BACKGROUND
The chemical process industry, petroleum refining,
utilities, and many other industries, use large quantities
of water for cooling.
There is an increased emphasis being placed upon
the re-use of cooling water by means of cooling towers.
The cooling effect is obtained by the evaporation of a
small fraction of water and heat exchange with the air
passing through the cooling tower. The problems
encountered in cooling systems are not usually with
the equipment, but with the water. As the water evap-
orates, the dissolved solids concentrate. These
impurities in water cause scale and corrosion in the
heat exchange equipment.
PROCESS
There are many variations in cooling towers and heat
exchange design. A common feature is the control of
the water quality with the use of continuous pH and
conductivity measurement while maintaining a given
set of conditions. This is done to further minimize
corrosion and protect the equipment. Continuous
recirculation of the cooling water causes the concen-
tration of the impurities to increase. The relative
concentration of the impurities in the water is
measured by a contacting conductivity sensor, such
as a Model 400 sensor. A conductivity controller initiates
the opening of a blowdown valve when the conductivity
becomes too high. This causes a demand for make-up
water, which is less concentrated in impurities, and
thus lowers the conductivity.
Most of the impurities in cooling water are alkaline,
which is indicated. The alkaline impurities, especially
calcium carbonate, are less soluble at high pH values.
Therefore, a small quantity of sulfuric acid is added to
the circulating water to lower the pH value and thus
prevent the formation of solids (scale). The ideal pH
sensor for this application is the general purpose
Model 3900. The Langelier Index is a factor obtained
from calcium hardness, alkalinity, pH, conductivity,
and temperature, and indicates scaling potential.
For cooling water containing a high level of suspended
solids, a toroidal conductivity sensor such as the
Model 228 and a fouling-resistant pH sensor such as
Model 396P are recommended.
Corrosion and scaling are further minimized by the
addition of chemical scale and corrosion inhibitors.
Inhibitors are fed based upon one of three methods: on
acid demand, on opening the blow down valve, and on
operating the make-up water valve. Inhibitors are fed
on acid demand when the acid pump runs and/or when
the inhibitor pump runs. On opening the blow down
valve, the inhibitor pump adds the inhibitor to another
part of the system and precisely balances the loss of
inhibitor by blowdown.
The warm water and air also produce an ideal environ-
ment for biological growth. To control algae and slime
growth, biocides (i.e., chlorine or bromine) are added
on a time basis, such as a given quantity once per day,
twice per week, once per week, or by one of the above
methods. Chlorine levels can be monitored using the
chlorine sensor Model 499ACL.
Dispersants are added to prevent coagulation or
flocculation of suspended solids (dust, living microor-
ganisms, dead cells, etc.). Dispersants are added in
the same manner as inhibitors.
Ozone treatment is a powerful alternative to chemical
treatment and will reduce operating costs significantly
while increasing safety. Unlike most chemicals, ozone
has a half-life of only 20 minutes and will not be found
in blow down water. The dissolved ozone sensor
Model 499AOZ is intended for continuous measure-
ment of dissolved ozone between 0 and 10 ppm. Use
of ozone treatment has seen a growing interest for
cooling tower control and is a cost-effective solution for
many applications.
Cooling Water Control
Theory
Application Data Sheet
ADS 43-006/rev.D
November 2010