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1	
	
	
and	
	 Aerospace	Engineering	
	 Ashby	Building	
	 Stranmillis	Road	
	 Belfast	
	 BT9	5AH	
	
	
	
	
	
Mechanical	and	Aerospace	Engineering	
	
	
	
	
	
	
	
Final	Year	Project	Technical	Report	
Project	3B	
AER3021	
	
	
Fabrication	and	Characterization	of	Novel	Boron	Nitride/Polymer	nanocomposite	
	
	
	
	
	
	
Author:	Sayed	Asif	Iqbal	[40110295]	
Project	Supervisor:	Dr	Dan	Sun	
Programme:	BEng	Aerospace	Engineering	
Date:	18th
	March	2016
2	
Table	of	Contents	
List	of	Symbols	and	Abbreviations	.......................................................................................	3	
1.0	Introduction	...................................................................................................................	4	
2.0	Literature	Review	...........................................................................................................	5	
2.1	BN	Nanofillers	.........................................................................................................................	5	
2.2	BN	Nanofillers	in	contrast	with	Carbon	precursors	................................................................	6	
2.3	Polymer	processing	Techniques	..............................................................................................	7	
2.4	Dispersion	of	Nanofillers	into	Polymer	matrix	........................................................................	8	
2.5	Post-extrusion	stretching	........................................................................................................	9	
3.0	Methodology	..........................................................................................................................	11	
3.1	Materials	...............................................................................................................................	11	
3.1.1	Polymers	and	Nanoparticles	..............................................................................................	11	
3.2	Pre-Melt-Mixing	Processes	...................................................................................................	11	
3.3	Melt-mixing	Process	..............................................................................................................	12	
3.3.1	Twin-screw	Configuration	..................................................................................................	12	
3.3.2	Twin-screw	Extrusion	Processing	.......................................................................................	13	
3.4	Characterization	...........................................................................................................	14	
3.4.1	Mechanical	Analysis	...........................................................................................................	14	
3.4.1.1	Tensile	test	in	room	temperature	conditions	.................................................................	14	
3.4.1.2	Uniaxial	stretching	at	elevated	temperature	conditions	................................................	15	
3.4.2	Thermal	Analysis	................................................................................................................	15	
3.4.3	Structural	Analysis	..............................................................................................................	16	
4.0	Results	and	Discussion	...........................................................................................................	16	
4.1	Mechanical	Analysis	..............................................................................................................	16	
4.2	Thermal	Analysis	...................................................................................................................	20	
4.3	Structural	Analysis	.................................................................................................................	23	
5.0	Conclusions	.............................................................................................................................	24	
6.0	Recommendation	of	further	work	.......................................................................................	25	
7.0	References	..............................................................................................................................	26
3	
	
List	of	Symbols	and	Abbreviations	
	
BN	 	 Boron	Nitride	
HDPE	 	 High	density	Polyethylene		 	
eV	 	 Electron	Volts	
h-BN	 	 Horizontal	Layered	Boron	Nitrite	
BNNs	 	 Boron	Nitride	nanosheets	
BNNTs	 	 Boron	Nitride	nanotubes	
CNT	 	 Carbon	nanotubes	
SR	 	 Stretching	Ratio	
Wt%	 	 Percentage	weight	
QUB	 	 Queen’s	University	Belfast	
CS	 	 Crosshead	speed	
Tm	 	 Melting	temperature	
Tc	 	 Crystallization	temperature	
Xc	 	 Crystallinity	content	
Impr	 	 Improvement
4	
	
1.0	Introduction	
	
Polymers,	according	to	Oxford	Dictionary,	are	simply	the	combinations	of	small	simple	molecules	
grouped	together	in	a	chain-like	order	to	form	large	and	long	groups	of	atoms.	The	word	‘polymer’	
was	first	coined	by	a	Swedish	chemist	called	‘Jöns	Jacob	Berzelius’	in	1832	[1]	and	later	established	
by	a	German	chemist	named	‘Hermann	Staudinger’	in	1905	[2].	The	beauty	behind	the	sciences	of	
such	‘macromolecules’	intrigued	the	chemists	from	the	very	start	of	1900s.	With	later	discoveries	
in	the	progression	of	time,	it	was	quite	surprising	to	find	out	that	polymers	existed	all	around	and	
within	us.	Macro	molecules	are	found	to	be	present	by	far	and	wide,	from	the	food	we	eat	which	
contains	starch	or	proteins,	to	the	very	bits	of	DNA	strands	inside	our	infinitesimal	body	cells	[3].		
	
	These	naturally	occurring	polymers	emerged	after	pursuits	of	tremendous	studies	conducted	to	
interpret	material	sciences	and	biophysics.	From	the	data	gathered	from	these	studies	to	the	in-
depth	understanding-	all	these	lead	to	the	evolution	of	synthetic	polymers,	and	now	it	is	nearly	
impossible	to	imagine	our	world	without	them.	Understanding	these	useful	macro	molecules	have	
enabled	us	to	customize	and	alter	their	structures	to	achieve	composite	materials	with	desired	
properties	relevant	to	its	use.	Greatest	evidences	will	include	usage	of	‘para-aramid’	in	bulletproof	
and	waterproof	vests,	‘meta-aramid’	in	the	hood	of	fire-fighter’s	mask,	‘copolyamid’	in	fiber	optic	
cables	and	many	more	[4].	To	get	the	most	out	of	these	materials	and	to	make	our	lives	easier,	two	
or	more	different	materials	are	blended	in	an	effort	to	accomplish	the	best	properties	of	both.	Such	
nanocomposite	materials	with	at	least	one	component	of	nanoscopic	scale	in	size	(10-9
m)	have	
remarkable	 properties	 like	 high	 surface	 to	 volume	 ratio,	 increased	 ductility	 and	 are	 scratch	
resistant,	and	so	on.	[5].		
	
This	project	is	about	fabrication	and	characterization	of	Boron	nitrite/high	density	polyethylene	
nanocomposites.	Along	with	a	comprehensive	research	for	the	understanding	of	the	structure	and	
properties	 of	 these	 materials,	 the	 project	 will	 also	 reflect	 and	 unfold	 the	 industrially	 relevant	
polymer	processing	technique	called	"extrusion".	Different	proportions	of	boron	nitrite	powders,	
ordered	from	SIGMA-ALDRICH,	will	be	melt-mixed	with	high	density	polyethylene	pallets	under	
twin-screw	 extrusion	 process.	 Suitable	 composite	 samples	 will	 be	 extracted	 from	 the	 extruded	
sheet	and	appropriate	testing	methods	standards	will	be	identified.	Samples	will	also	be	stretched	
in	 the	 uniaxial	 direction	 to	 scrutinize	 material	 behavior	 exposed	 to	 different	 test	 conditions.	
Moreover,	 these	 samples	 will	 be	 tested	 using	 different	 engineering	 equipment	 and	 detailed
5	
comparisons	will	be	obtained	and	investigated.	Result	analysis	will	later	be	discussed	to	provide	
better	reasoning	and	understanding	of	the	micro	structural	behavior.	
2.0	Literature	Review	
	
2.1	BN	Nanofillers	
	
After	 the	 evolution	 of	 Rubber	 technology	 at	 roughly	 1800s,	 synthetic	 polymers	 started	 being	
fabricated	and	just	prior	to	world	war	II,	this	industry	started	to	grow	introducing	different	arrays	
of	materials	referred	to	as	‘Plastics’.	These	pallets	or	powders	are	produced	by	mechanical	blending	
or	melt	state	mixing	procedures	[6].	Boron	nitride	nanocomposites,	a	structural	analogue	of	carbon	
precursors,	were	first	fabricated	at	the	late	90s.	Instead	of	carbon	atoms	linked	in	chains,	boron	
and	nitrogen	atoms	are	joined	up	alternatively	[7].	With	at	least	one	dimension	in	between	the	
scale	of	1	to	100	nanometers,	these	extraordinary	and	flexible	forms	of	nanostructures	can	be	
formed	 into	 various	 structural	 arrangements	 e.g.	 nanotubes,	 nanosheets,	 nanohorns,	 spherical	
nanoparticles,	etc[	8].		
	
