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DRYING TECHNOLOGIES
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CONTENTSINTRODUCTION TO THE TECHNOLOGY OF DRYERS
BELT ROTARY “JET ZONE”
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FOOD preservation / stabilisation unit operation
= decrease in product moisture
FOOD SAFETY
Decrease in product moisture
= ENERGY INPUT water evaporation
Reach the product's QUALITY OBJECTIVES
▪ Control and compliance with the H20 objective
▪ Organoleptic quality (formulation, texturization)
▪ Absence of enzymatic and non-enzymatic reactions, and of
the development of microorganisms
FUNCTIONALITIES AND OBJECTIVES OF
THE FOOD DRYING PROCESS
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QUALITY CRITERIA
PRODUCT MOISTURE
▪ Formula: H2O = 100*(water mass / wet product mass)
▪ RAPID measurement method:
• NIR = spectrophotometer close to infrared
• Scales to measure moisture= Method utilised at the research centre (during tests)
▪ STANDARD measurement method = DRY MATTER ANALYSIS
WATER ACTIVITY (aw) = availability of water in the analysed food
▪ Measurement range between 0 and 1
▪ Widely studied parameters in the food industry, for example: pet food, co-
extrusion, fruit cake, etc.
▪ Measurement with “aw meter - Water Activity Meter”
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Extruded Products Drying Theory
AIR NOTION
ABSOLUTE HUMIDITY (AH)
= mass of water / mass of dry air
Wet wick
DRY AIRFLOW
MOIST AIRFLOW
Initial (Ta) = DRY AIR TEMPERATURE
(In this case gaz type = Air)
Subsequent (Th) =MOIST AIR TEMPERATURE
=> Temperature given by a probe wrapped inside
a wet wick:
=> (Th) always < (Ta)
RELATIVE HUMIDITY (RH):
RH (%)= Actual Vapor Density / Saturated Vapor Density x 100%
Also known as the hygrometric degree
At saturation: RH = 100% (Dew Point)
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EXTRUDED PRODUCTS DRYING THEORYPRINCIPLE OF CONVECTION DRYING
Energy transmission = CONVECTION
Drying mode = DRIVEN
HOT AND DRY AIR FLOW
WET PRODUCT
• MOIST AIR FLOW
• COOLER
ENERGY
INCREASED PRODUCT TEMPERATURE:
• T product surface < :
• T hot air
• T boiling of water in the product
EVAPORATION OF THE
PRODUCT’S WATER
WATER VAPOR
SIMULTANEOUS
TRANSMISSION
HEAT / MATTER
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T0 = 29°C
T max = 65°C at t = 15 min
Bound water evaporation
▪ Water absorbed in the walls of structures
▪ Water more difficult to extract
Free water evaporation
▪ Superficial water
▪ Lightly bound to the product
EXTRUDED PRODUCTS DRYING THEORY
EVAPORATION NOTION (FREE & BOUNDED)
The availability of water depends on the product and has different functions.
Oxygen atom
(O)
Hydrogen atom (H)
Hydrogen atom (H)
Water (H2O)
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TYPICAL CURVE OF CONVECTION DRYING
Retention time
Product MOISTUREProduct Temperature
10 – 2 %
30 -15%
Initial sudden drop
Constant rise
Slow rise
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EXTRUDED PRODUCTS DRYING
DRYING KINETICS
PHASE 2 – CONSTANT DRYING SPEED
• Tp = Th = constant if constant air
conditions stable
• Driven Drying:
o High Air Temperature
o High air speed
o Dryer air
PHASE 1 – ADJUSTING TEMPERATURE
• Tp : product introduced cold or hot
• High Thermal Energy & Fast Drying speed
↗
• Evaporation at the product’s surface
PHASE 3 – DRYING DECREASE
• Drying speed ↘
• Contributed energy:
less water for evaporation
less drying energy required
Tp ↗ and Air Temperature ↗ and
drying ↘
1
2
3
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EXTRUDED PRODUCTS DRYING
BASIC FACTORES TO CONTROL DRYING
• TEMPERATURE
• AIR FLOW (VOLUME & SPEED)
• RELATIVE AIR MOISTURE
• RESIDENCE TIME
• PRODUCT VOLUME
• PRODUCT CHARARCTERISTICS
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WATER HOLDING CAPACITY BY THE AIR
➢ Heated air at 90°C has 100X of water holding capacity than air at 20 °C ➢With higher temperature the air can hold more water
EXTRUDED PRODUCTS DRYING
TEMPERATURE EFFECT
