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WHAT IS A FLASH DRYER?
Flash dryer is a continuous drying plant
used for drying variety of wet cakes by disintegrating wet cake into fine powder and dried
by hot air to form powder. The whole process is fully automatic requiring no handling or
human involvement. The feed rate is adjusted automatically as per the variation in
moisture content in wet cake thereby achieving consistent product quality.
The principle of Flash Drying is to
evaporate surface moisture instantaneously. The word "flash" is used, as the
drying time is very less from milli to few seconds. It is well known fact that the surface
area of wet lump increases as the size of lump decreases. The wet cake is disintegrated
into fines to increase the surface area. The drying is instantaneous and the material
remains at wet bulb temperature of air. Hence it is also called as "wet bulb
drying".
The air velocities are similar to that of
pneumatic conveying. The powder remains suspended in air and gets conveyed while drying.
Hence it is also called as pneumatic dryer. The retention of a given solids particles in
the system is very short, typically in seconds.
These make it ideal for drying heat
sensitive, easily oxidized, materials that cannot be exposed to process conditions for
extended periods.
Our flash dryer is energy efficient,
requiring no intermediate material handling. It is a continuous production machine
suitable for pasty / sticky wet cakes. These unique features make it ideal replacement for
conventional tray and rotary drying. |
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WORKING PRINCIPLE OF FLASH DRYER

Figure 1 depicts working of Flash dryer
- Wet cake is fed in feed mechanism. The feed mechanism
consists of balance tank, stirrer and screw feeder.
- The stirrer feeds the screw feeder. The screw feeder gives
controlled feed at rated capacity to disintegrator.
- The air after passing through Air Filter is heated in Oil
fired hot air generator or steam / thermic fluid based radiator.
- Hot air and wet cake get thoroughly mixed in the cage mill
type disintegrator. Disintegration and drying of wet cake takes place in disintegrator.
- Wet cake is rapidly dried and about 50% drying take place in
the disintegrator.
- Drying duct conveys the pulverized material to cyclone.
Drying gets completed in conveying duct.
- The time taken by disintegrated powder to travel through
drying duct is called residence time of drying.
- The material looses moisture that is absorbed by hot air.
The temperature of air reduces while its humidity increases.
- Powder is further dried in cyclone. Separation of dried
powder and air takes place in cyclone. Powder is discharged from cyclone through powder
discharge valves.
- Fine particles escaped from cyclone are conveyed to bag
filter.
- Bag filter recovers the fine particles. The air coming out
of bag filter is dust free and confirms to pollution control norms.
- Two blowers, one at inlet & other at outlet, working on
Push-Pull principle maintain the airflow in the system.
- Push-Pull principle ensures that the ambient pressure is
maintained at feeding system to avoid dusting of material. Also it avoids extreme
pressures (either positive or negative) in the system.
- The powder collected from cyclone and bag filter can be
pneumatically conveyed to storage bin or bagging section.
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OTHER COMPONENTS OF FLASH DRYER

1) AIR FILTER
- Air filter HDPE, 3ply of sufficient area for minimum
pressure drop.
- Flanged type construction for ease of removal for cleaning.
- Material selected for filter is water washable.
- Manometer is provided on filter for checking of blockage.
2) HOT AIR GENERATOR
Hot air generator is designed and
manufactured Transparent Energy Systems Pvt. Ltd. and have High Thermal efficiency of 93%
on NCV & 87% on GCV that gives large saving in fuel cost.
3) CYCLONE
- Optimally sized for the desired airflow rate.
- Low pressure drop.
- Settling vessel is provided to have highest powder
separation efficiency.
- Cleaning window is provided with hinged door.
- Air purging system is provided to prevent bridging.
4) SECONDARY DISINTEGRATOR.
- Secondary disintegrator is provided on-line for further
disintegrating the dried powder.
- It is belt driven to adjust the speed, which will control
the powder fineness.
- It is an add-on type assembly. Hence can be used whenever
required.
5) BAG FILTER
- Large filtering area of Bag filter reduced pressure
drop large savings in power consumption of blower.
- Anti-stick coat on bags reduced chocking.
- Low CAN velocity low powder entrainment reduce
chocking.
- Bustle type construction low powder entrainment
reduced chocking.