	
Fig	2.1:	TEM	image	of	BN	Nanosheets	
	
The	layered	nature	and	planar	networks	between	the	BN	hexagons	allow	such	flexibility	to	produce	
nanosized	BN	which	is	much	superior	in	various	properties	compared	to	the	traditional	microsized	
BN	fabricated	years	ago.	BN	nanostructures	are	equipped	with	novel	properties	intrinsically	which
6	
includes	wider	bandgap	up	to	6	eV,	anti-oxidation	and	structural	ability,	high	thermal	conductivity	
and	great	mechanical	properties	[8].	In	contrast	with	the	aforementioned	attributes	which	are	quite	
similar	to	corresponding	carbon	materials,	boron	nitride	analogues	possess	several	unique	features	
that	 makes	 them	 quite	 significant	 in	 modern	 world.	 These	 structures,	 unlike	 carbon	
nanocomposites,	 are	 white	 or	 transparent	 in	 color	 due	 to	 its	 wide	 bandgap	 so	 can	 be	 dyed	
depending	on	different	requirements	[8].	Moreover,	the	carbon	precursors	are	observed	to	lower	
the	 electrical	 insulation	 of	 polymers,	 whereas	 BN	 nanostructures	 are	 dielectric	 in	 nature	 that	
strengthen	 its	 use	 as	 gate	 layers	 and	 remarkable	 use	 in	 electronic	 packaging.	 In	 recent	 years,	
nanosized	BN	as	shown	in	figure	2.1	are	produced	with	very	high	aspect	ratio,	thermal	conductivity	
up	to	thousands	of	Wm-1
K-1
	(when	used	as	nanofillers)	and	tremendous	material	strength	[8].	
	
	
	
	
2.2	BN	Nanofillers	in	contrast	with	Carbon	precursors	
	
BN	nanosheets	are	comprised	of	one	or	few	layers	of	hexagonal	boron	nitride	(h-BN).	After	the	rise	
of	Graphene	in	the	year	of	2005,	the	first	pure	monolayer	h-BN	was	originated	in	a	mechanically	
milled	residue[9].	So	far,	various	methods	are	implemented	including	ball	milling	[11],	mechanical	
cleavage	[10],	the	reaction	between	boric	acid	and	urea[13-14]	and	high	energy	electron	beam	
irradiation	[12].	Ultrathin	nanosheets	are	produced	from	chemical	vapor	disposition	(CVD)	method	
[9].	Whereas	the	‘chemical	blowing’	method	is	considered	to	be	the	simplest	of	all	due	to	its	catalyst	
and	substrate-free	route	[9].	Besides,	it	not	only	gives	the	luxury	to	obtain	larger	lateral	dimensions	
of	 BN	 nanosheets	 that	 aids	 research	 to	 be	 carried	 out	 regarding	 its	 electrical	 and	 mechanical	
behaviors,	 but	 also	 can	 be	 used	 later	 on	 to	 produce	 strong	 polymer	 composites	 [9].	 The	 CVD	
method	is	widely	used	to	produce	both	BN	nanosheets	and	nanotubes:	one	or	few	layers	of	BN	
sheets	rolled	up	to	nanoscale.	Figure	2.1	represents	a	brief	tabular	comparison	between	graphene,	
BNNSs,	CNT	and	BNNTs	[8]:
7	
	
	
Fig	2.2:	Comparison	between	graphene,	BNNSs,	CNT	and	BNNTs	properties	in	different	fields	in	a	
nutshell	[8].	
	
	
2.3	Polymer	processing	Techniques	
	
In	the	plastic	processing	industry,	injection	moulding	is	widely	used	to	process	polymer	composites	
due	 to	 its	 cost-effective	 way	 of	 processing	 three-dimensional	 and	 complex	 thermoplastics	 at	
greater	quantities	[16].	However,	the	parts	and	equipment	like	hopper,	feed	throat,	barrel,	etc.	are	
expensive	to	maintain	and	it’s	costly	to	operate	the	machine	as	well.	With	series	of	procedures,	
polymers	are	processed	via	injection	moulding.	The	plastic	pallets	are	fed	to	the	injection	unit	
where	it	is	heated	by	the	barrel	and	melted	the	by	the	sheer	force	of	the	revolving	screw.	Later	the	
melted	polymers	are	pushed	into	the	mould	section	where	the	shape	of	the	plastic	is	altered	by	
heating	and	cooling	in	various	different	ways.	Other	moulding	techniques	like	blow	and	rotational	
moulding	are	also	used.	
Techniques	like	extrusion	and	injection	moulding	are	worth	mentioning.	Conventional	extrusion	
processes	 are	 material	 intensive	 techniques	 where	 the	 polymers	 are	 manipulated	 in	 molten	
state[6].	This	is	considered	as	the	state	of	the	art	technique	till	date	because	it	is	specialized	to	
produce	final	product	from	raw	polymers.	The	mechanism	is	quite	simple	where	the	nanofillers	are	
dispersed	into	the	polymer	matrix	by	melt	mixing	[6].	An	archetypal	extruder	can	be	of	two	types:	
single	 screw	 and	 twin	 screw	 extruder.	 Both	 extrusion	 processes	 have	 horizontal	 barrels	 with	
adjustable	temperature	cores,	a	hopper	to	collect	the	raw	materials,	extruder	and	die	section.	Raw
8	
materials	are	taken	down	and	then	crushed	and	melted	by	the	rotating	screw(s)	in	the	extruder,	
thus	dispersing	the	additives	into	the	polymer	matrix	[17].	The	final	products	then	exit	through	the	
end	 of	 the	 barrel	 or	 die	 section.	 The	 screw	 speed	 is	 alterable	 to	 maintain	 smooth	 mixing	 and	
dispersion	into	the	polymer	matrix,	even	if	the	melt	solution	gets	too	viscous	due	to	more	addition	
of	nanofillers[18].	
The	screw(s)	inside	the	barrel	play(s)	crucial	role	in	mixing	the	raw	materials.	Single-screw	extrusion	
process	implies	the	barrel	containing	one	screw	rotating	only	in	order	to	blend	the	raw	polymers	in	
few	different	stages.	The	screw,	when	analyzed,	is	seen	to	have	different	depths	along	its	length	
and	can	be	classified	into	three	sections	carrying	out	different	functions	in	each	region.	The	feed	
section	screw	will	simply	rotate	and	take	up	the	raw	materials	into	the	compression	section	which	
has	lesser	screw	depth	[18].	This	change	in	depth	not	only	allows	to	apply	pressure	and	compress	
the	polymers,	but	also	squeezes	the	air	bubble	and	send	them	back	to	the	previous	section	of	the	
rotating	screw.	The	polymers	are	sharply	and	gradually	melt	mixed	and	then	conveyed	to	the	meter	
section	where	the	screw	depth	is	lowest	and	is	constant	throughout	the	section.	Temperature	in	
each	section	will	differ	throughout	the	process	to	depending	on	the	melt	characteristics	of	the	
materials.	The	metering	screw	zone	will	homogenize	the	melt	until	fed	to	the	die	section	which	has	
constant	 temperature	 and	 pressure	 conditions	 [19].	 Moreover,	 the	 die	 section	 will	 filter	 and	
separate	by	getting	rid	of	extraneous	material	and	letting	the	expected	product	polymer	to	extrude	
out.	
	
For	twin-screw	extrusion	system,	two	screws	are	rotated	in	different	syntaxes	to	serve	the	purpose.	
The	two	collaborating	screws	can	be	positioned	into	four	types	of	screw	systems	including	co-	
rotating/counter-rotating	 intermeshed	 and	 co-rotating/counter	 rotating	 non-intermeshed.	 For	
intermeshing	 screws	 attached	 together,	 flow	 patterns	 are	 not	 allowed	 to	 pass	 in-between	 the	
screws.	 But	 for	 non-intermeshing	 arrangements	 small	 clearance	 is	 observed	 where	 the	 flow	
patterns	are	compared	with	the	figure-of-eight	[18].	Operation	variables	like	heat	generation	and	
mixing	efficiency	are	enhanced	to	get	optimized	outputs.	
	
