or pH. In addition, the performance of some UV
lamps is not impacted by water temperature variations.

2. 2
Several design standards and UV system validation protocols have evolved to support the
effective implementation of UV technologies. Examples include the National Water Research
Institute (USA) Ultraviolet Disinfection Guidelines for Drinking Water and Water Reuse, the
ÖNorm 2001 (Austria) and DVGW Standard W294 (Germany) developed for drinking water
applications, and the USEPA UV Design Guidance Manual (UVDGM) which was developed to
support the implementation of UV disinfection for drinking water applications in the United
States. Not all of these protocols are relevant to the ballast water treatment market, however
key principles and concepts derived from these protocols may be applied when considering
what factors need to be accounted for when findings for one BWMS are applied to an up (or
down-) scaled version of this system, or a type approval is issued for a range of capacities.
Background
Dose Delivery
Historically, the concept of “average dose” has been used to estimate the dose delivered by a
UV reactor. This technique is based on the assumption that the delivered dose is equal to the
average intensity within the reactor multiplied by the average retention time of the fluid within
the reactor. An average UV dose calculation is only relevant for an ideal UV reactor. An ideal
UV reactor is defined as a reactor in which every targeted organism receives the exact dose it
requires, no more, and no less, and where no UV-C photons are ‘wasted’ or absorbed by the
walls of the reactor.
In a real flow-through reactor, no two microbe, or particle, trajectories are the same and thus
each microbe flowing through the reactor will receive a unique dose. (See Figure 1). Thus, in a
real UV reactor, the interplay of flow fields and light fields determine true dose delivery.
Figure 1. Computational Fluid Dynamics Model Depicting Particles Flowing Through a UV Reactor
High Dose Microbe Path
Medium Dose Microbe Path
Low Dose Microbe Path
UV Lamp
Fluid Flow
UV Lamp

3. 3
Several authors have pointed out that hydraulic profiles and intensity gradients within UV
reactors give rise to a distribution of delivered doses as opposed to a fixed value (Qualls et al.,
1989; Scheible, 1985; Chiu et al., 1997). A dose histogram of a real UV reactor achieved by
Computational Fluid Dynamics (CFD) modeling is depicted in Figure 2. The key to predicting real
UV reactor performance is in the ability to accurately quantify the dose distribution for the
reactor at each UV transmittance (UVT), flow rate and lamp power condition.
Roughly, dose equals the intensity of the UV-C imparted on the target multiplied by the time the
target is exposed to this intensity. In a ‘normal’ reactor, the goal is to give all targets an equal
dose. However, in real life, each target receives varying intensities and retention times during
its path through the UV system. The accumulation of dose of the target at the end of the path is
what matters, and it is what determines the efficacy of the reactor as a whole. Each reactor is
unique in its hydraulic flow patterns and its intensity distribution.
UV Transmittance (UVT)
UV dose depends on the UV intensity, the flow rate, and the UV transmittance (UVT). Thus, UV
transmittance is also a key parameter to consider when designing UV systems. UVT is the
percentage of light passing through a water sample over a specified distance relative to distilled
water. The UVT is usually reported for a wavelength of 254 nm and a path length of 1-cm. UVT
is often represented as a percentage and is related to the UV absorbance (A254) by the
following equation (for a 1-cm path length): % UVT = 100 x 10-A
. If the average UVT of ballast
water reported in the literature is approximately 90%, this would mean that 90% of the light
penetrates one centimeter of water, and 81% of the light would pass the second centimeter
(Figure 3). If the UVT value is 50%, this would mean that 50% of the light penetrates one
centimeter of water and only 25% of the light would pass the second centimeter (Figure 4).
The lower the UVT of the water, the more energy that must be applied to achieve the desired
inactivation of organisms. It should be noted that a typical secondary effluent from a municipal
wastewater plant can range between approximately 50% to 65%, thus there is a great deal of
experience designing UV equipment to treat water of a similar nature to ballast water. Ballast