- Automatic air pulse jet system clean filter bags
on-line.
- Designed, manufactured & tested for
- Material.
- Airflow rate.
- Pressure drop at no dusting.
- Workmanship.
- Bag removal from top maintenance in dust free
atmosphere.
- Full SS construction (even on exhaust side).
- Bottom cone angle of drying chamber is 45° - powder slides.
- Air bleeding system linked with air temperature at inlet to
bag filter for protecting the bags.
6) ROTARY AIR VALVE
- Rotary air valves have very less gap between rotors and
stators. This reduces infiltration of air thereby maintaining high powder-separating
efficiencies.
- The rotary air valves has back pull type construction. This
facilitates easy and quick removal of rotor without necessity of removing drive end.
- Rotary air valves are provided with compressed air purging
system. This eliminates chocking of rotary air valve rotor by moist and hygroscopic
powders.
- Rotary air valves are provided with oil seals and double Z
ball bearings to avoid powder entering in bearings. This increases bearing life and
reliability of rotary air valve.
- All Stainless steel construction instead of cast aluminum
giving high abrasion resistance and long life.
- Safety grill at outlet is provided for safe operation.
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MAIN COMPONENTS OF FLASH DRYER

1) Feeding Mechanism:
The Feeding Mechanism feeds the wet
cake steadily in metered quantity. The entire feeding mechanism as depicted in Figure No. 2 it
consists of following-
See Figure No.2
- The Balance Tank holds the wet cake and acts as a buffer
tank.
- Many materials are sticky / pasty having tendency of forming
bridge if not kept agitated. Stirrer has special contour to keep the material agitated and
force the wet cake positively on screw feeder. This guarantees continuous flow of wet cake
to dryer as shown in Figure 3.
- It homogenizes the wet cake and increases uniformity of
constituents in dry powder.
- Stirrer speed and blades are designed to suit wet cake
properties.
- The agitation increases the flowability of wet cake. This
reduces the power required for screw feeder to push the material.
See Figure
No. 3
- The screw feeder has pipe type construction with minimum
gaps between screw and pipe. This ensures that there is no void space for material
accumulation and material move ahead positively as shown in Figure 4.
- The screw feeder remains clean avoiding drying of material
in voids. This avoids charring of material in screw feeder due to hot air and subsequent
contamination of dried product.
- Angular contact bearings are used to reduce friction, wear
& tear, thereby increasing life and reducing power requirement. Further, it eliminates
need of thrust bearing making the assembly compact.
See Figure
No. 4
- The material is discharged from screw feeder on rotating
cage of disintegrator. If the pigment is very pasty / sticky the material falls as a lump
on disintegrator rotating cage. The disintegrator will not be able to disintegrate this
lump fast, and layer of wet cake will form on disintegrator cages and subsequently chock
it. To avoid this, distributor is provided to distribute the material and feed it in small
nodule shapes. Figure 5 further explains the distributor function.
See
Figure No. 5A
See Figure
No. 5B
2) Cage Mill Disintegrator
The principle of Flash Drying is to
evaporate surface moisture instantaneously. The material has to be disintegrated into fine
particulate to increase the surface area for heat and mass transfer. Cage Mill
Disintegrator does this and hence is the heart of Flash Dryer.
Figure 2 shows the assembly of disintegrator along with feeding
system. The construction and working of Cage Mill Disintegrator is depicted in Figure 6.
See Figure
No. 6
- It consists of alternate rotating and stationary cages. The
cages have close pitched, large number of rods.
- The material and hot air are fed at center of rotating cage.
- It instantaneously disintegrates wet lump in fine
agglomerates exposing very high surface area for drying.
- Presence of highly turbulent hot air and intimate mixing of
hot air with finely divided agglomerates results reduction of moisture very rapidly. The
material looses its stickiness.
- Also strong centrifugal force totally prevents the material
from sticking to the rods.
- The mixture of hot air and agglomerates move with high
turbulence to the stationary cage. The agglomerates hit the rods of stationary cage with
very high velocities and further disintegrate exposing their core to rapid drying.
- Hitting agglomerates dislodge any agglomerate sticking to
stationary rods.
- The mixture of hot air and agglomerates undergo similar
severe action of disintegration and drying in subsequent rotating and stationary cages.