	
2.4	Dispersion	of	Nanofillers	into	Polymer	matrix		
As	far	as	dispersing	nanofillers	into	polymer	matrix	are	concerned,	dispersion	properties	or	types	
depend	directly	on	the	shear	forces	exerted	by	the	screw(s)	system.	Two	types	of	dispersion	are	
listed	as	dispersive	and	distributive	mixing.	Dispersive	mixing	is	concerned	with	the	process	where
9	
the	 screws	 exert	 high	 shear	 forces	 which	 breaks	 large	 clusters	 into	 small	 ones	 by	 overcoming	
interacting	forces	and	dispersing	them	throughout	the	solution.	Whereas	distributive	mixing,	on	
the	other	hand,	is	referred	to	take	place	in	a	low	shear	exertion	system	where	the	weak	forces	
interacting	 between	 the	 nanofillers,	 distributing	 them	 uniformly	 through	 the	 melt.	 Screw	
geometries	are	responsible	for	the	amount	of	shear	force	exerted	to	the	mixture	which,	therefore	
high	 shear	 forces	 are	 crucial	 to	 achieve	 dispersive	 mixing.	 However,	 high	 shear	 forces	 are	
responsible	for	breaking	the	clusters	into	finer	ones,	but	this	type	of	flow	is	not	enough	as	we	are	
required	to	disperse	the	nanofillers	as	well.	Applying	high	shear	forces	by	altering	screw	geometries	
is	only	half	the	job	done,	other	main	flow	type	is	solely	required	referred	to	as	elongation	plays	a	
great	 role	 in	 uniform	 dispersion	 [20].	 Higher	 extensional	 elongation	 can	 be	 applied	 to	 the	
nanoparticles	in	the	polymer	melt	in	the	twin	screw	extrusion	process.	It	is	also	observed	that	high	
screw	 speed	 and	 longer	 mixing	 time	 is	 the	 key	 to	 better	 morphology	 of	 the	 nanocomposites	
obtained.		
	
2.5	Post-extrusion	stretching		
	
Biaxial	and	uniaxial	stretching	takes	place	in	the	extrusion	process	where	the	nanoparticles	and	the	
polymer	while	in	melt	state.	Not	only	that	during	post	processing,	a	sample	cut	from	the	extruded	
sheet	can	be	taken	and	stretched	in	solid	state	in	one	or	both	direction	in	the	x,	y	plane.	It	is	
significant	to	observe	that	the	post-extrusion	stretched	nanocomposites	had	different	properties	
compared	to	that	of	un-stretched	ones.	In	a	research	carried	out	by	the	School	of	Aerospace	and	
Mechanical	 Engineering,	 QUB	 on	 biaxial	 stretching	 [21]	 of	 polymer	 nanocomposites,	 novel	
enhanced	properties	were	observed.	With	a	temperature	between	145-150	degrees	being	set	up,	
a	 76mm×76mm×1mm	 compression	 moulded	 sheet	 of	 PET/clay	 nanocomposite	 is	 biaxially	
stretched	at	1.5,	2.5,	3	and	3.5	stretching	ratios	and	loaded	at	the	strain	rate	of	8	and	16s-1.	Each	
test	were	repeated	twice	to	get	a	better	approximation	of	the	results.	The	forces	and	displacement	
at	x,	y	plane	were	recorded	by	the	help	of	Labview	Data	Logging	Package.	Looking	at	the	results,	it	
concludes	that	higher	strain	rates	were	driving	a	higher	yield	stress	of	the	sample	[21].	Moreover,	
addition	of	clay	as	a	filler	were	contributing	to	greater	entanglement	of	the	molecules.	Higher	yield	
stress	at	lower	temperature	was	also	observed	as	nanofilled	composite	materials	are	more	sensitive	
to	temperature.	Under	X-ray	diffraction	(XRD)	analysis,	it	is	monitored	that	the	d-spacing	in	the	
PET/clay	lattice	is	noted	to	reduce	at	the	strain	rate	of	1.5.	Besides,	the	d-spacing	slightly	increased	
with	higher	strain	rates	which	was	still	lower	than	that	of	the	unstretched	sheet.	So	this	overall	
decrease	took	place	because	of	the	compression	of	the	clay	particles	(nanofillers)	due	to	stretching
10	
[21].		
In	 TEM	 analysis,	 the	 stretched	 and	 unstretched	 samples	 are	 compared	 under	 ultrahigh	
magnification	 where	 it	 is	 observed	 that	 on	 stretching	 it	 is	 evident	 that	 the	 delamination	 of	
nanofillers	were	resulting	to	stack	up	and	align	the	particles.	Differential	Scanning	Calorimetry	(DSC)	
were	used	to	examine	the	crystallinity	of	the	test	sample.	It	was	observed	that	the	crystallinity	was	
increasing	with	higher	strain	rates	but	it	also	concluded	that	greater	crystallinity	doesn’t	contribute	
to	higher	mechanical	strength	[21].	It	is	also	seen	that	the	tensile	strength	only	increases,	when	the	
sample	is	stretched	and	the	highest	strength	is	achieved	at	the	highest	strain	rate	of	3.5,	also	giving	
rise	to	the	break	stress.	This	is	described	and	associated	with	the	better	unity	of	the	polymer	due	
to	temperature	application	and	stress	exertion.	It	is	also	very	important	to	notice	that	the	effect	on	
modulus	is	not	observed	until	the	sample	was	stretched	up	to	SR	2.5.	This	happens	because	the	
degree	of	alignment	of	the	molecules	are	only	articulated	at	this	very	stage.	This	rate	might	differ	
from	different	starting	material	to	form	the	nanocomposite	[21].		
Unlike	biaxial	stretching,	uniaxial	stretching	is	similar	but	the	sample	is	either	stretched	along	the	
length	 or	 perpendicular	 to	 the	 length.	 In	 terms	 of	 uniaxial	 stretching,	 equipment	 like	 two	
dimensional	wide	angle	x-ray	scattering	(2D-WAXS)	fit	to	serve	the	purpose	to	characterize	the	
sample	after	it	is	stretched.	DSC	is	also	used	in	biaxial	stretching	characterization.	The	process	is	
quite	 similar	 to	 biaxial	 stretching	 as	 the	 sample	 is	 uniformly	 heated	 and	 but	 stretched	 at	 one	
direction	only.	Hence	by	the	help	of	all	state	of	the	art	equipment,	like	WAXS	and	DSC,	the	sample	
uniaxial	stretched	sample	is	characterized	in	terms	of	thermal	or	mechanical	strengths.
11	
	
3.0	Methodology	
	
The	 mechanisms	 equipped	 in	 QUB	 to	 produce	 boron	 nitride/high	 density	 polyethylene	
nanocomposite	sheets	and	preparing	them	for	characterization	processes	are	shown	in	Fig	3.1:	
	
	
	
	
	
	
	
	
	
	
	
	
	
Fig	3.1:	Preparation	plan	for	high	density	polyethylene/boron	nitride	nanocomposites	samples	
	
	
3.1	Materials	
	
3.1.1	Polymers	and	Nanoparticles	
	
Non	hazardous	and	odorless	High	density	polyethylene,	ordered	from	Safripol,	were	used	as	a	
polymer	 matrix	 for	 this	 project.	 These	 pallets	 were	 grounded	 prior	 to	 twin-screw	 melt	 mixing	
process	 in	 order	 to	 ensure	 a	 homogenous	 mix.	 Boron	 Nitride	 powder,	 molecular	 weight	 of	
24.82g/mol,	were	procured	from	Sigma-Aldrich	in	order	to	be	used	as	filler	material	to	produce	
BN/HDPE	nanocomposite	sheets,	of	approximately	1mm	thickness,	through	an	industrially	relevant	
processing	route	called	twin-screw	extrusion.		
	
3.2	Pre-Melt-Mixing	Processes	
	
Five	transparent	plastic	bags	were	labelled	initially	with	an	intent	to	classify	different	percentage	
of	filler	composition	to	be	mixed	with	the	polymer	matrix.	Both	materials	were	weighed	manually	
using	 the	 available	 laboratory	 scale	 equipment	 in	 the	 Material	 processing	 hall	 at	 QUB.	 Five	
compositions	were	pre-melt-mixed	at	0	wt%,	0.1	wt%,	0.2	wt%,	0.5	wt%	and	1	wt%	BN	powders	
with	HDPE	pallets.	Five	plastic	bags	containing	the	aforementioned	composition	of	BN	powder	with	
HDPE	pallets	were	well	shaken	up	for	few	minutes.	Safety	measures	like	disposable	face	masks	and	
HDPE(Polymer)	
Pallets	
Boron	Nitride	
Powder	
Melt	Mixing	in	
QUB	Twin-screw	
extruder	
Extruded	
Sheet	
Cut	
Samples	
Characterization
12	
lab	eyewear	were	equipped	at	all	times	to	prevent	accidental	exposure	of	the	materials	with	human	
contact.		
	
