chapter ii experimental -...
TRANSCRIPT
Chapter II
Experimental
Chapter II : Experimental
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Introduction
This chapter describes about the laboratory at which the research work carried out,
the specifications and sources of different raw materials used for the research work.
Detailed description about sample preparation techniques, their designation,
morphological characterization and measurement of physico-mechanical properties are
also provided in this chapter.
2.1. Brief about Research Laboratory and its facilities like ISO, NABL
The Research work was carried out at “Indian Rubber manufacturers Research
Association” [IRMRA], Thane, Maharashtra. IRMRA is a Govt. of India affiliated
Research Institute established in 1959, to provide scientific and technological support to
rubber and allied industries. At present, IRMRA is under Administrative control of
Department of Industrial Policy and Promotion (DIPP), Ministry of Commerce and
Industry, Government of India. In the last 5 decades, IRMRA has rendered remarkable
service to rubber and allied Industries and has become internationally well known Centre
of excellence for tyre and Non tyre rubber products. IRMRA is well known for its
expertise in the field of Testing and Investigation, Research Products/Compound
development training & manpower development, consultancy services, and has
diversified its activities in the new sophisticated areas such as Nano technology and
Latex technology as well as Rubber Engineering.
2.2. Materials
Brief description of various raw polymers, Fillers and chemicals used for the
Research work are given below:
2.2.1. Polymers / Rubbers
Selection of Polymer / Rubber / Elastomer is the first step in compounding for any
specific application. Each polymer / elastomer has its own unique properties. All
elastomers are elastic, flexible, tough, and relatively impermeable to both water and air.
Elastomer is macromolecular material which can rapidly return to the approximate shape
from which they have been substantially distorted by a weak stress. Usually, there are
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double bonds in the backbone that can be vulcanized using sulphur in combination with
organic accelerators to give required elastic properties [1]
Table 2.1. Polymers / Rubbers, grade, their source of supply and specification:
S.No Name of Polymer
used
Supplier /
Manufacturer Grade & Specification
1.
Acrylonitrile
Butadiene Rubber
(NBR)
JSR
Corporations
Grade : JSR 230 S
ACN Content : 35 %
Mooney Viscosity : ML1+4(100°C): 56
Sp. Gr. : 0.98
2
Hydrogenated
Acrylonitrile
Butadiene Rubber
(HNBR)
Lanxess
Therban : Grade used : 3907
ACN content :39 %
Mooney Viscosity [ML1+4 @100°C): 70
Residual double bond : 0.9
Density : 0.96
3
Ethylene Propylene
Diene Monomer
Rubber (EPDM)
DSM
Elastomers
Keltan 512: DSM
Ethylene Content: 43.5 %
Mooney Viscosity [ML 1+4 (1000C ): 50
Density: 1.00
Table 2.1 gives the details about various rubbers which have been used in this
research study. These were obtained from the reputed source of manufacturer and also
verified for the purity of the grade and the chemical parameters were specified so that the
consistency of rubber qualities is maintained throughout the research.
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2.2.2 Nanofillers:
Table 2.2 shows the list of various fillers with specification and name of the
suppliers used in this research work
Table 2.2 Nano-fillers, their source of supply and specification:
S.
No.
Name of
Material Manufacturer Grade, if any and specification
1. Nano graphite
powders
Kaiyu industrial
(HK) limited
Chemical Formula: C
Atomic Weight of Carbon: 12.01
Boiling Point: Sublime
Melting Point: 3650oC (6602
oF)
Evaporation Rate: none
Appearance: Grey-black solid
Vapor Pressure: Negligible at room
temperature
Vapor Density: Negligible at room
temperature
Odor: Odorless
2. Nano Clay
Crystal Nanoclay,
Pune.
Crysnano 1010
Crysnano1010 is a natural
montmorillonite modified with
quaternary ammonium salt.
