Pharmaceutical Engineering: Drying
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Sep 30, 2020
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About This Presentation
Objective, mechanism of drying, moisture content, rate of drying curve, tray dryer, drum dryer, spray dryer, fluidized bed dryer, vacuum dryer, freeze dryer
Slide Content
DRYING
Parag Jain
Assistant Professor
Chhattrapati Shivaji Institute
of Pharmacy
Durg, Chhattisgarh
Presented by
Parag Jain
Assistant Professor
Chhattrapati Shivaji Institute
of Pharmacy
Durg, Chhattisgarh
Presented by
Drying
•Drying is commonly the last stage in a manufacture
process.
•Drying is the final removal of water from material
(usually by heat)
•Non-thermal drying
•As Squeezing wetted sponge
•Adsorption by desiccant (desiccation)
•Extraction
•Drying is commonly the last stage in a manufacture
process.
•Drying is the final removal of water from material
(usually by heat)
•Non-thermal drying
•As Squeezing wetted sponge
•Adsorption by desiccant (desiccation)
•Extraction
Importance
•To avoid or eliminate moisture which may lead to
corrosion and decrease the product or drug stability.
•To improve or keep the good properties of a material, e.g.
Flowability, compressibility.
•To reduce the cost of transportation of large
volume materials ( liquids).
•To make the material easy or more suitable for handling.
•Preservation.
•The final step in Evaporation, Filtration, Crystallization.
•To avoid or eliminate moisture which may lead to
corrosion and decrease the product or drug stability.
•To improve or keep the good properties of a material, e.g.
Flowability, compressibility.
•To reduce the cost of transportation of large
volume materials ( liquids).
•To make the material easy or more suitable for handling.
•Preservation.
•The final step in Evaporation, Filtration, Crystallization.
Rate of drying in a bed of powder:
•The rate at which drying occurs has been found to
show certain phases in which the change in moisture
content is plotted against time. From A to the
relationship is linear, which is known as the constant-
rate period, whereas from B to C the rate of loss of
moisture decreases and is known as the falling-rate
period. The end of the constant rate period, B, is
referred to as the critical moisture content.
•The rate at which drying occurs has been found to
show certain phases in which the change in moisture
content is plotted against time. From A to the
relationship is linear, which is known as the constant-
rate period, whereas from B to C the rate of loss of
moisture decreases and is known as the falling-rate
period. The end of the constant rate period, B, is
referred to as the critical moisture content.
- The first falling- rate period
has a linear relationship, that
is , the decrease in drying
rate is uniform, whereas in
the second falling-rate
period there is a continuous
decrease in the rate of
drying until the EMC is
reached.
has a linear relationship, that
is , the decrease in drying
rate is uniform, whereas in
the second falling-rate
period there is a continuous
decrease in the rate of
drying until the EMC is
reached.
•Constant-rate period: It is found that the evaporation
rate from the drying bed is similar to that of the solvent
alone from a free liquid surface under the same
conditions, indicating that the evaporation takes place
from the wet surface of the solid, and that the surface
remains wet in this period as a result of the liquid
being replaced from below as fast as it is vaporized
Controlling factors in this period are the rate at which
heat can be transferred and the rate of removal of the
vapour.
rate from the drying bed is similar to that of the solvent
alone from a free liquid surface under the same
conditions, indicating that the evaporation takes place
from the wet surface of the solid, and that the surface
remains wet in this period as a result of the liquid
being replaced from below as fast as it is vaporized
Controlling factors in this period are the rate at which
heat can be transferred and the rate of removal of the
vapour.
•First falling-rate period: As moisture is removed from the
surface, a point will be reached when the rate of
vaporization is insufficient to saturate the air in contact with
the surface. Under these conditions, the rate of drying will
be limited by the rate of capillary transfer of the liquid to the
surface of the wet bed, and this becomes increasingly
difficult as the bed dries, the solvent level decreases and
thus has further to travel to the point of evaporation.