3.3	Melt-mixing	Process	
	
3.3.1	Twin-screw	Configuration	
	
The	Collin	GmbH	twin-screw	extruder	were	set	up	at	a	particular	customized	screw	configuration	
to	enhance	mixing	of	the	materials	shown	below	in	figure	3.2.	The	screw	profile	consists	of	
kneading	blocks(KB),	conveying(GL)	and	mixing	elements(ZMI)	in	both	forward(R)	and	reverse(L)	
directional	flow	effects.	The	detailed	screw	configuration	indicates	the	variation	of	different	
mixing	inputs	at	each	section	of	the	screw	profile	which	contributes	to	the	enhancement	of	the	
mixing	quality	and	filler	dispersion.	
	
	
	
Fig	3.2:	Schematic	of	screw	profile	designed	to	enhance	mixing	
	
For	better	and	in-depth	understanding,	few	screw	elements	were	picked	from	this	configurations	
and	notations	were	described	in	figure	3.3	below:	
	
	 Overall	length	(mm)	
	 	Conveying	direction	(R=forward,	L=Reverse)	
	
	
	
Fig	3.3:	Nomenclature	for	ZK	25	co-rotating	twin-screw	extruder	screw	profile	
Width	of	discs	(mm)	(KB	only)	
Angular	offset	of	the	discs(KB);	Pitch	(mm)	
(GL)	
Nominal	diameter	(mm)
13	
3.3.2	Twin-screw	Extrusion	Processing		
		
The	melt-mixing	process,	with	an	intent	to	disperse	the	nanofillers	uniformly	into	the	polymer	
matrix,	were	conducted	using	the	Collin	GmbH	co-rotating	intermeshing	twin	screw	extruder.	With	
the	screw	diameter	of	25mm	and	barrel	length	of	750mm,	the	temperature	settings	of	six	different	
zones	were	configured	from	170	to	200	degrees	Celsius	ranging	from	zone	1	to	6.	Six	different	screw	
configurations	were	used	to	facilitate	mixing	as	mentioned	in	the	previous	section	of	the	report.		
	
The	premixed	BN	powders	and	HDPE	pallets	were	fed	to	the	hopper	using	screw	speed	of	85	rpm.	
With	a	residence	time	1.75	min	allowed	for	each	mixture	composition,	six	different	batched	were	
subjected	to	the	hopper	one	after	another.	The	initial	plan	was	to	create	a	master	batch	of	the	
extruded	composite	material	of	different	specifications	and	palletize	them	for	further	compression	
molding	in	the	QUB	platen	press	equipment.	But	due	to	the	lack	of	enough	materials	and	to	save	
time	the	batches	were	extruded	directly	into	sheets	of	1	mm	thickness	and	the	width	of	100	mm	
after	exiting	through	the	die	using	the	controllable	clearance	between	two	hydraulically	closed	chill	
rolls	in	three	roll	up	stack	configuration	depicted	in	figure	3.4.	The	following	table	3.1	gives	detailed	
picture	of	the	parameters	used	in	the	process:	
Table	3.1:	Process	parameters	set	for	BN/HDPE	twin-screw	extrusion	
	
	
Fig	3.4:	Chill	rolls	in	three	roll	up	stack	configuration	(left),	Collin	ZK	25	twin-screw	extruder	(right)	
BN/HDPE	 Zone	1	 Zone	2	 Zone	3	 Zone	4	 Zone	5	 Zone	6	 Die	
Set	Temperature(°C)	 170	 195	 200	 200	 200	 200	 205	
Actual	Temperature(°C)	 168	 195	 200	 201	 201	 200	 205	
Screw	Rotation	Direction	 Co-rotating	
Screw	Speed(rpm)	 85	
Residence	Time(min)	 1.75	
Feeding	rate(kg/h)	 3.5	
BN	Loading(%)	 0	 0.1	 0.2	 0.5	 1
14	
3.4	Characterization	
	
3.4.1	Mechanical	Analysis	
	
3.4.1.1	Tensile	test	in	room	temperature	conditions	
	
After	the	fabrication	process	were	carried	out	under	twin-screw	extrusion,	the	individual	extruded	
sheet	of	1mm	thickness	and	100mm	width	were	labelled	carefully	to	classify	four	filler	composition	
batches	with	the	virgin	material	batch	and	stored	for	testing	and	characterization	phase.	Stamping	
press	at	the	QUB	characterization	lab	was	used	to	cut	five	type	1BA	dumbbell	shaped	specimens	
from	each	fabricated	sheets	of	different	BN	loadings	along	the	extrusion	or	machine	direction(MD)	
as	shown	in	figure	3.5.	
	
Instron	 5564	 universal	 tester	 with	 a	 gauge	 length	 of	 55mm	 were	 set	 up	 at	 room	 temperature	
conditions,	where	samples	were	stretched	up	to	an	extension	of	10mm	at	5mm/min	crosshead	
speed.	At	this	specific	phase	the	elastic	modulus	was	found	from	the	slope	of	tensile	stress	and	
strain	curve,	and	the	test	was	repeated	four	more	times.	Specimen	thicknesses	were	measured	
before	 every	 repetition	 to	 enhance	 accuracy	 of	 the	 results.	 The	 equipment	 was	 also	 set	 up	 to	
increase	the	crosshead	speed	to	500mm/min	once	it	reached	the	extension	of	10mm,	subjecting	
the	 specimen	 up	 to	 its	 complete	 deformation	 or	 breaking	 point,	 to	 predict	 the	 strength	 and	
elongation	values	at	a	constant	gauge	length.	Detailed	and	in-depth	characterized	parameters	and	
findings	will	be	discussed	on	the	next	section	of	the	technical	report	(see	section	4.1).	
	
	
Fig	3.5:	Schematic	of	uniaxial	machine	direction	stretching
15	
3.4.1.2	Uniaxial	stretching	at	elevated	temperature	conditions	
	
BN/HDPE	composite	dumbbell	shaped	specimens	of	1mm	thickness	and	75mm	length	were	also	
exposed	 to	 higher	 temperature	 conditions	 and	 uniaxially	 stretched	 to	 detect	 temperature	
responsive	variations	in	material	behavior.	The	temperature	conditions	were	controlled	by	a	box	
shaped	 environmental	 chamber	 along	 with	 an	 in-built	 fan	 wrapped	 around	 the	 Instron	 5564	
universal	tester	crossheads	where	the	maximum	elongation	was	limited	to	60mm	due	to	structural	
constraints	or	limitations.		
	
The	 gauge	 length	 was	 reduced	 to	 25mm	 to	 accommodate	 the	 samples	 to	 be	 pulled	 up	 to	 the	
stretching	ratio	of	3.	Crosshead	speed	were	adjusted	according	to	the	strain	rate	of	4/s.	The	samples	
were	 loaded	 and	 the	 temperature	 was	 raised	 to	 125°C	 and	 stretched	 under	 aforementioned	
parameters	and	later	allowed	to	cool	down	back	to	room	temperature	normally.	Three	samples	
from	each	of	five	total	compositions	are	tested	to	minimize	errors.	Figure	3.6	below	shows	the	
environmental	 chamber	 equipment	 and	 a	 stretched	 sample.	 Strength	 and	 elongation	 values	
formulated	during	the	process	were	extracted	for	benchmarking	and	analysis.	
	
