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DRYING
◦ Drying is the universal method of conditioning grain by removing
moisture to a moisture content level that is in equilibrium with normal
atmospheric air in order to preserve its quality and nutritive value for
food and feed and its viability for seed.
◦ Generally, drying refers to the removal of relatively small amount of
moisture from a solid or nearly solid material by evaporation.
◦ Therefore, drying involves both heat and mass transfer operations
simultaneously.
◦ Two major moisture removal methods are drying (or dehydration) to
produce a solid product and evaporation to produce a more concentrated
liquid.
◦ Drying refers to removal of moisture from grains and other products to a
predetermined level, whereas dehydration means removal of moisture
to very low levels usually to bone dry condition.
Methods of drying grains
◦ Drying of grains can be done in
different ways depending upon the
source of heat utilized for the purpose.
The most common methods are based
on the
◦ mode of heat transfer: Conduction
drying:
◦ (i) conduction drying,
◦ (ii) convection drying, and
◦ (iii) radiation drying.
◦ The other methods of drying are: dielectric drying, chemical drying,
vacuum drying and freeze drying.
◦ Convection drying is commonly used for drying of all types of grain
and conduction drying can be employed for drying of parboiled grain.
◦ Conduction drying
◦ When the heat for drying is transferred to the wet
solid mainly by conduction through a solid surface
(usually metallic), the phenomenon is known as
conduction or contact drying.
◦ Convection drying
◦ The drying agent (hot gases) in contact with the wet
solid, is used to supply heat and carry away the
vaporized moisture. The heat is transferred to the
wet solid mainly by convection. Convection drying
is most popular in grain drying. Fuel consumption
per kg of moisture evaporated is always higher than
that of conduction drying.
◦ Radiation drying
◦ It is based on the absorption of radiant energy of the
sun and its transformation into heat energy by the
grain. Sun drying is an example of radiation drying.
Classification of grain drying
◦ Grain drying is classified based on two principles:
◦(i) Thin layer drying and
◦(ii) deep bed drying.
Thin layer drying
◦ Thin layer drying refers to the grain drying process in which all grains are fully
exposed to the drying air under constant drying conditions, i.e., at constant
temperature, and humidity.
◦ Generally, up to 20 cm thickness of grain bed is taken as thin layer.
◦ All commercial flow dryers are designed on thin layer drying principle.
The features of thin layer method of grain drying
are
◦ a) Limited to 20 cm of grain depth
◦ b) Drying rate is independent of air velocity
◦ c) At a given RH and moisture content, the drying rate is proportional to
the difference between the dry bulb temperatures of air in equilibrium
with the grain.
◦ d) The rate of drying is proportional to the difference between the vapour
pressure of moisture in the grain and vapour pressure of moisture in the
drying air.
Deep bed drying
◦ Deep bed drying process refers to the heterogeneous drying of grain in deep layer (more
than 20 cm deep) where drying is faster at the inlet end of drying chamber than at the
exhaust end.
◦ The drying of grain in a deep bin (Fig .) can be taken as the sum of several thin layers of
grain arranged one above another.
◦ The rate of moisture removal is maximum for the bottom layer and decreased
exponentially for subsequent layers. Dry air becomes cooler and moister as it moves up
in the grain bed.
◦ Actually, all grains in the drying chamber may be considered to be in 3 zones:
◦ (a) dried zone;
◦ (b) the drying zone;
◦ (c) the wet zone.
Drying process in deep bin
◦ The dried zone will gradually move upward as drying proceeds in the direction of
air movement.
◦ The air passes through the dried zone and picks up moisture in the drying zone until
it reaches equilibrium moisture content (EMC) in the case of very wet grain. In this
way, as the air moves, its drying capacity goes on decreasing.
◦ Drying will cease as soon as the product comes in equilibrium with the air. The
upper edge of the drying zone at the interface with the wet zone is called the drying
front.
◦ The drying front indicates the level of grains in the bin at which, the grain have just
started loosing moisture to the drying air. The volume of drying zone varies with the
temperature and humidity of entering air, the moisture content of the grain and
velocity of air movement.