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TEMPERATURE EFFECT IN THE RESIDENCE TIME FOR POROUS PRODUCTS
➢ Heated air at 90°C has 100X of water holding capacity than air at 20 °C ➢With higher temperature the air can hold more water
EXTRUDED PRODUCTS DRYING
TEMPERATURE EFFECT
Drying Temperature°C
Drying Time
(min)
100 120 140 160 180
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AIR FLOW EFFECT TO THE PRODUCT DRYING TIME
EXTRUDED PRODUCTS DRYING
AIR FLOW EFFECT
Air Flow Speed (m/s)
Drying Time (min)
The higher the air velocity the higher the heat transfert and drying speed
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DISTRIBUTION OF HOT AIRINTO THE PRODUCT’S LAYERS
140 °C
120 °C100 °C80 °C
150 °C
70 °C
IDEAL
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EXTRUDED PRODUCTS DRYING
PRODUCT LAYER EFFECT
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SNACK line example
DRYING TECHNOLOGYClextral EVOLUM belt dryer
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CLEXTRAL EVOLUM DRYER
1200
600
300
Models:
-EV300
-EV600
-EV1200
ProductsEV 300
(kg/h at Dryer Outlet)EV 600
(kg/h at Dryer Outlet)EV 1200
(kg/h at Dryer Outlet)
SNACKS 250 / 300 500 / 600 1000 / 1200
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Product
input
Product output
Conveyor belt
AIR CONDITIONS:
-Recirculation fan
-Air flow measurement in the
dryer
-Recirculation of part of the air
-Controlled T
-Uncontrolled RH
Air heated with gas burner or electric resistance
AIR EXTRACTOR
Air transmission
limitation
Receiving hopper
Product
Spreader
Under the plenum
Plenum
height
Zone 1
Zone 2
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DRYING TECHNOLOGY
ROTANTE Rotary dryer for small Ingredients
Example: Couscous line
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ROTANTE ROTARY DRYER
Short Pasta Line
1800 kg/h
3000 kg/h
Couscous Line
1200 kg/h
1800 kg/h
3600 kg/h
Ingredients Line
200 – 300 kg/h
350 – 600 kg/h
700 – 1000 kg/h
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SUPERIOR BUILD
- Centrifugal fans
- Batteries (Exchangers)
- Air extraction fan
INFERIOR BUILD
ROTANTE ROTARY DRYER
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Feeding inlet
DischargingOutlet
ROTANTE Rotary dryer - INFERIOR BUILD
Rolling drum cage
✓ Rolling drum cage
Product moves very slowly through the dryer
✓ Linear ascent on the Archimedes screws
✓ Rolling drum cage with Archimedes screws covered with steel
sheeting
2 Archimedes screws to recover fine particles
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ROTANTE Rotary dryer
COMPLEMENTARY FEATURES OF THE ROTARY DRYER
▪ ABSENCE OF DEAD ZONES:
• Homogeneous drying
• No contamination among different products
HYGIENE
▪ LINEAR PRODUCT FLOW:
• Drying control
• Possibility of defining 2 independent zones
FLEXIBILITY , CONSTANT PRODUCT QUALITY - RELIABILITY
Pertes thermiques totales par
les extractions
11%
Energie sensible cédée au
support
0%
Pertes thermiques totales par
les parois du sécheur
1%
Energie totale
cédée au produit
88%
Energy efficiency90%
Total thermal losses through the walls of the dryer 1 %
Total thermal losses through extractions 11%
Total energy transferred to the
product 88%
Sensible energy transferred to the
support 0%
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“JET ZONE” TYPE DRYER/TOASTER
Example: Extruded Flakes Line
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Two zones,
gas-activated direct air intrusion
toaster-dryer
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CRUNCHY
TOASTED FLAKES
Chewy
flakes
INTRUSION TOASTER
(FLUIDISED BED)
HOT AIR
185-195°C215- 225°C
Two zones, gas-activated direct air
intrusion toaster-dryer
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Drying Technology - Importance of the cooler
▪ Necessary operation for the preservation of food products
= FOOD SAFETY
▪ Prevents condensation of the evaporating water during cooling after leaving
the dryer
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