Filtration of fabric technical textile of engineering.ppt

FILTRATION
* Filtration may be defined as the separation of solid from a fluid by means of a porous
medium that retains the solid but allows the fluid to pass.
*The suspension of solid and liquid to be filtered is known as the slurry. The porous
medium used to retain the solids is described as the filter medium;
* The accumulation of solids on the filter is referred to as the filter cake, while the clear
liquid passing through the filter is the filtrate.
Factors Affecting Filtration
Filtration is affected by the characteristics of the slurry, including:
1- The properties of the liquid , such as density, viscosity, and corrosiveness.
2- The properties of the solid, for example, particle shape, particle size, particle size
distribution, and the rigidity or compressibility of the solid.
3- The proportion of solids in the slurry.
4- Whether the objective is to collect the solid, the liquid ,or both.
5- Whether the solids have to be washed free from the liquid or a solute.

Rate of Filtration:
• All other things being equal, the object of the operation is to filter the slurry
as quickly as possible.
• The factors affecting rate of filtration is known as Darcy”s law and may be
expressed as:
• dV / dt = KA P /ul ....................20.1
• where
• V= volume of filtrate, t = time of filtration , K = constant for the
filter medium and filter cake , A = area of filter medium , P = pressure
drop across the filter medium and filter cake , u = viscosity of the filtrate ,
and l = thickness of cake.
• Factors affecting rate of filtration
• 1- Permeability coefficient: The constant (K) represents the resistance of
both the filter medium and the filter cake. As the thickness of the cake
increase, the rate of filtration will decrease. Also the surface area of the
particles .the porosity of the cake, and rigidity or compressibility of the
particles could affect the permeability of the cake.
• 2- Area of filter medium: The total volume of filtrate flowing from the filter
will be proportional to the area of the filter. The area can be increased by
using larger filters. In the rotary drum filter, the continuous removal of the
filter cake will give an infinite area for filtration.

• 3- Pressure drop; The rate of filtration is proportional to the
pressure difference across both the filter medium and filter cake.
The pressure drop can be achieved in a number of ways:
– Gravity: A pressure difference could be obtained by
maintaining a head of slurry above the filter medium. The
pressure developed will depend on the density of the slurry.
– Vacuum: The pressure below the filter medium may be
reduced below atmospheric pressure by connecting the filtrate
receiver to a vacuum pump and creating a pressure difference
across the filter.
– Pressure: The simplest method being to pump the slurry into
the filter under pressure.
– Centrifugal force: The gravitational force could be replaced by
centrifugal force in particle separation,

• 4- Viscosity of filtrate:
• It would be expect that an increase in the viscosity of the filtrate will
increase the resistance of flow , so that the rate of filtration is inversely
proportional to the viscosity of the fluid.
• This problem can be overcome by two methods:
• a- The rate of filtration may be increased by raising the temperature of
the liquid, which lowers its viscosity. However, it is not practicable if
thermolabile materials are involved or if the filtrate is volatile.
• b- Dilution is another alternative but the rate must be doubled.
• 5- Thickness of filter cake;
• The rate of flow of the filtrate through the filter cake is inversely
proportional to thickness of the cake. Preliminary decantation may be
useful to decrease the amount of the solids.

Filter Media
• The surface upon which solids are deposited in a filter is called the
“Filter medium”
• Properties of ideal filter medium:
• 1- It must be capable of delivering a clear filtrate at a suitable
production rate.
• 2- It must withstand the mechanical stresses without rupturing or
being compressed.
• 3- No chemical or physical interactions with the components of the
filtrate should occur.
• 4- It must retain the solids without plugging at the start of filtration.
• 5- Sterile filtration imposes a special requirement since the pore
size must not exceed the dimension of bacteria or spores.

Classification of filter media
• 1- Woven filters: these include a- wire screening . b- fabrics of
cotton, wool, nylon.
• Wire screening e.g. stainless steel is durable, resistance to plugging and
easily cleaned.
• Cotton is a common filter ,however, Nylon is superior for pharmaceutical
use, since it is unaffected by mold, fungus or bacteria and has negligible
absorption properties .
• 2- Non- woven filters: Filter paper is a common filter medium since it
offers controlled porosity, limited absorption characteristic, and low cost.
• 3- Membrane filters: These are basic tools for micro-filtration, useful in
the preparation of sterile solutions. These filters are made by casting of
various esters of cellulose, or from nylon, Teflon, polyvinyl chloride. The
filter is a thin membrane with millions of pores per square centimeter of filter
surface.
• 4-Porous plates: These include perforated metal or rubber plates, natural
porous materials such as stone, porcelain or ceramics, and sintered glass.

