Environmental Science & Engineering - www.esemag.com - March 2004
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Multi-stage filtration for North Haven,Maine
By Robert Abernethy, P.Eng.
Clean and healthy water has
always been considered a basic
human right for citizens in
developed countries but there
have been some notable outbreaks of
water-borne diseases in several small
Canadian communities in recent years.
These have sharply focused the attention
of community leaders on the otherwise
mundane topic of water treatment.
One positive outcome has been
the realization by community leaders
of their responsibilities in the delivery
of water, including the protection of
source waters, the provision of adequate
water treatment, and the delivery
and monitoring of safe water by
trained water professionals.
Meeting these responsibilities has
been challenging for many communities.
The challenge for small communities
is compounded for several reasons,
mostly related to the problem of
economies of scale and lack of
resources. Small communities often do
not have the power or the resources to
protect watersheds and frequently rely
on poor water sources. Small communities
usually do not have local engineering
resources to design or manage
their water systems and must rely on
outside expertise. Local operators
often have multiple community
responsibilities and may not have the
time or training to operate complex
water treatment plants. Finally, the ongoing
cost to operate a water system
can be crippling to a small community.
While the monitoring and reporting
requirements for a community of
1,000 are not much different from a
community of 1,000,000, the financial
bases of the two communities are vastly
different and therefore the per capita
charges for water will also be vastly
different.
All of these problems escalate for
isolated communities typical of northern
Canada. Technicians, spare parts,
and treatment chemicals all need to be
flown in to many northern communities.
Unit costs for commodities such
as power, labour or treatment chemicals
are many times higher than in
southern communities. Isolated northern
communities have the doubleedged
sword of higher costs and smaller
resource bases.
For all of these reasons, small communities
are structurally different than
large communities and unique solutions
to water treatment are required.
It is not satisfactory to simply downscale
the water treatment technologies
used in large communities to smaller
sizes. The requirements are different
and therefore the technology selection
criteria are different.
The treatment technology must be
simple to operate. Operators do not
have an in-house engineering staff to
turn to when there is a chemical, electrical
or mechanical upset. A passive
treatment system (a system that does
not require changes to the process to
react to changing raw water conditions)
is often preferred over dynamic
systems. The level of complexity of
instrumentation, controls and/or chemistry
of the treatment chemicals in the
plant should reflect the level of training
and sophistication of the operator.
In many small communities, operators
have obtained only the bare minimum
level of training and experience.
Finally, operators cannot baby-sit their
water treatment plant, since they often
have numerous other responsibilities
in the community, such as grading
roads, maintaining parks, cleaning the
ice at hockey rinks, etc.
Such treatment systems should
minimize on-going operating costs.
While construction and capital costs
are often paid for by senior levels of
government, it is the local community
that must pay operations costs and
therefore operating costs should be the
paramount criteria in selecting a treatment
technology. Technologies that use
large amounts of power, chemicals,
labour or proprietary spare parts
should be avoided.
Slow sand filtration
These issues are not new or unique
to Canada. Agencies such as the
United States Environmental Protection
Agency (USEPA), the World
Health Organization (WHO) and the
United Nations Environmental Program
(UNEP) have all recognized the
special problems associated with water
treatment for small communities.
Each of these agencies has recommended
slow sand filtration as a “Best
Available Technology” for small communities,
based on the technology’s
simplicity, low costs and high efficiency
for removing water-borne pathogens
without the use of pre-treatment chemicals.
Over 200 slow sand filters are
installed across North America, mostly
for small and mid-sized communities.
Conventional slow sand filter
However, conventional slow sand
filtration has several disadvantages
that have limited its application in
recent years. Limitations of conventional slow sand filters include poor removal efficiencies
for organics such as algae, colour and naturally occurring
organic matter, which may lead to downstream disinfection
by-product formation, as well as the operational problems
involved with cleaning the surface of a slow sand filter.

Multi-stage filtration
The Multi-Stage Filter has been designed to provide all
of the benefits of slow sand filtration but with enhancements
to overcome the limitations of conventional slow
sand filtration. Enhancements include pre-ozonation,
roughing filtration and a non-destructive filter cleaning
technique. Granular activated carbon or limestone steps can
also be added if required for unique waters.
The benefits of multi-stage filtration include:
- 33% to 66% TOC removal, and a corresponding decrease
in disinfection by-products formation potential.
- Colour removal.
- Increased turbidity removal efficiency.
- Longer filter runs (2 – 6 month filter runs typical).
- Increased disinfection by ozonation.
- Improvements in taste and odour.
- Iron and manganese removal.
- No manual filter scraping and no sand replacement costs.

North Haven, Maine
The Town of North Haven is an island community,
approximately 20 kilometres off the coast of Maine. The
island has approximately 350 permanent residents, but the
population increases to over 2000 during the summer. The
peak day water demand is 950 m3/day. The island has one
fresh water source with generally good raw water quality.

