INJECTION MOULDING (IM)
INJECTION MOULDING (IM)
EXAMPLE OF PRODUCTS
EXAMPLE OF PRODUCTS
• SCHEMATIC DIAGRAM OF BASIC
PROCESS OF INJECTION MOULDING
AND TYPES OF INJECTION MOULDING
MACHINE
• Concept is simple
• Melt plastic, flow into mold and take part shape,
cool, de-mold (ejection)
FIGURE 1-4a
SCHEMATIC DIAGRAM OF
SCHEMATIC DIAGRAM OF
INJECTION MOULDING MACHINE
INJECTION MOULDING MACHINE
SCHEMATIC DIAGRAM OF
SCHEMATIC DIAGRAM OF
INJECTION MOULDING SYSTEM
INJECTION MOULDING SYSTEM
BASIC STEPS IN INJECTION
BASIC STEPS IN INJECTION
MOULDING PROCESS
MOULDING PROCESS
1. MELTING OF PLASTIC
2. INJECTION OF PLASTIC MELT INTO CLOSED
MOULD
3. COOLING OF PLASTIC IN CLOSED MOULD
4. MOULD OPENING AND EJECTION OF PLASTIC
PART/S
CONVENTIONAL INJECTION
CONVENTIONAL INJECTION
MOULDING
MOULDING
PISTON TYPE PREPLASTIFYING
PISTON TYPE PREPLASTIFYING
SCREW TYPE PREPLASTIFYING
SCREW TYPE PREPLASTIFYING
Plunger type machine
• used prior to the invention of the reciprocating screw
• Step 1: resin melts via thermal heaters and collects in a
pool called injection chamber
• Step 2: resin pushed forward by action of plunger (ram or
piston) driven by hydraulic system at the head of the
machine. A torpedo or spreader is used in barrel to
improve melting and mixing.
• Step 3: resin flows into mold
• Step 4: part cools and is ejected
Ram injection advantages
• less expensive
• better for marbling of plastics
RECIPROCATING SCREW
RECIPROCATING SCREW
INJECTION
INJECTION
• USUALLY USED FOR THERMOPLASTIC OR UN-
REINFORCED THERMOSET
• CAN BE USED TO PRODUCE COMPOSITE
MATERIALS (ALL TYPES ??)
• THIS IS DISCRETE OR DISCONTINUOUS
PROCESS
• CAN PRODUCE COMPLEX PRODUCTS/PARTS
• ALMOST ALL THERMOPLASTICS AND SOME
THERMOSETS CAN BE PROCESSED USING
INJECTION MOULDING
• PP, PA, PC
• IS THE MOST POPULAR MACHINE TO
PROCESS PLASTICS
Reciprocating screw advantages:
• more uniform melting
• more uniform mixing
• lower injection pressures
• larger permissible part area
• fewer stresses in part
• faster total cycle
CLASSIFICATION OF PLASTIC PERFORMANCE
CLASSIFICATION OF PLASTIC PERFORMANCE
RANGE
RANGE
ADVANTAGES OF INJECTION MOUDING
ADVANTAGES OF INJECTION MOUDING
• HIGH PRODUCTIVITY
• HIGH VOLUME PRODUCTION
• LOW LABOUR COST PER UNIT MACHINE (BUT
THE COST OF THE MACHINE IS VERY HIGH)
• DO NOT NEED FINISHING
• DIFFERENT SURFACE, COLOUR AND FINISHING
CAN BE PRODUCED
• DIFFERENT TYPES OF PLASTICS CAN BE
USED WITHOUT THE NEED TO CHANGE
MACHINE OR MOULD
• FOR MOST DESIGN, THIS PROCESS IS THE
MOST ECONOMICAL
• PROCESS IS AUTOMATED AND HIGHLY
REPEATABLE PART
DISADVANTAGES OF INJECTION MOULDING
DISADVANTAGES OF INJECTION MOULDING
• LOW PROFIT MARGIN
– THREE SHIFTS
• COST OF THE MOULD IS VERY HIGH
• PROCESS CONTROL IS NOT SO GOOD
• CONSISTENCY ISSUE DURING OPERATION
