„New generation of aluminium hydroxide flame retardant filler for the

„New generation of
aluminium hydroxide
flame retardant filler
for the wire and cable industry“
Dr. Reiner Sauerwein
Nabaltec GmbH
Cables 2003
Business Unit Fillers
Overview
• Introduction
• New ATH quality – product characteristics
• Powder handling properties during compounding
- conveyance
- feeding / metering
- dust behaviour
- filler uptake
• Compound properties
• Options for high performance ATH
- low process costs of standard LSFOH
- new compound developments
• Conclusions
Cables 2003
Business Unit Fillers
Introduction – Market Share of LSFOH
PE-consumption in 2001
Total 325.000 tons
for Western Europe
LSFOH 12%
XPE 41%
Germany
MD/HDPE 18%
15%
LLDPE 9% LDPE
Schwandorf
â
More than
70.000 tons of
ATH in PE-based
LSFOH compounds
Cellular PE 5%
A. Reynolds, „Raw materials
usage in the European cable
industry“ ; Cables 2002
Cables 2003
Business Unit Fillers
Introduction - cost factors of LSFOH
cable production
Raw material costs
• polymers
• ATH
• additives (stabilizers, coupling agents,...)
Process costs
ââ
Compounding costs
• energy consumption
• compound throughput
Reduction of process costs
„powder handling“
ATH showing
• good conveyance
• good metering / dosing
• fast uptake
in polymer melt
€ / unit
è
Extrusion costs
9 Compounds
• energy consumption
• extrusion speed / output
units / time
• high melt flow
• good rheology
• good extrusion
„compound performance“
Cables 2003
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Powder handling during Compounding - problems
• low bulk density
• dust emission
• flowability / conveyance
Þ Common Solutions
A) Physical Densification
- higher filler mass throughput during volumetric feeding
- better flow properties,
- non consistent bulk density during air suction/pressure conveyance
P
P
O
B) Organic Coating
- good flow
- low viscosities in compounds,
- sometimes poor mechanical properties
- poor electrical insulation properties (high water uptake)
Cables 2003
Business Unit Fillers
P
P
O
O
New Solution – Apyral® 40CD - characteristics
Apyral 40D
Apyral 40CD
1.2 - 1.5
1.0 – 1.3
3 – 4.5
3.5 - 5
Bulk density (g/l)
400
400
Moisture (%)
0.2
0.2
26 - 30
0.6 – 0.7
19 - 23
0.4 – 0.5
d50 (µm)
BET (m2/g)
Oil absorption (%)
Water uptake (ml/g)
No coating!
No densification!
1
Apyral 40D
wateruptake (ml/g)
Apyral® 40CD
shows extremely
low oil absorption
for a fine
precipitated ATH
quality !!!
0,8
Water Uptake measured
according to „Baumann“
(in line with DIN 53495)
0,6
0,4
Apyral 40CD
Significantly lower
water uptake of
Apyral 40® CD !!!
0,2
0
0
10
20
30
40
50
60
t (min)
Cables 2003
Business Unit Fillers
Compounding – critical process parameters
delivery/
storage/
input
of raw
materials
Silo
flow
BB-station
bulk
density
flow
dustemission
flow
Silo-truck
consistency of bulk
density
day-bin
preparation
of raw material
flow
bulk
density
dry mixing
Pipe conveyance
-air suction
-air pressure
dosing
compounding
compound
Cables 2003
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Conveyance trial
BB station
1
Air suction conveyance:
- Length 60m,
- pipe diameter
60mm
- vertical and
horizontal
elements
- 90° corners: 11
2
450
Receiving
set
bulk density
400
Vibration
bottom
350
300
Apyral® 40CD
Apyral® 40D
3
250
CD = consistent density
200
1
2
Cables 2003
BB
3
Business Unit Fillers
Flow behaviour – feeding during continuous
compounding
Gravimetric dosing of ATH
via two dosing units within
a buss-kneader-line (fixed
mass flow)
15-20% lower screw speed
needed for Apyral® 40CD!!!
