Injection
Molding Basic & Systematic Mold Proving ④
5. Preparation for Molding Work and
Mechanical Operation
Different from the factors that
influence the process, various other factors should be considered in order to
secure the zero defect production process. The items to be considered are
briefly described below.
1) Mold
If this was not performed as part of the
pre-inspection routine, the following should be checked before production.
Visual Inspection of Molds
• Has the repair work
required for the mold been completed?
• Are there items that are
suitable for the machine such as locate ring, sprue bush(nozzle diameter), and
ejector coupling of the mold?
• Has an insulation plate
been installed?
• Have you checked if any
damage exists on the visible side or the parting side?
• Is a clean banding
supplied?
• Has the date stamp been
set properly?
• Has grease been injected
into moving components?
Functional Inspection of Mold
• Have the mold protection
pressure and distance been optimally set?
• Is the ejector easy to
operate?
• Is the slide in the
correct position?
• Was the functionality of
the limit switch checked?
• Was the tightness of the
thermostat or hydraulic pipe in the mold verified?
• Was the transformation
process verified?
• Do you have a temperature
profile with regard to a hot runner or holding temperature while being heated?
• Are all coolants connected
properly?
• Is the output of a
thermostat sufficient?
• Was the initial product
thoroughly inspected?(comparison with the final product)
Mold Management after Production
Completion
• Conduct a rust-proofing
and grease it after cleaning the mold.
• Inspect if there was any
damage to the mold.
• Request mold repair if
necessary.
• Drain a medium so that the
thermostat can be sealed and seal the channel.
• Attach the final product
to the mold.
2) Materials
Injection molding machine, material
preparation and insufficient cleanliness around the facility can be a cause of
contamination in raw materials and molded products.
• Clean dryer, filter and
hopper when exchanging materials.
• Place a cover on the
hopper.
• Put a magnet into the hopper.
• Protect against
contamination by sealing the bags of the opened materials.
• Do not expose the
materials that absorb a lot of moisture after the drying process to humid
places for a long time.
• Dry the materials based on
accurate factors including drying time.
• In case of a low injection
volume, adjust the amount of resin in the hopper to prevent water absorption.
3) Machines
Periodic maintenance of injection
molding machines, molds and peripheral devices reduce unnecessary interruptions
that can occur during the production process.
• All monitoring devices
related to safety and function are regularly inspected. (For instance, safe
door, cover, limit switch, and location sensors, etc.)
• Check the temperature,
level, and condition of the operating oil (cleanness, kinetic viscosity,
metallic content, etc.).
• Check the lubrication
status of the central lubricating oil supply device or the machine.
• Check the temperature of
the resin supply section in the cylinder (barrel).
• Check the function and the
correct installation location of the temperature sensor.
• Check the proper
installation and fixation of the band heater.
• Check the function of the
non-return valve (screw tip).
• Check the wear and tear of
the plasticization cylinder (barrel).
• Check the leaking status
of the machine.
• Check if the maximum
clamping force is sufficient.
4) Peripherals
• Was the correct operating
temperature set into the thermostat?
• Is the throughput
sufficient?
• Is the capacity of the thermostat
used sufficient?
• Have you checked the
material shipment?
5) Process Transformation
The items below can be the causes of
the changes in cycle time or quality.
• Is there any change in the
amount of cushion remained?
– Check for wear and tear on
the non-return valve (screw tip) and heating cylinder
– Accurate suck back setting
– Measurement condition
check
– Increase in the initial
injection rate (To increase the closing behavior characteristics of the
non-return valve(screw tip))
• Set the correct back
pressure.
• Isn"t the amount of
cushion too small or too big within the optimal range?
• Is there any change in the
measurement time?
• Is the measurement time
within the cooling time?
• Very short measurement
time can result in heterogeneity of thermo-mechanical materials.(Checking the
measurement capacity of a machine)
• Is the injection volume
suitable for screw diameter?
• Is there any significant
change in injection pressure?
• Is there any excess or
fall short of the switchover point?
• Does the screw slide back
as soon as it reaches the switchover point?
• Inspect the temperature of
the resin supply section.
• Is the supply of materials
from the resin supply section smooth??
• Does the pressure reach
the injection pressure limit?
• Is the measurement value
of melting temperature within the recommended process temperature range?
• It should be injected
according to the injection profile configured by a melting.
• Measure the temperature
with a needle thermometer (remove the materials ejected from the frame of the
machine).
• Is there any change in
mold temperature during production?