• DIFFICULT TO CHECK THE QUALITY OF THE
PARTS IMMEDIATELY AFTER MOULDING
• COST OF THE MACHINE AND EQUIPMENT IS
HIGH
BASIC PROCESS
BASIC PROCESS
PLASTICISED PLASTIC OR
PLASTIC MELT WAS INJECTED OR
FORCED INTO A MOULD, COOLED
AND EJECTED IN SOLID FORM
(THE SHAPE SHOULD BE THE
SAME AS THE SHAPE OF THE
CAVITY/MOULD)
ONE/SINGLE CAVITY MOULD OR
MULTI CAVITY MOULD WITH THE
SAME OR DIFFERENT (??) SHAPE
AND SIZE (EACH ONE IS
CONNECTED BY FLOW CHANNEL
OR RUNNER) WHICH DIRECTED
THE MELT INTO EACH CAVITY
SPRUE, RUNNER, GATE DAN KAVITY
SPRUE, RUNNER, GATE DAN KAVITY
• Key terms
– sprue bushing- part of mold (cooled)
– nozzle- end of injection (heated)
– sprue channel- from bushing to runner
– runners- feeds material from sprue to part
– gate- mold area between runner and part
– mold cavity- concave part of mold
– mold core- convex part of mold
– multi-cavity- more than one part in a cavity
– ejectors- knock out pins
– mold inserts- multiple cavities for same base
– mold base- inserts used in same base
– MUD base- Master Unit Die (you can change insert without
to change the whole mould)
– draft angle- minimum angle from bottom to top of
part
– parting line- the split between core and cavity
molds
FOUR (4) BASIC OPERATIONS:
FOUR (4) BASIC OPERATIONS:
• INCREASED THE PLASTIC
TEMPERATURE – FLOW UNDER
PRESSURE – HEATING AND MIXING IN
ONE STEP – HOMOGENEOUS MELT
(TEMPERATURE AND VISCOSITY). THE
WHOLE PROCESS IS CALLED
‘PLASTICATION’ OR ‘PLASTICIZING’
• TO SOLIDIFY THE PLASTIC MELT INSIDE
CLOSE MOULD
• COOLING
• OPEN THE MOULD TO EJECT THE
PLASTIC PART/S OUT (EJECTION)
PRODUCTIVITY WILL DEPEND ON:
– HOW FAST TO MELT THE PLASTIC (HOW TO
CONTROL ??)
– HOW FAST TO INJECT THE MELT INTO THE
MOULD (HOW TO CONTROL ??)
– HOW LONG TIME TAKEN TO COOL THE MELT
IN THE MOULD (HOW TO CONTROL ??)
– INJECTION CYCLE (CYCLE TIME)
Typical Cycle Time
Typical Cycle Time
BASIC COMPONENTS FOR INJECTION
BASIC COMPONENTS FOR INJECTION
MOULDING SYSTEM:
MOULDING SYSTEM:
• COMPOUNDING
• DRYING (??)
• FEEDING
• METERING
• PLASTICATION (MELTING)
• INJECTION
• COOLING
• EJECTION
MECHANICAL MOVEMENT DURING
MECHANICAL MOVEMENT DURING
PROCESSING:
PROCESSING:
• MOULD CLOSED (CLAMPING)
• INJECTION RAM/SCREW MOVE FORWARD TO
INJECT THE PLASTIC MELT
• SCREW MOVE BACKWARD (COOLING OF THE
MELT INSIDE THE MOULD)
• SCREW STOP ROTATING AND MOULD OPEN
• EJECTION OF PLASTIC PART/S FROM THE
MOULD
Resin feed into
the barrel
Shot/plastic melt
accumulates here
CAVITY GETS
FILLED
SCREW
MOVES
FORWARD
COOLING LINES
PRESSURE IS MAINTAINED
IN CAVITY
MOULD IS OPENED
TO OBTAINED OPTIMUM RESULTS FOR
TO OBTAINED OPTIMUM RESULTS FOR
ANY PLASTIC AND MOULD:
ANY PLASTIC AND MOULD:
NEED TO OPTIMIZED:
• MELTING TEMPERATURE
• INJECTION PRESSURE
• INJECTION SPEED
MELTING TEMPERATURE
MELTING TEMPERATURE
