Understanding the fundamental dynamics of particle
separation as a fluid stream passes through a filter media and then the after
cake removal is crucial to suitable selection of suitable media and to
successful filter design and operation. From the standpoint of filtration
processes, the two basic modes of filtration are dead-end and cross- flow.
Additionally, the location of particle capture further complicated filter media
design and selection for a specific application that are the particles
basically captured within the depth of the media or on the media surface.
The types of particle filtration used in dead-end filtration
are depth filtration and surface filtration. In case of depth filtration, the
particles are held in the media while in surface filtration they are retained,
at the surface where after a cake of particles is developed. These types should
be considered to ensure suitable media design and choice for a specific
industrial application.
Depth filtration in gas and liquid service is mainly used in
applications where low particle levels should be separated, to secure
downstream equipment, for product purification to meet health, safety and
environment requirements. The particles penetrate in the media and are subsequently
held within its multiple layer structure. The multiple layer structure prevents
premature blocking of the media and increases capacity for particle holding and
on-stream lifetime. As the particles held in the depth of the media, the
filters are meant to be used once or cleaned off-line. This cleaning can be
accomplished with solvents, ultrasonic vibration, pyrolysis, steam cleaning or
water back flushing.
Surface filtration by sintered wire mesh in liquid
applications mainly uses particle capture through straining mechanism where
particles larger than the pore size of the filter media are separated at the
upstream surface of the filter, their size prevents them from entering or
passing through the pore openings. In gas service, particles are held on or
near the filter surface through additional capture mechanisms, i.e. primarily
impaction, interception and diffusion. For both liquid and gas service, after
particles accumulate as a cake that increases in thickness as more particle
laden fluid is forced on the filter media. The cake, with its potentially finer
pore structure may aid in the separation of finer particles than can be
received through its as filtration proceeds.
As surface filters are not
perfectly smooth or have perfectly uniform pore structure, depth filtration of
finer particles may occur that will influence the filter life. So, selection of
optimal media grade and knowledge of the particle size distribution particularly
the finer particles, is important to achieve long filter service life.
Sintered mesh filters used in high particle loading
applications discovered in both gas and liquid services are usually online back
pulsed cleaned to increase filter life. The operative filtration mechanism
becomes cake filtration as the media is particularly engineered to ensure
surface filtration and the feasibility of cake particulate removal through
pulse blowback cleaning. A particle cake is developed on the surface of the
filter media that becomes the filtration layer and results into further
pressure drop.
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