MINI PROJECT
ON
EXTRUDER
`
INTRODUCTION
 An extruder is a device that is specially designed to deliver
a raw material in molten form to a mold by means of labor
and die . An extruder is fed with solid-plastic (often granulate)
and releases molten plastic and slurry under pressure.
SCREW
 The screw drive supplies 80% of the melt energy.
 screw extruder:usually with a depth of around 0.5
mm, to obtain screw hardness of around 800 HV
and barrel hardness of approximately 1000 HV.
 Made of :Nitriding steels, Powder metallurgy steels,
or Bi-metals .The standard helix angle for most
extrusion screws is 17.6568º
HISTORY
1948, to blend molasses with
dry feedstuffs and compress
it into pellets.
1958, production of
expanded pet food.
TO UNDER STAND EXTRUDER
Extrusion
 Fixed cross-sectional
profile.
 A material is pushed
through a die
 very complex cross-
section, brittle,
because the material
only encounters
compressive and shear
stresses. Excellent
surface finish.
overview
TYPES OF EXTRUSION
 Based on ram position
 Based on crystalization
temperature
 Cold extrusion
 Hot extrusion
DIE DESIGN
 Replica of final product
circumference.
 Shapes
EXTRUDER
 Feed zone
 Melting
 mixing
FEEDING ZONE
 Screw
 Raw material
 motor
MELTING AND MIXING
 Addition of water
 Mixing
 Boiling to high
temperature
 Temperature
 Viscocity
SINGLE SCREW EXTRUDER
Fig: Single Screw Extruder
SINGLE SCREW EXTRUDER
PARTS & ITS FUNCTIONS
WENGER X20 SINGLE SCREW EXTRUDER
Fig: Wenger X20 Single Screw Extruder
PROCESS
1.In takes Raw material from the feeder,where there
is no need of driver to direct the material,we use
gravity in driving the materials.
.
2.The feeded material after undergoing volumetric
compression passes through single screw(clock
wise direction) for further compression of material
to get uniform composition
.
3.The mixed material after undergoing compression
along with addition of material is broken into
required dimension are sent for cooling down to
room temperature
.
4. Cooling of finished products take place at cooling
chamber containing moving layers
PARAMETERS
 Capacity:8-12t/h.
 Power:315kw.
 High efficiency.
 Efficiency:65%
 viscocity:1000Pa-s
 Flow rate:50g/m
 Internalpressure:0-60pa
 T mean=280f
RAW MATERIAL:
CONCLUSION
 High quality durable products.
 The man power reduction in making of food
products and evolution of extruder resulted in
 High efficiency.
 uniform flavoring.
 non-contaminating.
 uniform ingredient.
 We can achieve dust less and Improved product
THANK YOU

Extruder

  • 1.
  • 2.
    INTRODUCTION  An extruderis a device that is specially designed to deliver a raw material in molten form to a mold by means of labor and die . An extruder is fed with solid-plastic (often granulate) and releases molten plastic and slurry under pressure.
  • 3.
    SCREW  The screwdrive supplies 80% of the melt energy.  screw extruder:usually with a depth of around 0.5 mm, to obtain screw hardness of around 800 HV and barrel hardness of approximately 1000 HV.  Made of :Nitriding steels, Powder metallurgy steels, or Bi-metals .The standard helix angle for most extrusion screws is 17.6568º
  • 4.
    HISTORY 1948, to blendmolasses with dry feedstuffs and compress it into pellets. 1958, production of expanded pet food.
  • 5.
    TO UNDER STANDEXTRUDER Extrusion  Fixed cross-sectional profile.  A material is pushed through a die  very complex cross- section, brittle, because the material only encounters compressive and shear stresses. Excellent surface finish. overview
  • 6.
    TYPES OF EXTRUSION Based on ram position  Based on crystalization temperature  Cold extrusion  Hot extrusion
  • 7.
    DIE DESIGN  Replicaof final product circumference.  Shapes
  • 8.
    EXTRUDER  Feed zone Melting  mixing
  • 9.
    FEEDING ZONE  Screw Raw material  motor
  • 10.
    MELTING AND MIXING Addition of water  Mixing  Boiling to high temperature  Temperature  Viscocity
  • 11.
    SINGLE SCREW EXTRUDER Fig:Single Screw Extruder
  • 12.
  • 13.
    WENGER X20 SINGLESCREW EXTRUDER Fig: Wenger X20 Single Screw Extruder
  • 14.
    PROCESS 1.In takes Rawmaterial from the feeder,where there is no need of driver to direct the material,we use gravity in driving the materials.
  • 15.
    . 2.The feeded materialafter undergoing volumetric compression passes through single screw(clock wise direction) for further compression of material to get uniform composition
  • 16.
    . 3.The mixed materialafter undergoing compression along with addition of material is broken into required dimension are sent for cooling down to room temperature
  • 17.
    . 4. Cooling offinished products take place at cooling chamber containing moving layers
  • 18.
    PARAMETERS  Capacity:8-12t/h.  Power:315kw. High efficiency.  Efficiency:65%  viscocity:1000Pa-s  Flow rate:50g/m  Internalpressure:0-60pa  T mean=280f
  • 19.
  • 20.
    CONCLUSION  High qualitydurable products.  The man power reduction in making of food products and evolution of extruder resulted in  High efficiency.  uniform flavoring.  non-contaminating.  uniform ingredient.  We can achieve dust less and Improved product
  • 21.