• DIFFERENT PLASTICS WILL HAVE DIFFERENT
Tm
• DIFFERENT TYPES OF PLASTICS WILL HAVE
DIFFERENT VISCOSITY (EASE OF FLOW) –
DIFFERENT GRADES
• PLASTIC FLOW IS NON-NEWTONIAN (NON
LINEAR RELATIONSHIP BETWEEN PRESSURE
AND FLOW)
• FLOW BEHAVIOUR CANNOT BE REPRESENTED
BY ONE VALUE ONLY
EXAMPLE OF PLASTIC VISCOSITY
EXAMPLE OF PLASTIC VISCOSITY
AT DIFFERENT TEMPERATURE
AT DIFFERENT TEMPERATURE
MATERIAL
(NYLON)
VISCOSITY AT 1,000 s-1
240˚C 260˚C 280˚C 300˚C
1 98 78 63 50
2 149 115 89 69
3 394 319 259 210
EXAMPLE OF PLASTIC VISCOSITY
EXAMPLE OF PLASTIC VISCOSITY
AT DIFFERENT SHEAR RATE
AT DIFFERENT SHEAR RATE
MATERIAL VISCOSITY AT 280˚C
100s-1
1000s-1
10000s-1
100,000s-1
1 197 63 20 6
2 323 89 25 7
3 1220 259 55 12
• IN MOST CASES, PLASTIC WILL BEHAVE AS
PSEUDOPLASTIC - LESS VISCOS (FLOW EASILY)
WHEN THEY ARE MOVED FASTER
• VISCOSITY REDUCED WHEN SHEAR RATE IS
INCREASED (EASIER TO FILL THE MOULD)
• INCREASE THE MELTING TEMPERATURE WILL
REDUCE THE INJECTION PRESSURE NEEDED AT
SPECIFIC FLOW RATE
MOULDING TEMPERATURE OF DIFFERENT
MOULDING TEMPERATURE OF DIFFERENT
TYPES OF PLASTICS
TYPES OF PLASTICS
INJECTION PRESSURE
INJECTION PRESSURE
• DURING MOULD FILLING, HIGH INJECTION
PRESSURE IS NEEDED TO MAINTAIN
INJECTION SPEED DURING PROCESSING
• WHEN THE MOULD IS FILLED, HIGH
PRESSURE IS NO LONGER NEEDED
• 2 STEPS PRESSURE CAN BE USED
INJECTION SPEED
INJECTION SPEED
(SPEED TO FILL THE MOULD)
(SPEED TO FILL THE MOULD)
• WHEN MOULDING THIN PRODUCT, HIGH
SPEED IS NEEDED TO FILL THE MOULD
• TO OBTAIN GOOD SURFACE FINISH FOR
THICK PRODUCT, LOW INJECTION SPEED CAN
BE USED
• FOR ALMOST ALL MACHINE, TIME TO FILL THE
MOULD IS ABOUT 1 SECOND
Injection Unit
Injection Unit
• Purpose
– Melt solid pellets to liquid form and then inject into mold
• Steps
– Hopper- manual or pneumatic loaded. Can have a
mixer, volumetric or gravimetric units to meter material.
– Screw
• Reciprocating screw
– most common
– similar to general purpose extrusion screw
– much shorter than extrusion screws, L/D of 12:1 to 20:1
– compression ratios (diameter of feed to diameter of metering)
are often 2:1 to 5: 1 which is lower than for extrusion.
– lower compression ratio means less mechanical action and
heating
– Step 1: turns of the screw melts resin and collects it at end of
screw
– Step 2: the screw moves forward via a hydraulic mechanism
– Step 3: retraction of screw
– Step 4: part cooling and removal
Clamping
Clamping Unit
Unit
• Clamping Force
– Clamping unit holds the molds together while the resin is injected, packed, and
cooled, and ejected.
– Clamping force is the rating of the injection molder, e.g., 150 tons clamping force.
• Clamping force = Injection Pressure x Total Cavity Projected Area
– Projected area is the area projected into a single plane, that is, the widest area of
the part.