◦ The drying rate in a bin varies from layer to layer from time to time and depends
upon the characters of grains and the air used for drying.
Sun
drying
◦ This is a traditional method of
drying of crops and grains.
◦ Sun drying involves using the
energy of the sun to remove
moisture from the product.
◦ Major portion of crops is left in the
field and threshing yard for drying
under sun.
◦ A major quantity of grain is still
dried by the sun in most of the
developing countries.
Sun drying
Advantages
◦ 1. No fuel or mechanical energy is required.
◦ 2. Operation is very simple
◦ 3. Viability, germination, baking qualities are
fully preserved.
◦ 4. Microbial activity and insect/pest infestation
are reduced.
◦ 5. No pollution
◦ 6. Low capital requirement
◦ 7. Operating costs are considerable.
Disadvantages
◦ 1. Uncontrolled and non-uniform drying, results in sun
checks or cracks in kernels.
◦ 2. Completely dependent on weather.
◦ 3. Not possible round the clock and round the year.
◦ 4. Excessive losses occur due to shattering, birds,
rodents etc. It is usually 0.1 to 0.4%.
◦ 5. Require specially constructed large drying floor.
◦ 6. The entire process is unhygienic.
◦ 7. Unsuitable for handling large quantity of grain
within a short period of time.
◦ 8. Require large number of unskilled labour.
Mechanical drying
◦ This process utilizes mechanical means to circulate heated air at
constant temperature and humidity, through the grain mass to
accomplish the removal of excess moisture from the grain.
Mechanical drying features
◦ (a) the rate of drying can be controlled by adjusting the temperature of hot air
circulating through the grain mass. Therefore, increase in milling quality with possible
reduction in development of cracks in the grain.
◦ (b) Grains can be dried irrespective of weather condition, day or night; the process does
not depend on any natural sources like sun energy.
◦ (c) The process is automatic and requires unskilled labour, except a trained person to
operate the dryer.
◦ (d) there are practically no losses due to birds, rodents and insects.
◦ (e) The entire process is hygienic.
◦ (f) Possible round the clock and round the year and
◦ (g) Suitable for handling of large quantity of grain with in a short period of harvest.
◦ Mechanical drying requires very little space for operation.
◦ Mechanical drying, in conjunction with early harvest, improves the
milling quality of paddy considerably.
◦ The disadvantages of mechanical drying are:
◦ the process requires fuel and electrical or mechanical power to drive
the blower, elevators etc.
◦ Therefore, cost of drying is relatively higher compared to sun-drying
for commercial drying.
Mechanical dryers
◦ The mechanical dryers are classified as:
◦ (a) Sack driers (storage layer driers, batch driers or bin driers).
◦ (b) Rotary driers (batch or continuous)
◦ (c) Continuous flow dryers
◦ Non-mixing type - Recirculatory batch dryer
◦ Mixing type - LSU type dryer & Baffle dryer
Sack drier
◦ A sack drier consists of a large floor in a building with openings over which the sacks of
grain are placed.
◦ The openings are covered with a perforated material to support the sacks. A blower is
connected to an air chamber beneath the floor to supply the air.
◦ A sack dryer is best suited for drying a small quantity of grain. It eliminates
the problem of mixing various paddy varieties.
◦ This type of dryer requires high labour cost.
◦ Usually air temperature of 450C is used with air flow rate of 4 m3/min per
bag of 60 kg for fast drying.
◦ The sacks are turned over once during the drying operation.
Batch/Bin dryer
◦ This dryer dries a relatively small amount of batch of grain in
sacks or in bulk. The grain is normally remaining static during
the drying process. These batch dryers can be different shapes.
The holding capacity ranges from one ton to several tons of
grain. If the capacity is small they are called batch dryers
otherwise they are called “bin dryers” and the process is bin
drying. These bins could be circular, square, rectangular or
hexagonal. If they are small, they could be portable. Drying in
these bins is called deep bed drying. In a simple batch dryer,
the grain is placed in a bin and heated air is forced through it
until the desired moisture content is reached. The drying of the
grain in the bin takes place following the deep bed drying
principle. The normal air temperature recommended for batch
or bin drying is 45ºC to 50 ºC. The recommended maximum
depth of paddy grain is 200 to 250 cm and the minimum air
flow rate is 3 to 4 m3/min/cum of paddy.