Color : White
Purity : 98 %
Moisture content : < 2 %
Particle size : 90 % passing at 28
3. Nano Silica
Naoshell, USA Nano Shell: 99.8 % pure
Surface Area: 175-225 m2/gm
B.P: 2230 0C
M.P: 1600 0C
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2.2.3 Dispersion aids:
The Table 2.3 shows the dispersion aids, their source of supply and specification:
Table 2.3 Dispersion aids
S.No Name of
dispersion aid
Supplier /
Manufacturer Specification
1. Liq. NBR Nipol
% ACN Content : 28 %
Viscosity : 38-52 cps
Sp. Gr : 0.96
2. DOP Sigma-Aldrich
Physical Form : Liquid
Color : Color less
Boiling Point : 384 °C
Sp. Gr. : 0.980- 0.985 (20 °C)
3. Paraffinic Oil Apar Oil
As per IS 15078
Sp. Gr : 0.88 -0.92
Kinematic viscosity : 18-23 @ 40 °C
Aniline point : 70-90 °C
2.2.4 Activators
Table 2.4 shows the dispersion aids, their source of supply and specification
Table 2.4 Activators
S.No Name of Activators Specification
1. Zinc Oxide
As per IS 3399
Relative Density : 5.58 – 5.68
Moisture content = 1 % max
Loss on ignition @ 850 °C = 1 % max
2. Stearic Acid
As per IS 1676
Moisture content :0.25 %
Ash content @ 550 °C = 0.1 %
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2.2.5 Vulcanizing Agents
Table 2.5 Vulcanizing Agents, source of supply and their specification
S.No Name of curatives / Accelerators Specification
1. Sulphur
Appearance : Yellow fine powder
Ash content : 0.05 %
Heat Loss : 0.5 %
Sp. Gr. : 2.05-2.15
Melting Pt. : 113- 119 °C
2. DCP – 40
Sp. Gr : 1.60 +/- 0.1
40 % peroxide content
3. MBTS
As per IS 8483
Assay : :97 %
M.Pt : 165 °C
2.2.6 Antidegradants
The following antidegradants, listed in Table 2.6 with its specification and these
have been used for mixing as per formulation in the current research work. These
improve heat and oxidation resistance of rubber composite
Table 2.6 Antidegradants
S.No Name of Antidegradants Specification
1. TDQ
(2, 2, 4-trimethyl-1, 2-
dihydroquinoline)
Make: NOCIL
Density -1.110
Ash Content -0.3% max
Softening Point -88-95 0C
2. 6 PPD
N(1.3-dimethyl-butyl)-N'-
phenyl-P-phenylenediamine
Make: NOCIL
Ash Content – 0.08%
Solidifying point ≥ °C – 45.5
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2.3. Vulcanization of Rubbers:
Vulcanization, the process of crosslinking of elastomers, occurs by a chemical
process initiated through some form of energy input. It occurs between two statistically
favorable reactive sites. Such sites are available through double bonds in diene-
containing elastomers, double bonds pendant to the polymer backbone from cure-site
monomers (EPDM, etc.) chemically induced reactive sites left by the abstraction of
backbone hydrogen or halogen atoms. The sites are coupled to each other by covalent
bonding via one or more of the following mechanisms [2]
Carbon-carbon bonds through the backbone.
Insertion of difunctional curatives such as sulfur between reactive sites.
Insertion of di- and multifunctional monomers such as acrylates, phenolics, or
triazines between reactive sites.
In practical vulcanization, the most widely used group of elastomers consists of
those containing a diene site for crosslinking, i.e.; Natural rubber (NR) and Polyisoprene
(IR), Butadiene rubber (BR), Styrene-butadiene rubber (SBR), Isobutylene-isoprene
rubber (Butyl, IIR), and Nitrile-butadiene rubber (NBR) which are crosslinked by using
sulfur as a vulcanizing agent. The basic ingredients for a sulfur cure are:
Sulfur or sulfur donor (cross linker)
Organic accelerator(s)
Zinc oxide and fatty acid (activator)
Fatty Acids
Sulfur. The original and still the most widely used curative because of its versatility and
cost, sulfur exists in the elemental state as an eight-membered ring (S8) [1],. The sulfur
ring opening mechanism, as discussed by Coran[2], , involves either a free radical or an
ionic mechanism. The ionic mechanism is probably more logical, and can be rationalized
in terms of the generalized Lewis acid-base interactions discussed by Jensen which is
given in Table 2.5
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Organic Accelerator(s). These all contain nitrogen and can perform as electron donors or
acceptors as noted by Jensen (1). The mechanisms are discussed in detail by Coran (8)
and appear to proceed in the following steps:
a) The accelerator (Ac) reacts with sulfur (Sx) to give monomeric polysulfides of the
type Ac - (Sx) - Ac, where Ac, is the organic radical derived from the accelerator.
b) The polysulfides can interact with the rubber to give polymeric polysulfides of the
type rubber - (Sx ) - Ac.
c) The rubber polysulfides then react, either directly or through a reactive intermediate,
to give crosslinks or rubber polysulfides of the type rubber- (Sx )-rubber.
Zinc Oxide. This has been an important ingredient since the early days of rubber
compounding. Originally used as an extender to reduce cost, it was subsequently found to
have a reinforcing effect, and was later found to reduce vulcanization time. Organic
accelerators, which further reduce cure times, depend on zinc oxide to activate them. Zinc,
as a metal, is classified as a d-transition element. As such, it is capable of developing
relatively rare 5-coordinate complexes with fatty acid and organic accelerators. In the
crosslinking of chlorine-containing compounds, it readily abstracts chlorine. The zinc
oxide becomes zinc chloride, a very strong Lewis acid, and the reaction proceeds at an
auto catalytic rate. Zinc oxide also is a very effective heat stabilizer in peroxide-cured
elastomers. However, it serves no function in this crosslinking mechanism. The only
adverse reaction of Zinc oxide is in Epichlorohydrin elastomers (e.g., Herclor, Hydrin).