4. 4
water treatment systems must of necessity address water from different sources, and the UVT
of these source waters can be expected to vary dramatically from low values for sediment rich
harbor waters (river run-off) to higher values for cleaner waters such as protected
Mediterranean harbors that do not have a river inflow.
Figure 3. Water that absorbs less light, has a higher UVT. In this example, the water has 90%/cm UVT.
The amount of incident light remaining at 2 cm is 81%.
Figure 4. Water that absorbs more light, has a lower UVT. In this example, the water has 50%/cm UVT.
The amount of incident light remaining at 2 cm is only 25%.
25%
100%
50%
2 cm
100%
1 cm
60%
100%
1 cm
81%
100%
90%
2 cm
90%
50%

5. 5
Impact of UV Transmittance on System Design
The UV transmittance of the water being treated must be taken into account when assessing the
appropriate application of UV reactors for ballast water treatment. Two examples illustrate the
importance of this statement. Example 1 is a BWTS that was designed for 50% UVT water. A
system designed for this UVT will typically have lamps that are closely spaced together
compared to a system designed for a higher UVT. The close spacing ensures that no water being
treated gets in a low intensity or low ‘dose’ region. This is required as only 50% of the light
emitted by the lamp will penetrate the first 1 cm of the fluid being treated (Figure 3). This
system can be utilized for fluids with a much higher UVT (eg. 99%) because target organisms are
receiving much more than their required minimum target dose at higher UVT levels. The system
illustrated in Example 1 will be effective at treatment across the entire water quality range (50-
99% UVT).
Example 2 is a BWTS system that was designed for 90% UVT water. As the design UV
transmittance of the water being treated increases, lamps can typically be spaced further apart.
In this scenario, 90% of the light emitted by the lamp will penetrate through the first cm of
water being treated (Figure 3). This system will work for water with UVT greater than 90%,
however, it will not work for water with UVT less than 90%. For example, at 50% UVT this
system will have ‘dark zones’ or zones of inadequate UV intensity. If this is the case, the dose
delivered in these dark zones will be greatly reduced. As a result, many organisms will not
receive their required minimum target dose. Therefore, the system illustrated in Example 2 will
not be effective at treatment across the entire water quality range (50-99% UVT), rather its
effectiveness will be limited to the range greater than 90% UVT.
In summary, a UV system should be designed to be effective at the lowest UVT value of the
waters to be treated. It should also be noted that filtration and separation technologies will
likely impact UV system performance. Filtration may sometimes improve the UVT of the fluid,
and the required dose levels will change depending on the filtration pore size utilized in the
system.
UV Transmittance versus Turbidity
The unit of measurement of turbidity is NTU, or Nephelometric Turbidity Unit. The device that
measures this value is a nephelometer. The nephelometer is oriented 90 degrees to the light
source and measures the light scattered from the suspended solids in the water rather than
measuring the percentage of light absorbed from the particulate matter in the water, or
inversely, the percentage of light transmitted through the water. The particle colour, shape, and
size can affect the NTU value. It is important to note that turbidity measurements are made
using a light source with natural light wavelengths (ie. visible light), as apposed to light at the
wavelength of 254nm that is used for UVT measurements. As discussed previously, UVT is the
percentage of light passing through a water sample over a specified distance (typically 1 cm)
relative to distilled water. Turbidity can influence UVT, but they are not linearly connected, or
actually connected in any concrete way. For example, a fluid with a turbidity of 20 NTU could
have a UVT of 60% or higher, or of 5% or lower. Conversely, a fluid with a turbidity of 1 NTU
could have a UVT of 90% or greater, or 5% or lower. Fluid that is visibly clear to the human eye
may have contaminants in solution that do not block the long wavelengths of light (ie. visible
light) that a nephelometer uses to make a measurements, but these contaminants may block a