– Examples
• The force necessary to mold a part that has 100 in2
projected area and has
3,000 psi is 3,000 * 100 = 300,000 lbs force = 150 tons (note 1 ton = 2000
lbs)
• The maximum projected surface area of a part on a 200 ton machine with a
maximum injection pressure of 2,000 psi is: 400,000 lbs force / 2,000 psi =
200 in2
A
P
F 

INJECTION RATE
INJECTION RATE
• INJECTION RATE MAY BE VARIED
• FAST – THIN PRODUCT AND REDUCED TIME
• INJECTION RATE DEPEND ON MACHINE SIZE
• INJECTION RATE CAPABILITY IS DIRECTLY
PROPORTIONAL TO HYDRAULIC PUMP.
• HYDRAULIC PRESSURE WILL DETERMINE THE
INJECTION PRESSURE
• Part Design
– The underlying principles behind part design,
other than part functionality are
• cooling of plastic from melt to glassy state
• heat transfer from various sections
• thermal shrinkage of the plastic parts
– Heat transfer is best when the parts have the
same thickness
• Inside portions of parts cool more slowly than
the part surfaces
• Center portion will shrink more than the
surface
MACHINE SIZE
MACHINE SIZE
• FROM A FEW GRAMS TO A FEW POUNDS (CAN
GO UP TO 395 POUND, CLAMPING STRENGTH
UP TO 10,000 TON)
• ‘MINIATURE INJECTION MOULDING MACHINE’
(FIGURE). THERE MANY CHALLENGES IN THE
FUTURE. THE REQUIREMENTS FOR MICRO-
MOULD:
– ADVANCED HEATING AND COOLING
– VACUUM FOR CAVITI
– SPECIFIC SENSOR
– HIGH PRECISION TOOLINGS ARE NEEDED
MINIATURE INJECTION MOULDING MACHINE
MINIATURE INJECTION MOULDING MACHINE
• VERY BIG INJECTION MOULDING MACHINE (SEE
NEXT SLIDE) – AUTOMOTIVE, BUILDING,
AEROSPACE, SPORTS, CONSTRUCTION ETC.
– CAR PANEL/BODY
– WASHING MACHINE, FREEZER
– BOAT
– SWIMMING POOL
– EXAMPLE:
• HUSKEY E8000
• CLAMP FORCE - 8000 TON
• PLATEN SIZE: 19 X 16 X 13’
• INJECTION WEIGHT: 20 – 145 POUND
VERY BIG INJECTION MOULDING MACHINE
VERY BIG INJECTION MOULDING MACHINE
INJECTION MOULDING PART TWO BRIEF INTRODUCTION NOTES

INJECTION MOULDING PART TWO BRIEF INTRODUCTION NOTES

  • 1.
  • 2.
  • 3.
    • SCHEMATIC DIAGRAMOF BASIC PROCESS OF INJECTION MOULDING AND TYPES OF INJECTION MOULDING MACHINE • Concept is simple • Melt plastic, flow into mold and take part shape, cool, de-mold (ejection) FIGURE 1-4a
  • 5.
    SCHEMATIC DIAGRAM OF SCHEMATICDIAGRAM OF INJECTION MOULDING MACHINE INJECTION MOULDING MACHINE
  • 6.
    SCHEMATIC DIAGRAM OF SCHEMATICDIAGRAM OF INJECTION MOULDING SYSTEM INJECTION MOULDING SYSTEM
  • 9.
    BASIC STEPS ININJECTION BASIC STEPS IN INJECTION MOULDING PROCESS MOULDING PROCESS 1. MELTING OF PLASTIC 2. INJECTION OF PLASTIC MELT INTO CLOSED MOULD 3. COOLING OF PLASTIC IN CLOSED MOULD 4. MOULD OPENING AND EJECTION OF PLASTIC PART/S
  • 10.
  • 11.
  • 12.
  • 13.
    Plunger type machine •used prior to the invention of the reciprocating screw • Step 1: resin melts via thermal heaters and collects in a pool called injection chamber • Step 2: resin pushed forward by action of plunger (ram or piston) driven by hydraulic system at the head of the machine. A torpedo or spreader is used in barrel to improve melting and mixing. • Step 3: resin flows into mold • Step 4: part cools and is ejected Ram injection advantages • less expensive • better for marbling of plastics
  • 14.
  • 15.