Filter Aid
• Usually, the resistance to flow due to the filter medium itself is very low,
but will increase as a layer of solids builds up , blocking the pores of the
medium and forming a solid cake.
• The object of the filter aid is to prevent the medium from becoming
blocked and to form an open, porous cake, so reducing the resistance to
flow of the filtrate. The particles must be inert, insoluble, incompressible,
and irregular shaped.
• Filter aids may be used in either or both two ways:
• 1-Pre- coating technique: by forming a pre-coat over the filter medium
by filtering a suspension of the filter aid .
• 2-Body- mix technique: A small proportion of the filter aid (0.1-0.5 %) is
added to the slurry to be filtered. This slurry is recirculated through the
filter until a clear filtrate is obtained, filtration then proceeds to completion.
• The following filter aids may be used:
• Diatomite ( Kieselguhr ) , obtained from natural siliceous deposites.
• Perlite , it is an aluminium silicate.
• Cellulose and Asbestos.

Industrial Filters
• Four groups may be listed:
• A- Gravity filters. B- Vacuum filters
• C- Pressure filters. D- Centrifugal filters.
• A-Gravity filters,
• Employing thick granular beds
are widely used in water
filtration e.g. Sand Filter

B- Vacuum filters
• Vacuum filters operate practically at higher pressure differentials than gravity filters.
• Rotary vacuum filter and the leaf filter are most extensively used.
• The leaf filter:
• The leaf filter is consisting of a frame enclosing a drainage screen or grooved plate ,
the whole unite being covered with filter cloth.
• The outlet for the filtrate connects to the inside of the frame, the general arrangement
is shown in the Fig. which represents a vertical section through
the leaf. The frame may be circular, square or rectangular shapes.
• The operation: The leaf filter is immersed in the slurry and
a receiver and a vacuum system connected to the filtrate outlet.
• Advantages:
• 1- The slurry can be filtered from any vessel.
• 2-The cake can be washed simply by immersing the filter
in a vessel of Water.
• 3- Removal of the cake is facilitated by the use of reverse
air flow.
.Fig. Filter leaf

4- The filter can be modified by employing
a suitable number of unites.
5- The leaf filter is most satisfactory
if the solids content of the slurry is not
too high, 5 % being a suitable maximum.
6- Labour costs for operating the filter are
comparatively moderate.
An alternative method is to enclose the filter
leaf in a special vessel into which the slurry is
pumped under pressure. A number of leaves
are connected to a common outlet, to provide
a large area for filtration e.g. Sweetland filter.

Rotary vacuum filter (Rotary filter)
• In large –scale operation, continuous operation is sometimes
desirable and it may be necessary to filter slurries containing a high
proportion of solids.
• The rotary filter is continuous in operation and has a system for
removing the cake that is formed , so, it is suitable for use with
concentrated slurries.
• It is a metal cylinder mounted horizontally,
the curved surface being a perforated plate,
supporting a filter cloth. Internally, it is
divided into several sectors and a separate
connection is made between each sector
and a special rotary valve.

• Operation: The drum is immersed to the required depth in the slurry, which
is agitated to prevent settling of the solids, and vacuum is applied to those
sectors of the drum which is submerged.
• A cake of the desired thickness is produced by adjusting the speed of
rotation of the drum. Each sector is immersed in turn in the slurry and the
cake is then washed and
partially dried by means of a current of air.
Finally, pressure is applied
under the cloth to aid the removal
of the cake.
Removal of the washed and
partially dried cake is affected
by means of a doctor knife.

• Summary of the process:
• The drum is dipped into the slurry and vacuum applied to the outlet,
which is connected to the filtrate receiver. When the cake has formed,
the cake drained or partially dried by vacuum.
• The drum is sprayed with water to wash the cake. Retaining the
vacuum connection drains the cake and produces partial dryness
then, removed by a doctor knife.
• When the solids of the slurry are too much that the filter cloth
becomes blocked with the particles, a pre-coat filter may be used.
A pre-coat of filter aid is deposited on the drum prior to the filtration
process.

