Evaluation of the Influence of Fibre Aspect Ratio and Fibre Content on the Rheological Characteristic of High Yield Pulp Fibre Reinforced Polyamide 11 “HYP/PA11” Green Composite

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The rheological behavior of composites made with low-density polyamide 11 (PA11) and high yield pulp fibre (HYP) is evaluated. The rheological properties of high-yield, pulp-reinforced bio- based Nylon 11 HYP/PA11 composite were investigated using a capillary rheometer. The rheological tests were realized in function of the shear rate for different temperature conditions. The experimental results showed that identically for fibre content and aspect ratio, the shearing effects decreased as the temperature increased; that is, the HYP/PA11 became more non-Newtonian in the higher temperature region, which corresponds to the high pseudoplasticity of the HYP/PA11. At low HYP content, the shear viscosity is expected to increase rapidly with increasing concentrations of the fibres because of the rapidly increasing interactions between particles as they become more closely packed. However, at very high fibre content, random anisotropic structure of the fibres in polymer melts is created. The increase in shear viscosity is greater at lower shear rates, where fibre and polymer molecules are not completely oriented.

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Open Journal of Polymer Chemistry, 2015, 5, 1-8
Published Online February 2015 in SciRes. [http://www.scirp.org/journal/ojpchem](http://www.scirp.org/journal/ojpchem)
http://dx.doi.org/10.4236/ojpchem.2015.51001

# Evaluation of the Influence of Fibre Aspect Ratio and Fibre Content on the Rheological Characteristic of High Yield Pulp Fibre Reinforced Polyamide 11 “HYP/PA11” Green Composite

Robenson Cherizol 1,2,3* , Mohini Sain 1,3 , Jimi Tjong 2

1Centre for Biocomposites and Biomaterials Processing, Faculty of Forestry, University of Toronto,
Toronto, Canada
2Powertrain Engineering Research & Development Centre, Ford Motor Company, Windsor,
Canada
3Department of Chemical Engineering & Applied Chemistry, University of Toronto, Toronto,
Canada
Email: * [Robenson.cherizol@mail.utoronto.ca](mailto:Robenson.cherizol@mail.utoronto.ca)

Received 23 December 2014; accepted 16 January 2015; published 19 January 2015

Copyright © 2015 by authors and Scientific Research Publishing Inc.
This work is licensed under the Creative Commons Attribution International License (CC BY).
[http://creativecommons.org/licenses/by/4.0/](http://creativecommons.org/licenses/by/4.0/)

Abstract

The rheological behavior of composites made with low-density polyamide 11 (PA11) and high
yield pulp fibre (HYP) is evaluated. The rheological properties of high-yield, pulp-reinforced biobased Nylon 11 HYP/PA11 composite were investigated using a capillary rheometer. The rheological tests were realized in function of the shear rate for different temperature conditions. The experimental results showed that identically for fibre content and aspect ratio, the shearing effects
decreased as the temperature increased; that is, the HYP/PA11 became more non-Newtonian in
the higher temperature region, which corresponds to the high pseudoplasticity of the HYP/PA11.
At low HYP content, the shear viscosity is expected to increase rapidly with increasing concentrations of the fibres because of the rapidly increasing interactions between particles as they become
more closely packed. However, at very high fibre content, random anisotropic structure of the fibres in polymer melts is created. The increase in shear viscosity is greater at lower shear rates,
where fibre and polymer molecules are not completely oriented.

*Corresponding author.

How to cite this paper: Cherizol, R., Sain, M. and Tjong, J. (2015) Evaluation of the Influence of Fibre Aspect Ratio and Fibre
Content on the Rheological Characteristic of High Yield Pulp Fibre Reinforced Polyamide 11 “HYP/PA11” Green Composite.
_Open Journal of Polymer Chemistry_, 5 [, 1-8. http://dx.doi.org/10.4236/ojpchem.2015.51001](http://dx.doi.org/10.4236/ojpchem.2015.51001)

