This document discusses various types of filtration equipment and processes. It describes filtration, clarification, and some basic terminology related to filtration. It then covers different types of filtration like surface and depth filtration. Various factors affecting the rate of filtration are discussed. Different mechanisms of filtration like straining, impingement, and entanglement are described. The document also discusses filter media, materials used as filter media, and selection of filter media. Finally, it provides details on various industrial filters used in pharmaceutical industries like filter presses, filter leaves, rotary filters, and membrane filters.

1. -FILTRATION
-Filtration Equipment
-Filtration Equipment
-Dr Nisar Ahmed Arain
- Assistant Professor
-Anesthesia/Critical Care/ER

2. -How are you protecting
your patients from
CONTAMINATION
-Contamination by Bacteria, Viruses and Fungi

3. -HOW YOU KNOW THAT YOUR FILTER
FILTERS

4. -HOW YOU KNOW THAT YOUR FILTER
FILTERS

5. -CIRCUIT GUARD FILTERS
(example)

6. -COMPONENTS OF A GOOD FILTER

7. --ROUTES OF SPREAD OF INFECTION
AIR BORN

8. -Hundred per cent efficiency
against cross contamination

9. -DIRECTIONS OF USE

10. -DEFINITION
-FILTRATION
-It may be defined as a process of separation of
solids from a fluid by passing the same through
a porous medium that retains the solids but
allows the fluid to pass through
-CLARIFICATION
-When solids are present in very low
concentration that is not exceeding 1.0% w/v
(weight/ volume) the process of its separation
from liquid is called CLARIFICATION

11. -SOME BASIC TERMINOLOGY
USED UNDER THIS TOPIC
--SLURRY:-Suspension to be filtered
--FILTER MEDIUM:-Porous medium used to
retain solid
--FILTER CAKE:-Accumulated solids on the
filter
--FILTRATE:-Clear liquid passing through the
filter

12. -TYPES OF FILTERATION
-- SURFACE / SCREEN FILTERATION
--It is a screening action by which pores or holes
of medium prevent the passage of solids
-- DEPTH FILTERATION
--In this Slurry penetrates to a point where
the diameter of solid particles is greater
then that of the tortuous void or channel

13. -SURFACE FILTERATION
VS
DEPTH FILTERATION

14. -Difference between
SURFACE and DEPTH filtration

15. -FACTORS AFFECTING RATE OF FILTRATION
--1-SURFACE AREA
--2-TEMPERATURE
--3-VISCOSITY
--4-PRESURE DROP
--5-CONCENTRATION OF SLURRY
--6-PROPERTIES OF SOLID

16. --MECHENISM OF FILTRATION
--STRAINING:-
--Similar to sieving, i.e particles of larger size can’t
pass through smaller pore size of filtration medium.
--IMPINGEMENT:-
--Solids having the momentum move along the path of
streaming flow and strike(impinge) the filter medium.
Thus the solids are retained on the filter medium.
--ENTANGLEMENT:-
--Particles become entwined(entangled)in the masses
of fibers (of cloths with fine hairy surface or porous
felt) due to smaller size of particles then the pore size.
Thus solids are retained with in the filter medium
--ATTRACTIVE FORCES:-
--Solids are retained on the filter medium as a result of
attractive force between particles and filter medium, as
in case of Electrostatic filtration

17. --FILTER MEDIA
--The surface upon which solids are deposited in a filter is called
the “Filter Medium”
--PROPERTIES OF FILTER MEDIUM:- It should
--1-Be capable of delivering a clear filtrate at a suitable
production rate.
--2-Have a sufficient mechanical strength
--3-Benefit
--4-Retain the solids without plugging at the start of
filtration

18. --5-Not absorb dissolved material.
--6-Sterile filtration imposes a special requirement since the
pore size must not exceed the dimension of Bacteria or
Spores.
--SELECTION OF THE FILTER MEDIA DEPENDS ON THE FOLLOWING
--1-Size of the particle to be filtered
--2-Amount of liquid to be filtered
--3-Nature of product to be filtered
--4-Purpose of filter
-PROPERTIES OF FILTER MEDIUM:- CONT.