6. 6
relatively short wavelength of light such a 254 nm. High NTU values can be an indicator that the
water being evaluated may have a low UVT, but any further assumptions are very risky and
possibly incorrect. Accurate UVT measurements are critical to properly assess the impact of
water quality on UV system performance.
In addition to hydraulics and UV transmittance, other factors will impact dose delivery within a
UV reactor. Figure 5 below outlines the various factors that impact the performance of the UV
system.
Bioassay Protocols
The non-ideal behavior of real UV reactors and the complexity of their designs prohibits reliance
solely on theoretical calculations to reliably predict the UV dose delivered by the reactor, and
requires that the dose delivered by the reactor be validated using an empirical testing protocol.
The bioassay protocol is the standard approach provided by all current regulatory guidance, and
is currently the globally accepted approach for validation of the dose delivery performance of a
UV disinfection reactor. The bioassay protocol is divided into three parts: firstly the
development of a UV dose-response curve with an ideal laboratory reactor for a culture of
challenge organism (bacterium, bacterial spore or virus); secondly the passing of the challenge
organism from the same culture through the reactor being validated while it operates under
specified conditions of flow rate, lamp power level and water quality; and thirdly, a comparison
of the inactivation of the challenge organism following passage through the reactor with the
laboratory dose-response curve to determine which dose delivered by the ideal reactor gives
the same challenge organism inactivation. For those specified conditions of operation, the
reactor is thereby validated to deliver the Bioassay Equivalent Dose read from the dose-
response curve. For more extensive validation under different operating conditions (flow rate
and/or power level and/or water quality (UVT), the protocol is repeated from step two for each
operating condition.
Figure 5 Factors Affecting UV Disinfection Performance

7. 7
Comparing Average (Ideal) Doses to Bioassay Doses
Bioassay determined dose versus average (ideal) dose for a UV reactor system under varying
flow rates, UVTs and lamp power settings is plotted in Figure 6 (Petri and Olson, 2001). Poor
correlation exists between the ideal model and actual data, and using ideal dose calculations to
size UV reactor systems is, therefore, inappropriate, for several reasons:
(a) the spatial distribution of UV intensity is very difficult to model, especially since the absolute
UV lamp output is difficult to quantify
(b) hydraulic effects generally account for 20% to 50% of reactor inefficiency, meaning the ideal
model could lead to undersizing by a factor of 2 or more.
A simple example illustrates the fallacy of using ideal dose for sizing. Consider a reactor
delivering a dose of 100 mJ/cm2
for 99% of the flow and 0 mJ/cm2
for 1% of the flow.
Dose Value Discussion
Average (Ideal) 99 mJ/cm2
Average UV intensity within reactor multiplied
by average residence time
Bioassay 40 mJ/cm2
99% of the reactor achieves 5 log inactivation
of the target, while 1% of the reactor achieves
0 log inactivation. Only 2 log inactivation can
be achieved overall (100,000/100 ml organisms
to 1000.99/100 ml)
Table 1. Comparison of Average (Ideal) Versus Bioassay Dose Calculation
Ideal dose calculations would average out the dose to give dose delivered by the reactor as 99
mJ/cm2
. Clearly, only 2 log inactivation can be achieved by such a reactor. However, the ideal
dose of 99 mJ/cm2
leads one to believe that if the reactor were challenged with MS2 Phage,
where a dose of approximately 20 mJ/cm2
is required for one log inactivation, nearly 5 log
inactivation would be achieved. The preferred method to size UV reactor systems is through
bioassays, or bioassay validated computational tools.
Figure 6. Comparison between bioassay dose versus average (ideal) dose for a UV reactor system

