Testing of the CTS Treatment System Proves Reliable for Cooling Tower Water
In the April 2001 issue of Water Quality Products,associates of TCET presented a new method using ozone to treat cooling tower water. Cooling Treatment Systems, Inc. (CTS) of Englewood, Colo., has adapted this method to produce a water treatment system it now is marketing for cooling towers. CTS submitted this new technology to TCET for testing. The results of these tests are presented here.The Center for Environmental Technology (TCET) at Pierce
College, Woodland Hills, Calif., is engaged in the development and testing of
new environmental technologies. In the April 2001 issue of Water Quality
Products,1,2 associates of TCET presented a new method using ozone to treat
cooling tower water. Cooling Treatment Systems, Inc. (CTS) of Englewood, Colo.,
has adapted this method to produce a water treatment system it now is marketing
for cooling towers. CTS submitted this new technology to TCET for testing. The
results of these tests are presented here.
How the CTS System Works
The CTS system consists of two sidestream components. The first
treats water with ozone while the second removes particles from system water.
The ozone generator consists of a pair of 33-inch
ultraviolet (UV) (185 nm) lamps, each centered in a 2-inch-diameter stainless
steel tube cooled by a water jacket. Oxygen from an AirSep AS12 is passed
through the tubes at a rate of 15 scfh per tube. Measured on a BMT model 964 UV
spectrophotometer, each tube produced ozone at the rate of 2.5 grams/hour for a
total ozone output of 5 grams/hour for both tubes.
This is considerably less ozone than is produced by other
systems now on the market. According to CTS, this small amount is effective
because its High Shear Mixer (patent pending) is efficient. All water treatment
is accomplished within the confines of the mixer thus eliminating the need to
develop and sustain an ozone residual in the sump as required by other systems.
Water flows through the treatment loop at a rate of 43 gpm
with ozone added to the water via a venturi injector located immediately
upstream of the mixer. Treated water exiting the mixer is returned to the top
of the tower where the ozone is removed by air stripping as the water cascades
over fill elements. Since ozone has been removed from the sump water before it
is delivered to the chiller, there is no concern that ozone will corrode the
chiller or other components of the cooling loop.
Particle removal is accomplished by a second sidestream loop
with a centrifugal separator designed by CTS. This separator is modeled after
designs used in the paper and pulp industry. It is a common assumption that a
centrifugal separator is not appropriate for treatment of cooling tower waters
since good water quality requires removal of particles to micron size or less.3
Manufacturer claims for common centrifugal separators report minimum size
limits of 40 to 74 µ for particles that can be removed unless they are
composed of particularly dense materials not commonly found in cooling
towers.5? Therefore, it is interesting that the CTS system uses a
centrifugal separator rather than a sand filter for particle removal.
Testing the System
The CTS treatment system was tested on a 100-ton BAC cooling
tower with a York TurboPak Liquid Chilling Unit serving the performing arts
building at Pierce College. The mild California climate and the hot lighting of
the theater require that this building be air conditioned throughout the year.
From its installation in the 1970s until three years ago, a commercial chemical
treatment company maintained this tower. In 2000, it was dedicated to ozone
research by TCET and has been treated only with ozone since. Within two months
after ozone treatment began, both the tower and chiller had shed considerable
scale, the T dropped and the condenser amp draw was reduced by 35
percent. The following summer, the chiller did not suffer shutdown due to
thermal overload, a problem that was common in previous years. This period of
stable operation provides a baseline against which to evaluate any changes in
operating parameters that may occur after installation of the CTS system.
In January 2003, the tower sump was drained, cleaned and
refilled with city water and the CTS system was then installed. As of
publication of this article, it has been in operation for six months. For the
first three days after installation, the CTS ozone system was run continuously
and from 10:00 a.m. to 4:00 p.m. (six hrs/day) thereafter. The particle removal
system (centrifugal separator) has been operating continuously since startup.
Water chemistry and chiller performance T and condenser amps) were
monitored three times weekly during this period. After six months of operation,
there has been no detectable effect on chiller performance when compared to the
equivalent period before installation of the CTS unit. (See Table 1.)
Scaling and Corrosion
Ozone is incompatible with the chemicals commonly used for
water treatment and generally is used without additional chemicals. This has
led to concerns that the benefits provided by ozone for microbial control may,
in the absence of additional chemical treatment, be countered by increased
potential for corrosion or scaling. Though there are companies selling
ozone-compatible chemicals for water treatment, the ozone studies at TCET have
used only ozone without any other chemical additives.
The findings show that if the sump water is maintained at a
pH of about 8.4, neither corrosion nor scaling occurs. At this pH, conditions
are out of the corrosion range for the metals commonly used in cooling systems
and favors the formation of bicarbonate (HCO3-) over carbonate (CO3-2) ion
(Figure 1). Calcium bicarbonate is orders of magnitude more soluble than
calcium carbonate; therefore, no scale forms under normal operating conditions.
The pH of the makeup water at the site varies from 7.8 to 8.1. To maintain the
desired pH of 8.4, the system is set to blow down at the conductivity value
obtained when sump water reaches the desired pH. Depending on seasonal water
quality, this usually results in 2.0 to 3.5 cycles of concentration.
Corrosion is minimized by a combination of two factors.
