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Trang 1Water Intrusion Test
Integrity Testing
Trang 3Test description
Conventional integrity testing of
membrane filters using the
bub-ble point, diffusion or pressure
hold tests requires that the filter
membrane be completely wetted
with a suitable wetting agent
Hydrophobic filter elements can
be tested by this method only if
the surface tension of the
wetting agent is less than the
critical surface tension of the
filter material being used
Other-wise, complete wetting does not
take place
This is why different organic
solvents like ethanol or solvent |
water mixtures are used as
prac-tical wetting media This aspect is
especially detrimental when the
system is used as a “sterile air
filter" for venting tanks,
bio-reactors and fermenters
Integrity testing of filters for
liq-uids is usually performed in situ
However, the in situ integrity
testing of hydrophobic gas
filters is only possible to a limited
degree due to safety reasons (e.g.,
explosion protection when
test-ing with organic solvents) and to
keep the product from solvent
contamination Besides these
complicated individual tests must
be followed by a drying phase
before any filter elements can
be installed
Additionally the filter sealing in
the housing still has to be tested
in situ Since the filters should be
retested immediately aher in-line
steam sterilization, tests with a
solvent | water mixture are
impractical for the user
Moreover, the drying procedure
must be validated since solvent
residues can contaminate the
product if drying has been
insufficient
The Water Intrusion Test (WIT)
was developed to overcome all of
these disadvantages The WIT can
be used to run routine integrity
tests simply, easily and reliably
Definition Water Intrusion Test (WIT).
The Water Intrusion Test (WIT)
is an in-situ integrity test for hydrophobic filters The WIT measures the decay rate of
a pressure level imposed upon
a hydrophobic membrane enveloped in water.
Theoretical principles.
Among other things, a pressure gradient that is dependent on pore size is necessary to over-come negative capillary forces (cohesive forces) This pressure is generally called the "Water Penetration Point" (WPP), the pressure at which water is pressed through a hydrophobic membrane The WPP is depend-ent on the hydrophobicity of the filter material and the pore size and is comparable to the bubble point
The relationship can be illustrated as follows:
Dmax= Diameter of the largest
pore
σ = Surface tension of the
liquid in dynes/cm (water 72)
θ = Angle of contact
(greater than 90° in hydrophobic filters)
∆ p = Available upstream
differential pressure (bar | psi)
k = Correction factor
(required since membrane filter pores are not cylindrical capillaries)
Introduction
4 · σ · cos θ
Intrusion (ml/10 min)
Test Pressure (bar)
350 300 250 200 150 100 50 0
Water Intrusion
Water Penetration
Water Intrusion Characteristics at Different Test Pressures
Pore Size: 0.2 µm, Height: 10’’, Temperature: 20°C
Trang 4Principle of Water Intrusion Test
The Water Intrusion Test (WIT)
was developed as an integrity
testing method to test
hydropho-bic sterilizing grade filters These
filters are often used as inlet air
and off-gas filters for fermenters
bioreactors and for venting
sterilizers, freeze dryers
auto-claves and tanks
The WIT is employed in both the
qualification of filter elements
and as an inplace test procedure
The WIT - like the mercury
intrusion test - is based on the
capillary depression of non
wetting liquids on the outer
surface of the membrane To
withstand these capillary forces,
a certain pressure gradient,
which is dependent on the pore
size among other factors, is
necessary The test run is in a
similar manner to the Diffusion
Test, although there is a major
difference In the Diffusion Test,
the diffusive gas flow through a
wetted membrane is measured
However, during the WIT a
hydrophobic filter installed in a
filter housing is flooded with
water on the upstream side
The pressure drop detected by an
automatic integrity tester
indi-rectly measures the volume of
water intruding into the
mem-brane matrix At first the test
system has to be flooded with
water, pressurised at the defined
test pressure and then stabilised
for a defined time After the
stabilisation time
is complete, the
water intrusion
will be measured
Origin of the pressure drop.
