This chapter addresses the needs of both the architectural design team and the mechanical HVAC design
team. Architectural aspects are included because the building envelope must be designed to be suitable
for this high-dew-point application. Some aspects of the envelope design must be approached in a certain way because the
mechanical system cannot solve the problems they cause.
Many owners, designers, and facility operators are under the misconception that a properly designed HVAC
system can clean the air when chloramine odors become an issue and can make condensation issues go away.
This is not the case. If chemicals are offgassing, the source of the problem (water chemistry) must be
addressed. If the building envelope is not designed correctly and appropriately for this application,
there will be condensation and building degradation issues. The HVAC system can influence these issues
either positively or negatively, but will not resolve the issues.
The HVAC system and the water treatment system are critical to the success of the facility. These systems
must all work together to provide the best indoor air and water quality in the facility. If one of these
systems is compromised in any way, the other system will be affected and cannot correct the issue caused
by the shortcomings of the other system.
The owner and design team must put occupant health and safety first, and this requires budgeting for a
suitable building HVAC system and water treatment system. Compromises directly affect aspects of the
facility. Bad air quality, condensation, and building degradation negatively affect the facility’s
economic viability by increasing operating and maintenance costs while possibly reducing patron
memberships. Although most mechanical systems can be applied in any geographic location, some systems or
combination of technology may work better than others.
For both engineers and architects, the key to understanding indoor pools is understanding that this is a
high-dew-point application. The elevated dew point affects every aspect of this facility. This chapter
reviews the implications of this higher dew point, how to calculate loads, and best practices for best
possible occupant comfort and satisfaction.
Like most indoor spaces, a natatorium requires year-round humidity levels between 40 and 60% for
comfort, reasonable energy consumption, and building envelope protection. However, space
temperatures are generally 10 to 15°F warmer in a natatorium than in a
traditional space, and this drives up the dew point. To minimize operating costs, it is
recommended the humidity levels be allowed to go to the high end in summer, only trying to keep
humidity levels lower in winter. The designer must address humidity control, room pressure
control, ventilation requirements for air quality (outdoor and exhaust air), air
distribution, duct design, pool water chemistry, and evaporation rates. A humidity control
system alone will not provide satisfactory results if any of these items are overlooked. (See
Chapter 25 of the 2020 ASHRAE Handbook—HVAC Systems and
Equipment for dehumidifier application and design information.)
Many critical items affect a natatorium’s indoor air quality (IAQ). The design team must
work with all trades associated with the pool to ensure a complete system design is in place for
the best possible air quality. Chloramine reduction and control are critical aspects; source
capture exhaust, secondary disinfection, UV, and other technology to reduce or remove
chloramines are at least as important as the HVAC aspects of the design. The HVAC system must
effectively get air where it is needed. A stratified room or areas that do not get air turnover
will suffer.
When wet, people become more sensitive to relative humidity and experience an evaporative cooling
effect on the skin surface. Fluctuations in relative humidity outside the 50 to 60% range are
not recommended. Sustained levels above 60% can promote factors that reduce indoor air quality.
Relative humidity levels below 50% significantly increase the facility’s energy
consumption. For swimmers, 50 to 60% rh limits evaporation and corresponding heat loss from the
body and is comfortable without being extreme. Higher relative humidity levels can be
destructive to building components. Mold and mildew can attack wall, floor, and ceiling
coverings, and condensation can degrade many building materials. In the worst case, the roof
structure could fail because of corrosion from water condensing on the structure
There are three approaches to humidity control for indoor pools: compressorized, chilled-water
coil and ventilation. All are viable options, but must be fully evaluated to understand what
they will provide for year-round control. Geography and patron expectations will factor
significantly in on whether or not a ventilation only approach might be considered. Ventilation
supplemented with a compressor or chilled water coil are also sometimes considered. See Chapter
25 of the 2020 ASHRAE Handbook—HVAC Systems and
Equipment for
details on the compressorized dehumidifiers available.
The relation between temperature and humidity determines evaporation from the pool water surface
and the space’s condensation dew point. To minimize evaporation and operating costs, the
air temperature should be kept as warm as is practical, ideally at or above the water
temperature, with a maximum of 86°F db, which is generally understood to the
maximum for human comfort. All surfaces in the space must be maintained above the space dew
point to prevent condensation from developing that could damage the building and allow growth of
mold and fungi.