- At the outlet of last rotating cage material is
substantially dried and about 70% moisture is evaporated.
- Both the material and hot air move in radial outward
direction. This avoids back mixing of semi-dry material with fresh material.
- The hot air and material moves co-current. The hottest air
comes in contact with material having highest moisture. This avoids charring of material.
- These make it possible to use high inlet temperature of air
making the plant energy efficient. Further it makes the plant size small reducing the
capital cost of equipment, civil cost and so on.
- The rotating cages are dynamically balanced as per IS 1940
for smooth vibration free performance.
- The disintegration action depend upon rod gaps and impeller
speed. To obtain powders of various mesh sizes and thus to increase flexibility of
operation, the speed of disintegrator can be changed by variable speed drive or by
changing pulleys if made belt driven.
- To avoid dusting of powder from gap between shaft and
casing, air sealing is provided.
- The bearing block is robust, fabricated single piece
assembly with single setting machining. This ensures prolong life of bearings avoiding
maintenance and production loss.
- Cleaning windows are provided on casing that facilitates
washing of disintegrator reducing down time.
Combination of cage mill disintegrator with secondary
disintegrator make the plant ideal for fine powder applications in organic / inorganic
pigments and dyestuff.
3) F. D. Fan and I. D. Fan
- Blowers are designed for the required duty point. This
reduces the power requirement of blower.
- The blowers have high efficiency up to 80%.
- The blowers are tested for following parameters-
- Performance
- Vibrations as per IS 1940.
- Rise in bearing temperature.
This increases the reliability of blowers
reducing maintenance and down time of dryer.
- The bearing block is robust, fabricated single piece
assembly with single setting machining. This ensures prolong life of bearings avoiding
maintenance and production loss.
- Access door for inspection / cleaning facilitates
maintenance / washing.
- Drain plug is provided for removal of condensate while the
blower is running. This avoids plant stoppage increasing productivity.
- The flow rate of air is an important parameter for proper
drying. To control the quantity of air, damper is provided at outlet of blower.
- To monitor the performance of blower and in turn that of
dryer; manometer tappings at inlet and outlet are provided.
- The blowers are either belt driven or direct driven
depending upon blower size and customer requirements.
- Guard is provided at air inlet and on belt to make the
installation safe.
- The blower is mounted on rigid base frame and supports for
vibration free performance.
4) Drying cum Conveying Duct
The drying cum conveying duct provides
necessary residence time for particulate to dry. Moist, disintegrated material from
disintegrator enters the duct at one end while dried powder is discharged into cyclone at
other end as depicted in figure 1.
- The bends provided are smooth and curved
See Figure No.
7
- To reduce pressure drop in the system thereby saving power
required for blower
- To avoid settling of powder as depicted in figure 7. On
smooth surface powder does not get deposited easily than that on a rough surface. For heat
sensitive materials this is very important as deposited material gets charred with time.
- Horizontal run of drying duct is averted to avoid settling
of powder as depicted in figure 7.
- The drying duct also functions as conveying duct. The air
velocities are similar to that for pneumatic conveying. This ensures that powder get
conveyed properly without chocking the duct. Dryer runs continuously at rated capacity.
- Manholes / hand holes are provided for ease of cleaning
reducing cleaning and down time of machine.
- Control Panel & Instrumentation
The dryer is supplied along with a factory
pre-wired and tested control panel through which the entire dryer can be operated in
automatic as well as manual mode. The control panel has following instruments:
- All motors have starters, overload protection relays and
necessary fuses / circuit breakers.
- Digital temperature indicators and controllers for air are
provided at various points in the air circuit to indicate drying condition in the plant.
- Hot air generator burner is provided with its starter
sequence programmer, flame monitoring and failure safety instruments.
- A variable speed drive is provided for material screw feeder
that automatically adjusts feeding rate whenever moisture in feed material varies. This is
done by a PID temperature controller which senses outlet air temperature at inlet of
cyclone and gives signal to variable speed drive controller for increasing or decreasing
the feed rate so that set outlet temperature of air is maintained.
The control panel is provided with various
indicating lamps and rotary switches for convenient operation and trouble shooting.
Voltmeter and Ammeter are provided on panel for monitoring proper electrical supply
conditions.
