Integrity Testing Methods
Integrity testing sterilizing filters is a fundamental
requirement of critical process filtration applications in the pharmaceutical
industry. FDA Guidelines require integrity testing of filters used in the
processing of sterile solutions such as large volume paren terals (LVPs) and
small volume parenterals (SVPs). The FDA also requires corresponding testing
documentation be included with batch product records.
Two
classifications of integrity testing are destructive and non-destructive.
Millipore's practice is to perform destructive testing as a lot release
criteria on samples from each manufacturing lot of all fabricated
sterilizing-grade filter products, and non-destructive testing on each
sterilizing-grade filter prior to sale to insure its integrity.
Destructive Testing
Millipore performs destructive bacterial challenge testing
in accordance with ASTM F838-83 methodology. Destructive challenge testing is
the best way to determine a sterilizing filter's ability to retain bacteria.
Bacterial challenge testing provides assurance that the membrane and fabricated
device meet the critical performance criteria of a sterilizing filter. The test
is performed on a statistical sample of each lot of membrane and fabricated
devices produced.
During the Millipore bacterial retention test,
0.22 µm filter discs and devices are challenged with a solution of culture
medium containing bacteria (Brevundimonas diminuta ATCC 19146) at a
minimum challenge of 107 per cm2. The effluent is then
passed through a second 0.45 µm assay filter disc that is placed on an agar
plate and incubated.
Non-Destructive Testing
Non-destructive testing may be done on filters before and
after use. Integrity testing sterilizing filters before use monitors filter
integrity prior to batch processing, preventing use of a non-integral filter.
Integrity testing sterilizing filters after a batch has been filtered can
detect if the integrity of the filter has been compromised during the process.
Detecting a failed filter alerts operators to a problem immediately after batch
processing, eliminating delay and allowing rapid reprocessing.
There
are three types of non-destructive testing – the bubble point test, the
diffusion test, and the waterflow integrity test for hydrophobic filters
(HydroCorr™ Test). The pressure hold, forward flow, and pressure decay tests
are variations of the diffusion test. The stringent requirements of the
pharmaceutical industry dictate that non-destructive filter integrity testing
must be performed in each sterilizing application.
To be able to use
an in-process non-destructive integrity test, physical tests were developed
that correlate to the bacterial challenge test. A specification for the
physical test correlates directly to the bacterial challenge test. Once this
correlation is established, it is determined that a cartridge passing the
physical test is an integral sterilizing filter.
Bubble Point Test
The most widely used non-destructive integrity test is the
bubble point test. Bubble point is based on the fact that liquid is held in the
pores of the filter by surface tension and capillary forces. The minimum
pressure required to force liquid out of the pores is a measure of the pore
diameter (see formula).
P = bubble point pressure
d = pore
diameter
k = shape correction factor
cos Θ = liquid-solid contact
angle
Σ = surface tension
Bubble Point Procedure
1. Wet the filter with the appropriate fluid, typically
water for hydrophilic membranes or an alcohol/water mixture for hydrophobic
membranes.
2. Pressurize the system to about 80% of the expected
bubble point pressure which is stated in the manufacturer's literature.
3. Slowly increase the pressure until rapid continuous bubbling is
observed at the outlet.
4. A bubble point value lower than the
specification is an indication of one of the following:
- fluid with
different surface tension than the recommended test fluid
- integral
filter, but wrong pore size
- high temperature
- incompletely
wetted membrane
- non-integral membrane or seal
Diffusion Test
At differential gas pressures below the bubble point, gas molecules migrate through the water-filled pores of a wetted membrane following Fick's Law of Diffusion. The gas diffusional flow rate for a filter is proportional to the differential pressure and the total surface area of the filter. At a pressure approximately 80% of the minimum bubble point, the gas which diffuses through the membrane is measured to determine a filter's integrity. The flow of gas is very low in small area filters, but it is significant in large area filters. Maximum diffusional flow specifications have been determined for specific membranes and devices and are used to predict bacterial retention test results.
Diffusion Test Procedure
1. Thoroughly wet the filter with appropriate test fluid,
typically water for hydrophilic membranes or an alcohol/water mixture for
hydrophobic membranes.
2. Slowly increase pressure on the upstream
side of the filter to the recommended test pressure provided by the
manufacturer, typically at least 80% of the minimum bubble point
specification.
3. Allow the system to equilibrate.
4.
Measure the gas flow at the outlet for one minute with an inverted graduated
cylinder or a flow meter.
5. A diffusional flow reading higher than
the specification is an indication of one of the following:
- wrong pore
size
- temperature other than ambient
- incompletely wetted
membrane
- non-integral membrane or seal
- liquid/gas combination
different than the recommended fluids
- inadequate stabilization time
Pressure Hold Test
The Pressure Hold Test, also known as pressure decay or
pressure drop test, is a variation of the diffusion test. In this test, a
highly accurate gauge is used to monitor upstream pressure changes due to gas
diffusion through the filter. Because there is no need to measure gas flow
downstream of the filter, any risk to downstream sterility is eliminated.
The pressure hold value is dependent on the diffusional flow and
upstream volume. It can be calculated using the following equation:
Where:
D = Diffusion rate (mL/min)
T = Time
(minutes)
Pa = Atmosphere pressure (1 Atm or 14.7 psi)
Vh = Upstream
volume of apparatus (mL)
ΔP = Pressure Drop (bar or psi)