A pool’s indoor design dew point typically ranges from 62 to 69°F for
ambient conditions of 82 to 84°F and 50 to 60% rh. In comparison, a typical
space in winter might be 70°F at 40% rh with a 45°F dew point.
In summer, the 62 to 69°F space dew point is not a condensation concern. The
vapor pressure outdoors might be a little higher than it is indoors, but if the vapor migrates
through the building envelope, it is too warm for condensation to occur.
The serious concern is in winter, when the indoor vapor pressure is significantly higher than it
is outdoors and there is a push from indoors to outdoors to try to equalize pressure. If the
vapor is allowed to migrate through the wall, it will encounter a temperature at or below dew
point. Condensation or freezing will result, and the structure’s integrity will be
negatively affected.
A natatorium must always be maintained with a negative pressure at all elevations to prevent
moist air from migrating through the exterior walls and to prevent moisture and odors from
migrating through adjacent walls to other parts of the building. (Note that a significant
negative space pressure will not reduce or affect vapor migration to the outdoors in winter.) A
positively pressurized indoor pool can accelerate building damage by pushing the
high-moisture-content air into the building envelope, where it can condense.
One way to maintain negative pressure is balancing ventilation air and exhaust air. Another
approach is to maintain the differential pressures between the natatorium and the outdoors, and
the natatorium and an adjacent space, at set values.
Regardless of the control method chosen, accurate calculation of the amount of infiltration to
the natatorium is essential. If the infiltration rate is underestimated, the space may not be
able to achieve a negative pressure without an excessive amount of exhaust. To keep operational
costs for ventilation reasonable, the infiltration rate and performance of the air barrier are
very important. If the air barrier is not continuous, the amount of exhaust air increases.
Experience has shown that the offset between supply and exhaust air can sometimes reach 20 to
25% in poorly constructed natatoriums. Treating all air that will eventually be exhausted is a
continuous energy penalty, so efforts to minimize this will reduce operating costs.
To properly design the air barrier, there must be coordination and discussion with the architect,
who needs to detail and specify the correct sealants and joints for a continuous air barrier.
Ideally, the architect should clearly identify the location of the natatorium air barrier on the
construction documents.
The entire perimeter of the designated air barrier should be reviewed to ensure that ductwork
that crosses the air barrier does not contribute to the infiltration rate. Since most spaces
adjacent to the natatorium are on a nighttime control cycle, with the outdoor air damper closed
and the HVAC unit off, ducts that cross the air barrier can cause excessive infiltration during
the night cycle. Infiltration of adjacent space air into the natatorium is often overlooked
during design and construction and can lead to excessive energy costs and freezing conditions in
the adjacent spaces.
The architect should also include a whole-room air leakage test to ensure that the natatorium
leaks at a prescribed rate. (A whole-room leakage test is the same as a whole-building leakage
test but for just the natatorium.) The leakage rate and the test procedure should be discussed
between the architect and the HVAC engineer. ASTM Standard E779 is
an example of a whole-building leakage test that has been successfully used. Once the leakage
rate has been established, the engineer will know precisely how much offset will be needed to
achieve the negative space. All modes of operation that vary the amounts of outdoor and/or
exhaust air should be evaluated as part of the space pressure test to determine the correct
amount of exhaust air to maintain a negative space pressure. If the building HVAC equipment
other than the natatorium includes economizer operation, this should be in operation and its
effect on natatorium pressure evaluated. Any mode of operation that varies the amount of
ventilation and/or exhaust air (e.g., event mode, night setback) must be tested and evaluated so
a negative pressure is present at all times in the natatorium.
This negative space needs to take stack effect into consideration. During cold outdoor
temperatures, the bottom half of the natatorium is automatically in a negative pressure due to
the stack effect. The challenge is to also have the top of the natatorium negative to the
outdoors when it is cold outside. The colder it is and the taller the natatorium ceiling, the
greater the negative pressure will be at the deck. Door opening forces could exceed ICB 1010.1.3
(Door opening force) and a vestibule could be required. Establishing door opening force should
be coordinated with the architect. In some cases, the locker room can be designed as the
vestibule. Vestibules effectively cut the door opening force in half. For specifics on stack
effect, see Chapter 4.
