1
Classes of Polymeric Materials
Elastomers
Professor Joe Greene
CSU, CHICO
2
Elastomers
• Elastomers are rubber like polymers that are
thermoset or thermoplastic
– butyl rubber: natural rubber
– thermoset: polyurethane, silicone
– thermoplastic: thermoplastic urethanes (TPU),
thermoplastic elastomers (TPE), thermoplastic olefins
(TPO), thermoplastic rubbers (TPR)
• Elastomers exhibit more elastic properties versus
plastics which plastically deform and have a lower
elastic limit.
• Rubbers have the distinction of being stretched
200% and returned to original shape. Elastic limit is
3
Rubbers
• Rubbers have the distinction of being stretched 200%
and returned to original shape. Elastic limit is 200%
• Natural rubber (isoprene) is produced from gum resin
of certain trees and plants that grow in southeast Asia,
Ceylon, Liberia, and the Congo.
– The sap is an emulsion containing 40% water & 60% rubber particles
• Vulcanization occurs with the addition of sulfur (4%).
– Sulfur produces cross-links to make the rubber stiffer and harder.
– The cross-linkages reduce the slippage between chains and results in
higher elasticity.
– Some of the double covalent bonds between molecules are broken,
allowing the sulfur atoms to form cross-links.
– Soft rubber has 4% sulfur and is 10% cross-linked.
– Hard rubber (ebonite) has 45% sulfur and is highly cross-linked.
4
Rubber Additives and Modifiers
• Fillers can comprise half of the volume of the rubber
– Silica and carbon black.
– Reduce cost of material.
– Increase tensile strength and modulus.
– Improve abrasion resistance.
– Improve tear resistance.
– Improve resistance to light and weathering.
– Example,
• Tires produced from Latex contains 30% carbon black which improves the
body and abrasion resistance in tires.
• Additives
– Antioxidants, antiozonants, oil extenders to reduce cost
and soften rubber, fillers, reinforcement
5
Vulcanizable Elastomeric Compounds
• Rubbers are compounded into practical elastomers
– The rubber (elastomer) is the major component and other
components are given as weight per hundred weight rubber (phr)
• Sulfur is added in less than 10 phr
• Accelerators and activators with the sulfur
– hexamethylene tetramine (HMTA)
– zinc oxide as activators
• Protective agents are used to suppress the effects of oxygen and
ozone
– phenyl betabaphthylamine and alkyl paraphenylene diamine (APPD)
• Reinforcing filler
– carbon black
– silica when light colors are required
– calcium carbonate, clay, kaoilin
• Processing aids which reduce stiffness and cost
– Plasticizers, lubricants, mineral oils, paraffin waxes,
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Vulcanizable Rubber
• Typical tire tread
– Natural rubber smoked sheet (100),
– sulfur (2.5) sulfenamide (0.5), MBTS (0.1), strearic acid (3), zinc
oxide (3), PNBA (2), HAF carbon black (45), and mineral oil (3)
• Typical shoe sole compound
– SBR (styrene-butadiene-rubber) (100) and clay (90)
• Typical electrical cable cover
– polychloroprene (100), kaolin (120), FEF carbon black (15) and
mineral oil (12), vulcanization agent
7
Synthetic Rubber• Reactive system elastomers
– Low molecular weight monomers are reacted in a polymerization
step with very little cross-linking.
– Reaction is triggered by heat, catalyst, and mixing
• Urethanes processed with Reaction Injection Molding (RIM)
• Silicones processed with injection molding or extrusion
• Thermoplastic Elastomers
– Processing involves melting of polymers, not thermoset reaction
– Processed by injection molding, extrusion, blow molding, film
blowing, or rotational molding.
• Injection molded soles for footwear
– Advantages of thermoplastic elastomers
• Less expensive due to fast cycle times
• More complex designs are possible
• Wider range of properties due to copolymerization
– Disadvantage of thermoplastic elastomers
• Higher creep
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Thermoplastic Elastomers
• Four types of elastomers
– Olefinics and Styrenics
– Polyurethanes and Polyesters
• Olefinics (TPOs are used for bumper covers on cars)
– Produced by
• Blending copolymers of ethylene and propylene (EPR) or ter polymer of
ethylene-propylene diene (EPDM) with
• PP in ratios that determine the stiffness of the elastomer
– A 80/20 EPDM/PP ratio gives a soft elastomer (TPO)
• Styrenic thermoplastic elastomers (STPE)
– Long triblock copolymer molecules with
• an elastomeric central block (butadiene, isoprene, ethylene-butene, etc.) and
• end blocks (styrene, etc.) which form hard segments
– Other elastomers have varying amounts of soft and hard blocks
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Thermoplastic Elastomers
• Polyurethanes
– Have a hard block segment and soft block segment
• Soft block corresponds to polyol involved in polymerization in ether based
• Hard blocks involve the isocyanates and chain extenders
• Polyesters are etheresters or copolyester thermoplastic
elastomer
– Soft blocks contain ether groups are amorpous and flexible
– Hard blocks can consist of polybutylene terephthalate (PBT)
• Polyertheramide or polyetherblockamide elastomer
– Hard blocks consits of a crystallizing polyamide
Soft Hard
Hard
Hard
Soft Soft
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Commercial Elastomers
• Diene C=C double bonds and Related Elastomers
– Polyisoprene- (C5H8)20,000
• Basic structure of natural rubber
• Can be produced as a synthetic polymer
• Capable of very slow crystallization
• Tm = 28°C, Tg = -70°C for cis polyisoprene
• Tm = 68°C, Tg = -70°C for trans polyisoprene
– Trans is major component of gutta percha, the first plastic
– Natural rubber was first crosslinked into highly elastic network by
Charles Goodyear (vulcanization with sulfur in 1837)
• Sulfur crosslinked with the unsaturations C=C
– Natural rubber in unfilled form is widely used for products with
• very large elastic deformations or very high resilience,
• resistance to cold flow (low compression set) and
• resistance to abrasion, wear, and fatigue.
– Natural rubber does not have good intrinsic resistance to sunlight,
oxygen, ozone, heat aging, oils, or fuels.
C
H
C
C
H
H3HH
H
C C ][
C
H
C
H
HH
H
C C ][
CH3
Cis
Trans
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Commercial Elastomers
• Polybutadiene
– Basis for synthetic rubber as a major component in copolymers
Styrene-Butadiene Rubber (SBR, NBR) or in
– Blends with other rubbers (NR, SBR)
– Can improve low-temperature properties, resilence, and abrasion
or wear resistance
• Tg = -50°C
• Polychloroprene
– Polychloroprene or neoprene was the very first synthetic rubber
– Due to polar nature of molecule from Cl atom it has very good
resistance to oils and is flame resistant (Cl gas coats surface)
– Used for fuel lines, hoses, gaskets, cable covers, protective boots,
bridge pads, roofing materials, fabric coatings, and adhesives
– Tg = -65°C.
H H
C
H
C
H HH
C C ][
H H
C
H
C
Cl HH
C C ][
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Commercial Elastomers
• Butyl rubber- addition polymer of isobutylene.
