1.0 Introduction and Study Methods

Nonindigenous species invasions from ship ballast-water discharges are a growing ecological problem in coastal and inland waters throughout the world. There is consensus among scientific communities and regulatory agencies that future nonindigenous species invasions should be prevented. The current means to prevent aquatic invasions is for vessels to exchange ballast water in the mid ocean.1 In many cases, however, ocean exchange is neither possible nor practical because of the design or operation of the vessels, or because the vessels do not transit ocean waters.

The study reported herein evaluated three ballast-treatment technologies—ultraviolet radiation (UV), thermal (heat), and acoustic (ultrasonics)—for potential application to secondary treatment of ballast water (refer to Table 1-1). The study was sponsored by the Northeast-Midwest Institute (NEMW) and the Lake Carriers’ Association (LCA) under the Great Lakes Ballast Technology Demonstration Project (http://www.nemw.org/ERballast.htm).

Table 1-1. Biological Mode of Action
of Candidate Ballast Water Treatments

Ultraviolet Radiation (UV): UV treatment triggers photochemical reaction of cellular nucleic acids. When a microorganism is exposed to UV radiation, the energy is absorbed by the organism’s DNA. If the organism receives a sufficient number of UV photons in a short period, covalent bonds form between adjacent bases in the DNA. The formation of these bonds prevents the organism’s DNA from being "unzipped" for replication, and the organism’s cells are unable to reproduce. For short-lived microorganisms (e.g., viruses, bacteria, and protists), this means that a sufficiently dosed community of microorganisms will die during or soon after treatment. If exposure is insufficient to kill all of the organisms, genetic mutation of surviving individuals, as well as subsequent generations, is possible.

Thermal (Heat): Heat kills aquatic organisms by denaturing cellular proteins and/or increasing metabolism beyond sustainable levels. Death by metabolism shutdown generally occurs quicker and at lower temperatures for more complex organisms. Thermal treatment effectiveness is a function of species’ tolerances, temperature, and exposure period. Most microorganisms are able to tolerate relatively high temperatures for short periods, and lower temperatures for longer periods. Unlike with UV treatment, survivors of heat treatment are not likely to experience genetic damage/mutation.

Acoustic (Ultrasonics): Ultrasonic systems use transducers to convert electrical energy into vibratory energy of a specific amplitude and frequency. When this energy is passed through liquid, microscopic gas bubbles quickly form, expand, and implode. In the area immediately surrounding the bubbles, there are extreme temperatures and pressures, which increase chemical reactivity, polymer degradation, and free-radical production. Exposure of aquatic microorganism to ultrasonic treatment results in cellular disruption and organism death. Similar to heat treatment, ultrasonic-treatment effectiveness on microorganisms is a function of the magnitude of the transmitted energy and the exposure period. Like with heat treatment, survivors of ultrasonic treatment are not likely to experience genetic mutation.

The study was composed of three major, sequential steps:

  1. Data collection from treatment technology vendors and other sources
  2. Data synthesis
  3. Evaluation of biological effectiveness of the technologies

Data Collection from Treatment Technology Vendors and Other Sources

Vendors and manufacturers (hereafter collectively referred to as "vendors") of water-treatment technologies contacted during this study were asked to provide data on their current product lines and on products they are developing. Contacted vendors were identified through:

  • Professional contacts of Northeast-Midwest Institute and Battelle staff;
  • Library and worldwide-web internet searches;
  • Researchers, vendors, and regulatory agencies at nonindigenous species conferences and meetings; and
  • Trade publications and associations of the wastewater, drinking water, and aquaculture industries.

Although most of the useful information obtained during the study came from direct telephone surveys with treatment vendors in the wastewater and drinking water industries, valuable information and leads were obtained from each of the above-listed sources.

To secure both comprehensive and accurate data, Battelle distributed survey forms and held numerous telephone conversations with vendors and industry individuals. Significant effort was spent obtaining detailed equipment data for comparison within and among the three treatment technology categories. Vendors were asked for all pertinent equipment data for ballast-water treatment aboard a generic ship. As shown on the Vendor Survey sheet in Appendix C (distributed to all vendors), Battelle researchers specified onboard physical-operation parameters at 1,200 and 8,000-gpm (4,500 and 30,000 L/min) flow rates, 8-inch (200 mm) and 20-inch (500mm) intake diameters, 70-psi (4.8 bar) intake pressure, and four primary-treatment/filtration options. Requested vendor information included equipment weight, dimensions, power consumption, estimates of biological effectiveness, operations and maintenance procedures, known harmful materials in the systems, and cost of capital purchases. At the end of the study, 38 potential vendors had been contacted, and 15 vendors had provided useful information relevant to the current state of the three technologies.