    • USUALLY USEDFOR THERMOPLASTIC OR UN- REINFORCED THERMOSET • CAN BE USED TO PRODUCE COMPOSITE MATERIALS (ALL TYPES ??) • THIS IS DISCRETE OR DISCONTINUOUS PROCESS • CAN PRODUCE COMPLEX PRODUCTS/PARTS
  • 16.
    • ALMOST ALLTHERMOPLASTICS AND SOME THERMOSETS CAN BE PROCESSED USING INJECTION MOULDING • PP, PA, PC • IS THE MOST POPULAR MACHINE TO PROCESS PLASTICS
  • 17.
    Reciprocating screw advantages: •more uniform melting • more uniform mixing • lower injection pressures • larger permissible part area • fewer stresses in part • faster total cycle
  • 18.
    CLASSIFICATION OF PLASTICPERFORMANCE CLASSIFICATION OF PLASTIC PERFORMANCE RANGE RANGE
  • 19.
    ADVANTAGES OF INJECTIONMOUDING ADVANTAGES OF INJECTION MOUDING • HIGH PRODUCTIVITY • HIGH VOLUME PRODUCTION • LOW LABOUR COST PER UNIT MACHINE (BUT THE COST OF THE MACHINE IS VERY HIGH) • DO NOT NEED FINISHING • DIFFERENT SURFACE, COLOUR AND FINISHING CAN BE PRODUCED
  • 20.
    • DIFFERENT TYPESOF PLASTICS CAN BE USED WITHOUT THE NEED TO CHANGE MACHINE OR MOULD • FOR MOST DESIGN, THIS PROCESS IS THE MOST ECONOMICAL • PROCESS IS AUTOMATED AND HIGHLY REPEATABLE PART
  • 21.
    DISADVANTAGES OF INJECTIONMOULDING DISADVANTAGES OF INJECTION MOULDING • LOW PROFIT MARGIN – THREE SHIFTS • COST OF THE MOULD IS VERY HIGH • PROCESS CONTROL IS NOT SO GOOD • CONSISTENCY ISSUE DURING OPERATION • DIFFICULT TO CHECK THE QUALITY OF THE PARTS IMMEDIATELY AFTER MOULDING • COST OF THE MACHINE AND EQUIPMENT IS HIGH
  • 22.
    BASIC PROCESS BASIC PROCESS PLASTICISEDPLASTIC OR PLASTIC MELT WAS INJECTED OR FORCED INTO A MOULD, COOLED AND EJECTED IN SOLID FORM (THE SHAPE SHOULD BE THE SAME AS THE SHAPE OF THE CAVITY/MOULD)
  • 23.
    ONE/SINGLE CAVITY MOULDOR MULTI CAVITY MOULD WITH THE SAME OR DIFFERENT (??) SHAPE AND SIZE (EACH ONE IS CONNECTED BY FLOW CHANNEL OR RUNNER) WHICH DIRECTED THE MELT INTO EACH CAVITY
  • 24.
    SPRUE, RUNNER, GATEDAN KAVITY SPRUE, RUNNER, GATE DAN KAVITY
  • 30.
    • Key terms –sprue bushing- part of mold (cooled) – nozzle- end of injection (heated) – sprue channel- from bushing to runner – runners- feeds material from sprue to part – gate- mold area between runner and part – mold cavity- concave part of mold – mold core- convex part of mold – multi-cavity- more than one part in a cavity – ejectors- knock out pins – mold inserts- multiple cavities for same base – mold base- inserts used in same base – MUD base- Master Unit Die (you can change insert without to change the whole mould) – draft angle- minimum angle from bottom to top of part – parting line- the split between core and cavity molds
  • 31.
    FOUR (4) BASICOPERATIONS: FOUR (4) BASIC OPERATIONS: • INCREASED THE PLASTIC TEMPERATURE – FLOW UNDER PRESSURE – HEATING AND MIXING IN ONE STEP – HOMOGENEOUS MELT (TEMPERATURE AND VISCOSITY). THE WHOLE PROCESS IS CALLED ‘PLASTICATION’ OR ‘PLASTICIZING’
  • 32.
    • TO SOLIDIFYTHE PLASTIC MELT INSIDE CLOSE MOULD • COOLING • OPEN THE MOULD TO EJECT THE PLASTIC PART/S OUT (EJECTION)
  • 33.
