There is a constantly growing need for
products and technologies that for their realisation require hermetically
closed elements, vessels and tubes. Envelopes with greater or smaller vacuum
tightness had to assure a satisfactory isolation between external atmosphere
and inside over- or underpressure. Crytical leak spots in closed systems are usually:
connections, gaskets, welded and brazed joints, defects in material etc.
Regarding to quality demands in different production processes, technical
people very often encounter with standards for tightness testing. Wishing to
state if an element or system meets with corresponding standards we have to be
familiar with the procedures enabling the following appointments:
- question if
there is leakage or not
- settlement of
the leak size
- detection of
leak locality
For solving the mentioned problems different
treatments and techniques are known but among them there is no anuniversal method, Each testing is suitable only for a
selected leak rate or for fixed forms and technologies. Our article presents
the leak types, their sizes and various leak detection techniques.
Keywords: tightness, leakage, trace gas,
helium mass spectrometer leak detector, hermetic sealing
● The words "leak" and "leakage" appear
in the field of vessels' hermetical closing and do not confront only with
vacuum technologists but also engineers working with high pressures. A leak
means an unintended crack, hole or porosity in an enveloping wall or joint
which must contain or exclude different fluids and gases allowing the escape of
closed medium. The basic functions of leak detection are the localization and
size measurement of leaks in sealed products and systems For majority of examples, a leak test procedure is a
quality control step to assure a device integrity, and is one-time non destructivetest.
● Typical products in which the leak detection has to be
used are: vacuum chambers, TV- , and other cathode tubes, hermetically sealed
electronic components, pressure vessels, aerosol containers, vacuum thermal
isolation (e.g. dewars), pumps, refrigerating
systems, chemical and nuclear plants, beverage cans, products containing metal
bellows, electron microscopes, peace makers, etc.
● In spite of modem technologies it is practically
impossible to manufacture a sealed enclosure or system that can be guaranteed
to be leak proof without first being tested. The main question is: what is the
maximum acceptable leak rate consistent with reasonable performance life of the
product.
● We can distinguish different types of leak sources.
● Leaks caused by defects in the containing envelope. For example a too thin
wall of a plastic bottle becomes microscopic cracked at enough high pressure difference,
or in canning industry if the score mark is too deep in ring pull-tab can top,
or porous cast in machine housing metallurgy, etc.
● Leaks in newly manufactured products are most commonly imperfect joints or seals by which
various parts are assembled to form the final article. There are known
demountable and fixed joints. Between them the most often used are welds,
brazed and soldered joints glass-to-metal and ceramic-to-metal seals, O-rings
and other gaskets, etc.
● Materials permitting gas diffusion and permeationthrough the wall.
● Virtual leak, a special type of leak in vacuum technique, which is not really a leak
but is the internal source of gas or vapor.
These are cavities in a chamber wall with thin connections to the inner vessel
space such as improper welds, closed threads and holes etc.
The shapes of leaks (cracks, fissures,
porosity, damages, etc ...
)are very different, unknown and non-uniform. Therefore it is impossible
to measure their sizes with any geometrical dimension except of course in the
case of an ideal or artificial leak as used for calibration. How then to define
the leak size? A generally accepted method became the observation of gas or
fluid flow through it in certain conditions of temperature and pressure
difference. Consequently leak rates can be defined in two ways:
○ in terms of the application, e.g.: 3 g of refrigerant R-12 in 2
years at 5 bar, or 65 m of oil per year at 60 �C
at atmospheric pressure, etc...
○ in terms of vacuum leak detection method, e.g.: 2 mbar
pressure increase in I hour or 3x 10-7 mbar/s helium (using He-detection method)
Each of the mentioned examples gives a
legitimate description of leak rate but the generally accepted unit is the last
one because of very simple and understandable helium leak detection. Its
efficiency is the result of a fierce and highly competitive developments within
the last 15-20 years.
The basic experiment explaining the leakage of
hermetic system (increasing pressure method) is presented in Figure 1. The
tested vessel or system with known volume (Vo)
is by a valve connected to pump. After evacuation the connecting valve should
be closed and then the pressure in volume registered for a suitable long time
period. There are more possibilities: system is tight and clean (a), fight and
not clean (b), not tight and clean, i.e.: ideal leak (c), not tight and not
clean, i.e.: combination of leak and degassing.
As we can see in each case (except for a tight
vessel) we have pressure increase and regarding to the shape of diagram we can
conclude the type of leak. Using the curve inclination data the leak size can
be determined by the following formula:
Q = ^p * Vo/^ t
(mbarl/s)
This simple test helps us to describe the situation
at the beginning of leak tracing procedure. Very similar test can be realized
by pressurizing the the system (and
detecting the pressure decay) but gives only data on leak size and is not used
so often.
The leak rate Q does not only depend on the
geometric dimensions (diameter, length) of the leak but also on the physical
properties of the gas (or the liquid), such as viscosity, relative molecular
mass and on the pressure difference. For example: in the same environment
conditions helium flows through orifices 2.7 times faster than air. Because of
different results if the same leak is measured by various mediums it must be
always noted with which gas a testing was performed.