R. Cherizol _et al_ .

Keywords

HYP/PA11, Rheological Characteristic, Shear Viscosity, Shear Rate

1. Introduction

Green-fibre-reinforced thermoplastic composites are in high demand in the automotive, aerospace, and construction industries. Vegetable fibres are biodegradable and renewable, they consume less energy than glass fibres,
and consequently they generate less pollution [1]. Other reasons for the high demand for the utilization of green
fibres are their low density and good thermal and acoustic properties [2]. Pulp fibres, moreover, do not abrade
processing tools [2] [3]. Materials from biological sources regroup natural polymers, so they can be expected to
exhibit viscoelastic behavior. Appropriate processing and production conditions for polymer products are determined by their rheological characteristics. Short-fibre reinforced polymer composites are extensively used in
manufacturing industries due to their light weight and superior mechanical properties [4]-[6]. Hence, pulp fibre
has been used not only for its low lignin content but also for its potential thermal stability and its strong adhesion when bonded with high-temperature engineering thermoplastic polymers [7]-[10]. The high-yield pulp
“HYP” fibres derived from hardwood that were used in this study are short semicrystalline fibres.

Various experimental studies have emphasized the investigation of the role of flexibility on fluid viscosity.
They concluded that the more flexible the fibres, the more pronounced their effect on the rheological characteristics [9]-[13].

A novel study on the effect of fibre-length distribution on the rheological behavior of castor oil composite
showed that at high fibre length the shear viscosity becomes more dependent on shear rate [11] [12]. This behavior is due to elastic deformation of the fibres [13].

Recently, several researchers have investigated the effect of fibre content on polymer melt rheology [14]-[16].
One such study showed an important increase in shear viscosity with increased fibre loading at low shear rates,
but only a small increase in viscosity at high shear rates. Another similar study on polypropylene-based long fibre observed an increase in shear viscosity with increased fibre content and fibre length; however, this viscosity
increase was very small, which the authors attributed to high shear rates and fibre breakage during processing

[17] [18]. Non-Newtonian fluid characteristics such as shear thinning were also observed in these studies.

That said, the literature devoted to experimental studies of the rheology of pulp fibres in reinforced polymer
composites is very restricted. This is likely due to the complex nature of these materials, the difficulties encountered during their processing as well as the difficulty of characterizing them rheologically [19]-[25].

Processing technique and conditions have a significant influence on the rheological and overall properties of
pulp-fibre-reinforced polymer composites because they dictate the degree of dispersion and distribution of the
fibre in the polymer matrix [25]-[28]. Compared to other natural fibres, HYP is more thermally stable in presence of high-melting-temperature engineering thermoplastics (under 180˚C) such as PA11, PA6 and PA66.

The aim of this study was to investigate the rheological characteristics of high-yield-pulp-reinforced bio-based
polyamide 11 composite. Experiments were mainly carried out by varying therheological testing temperatures,
the fibre content and aspect ratio.

2. Materials and Methods

2.1. Materials

The matrix biopolymer bio-based Nylon 11, density 1.03, MFI 11, was supplied by Arkema, France. Aspen
HYP fibers were supplied by Tembec (Montreal, QC). The HYP is the type used in wood-free printing and in
writing-paper grades and multiple-coated folding-board grades; fibre length is 0.230 to 0.85 mm. Finally, the
pulp-fibre length was reduced by using a mechanical crib in order to investigate the aspect ratio effect on the
rheological behavior of the HYP/PA11.

2.2. Methods

2.2.1. Composites Preparation
The experiment was processed using a Conical Twin Screw Extruder. In the mixing method, the HYP fibre was

R. Cherizol _et al_ .

dried at 80˚C for 6 hours and then added to the corresponding PA11 and well mixed before it was introduced to
the extruder. The average temperature of the barrel was 200˚C.

2.2.2. Effect of Processing Conditions
Many processing parameters affect the properties of final products. For extrusion, temperature profiles affect the
fibre degradation. In addition, screw speed and feeding rate change fibre length, distribution, and orientation.
Mechanical properties are the reflection of all these changes. The processing parameters are optimized to obtain
the best properties. Table 1 represents the processing parameters for HYP/PA11 used in this study.