The formation of Zinc Chloride (strong Lewis acid) causes an acid-catalyzed backbone
cleavage. The subsequent effect is a polymer rearrangement that occurs by a Ketoenol
tautomerization mechanism.
Fatty acids. Chemically, these are aliphatic carboxylic acids. The highly polar carboxyl
group is very reactive through its ability to develop covalent and coordinate bonds and its
H-bonding activity. The aliphatic hydrocarbon chain component is equally nonpolar and
as such is highly soluble in nonpolar components. Zinc oxide and fatty acid constitute the
activator system, in which the zinc ion is made soluble by salt formation between the acid
and oxide (1). Fatty acids have long hydrocarbon chains with carbonyl oxygen that probably
coordinates with the zinc through ligand formation. The zinc complex thus formed is
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hydrophilic in the metal center and hydrophobic on the outside, the hydrophobic component
being very soluble in the hydrocarbon (diene) component of the elastomer.
2.4 Formulation for preparing nanocomposites:
2.4.1. NBR Nanocomposites
In this study, four types of nano fillers namely Nanographite, Nanosilica,
Nanoclay and Nano Titanium Dioxide were used. The dosage of nanofillers is kept such
that a significant level of interaction is absorbed.
Acrylonitrile–Butadiene rubber (NBR) / Expanded Graphite (EG) / Carbon black
(CB) micro- and nanocomposites were prepared by two different methods, and the
resulting mechanical and tribological properties were compared with those of NBR / CB
composites. Meanwhile, the effects of graphite dispersion and loading content, as well as
the applied load and sliding velocity on the tribological behavior of the above composites
under dry friction condition were also evaluated. The worn surfaces were analyzed by
scanning electron microscopy (SEM) to understand the wear mechanism. As expected,
the better the dispersion of graphite, the more is remarkable enhancement in tensile and
dynamic mechanical properties, and greater is the reduction in the coefficient of friction
(COF) and specific wear rate (Ws). It was found that a small amount of EG could
effectively decrease COF and Ws of NBR / CB composites because of the formation of
graphite lubricant films. The COF and Ws of NBR / CB / EG composites show a
decreasing trend with a rise in applied load and sliding velocity. NBR / CB / EG
nanocomposite always shows a stable wearing process with relatively low COF and Ws.
It is thought that well-dispersed graphite nano-sheets were beneficial to the formation of
a fine and durable lubricant film.[3]
Above all efforts made by various scientists have lead
us to investigate into the rubber nanocomposite and its synergetic effect on the final out
put that is end product application and evaluation of the same.
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2.4.1.1 NBR-Graphite Nanocomposites
NBR-Graphite Nanocomposites were prepared using the formulation given in
Table 2.7. The dosage of nano graphites were kept varied from 0, 3, 6 & 9 phr as shown
in the Table 2.7 and all other rubber chemical ingredients were kept constant.
Mixing of nanofillers in polymer were carried out in two stages. In the first stage,
the nanographite at different loading 3, 6 and 9 phr were mixed at ambient temperature
in highly viscous liquid Nitrile Rubber [20 phr] and made into a paste like material which
is known as BR-Nanographite master batch.
Table – 2.7 Formulation for preparation of NBR – Graphite-nanocomposites [ phr*]
Ingredients NBG-0 NBG-3 NBG-6 NBG-9
NBR 80 80 80 80
Liq. NBR 20 20 20 20
Sulphur 2 2 2 2
Zinc Oxide 4 4 4 4
Stearic Acid 1 1 1 1
Nanographite 0 3 6 9
MBTS accelerator 0.5 0.5 0.5 0.5
Antidegradants 2 2 2 2
Total Batch weight 109.5 112.5 115.5 118.5
*phr = Parts per hundred gram of rubber
In the second stage, the NBR-Nanographite master batch was blended with NBR
base polymer and then mixed with other rubber compounding chemicals, as per the
formulation given in Table 2.7 such as activators, curatives etc in a laboratory two roll mill.
During mixing sulphur was added in the polymer at initial stage as per conventional
mixing cycle followed by NBR. The rubber compound mixes were then passed several
times in two roll mill to get uniform NBR nanographite based rubber compound. The
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compounded rubber sheet was kept for maturation for 16 hrs and then taken for moulding
of various test specimens as per ASTM standard using hydraulic press at a temperature
150 C. The curing time was obtained from rheological studies carried out at 150 C
using Monsanto Rheometer.
2.4.1.2 NBR-TiO2 Nanocomposites
Mixing of nanofillers in NBR polymer was carried out in two stapes.
1st step:- In the first step, the nano-TiO2 at different loading 1, 3 and 5 phr were mixed
at ambient temperature in highly viscous liquid Nitrile Rubber [20 phr] and made into a
paste like material which is known as “NBR-Nano- TiO2 master batch”.
