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Leak Detection Products
Sensistor H2000
- Hydrogen Leak Detector for the Power Plant Industry,
HVAC, Aircraft, Automotive and Refrigeration Industry
H2000
Product Brochure for Power Industry

Call us at
800-331-2808 for more information and
price quotations.
Technical Information
The Sensistor uses a mixture of 95% nitrogen
and 5% hydrogen. This 95/5 mixture is totally non-combustible and is
labeled as a green label gas. Hydrogen as a tracer gas is effective
and efficient due to the cost, non-toxic qualities, and no
environmental concerns.
Finding Leaks in Tube-Sheets
and Generator Cooling Systems
Loss of efficiency is the
primary reason power plants need to leak check their condenser
vacuum systems. Helium leak detectors are the most effective method
of pinpointing these damaging leaks, and may be further applied to
finding leaks in tube-sheets and generator cooling systems.
Leak Checking the Tube-Sheets
Care must be taken not to
contaminate the polished condensate with coolant. Particularly
seawater coolant, in coastal-located generators, threatens the
integrity of the system by in leakage
leading to air in-leakage. Defects, wear
points, and tube-to-tube joints are all potential leak sources.
And each new leak raises the need for a costly partial shutdown and
tedious work in the hot environment of the water boxes. Helium leak
testing is fast and efficient and can be effectively accomplished
with the L200 Helium Leak Detector. Here is the procedure:
A
fan set up to exhaust the far water box is mandatory. This not only
keeps the worker in the near box cool, it pulls the helium down the
tubes and exhausts it. The snuffer probe is set up in the exhaust of
the Steam Jet Air Ejector or water-ring pump, just as it would be
for checking the condenser vacuum system. Then, with one worker
monitoring the leak detector, another climbs into the water box and
proceeds to spray some helium into each condenser tube.
With thousands of tubes, this cannot be done with an air gun in a
reasonable amount of time. The solution is to use tube-sheet
testers; hand-held plenums that spread the helium over an area of
the tube-sheet of approximately 2 square feet. Many workers like to
use chalk to mark around the plenum while they are holding the
helium valve open. That way, they can return to check the same
tubes if a leak has been located.
The two workers communicate with field phones or the worker in the
water box can wear headsets to listen to the audible pitch of the
leak detector. Walkie-talkies generally will not broadcast into the
water box. As helium is sprayed over a leak, it is drawn in through
the leak and pumped out of the condenser by the Steam Jet Air
Ejector or water-ring off-gas pump. As it passes the sniffer it will
be sensed and show up on the leak detector. Time response for the
helium varies, depending on the volume of the condenser and the
speed of the air ejector, but 45 seconds to 1½ minutes is typical.
Once there is a response to a leak, the “inside man” should wait for
it to clean up—that is, for the helium to be largely pumped out.
Then he should go over the same area, at the same speed, but in the
reverse direction, to locate the leak. When the response is
seen again, the leak will be halfway between where the plenum was
when he first heard the response and where the plenum is now. The
specific leaky tube can be pinpointed either by use of a smaller
plenum (perhaps 6" square) or by careful use of a spray gun on one
tube at a time.
Whether by using a spray gun or a plenum, the helium is drawn down
the tubes by the suction of the exhaust fan, exposing the entire
tube and tube-sheet weld at the far end to the helium. When a leaky
tube is found, it can be plugged then, or temporarily blocked until
all the leakers are located.
Use of the Sensistor and tube-sheet testers speeds
a hot, tedious job, while providing assurance that each leak has
been found.
Leak Checking the Generator Cooling System
Leaks in the hydrogen cooling system for generators are a natural
concern for power-plant workers. Not only are the systems large and
complicated, with many joints, seals, packing, etc., but hydrogen
leakage is especially hazardous despite the large volumes of the
turbine halls.
While hand-held hydrogen leak detectors are available, the Sensistor
hydrogen sniffer is very effective at this task, and is
more sensitive.
When searching for hydrogen leakage, one uses the hand piece of the
Sensistor is used to probe around all the potential leak sites, listening to the audible signal
through earphones. The response of the leak detector, operating in
this manner, is about one second, so the operator can easily
pinpoint the source of leakage.
Hydrogen usage should be a guide to the total leakage of the system.
For safety reasons, it is important to realize that leakage into a
pocket or closed space can easily build to an explosive level. And
anyone who has seen a small hydrogen flame “disappear” when lights
are turned on knows what a hazard these invisible fires can be.
Routine leak testing is so easy with the Sensistor that there is no reason to put it off.
In
recent years a number of authors have addressed the various costs to
power plant operators of vacuum leakage. These costs range from the
erosion and pitting of turbine “buckets,” through exhausting of
condensate polisher resins to simple loss of turbine efficiency, as
the condenser vacuum is lost. Other costs can include corrosion of
Admiralty-metal tubes by the high levels of hydrazine used to reduce
oxidized metals. All of these costs can be reduced (sometimes very
drastically) by adequate leak location methods, followed by
appropriate repairs.
Assessment of these costs as a function of leak rate is impossible
in many cases. (Fractured blades on a turbine disc bear a known cost
in parts and downtime, but how much oxygen causes the fracture is
not known.) An exception is the loss of turbine generator efficiency
at progressively higher base pressures due to in-leakage.
Two Examples
The experiences of two fossil-fueled plants can illustrate this. One
plant in the Northeast embarked on an ambitious program to minimize
leakage. They charted the vacuum pump exhaust flow for each of five
units on a daily basis, while using a Leybold Helium Leak Detector
to locate leaks. When they found a leaky relief valve on the
injection water return to condenser line and isolated it, they
reduced the permanent gas flow by 30 cfm and estimated fuel savings
of $35,000 per month. When they located and repaired a cracked weld
in an extraction steam line, permanent gas flow was reduced from 72
cfm to 17 cfm—generating estimated fuel savings of $9,000 per day.
The second plant, a 350-megawatt base loaded New England unit, has
computed their fuel cost directly as a function of suction pressure.
They determined that each half inch Hg of extra suction pressure
cost 4.6 barrels/hour of fuel. Their design rating pressure is 1.05
inches Hg absolute; a leak which would force the pressure to 1.55
inches Hg absolute would cost an extra 110.4 barrels/day, or
$2,000/day at $18/barrel. The amount of leakage necessary to raise
the suction pressure this much might be as little as 2 scfm (if a
steam-jet air ejector is used) or as much as 20 scfm if a mechanical
pump is used. In either case, a substantial cost penalty is borne by
the operator of the leaky plant.
The Sensistor has proved its worth in many
plants, nationwide and overseas. It is a fast, reliable approach,
which can easily be learned by maintenance personnel. Most
important, it can be applied while the plant is in operation, under
load, so there is no need to wait for a weekend shutdown to find a
new leak. The same system can be applied during shutdown to leaks in
the tubes and tube-sheets of the condenser.
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