Apyral 40D
screw speed (rpm)
500
Apyral 40CD
400
300
200
100
0
D1
D2
unit
Cablesdosing
2003
Business Unit Fillers
Dust behaviour – measurement according to
DIN 33897 – part 2
Benefits of this method
•
•
•
•
Simulation of discharge-, filling- and
conveyance- processes
Selective sampling and determination of
breathable (SE ; Def. acc. to DIN EN 481)
and alveoli passing dust (SA)
High sensitivity and reproduce ability
Further analyses of dust particles
possible
Lit:“Das Staubungsverhalten quarzfeinstaubhaltiger
Produkte“; Gefahrstoffe-Reinhaltung der Luft 60
(2000) Nr. 5, Mai.
Apparatus ; with the kind permission of
IGF Institut für Gefahrstoff-Forschung
der Bergbau-Berufsgenossenschaft
Cables 2003
Business Unit Fillers
Dust behaviour – results
Filler
SA
(mg/kg)
SE
(mg/kg)
Apyral® 40CD
< 0.3*
100
Apyral® 40D
< 0.3*
118
TiO2 (d50 = 1µm)
1.04
88
BaSO4 (d50 = 8µm)
8.7
205
39.8
704
Carbon black (d50 =
1.7µm)
*non traceable
Apyral® 40CD shows a 15 - 20% reduction of
breathable dust compared to standard ATH
qualities as e.g. Apyral® 40D !!!
Compared to other fillers, both ATH qualities are very low in SA dust and low to medium with regard to SE – dust!
Cables 2003
Business Unit Fillers
Compounding behaviour - Power Consumption
of Buss-kneader MDK 46
Apyral 40D
Apyral 40CD
Ø = 2,9kW
Ø = 2,7kW
Electrical power
uptake of
screw motor
Compounding
behaviour of
Apyral® 40D
is good
Cables 2003
Compounding behaviour
of Apyral® 40CD
better than
Apyral® 40D
Business Unit Fillers
Compound properties – EVA
EVA (19%VA) ; Aminosilane coupled
60 wt.-% ATH
Tensile strength
Elongation at bre ak (%)
12
Te nsile stre ngth (M Pa)
Elongation at break
250
14
10
8
6
4
200
150
100
50
2
0
0
Apyral 40D
4,5
190°C
3,5
3
Compounding in batch
dispersion kneader ;
specimens cut out of
compression moulded plates
Melt flow index
4
M VI (cm /10min)
Apyral 40D
Apyral 40CD
Apyral 40D
Apyral 40CD
Apyral 40CD
No impact on
„mechanics“!
3
2,5
160°C
30% increase
in MFI for
Apyral® 40CD!!!
2
1,5
1
0,5
0
1
Cables 2003
2
Business Unit Fillers
Compound properties – PE / EVA
PE/EVA ; Vinylsilane coupled
60 wt.-% ATH
12
Tensile strength
10
250
Elongation at break (%)
Tensile strength (MPa)
Elongation at break
300
8
6
4
200
150
100
50
2
0
0
Apyral 40D
Apyral 40D
Apyral 40CD
Melt flow index
Apyral 40D
Apyral 40CD
10
No impact on
„mechanics“!
160°C
More than
50% increase
in MFI for
Apyral® 40CD!!!
MVR (cm3/10min)
8
Continuous compounding in
Buss-co-kneader MDK46 ;
specimens cut out of extruded
tapes.