The pressure drop has two main reasons:
1 The upstream volume is in fact increasing due to remaining compaction processes Since this compaction is an asymp-totic process, it is never absolutely completed There-fore, a certain time has to be determined after which most
of the compaction is already done That is the main reason for the stabilization time of
10 Minutes
2 Water molecules actually get transported through the mem-brane In case of an integer membrane, this process is mainly due to evaporation of water molecules through the pore structure If the mem-brane is punctured, water is mainly flowing through the punctured hole
Water vanishes from the up-stream side The effect is, that the upstream volume is increasing (keep in mind that water is not subject to compaction) This amount of water (∆V) can be determined using the fundamen-tal law of Boyle and Mariott (p1· V1= p2· V2)
Principle of WIT testing
compressed air |gas
p1
p2
V1 · ∆p (p1- ∆p)
=
∆ V
∆t
Vn · ∆p (p1– ∆p) · ∆t
∆ V = V2- V1 = V1· - 1 =
with:
p1: Absolute pressure at the beginning of the pressure drop measurement [mbar]
p2: Absolute pressure at the end of the pressure drop measurement [mbar]
∆p: = p1- p2
V1: Upstream Volume at the beginning of the measurement [ml] (= Vn)
V2: Upstream Volume at the end of the measurement [ml]
The increase in Volume per time is defined as:
This value is defined – as one easily understands – as the “Water Flow Value” This value is basically linked to the Water Intrusion Value by a simple mathematical correlation:
The Water Intrusion is a value that has been defined in analogy to the diffusion For small pressure drops (< 5% of the absolute test pressure), the following equation holds:
with:
Vn: Upstream Volume [ml]
∆p: Pressure Drop [mbar]
1000 mbar: Reference Pressure
∆t: measurement duration [min]
Physically, air molecules pass through the wetted membrane If one collects all these molecules, they will fill a certain volume at 1000 mbar reference pressure at the ambient temperature as reference temperature This volume pre time is the Diffusion value
The Water Intrusion is calculated using the same formula:
If one imagines the volume ∆V that has been added to the upstream Volume due to the Water Flow to be filled with gas, it would use a different volume at an ambient pressure of 1000 mbar Again, the required volume at 1000 mbar (∆V10OO) can be calculated with Boyle Mariott's law to be:
∆V
∆t
Vn · ∆p (p1- ∆p) · ∆t WIT = · p1 - ∆p = · =
1000 mbar
(p1 - ∆p)
1000 mbar
Vn · ∆p
1000 mbar · ∆t
Diff = Vn · ∆p
1000 mbar · ∆t
WIT = Vn · ∆p
1000 mbar · ∆t
∆ V1000 = ∆ V · (p1 - ∆p)
1000 mbar
Trang 5Test parameters
Practical aspects Water
Intrusion Test.
• Allows inplace testing after
sterilization
• Avoids using wetting agents,
e.g IPA/Water
- Therefore no contamination
- No removal problems
No alcohol residue or
down-stream contamination
• The hydrophobicity of the
filter stays hydrophobic during
the test
• High sensitivity of the test
• The hydrophobicity of the filter
is evaluated by the test
• The time is reduced, especially
at multiple systems, which
reduces the shut down periods
• Directly correlated to the ASTM
Bacteria Challenge Test
System set-up.
The WIT can be used in a variety
of air filtration applications that require minimal engineering changes, however, some times systems may have to be reconfig-ured This is where the Sartorius Technical Support team comes to your assistance
The diagram to the right shows
an example of a manual WIT sys-tem The basic construction does not differ significantly from that used for the diffusion test In principle, WIT systems can be designed as manual, semi-auto-matic and fully autosemi-auto-matic units
to suit the applications, e.g., sterile venting systems for auto-claves, Iyophilizers, fermenters and tanks
Basic requirements for the test are:
1 The surface tensions of the water used must be > 72 dynes/cm
2 Minimized temperature differ-ence between the water and the inlet air ± 1k
3 Temperature fluctuations must
be avoided during the test
4 Filter element must be com-pletely hydrophobic
5 Adequate effective filter area, i.e., > 0.1 m2
6 The integrity tester must have sufficient accuracy, e.g., Sartocheck®unit
Operating sequence:
1 Completely fill the upstream side of the filter housing with water
2 Close all upstream valves
3 Connect the integrity tester, e.g., Sartocheck 3 unit
4 Start the test: The unit per-forms the WIT automatically
5 The test is completed and the results are printed out
6 Empty the filter housing through an appropriate drain
or condensate valve
7 Briefly vent dry using pressu-rized air with the inlet and drain valves open
8 Start operating the system
Trang 6Maximum permissible intrusion rates
False failures and
trouble-shooting.
If the filter cartridge does not
pass the test, it might be that
partial hydrophilization of the
membrane has occurred In this
case, the filter must be
steam-sterilized for at least 30 min at
121°C or 134°C and then
repeat-edly blown dry with hot air
Other false failures might be
attributable to water surface
tension and temperature
fluctua-tions All of these factors will
invariably cause elevated water
intrusion values (false failures)
Experience has shown that these
increased values indicate
“marginal“ failures and do not
lead to high water flow rates or
extreme pressure drops An
isopropanol|water test will
deter-mine whether one of these
causes is the problem or whether
the filter cartridge is out of
specification Fault free filters
will pass the solvent test because
this test cannot detect any
hydrophilization or reduced
sur-face tension of the water used
for the initial WIT
After the WIT, the filter
cartridges need to reach their
original air flow rate as quickly
as possible In other words, they
must not become blocked with
water, e.g., residual water in the
fleeces The time that the filter
cartridge needs to achieve 100%
of the original flow rate is called
the “blow-down" time
Test pressure.