19. -MATERIAL USED AS FILTER MEDIA
-FILTER PAPER
--Filter paper is common filter medium
since it offers controlled porosity,
limited absorption characteristic and
low cost
--It has different grades and qualities
different pore size such as
COARSE, MEDIUM, and FINE
DISADVANTAGES
--They shed very fine particle to the
filtrate
--Absorb small quantity of liquid

20. --WOVEN MATERIAL
-Woven wire cloth
--It is made from stainless steel
--It can be easily cleaned
--Long lasting
--It is resistant to the chemicals
-Nylon cloth
--It is superior to the cotton cloth
--It is not affected by Molds, Fungus, and Bacteria
--Has negligible absorption properties
--It is extremely strong as compared to cotton cloth

21. -COTTON WOOL
--Commonly used
--Small tough of cotton wool placed
in the neck of funnel
-GLASS WOOL
--Use for filtering highly corrosive chemicals
--May contaminate the filtrate with glass fibers

22. -ASBESTOS
--Also used for filtering the corrosive liquid
--They impart alkalinity to the filtrate.
--Alkaloids may get absorbed.
--May contaminate the filtrate

23. --MEMBRANE FILTER
--These are very common among
the ultra filtration methods
--Made up of cellulose, polyvinylchloride
Nylon and other cellulose derivatives
--They are very fine having a very wide
range of pore size from 8 Micron to 0.22
Micron

24. -PORE SIZE IN MICRON// PARTICLES REMOVED
--0.2 All Bacteria
--0.45 All Choliform group bacteria
--0.8 All air born particles
--1.2 All Non living particles
considered dangerous
in IV Fluid
--5 All significant cell from body
fluids
ADVANTAGES
--Bacteria are removed by sieving
--Absorption of Medicament is negligible
--In every new operation, a new disc is used
--Filtration is quite rapid
--Don’t liberate particles to the filtrate

25. DISADVANTAGES
--Fine pores may get clogged easily
--Soluble in certain organic solutions
e.g ketones and esters
--Very brittle when dry
SINTERED GLASS
--Consists of Pyrex glass powder
--Used for filtering parenteral
preparations.
--Useful for filtering the corrosive
liquid and oxidizing agent.
--Don’t shed particles.
--Don’t absorbs any liquid.
--Can be easily washed.

26. -OTHER FILTERS
--1-SAND FILTERS
--It consists of large bed of properly proportioned layers
of sand, stone and gravel. Used in large scale operations
such as municipal purification of drinking water
--2-BERKEFELD AND CHAMBERLAND FILTERS
---It is hollow cylinder or candle made up of unglazed porous
porcelain or diatomaceous earth
--3-SEITZ FILTER
--They are specially prepared of asbestos filters
--All these three types of filter required use of vacuum
for efficient filtration

27. -FILTER AIDS
--The substance which when added to the liquid
to be filtered reduce the resistance of the filter
cake and increase the filtration
--The objective of Filter aid is to prevent the
medium from becoming blocked and to form
an open, porous cake, hence reducing the
resistance to flow of the filtrate.
--Filter aid forms a surface deposit which screens
out the solids and also prevents the plugging of
the supporting filter medium

28. -PROPERTIES OF FILETR AIDS
--Chemically inert
--Light in weight
--Low specific gravity
--Insoluble I liquids
--Forms a porous cake
--Free from impurities
--Suitable particle size with irregular shape
--Able to remain suspended in liquids
--Free from moisture

29. -DISADVANTAGES
--Removed the coloured substances by absorbing
them
--Sometimes active principals such as alkaloids are
absorbed on filter aid
--Rarely filter aids are source of contamination such
as soluble Iron salts, which can provoke
degradation of sensitive ingredients
-EXAMPLES OF FILTER AIDS
--Diatomite(keiselgur)
-- Perlite, Cellulose, Asbestos, Charcoal, Talc,
Bentonite fullers earth etc.