– Copolymer with a few isoprene units, Tg =-65°C
– Contains only a few percent double bonds from isoprene
– Small extent of saturation are used for vulcanization
– Good regularity of the polymer chain makes it possible for the
elastomer to crystallize on stretching
– Soft polymer is usually compounded with carbon black to increase
modulus
• Nitrile rubber
– Copolymer of butadiene and acrylonitrile
– Solvent resistant rubber due to nitrile C:::N
– Irregular chain structure will not crystallize on stretching, like
SBR
– vulcanization is achieved with sulfur like SBR and natural rubber
• Thiokol- ethylene dichloride polymerized with sodium
H H3
C
CH3H
C
C
][
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Thermoplastic Elastomers
• Thermoplastic Elastomers result from copolymerization of
two or more monomers.
– One monomer is used to provide the hard, crystalline features, whereas
the other monomer produces the soft, amorphous features.
– Combined these form a thermoplastic material that exhibits properties
similar to the hard, vulcanized elastomers.
• Thermoplastic Urethanes (TPU)
– The first Thermoplastic Elastomer (TPE) used for seals gaskets,
etc.
• Other TPEs
– Copolyester for hydraulic hoses, couplings, and cable insulation.
– Styrene copolymers are less expensive than TPU with lower strength
– Styrene-butadiene (SBR) for medical products, tubing, packaging, etc.
– Olefins (TPO) for tubing, seals, gaskets, electrical, and automotive.
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Thermoplastic Elastomers
• Styrene-butadiene rubber (SBR)
– Developed during WWII
• Germany under the name of BUNA-S.
• North America as GR-S,Government rubber-styrene.
– Random copolymer of butadiene (67-85%) and styrene (15-33%)
– Tg of typical 75/25 blend is –60°C
– Not capable of crystallizing under strain and thus requires
reinforcing filler, carbon black, to get good properties.
– One of the least expensive rubbers and generally processes easily.
– Inferior to natural rubber in mechanical properties
– Superior to natural rubber in wear, heat aging, ozone resistance,
and resistance to oils.
– Applications include tires, footwear, wire, cable insulation,
industrial rubber products, adhesives, paints (latex or emulsion)
• More than half of the world’s synthetic rubber is SBR
• World usage of SBR equals natural rubber
C C
H
H H
n
H H
C
H
C
H HH
C C ][
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Acrylonitrile-butadiene rubber (NBR)
• Also called Nitrile rubber
– Developed as an oil resistant rubber due to
• the polar C:::N polar bond. Resistant to oils, fuels, and solvents.
– Copolymer of acrylonitrile (20-50%) and butadiene(80-50%)
– Moderate cost and a general purpose rubber.
– Excellent properties for heat aging and abrasion resistance
– Poor properties for ozone and weathering resistance.
– Has high dielectric losses and limited low temperature flexibility
– Applications include fuel and oil tubing; hose, gaskets, and seals; conveyer
belts, print rolls, and pads.
– Carboxylated nitrile rubbers (COX-NBR) has carboxyl side groups
(COOH)which improve
• Abrasion and wear resistance; ozone resistance; and low temperature flexibility
– NBR and PVC for miscible, but distinct polymer blend or polyalloy
• 30% addition of PVC improves ozone and fire resistance
H H
C
H
C
H HH
C C ][C C
H C:::N
H H
n
m
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Ethylene-propylene rubber (EPR)
• EPR and EPDM
– Form a noncrystallizing copolymer
• with a low Tg.
– The % PP and PE units determines properties
• Tg = -60°C for PE/PP of 67/33 to 50/50
– Unsaturated polymer since PP and PE are saturated
• Resistant to ozone, weathering, and heat aging
• Does not allow for conventional vulcanization
– Terpolymer with addition of small amount of third monomer (Diene D) has
unsaturations referred to as EPDM
• 1,4, hexadiene (HD); 5-ethylidene-2-norbornene (ENB); diclopentadiene (DCPB)
feature unsaturations in a side (pendant) group
• Feature excellent ozone and weathering resistance and good heat aging
– Limitations include poor resistance to oils and fuels, poor adhesion to many
substrates and reinforcements
– Applications include exterior automotive parts (TPO is PP/EPDM), construction
parts, weather strips, wire and cable insulation, hose and belt products, coated
fabrics.
C C
H H
H H
n
C C
H CH3
H H
m
C C
H CH2
H H
mCH
CH
CH3
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Ethylene Related Elastomers
• Chlorosulfonated Polyethylene (CSPE)
– Moderate random chlorination of PE (24-43%)
– Infrequent chlorosulfonic groups (SO2Cl)
– Sulfur content is 1-1.5%.
– CSPE is noted for excellent weathering resistance
• Good resistance to ozones, heat, chemicals, solvents.
• Good electrical properties, low gas permeability, good adhesion to substrates
– Applications include hose products, roll covers, tank linings, wire and cable
covers, footwear, and building products
• Chlorinated Polyethylene (CPE)
– Moderate random chlorination
• Suppresses crystallinity (rubber)
• Can be crosslinked with peroxides
• Cl range is 36-42% versus 56.8% for PVC
– Properties include good heat, oil, and ozone resistance
– Used as plasticizer for PVC
C C
H H
H H
n
C
Cl
H
m
C
S
H
k
Cl
O O
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Ethylene Related Elastomers
• Ethylene-vinylacetate Copolymer (EVA)
– Random copolymer of E and VA
• Amorphous and thus elastomeric
• VA range is 40-60%
• Can be crosslinked through organic peroxides
– Properties include
• Good heat, ozone, and weather resistance
• Ethylene-acrylate copolymer (EAR)
– Copolymer of Ethylene and methacrylate
• Contains carboxylic side groups (COOH)
– Properties include
• Excellent resistance to ozone and
• Excellent energy absorbers
– Better than butyl rubbers
C C
H H
H H
n
C C
H O
H H
O=CCH3
m
C C
H H
H H
n
C C
H C
H H
O
OCH3
m
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FluoroElastomers
• Polyvinylidene fluoride (PVDF)
– Tg = -35°C
• Poly chloro tri fluoro ethylene (PCTFE)
– Tg = 40°C
• Poly hexa fluoro propylene (PHFP)
– Tg = 11°C
• Poly tetra fluoro ethylene (PTFE)
– Tg = - 130°C
• Fluoroelastomers are produced by
– random copolymerization that
– suppresses the crystallinity and
– provides a mechanism for cross linking by terpolymerization
• Monomers include VDF, CTFE, HFP, and TFE
C C
H F
H F
n C C
F Cl
F F
n
C C
F CF3
F F
n
C C
F F
F F
n
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FluoroElastomers
• Fluoroelastomers are expensive but have outstanding
properties
– Exceptional resistance to chemicals, especially oils, solvents
– High temperature resistance, weathering and ozone resistance.
– Good barrier properties with low permeability to gases and vapors
• Applications
– Mechanical seals, packaging, O-rings, gaskets, diaphrams,
expansion joints, connectors, hose liners, roll covers, wire and
cable insulation.