Advantages & disadvantages of rotary drum filter
• Advantages:
• 1-The rotary filter is automatic and is continuous in operation, so that the labour costs
are very low.
• 2- The filter has a large capacity , so it is suitable for the filtration of highly
concentrated solutions.
• 3- Variation of the speed of rotation enables the cake thickness to be controlled.
• 4- Pre-coat of filter aid could used to accelerate the filtration rate.
• Disadvantages:
• 1- The rotary filter is a complex piece of equipment , with many moving parts and is
very expensive,.
• 2- In addition to the filter itself, some accessories are connected ,e.g, a vacuum
pump, vacuum receivers , slurry pumps and agitators are required .
• 3- The cake tends to crack due to the air drawn through by the vacuum system, so
that washing and drying are not efficient.
• 4- Being a vacuum filter, the pressure difference is limited to 1 bar and hot filtrates
may boil.
• 5- It is suitable only for straightforward slurries

• Uses:
• 1- The rotary filter for continuous operation on large quantities of
slurry.
2- Suitable for slurry contains considerable amounts of solids in the
range 15-30%.
• Examples of pharmaceutical application include the
collection of calcium carbonate, magnesium carbonate, and
starch, and the separation of the mycelium from the fermentation
liquor in the manufacture of antibiotics

String-discharge rotary drum filter

C- Pressure Filters
• C- Pressure Filters:
• Due to the formation of cakes of low permeability, many types of
slurry require higher pressure difference for effective filtration
than can be applied by vacuum techniques.
• Pressure filters are used for such operations.
• However, high operational pressures, may prohibit continuous
operation because of the difficulty of discharging the cake whilst
the filter is under pressure.
• Examples are the sweetland filter, plate and frame filter press.

Plate and Frame Filter Press
• This press is made up of two units, known respectively as plates
and frames, with a filter medium, usually filter cloth, between the
two.
• The frame is open, with an inlet for the slurry, while the plate has
grooved surface to support the filter cloth, and with an outlet for the
filtrate.
The operation
• The slurry enters the frame from the feed channel,
• The filtrate passes through the filter medium on to the surface of
the plate while the solids form a filter cake in the frame.
• The filtrate then drained down the surface of the plate , between the
projections on the surface and escapes from the outlet.
• Filtration is continued until the frame is filled with filter cake, when
the process is stopped , the frame emptied, and the cycle re-started.

• Channels for the slurry inlet and the filtrate outlet can be arranged by
fitting eyes to the plates and frames. This has the advantages that the
filtrate from each plate can be seen and, in the event of a broken cloth, the
faulty plate can be isolated and the filtration continued with one plate less.
• The thickness of the cake can be varied by using frames of different
thickness and, in general, there will be an optimum thickness of filter cake
for any slurry, depending on the solids content of the slurry and the
resistance of the filter cake.
• As filtration proceeds, the resistance of the cake increases and the filtration
rate will decrease. At a certain point it will be preferable in terms of the
overall output of the process, to stop and empty the press rather than to
continue filtration at a very low flow rate.
• Plates and frames may be made in various metals to provide
resistance to corrosion or prevent metallic contamination of the product.
Non-metals e.g. plastics is lighter, also varieties of wood are satisfactory
materials of construction.
• Plates and frames may be of considerable size, of about 1m square

Advantages &disadvantages
• Advantages:
• 1- Construction is very simple and a wide variety of materials can be
used.
• 2- It provides a large filtering area in a relatively small floor space.
• 3- It is versatile, the capacity being variable according to the thickness of
the frames and the number used.
• 4- The construction permits the use of considerable pressure difference.
• 5- Efficient washing of the cake is possible.
• 6- Operation and maintenance is straightforward , because there no
moving parts, filter cloths are easily renewable and, because all joints are
external, any leaks are visible and do not contaminate the filtrate.

Disadvantages
• 1- It is a batch filter, so it is a time consuming.
• 2- The filter press is an expensive filter, the emptying time, the
labour involved, and the wear and tear on the cloths resulting in high
costs.
• 3- Operation is critical, as the frames should be full, otherwise
washing is inefficient and the cake is difficult to remove.
• 4- The filter press is used for slurries containing less about 5 %
solids
• 5- In view of the high labour costs , it is most suitable for expensive
materials.e.g.the removal of precipitated proteins from insulin
liquors.

