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Thermal and mechanical properties of extruded LLDPE/wax blends

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The thermal and mechanical properties of linear low-density polyethylene (LLDPE)/wax blends, prepared in an extruder, were investigated, using differential scanning calorimetry (DSC) and tensile testing. DSC measurements indicated that blends consisting of 10 and 20% of wax are probably miscible in the crystalline phase. For 30% and more wax, phase separation of the two components were observed. The DSC curves of both pure LLDPE and blends show, beside the main exothermic peak, another small peak at about 70°C. Since this peak was observed for both pure LLDPE and the blends, it is probable that its origin is partly in the LLDPE structure, but it is also influenced by wax crystallization. An increase in Young’s modulus with an increase in wax content was observed. An increase in wax content causes a decrease in elongation at yield. A small increase in yield stress was observed for blends consisting of 10 and 20% of wax. For blends consisting of 30% and more wax, no yield point, but brittle rupture, was observed.
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Thermal and mechanical properties of extruded LLDPE/wax blends
I. Krupa
a
, A.S. Luyt
b,
*
a
Polymer Institute, Slovak Academy of Science, 842 36 Bratislava, Slovak Republic
b
School of Chemical Sciences, University of the North (Qwa-Qwa), Private Bag X13, Phuthaditjhaba 9866, South Africa
Received 24 January 2001; accepted 27 February 2001
Abstract
The thermal and mechanical properties of linear low-density polyethylene (LLDPE)/wax blends, prepared in an extruder, were
investigated, using differential scanning calorimetry (DSC) and tensile testing. DSC measurements indicated that blends consisting
of 10 and 20% of wax are probably miscible in the crystalline phase. For 30% and more wax, phase separation of the two com-
ponents were observed. The DSC curves of both pure LLDPE and blends show, beside the main exothermic peak, another small peak
at about 70C. Since this peak was observed for both pure LLDPE and the blends, it is probable that its origin is partly in the
LLDPE structure, but it is also influenced by wax crystallization. An increase in Young’s modulus with an increase in wax content
was observed. An increase in wax content causes a decrease in elongation at yield. A small increase in yield stress was observed for
blends consisting of 10 and 20% of wax. For blends consisting of 30% and more wax, no yield point, but brittle rupture, was observed.
#2001 Elsevier Science Ltd. All rights reserved.
Keywords: LLDPE/wax blends; Thermal analysis; Tensile properties
1. Introduction
Blending of different polymers is regarded as an eco-
nomical alternative to the development of new polymers.
Materials with improved properties can be obtained by
blending two or more polymers having different chemi-
cal composition and physical properties [1]. In this
paper we investigate some thermal and mechanical
properties of LLDPE/wax blends.
Linear low-density polyethylene (LLDPE) has good
mechanical properties and is often used in industry. Gro-
cery bags, heavy duty shipping sacks, agricultural films,
pipes, liners for consumers, landfills and waste ponds are
only a few examples [2–4].
Paraffins are a class of aliphatic hydrocarbons, char-
acterized by straight or branched carbon chains, generic
formula C
n
H
2n+2
. Paraffin waxes (Fischer–Tropsch
synthesis) are white, translucent, tasteless and odourless
solids consisting of a mixture of solid hydrocarbons of
high molecular weight. Common properties are water
repellency, smooth texture, low toxicity, freedom from
objectionable odour and colour. They are combustible
and have good dielectric properties. They are used for the
preparation of candles, paper coating, protective sealant
for food products and beverages, glass-cleaning pre-
paration, hot-melt carpet backing, biodegradable mulch,
lubricants, stoppers for acid bottles, electrical insulation
and others [5].
In our previous studies we devoted attention to pre-
paration and characterization of cross-linked and uncross-
linked LLDPE, low-density polyethylene (LDPE)/wax
blends [6–8]. In that case, blends were only mechanically
mixed. In this case, blends were blended in an industrial
extruder. Very different behaviour was observed for all
physical properties. It is therefore clear that the morphol-
ogy of the blends strongly influences the final properties
[1]. This strongly depends on processing conditions.