Consequently, the rate of drying decreases continuously.
surface, a point will be reached when the rate of
vaporization is insufficient to saturate the air in contact with
the surface. Under these conditions, the rate of drying will
be limited by the rate of capillary transfer of the liquid to the
surface of the wet bed, and this becomes increasingly
difficult as the bed dries, the solvent level decreases and
thus has further to travel to the point of evaporation.
Consequently, the rate of drying decreases continuously.
•Second falling-rate period: Any moisture that remains
within the drying bed at the end of the first falling –rate
period is unable to move, so that drying cannot take place
on the surface. i.e. the drying rate depends on the
movement of the vapour through the pores of the bed to
the surface, in general by molecular diffusion
within the drying bed at the end of the first falling –rate
period is unable to move, so that drying cannot take place
on the surface. i.e. the drying rate depends on the
movement of the vapour through the pores of the bed to
the surface, in general by molecular diffusion
Dryers for Solid Materials
Moisture content of wet solids
•The moisture content of a wet solid is expressed as
kilograms of moisture associated with 1 kg of the
moisture – free solid. Thus a moisture content of
0.4 means that 0.4 kg of removable water is
present per kg of the solid. It is sometimes
calculated as percentage moisture content.
Moisture content of wet solids
•The moisture content of a wet solid is expressed as
kilograms of moisture associated with 1 kg of the
moisture – free solid. Thus a moisture content of
0.4 means that 0.4 kg of removable water is
present per kg of the solid. It is sometimes
calculated as percentage moisture content.
•Total moisture content: This is the total amount of
liquid associated with a wet solid. The easily
removable water is known as the free moisture
content, and the moisture which is more difficult
to remove is the equilibrium moisture content.
The easily removable water is known as
unbound water.
•Unbound water: This water exists as a liquid and
exerts its fully vapour pressure, it can be removed
readily by evaporation. During a drying process
this water is easily lost but the resulting solid is
not completely free from water molecules.
liquid associated with a wet solid. The easily
removable water is known as the free moisture
content, and the moisture which is more difficult
to remove is the equilibrium moisture content.
The easily removable water is known as
unbound water.
•Unbound water: This water exists as a liquid and
exerts its fully vapour pressure, it can be removed
readily by evaporation. During a drying process
this water is easily lost but the resulting solid is
not completely free from water molecules.
Equilibrium moisture content:
•The moisture content present in a solid under steady-
state ambient conditions is termed the eq. moisture
content. Its value changes with temperature, humidity
and the nature of the solid.
Bound water:
•Part of the moisture present in a wet solid may be
adsorbed on surfaces of the solid or be adsorbed
within its structure to such an extent to prevent it from
developing its full vapour pressure and from being
easily removed by evaporation. Such moisture is
described as “bound” and is more difficult to remove
than unbound water.
•The moisture content present in a solid under steady-
state ambient conditions is termed the eq. moisture
content. Its value changes with temperature, humidity
and the nature of the solid.
Bound water:
•Part of the moisture present in a wet solid may be
adsorbed on surfaces of the solid or be adsorbed
within its structure to such an extent to prevent it from
developing its full vapour pressure and from being
easily removed by evaporation. Such moisture is
described as “bound” and is more difficult to remove
than unbound water.
•Equilibrium moisture content:
•The moisture content present in a solid under steady-state ambient
conditions is termed the eq. moisture content. Its value changes with
temperature, humidity and the nature of the solid.
•Bound water :
• Part of the moisture present in a wet solid may be adsorbed on
surfaces of the solid or be adsorbed within its structure to such an
extent to prevent it from developing its full vapour pressure and from
being easily removed by evaporation. Such moisture is described as
“bound” and is more difficult to remove than unbound water.
•The moisture content present in a solid under steady-state ambient
conditions is termed the eq. moisture content. Its value changes with
temperature, humidity and the nature of the solid.
•Bound water :
• Part of the moisture present in a wet solid may be adsorbed on
surfaces of the solid or be adsorbed within its structure to such an
extent to prevent it from developing its full vapour pressure and from
being easily removed by evaporation. Such moisture is described as
“bound” and is more difficult to remove than unbound water.
