Advantages Water is inexpensive,
non-toxic, and available over most of the earth's surface. Liquid cooling offers higher thermal conductivity than air cooling. Water has unusually high specific heat capacity among commonly available liquids at room temperature and atmospheric pressure allowing efficient heat transfer over distance with low rates of mass transfer. Cooling water may be recycled through a
recirculating system or used in a single-pass
once-through cooling (OTC) system. Water's high
enthalpy of vaporization allows the option of efficient evaporative cooling to remove waste heat in
cooling towers or
cooling ponds. Recirculating systems are
open if they rely upon evaporative cooling or
closed if heat removal is accomplished in
heat exchangers, thus with negligible evaporative loss. A heat exchanger or
condenser may separate
non-contact cooling water from a
fluid being cooled, or
contact cooling water may directly impinge on items like
saw blades where
phase difference allows easy
separation. Environmental regulations emphasize the reduced concentrations of waste products in non-contact cooling water.
Disadvantages Water accelerates the corrosion of metal parts and is a favorable medium for biological growth. Dissolved minerals in natural water supplies are concentrated by evaporation to leave deposits called scale. Cooling water often requires the addition of chemicals to minimize corrosion and insulating deposits of scale and biofouling. Water contains varying amounts of impurities from contact with the atmosphere, soil, and containers. Being both an electrical conductor and a solvent for metal ions and oxygen, water can accelerate corrosion of machinery being cooled. Corrosion reactions proceed more rapidly as temperature increases. Preservation of machinery in the presence of hot water has been improved by addition of
corrosion inhibitors including
zinc,
chromates and
phosphates. The first two have toxicity concerns; and the last has been associated with
eutrophication. Residual concentrations of biocides and corrosion inhibitors are of potential concern for OTC and blowdown from open recirculating cooling water systems. With the exception of machines with short design life, closed recirculating systems require periodic cooling-water treatment or replacement raising similar concern about ultimate disposal of cooling water containing chemicals used with environmental safety assumptions of a closed system.
Biofouling occurs because water is a favorable environment for many life forms. Flow characteristics of recirculating cooling water systems encourage colonization by
sessile organisms using the circulating supply of food,
oxygen and nutrients. Temperatures may become high enough to support
thermophilic populations of organisms such as types of
fungi. Biofouling of heat exchange surfaces can reduce heat transfer rates of the cooling system, and biofouling of cooling towers can alter flow distribution to reduce evaporative cooling rates. Biofouling may also create differential oxygen concentrations increasing corrosion rates. OTC and open recirculating systems are more susceptible to biofouling. Biofouling may be inhibited by temporary habitat modifications. Temperature differences may discourage the establishment of thermophilic populations in intermittently operated facilities, and intentional short-term temperature spikes may periodically kill less tolerant populations.
Biocides have been commonly used to control biofouling where sustained facility operation is required.
Chlorine may be added in the form of
hypochlorite to decrease biofouling in cooling water systems, but is later reduced to
chloride to minimize the toxicity of blowdown or OTC water returned to natural aquatic environments. Hypochlorite is increasingly destructive to wooden cooling towers as pH increases. Chlorinated phenols have been used as biocides or leached from preserved wood in cooling towers. Both hypochlorite and
pentachlorophenol have reduced effectiveness at pH values greater than 8. Non-oxidizing biocides may be more difficult to detoxify prior to release of blowdown or OTC water to natural aquatic environments. Concentrations of
polyphosphates or
phosphonates with zinc and chromates or similar compounds have been maintained in cooling systems to keep heat exchange surfaces clean enough that a film of
gamma iron oxide and
zinc phosphate can inhibit corrosion by passivating anodic and cathodic reaction points. These increase salinity and total dissolved solids, and
phosphorus compounds may provide the limiting essential nutrient for algal growth contributing to biofouling of the cooling system or to eutrophication of natural aquatic environments receiving blowdown or OTC water. Chromates reduce biofouling in addition to effective corrosion inhibition in the cooling water system, but residual toxicity in blowdown or OTC water has encouraged lower chromate concentrations and the use of less-flexible corrosion inhibitors. Blowdown may also contain
chromium leached from cooling towers constructed of wood preserved with
chromated copper arsenate.
Total dissolved solids or TDS (sometimes called filterable residue) is reported as the mass of residue remaining when a measured volume of
filtered water is
evaporated.
Salinity indicates water
density or
conductivity changes caused by dissolved materials. Probability of scale formation increases with increasing total dissolved solids. Solids commonly associated with scale formation are
calcium and
magnesium both as
carbonate and
sulfate. Corrosion rates initially increase with salinity in response to increasing electrical conductivity, but then decrease after reaching a peak as higher levels of salinity decrease dissolved oxygen levels. Some groundwater contains very little oxygen when pumped from wells, but most natural water supplies include dissolved oxygen. Increasing oxygen concentrations accelerate corrosion. Dissolved oxygen approaches saturation levels in cooling towers. It is beneficial in blowdown or OTC water being returned to natural aquatic environments. Water ionizes into
hydronium (H3O+)
cations and
hydroxide (OH−)
anions. The concentration of ionized
hydrogen (as protonated water) in a cooling water system is reported as the
pH level. Low pH values increase the rate of corrosion; high pH values encourage scale formation.
Amphoterism is uncommon among metals used in water cooling systems, but
aluminum corrosion rates increase with pH values above 9.
Galvanic corrosion may be severe in water systems with
copper and aluminum components.
Acid can be added to cooling water systems to prevent scale formation if the pH decrease will offset increased salinity and dissolved solids. == Steam power stations ==