    PRODUCTIVITY WILL DEPENDON: – HOW FAST TO MELT THE PLASTIC (HOW TO CONTROL ??) – HOW FAST TO INJECT THE MELT INTO THE MOULD (HOW TO CONTROL ??) – HOW LONG TIME TAKEN TO COOL THE MELT IN THE MOULD (HOW TO CONTROL ??) – INJECTION CYCLE (CYCLE TIME)
  • 34.
  • 35.
    BASIC COMPONENTS FORINJECTION BASIC COMPONENTS FOR INJECTION MOULDING SYSTEM: MOULDING SYSTEM: • COMPOUNDING • DRYING (??) • FEEDING • METERING • PLASTICATION (MELTING) • INJECTION • COOLING • EJECTION
  • 36.
    MECHANICAL MOVEMENT DURING MECHANICALMOVEMENT DURING PROCESSING: PROCESSING: • MOULD CLOSED (CLAMPING) • INJECTION RAM/SCREW MOVE FORWARD TO INJECT THE PLASTIC MELT • SCREW MOVE BACKWARD (COOLING OF THE MELT INSIDE THE MOULD) • SCREW STOP ROTATING AND MOULD OPEN • EJECTION OF PLASTIC PART/S FROM THE MOULD
  • 37.
    Resin feed into thebarrel Shot/plastic melt accumulates here
  • 38.
  • 39.
    COOLING LINES PRESSURE ISMAINTAINED IN CAVITY
  • 40.
  • 41.
    TO OBTAINED OPTIMUMRESULTS FOR TO OBTAINED OPTIMUM RESULTS FOR ANY PLASTIC AND MOULD: ANY PLASTIC AND MOULD: NEED TO OPTIMIZED: • MELTING TEMPERATURE • INJECTION PRESSURE • INJECTION SPEED
  • 42.
  • 43.
    • DIFFERENT PLASTICSWILL HAVE DIFFERENT Tm • DIFFERENT TYPES OF PLASTICS WILL HAVE DIFFERENT VISCOSITY (EASE OF FLOW) – DIFFERENT GRADES • PLASTIC FLOW IS NON-NEWTONIAN (NON LINEAR RELATIONSHIP BETWEEN PRESSURE AND FLOW) • FLOW BEHAVIOUR CANNOT BE REPRESENTED BY ONE VALUE ONLY
  • 45.
    EXAMPLE OF PLASTICVISCOSITY EXAMPLE OF PLASTIC VISCOSITY AT DIFFERENT TEMPERATURE AT DIFFERENT TEMPERATURE MATERIAL (NYLON) VISCOSITY AT 1,000 s-1 240˚C 260˚C 280˚C 300˚C 1 98 78 63 50 2 149 115 89 69 3 394 319 259 210
  • 46.
    EXAMPLE OF PLASTICVISCOSITY EXAMPLE OF PLASTIC VISCOSITY AT DIFFERENT SHEAR RATE AT DIFFERENT SHEAR RATE MATERIAL VISCOSITY AT 280˚C 100s-1 1000s-1 10000s-1 100,000s-1 1 197 63 20 6 2 323 89 25 7 3 1220 259 55 12
  • 47.
    • IN MOSTCASES, PLASTIC WILL BEHAVE AS PSEUDOPLASTIC - LESS VISCOS (FLOW EASILY) WHEN THEY ARE MOVED FASTER • VISCOSITY REDUCED WHEN SHEAR RATE IS INCREASED (EASIER TO FILL THE MOULD) • INCREASE THE MELTING TEMPERATURE WILL REDUCE THE INJECTION PRESSURE NEEDED AT SPECIFIC FLOW RATE
  • 48.
    MOULDING TEMPERATURE OFDIFFERENT MOULDING TEMPERATURE OF DIFFERENT TYPES OF PLASTICS TYPES OF PLASTICS
  • 49.
  • 50.
    • DURING MOULDFILLING, HIGH INJECTION PRESSURE IS NEEDED TO MAINTAIN INJECTION SPEED DURING PROCESSING • WHEN THE MOULD IS FILLED, HIGH PRESSURE IS NO LONGER NEEDED • 2 STEPS PRESSURE CAN BE USED
  • 51.