Table-2.8 Formulation for preparation of NBR – TiO2 nanocomposites [ in phr*]
Compounding Ingredients NBT-0 NBT-1 NBT-3 NBT-5
a. Master Batch
Liq. NBR 20 20 20 20
Nano- TiO2 0 1 3 5
b. Main Formulation
NBR Rubber [JSR 230] 80 80 80 80
Sulphur 2 2 2 2
Zinc Oxide 4 4 4 4
Stearic Acid 1 1 1 1
MBTS Accelerator 0.5 0.5 0.5 0.5
Anti-degradants 2 2 2 2
Total Batch weight 109.5 110.5 112.5 114.5
*phr = Parts per hundred gram of rubber
2nd
step:- In the second step, the raw NBR rubber is milled in two roll mill and then
NBR-Nano- TiO2 master batch was added to it to get uniform blending of liquid NBR
and NBR rubber. Then other rubber compounding chemicals, as per the formulation
given in Table 2.8 such as activators, curatives etc were added. During mixing sulphur
was added in the polymer at initial stage to ensure proper dispersion of sulphur in
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polymer matrix. Mixing was carried out in a controlled manner and same procedure was
followed for all the mixes. The mixing cycle time was kept constant for 25 min for all the
mixes. The polymer nanocomposite mixes were then passed several times in two roll mill
to get uniform NBR Nano - TiO2 based polymer nanocomposite.
2.4.1.3 NBR-Silica Nanocomposites
NBR- Silica Nanocomposites were prepared using the formulation given in Table 2.9.
The dosage of nanosilica were kept varied from 0, 1, 3 & 5 phr as shown in the Table 2.9
and all other rubber chemical ingredients were kept constant.
The formulation used for mixing NBR rubber and compounding ingredients is
tabulated in Table 2.9
Table-2.9 Formulation for preparation of NBR –Silica-nanocomposites [in phr*]
Compounding Ingredients NBS-0 NBS-1 NBS-3 NBS-5
a. Master Batch
Liq. NBR 20 20 20 20
Nano-silica 0 1 3 5
b. Main Formulation
NBR Rubber [JSR 230] 80 80 80 80
Sulphur 2 2 2 2
Zinc Oxide 4 4 4 4
Stearic Acid 1 1 1 1
MBTS Accelerator 0.5 0.5 0.5 0.5
Anti-degradants 2 2 2 2
Total Batch weight 109.5 110.5 112.5 114.5
*phr = Parts per hundred gram of rubber
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Mixing of nanofillers in NBR polymer was carried out in two steps.
1st step:- In the first step, the nano-silica at different loading 1, 3 and 5 phr were mixed
at ambient temperature in highly viscous liquid Nitrile Rubber [20 phr] and made into a
paste like material which is known as “NBR-Nano-silica master batch”.
2nd
step: - In the second step, the raw NBR rubber is milled in two roll mill and then
NBR-Nano-Silica master batch” was added to it to get uniform blending of liquid NBR
and NBR rubber. Then other rubber compounding chemicals, as per the formulation
given in Table 2.9 such as activators, curatives etc were added. During mixing sulphur
was added in the polymer at initial stage to ensure proper dispersion of sulphur in
polymer matrix. Mixing was carried out in a controlled manner and same procedure was
followed for all the mixes. The mixing cycle time was kept constant at 25 min for all the
mixes. The polymer nanocomposite mixes were then passed several times in two roll mill
to get uniform NBR Nano-silica based polymer nanocomposite.
2.4.1.4 NBR-Clay Nanocomposites
NBR-Clay Nanocomposites were prepared using the formulation given in Table
2.10 The dosage of nanoclay were kept varied from 0, 1, 3, 5 & 7 phr as shown in Table
2.10 and all other rubber chemical ingredients were kept constant.
Table-2.10 Formulation for preparation of NBR – Clay-nanocomposites [in phr*]
Compounding Ingredients* NC 0 NC1 NC 3 NC 5 NC 7
NBR-JSR 230 100 100 100 100 100
Sulphur 2 2 2 2 2
Zinc oxide 4 4 4 4 4
Stearic acid 1 1 1 1 1
Nano Clay 0 1 3 5 7
DOP 10 10 10 10 10
TDQ 1 1 1 1 1
6PPD 1 1 1 1 1
MBTS 0.5 0.5 0.5 0.5 0.5
Total Weight 119.5 120.5 122.5 124.5 126.5
*phr = Parts per hundred gram of rubber
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The compounds were mixed in a laboratory size (225 x 100 mm) mixing mill at a
friction ratio of 1 : 1.25 according to ASTM D 3182 standards while carefully controlling the
temperature, nip gap, mixing time, and uniform cutting operation. The temperature range for
mixing was maintained at 80 °C by carefully circulating water. After mixing, the elastomer
compositions were molded in an electrically heated hydraulic press to optimum cure (90% of
the maximum cure) using molding conditions determined by a Monsanto Rheometer.
2.4.2 HNBR Nanocomposites
In this study, two types of nano fillers namely Nanosilica and Nanoclay were used.