2. Experimental
In this work, linear low-density polyethylene (MFI=3.5
g/10 min, density=0.938 g cm
3
, particle size 90% less
than 600 m) and hard, brittle, straight hydrocarbon-chain
paraffin wax (carbon distribution C28–C120, average
molar mass 7.8510
1
kg mol
1
, density=9.410
2
kg
0141-3910/01/$ - see front matter #2001 Elsevier Science Ltd. All rights reserved.
PII: S0141-3910(01)00082-9
Polymer Degradation and Stability 73 (2001) 157–161
www.elsevier.nl/locate/polydegstab
* Corresponding author. Tel./fax: +27-58-713-0152.
E-mail address: luyt@uniqwa.ac.za (A.S. Luyt).
m
3
, melting point 104C) from Schu
¨mann–Sasol were
used. All blends were blended in an industrial extruder
(Bandera film blower at 100 r.p.m.) at 180C and then
pressed for 3 min at 180C.
Differential scanning calorimetry was carried out on a
Perkin Elmer DSC7 thermal analyzer in nitrogen atmo-
sphere. Samples were heated from 25 to 160C at a heat-
ing rate of 10C min
1
and then cooled at the same rate.
Thermal properties, like melting and crystallization tem-
peratures and enthalpies, were determined from the
second scan.
For the determination of mechanical properties a sim-
ple tensile tester (Hounsfield W5K ROM rev M73) was
used. The speed of deformation was 50 mm/min. The
final mechanical properties were evaluated from at least
six different measurements.
Scanning electron microscopy photos were taken of the
break interface of samples cooled in liquid nitrogen and
broken. A Philips XL30 DX4I scanning electron micro-
scope was used at 10 kV voltage.
3. Results and discussion
3.1. Differential scanning calorimetry
The results obtained from differential scanning calori-
metry (DSC) are summarized in Table 1. Fig. 1 shows
DSC heating curves for the blends. We see a difference
in the behaviour for different concentrations of wax.
For 10% wax only one endothermic peak is observed.
For 20% wax a very small indication of other peaks is
observable (it is seen more clearly on the original curves),
but they are not significant. In these cases (at least for
10% wax), we can say that LLDPE and wax are mis-
cible in the crystalline phase [9]. For 30% and more wax,
three significant peaks are observable one of them
corresponds to that of LLDPE and the other two (at
about 80 and 109C) correspond to that of wax. In this
concentration region, LLDPE and wax are, therefore,
not miscible with each other in the crystalline phase. T
o
and T
m
also decreases with an increase in wax portion
(Table 1, Fig. 1).
In our previous work, where blends were only mechani-
cally mixed [6], we observed different behaviour. The DSC
heating curves showed only one endothermic peak for all
the wax concentrations. This peak corresponded to the
LLDPE melting peak and the T
o
and T
m
temperatures of
the blends were not influenced by the amount of wax in
the blends.
The DSC cooling curves of the samples are shown in
Fig. 2. The crystallization of the blends is different. The
DSC curves of all the samples, both pure LLDPE and
blends, show beside the main exothermic peak, another
small peak at about 70C (peak at about 70Cis
obvious and reproducible in the original curves). Since
this peak was observed for both pure LLDPE and the
blends, it is probable that its origin is partly in the
LLDPE structure. Generally, LLDPEs themselves are
not simple materials; there is some evidence that they
may phase separate in the melt. The LLDPEs are linear
Table 1
The parameters obtained from DSC measurements for LLDPE/wax
a
Sample T
o,m
(C) T
p,m
=T
m
(C) H
m
(kJ kg
1
)T
o,c
=T
c
(C) T
p,c
(C) H
c
(kJ kg
1
)
LLDPE 121.7 130.0 155.90 114.2 110.6 174.49
90/10 120.8 127.0 161.67 (161.62) 112.8 109.8 184.28
80/20 121.0 125.4 168.68 (167.33) 115.4 107.8 187.72
70/30 119.9 124.9
b
172.13 (173.04) 111.0 108.1
c
194.92
60/40 118.8 123.0
b
173.34 (178.76) 110.2 107.7
c
205.56
50/50 116.9 123.0
b
184.23 (184.48) 109.1 106.3
c
204.19
Wax 60.1 77.2
d
213.06 95.2 91.8
e
211.21
a
T, is temperature; H, is specific enthalpy; m, melting; c, cooling; o, onset; p, peak. Notation x/y means weight portion of LLDPE and weight
portion of wax.