• Previous fluoroelastomners are referred to as
– Fluorohydrocarbon elastomers since they contain F, H, and C
atoms with O sometimes
• Two other classes of elastomers include fluorinated types
– Fluorosilicone elastomers remain flexible at low temperatures
– Fluorinated polyorganophosphazenes have good fuel resistance
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Silicone Polymers
• Silicone polymers or polysiloxanes (PDMS)
– Polymeric chains featuring
• Tg = -125°C
• Very stable alternating combination of
• Silicone and oxygen, and a variety of organic side groups attached to Si
– Two methyl, CH3, are very common side group generates
polydimethylsiloxane (PDMS)
• Unmodified PDMS has very flexible chains corresponding to low Tg
• Modified PDMS has substitution of bulky side groups (5-10%)
– Phenylmethlsiloxane or diphenylsiloxane suppress crystallization
• Substituted side groups, e.g., vinyl groups (.5%) featuring double bonds
(unsaturations ) enables crosslinking to form vinylmethylsiloxane (VMS)
• Degree of polymerization, DP, of polysiloxane = 200-1,000 for low
consistency chains to 3,000-10,000 for high consistency resins.
• Mechanism of crosslinking can be from a vinyl unsaturation or reactive end
groups (alkoxy, acetoxy)
Si
CH3
CH3
m
O
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Silicone Polymers
• Silicone polymers or polysiloxanes (PDMS)
– Properties
• Mediocre tear properties
• High temperature resistance from -90C to 250C.
• Surface properties are characterized by very low surface energy (surface
tension) giving good slip, lubricity, and release properties (antistick) nand
water repellency.
• Excellent adhesion is obtained for curing compounds for caulk.
Si
CH3
CH3
m
O
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Silicones
• Unmodified PDMS has very flexible chains with a low Tg.
– Regular structure allows for crystallization below Tm
– Addition of small amount of bulky side groups are used to
suppress crystallization
• Trifluoropropyl side groups enhance the resistance to solvent swelling and
are called fluorosilicones
• Linear form (uncrosslinked) polysiloxane corresponds to DP of 200-1000
for low consistency to 3,000-10,000 for high consistency resins
• Mechanism for crosslinking (vulcanization) can be based upon vinyl
unsaturations or reactive end groups (alkoxy)
– Silicone polymers are mostly elastomers with mediocre tear properties,
but with addition of silica can have outstanding properties unaffected by
a wide temp range from –90°C to 250°C
• Surface properties have low surface energy, giving good slip, lubricity,
release properties, water repellency, excellent adhesion for caulks
• Good chemical inertness but sensitive to swelling by hydrocarbons
• Good resistance to oils and solvents, UV radiation, temperature
• Electrical properties are excellent and stable for insulation and dielectric
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Silicones
• Properties
– Low index of reflection gives silicone contains useful combination
of high transmission and low reflectance
– Can be biologically inert and with low toxicity are well tolerated
by body tissue
– Polymers are normally crosslinked in the vulcanization stage. Four
groups
• Low consistency-room temperature curing resins (RTV)
• Low consistency-high temperature curing resins (LIM,LSR)
• High consistency-high temperature curing resins (HTV, HCE),
• Rigid resins
– RTV elastomers involve low molecular weight polysiloxanes and
rely on reactive end groups for crosslinking at room temperature.
• One component, or one part, packages rely on atmospheric moisture for
curing and are used for thin parts or coatings
• Two component systems have a catalyst and require a mixing stage and
result in a small exotherm where heat is given off.
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Silicones
• Properties
– LSR elastomers involve low molecular weight polysiloxanes but a
different curing system
• Relatively high temperature (150°C) for a faster cure (10-30s)
• Mixed system is largely unreactive at room temp (long pot life)
• Suitable for high speed liquid injection molding of small parts.
– HTV elastomers contain unsaturations that are suitable for
conventional rubber processing.
• Heat curable elastomers (HCE) are cross linked through high temperature
vulcanization (HTV) with the use of peroxides.
– Rigid silicones are cross linked into tight networks.
• Non-crosslinked systems are stable only in solutions that are limited to
paints, varnishes, coatings, and matrices for laminates
• Cross-linking takes place when the solvent evaporates.
• Post curing is recommended to complete reaction, e.g., silicone-epoxy
systems for electrical encapsulation.
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Silicones Applications• Most applications involve elastomeric form.
• Flexibility and hardness can be adjusted over a wide range
– Electrical applications high voltage and high or low temperatures
• Power cable insulation, high voltage leads and insulator boots, ignition
cables, spark plug boots, etc..
• Semi-conductors are encapsulated in silicone resins for potting.
– Mechanical applications requiring low and high-temperature
flexibility and chemical inertness
• ‘O-rings’, gaskets, seals for aircraft doors and windows, freezers, ovens, and
appliances, diaphragms flapper valves, protective boots and bellows.
– Casting molds and patterns for polyurethane, polyester, or epoxy
– Sealants and caulking agents
– Shock absorbers and vibration damping characteristics
• “Silly-Putty”: Non-crosslinked, high molecular weight PDMS-based
compound modified with fillers and plasticizers.
– Biomedical field for biological inertness include prosthetic devices
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Miscellaneous Other Elastomers
• Acrylic Rubber (AR)
– Polyethylacrylate (PEA) copolymerized with a small amount (5%)
of 2-chloro-ethyl-vinyl-ether CEVE, which is a cure site.
– The Tg of PEA is about -27°C and acrylic rubber is not suitable for
low temperature applications.
– Polybutylacrylate (PBR) has a Tg of -45°C.
– Applications
• Resistant to high temperatures, lubricating oils, including
sulfur-bearing oils.
• Include seals, gaskets, and hoses.
• Epichlorohydrin Rubber (ECHR)
– Polymerization of epichlorohydrin with a repeat unit of PECH.
– Excellent resistant to oils, fuels and flame resistance. (Cl presence)
– Copolymer with flexible ethyleneoxide (EO) provides Tg = -40C
– Applications include seals, gaskets, diaphragms, wire covers
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Miscellaneous Other Elastomers
• Polysulfide Rubbers (SR)
– One of the first synthetic rubbers. Tg =-27°C, PES Thiokol A
– Consists of adjacent ethylene and sulfide units giving a stiff chain.
– Flexibility is increased with addition of ethylene oxide for polyethylene-ether-
sulfide (PEES), Thiokol B
– Mechanical properties are not very good, but are used for outstanding resistance
to many oils, solvents and weathering.
– Applications include caulking, mastics, and putty.
• Propylene rubber (PROR)
– Does not crystallize in its atactic form and has a low Tg = -72°C.
– Has excellent dynamic properties
H
C
H
C
H
S S ][
H
S S
C C
H CH3
H H
n
O
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Miscellaneous Other Elastomers
• Polynorborene (PNB)
– Norborene polymerizes into highly molecular weight PNB.
– Tg = 35°C but can be plasticized with oils and vulcanized into an
elastomer with lower Tg = -65°C.
– Excellent damping properties that can be adjusted.
• Polyorgano-phosphazenes (PPZ)
– Form an example of a new class of polymeric materials involving
inorganic chains.
• Atoms of Nitrogen (azo) and Phosphorous form, the chain and a variety of
organic side groups, R1 and R2 can be attached to the phosphorous atom.
• Side groups include halo (Cl or F), amino (NH2 or NHR), alkoxy (methoxy,
ethoxy, etc.) and fluoroalkoxy groups.