8. 8
Filtration
A robust filtration system design is critical in ballast water treatment. The filtration system
loading rates which are designed for use in the ballast water treatment market are among the
highest in the filtration industry. This is done mainly to keep the size of the filtration equipment
within reason so it can be incorporated into an already limited available space aboard an
existing ship or a new build design.
Loading rate is key in filtration, especially in the simple screen filtration technologies which are
used in ballast water treatment and which have no depth component to them. The higher the
loading rate as measured in flow rate per area of filter media (e.g. GPM/FT2
) the more
differential pressure is produced. Higher differential pressure leads to degradation of filter
performance (more available force to drive retained particles through the thin filter media,
“particle shearing”). A filtration system not only has to catch the particles being removed, it also
has to retain them throughout the filtration cycle as well.
It is very important to note that the filtration system must be matched with UV equipment
design to achieve an efficient overall ballast water treatment system. It is important to design
systems in such a way as to optimize the strengths of both the separation and the disinfection
technology. You do not want to size the filtration system to remove particles of the size that the
UV system can easily inactivate and you do not want to oversize the UV system to inactivate
particles that can be easily removed by the separation technology. It is equally important to
align the two technologies so that there is no gap in performance between them as such a gap
would lead to a non-compliant system. The balance between filtration system performance
(particle size removal) and UV disinfection system performance (UV dose delivery to individual
targets and smaller particles) is critical to developing a robust, cost effective, and efficient
ballast water treatment system.
Discussion
For drinking water UV reactors, there are no convenient indicator organisms, like total coliforms,
that are abundantly available for routine monitoring of UV disinfection system performance for
wastewater applications; therefore, it is important that the full scale reactor be bioassay
validated to ensure delivery of the target UV dose whether the water being treated has the
indicator or not. As a result, the practice of scaling UV reactors up and down is not permitted
for drinking water applications in most jurisdictions around the world. To address higher flow
drinking water applications, duplicate validated reactors can be used in parallel to increase total
system capacity. In addition, duplicate validated reactors are sometimes employed in series to
deliver higher doses.
Scaling up is permitted under specific conditions for water reuse applications according to the
National Water Research Institute (NWRI) (USA) Ultraviolet Disinfection Guidelines for Drinking
Water and Water Reuse. Such applications generally use modular systems where the units are
scaled up by repeat units of identical geometry. For reclaimed-water application only (as they
are of lower risk to the public), if the velocity field for both the test and full-scale reactors can be
measured and the uniformity of the velocity field can be verified by empirical measurements
then larger reactors can also be used in full-scale applications. The full-scale and test reactors
must have identical lamp spacing. In addition, the full-scale reactor must be operated at the

9. 9
same velocity range and flow per lamp used for performance validation. The scale-up factor for
a given reactor is limited to 10 times the number of lamps used in the test reactor.
Filtration technologies are scalable by either of two ways; the first is by adding more of the
same model tested in a modular approach which could involve a header type arrangement or
some other method. This approach while technically accurate can become difficult to install and
manage depending on the number of overall units. The amount of plumbing, valves,
connections, and control mechanisms increases making the maintenance of such a system
cumbersome. The second way to scale a filtration technology is to extrapolate the important
design factors into a larger size unit. Unlike scaling up a UV system, a filtration system’s size can
be typically increased within reason, without sacrificing the integrity of the design or system
performance. One of the key design parameters to maintain throughout the scaling up of
various models is filter media surface area. Maintaining the same filter loading rate (flow rate
per unit of filter media area) from a smaller test unit tested should yield similar filtration
performance in a larger model.
Recommendation
It is paramount that any validation protocol for a filtration-UV ballast water treatment system
accounts for:
1. Overall system performance changes due to filter performance changes resulting from
changes in:
a. Hydraulic pressure and
b. Loading rate per unit filter surface area.
2. Overall system performance changes due to UV system performance changes resulting from
changes in:
a. Flow rate
b. UV transmittance of the water being treated
c. Changes in lamp power setting
In addition, the interrelationship between the type of filtration system and UV dose must also
be accounted for. A ballast water treatment system (BWTS) employing a smaller sized screen
(e.g. 30 microns) in the filtration system is likely to require a lower delivered UV dose for the UV
system than a BWTS employing a filter with a 50 micron screen. Therefore, the determination
of dose values over which a system is validated should be related to the filtration system utilized
in the overall system.
Scaling Filtration Systems
For filtration system scaling, if done within a reasonable factor and as long as best engineering
practices are used in the extrapolation of the key design parameters, a small scale (250 M³/hr)
filtration system should perform similarly to a larger scale filtration system (1250 M³/hr).
For ballast water filtration systems it is recommended that testing to validate encompass a
worst case scenario with respect to water quality. Typically the types of filtration systems used