2.4.2.1 HNBR-Clay Nanocomposites
HNBR-Clay Nanocomposite was prepared using the formulation given in Table 2.11.
The dosage of nanoclay were kept varied from 0, 3, 5 & 7 phr as shown in the Table 2.11
and all other rubber chemical ingredients were kept constant.
Conventional Mixing:
Table 2.11 Formulations for preparation of HNBR clay nanocomposite
Compounding Ingredients HNC 0 HNC 3 HNC 5 HNC 7
HNBR- Therban®3907 100 100 100 100
Dioctyl phthalate oil 20 20 20 20
MMT - Nano clay 0 3 5 7
Dicumyl Peroxide – 40 6 6 6 6
Total Batch Weight 126 129 131 133
The compound was prepared as per the compounding formulation given in
Table-2.11. Polymer nano compounds were prepared by mixing HNBR and other
compounding chemicals using a open two roll mixing mill operated at room temperature
and the speed ratio of the two rolls were maintained at 1:1.2. Mixing was completed
within 20 minutes and maintained similar mixing conditions for all compounds.
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Mixing with dispersed nanoclay
Table 2.12: Formulation for preparation of HNBR-clay nanocomposite using DOP as
dispersion oil
Compounding Ingredients Control DNC 3 DNC 5 DNC 7
Dispersion of MMT Nano Clay in DOP oil
Dioctyl phthalate oil 20 20 20 20
MMT - Nano clay 0 3 5 7
Mixing of Dispersion in Main polymer matrix
HNBR- Therban®3907, 100 100 100 100
Dicumyl peroxide – 40 6 6 6 6
2.4.2.2 HNBR-Silica Nanocomposites :
NBR- Silica Nanocomposites were prepared using the formulation given in Table
2.13 The dosage of nanosilica were kept varied from 0, 1, 3 & 5 phr as shown in the Table
2.13 and all other rubber chemical ingredients were kept constant.
Table 2.13 Formulation for preparation of HNBR – Nano Silica Nanocomposites [phr*]
Compounding Ingredients H 0 HNS 1 HNS 3 HNS 5
HNBR Rubber 100 100 100 100
Zinc Oxide 3 3 3 3
Stearic acid 1 1 1 1
TAC 1 1 1 1
Nano silica 0 1 3 5
DCP 40 3.5 3.5 3.5 3.5
Total Batch Weight 178.5 179.5 181.5 183.5
2.4.3 EPDM Nanocomposites
Ethylene-propylene rubbers are valuable for their excellent resistance to heat,
oxidation, ozone and weather ageing due to their stable, saturated polymer backbone
structure. As non-polar elastomers, they have good electrical resistivity, as well as resistance
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to polar solvents, such as water, acids, alkalies, phosphate esters and many ketones and
alcohols. Amorphous or low crystalline grades have excellent low temperature flexibility
with glass transition points of about minus 60°C. Heat ageing resistance up to 130°C can
be obtained with properly selected sulfur acceleration system and heat resistance up to
160°C can be obtained with peroxide cured compounds. Compression set resistance is
good, particularly at high temperatures, if sulfur donor or peroxide cure systems are used.
These polymers respond well to high filler and plasticizer loading, providing economical
compounds. They can develop high tensile and tear properties, excellent abrasion
resistance, as well as improved oil swell resistance and flame retardance. An attempt was
made to use nanofillers in EPDM matrix to improve the heat resistance, electrical
resistance properties.
In this study, two types of nano fillers namely Nanosilica and Nanoclay were used
and the nanocomposites were prepared and characterized [3-4]
2.4.3.1 EPDM-Silica Nanocomposites
EPDM – Silica Nanocomposites were prepared using the formulation given in
Table 2.14 The dosage of nanoclay were varied from 0, 1, 3, 5 & 7 phr as shown in the
Table 2.14 and all other rubber chemical ingredients were kept constant.
Table 2.14 Formulation for preparation of EPDM – Silica Nanocomposites
Compounding Ingredients E 0 ENS 1 ENS 3 ENS 5
EPDM-Keltan 512 100 100 100 100
Zinc Oxide 5 5 5 5
Paraffinic oil 5 5 5 5
Nano silica 0 1 3 5
DCP 40 4 4 4 4
Total Batch Weight 114 115 117 119
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2.4.2 EPDM-Clay Nanocomposites
EPDM –Clay Nanocomposites were prepared using the formulation given in
Table 2.15 The dosage of nanoclay were kept varied from 0, 1, 3, 5 & 7 phr as shown in
the Table 2.15 and all other rubber chemical ingredients were kept constant.