	
Fig	3.6:	Environmental	chamber	(left),	Stretched	specimen	(right)		
	
3.4.2	Thermal	Analysis	
	
Percentage	 of	 crystallinity	 of	 the	 BN/HDPE	 nanocomposite	 samples	 were	 investigated	 by	 DSC	
(Differential	 Scanning	 Calorimetry)	 using	 a	 Perkin-Elmer	 DSC	 model	 6	 under	 inert	 nitrogen	
atmosphere.	Uniaxially	stretched	and	unstretched	samples	were	taken	and	cut	into	small	samples,
16	
typical	mass	of	only	7-10mg,	followed	by	sealing	them	inside	small	aluminum	pans	and	lids	by	
crimping	them	in	the	press.	The	inner	and	outer	lids	of	the	DSC	furnace	were	removed	to	place	the	
sealed	sample	on	the	left	sample	pan.	The	furnace	lids	were	replaced	back	and	the	equipment	were	
set	up	to	raise	the	temperature	of	the	furnace	from	30°C	to	200°C	at	a	pace	10°C/min	for	both	
stretched	and	unstretched	samples.	Furthermore,	the	unstretched	samples	were	held	at	200°C	for	
3	minutes	and	cooled	down	to	30°C	at	the	same	rate	of	10°C/min	and	heated	back	to	200°C	again	
using	 the	 same	 gradient	 trend	 mentioned	 above	 to	 check	 the	 bulk	 properties	 have	 changed	
fundamentally	or	not.	Stretched	samples	were	not	checked	for	bulk	property	changes	because	they	
were	already	heated	again	while	stretching	under	elevated	temperature	conditions.	The	apparent	
percentage	crystallinity	of	the	content	is	measured	using	the	formula	below:	
	
%	𝑐𝑟𝑦𝑠𝑡𝑎𝑙𝑙𝑖𝑛𝑖𝑡𝑦 =
𝑚𝑒𝑎𝑠𝑢𝑟𝑒𝑑	∆𝐻
100%	𝑐𝑟𝑦𝑠𝑡𝑎𝑙	∆𝐻
×100	
∆𝐻 = 𝐻𝑒𝑎𝑡	𝑜𝑓	𝑓𝑢𝑠𝑖𝑜𝑛	
100%	𝑐𝑟𝑦𝑠𝑡𝑎𝑙	∆𝐻 = 293	J/g	[22]	
	
3.4.3	Structural	Analysis	
	
The	structure	of	the	samples	and	the	degree	of	dispersion	of	the	BN	fillers	into	the	HDPE	matrix	
were	investigated	using	Scanning	Electron	Microscopy	(SEM).	Reactive	ion	etching	system	were	
used	to	plasma	etch	the	samples.	This	high	speed	plasma	glow	discharge	is	shot	at	the	samples	for	
60	s	and	at	the	power	of	100w	and	then	gold	coated	or	sputtered	prior	to	imaging.	Joel	6500	Field	
Emission	Scanning	Electron	Microscopy	were	used	with	operating	voltages	of	3	and	5	kV	to	
examine	the	samples.		
	
	
4.0	Results	and	Discussion	
4.1	Mechanical	Analysis	 	
	
Dog	bone-shaped	samples	were	stretched	as	mention	previously	and	tensile	tests	were	carried	out	
at	room	temperature	conditions.	Five	samples	were	tested	till	breaking	stress	were	applied	and	
average	young’s	modulus	and	yield	stress	values	were	extracted	from	the	Instron	data	logging	
package.	Figure	4.1	provides	the	variation	of	tensile	modulus	and	yield	stress	values	with	different	
composition	of	boron	nitride	fillers	used	during	fabrication	process.
17	
	
	
Fig	4.1:	Variation	of	Young’s	Modulus	and	Yield	Stress	observed	in	Tensile	test	at	room	
temperature	
	
The	elastic	modulus	of	pure	HDPE	samples	was	measured	to	be	100.17	MPa	and	according	to	the	
graphical	 representation,	 these	 values	 were	 observed	 to	 increase	 with	 increasing	 wt%	 of	 filler	
boron	 nitride	 upto	 0.1	 wt%	 BN,	 but	 decrease	 dramatically	 with	 higher	 filler	 compositions.	 The	
moduli	values	were	seen	to	increase	2.4%	for	0.1	wt%	BN,	1.1%	for	0.2	wt%	BN,	decrease	afterwards	
to	5.5%	for	0.5	wt%	BN	and	3.3%	for	1	wt%	BN	with	respect	to	unfilled	pure	HDPE	samples.	All	these	
values	are	the	result	of	the	85rpm	rotation	speed	used	during	twin-screw	extrusion	fabrication	
process.	The	elastic	modulus	would	have	been	different	if	different	screw	speeds	were	used	during	
the	fabrication	process	due	to	different	degree	of	filler	distribution	into	the	polymer	matrix.	Higher	
screw	speeds	would	add	up	to	higher	shear	forces	at	increasing	mixing	energy	input	that	would	
have	 triggered	 the	 modulus	 values.	 However,	 there	 is	 a	 significant	 increase	 of	 2.4%	 in	 tensile	
modulus	at	0.1	wt%	BN	and	the	highest	value	achieved	was	1024.56	MPa	from	these	samples.	The	
increase	in	modulus	is	indicative	of	good	particle	dispersion	at	the	loading	level	of	0.1	wt%	BN	that	
resulted	higher	stiffness.	Moreover,	the	significant	elastic	modulus	drop	at	higher	BN	loadings	is	
suspected	to	result	due	to	the	increase	in	particle	agglomeration.	This	kind	of	behavior	is	suspected	
because	the	materials	were	melt-mixed	and	extruded	straight	to	sheets	of	1mm	thickness	rather	
than	extruding	them	into	pallets	and	preparing	the	samples	after	compression	molding.		
	
Besides,	the	yield	stress	values	were	seeming	to	drop	as	well	with	increasing	filler	composition	of	
BN.	The	stress	values	are	observed	to	drop	by	1.2%	at	0.1	wt%	BN,	1.19%	at	0.2	wt%	BN,	4.7%	at	
0.5	wt%	BN	and	6.1%	at	1	wt%	BN	with	respect	to	neat	unfilled	HDPE	samples.	This	indicates	that,
18	
the	stress	level	at	which	the	filled	polymers	ceased	to	behave	elastically	decreased	with	higher	filler	
composition,	probably	due	to	creation	of	microvoids	resulting	from	phase	separation	of	BN/HDPE	
interface	 [23].	 This	 can	 also	 result	 from	 lesser	 restriction	 on	 molecular	 mobility	 or	 decreased	
entanglement	of	molecules.	
	
By	 increasing	 the	 crosshead	 speed	 to	 500mm/min	 the	 samples	 were	 also	 examined	 to	 detect	
mechanical	 behavior	 in	 complete	 deformation	 process.	 The	 breaking	 stress	 is	 discovered	 to	
increase	till	0.1	and	0.2	wt%	BN	with	contrasting	value	drops	at	other	two	higher	BN	compositions.	
This	 might	 be	 attributed	 to	 the	 structural	 orientation	 of	 the	 molecules	 and	 non-uniform	 filler	
dispersion	on	higher	BN	loadings.	On	the	other	hand,	strain	to	failure	percentage	data	on	different	
filler	composition	is	scrutinized	to	show	very	low	fluctuations	except	0.1	wt%	BN.	The	bar	charts	
below	depict	the	breaking	stress	and	strain	fluctuations:	
	
	
Fig	4.2:	Effect	of	addition	of	BN	fillers	on	breaking	stress	and	strain	values	
	
Its	is	very	vital	to	note	that	all	these	aforementioned	tensile	tests	were	carried	out	under	normal	
room	 temperature	 conditions.	 On	 the	 other	 hand,	 samples	 were	 also	 subjected	 to	 elevated	
temperature	condition	of	125°C	by	stretching	them	up	to	the	ratio	of	three	and	strain	rate	of	4/s.	
With	respect	to	the	tensile	test	carried	out	at	room	temperature,	both	Young’s	modulus	and	yield	
stresses	are	observed	to	decrease	in	high	magnitudes	with	high	temperature	conditions.	Both	the	
filler	and	polymer	matrix	materials	are	observed	to	be	highly	responsive	to	temperature	and	strain	
rates	while	stretched	and	the	parameters	used	in	both	scenarios	are	very	different	from	each	other	
that	generated	such	significant	variation	in	the	extracted	values	presented	at	figure	4.3	below:
19	
	
	Fig	4.3:	Variation	of	Young’s	Modulus	and	Yield	Stress	observed	in	Tensile	test	at	125°C	
	