Data Synthesis

Many of the 15 vendors who provided information to this study, several sold only made-to-order equipment or did not market off-the-shelf equipment that could meet the parameters for ship use. In these cases, Battelle researchers asked for calculated technical data from the vendors. Vendors were asked to predict sizes, operational requirements, and performance specifications of their treatment systems if they were modified for shipboard use or scaled up to the necessary flow rates. In cases were vendor-calculated data were unavailable, Battelle researchers made estimations, if possible. All cases where Battelle researchers calculated technical data involved vendor equipment that operated at lower than required flow rates (i.e., <1,200 or 8,000 gpm). In these instances, it was assumed that low-volume equipment units could be plumbed in parallel configurations to achieve the 1,200 to 8,000 gpm rates, and that equipment dimensions and power requirements would be linear.2 Battelle researchers note, however, that scaled-up data for low-volume equipment is probably conservative. There will likely be significant economies realized if low-volume equipment is scaled-up in the design or manufacturing processes, or if mixes of different sized units are installed on a vessel to optimize treatment capacity.

Battelle did not manipulate biological performance data provided by the vendors. Much of these data, usually extracted from marketing materials, was neither verifiable nor comparable across vendors, particularly among the three technologies. Thus, biological performance data was accepted as accurate, and used in the data analysis at the discretion of the researchers.

Wherever possible, equivalent technical and performance data were compared in this study of secondary treatment technologies. Technical data that were scaled by either the vendors or Battelle were assumed to add uncertainty relative to quantifying treatment-equipment dimensions, weights, and power requirements. However, any generated inaccuracies are probably conservative with respect to operational requirements, and are unlikely to affect comparison of biological performance of the treatment equipment. Problems with accuracy and comparability among the biological performance data were handled by best professional judgement of the researchers.

Readers of this report should recognize that both ballast management and water treatment are rapidly advancing fields. The information presented in this report is a "snapshot" of the three studied technologies. Most of the vendors surveyed during the study are producing products for the highly competitive industrial-waste and municipal water treatment markets. The information that they provided to Battelle intentionally emphasized the positive attributes of their products. Despite this self-promotion, it was evident that all of the contacted vendors are continually improving their products. The equipment that they are currently marketing will likely become smaller, lighter, more efficient, and less expensive as the technological advances are made. Most vendors expressed certainty that once exact shipboard specifications are determined, an efficient treatment system with their technology could be designed for onboard ballast-water treatment.

Evaluation of Biological Effectiveness of the Technologies

The focus of this study was on the biological effectiveness of secondary-treatment systems for ballast water. Effectiveness was defined by a technology’s ability to disinfect ballast water of microorganism communities. Full disinfection of ballast water was defined as inactivation, destruction, and/or removal of bacteria, viruses, cysts, and other aquatic microorganisms for making the water "safe" for discharge in cargo-port waters. In this study, this level of disinfection is destruction of 99.9% of the viable microorganism population (a 3log reduction) or better.

Microbiologists concerned with the rate of killing of bacteria sometimes refer to "Chick’s law for killing," which hypothesizes that the rate of killing of bacteria follows first order kinetics when plotted exponentially (microbiologists only think in exponents as the numbers of microorganisms per sample are so high, in the order to e+4 to e+8 per milliliter in the real world). Roughly translated, any ionizing radiation, or heat, or certain chemicals will kill an individual bacterial cell with a single hit. However, due to the number, concentration, and size of small microorganisms (e.g., bacteria); and the intensity and size of photons, electrons, or chemical molecules; a straight line is generated when the log number of bacteria is plotted against the time of exposure. However, microbiologists have found this "law" to be only partially correct.

In treatment systems short of sterilization,3 surviving microorganisms will be more resistant to the successive treatments by the same agent. Resistance to a killing agent (chemicals, UV, heat, and ultrasonics) is most pronounced if exposure is low and over a prolonged period. Resistance development is generally not a concern in single-treatment ballast-water systems, especially if the killing agent is sufficiently strong and exposure is short duration. Resistance development could be of concern, however, if successive treatments of ballast water are considered (e.g., treating water on both intake and discharge).

Particles, films, and crevices are significant obstacles to killing microorganisms. Academic microbiologists generally only work with cultures in dissolved media, so that microorganisms are the biggest particles in the solutions. In real-world systems, anything bigger then a microorganism can potentially block the killing agent from getting to the microorganism. One classic example is a microbial film or "slime layer," where treatment of the outside of the layer with UV or heat has virtually no affect on microorganisms on the protected side of the layer. Barriers to chemical or physical killing agents are thus of major concern to the design and operation of a ballast-water treatment system.