Table 2.15 Formulation for preparation of EPDM – clay Nanocomposites
Compounding Ingredients EN 0 ENC 3 ENC 5 ENC 7
EPDM- Keltan 512 100 100 100 100
Zinc Oxide 5 5 5 5
Paraffinic oil 5 5 5 5
Nano clay 0 3 5 7
Di- cumyl peroxide - 40 4 4 4 4
Total Batch Weight 114 117 119 121
2.5. Mixing and homogenization on a mixing mill
Mixing is the process of making a thorough and uniform dispersion of various
ingredients in polymer matrix by shearing it in between two parallel rollers rotating
inwards. Mixing was carried out on a laboratory two roll mixing mill (size 6” x 12”) as
per ASTM D 3182–89. The mixing was carried out at a friction ratio of 1:1.25. The mill
opening was set at 0.2 mm and the elastomer was passed through the rolls twice without
banding. This was then banded on the slow roll with mill opening at 1.4 mm and was
increased to 1.9 mm as the band became smooth. The temperature of the rolls was
maintained at 70±5 °C. The compounding ingredients were added as per procedure given
in ASTM D 3182–89 in the following order: activator, filler, accelerator and curing
agents. Before the addition of accelerator and sulphur, the batch was thoroughly cooled
to avoid any scorching of rubber compound. After mixing all the ingredients,
homogenization of the compound was carried out by passing the rolled stock end wise six
times at a mill opening of 0.8 mm. The mill was opened to give a minimum stock
thickness of 6 mm and the stock was passed through the rolls four times folding it back
on itself each time.
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2.6. Cure characteristics
Cure characteristics of the mixes were determined as per ASTM D 2084–1995
using Rubber Process Analyzer (RPA 2000–Alpha technologies, Fig 2.1, It uses two
directly heated, opposed biconical dies that are designed to achieve a constant shear
gradient over the entire sample chamber. The sample of approximately 5 g was placed in
the lower die that is oscillated through a small deformation angle (0-2º) at a frequency of
50 cpm. The torque transducer on the upper die senses the forces being transmitted
through the rubber. The torque is plotted as a function of time and the curve is called a
cure graph. The important data that could be taken from the torque-time curve are
minimum torque ML(T90) ,maximum torque. (MH), scorch time (T10), and optimum
cure time.
Fig 2.1. Monsanto R-100 ODR
Rubber Process Analyzer
The rubber compound mixes were then passed several times in two roll mill to get
uniform NBR nanosilica based rubber compound. The curing time was obtained from
rheological studies carried out using RPA-2000.
Fig 2.2 RPA-2000
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2.7. Moulding
Moulding is a process of curing the compound by means of heat and pressure.
It includes many different methods like compression moulding, injection and transfer
moulding. Here we are mainly dealing with compression moulding technique because the
flow properties of rubber are very poor and it does not fill the mould cavities by using
other moulding techniques.8” X 8” X 2mm and 6” X 6” X 2mm sheets are compression
moulded using a 14” X 14” twin double daylight hydraulic Compression set buttons are
also compression moulded in the same press. Curing is done at 150 °C for NBR rubber
and 160 °C for EPDM and HNBR rubbers for a particular time which is obtained from
Rheological study.
2.6. Vulcanized samples
The compounded rubber sheet was kept for maturation for 16 hrs and then taken
for moulding of various test specimens as per ASTM standard using hydraulic press at a
temperature 150 C or 160 C as per the rheological data.
Time between vulcanization and testing:
For all test purposes, the minimum time between vulcanization and testing was
kept 16 hrs.
2.8. Mechanical properties
The thickness of the dumbbell was measured at the centre and at each end of the
test length with the help of thickness gauge. The median value of the three measurements
was taken to calculate the area of the cross-section. The width of the test piece was 4 mm
which was taken as the distance between the cutting edges of the die in the narrow part.
Tensile tests were carried out according to ASTM D412-98 on dumb-bell shaped
specimens using a universal tensile machine, Zwick 1445. Dumb-bell test pieces shall
have the outline shown in Fig.2.3. Measure the thickness at the centre and at each end of
the test length with the thickness gauge. The median value of the three measurements
shall be used in calculating the area of the cross-section. The nominal rate of traverse of
the moving grip was kept 500 mm/min.
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Fig 2.3 dumb-bell shaped specimens as per ASTM D 412
These tests were carried out using dumbbell specimens. The measurements were
carried out at a cross head speed of 500 mm/min on a Zwick tensile test in accordance
with ASTM D 412.
Fig 2.4 Tensile testing machine
2.9. Hardness:
The testing was done as per ASTM D 2240–1997 using Shore A type Durometer.
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Fig 2.5 Shore A type Durometer
Hardness of the samples were measured by a Durometer (Shore A type, ASTM D
2240) using the test button of 12 mm thickness. To get repeatable results, the hardness
tester was held in position with the centre of the indentor at least 12 mm from the edges
of the test piece and the pressure foot is applied to the test piece as rapidly as possible,
without shock, keeping the foot parallel to the surface of the test piece and ensuring that
the indenter is normal to the rubber surface. The reading was taken within 1 s after the
pressure foot is in firm contact with the test piece.
2.10 Ageing studies
All rubbers are subjected to deterioration at high temperature. Volume change and
Compression set are both influenced by heat. Hardness is influenced in a complex way.