b
The DSC heating curves of LLDPE/wax blends show three endothermic peaks. This one is the main peak. The others are at about 80 and
109C. See Fig. 1.
c
The DSC cooling curve of pure wax shows two exothermic peaks. This one is the main peak. The other one is at 80C. See Fig. 2.
d
The DSC heating curve of pure wax shows three endothermic peaks. This one is the main peak. The others are at about 90 and 101C. See Fig. 1.
e
The DSC cooling curve of pure wax shows two exothermic peaks. This one is the main peak. The other one is at 70C. See Fig. 2.
Fig. 1. DSC heating curves of LLDPE, wax and different LLDPE wax
blends prepared in an extruder.
158 I. Krupa, A.S. Luyt / Polymer Degradation and Stability 73 (2001) 157–161
but have a significant number of branches introduced by
using co-monomers, such as butene-1 or octene-1. The
co-monomer content is about 8–10% [10]. Marabella et
al. [11] and Deblieck and Mathot [12] have shown that,
when highly branched materials are quenched from the
melt, regions of differing crystallinity are manifested.
Various authors have analysed LLDPE materials by tem-
perature-rising elution fractionation (TREF) [13–15] and
have shown that LLDPEs contain molecules of very
different molecular weights and branched content. This
probably explains the existence of the second peak for
LLDPE. Since this peak is more intense for 30% and
more wax, it means that it is influenced by wax crystal-
lization. In this case we also observe a slightly decreas-
ing crystallization temperature with increasing wax
content. We observed similar behaviour during the
investigation of only mechanically mixed blends.
The specific enthalpy of melting of LLDPE/wax blends
increases with an increase in wax portion. The experi-
mental results (Table 1) and the values calculated accord-
ing to the additive rule [Eq. (1)] are in excellent agreement.
Hadd
m¼Hm;PEwPE þHm;wwwð1Þ
H
m,PE
,H
m,w
,H
m
add
are the specific enthalpies of
melting of LLDPE, wax and blends, and w
PE
,w
w
are
weight portions of LLDPE and wax in the blends.
3.2. Mechanical properties
An increase in Young’s modulus with an increase in
wax content was observed, indicating that the modulus
of this wax is higher than the modulus of LLDPE. It is
probably associated with its higher degree of crystal-
linity. The degrees of crystallinity of LLDPE and wax
are respectively 53.2 and 72.7%. These values were cal-
culated according to Eq. (2):
Xc¼Hm=Hþ
mð2Þ
where X
c
is the degree of crystallinity, H
m
is the specific
enthalpy of melting and H
+
m
is the specific enthalpy of
melting for 100% crystalline polyethylene. We used the
value H
+
m
=293 kJ kg
1
[16].
An increase in wax portion causes a decrease in elonga-
tion at yield. This is to be expected, since the wax is harder
than the LLDPE. As far as yield stress is concerned, a
small increase was observed for blends consisting of 10
and 20% of wax. For blends consisting of 30% of wax and
more, no yield point, but brittle rupture was observed.
Stress at break depends on the wax concentration.
Three different types of behaviour were observed. This is
shown schematically in Fig. 3, where a logarithmic scale
was used, because the differences in elongation between
the different samples were too large. Materials, which
undergo strain hardening during stretching, have higher
strength at break than materials which do not undergo
strain hardening [17]. In this case only pure LLDPE
undergoes significant strain hardening (Fig. 3), and there-
fore the value of stress at break for pure LLDPE is the
highest even higher than the yield stress (Table 2).