The maximum acceptable leak rate for a given
product depends on the nature of product. Since the cost of leak detection (and
manufacturing too hermetic envelopes) increases in inverse proportion to a leak
rate, it follows that testing for unnecessary small leaks causes unnecessary rise of production costs. Some
examples of tolerated leaks in different elements and systems are shown in
Table 1. We can see very wide range of sizes: from great with some tenths mbar
l/s in rough vacuum devices, to million- and more- times smaller in
hermetically closed electronic elements. It is possible to state there are no
ideal products without leakage. We only can demand they have leaks smaller than
the specified leak.
Table 1. Leak rate specification for various elements and
systems |
||
Element or System |
Max. permissible Leakage |
Remark |
chemical
process equipment |
10-1 to
1 mbar l/s |
great
process flows |
beverage
can bottom |
10-5 to
10-6 mbar l/s |
retention
of CO2 |
dynamic
pumped vacuum s. |
10-5 to
10-7 mbar l/s |
permanent
pumping |
IC-package |
10-7 to
10-8 mbar l/s |
|
pacemaker |
cca 10-9 mbar
l/s |
long time implanted
in body |
closed
vacuum elements |
10-8 to
10-10 mbar l/s |
e.g.
TV- and Xray- tubes |
A few leak detection techniques are known.
Their performances regarding to detecting sensitivity are presented in Fig 2.
Because of their advantages we shall concentrate attention on the helium mass
spectrometer techniques but at first a short description of others is presented,
The spark coil technique uses a high voltage or Tesla cod and sparkling
point to create the electromagnetic radiation which causes the generation of
glow discharge in neighbouring evacuated ampoules. Normally it is possible only
in non metalenvelopes, that means
first of all in glass and plastic elements or tubing. Drawing the leak antenna
along the tested element we can see plasma inside and coming to the leak, a
sharp arc passage between plasma and antenna appears. The defect spot is very
clearly marked and a skilled person can from the colour of plasma also estimate
the inner pressure. This simple method however has a number drawbacks; since
besides the restricted application it is also to be avoided because of radio
disturbances.
Pressure change method uses pressure gauges which are ordinary used to
monitor the system performance. Suspected leak sites can be squirted with a
solvent (i.e. acetone or similar) while watching the gauge for a pressure rise
that occurs when the solvent enters the leak. This method has limited
sensitivity (depending also on the type of pressure measurement cell) and some
shortcomings (possibility of solvent freezing causestemporary
stuffing of leak, solvents may attack vacuum grease and elastomer gaskets).
Figure
1. Testing of tightness by increasing pressure method and various possible
results |
Bubble test (soap painting) |
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Bubble test (air, water) |
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Bubble test (He, alcohol |
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He sniffer |
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Halogen sniffer |
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Pressure decay |
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Acoustical |
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Vacuum decay |
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Spark tester |
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Thermal conductivity |
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Radioisotope |
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Halogen detector |
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Mass spectrometer |
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Dye penetrant |
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mbarl/s |
100 |
10 |
1 |
10-1 |
10-2 |
10-3 |
10-4 |
10-5 |
10-6 |
10-7 |
10-8 |
10-9 |
10-10 |
10-11 |
10-12 |
Figure 2. Sensitivity ranges of various leak detection
methods |
Overpressure methods can be performed by fluid or gas with which the
tested element must be filled. As a fluid usually the water from house
installation is used. Observing the outside surface the wetted areas show us
great leaks and smaller ones up to approx. I mbarl/s.
Testing with gas, the vessel is subjected to overpressure of some bars
(depending on material and wall thickness) and immersed into the water. At
leaks the gas bubbles begin to escape. In this manner the leaks up to 1.
10-3 mbarl/s can be detected. If the vessel is
too great for immersion, the suspected points should be painted by soap
solution and again we can see the bubbles escaping if there is a leak. This
method enables detecting the leakage up to 10-5 mbarl/s
and is usable also for very large systems.
Halogen leak detectors are used in the detector-probe mode (to 10-3 mbarl/s), requiring that the system be pressurized with a
gas containing an organic halide, such as one of the Freons.
The exterior of the system is then scanned with a sniffer probe sensitive to
traces of the halogen -bearing gas (Fig. 3). The principle is based on the
increased positive ions (K or Na) emission because of sudden halide composition
presence. The ion current is the measure for a leak size. Halogen detectors can
be used also in turned mode: evacuated vessel is connected to detecting
instrument and is sprayed by freon. In this
manner its performance is up to 5.10-7 mbarl/s
and is used in rough, medium and high vacuum.