2.2.3. Fibre Content Analysis and Determination of Fibre Length Distribution (Original Fibre
Length)
The samples of the fibre as received from the provider were cut into small pieces and immersed in formic acid
for three days. The nylon 11 was dissolved by the formic acid and HYP was left. The wood fibre was filtered
and washed with formic acid, then dried in a vacuum oven for four hours. By measuring the weight of composite
and fibre, we could calculate the actual fibre content.

HYP fibre length was measured with the Fiber Quality Analyzer (FQA). Fibre was diluted with D.I. water.
The diluted fibre entered a thin planar channel. This channel helped to gently orient the fibre 2-dimensionally, so
that the fibre could be fully viewed by the camera. The picture taken by the camera was then analyzed by the
software to give the fibre length distribution.

2.2.4. Rheological Properties Measurements
The rheological measurements of the composites’ melt-flow properties of were carried out in a twin-bore Rosand Capillary Rheometer model RH2000. (The standard RH2000 range supports temperatures from −40˚C to
500˚C. The standard maximum force applied is 12 kN.) The composite samples for testing were cut into very
small pieces, then placed inside the barrel and forced down into the capillary with the plunger attached to the
moving cross-head. Representative steady-shear viscosity versus high shear rate is presented in the figures below for HYP/PA11, which was processed at the average extrusion temperature of 200˚C. The viscosity of the
sample was obtained from steady-shear measurements for different temperature profiles, with the rate ranging
from 50 to 5000 S −1 . The rheology “viscosity” data presented in this paper thus represent an average value of
three measurements.

2.2.5. Scanning Electron Microscopy
Studies on the morphology of the composites were carried out using a scanning electron microscope (SEM). The
rheological test samples were ruptured by the rheometer and the fracture surfaces were examined. A Hitachi
S-800 Scanning Electron Microscope (SEM) was used to study the fracture surface and dissolved HYP-reinforced PA11 composites. The observation conditions were the following: pressure 0.3 mbar, acceleration voltage 15 keV.

3. Results and Discussion

3.1. Effect of Fibre Content on the Length and Shape Distribution on High Yield Pulp Fibre
Reinforced Bio-Based Nylon Composite

During the extrusion process, the shear stress applied by the screw breaks the fibres. The resulting fibre lengths
affect the ultimate mechanical properties. In spite of the influence of fibre damage and breakage during processing, the initial fibre length in the feedstock determines the fibres’ final lengths. It is therefore important to

Table 1. Extrusion temperature profile for 10%, 20% and 30% HYP/PA11, 120 RPM (10% and 20%), 130 RPM (30%) and
10 RPM feed rate.

Temperature (˚C)

Zone 1 Zone 2 Zone 3 Zone 4 Zone 5 Zone 6 Zone 7 Zone 8 Zone 9 Zone 10

200 200 200 200 200 205 205 205 205 205

R. Cherizol _et al_ .

analyze the initial fibre-length distribution. Table 2 represents the effect of fibre content on the length and shape
distribution on high yield pulp fibre reinforced bio-based nylon composite.

The arithmetical length-weighted and weight-weighted values of fibre length were found to be 0.18 mm, 0.28
mm and 0.51 respectively for the fibres from 30% HYP/PA11. Most of the fibre lengths lie within the range of
0.2 to 0.52 mm, since crushed pulp was used in this study. To obtain these average fibre lengths, 1500 single fibres were examined. The measured initial fibre length is shorter than the actual length of the fibres company
provided.

3.2. Rheological Characteristics of High-Yield-Pulp-Reinforced Bio-Based Nylon

Rheological characteristics of the polymer, fibre, and interphasial phases influence the final characteristics of the
resultant microstructure of the composite materials; these characteristics in turn affect the mechanical properties
of a multiphase polymer-composite system. As obtained from experiment, the shear viscosity as a function of
the steady-shear rate of HYP/PA11 at 200˚C is shown in Figure 1 . (As noted, these results are the average of
three different experimental tests.)