Apyral 40CD
6
4
2
0
Apyral 40D
Cables 2003
Apyral 40CD
Business Unit Fillers
Flame Retardant Properties
Limiting Oxygen Index = LOI
ASTM D 2863-77
LOI of Apyral® 40CD
containing compounds
slightly enhanced
EVA (19%VA)
40
Aminosilane
Apyral 40D
Apyral 40CD
40
39
Vinylsilane
39
38
38
37
LOI (%O2)
LOI (%O2)
PE/EVA
36
35
34
37
36
35
34
33
33
32
Apyral 40D
32
Apyral 40CD
Apyral 40D
Cables 2003
Apyral 40CD
Business Unit Fillers
Good melt flow properties – options
5,5
EVA (19%VA) ; 60 wt.-% ATH
5
4,5
Apyral 40CD
4
3
MVR (cm /10min)
Melt Flow
as a function
of silane
content
3,5
Apyral 40D
3
2,5
2
0
0,1
0,2
0,3
0,4
0,5
0,6
0,7
0,8
Aminosilane (%)
Low process costs for
standard LSFOH compounds
Highly filled and flame
retarded LSFOH compounds
a Higher extrusion speeds
a „Freedom“ to increase filler level
a High productivity
a „Freedom“ to add synergistic
(mineral) additives
a High competitiveness against
alternative FR - compound
Cables 2003
Business Unit Fillers
Melt Rheology – PE / EVA
PE/EVA ; 60 wt.-% ATH ; Vinylsilane coupled
Capillary Rheometer ; 150°C
Shear Viscosity η s (Pas)
10000
1000
Apyral 40D
Apyral 40CD
100
10
100
1000
Apyral® 40CD
shows lower
compound
viscosity than
Apyral® 40D
over the
whole shear
velocity range
10000
Shear Velocity dγ/dt (s-1)
Cables 2003
Business Unit Fillers
Extrusion properties – PE / EVA
Set-up
ØExtruder with BM-screw at 30 rpm;
Ø0,5mm2 copper, round;
ØDiameter tip 0,85mm
ØDiameter die 1,4mm
Line speed: 650 m/min
Tm = 168°C
p (bar)
850
X
X
170
160
Tm = 151°C
800
pm = 800bar
X
p = 740bar
m
750
Apyral 40D
150
140
Apyral 40CD
700
Melt pressure and
melt temperature of
Apyral® 40CD is lower
than for Apyral® 40D
T (°C)
900
_ „freedom“ to
enhance line
speed by extruder
screw speed !!!
130
Cables 2003
Business Unit Fillers
Good melt flow properties – options
5,5
EVA (19%VA) ; 60 wt.-% ATH
5
4,5
Apyral 40CD
4
3
MVR (cm /10min)
Melt Flow
as a function
of silane
content
3,5
Apyral 40D
3
2,5
2
0
0,1
0,2
0,3
0,4
0,5
0,6
0,7
0,8
Aminosilane (%)
Low process costs for
standard LSFOH compounds
Highly filled and flame
retarded LSFOH compounds
a Higher extrusion speeds
a „Freedom“ to increase filler level
a High productivity
a „Freedom“ to add synergistic
(mineral) additives
a High competitiveness against
alternative FR - compounds
Cables 2003
Business Unit Fillers
EVA – 65wt.-% filler: mechanical properties
ATH
Elongation at break (%)
160
ATH+AOH
ATH+AOH
+ZnB
Apyral 40D
155
150
„Bi-blends“ of
Apyral® 40CD and
Apyral® AOH180 (=AOH)
and
... „tri-blends“ with
Zinc borate (=ZnB)
145
140
135
130
125
120
14,5
14
Tensile strength (MPa)
Apyral 40CD
show good balanced
physical properties at
65wt.-% filler content !!!
13,5
13
12,5
12
Compounding in batch
dispersion kneader ;
specimens cut out of
compression moulded plates
11,5
11
10,5
Cables 2003
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EVA – 65wt.-% filler: LOI ; MVR
ATH
ATH+AOH
50
ATH+AOH
+ZnB
LOI = 43,2 %O2
PHRR = 170 kW/m2
TTI = 78 sec
48
LOI (%O2)
46
44
LOI = 48,2 %O2
PHRR = 173 kW/m2
TTI = 80 sec
42
40
38
MVR
cm3 /
10min
2.0
2.4
1.4
1.7
1.9
2.1
Apyral® 40CD allows highly filled compounds
• having good melt flow properties
• showing good flame retardancy,
9
especially when combined with fine
boehmite filler (Apyral® AOH 180)
Cables 2003
Heat flux = 50 kW/m2
Horizontal orientation
Specimens cut out of
compression moulded plates
Business Unit Fillers
Conclusions
Apyral®40CD is a new non post treated fine precipitated ATH quality,
offering
• good conveyance properties without any loss on bulk density
• good flow, discharge and feeding properties
• low dust emissions during powder handling (discharge etc.)
• good filler uptake and dispersion (low power uptake, low torque)
9-
lower compound process costs (high throughput in
continuous lines, low batch times in case of internal mixers)
• good mechanical and flame retardancy properties and
• outstanding low melt viscosity of standard LSFOH compounds
• high extrusion speeds of standard LSFOH compounds
9lower extrusion costs
• an option for processable, highly filled and flame retardant LSFOH
compounds - especially when combined with other fillers
Cables 2003
Business Unit Fillers