30. -HANDLING OF FILTER AIDS
1--USE OF PRE-COAT OF FILTER AID
--Filter aid is used as Pre-coat or layer of filter aid is
applied before the material is poured or pumped
to the apparatus
--It prevents the colloidal particles from becoming
entangled in to filter media / filter cloth so
resistance of filter cloth becomes high
2--INCORPORATION OF MATERIAL
--Incorporation of certain percentage of filter aid is
added to the material before filtration
--Presence of filter aid increases the porosity of cake
and decreases its compressibility, reduces the
resistance of the cake during filtration process

31. 3-- USE OF PRE-COAT FOR SPECIAL FILTERS
--This is specially for ROTATORY drum filter with vacuum.
Slurry of filter aid is fed to the filter until pre-coat is laid
down than slurry / material to be filtered is fed

32. 1—Purpose of filtration
--Collection of solids after washing
--Collection of Filtrate
--Removal of Dust particles from air
--Removal of micro-organism from
air / Liquid
2—Condition of Filtration
--Pore size
--Chemical compatibility
--Maximum operating temperature
--Concentration of solid
--Characteristics of Filters
3—Filtration Cycle
-FACTORS AFFECTING
selection of filters

33. -THEOERIES OF FILTRATION
---Rate of any reaction can be defined as Rate =
Driving force / Resistance
---The Rate of filtration is expressed in terms of
Volume and time and time (dv / dt)
---Here for rate of filtration driving force is pressure
difference between upstream and down stream
and resistance is deposition of filter cake
---Resistance is not constant for filtration process
because it increases with increase in deposition
of solids

34. --The rate of flow will be greatest at the beginning of
filtration because the resistance is minimum as the
deposition increases resistance to flow increases

35. --Filter Press
--Filter Leaf
--Rotatory Filter / Rotatory Drum Filter
--Edge Filter / Meta Filter
--Cartridge Filter
--Membrane Filter
-Industrial filters used in
Pharmaceutical industries

36. -PRINCIPLE
--Mechanism is surface filtration.
--The slurry enters the frame by pressure and flows
through filter medium
--The Filtrate is collected on the plates and send to
outlet
--A number of frames and plates are used so that
surface area increases and consequently large
volumes of slurry can be processed
simultaneously with or without washing
-1-Plate and frame filter press

37. -Plate and frame filter press

38. --CONSTRUCTION
--The Filter press is made of two type of
units, plate and frames. Usually made
of aluminium alloy
--1)-Frame
--It contains a open space inside where in
the slurry reservoir is maintained for
filtration and an inlet to receive the slurry.
--It is indicated by two dots in the
description
--Frames of different thickness are available.
It is selected based on the thickness of
cake formed during filtration.
-SLURRY INLET

39. --The plate has a studded or grooved surface
to support the filter cloth and an outlet
--It is indicated by one Dot in description
--Plate supports the filter medium, receiving
the filtrate and outlet
a-The filter medium usually cloth is interposed
between plate and frame
b-Plate, Filter medium, Frame, filter medium
and plate are arranged in sequence and
clamed to a supporting structure
c-A number of Plates and Frames are employed
so that the filtration area is as large as
necessary. Number of filtration units are
operated in parallel
--2-PLATE:- --Through Channel
--Filtrate Outlet

40. --Channels for slurry inlet and filtrate outlet
can be arranged by fitting eyes to the
plates and Frames, these join together
to form a channel
--In some types only one inlet channel is
formed, while each plate is having
individual outlets controlled by valves

41. -WORKING
--
Slurry enters the frame
from the feed channel
andpasses through the
filter medium on the
surface of theplate
The solid forms a filter cake
and remain in the frame
The thickness of the cake
is half of the frame
thickness, because on
each side of frame
filtration occurs
As filtration proceeds,
the resistance of the
cake increases and
filtration rate decrease
The filtrate drains between
theprojections of the
surface of the plate and
escape from the outlet
Thus two filter cakes are
formed , which meet
eventually in the center
of the frame
At a certain point
process is stopped and
press is emptied and
cycle is restarted
-Working can be divided into two steps
-FILTRATION OPERATION

42. -2)WASHING OPERATION
---STEP-1
--Filtration proceeds in the ordinary way until the frames are filled with cake
---STEP-2
--To wash the filtrate cake, the outlets of washing plates are closed
---STEP-3
--Wash water is pumped in the washing channel
--The water enters through the inlets on the surface of washing plate
---STEP-4
--Water passes through the filter cloth and enters in the frame which contains the cake
--The water washes the cake, passes through the filter cloth and enters the plate
down the surface
---STEP-5
--Finally washed water escapes through the outlet of the plate