• High molecular weight is flexible with a low Tg
• Excellent inherent fire resistance, weatherability, and water & oil repellency
• Applications
– coatings, fibers, and biomedical materials
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Commercial Elastomers
• Characteristics
Name Chemical Name Vucanization agent
Natural rubber cis polyisoprene sulfur
Polyisoprene cis polyisoprene sulfur
Polybutadiene Polybutadiene sulfur
SBR Polybutadiene-styrene sulfur
Nitrile Polybutadiene-acrylonitrile sulfur
Butyl Poly isobutylene-isoprene sulfur
EPR (EPDM) Poly ethylene propylene- diene Peroxies or sulfur
Neoprene Polychloroprene MgO
Silicone Polydimethylsiloxane peroxides
Thiokol Polyslkylenesulfide ZnO
Urethanes Polyester or polyether urethanes Diisocycanates
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Commercial Elastomers
• Costs
Name Consumption 1983 (metric tons) $/lb Type
Natural rubber 676,267 $0.44 General Purpose
Polyisoprene $0.72 General Purpose
Polybutadiene 335,541 $0.74 General Purpose
SBR 887,005 $0.66 General Purpose
Nitrile 57,239 $1.10 Solvent Resistant
Butyl $0.76 General Purpose
EPR (EPDM) 141,490 $1.01 General Purpose
Neoprene 85,096 $1.29 Solvent Resistant
Silicone $4.40 Heat Resistant
Thiokol Psulfides $1.83 Solvent Resistant
Urethanes $3.70 Solvent Resistant
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Polymerization Mechanisms
• Step-wise (Condensation) Polymerization
– Monomers combine to form blocks 2 units long
– 2 unit blocks form 4, which intern form 8 and son on
until the process is terminated.
– Results in by-products (CO2, H2O, Acetic acid, HCl
etc.)
• Chain Growth (Addition) Polymerization
– Polymerization begins at one location on the monomer
by an initiator
– Instantaneously, the polymer chain forms with no by-
products
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Condensation Polymerization Example
• Polyamides
– Condensation Polymerization
• Nylon 6/6 because both the acid and amine contain
6 carbon atoms
NH2(CH2)6NH2 + COOH(CH2)4COOH
Hexamethylene diamene Adipic acid
n[NH2(CH2)6NH2 ·CO(CH2)4COOH] (heat)
Nylon salt
[NH(CH2)4NH·CO(CH2)4CO]n + nH2O
Nylon 6,6 polymer chain
34
Condensation Polymerization Example
• Polyurethane
– Reaction of isocyanate and polyether-alcohol (polyol)
• Polyester
– Polymerization of acid and and alcohol
• Polycarbonate
– Polycarbonates are linear, amorphous polyesters
because they contain esters of carbonic acid and an
aromatic bisphenol (C6H5OH)
Phenol + Acetone Bisphenol-A + water
2
OH
+
H2O+
C CH2CH3
O
C
CH2
CH2
OHOH
35
Other Condensation Polymers
• Thermoplastic Polyesters
– Saturated polyesters (Dacron).
• Linear polymers with high MW and no
crosslinking.
• Polyethylene Terephthalate (PET). Controlled
crystallinity.
• Polybutylene Terephthalate (PBT).
– Aromatic polyesters (Mylar) O C
O
R O C
O
R
C
O
C
O
R R
36
Step-Growth Polymerization
Condensation Polymerizatio
• Main feature is that all molecular species in the
system can react with each other to form higher
molecular weight species.
– Step-growth polymerization reactions fall into two
classes
• A-R1-A + B-R2-B => A-R1-R2-B + AB
• A-R1-A + B-R2-B => A-R1-AB-R2-B
– where A and B are repeat polymer groups which react with each other;
» Example, for polyurethanes A = Isocyanate and B = Polyol and the
by-product is water.
– and R1 and R2 are long chain polymers
37
Formation of Polymers
• Condensation Polymerization
– Step-growth polymerization proceeds by several steps which result
in by-products.
• Step-wise (Condensation) Polymerization
– Monomers combine to form blocks 2 units long
– 2 unit blocks form 4, which intern form 8 and son on until the
process is terminated.
– Results in by-products (CO2, H2O, Acetic acid, HCl etc.)
38
Chain Growth (Addition)
Polymerization
• Chain Growth (Addition) Polymerization by
Free Radical Mechanism
– Involves three primary steps
• Initiation- formation of free radicals through homolytic
dissociation of weak bonds (e.g., peroxides). Results in opening
up unsaturated (C=C) bonds to saturated (C-C) bonds)
• Propagation- formation of long chain polymers of the now free
C-C bonds
• Termination- reactions at the ends of the polymer cause C-C to
terminate with a functional group that does not have any free
electrons to bond with and results in unsaturated end group (C-
C=CX)
39
Chain Growth (Addition)
Polymerization
• Special case of Diene polymerization
– Very important in elastomers- mostly addition
– Polydienes are the backbone of the synthetic
rubber are produced by free radical
polymerization
– Early attempts of polymerization was slow and
produced low molecular weight polymers (oils)
– Emulsion polymerization (1930s) was introduced
to speed up polymerization and higher Molecular
weights
40
Polymerization Methods
• 4 Methods to produce polymers
– Some polymers have been produced by all four methods
• PE, PP and PVC are can be produced by several of these
methods
• The choice of method depends upon the final polymer form, the
intrinsic polymer arrangement (isotactic, atactic, etc), and the
yield and throughput of the polymer desired.
– Bulk Polymerization
– Solution Polymerization
– Suspension Polymerization
– Emulsion Polymerization
41
Formation of Polymers
• Polymers from Addition reaction
– LDPE HDPE PP
– PVC PS
C C
H H
H H
n
C C
H H
H H
n
C C
H CH3
H H
n
C C
H Cl
H H
n
C C
H
H H
n
42
Other Addition Polymers
• Vinyl- Large group of addition
polymers with the formula:
– Radicals (X,Y) may be attached to this
repeating vinyl group as side groups to form
several related polymers.
• Polyvinyls
– Polyvinyl chloride
– Polyvinyl dichloride
(polyvinylidene chloride)
– Polyvinyl Acetate (PVAc)
C C
H X
H Y
or
C C
H X
H H
CC
H Cl
H H
C C
H Cl
H Cl
C C
H OCOCH3
H H
43
Manufacturing of Emulsion SBR
• Free-radical emulsion process
– Developed in 1930s and still in use
– Typical process (Figure)
• Soap stabilized water emulsion of two monomers is converted in a train of
10 continuous reactors (4000 gallons each)
• Water, butadiene, styrene, soaps, initiators, buffers, and modifier are fed
continuously
• Temp is 5 to 10°C and conversion proceeds until 60% of the reactants have
polymerized in the last reactor.
• Shortstop is added in the emulsion to stop the conversion at 60%
• Unreacted butadiene is flashed off with steam and recycled
• Unreacted styrene is stripped off in a distillation column that separates
liquid rubber emulsion from the gas styrene.
• Rubber is recovered from the latex in a series of operations.
– Introduction of antioxidants, blending with oils, dilution with brine,
coagulation, dewatering, drying, and packaging the rubber
44
Manufacturing of Emulsion SBR
• Polymerization
– Cold SBR: at 5 to 10°C is called the cold process,
• Better abrasion resistant, treadwear, and dynamic properties.
– Hot SBR: at about 50°C is called the hot process.
• Conversion is allowed to proceed to 70%
• Higher branching occurs and incipient gelation.
