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To
select a proper filter system for the requirements
of a given application, knowledge of filter
efficiency and dirt capacity is required. The
filter manufacturer needs to provide data, which
are based on test procedures simulating real
parameters on a laboratory scale. At present
there is no standard for liquid filter testing
(except multipass test to ISO 4572, which is
for hydraulic filters).
Early
cartridge filters were constructed from a square
weave S.S. mesh. In this case, every hole or
pore is nominally the same size. This measurement
can be accomplished by evaluation of wire counts
and thickness or by direct observation under
microscope. As filter developed, different weaves
(Photograph of woven wire mesh) for the mesh
is being used and now it is difficult to measure
by count and thickness of wire. Consequently,
a number of methods of establishing the particle
removal rating were developed.
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GLASS
BEAD TEST:
Glass
beads suspension is passing through a
test filter under defined test conditions,
and then passing the filtered suspension
through an analysis membrane. The analysis
membrane was than observed, and the largest
glass bead identified and measured. This
measurement was taken as the absolute
rating of the filter. So, the absolute
rating of the filter was defined as the
largest hard spherical particle, which
would just pass through the filter.
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BUBBLE
POINT TEST:
As
described in ARP901 (Ref2), this is based on
the observation that, if a circular hole in
a flat plate is fully wetted in liquid, the
minimum bubble radius that the hole will support
is the radius of the hole. The differential
pressure across the bubble under these conditions
is controlled by the surface tension, so that
¶P = 2s Where ¶P = differential pressur
r s = Surface tension
Since
the minimum bubble radius corresponds to the
maximum differential pressure before bubbles
are released from the hole, the measurement
of differential pressure can be used to establish
a size for the hole.
(Picture of bubble point test)
ARP901
extends the method to triangular holes in flat
plates, but it must be recognized that the measured
differential pressure is also dependent on the
shape of the hole.
¶P = Ks s = surface
tension
r r = pore
size
Both
the glass bead test and the bubble point test
were historically reputed to provide an absolute
rating for the filter media, but also implied
that this was a cut-off point, in the sense
that in service no particles below this size
were removed, and all particles above this size
were removed. Both methods were based on spherical
particles, which only occur rarely in real filtration
applications.
In
an effort to address these difficulties, a further
test was developed, and is also included in
MIL-F-8815. This has been called the "nominal
rating".
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MULTIPASS TEST (ISO 4572):
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This
is used for the evaluation of hydraulic filters.
A test contaminant is added to hydraulic oil
and re-circulated through the filter under test.
Samples are taken from upstream and downstream
of the filter for particle counting, and hence
efficiency evaluation. The amount of solids
added can be used to determine the apparent
dirt capacity.
The
test simulates the conditions a hydraulic filter
would see of a re-circulating contaminant in
a closed loop. For most filters used in the
process industries this type of operation is
not applicable. Generally they are used for
low viscosity fluids such as water, on a single-pass
through the filters. The concern of the user
is the quality of filtrate downstream of the
filter after a single-pass, and the life on
stream.
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SINGLE PASS F2 TEST :
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AC
Fine Test Dust is dispersed in water using
a mixer, then agitated using high shear mixer
for long period for reproducible dispersion
of particles in water. The resulting slurry
is used to challenge the test filter. The
test apparatus consists of a test reservoir,
a pump, test filter and housing, and a clean-up
filter. Automatic particle counting systems
are installed at upstream and downstream of
the test filter. A differential pressure gauge
is installed across the filter.
First
flow rate is set for the test housing (without
cartridge). Generally 10 lit/min/10"
cartridge is desired. The rig is run with
only the clean-up filters, rated at 0.2 .
Once low, stable level of background contaminants
is achieved the test can be started. The test
cartridge is installed in the housing and
any air in the system is bled off. The rig
is restarted, so the clean differential pressure
across the filter can be determined under
the test conditions, with clean re-circulating
water.
The
contaminant slurry is charged to a dosing
tank. The actual quantity and concentration
is determined by calculation from the desired
test time, expected filter performance and
the expected dirt capacity. From this tank
it is injected into the re-circulating system
at a steady rate.
Particle
count machine can be sat for 6 different size
range of contamination. Samples from upstream
and downstream of the filter are analyzed
and the results recorded automatically. The
filter differential pressure is also recorded,
with flow rate. The test parameters (flow
rate, solids loading, temperature) are held
constant for the duration of the test.
The
results recorded can be analyzed by the calculation
of ratio, or filtration efficiency as shown
Nu
bx = -----
Nd
Where
bx = filtration efficiency at x (microns
or micrometer)
Nu
= Number of particles of diameter x or larger
at upstream of the filter.
Nd = Number of particles of diameter x or
larger at downstream of the filter.
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