Figure
3. Halogen leak detector |
Dye penetrant method is an adaptation of a technique used to find cracks in metals and defects
in welds. It uses a low viscosity fluid that exhibits a high rate of surface
migration. This fluid is painted on one side of a suspected leak site, and
after a time, it is detected on the other side of the wall. The test is simple,
low cost, it leaves records, thesensitivity can
be as high as 10-6 mbarl/s
Acoustical leak detection uses the sonic or ultrasonic energy generated by
gas as it expands through an orifice. Pressurized gas proceeds from tested
system through leaks which are detected outside by sensible microphone (tipically about 40 000 Hz). Acoustical leak detection
is widely used in testing high pressure lines, ductworks etc. It requires
modest instrumentation; it is simple and fast but is limited to about
10-3 mbarl/s.
Radioisotope method is useful only for testing hermetically sealed
components. They are placed in a chamber which is to be evacuated and filled
with radioactive tracer gas (tipically krypton
85). It difusesthrough present leaks in the
components and after removing it from environs test gas expands through leaks
back and can be detected by radiation sensor. The instruments for this type
leak tracing are very expensive but they enables the measurement of flows up to
10- 11 mbarl/s.
Mass spectrometers as leak detectors are used as most sensitive instruments for stating leak
existence and presence in vacuum systems. They are adjusted on the atom
respectively molecular weight of tracer gas. It is usually helium because of.
- its small mass and atom volume assures good
supply of gas through a leak -relatively great mass distance from neighbour
mass enables greater sensitivity - its partial pressure in air is low, approx.
4.10-3 mbar
The first next suitable gas for leak detection
purposes would be H2 but it is dangerous and residual
atmosphere in vacuum systems always contains this gas. There are also
spectrometers adjustable to other gases e.g. argon.
● Helium leak detection systems work as follows: He is
introduced to a test part that is connected to the leak detector. The helium
travels through leak into the leak detector, its partial pressure is sensed
respectively measured and results are displayed on instrument as flow rate.
● The main part of the device is mass spectrometer, a
sensor for different gas masses. In very low pressure (or vacuum) the molecules
of rest gasses are transformed in ions by electron impact. Separating the
ionized particles of different mass to charge ratios (q/m) it is possible to
state the partial pressures of present gases - in our case also the presence of
the sought gas helium. For helium MS- leak detectors, magnetic sector type mass
spectrometers are preferably used as gas search sensors. The low pressure (less
than 2x10-4 mbar) required for operation of the mass spectrometers is produced
by an integrated high vacuum pump system. The auxiliary vacuum pump required
for rough pumping the tested equipment is either incorporated or can be
attached via suitable connection.
Figure
4. Conventional type of the helium leak detection apparatus |
● As the necessary pressure for the mass spectrometer
cannot always be attained in the tested equipment within a reasonable pump-down
time, various types of MS-leak detectors with different performances have been
developed. The most used are constructions with "full flow operation"
(conventional) and with "contra-flow operation", regarding to the way
in which He is supplied towards MS- sensor. For example the figure 4 shows
schematically the conventional type MS leak detector. In presented system,
vacuum is maintained in the spectrometer tube by use of a diffusion pump in
combination with mechanical pump. A cold trap pumps condensable vapors such as oil and water. A roughing pump is
provided to evacuate the test port (and the connected sample to be tested) to a
pressure level that will not disrupt diffusion pump operation. Reaching a
suitable vacuum the sample is valved off
from the rough pump and by opening test valve joint to the MS- vacuum system.
Helium sprayed near the leak on the sample surface has now an open way to the
MS-tube and there it is detected. After completing procedure the test port
is valved off from the leak detector and
vented to air; than we can change the sample.
● How to use a helium MS- leak detector? There are
basically four different techniques for finding leaks: two
"OUTSIDE-IN" and two "INSIDE-OUT" methods (Fig.5).
● In the most commonly used "outside-in"
technique, the sample to be tested is connected to leak detector and evacuated
(Fig.5a). Than its surface is "probed" with a pointed jet of helium.
Coming over a leak detector gives an acoustic or visible sign (exactly
location) and the data about leak size.
● The second technique (Fig.5b) consists of evacuating and
hooding the sample with something like a plastic sheet and flooding the hood
with helium. So it is possible quickly to establish whether or not a sample
leaks and to establish the total leak rate. This technique is most useful on
production lines where a test piece must be accepted or rejected.
● In "inside-out" techniques the test
configuration is reversed. Instead of being evacuated, the sample is
pressurized with He. In this case the leak
detector is equipped with so called detector probe and it can be used in two
modes presented in figures 5c and 5d. In mode c) the test piece is probed with
the detector probe around suspected leak sites. This method sensitivity (up to
1. 10-6 mbarl/s) is not as good as by others
because the helium in the air is constantly being admitted into the detector.
● Figure 5. Main leak detection techniques with MS-leak
detector and The tracing gas. In one mode (examples a and b) He flows from
outside into vacuum and in other it expands from inner overpressure in
atmosphere |
● Mode d) allows testing of a large number of samples
simultaneously. It is often called the bombing technique because the parts are
previously placed in a pressurized The vessel
where the helium leaks into the parts which leak. All parts are than exposed to
detector probe in closed container. The mentioned leak test techniques are the
main methods for establishing whether leaks exist and for locating where they
are. Each has its own advantages and shortcomings, each has also its own
individual set of variations.