– Typical SBR recipes, Table from Morton’s Rubber
technology
45
Manufacturing of Emulsion SBR
• Compounding and Processing
– Similar to natural rubber
– Materials for large scale use, e.g., tires, based on
• Rubber, fillers (carbon black), extending oils, zinc oxide,
sulfur, accelerators, antioxidants, antiozonants, and waxes.
– Materials are mixed in a mill or twin rollers or calendered
– Processing into smooth compounds that can be quickly
pressed, sheeted, calendered, or extruded
• Recipes
– Large parts, e.g., tires and hoses, are given in Tables 7.6,
7.7, 7.8, and 7.9
46
Polymerization of Elastomers
• Butadiene-Acrylonitrile (Nitrile) Rubber
– Produced by emulsion polymerization
– Nitrile rubbers have nitrile contents from 10 to 40%.
• Chloroprene rubber
– Produced by emulsion polymerization
– Produced as a homopolymer that has a high trans 1,4
chain structure and is susceptible to strain-induced
crystallization, much like natural rubber.
• Leads to high tensile strength
– Does not lead itself to copolymerization
47
Polymerization of Elastomers
• Butyl Rubber-
– Only important commercial rubber prepared by cationic
polymerization
• Processes with AlCl at –98 to –90°C
– Copolymer of isobutene and isoprene with isoprene used
in 1.5 % quantities
• The isoprene is introduced to provide sufficient unsaturations
for sulfur vulcanization.
– MW is in the range of 300,000 to 500,000
48
Processing of Elastomers
• Rubber Products
– 50% of all rubber produced goes into automobile tires;
– 50% goes into mechanical parts such as
• mountings, gaskets, belts, and hoses, as well as
• consumer products such as shoes, clothing, furniture, and toys
• Elastomers and Rubbers
– Thermoset rubbers
• Compounding the ingredients in recipe into the raw rubber with
a mill, calender, or Banbury (internal) mixer
• Compression molding of tires
– Thermoplastic elastomers
• Compression molding, extrusion, injection molding, casting.
49
Processing of Elastomers
• Rubber Processors
– Mills and Banbury mixers
50
Compression Molding Process
• Materials
•Elastomers:
•Thermoplastic
•Thermoplastic Olefin (TPO), Thermoplastic Elastomer (TPE),
Thermoplastic Rubber (TPR)
•Thermoset rubbers
•Styrene Butadiene Rubber, isoprene
Thermoplastic:
Heat Plastic
prior to molding
Thermosets:
Heat Mold
during molding
51
Polyurethane Processing
• Polyurethane can be processed by
– Slow process: Casting or foaming, or
– Fast process: Reaction Injection Molding (RIM)
52
Injection Molding Glass Elastomers
• Plastic pellets with copolymer elastomers.
– Similar processing requirements as with injection
molding of commodity and engineering plastics
• Injection pressures, tonnage, pack pressure, shrinkage
53
Transfer Molding of Rubbers
• Transfer molding is a process by which uncured rubber
compound is transferred from a holding vessel (transfer pot) to
the mold cavities using a hydraulically operated piston.
Transfer molding is especially conducive to multicavity designs
and can produce nearly flashless parts.
54
Calendering of Rubbers
• Calendering is the process for producing long runs of uniform
thickness sheets of rubber either unsupported or on a fabric
backing. A standard 3 or 4 roll calender with linear speed range
of 2 to 10 feet/minute is typical for silicone rubber. Firm
compound with good green strength and resistance to
overmilling works the best for calendering.
55
Curing of Rubbers
• Extruded profile may be cured by hot air vulcanization (HAV),
steam vulcanization (CV) or liquid-medium cure. HAV consists
of a heated tunnel through which the profile is fed continuously
on a moving conveyor. Air temperature reaches 600°F to
1200°F, and cure times are usually short, on the order of 3 to 12
seconds. The recommended curing agents are DCBP-50 or
addition cure, both of which provide rapid cure with no
porosity.
• Steam cure commonly refers to the steam curing systems used
by the wire and cable industry and consists of chambers 4” –
6” in diameter and 100 – 150 feet in length. Steam pressure
varies from 50 psig to 225 psig depending on wall thickness of
the insulation.
• For liquid-medium cure, continuous lengths of extruded profile
are fed into a bath of moltenmaterial (salt or lead) which cures
the extrudate.
56
Polymer Length
• Polymer Length
– Polymer notation represents the repeating group
• Example, -[A]-n where A is the repeating monomer and n represents the
number of repeating units.
• Molecular Weight
– Way to measure the average chain length of the polymer
– Defined as sum of the atomic weights of each of the atoms in the
molecule.
• Example,
– Water (H2O) is 2 H (1g) and one O (16g) = 2*(1) + 1*(16)= 18g/mole
– Methane CH4 is 1 C (12g) and 4 H (1g)= 1*(12) + 4 *(1) = 16g/mole
– Polyethylene -(C2H4)-1000= 2 C (12g) + 4H (1g) = 28g/mole * 1000 = 28,000
g/mole
57
Molecular Weight
• Average Molecular Weight
– Polymers are made up of many molecular weights or a
distribution of chain lengths.
• The polymer is comprised of a bag of worms of the same
repeating unit, ethylene (C2H4) with different lengths; some
longer than others.
• Example,
– Polyethylene -(C2H4)-1000 has some chains (worms) with 1001 repeating
ethylene units, some with 1010 ethylene units, some with 999 repeating
units, and some with 990 repeating units.
– The average number of repeating units or chain length is 1000 repeating
ethylene units for a molecular weight of 28*1000 or 28,000 g/mole .
58
Molecular Weight
• Average Molecular Weight
– Distribution of values is useful statistical way to
characterize polymers.
• For example,
– Value could be the heights of students in a room.
– Distribution is determined by counting the number of students in the
class of each height.
– The distribution can be visualized by plotting the number of students on
the x-axis and the various heights on the y-axis.
Histogram of Heights of Students
0
5
10
15
20
25
60 70 80
Height, inches
Frequency
Series1
59
Molecular Weight
• Molecular Weight Distribution
– Count the number of molecules of each molecular weight
– The molecular weights are counted in values or groups that have similar lengths,
e.g., between 100,000 and 110,000
• For example,
– Group the heights of students between 65 and 70 inches in one group, 70 to 75
inches in another group, 75 and 80 inches in another group.
• The groups are on the x-axis and the frequency on the y-axis.
• The counting cells are rectangles with the width the spread of the cells and
the height is the frequency or number of molecules
• Figure 3.1
• A curve is drawn representing the overall shape of the plot by connecting
the tops of each of the cells at their midpoints.
• The curve is called the Molecular Weight Distribution (MWD)
60
Molecular Weight
• Average Molecular Weight
– Determined by summing the weights of all of the chains
and then dividing by the total number of chains.
– Average molecular weight is an important method of
characterizing polymers.
– 3 ways to represent Average molecular weight
• Number average molecular weight
• Weight average molecular weight
• Z-average molecular weight
61
Gel Permeation Chromatography
• GPC Used to measure Molecular Weights
– form of size-exclusion chromatography
– smallest molecules pass through bead pores, resulting in
a relatively long flow path
– largest molecules flow around beads, resulting in a
relatively short flow path
– chromatogram obtained shows intensity vs. elution
volume
– correct pore sizes and solvent critical
62
Gel Permeation Chromatography
63
Number Average Molecular Weight, Mn
•
• where Mi is the molecular weight of that species (on the x-axis)
• where Ni is the number of molecules of a particular molecular species I (on
the y-axis).