Rotary dryer
◦ This dryer could be a batch or a continuous type. It is also called rotating drum dryer as it consists of a
large drum 2m in diameter and 3 to 6 m in length, placed on a slight incline .
◦ Grain is fed into the upper end and as the unit rotates the grain move downwards and mixes with the air
flowing around the grain and finally drops down on the lower end (grain and the air move in the same
direction).
◦ This provides a continuous mixing of the grain with the drying air until the grain leaves the dryer at the
lower end of the drum.
◦ Heated air acts here mainly as a carrier of moisture from the dryer.
◦ While traveling the grain from feed end to discharge end of the dryer, the
parboiled paddy comes into contact with the steam heated pipes for a very short
time in each rotation and is gradually dried. As parboiled paddy can stand high
temperature without significant increase of cracks in grains, these dryers can be
employed for rapid drying of parboiled paddy using temperatures as high as 100
to 110ºC.
◦ The cylindrical shell of the dryer is rotated at 2 to 6 rpm by a motor through speed
reduction gear, pulley and belt drive system.
◦ In India, the Jadavpur university, Calcutta introduced a rotary dryer of 1
tonne/hour capacity for the drying of parboiled paddy.
Continuous flow mixing type dryers
◦ There are several types of
continuous flow mixing type
dryers.
◦ The most popular type in India
and USA is the LSU type.
◦ The main advantages of continuous flow dryers are:
◦ 1. A shorter drying period, which is necessary with less danger of spoilage
during wet season.
◦ 2. Larger volumes of paddy can be dried in less time.
◦ 3. Drying losses are less
◦ 4. Drying is more uniform as there is mixing of grain with air
◦ 5. The milling quality of paddy is better
◦ 6. Higher air flow rates could be obtained
◦ 7. The drying parameters can be controlled and therefore, also the drying
rate.
Louisiana state university (LSU) dryer
◦ This is a continuous flow-mixing type of grain dryer which is popular in
India and the U.S.A.
◦ It was developed at Louisiana State University Baton Rouge, USA in
1949.
◦ Construction: It consists of :
◦ (1) a rectangular drying chamber fitted with air ports and the holding bin,
◦ (2) an air blower with duct,
◦ (3) grain discharging mechanism with a hopper bottom, and
◦ (4) an air heating system .
◦ (1) Rectangular bin: Usually the following top square sections of the bin are used for the design of LSU
dryers:
◦ (i) 1.2m x 1.2 m, (ii) 1.5 m x 1.5 m,
◦ (iii) 1.8 m x 1.8 m and (iv) 2.1 m x 2.1 m.
◦ The rectangular bin can be divided into two sections, namely, top holding bin and bottom drying chamber.
◦ (2) Air Distribution system: Layers of inverted trough or V- shaped channels (called inverted V-ports) are
installed in the drying chamber.
◦ Alternate rows of these ports are opened on the blower and closed on the exhaust end. These are called inlet
ports Hot air enters the drying chamber through these ports.
◦ The other alternative rows of ports are closed on the blower end and are opened on the exhaust end. These
are called outlet or exhaust ports as the drying air goes out through these ports.
◦ The inlet and outlet ports are of uniform sizes and equal in number with equal spacing in between them.
◦ Usually the inlet ports are given in 3 columns and outlet ports in 4 columns ( 2 column of full size ports and
2 columns of half-size ports). The number of ports containing a dryer varies widely depending on the size
of the dryer.
(a) LSU type dryer and (b) flow pattern in LSU dryer
◦ The inlet and outlet ports are arranged one below the other in a zig-zag path, so that when paddy flows down
between these ports, it takes a zig-zag path.
