EXTRUDER - libvolume5.xyzlibvolume5.xyz/industrialmanagementengineering/btech/semester6/...Extruder...
Transcript of EXTRUDER - libvolume5.xyzlibvolume5.xyz/industrialmanagementengineering/btech/semester6/...Extruder...
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EXTRUDER
Motor
Water
pump
Hopper
Feeder
Cutter
Feeding
barrel
Heating
system
Cooling
system
Die
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Clextral EVOLUM 53 Extruder
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Extruder
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Extruder development in the food industry
Mid-1930s Single screw continuous pasta press
1940 Oil extraction
1950 Pet foods
1960s RTE cereals
1980s Aquatic feeds
In 1998 Retail value of extruded products: $3.62 billion
or 3.7 million tons of production
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Extruder Classification
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Heat Generation
Adiabatic Isothermal Polytropic
Extruders
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Single
screw
extruders
Intermeshed Non
intermeshined
Counter rotating
Self-wiping Partially
self-wiping
Intermeshed non
Intermeshed
Co-rotating
Twin
screw
extruders
Continuous screw extruders
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Feed
Moisture
(%)
Product
Temperature
(oC)
Screw
Speed
(rpm)
Typical
Products
Twin-screw
cooking
extruder
11-35 80-200 200-500 Puffed snacks
RTE cereals
High-shear
cooking
extruder
15-20 120-180 350-500 Modified
starch
Low-shear
cooking
extruder
11-16 170-200 300 Puffed snacks
High-pressure
forming
extruder
25 65-80 40 Cereal pellets
Half-product
snacks
Pasta press 32 30-52 30 Pasta
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Screw(s) Die
Basic extruder components
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SCREWS and SHAFTS
Conical
screw
caps
Shaft
Screw
elements
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1/2 P - 6 unitsTwin-flight
3/4 P - 9 units
Twin-flight
3/4 P - 9 unitsSingle-flight
1/2 P - 9 unitsTwin-flight
1/1 P - 9 units
Twin-flight
3/4 P - 6 unitsTwin-flight
Cone-screw
Washer
1/2 P -cut6 units
Twin-flight
Paddles 0.75 units Paddles 1
unit
3/4 P4.5 units
Twin-flight
3/4 P - cone9 units
1/2 P - Rev1.5 units
1/2 P0.75 units
3/4 P - cone9 units - cut
Shaft Collar
3 units
Disks 0.75 units
3/4 P - cut9 units
Twin-flight
1/2 P - Rev0.75 units
1/2 P - Rev6 unitsTwin-flight
Elements for generating screw profiles and pressures
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D= screw diameter
h= channel depth
t= pitch
N= screw speed
=
D
t 2/ tan 1-φ
e= axial flight tip thickness
n= number of screw threads,
δ= clearance between flight tips and barrel
φ= screw helix angle (a function of diameter and pitch)
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Advantages of Extrusion Process
�Adaptability
� Product variety
� Energy efficiency
� Low cost
� Unique products
� Increased throughput
� Product quality
�Minimal waste
�Minimum labor
� Combine several steps in conventional process
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Processing steps with conventional process Product
group
Product
example
Conventional
process
Cooking
Baking
Gelatinizing
Roasting
Caramelizing
Crystallizing
Material exch
ange
Reaction
Maillard
reaction
Enzym
e inactivation
Sterilization
Alkalizing
Drying
Precipitation
Mixing, kneading
Dispersing
Shaping
Expanding
Heating
Cooling
Den
aturing
Modified
flours
Baby food Drum dryer
Texturized
proteins
Meat
substitutes
Spinning
system
Aquaculture Presses Animal feeds
Pet food Oven
Flavors Meat flavors
Caramel
Roasting
kettle
Baked goods Flat bread, bread crumbs
Baking oven
Puffed grains Puffing-gun Breakfast
cereals Cereal flakes Cooker
Pasta Oriental noodles
Cooker
Coffee Roaster Drinks
Instant powders
Cooker
Liquorice Cooker
Chocolate Press
Confections
Sugar Crystallizer
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PROCESSING STEPS IN A EXTRUDER
Feeder Die
Feeding
zone
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Single screw extruder
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Twin screw extruder (Corotating)
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Twin screw extruder (Counterrotating)