	 Young’s	Modulus(MPa)	
At	rtp,	cs	5mm/m	 At	125°C,	sr=3	 Drop(%)	
100	HDPE	 1000.17	 28.75	 97.12	
0.1	wt%	BN	 1024.56	 24.73	 97.58	
0.2	wt%	BN	 1010.83	 23.88	 97.63	
0.5	wt%	BN	 944.72	 24.45	 97.41	
1	wt%	BN	 966.70	 26.56	 97.25	
	 Yield	Stress(MPa)	
100	HDPE	 26.10	 2.77	 89.38	
0.1	wt%	BN	 25.77	 1.91	 92.59	
0.2	wt%	BN	 25.79	 2.39	 90.73	
0.5	wt%	BN	 24.88	 2.47	 90.07	
1	wt%	BN	 24.52	 2.46	 89.96	
Table	4.1:	Effect	of	temperature	and	strain	rate	on	tensile	properties	
	
It	 is	 observed	 that	 both	 young’s	 modulus	 and	 yield	 stress	 dropped	 remarkably	 with	 increasing	
temperature	and	strain	rate	conditions	up	to	97.63%	and	90.73%	respectively.	It	is	also	discovered	
that	under	elevated	temperature	conditions	that	filled	HDPE	samples	were	characterized	to	have	
lower	elastic	modulus	with	respect	to	the	unfilled	samples.	It	is	believed	that	the	drop	in	both	of	
these	mechanical	parameters	is	related	to	the	fall	in	strain	hardening	rate	of	the	materials.	It	is	
expected	that	the	temperature	applied	were	close	to	the	glass	transition	temperature	of	HDPE	
where	molecular	segmental	motions	were	activated	and	less	force	was	required	for	deformation	
as	elastic	modulus	is	basically	a	measure	of	stiffness	or	hardness.	HDPE	is	a	semi	crystalline	polymer	
where	the	main	crystalline	regions	break	down	close	to	the	melting	temperatures.	It	is	indicative	of	
the	partial	polymer	chain	rotations	that	resulted	such	a	high	drop	in	the	elastic	modulus.	It	is	also	
detected	that	at	high	temperature	the	variation	or	standard	deviation	between	the	moduli	values	
are	also	decreased	substantially	with	a	similar	pattern	in	the	stress	at	yielding	stage.
20	
4.2	Thermal	Analysis	
	
For	DSC	examination,	the	stretched	and	unstretched	samples	were	taken	up	and	tested	to	measure	
percentage	crystallinity	of	five	different	BN	loadings	for	unstretched	and	three	BN	composition	for	
stretched	 samples.	 Melting	 and	 crystallization	 behavior	 for	 these	 samples	 were	 extracted	 and	
presented	 in	 figure	 4.4.	 The	 thermograms	 of	 the	 unstretched	 samples	 are	 compared	 within	
different	phases	that	refers	to	the	first	heating	cycle,	cooling	down	in	the	same	rate	and	heating	
again	for	second	time	to	delete	thermal	history	and	to	check	if	the	bulk	polymer	may	have	changed	
fundamentally	or	not.	
	
It	is	clearly	visible	on	figure	4.4	that	the	crystallization	endotherms	have	changed	its	shape	with	
increasing	BN	filler	addition	as	the	crystallization	peaks	get	wider	due	to	the	change	in	crystal	type	
and	perfection.	This	can	happen	because	less	perfect	crystallites	melt	partially	at	low	temperatures	
making	the	average	crystal	shape	larger	[24].	And	at	higher	temperatures	the	molecular	chains	are	
more	 mobile	 producing	 more	 crystallites	 and	 making	 the	 average	 crystal	 size	 smaller.	 These	
recrystallized	crystallites	are	also	detected	to	have	higher	melting	peaks	corresponding	to	higher	
BN	 loadings	 due	 to	 the	 formation	 of	 more	 perfect	 crystals	 with	 greater	 dimensions	 and	 lesser	
deformity.			
	
Fig	4.4:	Crystallization	exotherms	of	unstretched	samples	
	
The	addition	of	BN	have	contributed	to	slight	improvement	in	percentage	crystallinity	with	respect	
to	the	unfilled	neat	HDPE.	Highest	improvement	in	crystallinity	for	unstretched	samples	are	found	
to	be	67.05%	for	0.2	wt%	BN	loading	which	enhanced	the	unfilled	HDPE	up	to	9.58%.	At	higher	filler
21	
composition	the	enhancements	are	found	to	be	a	bit	upsetting	as	higher	loadings	of	0.5	and	1	wt%	
BN	did	improve	the	crystallinity	with	respect	to	neat	HDPE	but	reduced	with	respect	to	unstretched	
0.2	wt%	BN	samples.	This	explains	that	at	higher	BN	loadings,	it	is	relatively	difficult	to	disperse	the	
fillers	into	the	polymer	matrix	during	melt-mixing.	Higher	screw	speeds	might	have	been	required	
to	enhance	mixing	and	enhance	the	availability	of	nucleating	sites	for	HDPE	crystallization	[25].		
	
	
Fig	4.5:	Comparison	of	melting	endotherms	with	first	and	second	stage	heating	
	
Other	set	of	stretched	samples	are	only	tested	for	first	heating	cycle	as	they	have	already	been	
subjected	to	higher	temperature	during	uniaxial	stretching.	The	generated	endotherms	are	found	
to	be	potent	and	narrower,	implying	that	the	uniaxial	stretching	has	contributed	to	more	ordered	
and	synchronized	crystallite	patterns.	Addition	of	BN	and	stretching	barely	affected	the	melting	
temperature.	It	is	also	important	to	note	that,	the	highest	enhancement	in	percentage	crystallinity	
is	found	in	stretched	1wt%	BN	samples	where	it	is	calculated	out	to	be	15.94%	higher	than	the	
unfilled	stretched	sample	(see	Table	4.2	and	Figure	4.6).	Moreover,	a	contrasting	behavior	can	be	
pointed	out	if	compared	to	the	unstretched	material	of	same	BN	loading	of	1wt%.	Moreover,	the	
crystallinity	content	increased	by	18.6%	higher	due	to	stretching	at	higher	temperature	condition	
that	 helped	 the	 molecular	 chains	 to	 align	 in	 a	 better	 orientation	 with	 the	 fillers.	 Percentage	
crystallization	Xc		of	unfilled	HDPE	were	measured	to	be	about	61.2%	that	raised	to	63.9%	with	an	
addition	of	1wt%	BN,	which	further	increased	to	74.8%	after	being	stretched	uniaxially	at	125°C.	
This	undoubtedly	indicates	that	both	BN	nucleated	and	strain	induced	HDPE	crystallization	has	
contributed	to	the	higher	crystallization	content	achieved.
22	
	
	
	
Fig	4.6:	Melting	Endotherms	of	Stretched	samples	at	high	temperatures	
	
Table	4.2:	Effect	of	wt%	MWCNT	and	the	uniaxial	stretching	on	the	Thermal	properties	of	unfilled	
HDPE	and	BN/HDPE	composites.
First	Heating	Cycle	 Cooling	stage	 Second	Heating	Cycle	
	 Tm	
(°C)	
Impr	
(%)	
∆H	
(J/g)	
Xc	
(%)	
Impr	
(%)	
Tc	
(°C)	
Impr	
(%)	
∆H	
(J/g)	
Tm	
(°C)	
∆H	
(J/g)	
Xc	
(%)	
Impr	
(%)	
Unstretched	Samples	
Unfilled	
HDPE	
133.85	 	 199.48	 68.10	 	 113.27	 	 194.93	 135.07	 179.30	 61.19	 	
0.1	
wt%	BN	
132.69	 -0.87	 205.49	 70.13	 2.90	 114.27	 0.88	 186.58	 134.69	 187.26	 63.91	 4.45	
0.2	
wt%	BN	
133.02	 -0.62	 205.79	 70.23	 3.12	 114.31	 0.91	 193.89	 134.78	 196.45	 67.05	 9.58	
0.5	
wt%	BN	
133.02	 -0.62	 194.29	 66.31	 -2.63	 113.69	 0.37	 194.08	 134.91	 189.84	 64.79	 5.89	
1	wt%	
BN	
133.07	 -0.58	 181.47	 61.93	 -9.05	 114.11	 0.74	 192.18	 136.00	 184.75	 63.05	 3.03	
Stretched	Samples*	
Unfilled	
HDPE	
136.16	 	 189.01	 64.51	 	 *	Stretched	samples	at	125°C	 	
	