As noted, the composite material used in the experimental study had an average fibre length of 0.73 mm, and
the experiment was conducted at 200˚C. The experimental results showed that the viscosity of HYP/PA11 composite decreases with increasing shear rate. This decrease in the shear viscosity with the increase of the shear
rate corresponds to the pseudoplastic fluid characteristic of the composites. This pseudoplastic behavior (also
referred to as shear-thinning behavior) as plotted in Figure 1 is mainly influenced by the orientation of the polymer molecules, the agglomeration of the flexible pulp fibre, and the entanglements within the polymer chains
in the capillary rheometer. On the other hand, the chain agglomerations are produced simultaneously as one
chain is collapsed into another chain. The entanglements that lead to agglomerations of the chains, as well as the
entanglements within the chains, are caused by the Brownian motions and low relaxation of HYP fibre. The high
shear-thinning behavior obtained for HYP/PA11 can be also associated to the thermal degradation of HYP during the rheological testing and the compounding process. The molten polymers tend to arrange themselves with
their major axes in the direction of shear, whereby points of entanglement are reduced. As a result, the viscosity
decreases. In other words, in this instance of non-Newtonian flow behavior in polymer melts, the decrease in
viscosity when the shear rate is increased by applying load is associated with high shear-thinning behavior and

Table 2. Fibre length distribution of pulp fibre (original fibre length).

Fibre

Mean Length (Measured)

Arithmetic (mm) Length Weight (mm) Weight Weighted (mm)

Only HYP 0.38 0.57 0.73

HYP (10%) 0.20 0.29 0.44

HYP (20%) 0.20 0.29 0.43

HYP (30%) 0.18 0.28 0.51

800

700

600

500

400

300

200

100

0 500 1000 1500 2000 2500 3000 3500 4000 4500 5000

Shear rate (s −1 )

Figure 1. Shear viscosity vs. shear rate of HYP/PA11 at 200˚C.

R. Cherizol _et al_ .

with viscoelastic characteristics of biocomposite materials. However, at very high shear rates (from 3000 to
5000 S −1 ); the molten HYP/PA11 showed a less restrained decrease in viscosity. This non-Newtonian behavior
is associated with the alignment and orientation of the fibre in the polymer chains and the effect of the fibre aspect ratio. Both at low and high shear rates the formation of agglomerates is evident; therefore the pulp molecules are completely oriented due to the good dispersion in the bio-based PA11 matrix. This means that the
breakage of the fibre length allows the maintenance of an accurate fibre-aspect ratio when the diameter of flexible HYP is kept unchangeable during the process. The shorter length of the fibres also supports their alignment
in the direction of the flow, thus reducing the fibre-fibre collisions and leading to a greater decrease in viscosity.

3.3. Effect of the Temperature on the Shear Viscosity versus Shear Rate of
HYP-Reinforced PA11

The variation in shear viscosity as a function of the shear rate of HYP/PA11 at various temperatures was investigated and the rheological test results are presented in Figure 2 . The rheological conditions were kept constant
while different tests were run for 190˚C, 200˚C and 210˚C. The results are presented in the figure below.

The shear viscosity of the HYP/PA11 depended on the rate of shear at which it was measured and presented.
The shearing effects decreased as the temperature increased; that is, the HYP/PA11 became more non-Newtonian in the higher temperature region. At higher temperatures the reduction of shear viscosity is more pronounced at intermediate shear rate, while for 190˚C, this reduction is maximized at higher shear rates (from
3000 to 5000 S −1 ). At low testing temperature (190˚C) and for low and intermediate shear rate, the flow deformation is challenging. This is due to the fact that the HYP-reinforced PA11 fibres are entangled and agglomerated. At this point, such rheological behavior is called near-Newtonian. At high shear rate, the shearing effects
increased while the effect of temperature was less pronounced, and flow deformation was mostly dominated by
the shearing effect. However, from 3000 to 5000 S −1 all the shear-viscosity variations in function shear rates
followed the same rate of deformation for different temperature profiles, which corresponds to shear-thinning
behavior.

3.4. Effect of High Yield Pulp Fibre Content on the Rheological Behavior of HYP/PA11

The effect of fibre content on the rheological characteristics of the composite was investigated. Figure 3 shows
the experimental results for 10%, 20% and 30% HYPP reinforced polyamide 11. These curves are typical of
pseudoplastic materials, which show a decrease in viscosity with increasing shear rate. At high fibre content, the
material offers higher shear viscosity even for high shear rate. In general, the incorporation of fibres in polymer
systems increases the viscosity, which rises further as fibre content is increased.