Equipments
1.Drum dryer (Film drying)
2.Spray dryer
3.Freeze Dryer
4.Tray drier
5.Fluidized Bed Dryer
6.Vacuum Dryer
1.Drum dryer (Film drying)
2.Spray dryer
3.Freeze Dryer
4.Tray drier
5.Fluidized Bed Dryer
6.Vacuum Dryer
Drum dryer
(Roller dryer/Film drum dryer)
Principal:
•Material on drum & dried.
Construction:
•Hollow steel Drum
•Feed pan
•Spreader
•Doctor’s knife
•Storage bin (A conveyor)
(Roller dryer/Film drum dryer)
Principal:
•Material on drum & dried.
Construction:
•Hollow steel Drum
•Feed pan
•Spreader
•Doctor’s knife
•Storage bin (A conveyor)
Drum Dryer (Film Drying)
•It consists of a drum of about 0.75-1.5 m in diameter
and 2-4 m in length, heated internally, usually by steam
and rotated on its longitudinal axis.
•Operation: The liquid is applied to the surface and
spread to a film, this may be done in various ways, but
the simplest method is that shown in the diagram, where
the drum dips into a feed pan.
•Drying rate is controlled by using a suitable speed of
rotation and the drum temperature. The product is
scraped from the surface of the drum by means of a
doctor knife.
•It consists of a drum of about 0.75-1.5 m in diameter
and 2-4 m in length, heated internally, usually by steam
and rotated on its longitudinal axis.
•Operation: The liquid is applied to the surface and
spread to a film, this may be done in various ways, but
the simplest method is that shown in the diagram, where
the drum dips into a feed pan.
•Drying rate is controlled by using a suitable speed of
rotation and the drum temperature. The product is
scraped from the surface of the drum by means of a
doctor knife.
Working:
•Steam in drum- drum is rotated – through
feed pan.
•Material adhere to pan- thin layer form.
•Material dry during rotation.
•Doctor’s knife- Dry material is scrap –fall in
storage bin.
Application:
•For drying- solutions, slurries, Suspensions,
milk products, starch products, antibiotics,
various substances etc,.
•Steam in drum- drum is rotated – through
feed pan.
•Material adhere to pan- thin layer form.
•Material dry during rotation.
•Doctor’s knife- Dry material is scrap –fall in
storage bin.
Application:
•For drying- solutions, slurries, Suspensions,
milk products, starch products, antibiotics,
various substances etc,.
Advantages
•1- The method gives rapid drying, the thin film spread over a
large area resulting in rapid heat and mass transfer.
•2- The equipment is compact, occupying much less space
than other dryers.
•3- Heating time is short, being only a few seconds.
•4- The drum can be enclosed in a vacuum jacket, enabling
the temperature of drying to be reduced.
•5- The product is obtained in flake form, which is convenient
for many purposes.
•The only disadvantage : is that operating conditions are
critical and it is necessary to introduce careful control on
feed rate, film thickness, speed of drum rotation and drum
temperature.
•1- The method gives rapid drying, the thin film spread over a
large area resulting in rapid heat and mass transfer.
•2- The equipment is compact, occupying much less space
than other dryers.
•3- Heating time is short, being only a few seconds.
•4- The drum can be enclosed in a vacuum jacket, enabling
the temperature of drying to be reduced.
•5- The product is obtained in flake form, which is convenient
for many purposes.
•The only disadvantage : is that operating conditions are
critical and it is necessary to introduce careful control on
feed rate, film thickness, speed of drum rotation and drum
temperature.
Spray dryer
Principal:
•Material to fine droplets- moving stream of
hot gas.
Construction:
•Large cylindrical drying chamber.
•Inlet of hot air & atomizer- In Roof.
•Connected to a cyclone separator.
Principal:
•Material to fine droplets- moving stream of
hot gas.
Construction:
•Large cylindrical drying chamber.
•Inlet of hot air & atomizer- In Roof.