Screw Speed Curve
Maximum Circumference Speed (m/s)
PS
|
1
|
ABS
|
0.3
|
PMMA
|
0.3
|
PC
|
0.3
|
PA
|
0.6
|
PE
|
1
|
PP
|
1
|
POM
|
0.6
|
SB
|
0.6
|
SAN
|
0.3
|
PETP
|
0.2
|
PBTP
|
0.2
|
6. Data of Plastic Resin
Uncrystalline Thermoplastic Resin
Material
|
Melting Temperature
℃
|
Mold Temperature
℃
|
Resin Supply Section
temperature ℃
|
Absolute Back Pressure
bar
|
Measuring Speed
m/s
|
Drying Temperature
℃
|
Drying Time
hr
|
ABS
|
220 – 260
|
40 – 80
|
30 – 50
|
70 – 150
|
0.3
|
80
|
2 – 3
|
CA
|
180 – 220
|
50 – 80
|
40
|
80 – 100
|
0.3
|
60 – 65
|
2 – 3
|
CAB
|
180 – 220
|
50 – 80
|
40
|
80 – 100
|
0.6
|
60
|
2 – 3
|
CP
|
180 – 220
|
50 – 80
|
40
|
80 – 100
|
0.6
|
60
|
2 – 3
|
PA amorph
|
260 – 300
|
70 – 100
|
60 – 80
|
50 – 100
|
0.6
|
100 – 120
|
6 – 12
|
PC
|
280 – 320
|
80 – 120
|
70 – 90
|
50 – 150
|
0.3
|
120
|
2 – 3
|
PC/ABS
|
250 – 290
|
60 – 90
|
60 – 80
|
50 – 150
|
0.2
|
90 – 110
|
2 – 4
|
PEI
|
340 – 425
|
140 – 180
|
100 – 120
|
|
0.5
|
150
|
4 – 6
|
PES
|
330 – 370
|
100 – 150
|
|
30 – 80
|
0.6
|
190
|
3
|
PMMA
|
220 – 260
|
50 – 80
|
50 – 60
|
30 – 90
|
0.3
|
80
|
3
|
PPO
|
270 – 310
|
70 – 120
|
40
|
60 – 80
|
1.3
|
110
|
2
|
PS
|
190 – 280
|
20 – 80
|
20 – 30
|
150 – 300
|
1
|
80
|
1 – 2
|
PSU
|
310 – 390
|
95 – 115
|
|
|
0.6
|
120 – 135
|
2 – 3
|
PVC hard
|
170 – 210
|
20 – 60
|
30 – 50
|
70 – 200
|
0.2
|
70
|
1
|
PVC soft
|
140 – 200
|
20 – 60
|
40
|
70 – 200
|
0.3
|
70
|
1
|
SAN
|
220 – 260
|
20 – 80
|
40
|
30 – 90
|
0.3
|
80
|
2 – 3
|
SB
|
180 – 280
|
20 – 80
|
20 – 30
|
50 – 100
|
0.6
|
80
|
1 – 2
|
Semi-crystalline Thermoplastic Resin
Material
|
Melting Temperature
℃
|
Mold Temperature
℃
|
Resin Supply Section
temperature ℃
|
Absolute Back Pressure
bar
|
Measuring Speed
m/s
|
Drying Temperature
℃
|
Drying Time
hr
|
PE-HD
|
180 – 300
|
10 – 60
|
20 – 30
|
150 – 450
|
1
|
*
|
|
PE-LD
|
180 – 260
|
10 – 60
|
20 – 30
|
150 – 450
|
1
|
*
|
|
PA 6
|
240 – 270
|
40 – 90
|
60 – 80
|
70 – 120
|
0.6
|
80
|
3 – 5
|
PA 6.6
|
270 – 320
|
40 – 90
|
60 – 80
|
50 – 150
|
0.6
|
80
|
3 – 5
|
PA 6.10
|
230 – 280
|
30 – 60
|
60 – 80
|
50 – 150
|
0.6
|
80
|
3 – 5
|
PA 11
|
200 – 250
|
20 – 100
|
60 – 80
|
50 – 150
|
0.6
|
85
|
4 – 6
|
PA 12
|
200 – 250
|
20 – 100
|
60 – 80
|
50 – 200
|
0.6
|
85
|
4 – 6
|
PEEK
|
350 – 380
|
150 – 180
|
|
2 – 50
|
0.2
|
150
|
2 – 3
|
LCP
|
295 – 385
|
80 – 120
|
60 – 80
|
0 – 30
|
0.2
|
150
|
4 – 6
|
LCP+GF
|
320 – 350
|
80 – 120
|
60 – 80
|
0 – 30
|
0.2
|
170
|
4 – 6
|
PBT
|
250 – 280
|
60 – 120
|
80
|
70 – 120
|
0.2
|
120
|
2 – 3
|
PC/PBT
|
255 – 270
|
40 – 80
|
40 – 80
|
50 – 120
|
0.4
|
100 – 120
|
2 – 4
|
POM
|
180 – 225
|
40 – 120
|
30 – 40
|
30 – 90
|
0.6
|
100
|
2 – 3
|
PP
|
200 – 260
|
10 – 60
|
20 – 30
|
150 – 450
|
0.9
|
*
|
|
PPS
|
310 – 320
|
140 – 160
|
100 – 120
|
15 – 30
|
0.4
|
110 – 120
|
2 – 4
|
PPS+GF
|
330 – 350
|
140 – 160
|
100 – 120
|
15 – 30
|
0.4
|
130 – 150
|
2 – 4
|
* Source: www.lsinjection.com