First, by maintaining a pH of 8.4, the water is out of the corrosion range
indicated by the Langalier Saturation Index, Ryznor's Index and others used to
detect corrosive conditions. Second, since the ozone is stripped out of the
water before it is returned to the sump and chiller, there is no contact
between ozone and potential corrosive sites in the system. Corrosion coupons
installed in May 2002 have been in place throughout the six-month period of CTS
system operation. As Table 2 illustrates, corrosion rates were minimal.
The small amount of ozone generated by the CTS system
produced excellent bacterial control. On day three (Jan. 4, 2003) of operation,
qualitative bacteria tests using a Hach paddle test were unable to detect
bacteria (Figure 2). Regular testing revealed bacterial levels have remained
low or undetectable since. On occasion, since there is no ozone residual in the
sump, slight growths of algae occurred on submerged surfaces receiving sunlight.
This is effectively eliminated by the addition of a single 3-inch chlorine
tablet to the sump every several months as needed. This is consistent with the
practice of rotating biocides to prevent development of bacterial resistance.3
To date, no algal growth has occurred on fill elements. It seems likely that as
the ozonated water is air-stripped in the fill cascade, algal growth is
In May 2003, a disinfection rate experiment was conducted to
obtain a quantitative measure of bacterial control and determine the minimum
daily time period required to accomplish it. For this determination, the ozone
system was shut down for a week to allow a bacteria population to develop. When
qualitative paddle tests indicated an elevated bacterial count in the sump water,
the ozone system was turned on and water samples were collected for
microbiological analysis at two-hour intervals for 12 hours with a final sample
collected at 24 hours. These samples were submitted to Silliker Laboratories,
Carson, Calif., for heterotrophic plate counts (HPC) to provide a quantitative
measure of bacterial levels at each sampling interval.
As indicated in Figure 3, the microbial population had
reached 8,000 cfu/ml at the start of the test. Within the first two hours the
population was reduced to 100 cfu/ml and remained low throughout the test. At
4:30 p.m., the chiller was activated to cool theater activities, and the
untreated water in the chiller loop was circulated to the sump. This could
account for the slight spike (1,700 cfu/ml) seen in the 5:00 p.m. sample. Based
on the results of this experiment, it is planned to test the effect of lowering
the operational period to four hours per day during the summer months when
bacterial growth is at a maximum and there are no students on campus.
When the CTS system was installed, the sand filter that was
previously used to remove particulates was replaced with a centrifugal
separator. This has not resulted in any visible reduction of water clarity.
When a panel of students was shown samples of tap water and tower water, a
majority was unable to distinguish between the two.
To provide a quantitative evaluation of the effectiveness of
the CTS centrifugal separator, a comparison between it and a sand filter was
conducted. A sand filter manufactured by Process Efficiency Products (24-inch,
0.85 mm media) was plumbed into the sidestream line feeding the separator. This
was done in a fashion that allows the flow (43 gpm) to be switched between the
sand filter and centrifugal separator. Sump water samples were collected daily
for five days while the separator was operating. The particle removal system
was turned off for two days then the flow was routed through the sand filter.
Daily sump water samples again were collected for five days. Both sets of
samples were submitted to Particle Analysis Laboratories to determine particle
counts in various size ranges using a laser particle counter.
Both particle removal systems proved quite effective. For
comparison, Table 3 shows before and after filtration results reported by
Process Efficiency Products. Both the sand filter and separator produced
results comparable to those presented in Table 3, and results were even better
for the larger size ranges. (See Figure 4.) As indicated in Figure 4, the sand
filter was slightly more effective at removing particles in all size ranges. An
unexpected result was the CTS separator's particle counts in the 0.5-5
µ range, which were comparable to those obtained by the sand filter.
Removal of these smallest particles is especially important since they produce
a significant part of the deleterious particle effects and must be removed to
provide best protection. Surprisingly, the differences were most pronounced for
larger particle sizes.
The CTS system performed as claimed by the manufacturer.
Though no chemical treatment was used, continuous monitoring of machine
parameters revealed no evidence of abnormal corrosion or scaling.
The low levels of ozone used for water treatment, when
coupled with their mixer technology, produced excellent bacterial control with
HPCs in the hundreds of cfu/ml (Figures 2 and 3). For comparison, EPA standards
allow a maximum HPC of 500 cfu/ml for drinking water. Chemically treated towers
often have HPCs in the tens of thousands, and people in the chemical treatment
industry have claimed that an HPC of one million may be acceptable in cooling
The CTS centrifugal separator performed better than the
reputation for this technology would suggest. Though slightly less effective than
the sand filter in comparative tests, the CTS system performed well using the
separator, indicating that, in this application, the separator generally is
comparable to sand filtration in effectiveness.
The results of this test indicate that the CTS cooling tower
treatment system is an effective option for treatment of cooling tower water in
smaller volume systems where oxygen demands will not exceed its limited ozone
generation capacity (CTS has a similar system using corona discharge for larger
cooling systems). Though no cost data were supplied, the simplicity of the CTS
system and its low energy demand when compared to units using corona discharge
for ozone generation suggest this system should be obtainable at reasonable
cost. The simplicity of the system also leaves few areas for problems to occur.
The simple UV lamp used to generate ozone depends on a ballast for power and
should run as dependably as a fluorescent light system. Throughout the course
of this test, none of the system's components failed to operate as designed.
Thanks must be give to Daniel Sanchez for his help in
monitoring the performance of the CTS system throughout this study and to Frank
Vitone, head of the HVAC department at Pierce College, and the other members of
the HVAC department for their help and advice.