•Connected to a cyclone separator.
Spray Dryer
•The spray dryer provides a large surface area for heat
and mass transfer by atomizing the liquid to small
droplets.
•These are sprayed into a stream of hot air, so that each
droplet dries to a solid particle.
•The drying chamber resembles the cyclone ensuring
good circulation of air, to facilitate heat and mass
transfer, and that dried particles are separated by the
centrifugal action.
•Spray dryer can be operated efficiently at various feed
rates.
•The spray dryer provides a large surface area for heat
and mass transfer by atomizing the liquid to small
droplets.
•These are sprayed into a stream of hot air, so that each
droplet dries to a solid particle.
•The drying chamber resembles the cyclone ensuring
good circulation of air, to facilitate heat and mass
transfer, and that dried particles are separated by the
centrifugal action.
•Spray dryer can be operated efficiently at various feed
rates.
Spray Dryer
Working:
1.Atomization of the liquid: Liquid feed- into
chamber through atomizer.
2.Drying of liquid droplets: Due to hot air
drying.
3.Recovery of dried product: Recovery in last
step.
Application:
•For drying of large quantity material.
•Drying of thermo-labile, hygroscopic material.
•Drying of medicine like chloramphenicol.
1.Atomization of the liquid: Liquid feed- into
chamber through atomizer.
2.Drying of liquid droplets: Due to hot air
drying.
3.Recovery of dried product: Recovery in last
step.
Application:
•For drying of large quantity material.
•Drying of thermo-labile, hygroscopic material.
•Drying of medicine like chloramphenicol.
Advantages
•The droplets are small, giving a large surface area for
heat transfer, so that evaporation is very rapid. The
actual drying time of a droplet is only a fraction of a
second, and the overall time in the dryer is only a few
seconds.
•Because evaporation is very rapid, the droplets do not
attain a high temperature, most of the heat being used
as latent heat of vaporization.
•The characteristic particle form gives the product a
high bulk density and, in turn, ready solubility.
•The powder will have a uniform and controllable
particle size.
•The droplets are small, giving a large surface area for
heat transfer, so that evaporation is very rapid. The
actual drying time of a droplet is only a fraction of a
second, and the overall time in the dryer is only a few
seconds.
•Because evaporation is very rapid, the droplets do not
attain a high temperature, most of the heat being used
as latent heat of vaporization.
•The characteristic particle form gives the product a
high bulk density and, in turn, ready solubility.
•The powder will have a uniform and controllable
particle size.
Disadvantages
•The equipment is very bulky, connected to accessories, fans, heaters,)
•That is make it expensive.
•Uses:
•1- Drying of any substance in solution or in suspension form
•2- It is most useful for drying of thermo labile materials e.g. antibiotics.
•3- Suitable for large quantities solution.
•4- Suitable for both soluble and insoluble substances e.g. citric acid,
gelatin, starch.
•5- It can produce spherical particles in the respiratory range e.g. dry
powder inhalers.
•6- Drying of milk, soap and detergents which is pharmaceutically
related compounds.
•The equipment is very bulky, connected to accessories, fans, heaters,)
•That is make it expensive.
•Uses:
•1- Drying of any substance in solution or in suspension form
•2- It is most useful for drying of thermo labile materials e.g. antibiotics.
•3- Suitable for large quantities solution.
•4- Suitable for both soluble and insoluble substances e.g. citric acid,
gelatin, starch.
•5- It can produce spherical particles in the respiratory range e.g. dry
powder inhalers.
•6- Drying of milk, soap and detergents which is pharmaceutically
related compounds.
Freeze Dryer
•Freeze drying is a process used to dry extremely heat-
sensitive materials. It allows the drying , without excessive
damage, of proteins, blood products and even
microorganisms, which retain a small but significant
viability.
•In this process the initial liquid solution or
suspension is frozen, the pressure above the frozen state
is reduced and the water removed by sublimation.
•Thus a liquid-to-vapour transition takes place, but here
three states of matter involved: liquid to solid, then
solid to vapour.