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EXCLUSIVE FEATURES OF FLASH DRYING PLANT
Reduced running cost.
Continuous production machine without human touch.
Ideal replacement for tray drying of wet cakes.
Extremely sticky /pasty wet cake can be handled.
Particle size as fine as 500 mesh is achievable.
Low residence time minimum exposure to heat
retains original product quality.
On line particle size reduction-eliminating need of separate
pulverizer.
No product degradation or charring.
Proprietary design of disintegrator ensures uniform mixing
of wet cake and hot air giving consistent and homogeneous powder quality.
Fully Automatic needs little running attention.
Negligible material dusting.
High volume processing.
Large filtering area of Bag filter reduced pressure
drop large savings in power consumption of blower.
Measurement of pressure drops at various places facilitates
easy trouble shooting and maintenance.
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APPLICATIONS OF FLASH DRYER

Our Flash Dryer is a versatile machine and
ideal for wet / pasty press cakes. We list below industries where it can be used.
- Chemicals - Inorganic & Organic
- Pesticides and Agricultural Chemicals
- Dyestuff and Pigments Organic & Inorganic
- Fertilizers
- Mineral Ore Concentrates
- Technical Ceramics
- Food Industry
- Pharmaceutical Industry
- Agricultural extracts
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HOW WE MAKE FLASH DRYING PLANT HIGHLY ENERGY
EFFICIENT?

We ensure lowest drying cost by designing and manufacturing
energy efficient Flash Drying Plant. Our Flash Drying plant is highly Energy Efficient due
to following-
- Fuel cost is dominant in drying cost. We use 93% efficient
Hot Air Generator manufactured by our associate company. This reduces the fuel consumption
thereby reducing drying cost.
- The unique cage mill disintegrator with feeding system
allows high inlet air temperature without charring the material. This increases the
thermal efficiency of dryer decreasing drying cost.
- The use of high inlet air temperature reduces the plant size
thereby reducing the capital and civil cost.
- The individual components and sub-assemblies are tested as
per "Quality Assurance Plan" and then send to site. This reduces possibility of
malfunction of components and sub-assemblies thereby reducing downtime of Plant. Typical
Quality Assurance Plan is enclosed for reference.
- We use high efficiency blowers having efficiency up to 80%.
This reduces power consumption and drying cost.
- We design and select following components for low air
pressure drops-
- Air filter.
- Cage Mill Disintegrator.
- Duct and bends.
- Cyclone.
- Bag filter.
- Hot air generator.
Reduced pressure drop reduces the total
head requirement for the blower. This reduces the electrical power consumption of the
blowers thereby reducing drying cost.
- Provision of on-line secondary disintegrator eliminates the
need of separate pulverizer. This eliminates wastage of material and manpower required for
intermediate handling. This increases production and reduces drying cost.
- The plant is fully automatic requiring minimum manpower.
- On-line cleaning system like pulse-jet for filter bags
cleaning and knockers minimize the down time. This increases productivity reducing drying
cost.
There are many minute aspects to reduce the power
consumption, increase production yield, and reduce down time. These aspects are explained
in detail under the head "Main Components of Flash Dryer" and "Other
Components of Flash Dryer". |
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HOW
WE MAKE FLASH DRYING PLANT EASY TO OPERATE AND DIAGNOSE PROBLEMS?

1) Easy to Operate
- Fully automatic machine consisting of following
- Appropriate safety interlocks.
- PID temperature controller for ensuring constant air inlet
temperature. Steady state of burner giving minimum maintenance of burner.
- PID temperature controller with variable speed drive for
screw feeder ensuring constant air outlet temperature.
- Audio alarms for any deviation from the set parameter.
- Continuous monitoring / recording of vital parameters.
- Parameters like airflow rate, fuel firing rate, temperatures
and so on, are set once for all for a given material properties at the time of
commissioning. Hence it is easy to operate in subsequent runs.
2) Easy to diagnose problems
- The dryer is easy to diagnose for problems due to following
facilities-
- Continuous visual indication.
- Manometers for pressure drops of critical components.
- Viewing windows at strategic locations.
- In our service manual exhaustive troubleshooting chart is
given. Prior to handing over the dryer our service engineer educates the operators by
simulating various operating conditions.