◦ Hot air enters the inlet ports from the blower end. Since these ports are closed on exhaust end, the hot air
from these channels or ports flows down through the paddy and enter the outlet ports and leave the drying
chamber through exhaust side.
◦ Some degree of mixing of hot air and paddy occurs in this chamber while air is flowing across it in zig-zag
path and paddy flowing downwards.
◦ Three fluted rolls are attached at the bottom, which are rotated at a slow speed. The discharge of the paddy is
regulated with these fluted rolls. To provide hot air for drying, fuel is burnt to raise the ambient air
temperature.
◦ Heat may be supplied by the direct fired burners or direct or indirect heat exchangers.
◦ In general, the capacity of the dryer varies from 2 to 12
tonnes of grain, but sometimes dryers of higher capacities
are also installed.
◦ Accordingly power requirement varies widely.
◦ Recommended air flow rate is 70 m3/min/tonne of dry
paddy and optimum air temperatures are 60-70O C and
85O C for raw and parboiled paddy respectively.
◦ A series of dryers can also be installed. In continuous flow
dryers, drying air temperature may be as high as 700C,
where as for batch dryers, this temperature seldom
exceeds 450C.
Following are some recommendations for the drying operation with
particular reference to the operation of an LSU Dryer:
◦ a) A drying cycle chart in the control room will be a great help and to guide the operator.
◦ b) The dryer should not be operated until it is filled completely with grain.
◦ c) The recommended drying air temperature is 60O C and the air flow rate is 70 cu m/min./
ton of holding capacity of dryer.
◦ d) Tempering in between drying process is recommended to reduce the total drying time.
Normally, this tempering period is of 8 hour duration.
◦ e) Feed roll clearance should be the same for all the fluted rolls for uniform drying.
◦ f) The grain temperature during drying should not exceed 40O C.
◦ g) The burner should be started only after the blower has been started.
◦ h) There should be appropriate controls to put the flame off in case of blower failure due
to either power or mechanical failure. An automatic fuel cut-off valve is recommended for
this purpose.

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Drying

  • 2.
  • 3. ◦ Drying is the universal method of conditioning grain by removing moisture to a moisture content level that is in equilibrium with normal atmospheric air in order to preserve its quality and nutritive value for food and feed and its viability for seed. ◦ Generally, drying refers to the removal of relatively small amount of moisture from a solid or nearly solid material by evaporation. ◦ Therefore, drying involves both heat and mass transfer operations simultaneously. ◦ Two major moisture removal methods are drying (or dehydration) to produce a solid product and evaporation to produce a more concentrated liquid. ◦ Drying refers to removal of moisture from grains and other products to a predetermined level, whereas dehydration means removal of moisture to very low levels usually to bone dry condition.
  • 4. Methods of drying grains ◦ Drying of grains can be done in different ways depending upon the source of heat utilized for the purpose. The most common methods are based on the ◦ mode of heat transfer: Conduction drying: ◦ (i) conduction drying, ◦ (ii) convection drying, and ◦ (iii) radiation drying.
  • 5. ◦ The other methods of drying are: dielectric drying, chemical drying, vacuum drying and freeze drying. ◦ Convection drying is commonly used for drying of all types of grain and conduction drying can be employed for drying of parboiled grain.
  • 6. ◦ Conduction drying ◦ When the heat for drying is transferred to the wet solid mainly by conduction through a solid surface (usually metallic), the phenomenon is known as conduction or contact drying. ◦ Convection drying ◦ The drying agent (hot gases) in contact with the wet solid, is used to supply heat and carry away the vaporized moisture. The heat is transferred to the wet solid mainly by convection. Convection drying is most popular in grain drying. Fuel consumption per kg of moisture evaporated is always higher than that of conduction drying. ◦ Radiation drying ◦ It is based on the absorption of radiant energy of the sun and its transformation into heat energy by the grain. Sun drying is an example of radiation drying.
  • 7. Classification of grain drying ◦ Grain drying is classified based on two principles: ◦(i) Thin layer drying and ◦(ii) deep bed drying.