•Freeze drying is a process used to dry extremely heat-
sensitive materials. It allows the drying , without excessive
damage, of proteins, blood products and even
microorganisms, which retain a small but significant
viability.
•In this process the initial liquid solution or
suspension is frozen, the pressure above the frozen state
is reduced and the water removed by sublimation.
•Thus a liquid-to-vapour transition takes place, but here
three states of matter involved: liquid to solid, then
solid to vapour.
Freeze dryer
(Lyophilization)
Principal:
•Drying by sublimation-triple point- temp. &
pressure below triple point.
Construction:
•Drying chamber in trays.
•Heating coils.
•Vapor condensing or adsorption system with
refrigerator.
•Vacuum pump.
(Lyophilization)
Principal:
•Drying by sublimation-triple point- temp. &
pressure below triple point.
Construction:
•Drying chamber in trays.
•Heating coils.
•Vapor condensing or adsorption system with
refrigerator.
•Vacuum pump.
Door
Condenser
Vacuum
pump
Shelves
Heating
System
Refrigerator
Fig. Industrial freeze dryer
Drying
chamber
Condenser
Vacuum
pump
Shelves
Heating
System
Refrigerator
Fig. Industrial freeze dryer
Drying
chamber
Working:
1.Preparation & pretreatment: vacuum ay vacuum
tray dryers
2.Pre-freezing for solidifying water: cold (-50oC)
3.Primary drying (Sublimation of ice under
vacuum): at 0.0098oC & 0.533 kilopasals.
temperature is increased to 300C within 2 hours.
Then temperature kept constant. around 98 to 99%
water is removed.
4.Secondary drying (Removal of moisture at high
vacuum): temp as 50 to 60oC & low vacuum.
5.Packing: air replace with gas and seal.
1.Preparation & pretreatment: vacuum ay vacuum
tray dryers
2.Pre-freezing for solidifying water: cold (-50oC)
3.Primary drying (Sublimation of ice under
vacuum): at 0.0098oC & 0.533 kilopasals.
temperature is increased to 300C within 2 hours.
Then temperature kept constant. around 98 to 99%
water is removed.
4.Secondary drying (Removal of moisture at high
vacuum): temp as 50 to 60oC & low vacuum.
5.Packing: air replace with gas and seal.
Application:
•For production of dosage forms as injections,
solutions, suspensions.
•For drying of Blood plasma and its
fractionated products, Bacterial & viral
cultures, Human tissue, Antibiotics, Steroids,
Food items (Prawns etc)
•For production of dosage forms as injections,
solutions, suspensions.
•For drying of Blood plasma and its
fractionated products, Bacterial & viral
cultures, Human tissue, Antibiotics, Steroids,
Food items (Prawns etc)
Advantages :
•Suitable for thermo-labile material.
•Loss of volatile is less.
•No migration occurs.
•Suitable for moisture sensitive material.
•Sterility maintain
Disadvantages:
•High costs.
•Time consuming.
•Oxidation may occurs.
•Suitable for thermo-labile material.
•Loss of volatile is less.
•No migration occurs.
•Suitable for moisture sensitive material.
•Sterility maintain
Disadvantages:
•High costs.
•Time consuming.
•Oxidation may occurs.
TRAY DRYER
(TRAY DRYER / TRUCK DRYER / SHELF DRYER / CABINET DRYER /
COMPARTMENT DRYER )
Principal:
•Hot air- Circulation.
Construction:
•Small or a large cabinet insulated (to reduce
heat loss) compartment in which trays.
•Heater- Heating of air
•Fan: Circulate the air
•Inlet & Outlet.
(TRAY DRYER / TRUCK DRYER / SHELF DRYER / CABINET DRYER /
COMPARTMENT DRYER )
Principal:
•Hot air- Circulation.
Construction:
•Small or a large cabinet insulated (to reduce
heat loss) compartment in which trays.
•Heater- Heating of air
•Fan: Circulate the air
•Inlet & Outlet.