The first effect of high temperature is to soften the compound. This is a physical change,
and will reverse when the temperature drops. In high pressure application the product
may begin to flow through the clearance gap as the temperature rises due to this softening
effect. With increasing time at high temperature, chemical changes occur. These
generally cause an increase in hardness, along with volume and compression set changes.
Changes in tensile strength and elongation are also involved. Being chemical in nature,
these changes are not reversible. The changes induced by low temperature are primarily
physical and reversible. An elastomer will almost completely regain its original
properties when warmed.
Effect of nanofillers on the properties of accelerated ageing and heat resistance of
polymer nanocomposites were performed to estimate the relative resistance of polymer
nanocomposites [having no and different doses of nanofillers] to deterioration with the
passage of time. For this purpose, the polymer nanocomposites were subjected to
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controlled deteriorating influences for definite periods, after which appropriate properties
are measured and compared with the corresponding properties of the unaged polymer
nanocomposites. In accelerated ageing, the polymer nanocomposites is subjected to a test
environment intended to produce the effect of natural ageing in a shorter time. In case of
heat resistance tests, the polymer nanocomposites is subjected to prolonged period at the
same temperature as that in service.
2.11 Tear Strength
The tear specimen was clamped on the testing machine, taking care that the bite
of the jaws shall be at the centre of the tab ends and in line with the direction of load
application. Apply the load with a lower jaw speed of 500 mm per minute. After rupture
of the specimen, the breaking load was printed and recorded together with the average
thickness of the specimen.
Calculation - Tear strength is calculated by dividing the load in kg by thickness in
centimeter of the test specimen and is expressed as kg/cm thickness.
F
Tear Strength = ---------
D
Fig 2.6 Tear strength specimen
Where, F is the maximum force, in newtons, and the median force, in Newton
recorded in tensile machine. D is the median thickness, in millimeters, of the test piece.
Determine the median and the range of the values for each direction of testing.
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2.12. Thermal Degradation Studies
Thermo gravimetric analysis was done using Perkin Elmer Instrument, Diamond
TG-DTA, (Waltham, MA, USA) (Fig.2.7). The samples (3-5 mg) were heated from
ambient temperature to 800 °C in the furnace of the instrument under oxygen atmosphere
at 100 ml/min and at a heating rate of 20 °C/min and the data of weight loss Vs
temperature were recorded. Although the experiments were recorded in nitrogen as well
as in air, there was major difference amongst the samples when oxygen was used as the
medium. The analysis of the thermo gravimetric (TG) and derivative thermo gravimetric
curves (DTG) was done in oxygen and the onset temperature, weight loss at major
degradation steps and temperature corresponding to the maximum value in the derivative
thermogram were recorded. The temperature at which maximum degradation took place
is denoted as Tmax and onset temperature of degradation is denoted as Ti. The error in the
measurement was ± 1 °C.
Fig. 2.7 TGA, Perkin Elmer Instrument
Thermal decomposition is a chemical process in which solid material generates
volatile fragments which can burn above the solid material. Polymer can break down
thermally by oxidative process or by the action of heat. In the presence of oxidants, the
decomposition process is accelerated. There are several ways in which polymers decompose:
random-chain scission, end-chain scission, chain stripping and cross-linking. The most
common types of degradation occur through chemical reactions at the molecular level.
The thermal degradation kinetics in polymers are more complicated than in inorganic
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Rajkumar. K 64
materials due to the nature of polydispersity of polymer chains. Upon thermal excitation,
the covalent bonds in polymer chains undergo complex vibration and rotation motions
within their local space. With further excitation these bonds can break to form a variety
of fragment radicals or small molecules, which may further mutually recombine or break.
Ultimately, the resulting fragments may be vaporized, diffused out, or carbonized. The
thermal behavior of materials can be improved if the information about the thermal
degradation kinetics and degradation mechanisms can be employed to decrease the
thermal degradation rate or increase the heat resistance. Thermogravimetric analysis
(TGA) is an excellent tool for studying the kinetics of thermal degradation.
It provides information on frequency factor, activation energy, and overall reaction order.
However, it does not provide clear information on thermal degradation mechanisms.
Polymer chains undergo degradation (depolymerization) through a variety of mechanisms
including shear action, chemical attack, and nuclear, ultraviolet, and ultrasonic irradiation.
2.13 Energy-dispersive X-ray spectroscopy
EDS makes use of the X-ray spectrum emitted by a solid sample bombarded with
a focused beam of electrons to obtain a localized chemical analysis. All elements from
atomic number 4 (Be) to 92 (U) can be detected in principle, though not all instruments
are equipped for 'light'
Fig 2.8 Energy-dispersive X-ray spectroscopy
elements (Z < 10). Qualitative analysis involves the identification of the lines in the
spectrum and is fairly straightforward owing to the simplicity of X-ray spectra.