Ventilation air should be calculated as the minimum amount recommended in the current ASHRAE
Standard 62.1. The effect of these amounts must be reviewed to
compensate for any additional moisture being introduced to the space and any effects on
increased evaporation, human comfort, and space operating costs. How the ventilation air is
introduced to the space must be evaluated to ensure the temperature is above the space dew point
to prevent fogging and condensation.
Exhaust air must always be in amounts greater than the ventilation air to maintain negative
pressure, but the amount by which exhaust must exceed ventilation depends on building tightness.
Strategic exhaust has a positive influence on IAQ. Low exhaust air at or near the surface of the
pool water surface should also be evaluated to assist in evacuating any chloramines from the
space. This exhaust air is rich in energy, and heat recovery is highly recommended to help
reduce operating costs.
Location of Mechanical Equipment
The location of mechanical and electrical equipment rooms affects the degree of sound attenuation
treatment required.
Condensation (water vapor changing from gaseous to liquid state) is the major issue for indoor
swimming pools. Both visible and concealed condensation must be prevented. To understand how this
happens, a basic familiarity with psychometrics is necessary. The following five terms are commonly
encountered when dealing with a psychometric chart (Figure 1):
-
Dry bulb (db) temperature is the sensible
temperature of the air (i.e., what can be read from a common thermometer).
-
Wet-bulb (wb) temperature is taken by
surrounding the sensor with a wet wick and measuring the temperature as the water
evaporates from the wick. As the water evaporates from the wick, it draws heat required
for evaporation from the thermometer bulb, cooling the thermometer in proportion to the
amount of evaporation.
-
Dew-point (dp) temperature is the temperature
at which moisture condenses and forms visible water. The colder the air, the less
moisture it can hold.
-
Relative humidity (rh) expresses the moisture
content of air as a percentage of saturation.
-
Specific humidity is the weight
of the moisture in the air compared to the weight of air. The weight
is measured in grains, and there are 7000 grains in a pound of air.
A complete understanding of dew point is important. Figure
2 shows three stages of moisture condensation from the air:
-
In Figure
2A, the surface of the glass is clear. This means the glass temperature is above
the dew-point temperature.
-
In Figure
2B, water is starting to form on the surface of the glass, so the glass
temperature is at the dew point.
-
In Figure
2C, the glass surface is below the dew point and condensate has formed on the
surface.
Without proper understanding and control of dew point and condensation, moisture can form on the
indoor and outdoor surfaces of the structure. Figure
3 shows examples of moisture formation and the results.
In a typical indoor pool, indoor temperature ranges from 78 to 86°F db. Figure 4 shows three plotted curves
with values derived from the psychometric chart. This graph allows plotting the dew-point
temperature at indoor temperatures of 82°F db, 84°F db, and
86°F db and relative humidity values from 30 to 60%. An example is shown at
84°F db and 50% rh, showing that the dew point is 64°F.
This example shows that all surfaces inside the pool room must be kept above the dew-point
temperature of 64°F to prevent visible condensation. Common design practice adds
5°F to this temperature as a safety factor.
The architect’s responsibility is to design wall and ceiling components with this surface
temperature in mind, to assist the HVAC design engineer in preventing moisture from forming inside
the structure.
Equation (1) calculates
the surface temperature of a structural component:
where
| Ts = surface temperature |
| Ti = indoor space temperature |
| K = indoor air film coefficient; 0.68 for vertical surface, 0.95
for horizontal roof or skylight, 0.76 for 45° roof or skylight |
| R = total R-value of structural component |
| To = outdoor temperature |
To apply Equation (1)
to a window, the published window U-factor (see Chapter 15 of the 2021 ASHRAE
Handbook—Fundamentals) must be converted to the required R-value; for
example,
In this example, the indoor temperature is 84°F db and the outdoor temperature is
0°F db. This gives a 61.2°F surface temperature on the window. If
the indoor space is at 50% rh, the dew point would be 64°F, which would lead to
condensation on the glass surface unless the window glass is heated above the dew point (Figure
5).
Figure
6 plots three indoor conditions and several window U-values at different outdoor
temperatures: 25°F, 0°F, and –25°F. The
left vertical axis shows the relative humidity at which condensation will occur: whenever the indoor
relative humidity exceeds these values at the given outdoor condition, condensation will form on the
window surface unless the window surface is warmed above the indoor dew point.