  • 8. Thin layer drying ◦ Thin layer drying refers to the grain drying process in which all grains are fully exposed to the drying air under constant drying conditions, i.e., at constant temperature, and humidity. ◦ Generally, up to 20 cm thickness of grain bed is taken as thin layer. ◦ All commercial flow dryers are designed on thin layer drying principle.
  • 9. The features of thin layer method of grain drying are ◦ a) Limited to 20 cm of grain depth ◦ b) Drying rate is independent of air velocity ◦ c) At a given RH and moisture content, the drying rate is proportional to the difference between the dry bulb temperatures of air in equilibrium with the grain. ◦ d) The rate of drying is proportional to the difference between the vapour pressure of moisture in the grain and vapour pressure of moisture in the drying air.
  • 10.
  • 11.
  • 12. Deep bed drying ◦ Deep bed drying process refers to the heterogeneous drying of grain in deep layer (more than 20 cm deep) where drying is faster at the inlet end of drying chamber than at the exhaust end. ◦ The drying of grain in a deep bin (Fig .) can be taken as the sum of several thin layers of grain arranged one above another. ◦ The rate of moisture removal is maximum for the bottom layer and decreased exponentially for subsequent layers. Dry air becomes cooler and moister as it moves up in the grain bed. ◦ Actually, all grains in the drying chamber may be considered to be in 3 zones: ◦ (a) dried zone; ◦ (b) the drying zone; ◦ (c) the wet zone.
  • 13. Drying process in deep bin
  • 14. ◦ The dried zone will gradually move upward as drying proceeds in the direction of air movement. ◦ The air passes through the dried zone and picks up moisture in the drying zone until it reaches equilibrium moisture content (EMC) in the case of very wet grain. In this way, as the air moves, its drying capacity goes on decreasing. ◦ Drying will cease as soon as the product comes in equilibrium with the air. The upper edge of the drying zone at the interface with the wet zone is called the drying front. ◦ The drying front indicates the level of grains in the bin at which, the grain have just started loosing moisture to the drying air. The volume of drying zone varies with the temperature and humidity of entering air, the moisture content of the grain and velocity of air movement. ◦ The drying rate in a bin varies from layer to layer from time to time and depends upon the characters of grains and the air used for drying.
  • 15. Sun drying ◦ This is a traditional method of drying of crops and grains. ◦ Sun drying involves using the energy of the sun to remove moisture from the product. ◦ Major portion of crops is left in the field and threshing yard for drying under sun. ◦ A major quantity of grain is still dried by the sun in most of the developing countries.
  • 16.
  • 17. Sun drying Advantages ◦ 1. No fuel or mechanical energy is required. ◦ 2. Operation is very simple ◦ 3. Viability, germination, baking qualities are fully preserved. ◦ 4. Microbial activity and insect/pest infestation are reduced. ◦ 5. No pollution ◦ 6. Low capital requirement ◦ 7. Operating costs are considerable. Disadvantages ◦ 1. Uncontrolled and non-uniform drying, results in sun checks or cracks in kernels. ◦ 2. Completely dependent on weather. ◦ 3. Not possible round the clock and round the year. ◦ 4. Excessive losses occur due to shattering, birds, rodents etc. It is usually 0.1 to 0.4%. ◦ 5. Require specially constructed large drying floor. ◦ 6. The entire process is unhygienic. ◦ 7. Unsuitable for handling large quantity of grain within a short period of time. ◦ 8. Require large number of unskilled labour.
  • 18. Mechanical drying ◦ This process utilizes mechanical means to circulate heated air at constant temperature and humidity, through the grain mass to accomplish the removal of excess moisture from the grain.
  • 19. Mechanical drying features ◦ (a) the rate of drying can be controlled by adjusting the temperature of hot air circulating through the grain mass. Therefore, increase in milling quality with possible reduction in development of cracks in the grain. ◦ (b) Grains can be dried irrespective of weather condition, day or night; the process does not depend on any natural sources like sun energy. ◦ (c) The process is automatic and requires unskilled labour, except a trained person to operate the dryer. ◦ (d) there are practically no losses due to birds, rodents and insects. ◦ (e) The entire process is hygienic. ◦ (f) Possible round the clock and round the year and ◦ (g) Suitable for handling of large quantity of grain with in a short period of harvest.