0.2	
wt%	BN	
136.62	 0.33	 188.01	 64.16	 -0.54	
1	wt%	
BN	
136.15	 -0.01	 219.13	 74.79	 15.94
23	
	
4.3	Structural	Analysis	
	
Typical	SEM	micrographs	were	obtained	from	the	plasma	etched	samples	to	conduct	structural	and	
morphological	study	effected	from	the	addition	of	BN	fillers.	The	pure	HDPE	micrographs	gives	a	
vivid	identity	of	semi-crystalline	structure	of	HDPE	chains	with	the	mixture	of	both	semi-crystalline	
and	amorphous	regions.	Furthermore,	SEM	image	of	a	filled	0.5wt%	BN	samples	were	clicked	at	
higher	magnifications	to	understand	the	degree	of	dispersion	of	BN	fillers	in	the	HDPE	polymer	
matrix.	 It	 is	 seen	 and	 discovered	 that	 the	 filler	 distribution	 is	 not	 that	 uniform	 and	 lot	 of	
agglomeration	regions	are	pointed	out	that	can	be	the	reason	why	higher	BN	loadings	did	not	
achieve	remarkable	enhancement	in	crystallinity	content.	Besides,	microscopic	voids	were	detected	
in	 the	 image	 of	 the	 same	 BN	 loading	 sample	 that	 might	 have	 resulted	 from	 phase	 separation	
BN/HDPE	interface	which,	in	turn,	have	decreased	the	yield	stresses	with	increasing	BN	additions.		
	
With	 even	 higher	 magnifications	 the	 stretched	 samples	 at	 1wt%BN	 at	 high	 temperature	 were	
scrutinized	to	detect	the	shear	and	stretching	direction.	These	micrographs	are	the	evidence	that	
stretching	and	high	temperature	exposure	of	these	samples	contributed	to	better	alignment	of	the	
BN	fillers	and	molecular	mobility	that	enhanced	the	crystallinity	content.	
	
	
Fig	4.7:		Unfilled	HDPE	(upper	left);	unstretched	0.5	wt%BN	(upper	right);	stretched	
1wt%BN(lower)
24	
	
5.0	Conclusions	
	
• Young’s	Modulus	for	tensile	testing	at	room	temperature	have	increased	highest	up	to	2.4%	
at	 0.1wt%BN	 resulted	 from	 good	 particle	 dispersion,	 and	 decreased	 up	 to	 5.5%	 at	
0.5wt%BN	loading	levels	suspected	due	to	higher	particle	agglomeration.	Yield	stresses	
were	measured	to	drop	at	all	higher	BN	loading	levels	with	the	highest	of	6.1%	at	1wt%BN.	
Breaking	stresses	at	higher	crosshead	speed	showed	similar	patterns	with	young’s	modulus	
whereas	percentage	strain	at	break	got	barely	affected	with	different	BN	loading	levels.	
• Both	BN	and	HDPE	were	observed	to	be	highly	responsive	to	temperature	and	strain	rates	
as	both	young’s	modulus	and	yield	stress	values	dropped	significantly	attributed	to	the	
decreasing	 strain	 hardening	 rate	 of	 the	 materials	 while	 subjected	 to	 125°C.	 At	 such	
conditions	the	standard	deviations	of	the	moduli	values	were	very	low	compared	to	that	of	
lower	room	temperature	settings.		
• For	unstretched	samples,	addition	of	BN	fillers	have	triggered	a	slight	improvement	in	the	
crystallinity	contents.	Highest	Xc	was	measured	to	be	67.05%	at	0.2wt%BN.	Moreover,	with	
higher	BN	loadings	than	0.2wt%	the	crystallinity	content	were	measured	to	drop	indicating	
the	difficulty	to	disperse	the	filler	material	in	the	polymer	matrix	in	melt-mixing.	
• For	 uniaxially	 stretched	 at	 high	 temperature	 samples,	 highest	 Xc	 among	 all	 other	
crystallinity	content	were	measured	to	be	74.8%	at	1wt%	BN.	This	is	attributed	to	the	better	
ordering	of	the	crystallites	pattern	that	enabled	better	alignment	of	the	fillers	with	the	
HDPE	molecular	chains.	BN	addition	and	high	temperature	stretching	had	both	collectively	
contributed	to	the	improvement	in	crystallization	content.
25	
	
	
6.0	Recommendation	of	further	work		
	
• The	samples	selected	for	this	project	includes	small	percentage	(0.1,	0.2,	0.5,	and	1)	of	BN	
loadings	 to	 be	 added	 with	 HDPE	 that	 implies	 the	 difficulty	 to	 compare	 characterized	
parameters.	 With	 such	 small	 composition	 of	 fillers,	 little	 interference	 might	 add	 up	 to	
higher	 margin	 of	 error	 that	 makes	 difficult	 to	 draw	 conclusions.	 Higher	 BN	 loadings	
composite	 materials	 like	 5wt%,	 10wt%	 and	 20wt%	 can	 be	 processed	 by	 twin	 screw	
extrusion	process.		
• Regardless	of	the	fact	that	we	are	dealing	with	lower	or	higher	compositions,	different	
screw	 speeds	 can	 be	 applied	 while	 melt	 mixing	 to	 detect	 the	 effect	 of	 screw	 speed	 in	
mechanical	and	thermal	properties	of	the	fabricated	composite	material.	
• The	samples	can	also	be	stretched	biaxially	and	tested	later	by	DSC	to	see	the	change	of	
crystallinity	content,	melting	and	crystallization	peaks	with	respect	to	uniaxially	stretched	
samples.		
• The	uniaxially	stretched	samples	which	were	tested	in	DSC	can	be	later	tested	again	at	
Instron	till	breaking	or	totally	deforming	the	sample	at	room	temperature	to	measure	the	
difference	in	young’s	modulus,	yield	stress	and	other	vital	elongation	values	with	respect	
to	the	unstretched	samples.
26	
6.0 References	
	
	
1. Berzelius,	J.J.	and	Svanberg,	“Jahres-Bericht	über	die	Fortschritte	der	Chemie”,	Vol.	11-13,	
p-64,	1832.	
2. Mülhaupt,	 R.,	 “Hermann	 Staudinger	 and	 the	 Origin	 of	 Macromolecular	 Chemistry”,	
Angewandte	Chemie	International	Edition,	43:	1054–1063.	doi:10.1002/anie.200330070,	
2004.	
3. John,	M.J.	and	Thomas,	S.,	“Natural	Polymers:	Composites”,	Royal	Society	of	Chemistry,	
2012.		
4. Peacock,	A.J.	and	Calhoun,	A.R.,	“Polymer	Chemistry:	Properties	and	Application”,	Hanser	
Gardner	Publications,	2006.		
5. Twardowski,	 T.D.,	 “Introduction	 to	 Nanocomposite	 Materials:	 Properties,	 Processing,	
Characterization”,	DEStech	Publications,	pp.	2-3,	2007.		
6. Strutt,	 J.V.a.D.,	 Polymer	 Processing.	 Materials	 Science	 and	 Technology,	 2003.	 19(9):	 p.	
1161-1169.	
7. Chopra,	N.G.,	Luyken,	R.J.,	Cherrey,	K.,	Crespi,	V.H.,	Cohen,	M.L.,	Louie,	S.G.,	Zettl,	A.,	Boron	
nitride	nanotubes.	Science,	1995.	269(5226):	p.	2	
8. Wenjun	Meng,	Y.H.,	Yuqiao	Fu,	Zifeng	Wanga	and	Chunyi	Zhi,	Polymer	composites	of	boron	
nitride	nanotubes	and	nanosheets	Journal	of	Material	Chemistry	C,	2014(2):	p.	13.	
9. Xuebin	 Wang,	 C.Z.,	 Qunhong	 Weng,	 Yoshio	 Bando	 and	 Dmitri	 Golberg,	 Boron	 Nitride	
Nanosheets:	novel	Syntheses	and	Applications	in	polymeric	Composites	Journal	of	physics,	
2013(471):	p.	10.	
	