Outdoor air ventilation rates (as prescribed by ASHRAE Standard 62.1)
can be a major portion of the total load, depending on the geographic location. The latent load
(dehumidification and humidification) and energy used to maintain relative humidity within
prescribed limits are also concerns. Humidity must be maintained at proper levels to prevent
mold and mildew growth and for acceptable indoor air quality and comfort.
Loads for a natatorium include heat gains and losses from outdoor air, lighting, walls, roof, and
glass. Internal latent loads are generally from people and evaporation. Evaporation loads in
pools and spas are significant relative to other load elements and may vary widely depending on
pool/water features, areas of water and wet deck, water temperature, and activity level in the
pool.
Evaporation. The rate of evaporation can be estimated
from empirical Equation (2). This equation is valid for pools at normal activity
levels, allowing for splashing and a limited area of wetted deck. Other pool uses may have more
or less evaporation (Smith et al. 1993).
where
| wp = evaporation of water, lb/h |
| A = area of pool surface, ft2 |
| Y = latent heat required to change water to vapor at surface
water temperature, Btu/lb |
| pw = saturation vapor pressure taken at surface
water temperature, in. Hg |
| pa = saturation pressure at room air dew point,
in. Hg
|
| V = air velocity over water surface, fpm |
Units for the constant 95 are
Btu/(h · ft2 · in. Hg). Units
for the constant 0.425 are
Btu · min/(h · ft3 · in.
Hg).
Equation (2) may be
modified by multiplying it by an activity factor Fa to
alter the estimate of evaporation rate based on the level of activity supported. For Y values of about 1000 Btu/lb and V values ranging from 10 to 30 fpm, Equation (2) can be reduced to
Table
1 lists activity factors that should be applied to the areas of specific features, and
not to the entire wetted area.
The effectiveness of controlling the natatorium environment depends on correct estimation of
water evaporation rates. Applying the correct activity factors is extremely important in
determining water evaporation rates. The difference in peak evaporation rates between private
pools and active public pools of comparable size may be more than 100%.
Actual operating temperatures and relative humidity conditions should be established before
design. How the area will be used usually dictates design (Table 2).
Air temperatures in public and institutional pools are recommended to be maintained 2 to
4°F above the water temperature (but not above the comfort threshold of
86°F) for energy conservation through reduced evaporation and to avoid chill
effects on swimmers.
Competition pools that host swim meets have two distinct operating profiles: (1) swim meets and
(2) normal occupancy. It is recommended that both be fully modeled to evaluate the
facility’s needs. Although swim meets tend to be infrequent, the loads during meets are
often considerably higher than during normal operations. To model the swim meet load accurately,
it is recommended that the designer know the number of spectators, number of swimmers on the
deck, and operating conditions required during the meets. The operator may request a peak
relative humidity of 55%, which has a significant effect on total loads. A system designed for
swim meet loads should also be designed to operate for considerable portions of the year at part
loads. Depending on the layout of the space and location of the spectator gallery, it might be
beneficial to provide a separate microclimate to that area, with a separate dedicated unit.
Water parks and water feature (slides, spray cannons, arches, etc.) loads are not fully covered
by this chapter. Use caution when evaluating the evaporation from water features/toys installed
in natatoriums. Applying higher activity factors when evaluating the evaporation rates at water
parks and water features/toys is only one component of accounting for this evaporation.
Currently the design professional must rely on experience and professional judgment when
calculating the evaporation in water parks and from the water features/toys because
manufacturers of these items do not publish evaporation rates. Since these loads are not
guaranteed to be accurate, the designer is encouraged to manage space condition expectations by
disclosing that the loads are estimates and the space conditions may fluctuate from the design.
It is recommended that the dehumidification load generated by each water feature be calculated
individually. The water toys’ manufacturers should be contacted to provide specifications
related to the pattern and size of the sheet of water that is generated by each water
feature/toy to allow for proper load determination. The wet area created by the water
toy/feature must be included as wet deck when calculating the ventilation air required for the
space as well as the wetted surface for the evaporation load. Because of the concentrated nature
of the loads in these facilities, it is recommended that more supply air and outdoor air be used
in these facilities compared to what is recommended for traditional pools.