– Number Average Molecular Weight gives the same weight to all polymer
lengths, long and short.
• Example, What is the molecular weight of a polymer sample in which the polymers
molecules are divided into 5 categories.
– Group Frequency
– 50,000 1
– 100,000 4
– 200,000 5
– 500,000 3
– 700,000 1
...
...
321
332211
+++
+++
==
∑
∑
NNN
MNMNMN
N
MN
M
i
ii
n
000,260
)13541(
)700(1)500(3)200(5)100(4)50(1
...
...
321
332211
=
++++
++++
=
+++
+++
==
∑
∑
n
n
i
ii
n
M
KKKKK
M
NNN
MNMNMN
N
MN
M
64
Molecular Weight
• Number Average Molecular Weight. Figure 3.2
– The data yields a nonsymmetrical curve (common)
– The curve is skewed with a tail towards the high MW
– The Mn is determined experimentally by analyzing the number of
end groups (which permit the determination of the number of
chains)
– The number of repeating units, n, can be found by the ratio of the
Mn and the molecualr weight of the repeating unit, M0, for
example for polyethylene, M0 = 28 g/mole
– The number of repeating units, n, is often called the degree of
polymerization, DP.
– DP relates the amount of
monomer that has been converted to polymer.
0M
M
n n
=
65
Weight Average Molecular Weight, Mw
• Weight Average Molecular Weight, Mw
– Favors large molecules versus small ones
– Useful for understanding polymer properties that relate to
the weight of the polymer, e.g., penetration through a
membrane or light scattering.
– Example,
• Same data as before would give a higher value for the
Molecular Weight. Or, Mw = 420,000 g/mole
...
...
332211
2
33
2
22
2
11
2
+++
+++
==
∑
∑
MNMNMN
MNMNMN
MN
MN
M
ii
ii
w
66
Z- Average Molecular Weight
– Emphasizes large molecules even more than Mw
– Useful for some calculations involving mechanical
properties.
– Method uses a centrifuge to separate the polymer
...
...
2
33
2
22
2
11
3
33
3
22
3
11
2
3
+++
+++
==
∑
∑
MNMNMN
MNMNMN
MN
MN
M
ii
ii
z
67
Molecular Weight Distribution
• Molecular Weight Distribution represents the
frequency of the polymer lengths
• The frequency can be Narrow or Broad, Fig 3.3
• Narrow distribution represents polymers of about
the same length.
• Broad distribution represents polymers with varying
lengths
• MW distribution is controlled by the conditions
during polymerization
• MW distributions can be symmetrical or skewed.
68
Physical and Mechanical Property
Implications of MW and MWD
• Higher MW increases
• Tensile Strength, impact toughness, creep resistance, and
melting temperature.
– Due to entanglement, which is wrapping of polymer
chains around each other.
– Higher MW implies higher entanglement which yields
higher mechanical properties.
– Entanglement results in similar forces as secondary or
hydrogen bonding, which require lower energy to break
than crosslinks.
69
Physical and Mechanical Property Implications
of MW and MWD
• Higher MW increases tensile strength
• Resistance to an applied load pulling in opposite directions
• Tension forces cause the polymers to align and reduce the number of
entanglements. If the polymer has many entanglements, the force would be
greater.
• Broader MW Distribution decreases tensile strength
• Broad MW distribution represents polymer with many shorter molecules
which are not as entangled and slide easily.
• Higher MW increases impact strength
• Impact toughness or impact strength are increased with longer polymer
chains because the energy is transmitted down chain.
• Broader MW Distribution decreases impact strength
• Shorter chains do not transmit as much energy during impact
70
Thermal Property Implications of MW & MWD
• Higher MW increases Melting Point
• Melting point is a measure of the amount of energy necessary
to have molecules slide freely past one another.
• If the polymer has many entanglements, the energy required
would be greater.
• Low molecular weights reduce melting point and increase ease
of processing.
• Broader MW Distribution decreases Melting Point
• Broad MW distribution represents polymer with many shorter
molecules which are not as entangled and melt sooner.
• Broad MW distribution yields an easier processed polymer
Mechanical
Properties
Melting
Point
* Decomposition
71
Example of High Molecular Weight
• Ultra High Molecular Weight Polyethylene (UHWMPE)
• Modifying the MWD of Polyethylene yields a polymer with
– Extremely long polymer chains with narrow distribution
– Excellent strength
– Excellent toughness and high melting point.
• Material works well in injection molding (though high melt T)
• Does not work well in extrusion or blow molding, which
require high melt strength.
• Melt temperature range is narrow and tough to process.
• Properties improved if lower MW polyethylene
– Acts as a low-melting lubricant
– Provides bimodal distributions, Figure 3.5
– Provides a hybrid material with hybrid properties

ABOUT ELASTOMER TYPES AND VULCANISATION

  • 1.
    1 Classes of PolymericMaterials Elastomers Professor Joe Greene CSU, CHICO
  • 2.
    2 Elastomers • Elastomers arerubber like polymers that are thermoset or thermoplastic – butyl rubber: natural rubber – thermoset: polyurethane, silicone – thermoplastic: thermoplastic urethanes (TPU), thermoplastic elastomers (TPE), thermoplastic olefins (TPO), thermoplastic rubbers (TPR) • Elastomers exhibit more elastic properties versus plastics which plastically deform and have a lower elastic limit. • Rubbers have the distinction of being stretched 200% and returned to original shape. Elastic limit is
  • 3.
    3 Rubbers • Rubbers havethe distinction of being stretched 200% and returned to original shape. Elastic limit is 200% • Natural rubber (isoprene) is produced from gum resin of certain trees and plants that grow in southeast Asia, Ceylon, Liberia, and the Congo. – The sap is an emulsion containing 40% water & 60% rubber particles • Vulcanization occurs with the addition of sulfur (4%). – Sulfur produces cross-links to make the rubber stiffer and harder. – The cross-linkages reduce the slippage between chains and results in higher elasticity. – Some of the double covalent bonds between molecules are broken, allowing the sulfur atoms to form cross-links. – Soft rubber has 4% sulfur and is 10% cross-linked. – Hard rubber (ebonite) has 45% sulfur and is highly cross-linked.
  • 4.
    4 Rubber Additives andModifiers • Fillers can comprise half of the volume of the rubber – Silica and carbon black. – Reduce cost of material. – Increase tensile strength and modulus. – Improve abrasion resistance. – Improve tear resistance. – Improve resistance to light and weathering. – Example, • Tires produced from Latex contains 30% carbon black which improves the body and abrasion resistance in tires. • Additives – Antioxidants, antiozonants, oil extenders to reduce cost and soften rubber, fillers, reinforcement
  • 5.