Samples, which consisted of 10 and 20% wax, reached
yield point, then underwent strain softening, but when
they reached draw stress (the minimum stress reached
during stress softening), the orientation hardening is very
small. In these cases, stress at break is much smaller than
yield stress (Table 2). Samples, which consisted of 30%
and more wax, does not have a yield point. They exhibit
brittle rupture and do not undergo strain softening. In
these cases, an increase in stress at break was observed.
An increase in wax content results in a decrease in
elongation at break at all concentrations investigated.
This decrease is the sharpest when the wax content is
higher than 30% (Table 2). In this case the material loses
its drawability and is very brittle.
The above behaviour is closely associated with the mis-
cibility of components, as we have discussed above. The
DSC measurements indicated that blends containing 10
and 20% of wax are miscible in the crystalline phase and
Fig. 2. DSC cooling curves of LLDPE, wax and different LLDPE wax
blends prepared in an extruder.
Fig. 3. Stress–strain curves of LLDPE and two LLDPE/wax blends
prepared in an extruder.
I. Krupa, A.S. Luyt / Polymer Degradation and Stability 73 (2001) 157–161 159
only one melting peak is observed. If the concentration of
wax is 30% and more, the components are more or less
separated. It has an influence on some mechanical prop-
erties: the material loses drawability, a yield point does
not exist, and elongation at break strongly decreases. In
our previous work we observed much higher values for
elongation at break [7].
The change in the mechanism of rupture is demon-
strated in Fig. 4. From these SEM photos it is clear that
an increase in wax portion causes LLDPE/wax blends
to rupture along different lines.
4. Conclusions
DSC measurements indicated that blends consisting
of 10 and 20% of wax are probably miscible in the crys-
talline phase. Only one peak was observed in the DSC
Table 2
Mechanical properties of LLDPE/wax blends
a
Sample "
y
Se
y
(%)
y
Ss
y
(MPa) "
b
Se
b
(%)
b
Ss
b
(MPa) ES
E
(MPa)
LLDPE 24.53.2 16.2 0.9 1249132 22.21.4 123 9
90/10 21.51.3 21.1 0.3 730 192 15.12.1 145 11
80/20 16.03.5 19.0 0.9 142 37 11.20.9 199 12
70/30 X X 186 18.72.1 225 16
60/40 X X 103 17.43.3 283 14
50/50 X X 72 17.13.3 29516
a
"
y
,
y,
"
b
,
b
,Eare elongation at yield, yield stress, elongation at break, stress at break, Young’s modulus of elasticity; Se
y
,Ss
y
,Se
b
,Ss
b
,S
E
are
their standard deviations; X, brittle rupture, no yield point was observed. The notation x/y means weight portion of LLDPE/weight portion of wax
in the blend.
Fig. 4. SEM photographs of samples of ruptured (a) LLDPE, (b) 90/10 LLDPE/wax, and (c) 60/40 LLDPE/wax.
160 I. Krupa, A.S. Luyt / Polymer Degradation and Stability 73 (2001) 157–161
curve. For 30% and more wax two other peaks were
observed. It indicates phase separation of components.
It also has an influence on the mechanical properties. T
o
and T
m
decrease with an increase in wax content.
The DSC curves of both pure LLDPE and blends
show, beside the main exothermic peak, another small
peak at about 70C. Since this peak was observed for
both pure LLDPE and the blends, it is probable that its
origin is partly in the LLDPE structure. On the other
hand, for blends consisting of 30% and more wax, this
peak is more intense, which means that it is influenced
by wax crystallization. In this case we also observe that
an increase in wax content slightly decreases the tem-
perature of crystallization.
An increase in Young’s modulus with an increase in
wax content was observed, indicating that the modulus
of this wax is higher than the modulus of LLDPE. It is
probably associated with its higher degree of crystallinity.