The difference between 10% and 20% fibre at intermediate and high shear rate is not very significant. At low
HYP content, shear viscosity is expected to rise rapidly with increasing concentrations of fibre because of the
rapidly increasing interactions between particles as they become more closely packed. Nevertheless, at very high

190 degree

200 degree

210 degree

Shear rate (s −1 )

Figure 2. Variation of the viscosity with a function of shear rate of
HYP/PA11 at various temperatures.

R. Cherizol _et al_ .

900

800

700

600

500

400

300

200

100

10%BCTMP/PA11

20%BCTMP/PA11

30%BCTMP/PA11

0 1000 2000 3000 4000 5000

Shear rate (s-1)Shear rate (s −1 )

Figure 3. Shear viscosity vs. shear rate of HYP/PA11 at 200˚C.

fibre content, random anisotropic structures of the fibres in polymer melts are created. The increase in shear
viscosity is found to be more predominant at lower shear rates, where fibre and polymer molecules are not completely oriented.

3.5. Effect of High-Yield-Pulpfibre Aspect Ratio on Rheological Properties

The results from the study of the effect of the aspect ratio of flexible-pulp-fibre-reinforced bio-based nylon 11
are presented below in Figure 4 .

At low fibre aspect ratio, the decrease in viscosity as a function of the shear rate is greater for both low and
high shear rate. Contrarily, at higher fibre-aspect ratio the shear viscosity shows a moderate decrease for low and
intermediate shear rate.

At low and intermediate shear rate, the viscosity curves are slightly decreased and the distance between each
viscosity curve remains large. However, at high shear rate the viscosity plots are tightly close. This is because
fibre agglomeration and entanglement are not pronounced at high shear rate or frequency, due to the complete
orientation of the fibre and polymer molecules. Much as with high fibre content, the increase in shear viscosity
is found to be greater at lower shear rates, where fibre and polymer molecules are not completely oriented.

3.6. Scanning Electron Microscopy

Fracture surfaces of the extrudate of HYP/PA11 composite were examined using SEM. No fibre pullout was
observed. The chemical structures of polyamide and wood fibre both include a hydrogen bond, which makes for
better compatibility between high-yield pulp and polyamide. Figure 5 represents the SEM micrograph of HYP/
PA11 composite.

This micrograph indicated efficient bonding between the high-yield fibre and bio-based nylon. The experimental and predicted data fit very well, which meant that there was strong adhesion at their interface due to the
presence of the third phase.

4. Conclusion

This study demonstrates that it is possible to extrudate natural fibre with high-thermoplastic-engineering biobased nylon. Fibre distribution after processing has been characterized by FQA for high-yield fibre in composites containing 10%, 20% and 30% fibres. The low-temperature–process compounding presents higher shear
viscosity than the high-temperature processing of HYP/PA11 for the same rheological parameters. This is because during the process the temperature was low and the mixing and melting processes were generated by the
high shear rate created during extrusion. Experimental test results of HYP/PA11 for both processing parameters
show a steep decrease in shear viscosity with increasing shear rate, and this melt-flow characteristic corresponds
to shear thinning behavior in HYP/PA11. Experimental results showed high shear-thinning behavior in
HYP/PA11 associated with a high degree of pseudoplasticity; this was due to the good dispersion of high-yield
pulp fibre into Nylon11 and the orientation of the flexible pulp fibre in the direction of the molten PA11. Finally, the
morphological properties of HYP/PA11 composite were examined using scanning electron microscopy (SEM). Due

R. Cherizol _et al_ .

Figure 4. Shear viscosity vs. shear rate of HYP/PA11 at 200˚C.

Figure 5. An SEM micrograph of pulp-fibre-reinforced polyamide compo-
site fracture surface showing partially melted nylon fibre.

to the presence of the hydrogen bond, no fibre pullout was observed and there was good adhesion between highyield pulp fibre and polyamide.

Acknowledgements

This work was carried out with the support of Mitacs funding; the University of Toronto and the Ford Motor
Company financially supported this study.

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