    5 Vulcanizable Elastomeric Compounds •Rubbers are compounded into practical elastomers – The rubber (elastomer) is the major component and other components are given as weight per hundred weight rubber (phr) • Sulfur is added in less than 10 phr • Accelerators and activators with the sulfur – hexamethylene tetramine (HMTA) – zinc oxide as activators • Protective agents are used to suppress the effects of oxygen and ozone – phenyl betabaphthylamine and alkyl paraphenylene diamine (APPD) • Reinforcing filler – carbon black – silica when light colors are required – calcium carbonate, clay, kaoilin • Processing aids which reduce stiffness and cost – Plasticizers, lubricants, mineral oils, paraffin waxes,
  • 6.
    6 Vulcanizable Rubber • Typicaltire tread – Natural rubber smoked sheet (100), – sulfur (2.5) sulfenamide (0.5), MBTS (0.1), strearic acid (3), zinc oxide (3), PNBA (2), HAF carbon black (45), and mineral oil (3) • Typical shoe sole compound – SBR (styrene-butadiene-rubber) (100) and clay (90) • Typical electrical cable cover – polychloroprene (100), kaolin (120), FEF carbon black (15) and mineral oil (12), vulcanization agent
  • 7.
    7 Synthetic Rubber• Reactivesystem elastomers – Low molecular weight monomers are reacted in a polymerization step with very little cross-linking. – Reaction is triggered by heat, catalyst, and mixing • Urethanes processed with Reaction Injection Molding (RIM) • Silicones processed with injection molding or extrusion • Thermoplastic Elastomers – Processing involves melting of polymers, not thermoset reaction – Processed by injection molding, extrusion, blow molding, film blowing, or rotational molding. • Injection molded soles for footwear – Advantages of thermoplastic elastomers • Less expensive due to fast cycle times • More complex designs are possible • Wider range of properties due to copolymerization – Disadvantage of thermoplastic elastomers • Higher creep
  • 8.
    8 Thermoplastic Elastomers • Fourtypes of elastomers – Olefinics and Styrenics – Polyurethanes and Polyesters • Olefinics (TPOs are used for bumper covers on cars) – Produced by • Blending copolymers of ethylene and propylene (EPR) or ter polymer of ethylene-propylene diene (EPDM) with • PP in ratios that determine the stiffness of the elastomer – A 80/20 EPDM/PP ratio gives a soft elastomer (TPO) • Styrenic thermoplastic elastomers (STPE) – Long triblock copolymer molecules with • an elastomeric central block (butadiene, isoprene, ethylene-butene, etc.) and • end blocks (styrene, etc.) which form hard segments – Other elastomers have varying amounts of soft and hard blocks
  • 9.
    9 Thermoplastic Elastomers • Polyurethanes –Have a hard block segment and soft block segment • Soft block corresponds to polyol involved in polymerization in ether based • Hard blocks involve the isocyanates and chain extenders • Polyesters are etheresters or copolyester thermoplastic elastomer – Soft blocks contain ether groups are amorpous and flexible – Hard blocks can consist of polybutylene terephthalate (PBT) • Polyertheramide or polyetherblockamide elastomer – Hard blocks consits of a crystallizing polyamide Soft Hard Hard Hard Soft Soft
  • 10.
    10 Commercial Elastomers • DieneC=C double bonds and Related Elastomers – Polyisoprene- (C5H8)20,000 • Basic structure of natural rubber • Can be produced as a synthetic polymer • Capable of very slow crystallization • Tm = 28°C, Tg = -70°C for cis polyisoprene • Tm = 68°C, Tg = -70°C for trans polyisoprene – Trans is major component of gutta percha, the first plastic – Natural rubber was first crosslinked into highly elastic network by Charles Goodyear (vulcanization with sulfur in 1837) • Sulfur crosslinked with the unsaturations C=C – Natural rubber in unfilled form is widely used for products with • very large elastic deformations or very high resilience, • resistance to cold flow (low compression set) and • resistance to abrasion, wear, and fatigue. – Natural rubber does not have good intrinsic resistance to sunlight, oxygen, ozone, heat aging, oils, or fuels. C H C C H H3HH H C C ][ C H C H HH H C C ][ CH3 Cis Trans
  • 11.
    11 Commercial Elastomers • Polybutadiene –Basis for synthetic rubber as a major component in copolymers Styrene-Butadiene Rubber (SBR, NBR) or in – Blends with other rubbers (NR, SBR) – Can improve low-temperature properties, resilence, and abrasion or wear resistance • Tg = -50°C • Polychloroprene – Polychloroprene or neoprene was the very first synthetic rubber – Due to polar nature of molecule from Cl atom it has very good resistance to oils and is flame resistant (Cl gas coats surface) – Used for fuel lines, hoses, gaskets, cable covers, protective boots, bridge pads, roofing materials, fabric coatings, and adhesives – Tg = -65°C. H H C H C H HH C C ][ H H C H C Cl HH C C ][
  • 12.
    12 Commercial Elastomers • Butylrubber- addition polymer of isobutylene. – Copolymer with a few isoprene units, Tg =-65°C – Contains only a few percent double bonds from isoprene – Small extent of saturation are used for vulcanization – Good regularity of the polymer chain makes it possible for the elastomer to crystallize on stretching – Soft polymer is usually compounded with carbon black to increase modulus • Nitrile rubber – Copolymer of butadiene and acrylonitrile – Solvent resistant rubber due to nitrile C:::N – Irregular chain structure will not crystallize on stretching, like SBR – vulcanization is achieved with sulfur like SBR and natural rubber • Thiokol- ethylene dichloride polymerized with sodium H H3 C CH3H C C ][
  • 13.
    13 Thermoplastic Elastomers • ThermoplasticElastomers result from copolymerization of two or more monomers. – One monomer is used to provide the hard, crystalline features, whereas the other monomer produces the soft, amorphous features. – Combined these form a thermoplastic material that exhibits properties similar to the hard, vulcanized elastomers. • Thermoplastic Urethanes (TPU) – The first Thermoplastic Elastomer (TPE) used for seals gaskets, etc. • Other TPEs – Copolyester for hydraulic hoses, couplings, and cable insulation. – Styrene copolymers are less expensive than TPU with lower strength – Styrene-butadiene (SBR) for medical products, tubing, packaging, etc. – Olefins (TPO) for tubing, seals, gaskets, electrical, and automotive.
  • 14.
    14 Thermoplastic Elastomers • Styrene-butadienerubber (SBR) – Developed during WWII • Germany under the name of BUNA-S. • North America as GR-S,Government rubber-styrene. – Random copolymer of butadiene (67-85%) and styrene (15-33%) – Tg of typical 75/25 blend is –60°C – Not capable of crystallizing under strain and thus requires reinforcing filler, carbon black, to get good properties. – One of the least expensive rubbers and generally processes easily. – Inferior to natural rubber in mechanical properties – Superior to natural rubber in wear, heat aging, ozone resistance, and resistance to oils. – Applications include tires, footwear, wire, cable insulation, industrial rubber products, adhesives, paints (latex or emulsion) • More than half of the world’s synthetic rubber is SBR • World usage of SBR equals natural rubber C C H H H n H H C H C H HH C C ][
  • 15.