Quantitative analysis (determination of the concentrations of the elements present) entails
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measuring line intensities for each element in the sample and for the same elements in
calibration Standards of known composition
2.14 Fourier Transforms Infra-Red spectroscopy
FT-IR spectra of thin films were recorded using a Fourier Transform Infrared
Spectrophotometer (Nicolet, Model 410, USA) using ATR technique (Fig.2.9).
All the clays show a sharp band around 3627 cm-1
, resulting from the O-H
stretching, vibration of the silicate and a broad band between 3550-3100 cm-1
,
characteristic of the stretching and deformation vibrations of the interlayer water. Infrared
signal of adsorbed H2O is visible also around 1635 cm-1
(bending vibrations).
Fig 2.9 Fourier transforms infra-red spectroscopy/ATR
Additionally, the absorption pick at about 1040 cm-1
is ascribed to Si-O-Si
stretching vibrations of clays. The other two absorption bands are around 520 cm-1
and
465 cm-1
derived from Al-O stretching and Si-O bending vibrations of silicate. The
organo-montmorillonites display some bands which are not exhibited by the pristine clay.
These bands appear at 2920, 2850 and 1468 cm-1
and are attributed to the C–H vibrations
of the methylene groups (asymmetric stretching, symmetric stretching and bending,
respectively) from chemical structure of the organo-modifiers.
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2.15 X-ray diffraction studies
Small angle X-ray diffraction (XRD) study of the Nanocomposites were
performed at room temperature using a Philips PW 1710 diffractometer in the angular
range of 0˚ to 10˚ 2θ (SAXD). The target was copper and the (Cu Kα) radiation
(λ= 1.540598˚A) was obtained on applying 50 KV voltage to the generator and the
current was 40 mA. The basal spacing of nano graphite layers was estimated from the
position of the plane peak in the SAXD intensity profile. Specimens for X-ray diffraction
were taken from compression-molded sheets of 2 mm thickness.
Fig 2.10 X-ray diffraction
2.16 Electrical properties
The electrical behavior of rubber products used in particular applications is
important for a variety of reasons such as safety, static changes, current transmission, etc.
This test method is useful in predicting the behavior of such rubber products.
2.17 Barrier Properties
Several studies demonstrated that nanofillers highly improve barrier properties of
nanocomposite films. This behaviour is due to creating a „tortuous path‟. Air as
illustrated in the fig. that retards the progress of the gas molecules through the matrix. Air
permeability studies were conducted with circular specimens (diameter 9 cm, IS: 3400
part 21-1980) (Fig 2.12).
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Fig 2.11 Air Permeability Tester
The cavity of a test cell, maintained at a constant temperature, is divided by a disc
test piece into a high pressure and a low (atmospheric) pressure side. The high pressure
side is connected to a constant pressure gas reservoir or is of such volume that once filled,
it stays at practically constant pressure. The gas permeates into the low pressure side,
which is of a very low volume and connected to a capillary tube; this is provided for
measuring the permeated volume, while keeping or restoring the same low pressure within
this side. Absolute pressure for the high pressure side is maintained in the range of 0.3 to 1.5
MPa* and for low pressure side it is maintained at the prevailing atmospheric pressure.
For normal comparison of permeability of different rubber vulcanizates, the test
temperature is a standard laboratory temperature ( 27 + 1 oC) , but higher preferred
temperature may be used where conditions are required to approximate to the service
temperature of rubber products. When higher preferred temperatures are used, the
capillary tube shall be brought to the test temperature and maintained at that temperature
throughout the test.
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2.18 Transmission Electron Microscopy (TEM)
The samples for TEM analysis were prepared by ultracryomicrotomy with a Leica
Ultracut UCT (Leica Microsystems GmbH, Vienna, Austria). Freshly sharpened glass
knives with cutting edges of 45° were used to obtain cryosections of about 100 nm
thicknesse at -90 °C. The cryosections were collected individually in sucrose solution and
directly supported on a copper grid of 300 mesh size. Microscopy was performed with
JEOL 2100, Japan (Fig. 2.13). Transmission electron microscope was operated at an
accelerating voltage of 200 KV.
Fig 2.12 Transmission Electron Microscopy
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2.19 References:
1. Richard Karpeles and Anthony V. Grossi, “EPDM Rubber Technology”, Handbook of
Elastomers, 2nd
Ed., Anil K. Bhowmick and Howard L. Stephens [Editors], pp. 845-876,
Marcel Decker, Inc., New York (2001).
2. Lei Wang, Li Qun Zhang, Ming Tian, Materials and Design 39 450–457 (2012).
3. Gary Ver Strate, “Ethylene Propylene Elastomers”, Encyclopedia of Polymer Science &
Engineering, vol. 6, pp. 522-564 (1986).
4. John A. Riedel and Robert Vander Laan, “Ethylene Propylene Rubbers”, The Vanderbilt
Rubber Handbook, 13th
Ed., pp. 123-148, R.T. Vanderbilt Co., Inc., Norwalk, CT (1990).