    INJECTION SPEED INJECTION SPEED (SPEEDTO FILL THE MOULD) (SPEED TO FILL THE MOULD)
  • 52.
    • WHEN MOULDINGTHIN PRODUCT, HIGH SPEED IS NEEDED TO FILL THE MOULD • TO OBTAIN GOOD SURFACE FINISH FOR THICK PRODUCT, LOW INJECTION SPEED CAN BE USED • FOR ALMOST ALL MACHINE, TIME TO FILL THE MOULD IS ABOUT 1 SECOND
  • 53.
    Injection Unit Injection Unit •Purpose – Melt solid pellets to liquid form and then inject into mold • Steps – Hopper- manual or pneumatic loaded. Can have a mixer, volumetric or gravimetric units to meter material. – Screw • Reciprocating screw – most common – similar to general purpose extrusion screw – much shorter than extrusion screws, L/D of 12:1 to 20:1 – compression ratios (diameter of feed to diameter of metering) are often 2:1 to 5: 1 which is lower than for extrusion. – lower compression ratio means less mechanical action and heating – Step 1: turns of the screw melts resin and collects it at end of screw – Step 2: the screw moves forward via a hydraulic mechanism – Step 3: retraction of screw – Step 4: part cooling and removal
  • 54.
    Clamping Clamping Unit Unit • ClampingForce – Clamping unit holds the molds together while the resin is injected, packed, and cooled, and ejected. – Clamping force is the rating of the injection molder, e.g., 150 tons clamping force. • Clamping force = Injection Pressure x Total Cavity Projected Area – Projected area is the area projected into a single plane, that is, the widest area of the part. – Examples • The force necessary to mold a part that has 100 in2 projected area and has 3,000 psi is 3,000 * 100 = 300,000 lbs force = 150 tons (note 1 ton = 2000 lbs) • The maximum projected surface area of a part on a 200 ton machine with a maximum injection pressure of 2,000 psi is: 400,000 lbs force / 2,000 psi = 200 in2 A P F  
  • 55.
    INJECTION RATE INJECTION RATE •INJECTION RATE MAY BE VARIED • FAST – THIN PRODUCT AND REDUCED TIME • INJECTION RATE DEPEND ON MACHINE SIZE • INJECTION RATE CAPABILITY IS DIRECTLY PROPORTIONAL TO HYDRAULIC PUMP. • HYDRAULIC PRESSURE WILL DETERMINE THE INJECTION PRESSURE
  • 56.
    • Part Design –The underlying principles behind part design, other than part functionality are • cooling of plastic from melt to glassy state • heat transfer from various sections • thermal shrinkage of the plastic parts – Heat transfer is best when the parts have the same thickness • Inside portions of parts cool more slowly than the part surfaces • Center portion will shrink more than the surface
  • 59.
    MACHINE SIZE MACHINE SIZE •FROM A FEW GRAMS TO A FEW POUNDS (CAN GO UP TO 395 POUND, CLAMPING STRENGTH UP TO 10,000 TON) • ‘MINIATURE INJECTION MOULDING MACHINE’ (FIGURE). THERE MANY CHALLENGES IN THE FUTURE. THE REQUIREMENTS FOR MICRO- MOULD: – ADVANCED HEATING AND COOLING – VACUUM FOR CAVITI – SPECIFIC SENSOR – HIGH PRECISION TOOLINGS ARE NEEDED
  • 60.
    MINIATURE INJECTION MOULDINGMACHINE MINIATURE INJECTION MOULDING MACHINE
  • 62.
    • VERY BIGINJECTION MOULDING MACHINE (SEE NEXT SLIDE) – AUTOMOTIVE, BUILDING, AEROSPACE, SPORTS, CONSTRUCTION ETC. – CAR PANEL/BODY – WASHING MACHINE, FREEZER – BOAT – SWIMMING POOL – EXAMPLE: • HUSKEY E8000 • CLAMP FORCE - 8000 TON • PLATEN SIZE: 19 X 16 X 13’ • INJECTION WEIGHT: 20 – 145 POUND
  • 63.
    VERY BIG INJECTIONMOULDING MACHINE VERY BIG INJECTION MOULDING MACHINE