Air Quality. Outdoor air ventilation rates prescribed
by ASHRAE Standard 62.1 are intended to provide acceptable air
quality conditions for the average pool (where chlorine is used for primary disinfection). The
ventilation requirement may be excessive for private pools and installations with low use, and
may also prove inadequate for high-occupancy public or water park installations.
Air quality problems in pools and spas are often caused by water quality problems, so simply
increasing ventilation rates may prove both expensive and ineffective. Water quality conditions
are a direct function of pool use and the type and effectiveness of water disinfection used.
It is recommended that the ASHRAE climate data included with Chapter 14 of the 2021 ASHRAE Handbook—Fundamentals (full data are provided
with the
PDF download and Handbook Online versions of the chapter) be used when calculating the effects
of ventilation air on the natatorium’s latent load, as mentioned in ASHRAE Standard 62.1.
Because indoor pools usually have high ceilings, temperature stratification and stack effect (see
Chapter 16 of the 2021 ASHRAE Handbook—Fundamentals) can have
a detrimental effect on indoor air quality. Careful duct layout is necessary to ensure that the
space receives proper air changes and homogeneous air quality throughout. Some air movement at
the deck and pool water level is essential to ensure acceptable air quality. Complaints from
swimmers indicate that the greatest chloramine (see the section on Pool Water Chemistry)
concentrations occur at the water surface. Children are especially vulnerable to the ill effects
of chloramine inhalation.
Pool and spa areas should be maintained at a negative pressure of 0.05 to 0.15 in. of
water relative to the outdoors and adjacent areas of the building to prevent moisture
and chloramine odor migration. Active methods of pressure control may prove more effective than
static balancing and may be necessary where outdoor air is used as a part of an active humidity
control strategy. Openings from the pool to other areas should be minimized and controlled.
Passageways should be equipped with doors with automatic closers and sweeps to inhibit migration
of moisture and air.
Exhaust air from pools is rich in moisture and may contain high levels of corrosive chloramine
compounds. Exhaust air intake grilles should be located as close as possible to the warmest body
of water in the facility. Warmer and more agitated waters offgas chemicals at higher rates
compared to traditional pools. This also allows body oils to become airborne. Ideally, these
pollutants should be removed from close to the source before they have a chance to diffuse and
negatively affect air quality. Installations with intakes directly above whirlpools have
resulted in the best air quality.
Air Delivery Rates. Most codes require a minimum of
six air changes per hour, except where mechanical cooling is used. This rate may prove
inadequate for some occupancy and use. Note: the term “air
changes” here refers to the number of air exchanges in the space, not the amount of air
being exchanged with new outdoor ventilation air.
Where mechanical dehumidification is provided, air delivery rates should be established to
maintain appropriate conditions of temperature and humidity. The following rates are typically
desired:
Ventilation air is the amount of air required by local codes to be introduced during occupied
hours to maintain a healthy environment for the occupants. ASHRAE Standard 62.1 is used by most local code departments to determine this
minimum amount of outdoor air. When outdoor air is also used for climate control, the
design team must understand that ventilation air and climate control air are interchangeable
terms for that project.
Climate control outdoor air is used to control the
humidity and temperature in the space. This type of design is usually referred to as 100% outdoor air systems (i.e., the maximum amount of
outdoor air that the fan can supply from the mechanical piece of equipment to the space is
100%). A detailed evaluation of the annual bin weather conditions of the outdoor air must be
developed for the natatorium’s specific geographical location. The annual bin profile
analysis will help determine if climate control outdoor air is viable for space condition
control and how much heating and cooling might be required to maintain space conditions within
acceptable ranges. A well-designed system will operate between the code-required minimum outdoor
air levels and 100% outdoor air while always trying to use the least amount of outdoor air to
try to minimize operating costs. Heat recovery is strongly recommended to help keep the
operating costs to a minimum.
The indoor pool’s moisture load needs to be calculated first to establish an accurate
system load to maintain the desired space humidity from all moisture-generating items (e.g.,
water surfaces, spectators, swimmers, water toys). Once the moisture load is established, the
amount of outdoor air required to remove this moisture can be calculated based on the ASHRAE
weather data for the project location (see the climate data tables download accompanying Chapter
14 of the 2021 ASHRAE Handbook—Fundamentals). The
amount of
sensible heat and cooling can also be calculated to provide room-neutral air to the space.