  • 20. ◦ Mechanical drying requires very little space for operation. ◦ Mechanical drying, in conjunction with early harvest, improves the milling quality of paddy considerably. ◦ The disadvantages of mechanical drying are: ◦ the process requires fuel and electrical or mechanical power to drive the blower, elevators etc. ◦ Therefore, cost of drying is relatively higher compared to sun-drying for commercial drying.
  • 21. Mechanical dryers ◦ The mechanical dryers are classified as: ◦ (a) Sack driers (storage layer driers, batch driers or bin driers). ◦ (b) Rotary driers (batch or continuous) ◦ (c) Continuous flow dryers ◦ Non-mixing type - Recirculatory batch dryer ◦ Mixing type - LSU type dryer & Baffle dryer
  • 22. Sack drier ◦ A sack drier consists of a large floor in a building with openings over which the sacks of grain are placed. ◦ The openings are covered with a perforated material to support the sacks. A blower is connected to an air chamber beneath the floor to supply the air.
  • 23. ◦ A sack dryer is best suited for drying a small quantity of grain. It eliminates the problem of mixing various paddy varieties. ◦ This type of dryer requires high labour cost. ◦ Usually air temperature of 450C is used with air flow rate of 4 m3/min per bag of 60 kg for fast drying. ◦ The sacks are turned over once during the drying operation.
  • 24. Batch/Bin dryer ◦ This dryer dries a relatively small amount of batch of grain in sacks or in bulk. The grain is normally remaining static during the drying process. These batch dryers can be different shapes. The holding capacity ranges from one ton to several tons of grain. If the capacity is small they are called batch dryers otherwise they are called “bin dryers” and the process is bin drying. These bins could be circular, square, rectangular or hexagonal. If they are small, they could be portable. Drying in these bins is called deep bed drying. In a simple batch dryer, the grain is placed in a bin and heated air is forced through it until the desired moisture content is reached. The drying of the grain in the bin takes place following the deep bed drying principle. The normal air temperature recommended for batch or bin drying is 45ºC to 50 ºC. The recommended maximum depth of paddy grain is 200 to 250 cm and the minimum air flow rate is 3 to 4 m3/min/cum of paddy.
  • 25. Rotary dryer ◦ This dryer could be a batch or a continuous type. It is also called rotating drum dryer as it consists of a large drum 2m in diameter and 3 to 6 m in length, placed on a slight incline . ◦ Grain is fed into the upper end and as the unit rotates the grain move downwards and mixes with the air flowing around the grain and finally drops down on the lower end (grain and the air move in the same direction). ◦ This provides a continuous mixing of the grain with the drying air until the grain leaves the dryer at the lower end of the drum.
  • 26.
  • 27. ◦ Heated air acts here mainly as a carrier of moisture from the dryer. ◦ While traveling the grain from feed end to discharge end of the dryer, the parboiled paddy comes into contact with the steam heated pipes for a very short time in each rotation and is gradually dried. As parboiled paddy can stand high temperature without significant increase of cracks in grains, these dryers can be employed for rapid drying of parboiled paddy using temperatures as high as 100 to 110ºC. ◦ The cylindrical shell of the dryer is rotated at 2 to 6 rpm by a motor through speed reduction gear, pulley and belt drive system. ◦ In India, the Jadavpur university, Calcutta introduced a rotary dryer of 1 tonne/hour capacity for the drying of parboiled paddy.
  • 28. Continuous flow mixing type dryers ◦ There are several types of continuous flow mixing type dryers. ◦ The most popular type in India and USA is the LSU type.
  • 29. ◦ The main advantages of continuous flow dryers are: ◦ 1. A shorter drying period, which is necessary with less danger of spoilage during wet season. ◦ 2. Larger volumes of paddy can be dried in less time. ◦ 3. Drying losses are less ◦ 4. Drying is more uniform as there is mixing of grain with air ◦ 5. The milling quality of paddy is better ◦ 6. Higher air flow rates could be obtained ◦ 7. The drying parameters can be controlled and therefore, also the drying rate.