10. 10
in ballast water filtration will work as well and in most cases better, in relativity clean water than
they do in the most challenging waters. There are several water quality parameters that need
to be tested such as turbidity, total suspended solids, particle counts and biological loading
while monitoring and recording the differential pressure through out the filtration cycle. Each of
these parameters needs to be tested at the pre and post filtration sample locations to
determine overall filtration performance throughout the filtration cycle. A filtration cycle begins
with a clean filtration system and continues until the differential pressure measured across the
filtration system reaches the terminal head loss point as determined by the system
manufacturer.
When scaling a filtration system, the test water should have turbidity influent levels of a NTU
range that is representative of harbor waters. In addition, the test waters should have total
suspended solids levels that are appropriate for a challenge. Influent particle counts should
have an appropriate particle size distribution so as to challenge the filtration system and the
effluent particle counts should be monitored. Biological loading should consist of organisms
that are representative of the IMO guidelines with regards to numbers, size, and type. This
filtration testing is to be done in conjunction with the UV system testing protocol to insure total
system compliance.
Scaling UV Systems
In ballast water treatment, there are not necessarily going to be convenient indicator organisms
universally and always present in the untreated ballast water, and therefore monitoring of the
treated effluent is not currently a practical solution. For UV systems, the following approach is
recommended. First, at least one system configuration (e.g. 250 m3
/h) should be bioassay
tested at a specific set of operating variables (design flow, minimum UVT, power) in accordance
with IMO testing protocols and requirements at an approved test facility.
To increase the flow capacity of the system, two approaches, multiplication and scaling may be
utilized. First, unlimited multiples, ‘N’, of the tested system (e.g. 250 m3
/h) could be used in
parallel to increase the total flow capacity of the system. In this example, a 1000 m3
/h system
may employ ‘N’ or four of the 250 m3
/h previous validated systems to attain this flow
requirement. Again, there should be no limitation on the parallel multiples allowed given that
the unit has been extensively performance tested. If a parallel arrangement is not appropriate,
another option would be to use a scaled up higher flow system that may be more cost effective
in treating the higher flows. The scaling should be limited to five times the flow of the validated
unit as long as the following conditions are met:
1. The scaled up UV system has the same lamp spacing and hydraulic configuration of the
bioassay tested validated unit.
2. The scaled up UV system employs the exact same lamp and power level as the bioassay
tested validated unit.
3. The scaled up UV system has a similar flow/velocity per lamp.
The intent of the above conditions is to ensure that the scaled up UV system has a similar UV
dose distribution as the base validated unit. By ensuring that the scaled up system has the same
lamp and lamp spacing, an attempt is being made to ensure that the light intensity is similar
between units. In addition, the requirement to have a similar flow/velocity per lamp attempts

11. 11
to manage hydraulic flow patterns in the UV system. It should be noted that this suggested
approach falls between the accepted drinking water validation approach of extensively
bioassaying each model of UV system and that of the grey water approach for scaling that is
used by NWRI in North America.
To manage the above factors, Computational Fluid Dynamics and Light Intensity modeling may
be used. Over a decade of experience exists in using these models to manage the above factors.
Specifically, ballast water treatment system manufacturers should be required to submit this
modeling to demonstrate the proper scaling of different configurations.
These models may also be used to scale system pipe diameters or other components that affect
the inflow or outflow of the BWTS so as to correlate the scaled up design to the performance
tested validated configuration.
References
Chiu, K., Lyn, D.A. and Blatchley, E.R. (1997). Hydrodynamic behaviour in open-channel UV
systems: Effects on microbial inactivation. CSCE/ASCE Env. Eng. Conf., 1189–1199.
DVGW. 2003. UV Disinfection Devices for Drinking Water Supply––Requirements and Testing.
DVGW W294. German Gas and Water Management Union DVGW), Bonn, Germany.
Lawryshyn, Y.A. and Cairns, B. (2003). UV disinfection of water: the need for UV reactor
validation. Water Science and Technology: Water Supply Vol 3 No 4 pp 293–300.
Petri, B.M. and Olson, D.A. (2001). Bioassay-validated numerical models for UV reactor design
and scale-up. Proc. the First Int. Congress on Ultraviolet Tech., Washington DC., USA, 14–16
June.
Qualls, R.G., Dorfman, M.H. and Johnson, J.D. (1989). Evaluation of the efficiency of ultraviolet
disinfection systems. Wat. Res., 23(3), 317–325.
Scheible, O.K. (1985). Development of a rationally based design protocol for the ultraviolet light
disinfection process. 58th Annual WPCF National Conf., Kansas City, Missouri, USA.
USEPA 2006. Ultraviolet Disinfection Guidance Manual. United States Environmental
Protection Agency, Office of Water, Washington, D.C.
Wright, H.B. and Lawryshyn, Y.A. (2000). An assessment of the bioassay concept for UV reactor
validation. Proc. Wat. Env. Specialty Conf. on Disinfection, New Orleans, Louisiana, USA, 15–18
March.