10. Novoselov	KS,	Jiang	D,	Schedin	F,	J	Booth	T,	Khotkevich	VV,	Morozov	SV	and	Geim	AK	2005	
Proc.	Natl.	Acad.	Sci.	USA	102,	10451	
	
11. Pacile	D,	Meyer	JC,	Girit	CO	and	Zettl	A	2008	Appl.	Phys.	Lett.	92,	133107	
	
12. Li	LH,	Chen	Y,	Behan	G,	Zhang	HZ,	Petravic	M	and	Glushenkov	AM	2011	J.	Mater.	Chem.	21,	
11862	
	
13. Jin	C,	Lin	F,	Suenaga	K	and	Iijima	S	2009	Phys.	Rev.	Lett.	102,	195505	
	
14. Nag	A,	Raidongia	K,	Hembram	KPSS,	Datta	R,	Waghmare	UV	and	Rao	CNR	2010	ACS	Nano	
4,	1539	
	
15. Raidongia	K,	Nag	A,	Hembram	KPSS,	Waghmare	UV,	Datta	R	and	Rao	CNR	2010	Chem.	Eur.	
J.	16,	149	

27	
16. Kennedy,	 P.	 (1995).	 Flow	 Analysis	 of	 Injection	 Molds.	 Cincinatti,	 Hanser/Gardner	
Publications.	
	
17. Crawford,	R.	J.,	(1998),	“Plastics	Engineering”,	3rd	edition,	BH.,	Oxford.	
	
18. Mark,	J.E.,	(2007),	“Physical	properties	of	polymers	handbook”,	2nd	edition,	Springer,	New	
York.	
	
19. Kroschwitz,	J.I.,	Mark	H.F.,	(2003),	“Encyclopedia	of	polymer	science	and	technology”,	3rd	
Edition,	Wiley	Interscience.	
	
20. Giles	H.F.,	Wagner	J.	R.,	Mount,	E.M.	(2004)	Extrusion:	The	definitive	processing	guide	and	
handbook.	William	Andrew	Inc.,	11,	97-101;	12,	115-120;	13,	133-136.	
	
21. Abu-Zurayk,	R,	Harkin-Jones,	E.,	McNally,	T.,	Menary,	G.,	Martin,	P.,	Armstrong,	C.	Biaxial	
deformation	behavior	and	mechanical	properties	of	a	polypropylene/clay	nanocomposite,	
Composites	Science	and	Technology	69	(2009)	1644–1652.	
	
22. Wunderlich,	B.,	Macromolecular	Physics,	Crystal	structure,	Morphology,	Defects,	Vol.	1,	
Academic	press,	1973.	
23. Astarita	G.,	Nicolais	L.,	Polymer	Processing	and	Properties,	Springer	Science	and	Business	
Media,	2012.		
24. Tzavalas,	S.,	Mouzakis,	D.E.,	Drakonakis,	V.,	Gregoriou,	V.G.	(2008)	‘Polyethylene	
terephthalate-multiwall	nanotubes	nanocomposites:	Effect	of	nanotubes	on	the	
conformations,	crystallinity	and	crystallization	behavior	of	PET’,	J.	Polym.	Sci.,	Part	B:	
Polym.	Phys,	46,	668-676.		
25. G.	Gamon,	Ph.	Evon	and	L.	Rigal,	Industrial	Crops	and	Products,	2013,	46,	173. 

28	
	
	
	
	
	
	
	
Appendix	A	Project	Management	
	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 16/11/2015	 Location	 Ashby(06.035)	
Review	of	actions	from	previous	meeting	
Progression	of	reading	more	papers	about	the	topic.	Lab	induction	attended	along	with	gaining	
lab	access.	BN	powders	ordered	from	Sigma	Alrich.	
Discussions,	Decisions,	Assignments	
Few	aspects	of	the	confusions	arised	from	the	research	papers	are	clarified.	Guidance	about	
progress	report	is	provided.	Contents	to	be	written	are	suggested.		
Agreed	actions	and	completion	dates	
Progress	report	is	to	be	completed	and	submitted	by	20th
	of	November	
Date	and	time	of	
next	meeting	
23/11/15	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 23/11/2015	 Location	 Ashby(06.035)	
Review	of	actions	from	previous	meeting	
Progress	report	handed	in.	
Discussions,	Decisions,	Assignments	
Sample	preparation	using	single/twin	screw	extrusion	method	using	different	percentage	of	BN	
powders.	Multiples	samples	are	to	be	prepared	for	stretching	and	distinguished.	Get	5	samples	
each	for	different	tests.		
Agreed	actions	and	completion	dates	
Get	the	sample	size	dimensions	used	in	a	previous	study	of	such	kind	
Date	and	time	of	
next	meeting	
30/11/15
29	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 1/12/2015	 Location	 Ashby(06.035)	
Discussions,	Decisions,	Assignments	
Quantities	of	samples	to	be	formed	(six	for	each).	Use	SEM	to	analyze	morphology	of	the	
stretched	and	unstretched	samples.		
Agreed	actions	and	completion	dates	
Contact	Physics	building	to	Book	SEM	
Complete	sample	cutting	before	next	meeting	
Date	and	time	of	
next	meeting	
8/12/15	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 14/12/2015	 Location	 Ashby(06.035)	
Discussions,	Decisions,	Assignments	
Cut	more	dumb-bell-shaped	samples	for	tensile	testing	along	the	machine	direction.	Try	
different	strain	rates	at	higher	temperature	condition.		
Agreed	actions	and	completion	dates	
Meet	Dr.	Beatriz	to	discuss	about	characterization	
Book	Instron	and	DSC	
Date	and	time	of	
next	meeting	
25/01/2016	
	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 25/01/2016	 Location	 Ashby(06.035)	
Review	of	actions	from	previous	meeting	
Additional	tensile	test	samples	were	cut.			
Discussions,	Decisions,	Assignments	
Availability	of	the	test	equipments.	Biaxial	samples	to	be	cut.	
Agreed	actions	and	completion	dates	
Contract	Dr.	Richao	to	see	how	tensile	tests	are	done	
Understand	DSC	procedures		
Date	and	time	of	
next	meeting	
02/02/2016	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 02/02/2016	 Location	 Ashby(06.035)	
Review	of	actions	from	previous	meeting	
Instron	booked	for	9th
	February	
Discussions,	Decisions,	Assignments	
Biaxial	stretching	procedures.	DSC	procedures	
Agreed	actions	and	completion	dates	
Contract	Dr.	Richao	to	see	how	tensile	tests	are	done	
Understand	DSC	procedures		
Date	and	time	of	
next	meeting	
16/02/2016
30	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 16/02/2016	 Location	 Ashby(06.035)	
Review	of	actions	from	previous	meeting	
Tensile	tests	carried	out.	More	samples	are	cut	for	biaxial	stretching	
Discussions,	Decisions,	Assignments	
Choice	of	protocol	for	DSC	procedures	
Agreed	actions	and	completion	dates	
Finish	biaxial	stretching	as	soon	as	possible		
Date	and	time	of	
next	meeting	
01/03/2016	
	
Project	Title	 Fabrication	and	Characterization	of	Novel	BN/HDPE	nanocomposites	
Supervisor	 Dr	Dan	Sun	 Student	 Sayed	Asif	Iqbal	
Date	And	Time	 01/03/2016	 Location	 Ashby(06.035)	
Review	of	actions	from	previous	meeting	
Biaxial	stretching	were	attempted	several	times,		but	couldn’t	be	carried	out	due	to	technical	
difficulties.	DSC	done	for	8	samples	in	total	
Discussions,	Decisions,	Assignments	
Comparison	of	stretched	and	unstretched	samples.	Mechanical,	thermal	and	structural	analysis	
suggestions	were	given	out	by	the	supervisor.	Conclusion	and	future	recommendations	are	to	
be	included	in	the	final	year	technical	report.		
Agreed	actions	and	completion	dates	
Write	up	final	technical	report	within	18th
	march	2016		
Date	and	time	of	
next	meeting	
	
	
	
Appendix	B	Turnitin	Originality	Check

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