Tray drier
•Air flows in direction of the arrows over each
shelf in turn.
•The wet material is spread on shallow trays
resting on the shelves.
•Electrical elements or steam-heated pipes are
positioned as shown, so that the air is
periodically reheated after it has cooled by
passage over the wet material on one shelf
before it passes on the next.
•Air flows in direction of the arrows over each
shelf in turn.
•The wet material is spread on shallow trays
resting on the shelves.
•Electrical elements or steam-heated pipes are
positioned as shown, so that the air is
periodically reheated after it has cooled by
passage over the wet material on one shelf
before it passes on the next.
Tray drier
Working:
•Material loaded in trays- Fresh air is introduced.
•The material is heated by hot air circulated.
•The trays containing the load remain in the
dryer until drying is complete,
•After which they are withdrawn, emptied and
recharged for drying the next batch.
Application:
•For drying of sticky material & granular mass.
•Drying of crude drugs, chemicals, powders,
tablet granules etc.
•Material loaded in trays- Fresh air is introduced.
•The material is heated by hot air circulated.
•The trays containing the load remain in the
dryer until drying is complete,
•After which they are withdrawn, emptied and
recharged for drying the next batch.
Application:
•For drying of sticky material & granular mass.
•Drying of crude drugs, chemicals, powders,
tablet granules etc.
Advantages :
•Easy to operate.
•Batch process for different product.
•Can useful for drying of verity of material.
Disadvantages:
•Require labor.
•Cost increasing
•Time consuming
•Easy to operate.
•Batch process for different product.
•Can useful for drying of verity of material.
Disadvantages:
•Require labor.
•Cost increasing
•Time consuming
Disadvantages of tray drying :
•The drying time is long
•Dissolved material can migrate to the upper surface of
the bed of granules
•Granules may aggregate owing to bridge formation at
the points of contact of the granules.
•The drying time is long
•Dissolved material can migrate to the upper surface of
the bed of granules
•Granules may aggregate owing to bridge formation at
the points of contact of the granules.
Fluidized Bed Dryer
•‘Fluidized’ means something that behaves like liquid. In
the fluidized bed dryer, the mixture of solids and gas
behave like a liquid and solid are called fluidized.
•It provides good contact between hot air and particles to
obtain efficient drying.
•The hot air is passed through a mesh, which supports
the conical vessel with a porous base.
•This vessel is filled with powder to be dried.
•It has wheels and can be clipped to the central plate by
means of a rapid acting ring closure.
•‘Fluidized’ means something that behaves like liquid. In
the fluidized bed dryer, the mixture of solids and gas
behave like a liquid and solid are called fluidized.
•It provides good contact between hot air and particles to
obtain efficient drying.
•The hot air is passed through a mesh, which supports
the conical vessel with a porous base.
•This vessel is filled with powder to be dried.
•It has wheels and can be clipped to the central plate by
means of a rapid acting ring closure.
Fluidized bed dryer
Principal:
•Hot air-trough bed of granules.
•Granules lifted from bottom & suspend in air
(Fluidized state).
Construction:
•Fluidized bed dryer- steel or plastic.
•Detachable bowl- perforated bottom with wire
mesh-support material.
•Fan- upper part- circulate air.
•Fresh air inlet/pre-filter/heat exchanger- to heat
air.
•Bag filters- collect fine
Principal:
•Hot air-trough bed of granules.
•Granules lifted from bottom & suspend in air
(Fluidized state).
Construction:
•Fluidized bed dryer- steel or plastic.
•Detachable bowl- perforated bottom with wire
mesh-support material.
•Fan- upper part- circulate air.
•Fresh air inlet/pre-filter/heat exchanger- to heat
air.
•Bag filters- collect fine
Working:
•Material load – detachable bowl.
•Fresh enter – inlet- heater- hot air- through
bed-with optimum velocity.
•Particle suspend- fluidized state- drying takes
place.
Application:
•Drying of tablet granules.
•Suitable for other process to mixing etc.
•Modified form – use for coating of granules.