D- Centrifugal Filters
A centrifuge consists of a basket in which mixture of solid and liquid , or
mixture of two liquids is rotated at high speed so that it is separated into its
constituents by the action of centrifugal force.
• Types of baskets:
A- Imperforated, in which the liquid is removed through a skimming tube , while the
solid particles, sediment to the wall.
• In pharmacy, the centrifuge is commonly used for drying crystals and for
separating emulsions into their constituent liquids.
B- Perforated basket, in which the liquid passes out through the holes.
1-The perforated basket centrifuge:
• A vessel about 1m. in diameter and its outer wall is perforated. It is
mounted on a vertical shaft by means it can be rotated at a high speed. An
outer casing with an outlet collects the liquid thrown out from the basket.
• The drive motor may be below the centrifuge and it is called under-driven,
• Other form is over-driven,.

Advantages & Disadvantages:
• Advantages of a centrifuge:
• 1- It is very compact, occupying very little floor space,
• 2- It is capable of handling slurries with high proportions of solids .
• 3- The final product has generally, a very low moisture content if
compared to a filter cake of a similar material.
• Disadvantages:
• 1- Batch process
• 2- It involves a considerable labour cost, making the process
expensive.
• ....................Fig Perforated basket centrifuge....., Ass,p 38.

2-The pusher-type centrifuge
• This type of centrifuge is used for the separation of suspensions,
and is fitted with a perforated basket.
• The operation:
• The feed is introduced through a centrally located conical funnel,
and the cake is formed in the space between the flange and the
vertical base of the basket.
• A reciprocating pusher disc moves the formed cake along the
surface of the basket freeing the surface for further cake deposition.
• The pusher makes one stroke forward and backward, until a
further layer of solids is built up when a second stroke follows, and
so on. The filtrate passes through the holes of the basket and is
collected by suitable piping.
• In a second stage, a washing spray is admitted by a perforated
head.
• In a third stage, drainage, and partial drying of the cake takes place
after which the dry solid may be automatically collected.

• Advantages:
• 1- Continuously operated apparatus.
• 2-Thus reducing the coast of operation
• Disadvantages: The pusher piston mechanism adds to the initial
costs of the centrifuge.
• 3- The Tubular centrifuge ( Supercentrifuge)
• Principle of operation : High centrifugal effects can be obtained by
using a centrifuge of small diameter rotated at a high speed.
• Uses:
• 1- It can separate solids of small particle size from liquids.
• 2- It can be used to separate immiscible liquids from one
another.e.g. the two components of emulsion.
• 3- It can be used for filtration of very diluted suspensions i.e.
solutions containing very low concentration of solids.

• Advantages:
• 1- Due to the very high centrifugal speed ( 15.000- 60,000),
It can be used for clarification of much diluted solutions due to the
accelerated gravitational force.
• 2- On separation of two immiscible liquids , the centrifugal force will
form two layers, with the heavier liquid adjacent the wall.

The disc- Bowl Centrifuge:
Equipment selection:
• Ideally the equipment chosen should allow a fast filtration rate to minimize
production costs, be cheap to by and run, be easily cleaned and resistant to
corrosion, and be capable of filtering large volumes of products.
• There are a number of product – related factors that should
be considered when selecting a filter for a particulate
process.
These include:
1- The chemical nature of the product. Interactions with the filter medium may
lead to leaching of the filter components, degradation or swelling of the
filter medium or adsorption of components of the filtered product on the
filter. All of these may influence the efficiency of the filtration process or
the quality of the filtered product.
2- The volume to be filtered and the filtration rate required.
3- The operating pressure needed. This is governing the filtration rate .

• 4- The amount of material to be removed. Prefilters (decantation) may
be required or filter where the cake can be continuously removed.
• 5- The degree of filtration required. This affect the chosen pore size of
membrane filters or the filter grade to be used.
• 6- If sterility is required , then the equipment should itself be capable of
being sterilized, and must ensure that contamination does not occur after
the product has passed the filter.
• 7- The product viscosity and filtration temperature. A high product
viscosity may require elevated pressure to be used.

Application of solid/liquid filtration
1- Improvement of the appearance of solutions, mouth
washes, etc.....
• 2- Removal of potential irritants, e.g. from eye drop preparations or
solutions applied to mucous membranes.
• 3- Recovery of desired solid material from suspension or slurry ,e.g.
to obtain drug after crystallization process.
• 4- Certain operations, such as the extraction of vegetable drugs with
a solvent, may yield a turbid product with a small quantity fine
suspended colloidal matter; this can be removed by filtration.
• 5- Detection of microorganisms present in liquids, This can be
achieved by analyzing a suitable filter on which the bacteria are
retained .This method can also be used to assess the efficiency of
preservatives.

Filtration of fabric technical textile of engineering.ppt

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