43. -ADVANTAGES
--Construction of filter press is very simple and variety of
materials can be used
a-Cast Iron---for handling common substances
b-Bronze-----for small units
c-Stainless steel---Contamination can be avoided
d-Hard rubber and plastic---used where metals can be avoided
e-Wood---for lightness though it must be kept wet
--Provide large filtration area in relatively small floor space.
The capacity being variable according to thickness of frames
and number used.
--Sturdy construction permits the use of considerable pressure
difference. (2000 Kilo-pascals normally used)
--Efficient washing of cake is possible.
--Operation and maintenance is easy
--It produce dry cake in form of slab.

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

45. 2-FILTER LEAF
PRINCIPLE:-
--It is an apparatus consisting of a longitudinal drainage screen
covered with a filter cloth.
--The mechanism is surface filtration and acts as sieve or strainer
--vacuum or pressure can be applied to increase the rate of
filtration
CONSTRUCTION:-
--The leaf filter is consisting of a frame enclosing a drainage screen
or grooved plate
--The frame may be of any shape Circular, Square, or Rectangular
--The whole unit being covered with filter cloth
--The outlet for the filtrate connects to the inside of the frame
through suction

46. --FILTER LEAF process

47. -WORKING
-STEP-1
--The filter leaf
is immersed in
the slurry
-STEP-2
--Vacuum
system is
connected to
the outlet
--STEP-3
--The slurry
passes
through the
filter cloth
--STEP-4
--Finally filtrate
enters the drainage
canal and goes
through the outlet
into the receiver
--STEP-5
--Air is passed to
flow in reverse
Direction which
facilitates
removal of cake

48. -ADVANTAGES
--Simplest form of filter used for batch process.
--A number of units can be connected in parallel to increase the surface
area of filtration
--Pressure difference can be obtained either with vacuum or using
pressure upto the order of 800 Kilopascals
--Labour cost for operating the filter leaf are fairly moderate
--The efficiency of washing is high
--The slurry can be filtered from any vessel
--The cake can be washed simply by immersing the filter in a vessel of
water.
USES:-
--Use for the filtration of slurry which do not contain high solid content,
about 5% i.e. dilute suspensions

49. --3-SWEET LAND FILTER
Variant of filter leaf
--An alternative method is to enclose the filter leaf in a special vessel in which the slurry is
pumped under pressure
--A number of leaves are connected to a common outlet, to provide a large area for filtration

50. -4-META-FILTER
-PRINCIPLE
--Mechanism is surface filtration
--In this, metal rings contain semi-circular
projections, which are arranged as a nest
to form channels on the edges
--This channel offers resistance (strainer) to
the flow of solids (coarse particles)
--The clear liquid is collected into receiver
from the top

51. -META-FILTER

52. -CONSTRUCTION
--Metafilter consists of a series of metal rings. These are threaded
so that a channel is formed on the edges
--It contains a grooved drainage column on which a series of metal
rings are packed
--These rings are usually made up of stainless steel and have
dimensions of about 15.0 mm internal diameter and 22.0 mm
external diameter
--Each metal ring has a series of metal ring projections (0.8 mm in
thickness) on one side of surface
--The projections are arranged as a nest to form channels on the
edges
--These rings are tightened on the drainage column with a nut.

53. -WORKING
--Filters are
placed in a
vessel
--Slurry is pumped
under pressure/
occasionally by
applying reduced
pressure to the
outlet side
--Slurry passes
through the
channels formed on
the edges between
the rings
---The clear liquid
rises up and
collected from the
outlet into receiver
--For separation of fine particles, a bed of suitable materials such as Kieselguhr is first built up
--The pack of rings serves essentially as a base on which the true filter medium is supported