This makes the Flash Dryer user friendly.
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COMPARISON BETWEEN TRAY DRYER & FLASH DRYER

Tray
Dryer |
Flash
Dryer |
1. |
Batch Type
Operation equipment. |
1. |
Continuous
operation equipment. |
2. |
Extensively
labour oriented, as labour is required for charging, arranging trays, pulverizing etc. |
2. |
No manual
handling involved hence substantial saving in labour cost. |
3. |
Separate
pulverizing operation needed. |
3. |
Pulverizing
and drying operation takes place simultaneously. |
4. |
Due to
considerable manual handling lot of material wastage and dusting takes place. |
4. |
Negligible
material wastage and dusting takes place. |
5. |
The material
being stacked in layers in the tray, uniform heating is not guaranteed and hence variation
in product quality, moisture content or the possibility of material in top layer getting
charred exists. |
5. |
Material being
disintegrated uniformly and thorough mixing of hot air & feed in disintegrator,
consistent product quality is ensured |
| 6. |
System
efficiency is low due to :
- Low inlet air temperature is required to avoid charring of
material, hence low thermal efficiency.
- Drying time is very high and much heat is wasted in the
exhaust.
|
6. |
High system
efficiency due to:
- High inlet air temperature can be used due to unique design
of cage mill type disintegrator.
- Low pressure drops in various components, requiring less
power for blowers.
- High efficiency Hot Air Generator.
- Fully automatic plant.
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RUNNING
COST COMPARISON BETWEEN FLASH AND TRAY DRYER
Parameter |
OUR FLASH
DRYER |
TRAY DRYER |
| Moisture evaporation rate |
500 kg/hr |
500 kg/hr |
| Product Output |
500 kg/hr |
500 kg/hr |
| Air temperature ° C |
250 / 110 |
100 |
| Utility consumption per hour |
Indirect fired
hot air generator |
Steam based
radiator |
|
|
60 liters |
120 liters |
|
|
90 kW |
20 Kw |
| Running cost per hour |
|
|
| Fuel (10 Rs/liter) |
600 Rs. |
1200 Rs. |
| Electricity (4 Rs/kWhr) |
360 Rs |
80 Rs. |
| Total Running Cost per hour |
960 Rs |
1280 Rs. |
| Savings per hour |
320 Rs. |
Nil |
| Savings per annum (7200 hours
per year) |
23,04,000
Rs. |
Nil |
|
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COMPARISON OF OUR FLASH DRYER AND SPIN FLASH DRYER
|
OUR
FLASH DRYER |
|
SPIN
FLASH DRYER |
1. |
No back mixing
of dry material with wet material takes place. |
1. |
Back mixing of
dry material with wet material takes place. |
2. |
Only fresh
material comes in contact with incoming hot air blast. This avoids charring of material. |
2. |
Both fresh and
back mixed dry material comes in contact with incoming hot air blast. This chars the
material |
3. |
No
classification of material occurs. |
3. |
Classification
of material occurs due to cyclonic motion of air. |
4. |
No sticking of
material to walls and no prolonged exposure to heat occurs, hence no degradation of
product. |
4. |
Sticking of
material to walls and prolonged exposure to heat degrades the product. |
See Figure
No. 8
RUNNING COST COMPARISON
Parameter |
OUR FLASH
DRYER |
SPIN FLASH
DRYER |
| Moisture evaporation rate |
500 kg/hr |
500 kg/hr |
| Product Output |
500 kg/hr |
500 kg/hr |
| Heat sensitive temperature °C |
150 |
150 |
| Air temperature °C |
250 / 110 |
150 / 80 |
| Utility consumption per hour |
Indirect fired
hot air generator |
Indirect fired
hot air generator |
|
|
60 liters |
120 liters |
|
|
90 kW |
180 kW |
| Running cost per hour |
|
|
| Fuel (10 Rs/liter) |
600 Rs. |
1200 Rs. |
| Electricity (4 Rs/kWhr) |
360 Rs |
720 Rs. |
| Total Running Cost per hour |
960 Rs |
1920 Rs. |
| Savings per hour |
960 Rs. |
Nil |
| Savings per annum (7200 hours
per year) |
69,12,000
Rs. |
Nil |
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