An increase in wax content causes a decrease in elongation
at yield. This is to be expected, since the wax is harder than
the LLDPE. A small increase in yield stress was observed
for blends consisting of 10 and 20% of wax. For blends
consisting of 30% and more wax, no yield point, but brit-
tle rupture, was observed.
The influence of wax content on stress at break depends
on its concentration. Since pure LLDPE undergoes sig-
nificant strain hardening, its value of stress at break is
the highest even higher than yield stress. Samples
containing 10 and 20% wax underwent strain softening
after their yield points. Stress at break is therefore much
smaller than yield stress. Samples, which consist of 30%
and more wax, do not have yield points, and exhibit
brittle rupture increase in stress at break. An increase
in wax content results in a decrease in elongation at break
in the whole concentration region. This decrease is the
sharpest for 30% and more wax in the blends. In this
case, the material loses its drawability and is very brittle.
The SEM photos also confirm that an increase in wax
content causes LLDPE/wax blends to rupture along
different lines.
We also discussed these results in comparison with our
previous work. We showed that the route of sample
preparation mechanical mixing versus blending in the
melt has a marked (yet unexplained) influence on all
properties investigated.
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I. Krupa, A.S. Luyt / Polymer Degradation and Stability 73 (2001) 157–161 161
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This study deals with the effect of two types of conductive fillers (viz., boron nitride and single walled carbon nanotubes) on the properties of the linear low-density polyethylene (LLDPE) matrix and LLDPE/paraffin wax (PW) blend. Pure LLDPE and paraffin wax/LLDPE blend (30/70) were melt mixed with 2 wt% content of boron nitride (BN) and single walled carbon nanotube (SWCNT), as well as their synergy at 2 wt%. Because it is well known that both conductive fillers were able to improve the thermal conductivity of the paraffin wax/polymer blends, the aim of this study was to focus on the effect of both conductive fillers on the dispersion of paraffin wax into LLDPE matrix, mechanical properties, crystallization behavior, and thermal stability of the LLDPE/wax blend. Scanning electron microscopy (SEM) images of the LLDPE/paraffin wax blends depicted a phase separated system, which was further supported by two separate peaks from the differential scanning calorimetry (DSC). The morphology of the system showed that the addition of boron nitride (BN) into the LLDPE/paraffin wax blend had no affinity with the paraffin wax, while the addition of single walled carbon nanotubes (SWCNT) showed better dispersion into the LLDPE/paraffin wax/BN blend composites. The incorporation of the SWCNT and its synergy with BN enhanced the thermal stability of the LLDPE.
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The influence of residual wax content on the thermal, rheological, and mechanical behavior of two high‐density polyethylene (HDPE) samples from different lots of the same supplier was characterized. HDPE with a low wax content presented a higher melting temperature and a wider melting endotherm. A decrease in the degree of crystallinity and thermal stability of HDPE with a higher wax content was observed. Thermograms obtained by DSC indicated a small additional exothermic transition associated with the exclusion of residual wax. A higher wax content in HDPE produces a decrease in its viscosity due to a lubricating effect, which allows the sliding of HDPE chains of high molecular weight. In contrast, HDPE with lower wax content achieves greater elongational viscosity and melt strength. The mechanical testing results show that HDPE with higher wax content presented lower Young's modulus, tensile strength, elongation at break, and Izod impact strength than HDPE with lower wax content. The results obtained show that a relatively slight difference in wax content significantly affects HDPE properties. Low‐molecular‐weight waxes are produced with the polymerization of high‐density polyethylene. A high percentage of them are removed because they have a high commercial value; however, a residual content remains in the polymer. In few studies, the effect of the variation in the residual wax content on the polyethylene and its effects on its properties have been studied, which will have a significant effect during its processing as well as its final application.