Varying the amount of climate control outdoor air (while never dropping below the code-required
ventilation outdoor air requirements) during seasonal changes can help reduce overdrying the
air. Overdrying can increase evaporation loads and greater chemical requirements, adding to the
facility’s operating costs.
Air Distribution Effectiveness and
Duct Design
Proper duct design and installation in a natatorium is critical. Failure to effectively deliver
air where needed will result in air quality problems, condensation, stratification, and poor
equipment performance. Ductwork that fails to deliver airflow into the breathing zone at the
pool deck level and water surface, for example, will lead to air quality problems in those
areas. The following duct construction practices apply to indoor pools:
-
Deliver air into the breathing zone at the deck. ASHRAE Standard 62.1 defines the breathing zone as the area
between 3 and 72 in. from the floor level. The best quality air in the
facility is what is delivered from the supply duct. That air must get to where the
patrons are to ensure they are breathing the best possible quality air.
-
Supply air should be directed against envelope surfaces prone to condensation (glass
and doors). Air movement over the pool water surface must not exceed 30
fpm (as per the evaporation rate wp in Equation [2]). If
air movement over the water surface is increased from the standard 30 fpm to
125 fpm, the evaporation will increase by approximately 30%. Air that
moves across the water surface is best handled by a source-capture-type exhaust
system. Evaporation from the water surface should be evaluated using Equation (2).
-
Return air inlets should be located to recover warm, humid air and return it to the
air handler system for treatment, to prevent supply air from short-circuiting and to
minimize recirculation of chloramines. It is recommended that return air inlets be
located both high and low. This helps prevent air stratification and ensure that
incoming ventilation air reaches the breathing zone, as recommended in ASHRAE Standard 62.1.
-
Exhaust air inlets should be located to maximize capture effectiveness and minimize
recirculation of chloramines. Exhausting from directly above whirlpools is also
desirable. Exhaust air should be taken directly to the outdoors, through heat
recovery devices when provided.
-
Source capture exhaust (i.e., exhaust air
taken as close as possible to the water surface and exhausted to the outdoors) could
be part of the climate control equipment or an independent piece of equipment. If
the latter, it must be coordinated with the climate control equipment operation.
-
Duct materials and hardware must be resistant to chemical corrosion from the pool
atmosphere. Stainless steels, even the 316 series, are readily attacked by chlorides
and are prone to pitting. They require treatment to adequately perform in a
natatorium environment. Galvanized steel and aluminum sheet metal may be used for
exposed duct systems. If galvanized duct is used, steps should be taken to
adequately protect the metal from corrosion. It is recommended that, at a minimum,
the galvanized ducts be properly prepared and painted with epoxy-based or other
durable paint suitable to protect metal surfaces in a pool environment. Note that
galvannealed ductwork is easier to weld and paint than hot-dip galvanized, but
galvannealed is more susceptible to corrosion if left bare. Certain types of fabric
duct (airtight) with appropriate grilles sewn in are also a good choice. Buried
ductwork should be constructed from nonmetallic fiberglass-reinforced or PVC
materials because of the more demanding environment. Proper means of water drainage
in the duct must be considered when ductwork is buried.
-
Grilles, registers, and diffusers should be constructed from aluminum. They should be
selected for low static pressure loss and for appropriate throws for proper air
distribution.
-
Filtration should be selected to provide 45 to 65% efficiencies (as defined in ASHRAE
Standard 52.1) and be installed in locations selected to
prevent condensation in the filter bank. Filter media and support materials should
be resistant to moisture degradation.
-
Fiberglass duct liner should not be used. Where condensation may occur, the
insulation must be applied to the duct exterior.
-
Air systems should be designed for noise levels listed in Table 1 of Chapter 48
(NC 45 to 50); however, the room wall, floor, and ceiling surfaces should be
evaluated for their reverberation times and speech intelligibility.
An indoor pool is a special-application structure and requires care to ensure the entire
structure is suitable for a high-dew-point application. There must be
-
Enough insulation that no exterior wall or roof surface ever falls below the space
dew-point temperature in cold weather.
-
Effective vapor migration protections to ensure moisture from the space is prevented
from migrating into any build sections (walls, roofs, joints where they meet). A
vapor retarder analysis (as in Figure 10 in Chapter 27 of the 2021 ASHRAE
Handbook—Fundamentals) should be prepared.