The high air pressures needed to
force water penetration of the
PTFE membranes used in the
Sartofluor filter cartridges result
in very high test pressures used
for the various pore size ratings
This increases the tests reliability,
accuracy and precision
Pore Size Water WIT Test
Penetration Pressure
Pressure
bar psi bar psi
0.20 µm 4.5 65 2.5 36
0.45 µm 2.8 41 1.5 22
These variables are dependent on
the introduction of water with a
surface tension of > 72 dynes/cm
Stabilization and test time
The compressible upstream air volume above the water column and the actual water intrusion level are both low This illustrates the importance of maintaining sufficient stabilization and test times Enough time must be available for the water column to become saturated with air at the test pressure Similarly, the water must be distributed over the entire membrane area without the presence of air bubbles and the filter pleating must be fully compacted The following, values have been established for the stabilization and test times:
Stabilization time 1 13 min Stabilization time 2 10 min Test time 10 min
If these times are shortened the intrusion values may be too high due to insufficient distribution
of water across the membrane surface or faulty compacting of the membrane pleats
As in the diffusion test (and in all integrity tests), the maximum permissible water intrusion rates given by the filter manufacturer for the WIT must follow the ASTM bacteria challenge test methodology (HIMA Document
No 3, Vol 4, April 1982)
Trang 7Factors influencing the Water Intrusion Test
Hydrophilizing active agents.
As already mentioned, the use of
WIT requires that the filter
elements be com pletely dry and
hydrophobic Surface active
agents like solvent vapors,
detergents or oils can lead to
partial membrane
hydrophiliza-tion and thus to false negative
results
Moreover, these agents might
also reduce the air flow rate if
parts of the membrane matrix are
blocked by these agents During
normal operations, strict
atten-tion must be paid to these factors
and appropriate counter
measu-res taken when necessary
If partial hydrophilization occurs
the filter cartridge must be
hand-led as described on previously
page
Difference in temperature.
False failures may occur if the temperature difference between the test air and the water is too great If the water temperature
is much lower than the air tem-perature, great drops in pressure and high intrusion rates can result If the water temperature is much higher, the pressure drops will be too low
This situation can be remedied by storing the water in a storage tank in the room where the test will be performed or by filling the housing with water adjusted to the right temperature
Low surface tension of the water.
This situation mostly arises when the tanks being used are not cleaned and rinsed thoroughly, old ion exchange resins are used for preparing the water, or the water temperature is too high (> 32°C|90° F) These parameters can be avoided by taking preven-tive measures or adapting the water temperature
Fluctuations in ambient temperature.
Such temperature fluctuations affect the pressure drop measured during the test The same applies to the diffusion and pressure drop test The possi-bilities for the test being affected are minimized because the area
of the housing that comes into contact with the test air is very small compared to that in the diffusion test
Moreover, the great heat capacity of water compensates for any fluctuations Integrity tests are normally performed
in airconditioned rooms This source of error is therefore encountered very rarely
Inlet volume.
Generally with large-volume systems, the precise volume can
be easily determined, whereas the measured pressure drop may merely amount to a few mbar The results may then border
on the accuracy limits of the integrity tester and false results could be obtained
Similarly, when dealing with very low net volumes, high pressure drops can occur, leading to inaccurate test results
The net inlet volume must there-fore be selected so that both parameters relevant for intrusion measurement – namely, volume and pressure drop – can be deter-mined as accurately as possible
Trang 8Sartorius AG
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Phone +49.551.308.0
Fax +49.551.308.3289
www.sartorius.com
Sartorius Corporation
131 Heartland Boulevard,
Edgewood, New York 11717, USA
Phone +1.631.2544249
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KT199QN, Great Britain
Phone +44.1372.737159
Fax +44.1372.726171
Sartorius S.A
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91127 Palaiseau, France
Phone +33.1.69192100
Fax +33.1.69200922
Sartorius S.p.A Via dell’Antella, 76 /A
50011 Antella (FI), Italy Phone +39.055.634041 Fax +39.055.6340526
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No 3 Hoya Building 8–17 Kamitakaido 1-chome Suginami-ku Tokyo 168-0074, Japan Phone +81.3.33295533 Fax +81.3.33295543
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C/Isabel Colbrand 10-12 Edificio Alfa III planta 4, of 121
28050 Madrid, Spain Phone +34.91.3586100 Fax +34.91.3588804
Specifications subject to change
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Publication No.: SP-4504-e04014