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Three grades of polyethylene differing mainly in their molecular weight were irradiation and peroxide crosslinked. Their gel content, degree of swelling, melting temperature, degree of crystallinity, and tensile properties were determined. The irradiation and peroxide crosslinking of the same polymers makes it possible to properly compare the effects of the two crosslinking methods. Upon irradiation the competition between crosslinking and chain scission reactions determines the level of the critical dose required to form the first gel and the magnitude of maximum attainable gel content. Crosslinking causes trapping of entanglements which then contribute to the effective network density determined by solvent swelling. crystalline polyethylene enhances the degree of crystallinity and crystal perfection while subsequent crystallization from the melt is hindered by the presence of crosslinks. The homogeneity of the crosslinked network, or distribution of crosslinks, depends on the crosslinking method. Irradiation crosslinking is essentially a selective process taking place mainly in amorphous regions. The resulting structural changes by the two crosslinking methods significantly affect the polymers' tensile behavior.
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The mechanical properties of uncrosslinked and crosslinked linear low-density polyethylene (LLDPE)/wax blends were investigated, using differential scanning calorimetry (DSC), tensile testing, and melt flow indexing. A decrease in the degree of crystallinity, as determined from the DSC melting enthalpies, was observed with an increase in the dicumyl peroxide (DCP) concentration. The Young's modulus increased with increased wax portions, and there was a higher increase for crosslinked blends. The yield stress generally decreased with increased peroxide content. Crosslinking caused an increase in elongation at yield, but increased wax content caused a decrease in elongation at yield. The stress at break generally increased with increasing peroxide content, but it decreased with increased wax content. The elongation at break decreased with an increase in the DCP concentration. Melt flow rate measurements indicated a mutual miscibility in LLDPE/wax blends. © 2001 John Wiley & Sons, Inc. J Appl Polym Sci 81: 973–980, 2001
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Fracture mechanics tests on two low density polyethylenes and two linear low density polyethylenes are described. The very low yield stresses give rise to crack blunting but at temperatures <0°C crack growth occurs. The LDPE grades had rather low toughness but LLDPE gave much greater values and recourse to J methods was necessary. LLDPE materials would appear to have good prospects as tough, engineering plastics.
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Blends of linear low density polyethylene (ethylene-octene-1 copolymer) and ethylene-propylene-butene-1 terpolymer (ter-PP) mixed in a twin-screw extruder have been characterized by using differential scanning calorimetry (DSC), dynamic mechanical thermal analysis, scanning electron microscopy (SEM), rheometric mechanical spectrometry, a capillary rheometer, and a universal test machine. Melting and crystallization behaviors by DSC and the α, β, and γ dynamic mechanical relaxations proposed that the blend is immiscible in the amorphous and crystalline phases by observing the characteristic peaks arised solely from those of the constituents. The lack of interfacial interaction between the components was suggested by the SEM study. A strong negative deviation of melt viscosity from the additive rule and the Cole-Cole plot confirmed the immiscibility in melt state. Incorporation of ter-PP induced a reduction in melt viscosity, shear stress, and final load. Flexural modulus and yield stress were linearly increased with ter-PP content, while the tensile strength and elongation at break were more or less changed. Although this blend system is immiscible in the solid and melt states, addition of less than 20 wt % ter-PP in the blend is viable for engineering applications with the advantages of improved processibility and mechanical properties. © 1997 John Wiley & Sons, Inc. J Appl Polym Sci 63: 1265–1274, 1997
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In this presentation we shall discuss the static mechanical properties such as Young's modulus, yield point, ultimate properties and toughness of both uncross-linked and cross- linked LLDPE/wax blends and their dependence on the concentration of cross-linking agent (dicumyl peroxide) and wax portion. Flow rates of uncross-linked blends are also discussed. The conservation of good mechanical properties of polyethylene and an improvement in the flow rate of the melt was the aim of this work. The following materials were used: linear low density polyethylene (MFI = 3.5 g / 10 min., density = 0.938 g/cm3, particle size - 90% less than 600 :m), hard, brittle, straight- hydrocarbon chain paraffin wax from Schümann-Sasol and dicumyl peroxide from Sigma Aldrich Co. Ltd. All blends were at first mechanically mixed a for few minutes and then pressed for 10 minutes at 180 oC. Homogeneity of blends was checked in terms of reproducibility of results. Mechanical properties were tested by the Polymer Institute of the Cape Technikon. The flow rates of the molten blends were determined in a Melt Flow Junior apparatus (Torino, Italy) at 190 0C and under 1 kg mass. Efficiency of cross-linking was determined gravimetrically in terms of insoluble portion (gel) after 12 hours extraction of the samples in boiling xylene. References
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Thermal properties of cross-linked and uncross-linked LLDPE/wax blends were investigated. The blends were prepared through thorough mixing of the powdery ingredients, followed by 10 min pressing at 180°C. The extent of cross-linking was determined through gravimetric analysis of the gel content of the samples. The thermal properties were determined with a differential scanning calorimeter (DSC), while a thermogravimetric analyzer (TGA) was used to determine the thermal stability of the samples. The analyses of cross-link density of the samples indicated that the wax is grafted onto the LLDPE chains at higher wax concentrations. The DSC results indicated that LLDPE and wax are miscible in the crystalline phase, and that cross-linking reduces polyolefin crystallinity. The TGA results indicated a reduction in thermal stability of the blends with increasing wax portion.
