R.
James Seffrin Jersey
Infrared Consultants
P.O. Box 39
Burlington, NJ 08016
609-386-1281
Infraspection
Institute Newsletter Summer
1989
Infrared thermography has long been reported
to be an effective maintenance tool for steam traps. However,
recent research has raised serious questions regarding thermography's
effectiveness for steam trap inspections.
In order to understand how infrared thermography
is applied to steam trap inspections, we first need to understand
the steam system itself.
In most plants, steam is produced in a power
plant with a boiler. This allows the majority of heat energy
to be produced in a central location. The steam is then piped
throughout the facility via steam lines to locations where
heat energy is needed. In many cities, steam may be purchased
from local utilities. Regardless of the source, steam is expensive
and preventable losses are unacceptable.
Steam is an odorless, colorless, tasteless
gas which forms when water is heated above 212°F (100°C).
In a pressurized system, steam is capable of storing and transporting
large quantities of energy. Once steam has formed, more energy
can be introduced by further heating. This causes both its
temperature and pressure to rise.
Once steam leaves the boiler, it begins to
lose energy and cool. As its temperature falls, the steam
condenses back into water. Failure to remove condensate from
the steam system sets up a vicious cycle.
When condensate forms, the overall temperature
of the remaining steam drops, causing the steam to condense
at an exponential rate, greatly reducing the efficiency of
the steam system to transport energy. In turn, this temperature
drop causes more steam to condense causing a further temperature
drop. If left unchecked, this process will continue until
all steam has returned to water. In order to maintain optimum
steam system performance, steam traps are used to remove condensate
from the system.
Simply put, steam traps are automatic mechanical
valves designed to discharge condensate and air from the steam
system. Steam traps come in a variety of styles. The style
of trap used depends upon the application of the steam system.
Some of the more common styles are:
Inverted Bucket
Thermodynamic (Disc)
Thermostatic (Bellows)
Float
Float and Thermostatic
Like all mechanical devices, steam traps
eventually fail. Failure in an open position allows costly
steam losses to add up quickly. Failure in a closed position
not only reduces steam system efficiency but also allows acidic
condensate to attack steam system components. Visually, failed
steam traps usually exhibit no unusual symptoms.
According to some industry estimates, steam
trap failures can run as high as 40% at a given facility.
Such a high failure rate, combined with the high cost of steam
production, can account for losses exceeding several hundred
thousand dollars annually.
To date, steam trap testing has most often
been accomplished by either thermographic inspections or by
ultrasonic testing. Each of these methods has its merits;
however, each has its limitations.
Thermographic inspections traditionally measure
both the inlet and outlet pipe temperatures of the trap to
determine the temperature difference (delta-T). While this
technique may be somewhat effective for some of the simpler
trap designs such as disc traps, it does not work well for
the more complex traps such as float and thermostatic traps.
It also does not work well for traps where condensate load
constantly changes or where several traps in close proximity
discharge into a common condensate line. Delta-T temperature
measurement is a crude indicator of trap condition as small
to moderate leaks may not be detected.
Ultrasonic testing employs an ultrasonic
translator to actually listen to the trap operate. The ultrasonic
translator uses a contact probe to detect ultrasonic frequencies
(above 20 kHz) in the trap and translate these frequencies
into sounds that an operator can hear. Like thermography,
ultrasonics is a non-destructive, on-line test that requires
no system shutdown. Typically, ultrasonic translators are
very sensitive and can detect traps that are just beginning
to leak steam. However, ultrasonic translators cannot detect
"quiet" failures such as traps failed in the closed position,
air locked traps, or steam traps not under load.
Most ultrasonic translators are fairly simple
to operate; however, experience is necessary to accurately
interpret results. By incorporating both thermography and
ultrasonic testing together, the limitations of each method
are overcome and a highly accurate inspection technique is
realized.
When using both ultrasound and thermography
to inspect steam traps, the thermal imager is first used to
measure the inlet pipe (uninsulated) temperature at the trap.
The inlet pipe temperature should be close to the system's
steam temperature, which indicates that live steam is reaching
the trap and that the trap is neither air locked nor failed
in the closed position.
If inlet pipe temperature is significantly
less than steam temperature, steam is not reaching the trap
and investigation as to the cause is necessary. Most often
this is due to an upstream valve being closed; however, pipeline
obstructions may also prevent steam from reaching the trap.
Thermal imagers are particularly well-suited to quickly locate
closed valves or steam line blockages.
Once it has been determined that steam is
reaching the trap, the ultrasonic translator is used to listen
to the trap operate. Properly working traps are generally
quiet except during cycling. Typically, a hissing or rushing
sound indicates a failed trap. Trap cycle time, trap orifice
and air vent can also be checked. In cases where several traps
are located in close proximity, each trap can be accurately
tested on an individual basis.
Like other types of non-destructive testing,
results will depend upon operator training, experience, and
test equipment. Quality test instruments as well as thorough
knowledge of steam system operation will help to ensure accurate
results and tremendous cost savings.