Treatment technology criteria
Wright-Pierce Engineering of Topsham, Maine, were
engaged by the town to select a treatment technology.
Several criteria were considered in selecting the best technology,
including:
- The technology had to meet the USEPA Surface Water
Treatment Rule and Enhanced Surface Water Treatment
Rule for filtration of giardia, viruses, and cryptosporidium
(based on turbidity), and needed to meet the Disinfection
By-Product Rule for limitations of TOC, THMs and HAAs,
and ozonation by-products.
- Routine delivery of chemicals was difficult due to the
remote location and transportation restrictions on State
Ferries.
- Electricity is generated locally by diesel generators at a
high cost. The water treatment technology had to minimize
power consumption.
- Operational simplicity was essential. Local operators have
other municipal responsibilities and lower certification levels.
- The technology needed to be cost competitive.
- A simple corrosion control method was required due to
the low alkalinity of the water.
Three treatment options were considered and pilot tested,
including, a) conventional slow sand filtration, b) UF
membrane filtration, and c) multi-stage filtration.
Conventional slow sand filtration was pilot tested in
1998 and was observed to meet all of the filtration requirements
of the Surface Water Treatment Rule. However, the
TOC removal efficiency was not sufficient to meet the TOC
removal requirements of the Disinfection By-Product Rule.
Furthermore, since no package plant option exists for a
conventional slow sand filter, this option would involve the
construction of concrete tanks which would be very costly
due to the transportation requirements of concrete.
Ultrafiltration membrane technology was pilot tested in
1999 and was also demonstrated to be effective at removing
colour and TOC and meeting the SWTR. However, this
technology was ultimately not selected due to concerns
about membrane fouling due to the high organic load and
concerns about the long-term expense of system maintenance.
Additionally, the local operators would need to
upgrade their operating certification in order to operate a
membrane plant.
The Multi-Stage Filtration process was piloted in 2000
and was found to be effective for reducing TOC and colour
as well as satisfying all of the other selection criteria.
Finally, the package design of the Multi-Stage Filter was
attractive for transportation and construction on the island.
Plant design
The following design parameters for the Multi-Stage
Filter were used based on the pilot test results:
The normal design flow rate for
slow sand filters is between 0.1 m/hr
and 0.4 m/hr. Several large European
slow sand filtration plants that practise
pretreatment, such as in London and
Zurich, have filtration rates as high as
0.6 m/hr to 0.8 m/hr. A conservative
filtration rate of 0.29 m/hr was chosen
for the North Haven design.
Construction of the plant took place
in the winter of 2003. Four Multi-
Stage Filter tanks were purchased from
MS Filter Inc. of Newmarket, Ontario,
and installed, each with a flow capacity
of 238 m3/day. Each tank consisted
of a roughing filter,
slow sand filter,
and limestone
contactor. The limestone
contactor was
filled with crushed
limestone and is
used to raise the
pH and add alkalinity
that provides
corrosion control
in a simple, passive
design. Water
flows by gravity
through the entire filter and no chemicals
are added to the process.
The ozone system consists of modular
ozone generators, venturi injectors,
two ozone contactors (3.2m H x
0.36m diameter), and appropriate
instrumentation and controls. The
ozone generators create ozone by the
corona discharge method using dried
air. The ozone and air mixture is drawn
into the water line using a venturi
injection system so that the ozone
delivery line is always under vacuum
as a fail-safe against ozone leaks.
Ozone is distributed in the ozone contactor using a mass transfer multiplier
and a perforated plenum. Ozone mixing
is assisted by packing the column
with 2” plastic saddles.
The filter tanks and media were set in place prior to construction of the filter
building, allowing water to flow to
the filters during construction by a
temporary water line. The filters took
approximately one month to ripen
under cold water and low flow conditions,
but were already meeting turbidity
treatment requirements (<1 NTU)
during start-up of the rest of the plant.
The plant was commissioned in
June of 2003 and was producing the
following water quality:
Unlike slow sand filters, Multi-
Stage Filters have a non-destructive
cleaning technique, which means that
the surface is not scraped and sand is
not replaced. The roughing filter is
backwashed to waste and the slow
sand filter is surface washed using a
modified wet-harrow process. Wastewater
is sent out to a holding pond
where it evaporates. Annual wastewater
production is less than 0.1% of
plant capacity. Sludge production is
minimal (< 10 kg/year) since no chemical
coagulants are added to the
process. The length of the filter runs
(time between filter cleanings) is 2 – 3
months. Filter cleaning takes less than
one hour per filter and the filters can
be placed back on line after several
hours. No other maintenance of the filters
is required.
The total cost of the entire water
treatment facility, including the package
plant, filtration and administration
building, design, and administration,
was $US 2,216,747.00. These costs
were likely 25% - 40% higher than
normal due to the unusual costs related
to building a facility on a remote
access island. Annual costs directly
related to the Multi-Stage Filter
(power, labour, building heat, annualized
replacement costs) are < $US
20,000/year or <$0.12/m3 (at average
flow rates).
Robert Abernethy is President of MS
Filter. Contact, e-mail: rabernethy@msfilter.com.
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