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www.distrupol.com
The “Right” machine for
the job?
2 www.distrupol.com
Introduction
The Tool
The Material
3 www.distrupol.com
But which Machines?????????
4 www.distrupol.com
LegalRequirement
MSDS
5 www.distrupol.com
Moulding
6 www.distrupol.com
What is Polycarbonate?
CC
CHCH
CHCH
33
33
CC
OO
nn
OO OO
7 www.distrupol.com
Molecular Weight Vs. Strength
Molecular weight Molecular weight (x10 )(x10 )
Te n
s ile
str
e ngt
h
Te n
s ile
str
e ngt
h
(kg /
c m2 )
(kg /
c m2 )
Izod
imp
act
stre
ngt
h
Izod
imp
act
stre
ngt
h (k
g cm
/cm
)(k
g cm
/cm
)800800
700700
600600
100100
5050
0022 2.52.5 3.03.0
4
8 www.distrupol.com
Molecular Weight Vs. Flow
Molecular weightMolecular weight
Flo
w V
alu
e F
low
Val
ue
(10
m/s
ec)
(10
m/s
ec)
1.51.5
22
33
44
55
66
1010
20,00020,000 25,00025,000 30,00030,000
9 www.distrupol.com
Hopper
Screw & Barrel
Nozzle
Clamping unit
Injection Moulding
10 www.distrupol.com
Calculated by multiplying the projected area of the cavity (cavities), including runner system by the maximum internal pressure (hold pressure).
Clamping Pressure
11 www.distrupol.com
• ABS 0.45 to 0.65 T/cm2
• LCP 0.75 to 0.8 T/cm2
• PA 0.65 to 0.75 T/cm2
• PBTP 0.65 to 0.75 T/cm2
• PC 0.5 to 0.8 T/cm2
• PE 0.15 to 0.55 T/cm2
• PETP 0.65 to 0.75 T/cm2
• PMMA 0.45 to 0.75 T/cm2
• POM 0.85 to 1 T/cm2
• PP 0.15 to 0.55 T/cm2
• PPS 0.3 to 0.6 T/cm2
• PS 0.3 to 0.5 T/cm2
Clamping Pressure
12 www.distrupol.com
Injection Unit
Hopper
Screw & Barrel
Nozzle
13 www.distrupol.com
Screw Design
14 www.distrupol.com
Screw Types
15 www.distrupol.com
Screw Tangential Speed-M/S
• ABS 0.2 (GR,FR) - 0.3• ETPV 0.2• PA 0.15 (GR,FR) – 0.4• PBTP 0.2 (GR,FR) – 0.3• PC 0.2 (GR,FR) - 0.3• PE 0.5 – 0.6• PETP 0.15 (FR) – 0.20• PMMA 0.2 (ST) – 0.3
16 www.distrupol.com
• POM 0.15 (GR,ST) – 0.3• PP 0.3 (GR) – 0.6• PPA 0.15• PPS 0.15• PS 0.3 (HI) - 0.6• PVC <0.1• SAN 0.3• TPC-ET <0.2• TPUR <0.15
Screw Tangential Speed-M/S
17 www.distrupol.com
Beware: High speed = high heat (through shear).High speed = high abrasionwith filled Materials.
Beware: High back pressure increases shear (temperature) and cycle time but not necessary melt quality.
Screw Speed Calculation
18 www.distrupol.com
Melt Viscosity characteristics
280c280c
300c300c
320c320c
Shear Rate (Sec )Shear Rate (Sec )
Mel
t vi
scos
ity
(poi
se)
Mel
t vi
scos
ity
(poi
se)
1010 1010
1010
1010
33
33
44
44
-1-1
19 www.distrupol.com
Pressure Vs. Flow
PPHPPHPA 6PA 6
GPPSGPPS
PPCPPC
HDPEHDPELDPELDPE
POMPOMABSABS
PolycarbonatePolycarbonate
Injection PressureInjection Pressure
Sp
iral
flo
w le
ngt
h (
cm)
Sp
iral
flo
w le
ngt
h (
cm)
4040 140140 (Kg/cm G)22
4040
8080
120120
20 www.distrupol.com
100
1000
10000
350 340 320 300 280
Moulding temp (deg.C)
Lo
wer
ing
of
mo
l. w
t. (
Mv)
35 min35 min
20 min20 min
5 min5 min Res
iden
ce t
ime
Res
iden
ce t
ime
Temp. Vs. Molecular Weight
21 www.distrupol.com
Toughened Nylon 6.6
Hold-on-time
22 www.distrupol.com
Temperature Profiles
23 www.distrupol.com
The right Melt temperature The right Melt quality
Conclusion
www.distrupol.com
A Polymer for Every Application