  • 30. Louisiana state university (LSU) dryer ◦ This is a continuous flow-mixing type of grain dryer which is popular in India and the U.S.A. ◦ It was developed at Louisiana State University Baton Rouge, USA in 1949. ◦ Construction: It consists of : ◦ (1) a rectangular drying chamber fitted with air ports and the holding bin, ◦ (2) an air blower with duct, ◦ (3) grain discharging mechanism with a hopper bottom, and ◦ (4) an air heating system .
  • 31.
  • 32. ◦ (1) Rectangular bin: Usually the following top square sections of the bin are used for the design of LSU dryers: ◦ (i) 1.2m x 1.2 m, (ii) 1.5 m x 1.5 m, ◦ (iii) 1.8 m x 1.8 m and (iv) 2.1 m x 2.1 m. ◦ The rectangular bin can be divided into two sections, namely, top holding bin and bottom drying chamber. ◦ (2) Air Distribution system: Layers of inverted trough or V- shaped channels (called inverted V-ports) are installed in the drying chamber.
  • 33. ◦ Alternate rows of these ports are opened on the blower and closed on the exhaust end. These are called inlet ports Hot air enters the drying chamber through these ports. ◦ The other alternative rows of ports are closed on the blower end and are opened on the exhaust end. These are called outlet or exhaust ports as the drying air goes out through these ports. ◦ The inlet and outlet ports are of uniform sizes and equal in number with equal spacing in between them. ◦ Usually the inlet ports are given in 3 columns and outlet ports in 4 columns ( 2 column of full size ports and 2 columns of half-size ports). The number of ports containing a dryer varies widely depending on the size of the dryer. (a) LSU type dryer and (b) flow pattern in LSU dryer
  • 34. ◦ The inlet and outlet ports are arranged one below the other in a zig-zag path, so that when paddy flows down between these ports, it takes a zig-zag path. ◦ Hot air enters the inlet ports from the blower end. Since these ports are closed on exhaust end, the hot air from these channels or ports flows down through the paddy and enter the outlet ports and leave the drying chamber through exhaust side. ◦ Some degree of mixing of hot air and paddy occurs in this chamber while air is flowing across it in zig-zag path and paddy flowing downwards. ◦ Three fluted rolls are attached at the bottom, which are rotated at a slow speed. The discharge of the paddy is regulated with these fluted rolls. To provide hot air for drying, fuel is burnt to raise the ambient air temperature. ◦ Heat may be supplied by the direct fired burners or direct or indirect heat exchangers.
  • 35. ◦ In general, the capacity of the dryer varies from 2 to 12 tonnes of grain, but sometimes dryers of higher capacities are also installed. ◦ Accordingly power requirement varies widely. ◦ Recommended air flow rate is 70 m3/min/tonne of dry paddy and optimum air temperatures are 60-70O C and 85O C for raw and parboiled paddy respectively. ◦ A series of dryers can also be installed. In continuous flow dryers, drying air temperature may be as high as 700C, where as for batch dryers, this temperature seldom exceeds 450C.
  • 36. Following are some recommendations for the drying operation with particular reference to the operation of an LSU Dryer: ◦ a) A drying cycle chart in the control room will be a great help and to guide the operator. ◦ b) The dryer should not be operated until it is filled completely with grain. ◦ c) The recommended drying air temperature is 60O C and the air flow rate is 70 cu m/min./ ton of holding capacity of dryer. ◦ d) Tempering in between drying process is recommended to reduce the total drying time. Normally, this tempering period is of 8 hour duration. ◦ e) Feed roll clearance should be the same for all the fluted rolls for uniform drying. ◦ f) The grain temperature during drying should not exceed 40O C. ◦ g) The burner should be started only after the blower has been started. ◦ h) There should be appropriate controls to put the flame off in case of blower failure due to either power or mechanical failure. An automatic fuel cut-off valve is recommended for this purpose.