•Material load – detachable bowl.
•Fresh enter – inlet- heater- hot air- through
bed-with optimum velocity.
•Particle suspend- fluidized state- drying takes
place.
Application:
•Drying of tablet granules.
•Suitable for other process to mixing etc.
•Modified form – use for coating of granules.
Advantages :
•Fast process.
•Available in different capacity.
•Easy handling, reduce labor cost.
•High thermal efficiency.
•Suitable for applying high temp.
•Suitable for thermo-labile substances.
Disadvantages:
•Develops electric charges.
•Attrition may occur.
•Fast process.
•Available in different capacity.
•Easy handling, reduce labor cost.
•High thermal efficiency.
•Suitable for applying high temp.
•Suitable for thermo-labile substances.
Disadvantages:
•Develops electric charges.
•Attrition may occur.
Vacuum Dryer
•This equipment is a good example of conduction drier.
The vacuum oven consists of a jacketed vessel to
withstand vacuum within the oven.
•There are supports for the shelves giving a larger area
for conduction heat transfer. The oven can be closed by
a door.
•The oven is connected through a condenser and liquid
receiver to a vacuum pump.
•Operating pressure can be as low as 0.03-0.03 bar, at
which pressures water boils at 25-35
0C.
•This equipment is a good example of conduction drier.
The vacuum oven consists of a jacketed vessel to
withstand vacuum within the oven.
•There are supports for the shelves giving a larger area
for conduction heat transfer. The oven can be closed by
a door.
•The oven is connected through a condenser and liquid
receiver to a vacuum pump.
•Operating pressure can be as low as 0.03-0.03 bar, at
which pressures water boils at 25-35
0C.
Vacuum Dryer
Principal:
•Drying – by application of vacuum.
Construction:
•Iron heavy jacketed vessel.
•Hallow shelves.
•Metal trays.
•Oven to vacuum pump.
Principal:
•Drying – by application of vacuum.
Construction:
•Iron heavy jacketed vessel.
•Hallow shelves.
•Metal trays.
•Oven to vacuum pump.
Working:
•Material of trays- placed on shelves.
•Pressure decreased by vacuum pump.
•Steam/hot hair- into jacket of shelves.
•Drying will takes place.
Application:
•Drying of heat sensitive material, dusty
hygroscopic material,
•Drugs containing toxic solvents.
•Material of trays- placed on shelves.
•Pressure decreased by vacuum pump.
•Steam/hot hair- into jacket of shelves.
•Drying will takes place.
Application:
•Drying of heat sensitive material, dusty
hygroscopic material,
•Drugs containing toxic solvents.
Advantages :
•Easy operating
•Easy for batch process of different compounds.
•Various modes can be used for heating.
•Drying takes place at a low temperature.
•There is little air present, so, there is minimum
risk of oxidation.
Disadvantages:
•Low heat transfer efficiency.
•Limited capacity.
•More expensive.
•Easy operating
•Easy for batch process of different compounds.
•Various modes can be used for heating.
•Drying takes place at a low temperature.
•There is little air present, so, there is minimum
risk of oxidation.
Disadvantages:
•Low heat transfer efficiency.
•Limited capacity.
•More expensive.
Advantages of vacuum oven:
•Drying takes place at a low temperature.
•There is little air present, so, there is minimum risk of
oxidation.
•Drying takes place at a low temperature.
•There is little air present, so, there is minimum risk of
oxidation.
Website: www.probecell.com Email: [email protected]
Ph: 7415211131
Office: Smriti Nagar, Bhilai, Chhattisgarh - 490020
https://youtube.com/c/ParagJainthunderpassionate https://www.facebook.com/thesisresearchwriting
Research article Review article ThesisSynopsisPhD Title Research guidance
Ph: 7415211131
Office: Smriti Nagar, Bhilai, Chhattisgarh - 490020
https://youtube.com/c/ParagJainthunderpassionate https://www.facebook.com/thesisresearchwriting
Research article Review article ThesisSynopsisPhD Title Research guidance
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