54. -ADVANTAGES
---It can be used under high pressure without any danger of
bursting the filter medium
--Running cost is low, as separate medium is not used
--It can be constructed from a material that can provide
excellent resistance to corrosion and avoid contamination
of sensitive products
--It is extremely versatile filter because it is fine as well as
large both type of particles can be separated
--Removal of cake can be carried out by simply back-flushing
with water
--Change over from one batch to another or one product to
another is easy
--Sterile products can be easily handled

55. --USES
METAFILTERS CAN BE USED FOR
--Clarifications of syrups
--Filtration of injection solutions
--Clarification of insulin liquors
--Filtration of viscous liquids can be achieved by
applying pressure

56. -5-CARTRIDGE FILTER
-PRINCIPLE
--It is thin porous membrane in which pre-filter and membrane filter are
combined in a single unit
--The filtration action is mainly sieve like and particles are retained on
the surface
-CONSTRUCTION
--It has cylindrical configuration made with disposable or changeable
filter media
--Made up of either Plastic or Metal
--Consists of two membrane filters(sieve like) made of polypropylene
Pre-Filter and actual filter for filtration
--A protective layer surrounds them
--The cartridge are housed in a holder and a number of cartridges
can be placed in a same housing
--The housing is closed with the lid.
--Housing has provisions for slurry inlet and outlets

57. -CARTRIDGE FILTER

58. -WORKING
--Slurry is pumped into cartridge holder
--It passes through cartridge filter unit by straining
--The clear liquid passes through the center
--Moves upto collect through outlet
USES
--Particularly useful for preparation of particulate free
solutions for Parenteral and Opthalmic uses
--This filter holder will process 1000 – 15000 liters of
sterile solution per hour

59. -ADVANTAGES
--Autoclaving can be done for sterile operations due to
stainless steel construction
--Cartridge with self cleaning devices are advantageous
--Rapid dis-assembling as well as re using of filter medium
is possible
--Cartridges are not brittle, when they are dry
--Used as inline continuous filtration, which reduces
handling of solutions. It minimizes chances of
contaminations

60. -DIS-ADVANTAGES
--A number of manufacturers provide he components
which are generally not interchangeable between
suppliers
-- Cost of disposable elements offsets the labour saving
in terms of assembly and cleaning of cartridge
clarifiers

61. -6-ROTARY DRUM FILTER
PRINCIPLE
--Slurry filtered through sieve like mechanism on the rotation
drum surface, under the condition of vacuum
--In addition compression, drying(using hot air)and removing
the filter cake (using knife) are possible
CONSTRUCTION
--It consists of a metal cylinder mounted horizontally.
--The drum may be upto 3 meters in Diameter and 3.5 meters
in length and gives surface area of 20 meters square
--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
rotatory valve

62. -ROTARY DRUM FILTER

63. -WORKING
--The Drum is dipped into the slurry and vacuum is
applied to the outlet, which is connected to the
filter 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

64. -USES
--The Rotatory filter for continuous operation
on large quantities of slurry
--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.
--The separation of the mycelium from the
fermentation liquor in the manufacture
of Antibiotics

65. -ADVANTAGES
--The Rotatory Filter is automatic and is
continuous in operation so that the
labour costs are very low
--The filter has a large capacity, so it is
suitable for the filtration of highly
concentrated solutions
--Variation of the speed of rotation
enables the cake thickness to be
controlled
--Pre-coat of filter aid could be used to
accelerate the filtration rate
--Filter has a large surface area

66. -DISADVANTAGES
--The Rotatory filter is a complex piece of equipment
with many moving parts and is very expensive.
--In addition to the filter itself, some accessories are
also connected to it e.g
a-A vacuum pump
b-Vacuum receiver
c-Slurry pumps and
d-Agitators are required
The cake tends to crack due to the air drawn through
by the vacuum system so that washing and Drying
are not efficient
--Being a vacuum filter, the pressure difference is
limited to 1 bar and Hot filters may boil
--It is suitable only for straight-forward slurries

67. - THANK YOU

69. -4-METAFILTER
-PRINCIPLE:-
--Mechanism is surface filtration
--In this the metal rings contains the semi-circular
projections, which are arranged as a nest to form
channels on the edges
--This channel offers resistance (strainer) to the flow
of solids (coarse particles)
--The clear liquid is collected into receiver from the top