摘要
The importance of clean air to the well-being of people and for the protection of
industrial equipment has highlighted the critical role of air filter performance. The
objective of this thesis is to study the filter performance characteristics namely; the
pressure drop and the fractional efficiency of standard full scale (592x592x400 mm)
mini-pleated HEPA absolute fibrous filters. Accurate filter performance prediction
plays a significant role in estimating the lifetime of filters and reducing energy and
maintenance operating costs. To ensure the appropriate filter selection has been made
for a specific application, filter design must be further investigated to include pleat
count and its corresponding surface area.
The investigations undertaken in this work were based on using standard SAE coarse
and fine dust. This guaranteed that the results would be applicable globally
irrespective of the geographical location or the field of application of the filtration
technology. However, the performance of air filters used in gas turbine and HVAC
applications tend to deviate from that predicted by laboratory results using standard
air dust. This is especially true in regions known to have dust with characteristics
deviating from that of standard dust, such as in Kuwait. Therefore, as part of this
thesis, the Kuwaiti atmospheric dust has been characterized both chemically and
physically in order to investigate the possible impact of these characteristics on the
results of the filter performance. It transpired, however, that the characteristics of dust
with extreme properties, represented in this case by Kuwaiti dust, fell between those
of the characteristics of the two standard types of dust, namely, SAE coarse and fine
dust. This finding, therefore, provides additional confidence in the generality of the
results pertaining to the filter performance.
The work investigated the effects of ten different flow rates ranging from 500 to 5000
m3/h with increment of 500 m3/h. The four different pleating densities used to
construct the filter were 28, 30, 32 and 34 pleats per 100mm. This experimental work
was conducted while keeping other parameters such as filter media class unchanged.
Pleating density may play a major role in achieving the optimum pressure drop and
the required efficiency expected from such a filter. Such optimization was expected to
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facilitate design alternatives supported by experimental results. A testing facility
located in Limburg Germany at the EMW Filtertechnik GmbH was used for this
testing. Two different particle size counters were used to cover a considerable
particle size range. The results of the particle counter with size range of: 0.065 – 0.9
μm was used for the analysis since it covered the study of the Most Penetrating
Particle Size (MPPS) with respect to the filter pleat density and face velocities. This
experimental work involved testing ten industrial full scale HEPA filters, which were
divided into three groups. The first two Groups (Group A and B), each consisted of
four filters manufactured with different pleat densities of 28, 30, 32 and 34 pleat per
100 mm. The third Group C consisted of two filters; the first filter had horizontal pleat
orientation while the second pleats were oriented vertically. Both filters in Group C
had a pleat density of 28 pleat per 100 mm. Filters of Groups A and B were
challenged with SAE coarse and fine dust, respectively. In the case of filters of Group
C, only the initial pressure drop and efficiency measurements were conducted.
This experimental work has highlighted the underlying reasons behind the reduction
in filter permeability due to the increase of face velocity and pleat density. The
reasons which led to surface area losses of filtration media are due to one or
combination of the following effects: pleat crowding, deflection of the entire pleated
panel, pleat distortion at the corner of the pleat and/or filtration medium compression.
The experimental data for fractional efficiency were fitted using a modified Lee and
Liu [1982a] model. The proposed modified model was verified to show a good
agreement with the experimental results. It is evident from entire array of experiments
that as the particle size increases, the efficiency decreases until the MPPS is reached.
Beyond the MPPS, the efficiency increases with increase of particle size. The MPPS
shifts to a smaller particle size as the face velocity increases and the pleating density
and orientation did not have a pronounced effect on the MPPS. The second part of this
experimental work involved the dust loading process which showed a higher
efficiency and pressure drop response of SAE fine dust when compared to SAE coarse
dust. Increasing the mass of dust loads and flow rates have a significant effect on the
filter efficiency while the effect of varying pleating density was negligible.
Throughout this study, optimal pleat count which satisfies both initial and dust loaded
pressure drop and efficiency requirements may not have necessarily existed. This
experimental work has also suggested that a valid comparison of the pleat densities
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should be based on the effective surface area which participates in the filtration action
and not the total surface area the pleat density provides.
The work in this thesis has presented novel contribution in four aspects. Firstly, the
full scale nature of the experiments resulted from using full scale standard industrial
size HEPA filters constructed in V-shape banks cartridge in all the tests. Secondly, a
novel explanation of when the surface area losses become a dominant factor in the
filter permeability reduction. Thirdly, the discovery of the fact that increasing the
pleating density could be counterproductive in terms of effective filtration surface
area and filter permeability. Finally, the work has proposed new design alterations for
maintaining effective surface areas. All design improvements are currently under
review as they might require developmental work and investigation prior to any
possible future implementation.