Failure
to install an effective vapor retarder results in condensation forming in the
structure, and potentially serious envelope damage.
-
Complete elimination of thermal bridging. Window and door frames must be thermally
broken.
Figure
7 shows where the vapor retarder should be located in a wall for an indoor pool
application. The vapor retarder must be on the warm side of the dew point. The entire pool
enclosure (walls and ceilings) must have a vapor retarder in the correct location. Where walls
join the roof or floor meet, it is especially vital to ensure there is no breach in the vapor
barrier.
A properly located and installed vapor retarder is the only way to protect a structure from vapor
migration and the ensuing moisture damage.
Condensation forms on exterior windows when the outdoor temperature drops below the pool
room’s dew point (typically between 62 and 70°F). The design goal is to
keep the surface temperature of the glass and the window frames at least 3 to
5°F above the pool room’s dew point. Windows must allow unobstructed air
movement on indoor surfaces, and thermal break frames should be used to raise the window’s
indoor temperature. Avoid recessed windows and protruding window frames. Skylights are
especially vulnerable and require attention to control condensation. Wall and roof vapor
retarder designs should be carefully reviewed, especially at wall-to-wall and wall-to-roof
junctures and at window, door, skylight, and duct penetrations.
Exterior windows and doors are primary condensation concerns, so it is extremely important that
supply air is focused there. Warm air from the dehumidifier keeps the window surface temperature
above the dew-point temperature, which ensures that windows and exterior doors remain
condensation free.
Exterior windows, exterior surfaces, and other condensation-prone areas should be blanketed with
supply air (Figure
8). A good rule of thumb is 3 to 5 cfm per square foot of exterior glass.
Select grilles, registers, and diffusers that deliver the required throw distance, and the
specified volumetric flow rating.
Pool Water Chemistry and Air Quality
Failure to maintain proper chemistry in the pool water causes serious air quality problems and
deterioration of mechanical systems and building components. Water treatment equipment and
chemicals should be located in a separate, dedicated, well-ventilated space that is under
negative pressure. Pool water treatment consists of primary disinfection, pH control, water
filtration and purging, and water heating. For further information, see Kowalsky (1990).
Air quality problems are usually caused by the reaction of chlorine with biological wastes, and
particularly with ammonia, which is a by-product of the breakdown of urine and perspiration.
Chlorine reacts with these wastes, creating chloramines (monochloramine, dichloramine, and
nitrogen trichloride) that are commonly measured as combined chlorine. Adding chemicals to pool
water increases total contaminant levels. In high-occupancy pools, water contaminant levels can
double in a single day of operation.
Chlorine’s efficiency at reducing ammonia is affected by several factors, including water
temperature, water pH, total chlorine concentration, and level of dissolved solids in the water.
Because of their higher operating temperature and higher ratio of occupancy per unit water
volume, spas produce greater quantities of air contaminants than pools.
The following measures have demonstrated a potential to reduce chloramine concentrations in the
air and water; before implementing any of these steps, however, be sure to confirm with local
codes that the measures are acceptable.
-
Ozonation. In low concentrations, ozone
can substantially reduce the concentration of combined chlorine in the water. In
high concentrations, ozone can replace chlorine as the primary disinfection process;
however, ozone cannot remain at sufficient residual levels in the water to maintain
a latent biocidal effect, so chlorine must be kept as a residual process at
concentrations of 0.5 to 1.5 ppm.
-
Water exchange rates. High concentrations
of dissolved solids in water directly contribute to high combined chlorine
(chloramine) levels. Adequate water exchange rates are necessary to prevent build-up
of biological wastes and their oxidized components in pool and spa water.
Conductivity measurement is an effective method to control the exchange rate of
water in pools and spas to effectively maintain water quality and minimize water
use. In high-occupancy pools, heat recovery may prove useful in reducing water
heating energy requirements.
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Medium-pressure UV. Using medium-pressure
UV lamps for water treatment can reduce the amount of chloramines, and should be
evaluated during design. Medium-pressure UV can replace chlorine as the primary
disinfection process; however, it does not remain at sufficient residual levels in
the water to maintain a latent biocidal effect. Consequently, chlorine is required
as a residual process at concentrations of 0.5 to 1.5 ppm.
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Secondary disinfectants. These can reduce
trichloramine levels.