In summary, it is important to understand that the 3log disinfection level used as a measurement standard for biological effectiveness is somewhat arbitrary. With the very large volumes of water being quickly treated in shipboard systems, 3log disinfection means that many individual organisms (0.01% of the original population) will survive and potentially invade a new environment. However, readers should also realize that 3log disinfection is a substantial change. In other treatment processes (e.g., food and beverages), a 3log disinfection is considered "sterile." In a practical sense, the remaining numbers of microorganisms are generally too low to cause spoilage within normal holding times for milk, water, or other material. Furthermore, natural defense systems (e.g., in the human body) can overcome small numbers of disease organisms. Analogously, receiving waters are the human body. Released microorganism populations that have undergone 3log disinfection are considered by the authors of this report to have low potential for successfully invading a new environment.

Organism and Sediment Size vs. Treatment. The relationship of target organism size and suspended sediment size is very important relative to the primary and secondary ballast-water treatment. This study evaluated secondary treatment efficacy under no-, 250-m m-, 100-m m-, and 25-m m primary treatment filtration scenarios.4

Under the no-filtration pretreatment scenario, the size of organisms and sediment particles drawn into a ship’s ballast water intake is limited only by steel grates or strainers on ships’ ballast intakes. Strainer openings are usually 10-15 mm (0.4-0.6 inches), but fouling and corrosion can significantly change this pore size (AQIS, 1993; Carlton et al., 1995). For the purposes of this study, we assumed that incoming, unfiltered ballast water contains biological and nonbiological matter no greater than 15-mm diameter. Consequently, biological components of screened ballast-intake water can potentially include all suspended sediment in the water and any of the organism groups listed in Table 1-2. The sediment portion includes all nonliving, dissolved and suspended organic and inorganic particulate matter in the water column. With respect to ballast water treatment, suspended sediment is of major concern because its presence can negatively affect performance (i.e., killing of live organisms) of all three of the treatment technologies evaluated in this study.

 

Table 1-2. Relative Sizes of Microorganisms

Microorganism

Approx. Size

Examples

Viruses

0.02 – 1 m m

Hepatitis virus, 0.02 m m; HIV, 0.08
Bacteria, cocci (spherical) and bacilli (rod-shaped)

0.25 – 5 m m

Pseudomonas, 0.5 – 0.62 m m
Vibrio cholerae, 1 m m
Protozoans

1 – 80 m m

Myxosporeans, 5 – 30 m m
Microsporidians, 1 – 10 m m
Fungi

1 – 100 m m

Aphanomyces
Cyanobacteria (blue-green algae)

0.2 – 2 m m

Microcystis elebans, 2-6 µm
Spirulina subsalsa, 0.4-4 µm
Chroococcus limneticus, 6-12µm
Phytoplankton (includes diatoms, dinoflagellates, cryptomonads, macrophyte spores, and other pico-, nano-, micro-, and colonial phytoplankton)

2 m m – 2 mm

Skelatomina, 7-15 m m
Thalassiosira eccentrica, 40-120 m m
Cryptomonas, pseudobaltica, 18-30 m m
Chroomonas amphioxera 10-19 m m
Euglena proxima, 18-25µm
Pfiesteria, 5-450 m m (cyst stage, 7-60 m m)
Gymnodinium (red tide species), 20-25 m m
Gonyalaux (red tide species), 28-43 m m
Zooplankton

30+ m m

zebra mussel veligers, 30 – 65 m m
adult calanoid copepods, 1.6 – 12 mm
various crab and shrimp zoea, 5 mm
starfish (Asterias rubins) larvae, 2 mm
Fish eggs

0.5 – 5.0 mm

 
Larval fish

2+ mm

 

 

The chemical and physical characterization of suspended sediment is highly variable on both spatial and temporal scales. In general, suspended sediment concentrations are greater in coastal areas and greatest river mouths. Fast currents and high waves can keep relatively large-size sediment particles (1+-mm diameter) in suspension and available for suction into ballast tanks. However, in quiescent areas, these larger particles rapidly sink to the bottom. In comparison, small particles of sediment can remain in suspension long after current and wave energy has subsided. These fine-grain suspended sediments are usually present in shallow water columns typical of port areas.