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The fracture toughness of commercial linear low-density polyethylenes (LLDPE) has been found to be extraordinarily high relative to commercial low-density (LDPE) and high-density (HDPE) polyethylenes in previously reported investigations. The present investigation shows that this extraordinary fracture toughness cannot be explained by differences in molecular structure variables, such as molecular weight, long-chain and short-chain branching, fractional crystallinity, and comonomer content. Instead, the presence of a second soft phase, which was extractable with a weak solvent, in a hard semicrystalline matrix was discovered by morphological investigations of LLDPE resins. This second phase arises from the extreme compositional heterogeneity of the copolymers which comprise these LLDPE resins. No evidence for a similar morphological entity was found in LDPE and HDPE resins. This finding provides persuasive evidence that this very-low-crystallinity second phase performs a function similar to that of the rubberlike second phase in other high impact resins and, thus, leads to the observed extraordinary fracture toughness of LLDPE resins. Evidence for the nature and existence of this second phase is given from temperature-rising elution fractionation and scanning electron microscopy investigations.
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The thermal, tensile and flow properties, as well as the surface tension, of blends of linear low-density polyethylene (LLDPE) and oxidized hard paraffin wax were determined. DSC analysis showed only one endothermic peak, despite the fact that pure wax shows two significant peaks. An increase in wax content of the blends hardly changes the onset and peak temperatures, or the specific enthalpies of melting of the blends. The TGA analyses of the blends show that the thermal stability of blends decreases with an increase in wax content, particularly after the 50% stage, since the thermal stability of the wax is much lower than the thermal stability of LLDPE. A small increase in Young's modulus of the blends with an increase in wax content was observed. Wax content was found to have no influence on the yield point (elongation at yield and yield stress) of the blends. An increase in wax content decreases both stress and elongation at break. An increase in flow rate with an increase in wax content of the blends was observed. We also observed that our wax slightly improves the polarity of the blends. There is, however, no direct correlation between the surface tension and wax content in the blends.
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Heat capacity measurements with DSC on 1-octene-based very low density polyethylenes (VLDPEs), with densities from 888 to 907 kg/m3, show crystallization between 120 and −60°C and melting between −60 and 130°C. Under the assumption that hardly any octene groups are present in the crystal lattice, the experimental heat capacity values were compared with reference values for purely amorphous and purely crystalline linear polyethylene on the basis of a two-phase model. The enthalpy-based weight crystallinity data as a function of temperature show that the crystallinities at −60°C are about 40% higher than those at room temperature, which vary from 25 to 40% and are in good agreement with volume-based weight crystallinities. The crystallization and melting curves show several peaks. Fractionations by the crystallization/dissolution method and the direct extraction method show that this is due to intermolecular heterogeneity of comonomer incorporation and that VLDPE is a reactor blend of molecules ranging from the uncrystallizable and poorly crystallizable type to the HDPE type.