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Swimmer showers. Requiring each swimmer to
shower before entering the water helps reduce the amount of body oils released into
the water, thereby reducing the amount of chloramines generated.
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Bathroom breaks. Facilities that require
all swimmers to exit the pool every hour and visit the restrooms dramatically reduce
the amount of urine introduced into the pool.
Natatoriums can be a major energy
burden on facilities, so they represent a significant opportunity for energy conservation and
recovery. ASHRAE Standard 90.1 offers some recommendations. Several
design solutions are possible using both dehumidification and ventilation strategies. When
evaluating a system, the seasonal space conditions and energy consumed by all elements should be
considered, including primary heating and cooling systems, fan motors, water heaters, and pumps.
Operating conditions factor significantly in the total energy requirements of a natatorium.
Although occupant comfort is a primary concern, the effects of low space temperatures and
relative humidity levels below 50% (especially in winter) should be discussed with the
owner/operator:
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Lower room air temperature or lower relative humidity increases evaporation from the
pools, thus increasing dehumidification requirements and increasing pool water
heating costs
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Warmer water temperatures increase evaporation from the pools, thus increasing the
dehumidification requirements and increasing pool water heating costs
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Matching equipment staging capabilities to occupied/unoccupied, consistent, or
seasonal activity level changes can also reduce energy operating costs
It is recommended to model the space on both a summer and winter design day to establish whether
higher summertime indoor relative humidity level is beneficial to reducing equipment size and
operating costs.
Because these facilities require considerable air movement and the supply fans operate 24/7/365,
fans and equipment that uses less fan energy lead to considerable energy savings over the
equipment life.
These facilities require outdoor and exhaust air. This gives the opportunity for energy recovery
from the exhaust air to preheat outdoor air. The economics of a heat recovery decision should be
always reviewed, regardless of the facility location: these facilities have warm indoor
conditions and show good paybacks for energy recovery, even in warmer climates. A detailed
evaluation of the heat exchange process must be done to ensure no condensation develops in the
energy recovery device so, in cold climates, ice does not develop and damage equipment or
develop an imbalance of airflow.
Compressorized systems can optionally heat pool water with compressor waste heat. The economics
of this option should always be reviewed: the heating contributions can be significant and have
a dramatic return on investment (ROI).
Natatoriums with fixed outdoor air ventilation rates without dehumidification generally have
seasonally fluctuating space temperature and humidity levels. Systems designed to provide
minimum ventilation rates without dehumidification are unable to maintain relative humidity
conditions within prescribed limits, and may facilitate mold and mildew growth and be unable to
provide acceptable IAQ. Peak dehumidification loads vary with activity levels and during the
cooling season, when ventilation air becomes an additional dehumidification load to the space.
Automated controls should be used to reduce large fluctuations in temperature and humidity.
Examples include
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Staging of heating, cooling, and dehumidification equipment to match the varying
occupant or seasonal loads
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Staging of exhaust and ventilation air to match
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Building negative pressure control
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Energy recovery from
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Exhaust air
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Condenser heat recovery
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Chlorine usage based on water and air readings
The following items should be addressed when evaluating and designing a system for an indoor pool
climate control system. This list is a minimum, and additional items can be added by the design
team.
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With design team and owner/operators, identify (1) indoor space temperature, (2)
water temperature, and (3) design relative humidity levels for both summer and
winter.
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Obtain minimum R and U values from architect to determine minimum surface temperature
for condensation.
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Include a proper vapor retarder and install it correctly with no breaks.
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Determine correct amount of ventilation air required for proper IAQ and to meet local
code requirements.
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Determine correct amount of exhaust air to provide negative building pressure.
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Evaluate whether a source capture exhaust system is needed.
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Evaluate outdoor air/exhaust air energy recovery systems.
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Use correct dehumidification weather data to determine moisture load from the
ventilation air.
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Total all moisture/latent loads from (1) people, (2) ventilation air, and (3) water
surface.
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Total all sensible loads from (1) building envelope, (2) people, (3) ventilation air,
(4) lighting, and (5) other sources.
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Select equipment to meet both sensible and latent peak loads.
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Design air distribution system to deliver air into the breathing zone and prevent air
stratification and visible condensation.
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Properly commission equipment and building.
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Include a quarterly equipment maintenance contract as part of operating expense.