For the purposes of this study, we were primarily concerned with how the attributes of the suspended sediment in the range of 0.1 to 100 m m, and how the entrainment of this sediment affects secondary ballast-water treatment. Sediment particles of this grain size can easily be sucked into the ballast system and remain suspended in the fast moving water, until it is either filtered by a device with <100-m m pore size, or pumped into ballast tanks (where it can settle to the bottom). Compared to larger diameters (i.e., >100-m m), this sediment class is also much more likely to be contaminated with organic and inorganic pollutants, be associated with microflora and fauna (including nonindigenous species and pathogens) (Smith et al., 1996), and is sufficiently large to shield microflora and fauna from some treatment processes (refer to Table 1-2).

In general, the removal of sediment via filtration (1) increases treatment plant performance and (2) reduces treatment-plant energy requirements. Furthermore, primary treatment also removes microorganisms that are larger than the pore size of the filtration system.

Table 1-3 provides a summary of microorganism and sediment size, verses the four pretreatment scenarios used in this study. Readers should keep in mind that while the generalities presented Table 1-3 hold for the four scenarios, numerous ballast-site specific and ship-specific variables also affect treatment performance.

  • Intake water will contain different amounts of sediment and organisms depending on regional weather events, water temperatures, seasons, and proximity of the ship’s ballast intake to the shoreline and sea bottom.
  • Ship-specific variables include intake velocities, location of intakes on ships’ hulls, pore size of the intake screens, and pumping configurations.
  • Microorganism mortality/survival of the secondary-treatment processes is a function of the operational efficiency of the equipment and the organisms’ exposure to the treatment process.

Presentation of technology data and analysis. Descriptions of current UV, ultrasonics, and heat treatment technologies follow in Section 2, 3, and 4. Following the presentation of the technologies, Section 5 compares and contrasts pertinent attributes and performance information of the technologies. Section 6 briefly describes two other potential ballast water treatments encountered during the course of this study. References and appendices follow at the end of the report.

 

Table 1-3. General Characteristics of Ballast Water
Entering Secondary Treatment Equipment under the Four
Pretreatment (Filtration) Scenarios Evaluated in this Study

Pretreatment Scenario

Intake Quality for Secondary Treatment

No Filtration In the no-filtration scenario, intake water is screened to 15-mm at the hull fitting. This excludes large macrophytes, fish, and invertebrates. Juvenile fish, adult and juvenile zooplankton (e.g., copepods), vertebrate and invertebrate fish larvae and eggs, phytoplankton, as well as cyanobacteria, fungi, protozoa, bacteria, and viruses will enter the secondary treatment system. All suspended sediment entering the intakes will be delivered to the secondary treatment system.
250-m m Filtration The 250-m m filtration scenario excludes all fish, most invertebrates, and all macrophytes. Small zooplankton (e.g., zebra mussel veligers) will get into the system. All phytoplankton, cyanobacteria, fungi, protozoa, bacteria, and viruses will make it through the 250-m m filter. Suspended sediment load will be the same as for the no filtration scenario.
100-m m Filtration The 100-m m filtration scenario excludes all fish, all invertebrates with the exception of small juvenile forms (e.g., zebra mussel veligers), and all macrophytes. Some colonial and chain-forming phytoplankton will be excluded by the 100-m m filter. Most phytoplankton, however, as well as all cyanobacteria, fungi, protozoa, bacteria, and viruses will pass enter the secondary treatment system. If the intake water is exceptional turbid, some of the large-fraction grain sizes will be trapped in the filter, but most suspended sediment will enter the secondary treatment system.
25-m m Filtration The 25-m m filtration scenario excludes all fish, all invertebrates, most phytoplankton, and some large forms of aquatic fungi and protozoans. Most cyst stages (e.g., dinoflagellates) will also be excluded, as will most of suspended sediment fractions. Cyanobacteria, bacteria, and viruses, and the remaining fungi and protozoans will enter the secondary treatment system (only ultrafiltration or reverse osmosis is capable of removing bacteria and viruses).

 

Endnotes

1 On April 10, 1998, the U.S. Coast Guard issued a proposed Federal rule, pursuant to the National Invasive Species Act of 1996 (NISA), that amends existing regulations for the Great Lakes ecosystem, establishes voluntary ballast water exchange guidelines for all other waters of the United States, and establishes mandatory reporting and sampling procedures for vessels entering U.S. waters.

2 Scale-up of low-flow vendor equipment was conducted in whole-equipment equivalents. For example, if a vendor only marketed 500 gpm units, Battelle researchers multiplied the 500-gpm equipment dimensions, weight, and power consumption by a factor of 3 to allow comparison to 1,200-gpm units marketed by other vendors.

3 Sterilization is usually defined as killing >12 logs.

4 Measurement equivalents: 1 m m = 10-3 mm = 10-6 m; 1000 m m = 1 mm = 0.001 m

01 April 2001
http://www.nemw.org/Balsurv1_Intro.htm