    15 Acrylonitrile-butadiene rubber (NBR) •Also called Nitrile rubber – Developed as an oil resistant rubber due to • the polar C:::N polar bond. Resistant to oils, fuels, and solvents. – Copolymer of acrylonitrile (20-50%) and butadiene(80-50%) – Moderate cost and a general purpose rubber. – Excellent properties for heat aging and abrasion resistance – Poor properties for ozone and weathering resistance. – Has high dielectric losses and limited low temperature flexibility – Applications include fuel and oil tubing; hose, gaskets, and seals; conveyer belts, print rolls, and pads. – Carboxylated nitrile rubbers (COX-NBR) has carboxyl side groups (COOH)which improve • Abrasion and wear resistance; ozone resistance; and low temperature flexibility – NBR and PVC for miscible, but distinct polymer blend or polyalloy • 30% addition of PVC improves ozone and fire resistance H H C H C H HH C C ][C C H C:::N H H n m
  • 16.
    16 Ethylene-propylene rubber (EPR) •EPR and EPDM – Form a noncrystallizing copolymer • with a low Tg. – The % PP and PE units determines properties • Tg = -60°C for PE/PP of 67/33 to 50/50 – Unsaturated polymer since PP and PE are saturated • Resistant to ozone, weathering, and heat aging • Does not allow for conventional vulcanization – Terpolymer with addition of small amount of third monomer (Diene D) has unsaturations referred to as EPDM • 1,4, hexadiene (HD); 5-ethylidene-2-norbornene (ENB); diclopentadiene (DCPB) feature unsaturations in a side (pendant) group • Feature excellent ozone and weathering resistance and good heat aging – Limitations include poor resistance to oils and fuels, poor adhesion to many substrates and reinforcements – Applications include exterior automotive parts (TPO is PP/EPDM), construction parts, weather strips, wire and cable insulation, hose and belt products, coated fabrics. C C H H H H n C C H CH3 H H m C C H CH2 H H mCH CH CH3
  • 17.
    17 Ethylene Related Elastomers •Chlorosulfonated Polyethylene (CSPE) – Moderate random chlorination of PE (24-43%) – Infrequent chlorosulfonic groups (SO2Cl) – Sulfur content is 1-1.5%. – CSPE is noted for excellent weathering resistance • Good resistance to ozones, heat, chemicals, solvents. • Good electrical properties, low gas permeability, good adhesion to substrates – Applications include hose products, roll covers, tank linings, wire and cable covers, footwear, and building products • Chlorinated Polyethylene (CPE) – Moderate random chlorination • Suppresses crystallinity (rubber) • Can be crosslinked with peroxides • Cl range is 36-42% versus 56.8% for PVC – Properties include good heat, oil, and ozone resistance – Used as plasticizer for PVC C C H H H H n C Cl H m C S H k Cl O O
  • 18.
    18 Ethylene Related Elastomers •Ethylene-vinylacetate Copolymer (EVA) – Random copolymer of E and VA • Amorphous and thus elastomeric • VA range is 40-60% • Can be crosslinked through organic peroxides – Properties include • Good heat, ozone, and weather resistance • Ethylene-acrylate copolymer (EAR) – Copolymer of Ethylene and methacrylate • Contains carboxylic side groups (COOH) – Properties include • Excellent resistance to ozone and • Excellent energy absorbers – Better than butyl rubbers C C H H H H n C C H O H H O=CCH3 m C C H H H H n C C H C H H O OCH3 m
  • 19.
    19 FluoroElastomers • Polyvinylidene fluoride(PVDF) – Tg = -35°C • Poly chloro tri fluoro ethylene (PCTFE) – Tg = 40°C • Poly hexa fluoro propylene (PHFP) – Tg = 11°C • Poly tetra fluoro ethylene (PTFE) – Tg = - 130°C • Fluoroelastomers are produced by – random copolymerization that – suppresses the crystallinity and – provides a mechanism for cross linking by terpolymerization • Monomers include VDF, CTFE, HFP, and TFE C C H F H F n C C F Cl F F n C C F CF3 F F n C C F F F F n
  • 20.
    20 FluoroElastomers • Fluoroelastomers areexpensive but have outstanding properties – Exceptional resistance to chemicals, especially oils, solvents – High temperature resistance, weathering and ozone resistance. – Good barrier properties with low permeability to gases and vapors • Applications – Mechanical seals, packaging, O-rings, gaskets, diaphrams, expansion joints, connectors, hose liners, roll covers, wire and cable insulation. • Previous fluoroelastomners are referred to as – Fluorohydrocarbon elastomers since they contain F, H, and C atoms with O sometimes • Two other classes of elastomers include fluorinated types – Fluorosilicone elastomers remain flexible at low temperatures – Fluorinated polyorganophosphazenes have good fuel resistance
  • 21.
    21 Silicone Polymers • Siliconepolymers or polysiloxanes (PDMS) – Polymeric chains featuring • Tg = -125°C • Very stable alternating combination of • Silicone and oxygen, and a variety of organic side groups attached to Si – Two methyl, CH3, are very common side group generates polydimethylsiloxane (PDMS) • Unmodified PDMS has very flexible chains corresponding to low Tg • Modified PDMS has substitution of bulky side groups (5-10%) – Phenylmethlsiloxane or diphenylsiloxane suppress crystallization • Substituted side groups, e.g., vinyl groups (.5%) featuring double bonds (unsaturations ) enables crosslinking to form vinylmethylsiloxane (VMS) • Degree of polymerization, DP, of polysiloxane = 200-1,000 for low consistency chains to 3,000-10,000 for high consistency resins. • Mechanism of crosslinking can be from a vinyl unsaturation or reactive end groups (alkoxy, acetoxy) Si CH3 CH3 m O
  • 22.
    22 Silicone Polymers • Siliconepolymers or polysiloxanes (PDMS) – Properties • Mediocre tear properties • High temperature resistance from -90C to 250C. • Surface properties are characterized by very low surface energy (surface tension) giving good slip, lubricity, and release properties (antistick) nand water repellency. • Excellent adhesion is obtained for curing compounds for caulk. Si CH3 CH3 m O
  • 23.
    23 Silicones • Unmodified PDMShas very flexible chains with a low Tg. – Regular structure allows for crystallization below Tm – Addition of small amount of bulky side groups are used to suppress crystallization • Trifluoropropyl side groups enhance the resistance to solvent swelling and are called fluorosilicones • Linear form (uncrosslinked) polysiloxane corresponds to DP of 200-1000 for low consistency to 3,000-10,000 for high consistency resins • Mechanism for crosslinking (vulcanization) can be based upon vinyl unsaturations or reactive end groups (alkoxy) – Silicone polymers are mostly elastomers with mediocre tear properties, but with addition of silica can have outstanding properties unaffected by a wide temp range from –90°C to 250°C • Surface properties have low surface energy, giving good slip, lubricity, release properties, water repellency, excellent adhesion for caulks • Good chemical inertness but sensitive to swelling by hydrocarbons • Good resistance to oils and solvents, UV radiation, temperature • Electrical properties are excellent and stable for insulation and dielectric
  • 24.
    24 Silicones • Properties – Lowindex of reflection gives silicone contains useful combination of high transmission and low reflectance – Can be biologically inert and with low toxicity are well tolerated by body tissue – Polymers are normally crosslinked in the vulcanization stage. Four groups • Low consistency-room temperature curing resins (RTV) • Low consistency-high temperature curing resins (LIM,LSR) • High consistency-high temperature curing resins (HTV, HCE), • Rigid resins – RTV elastomers involve low molecular weight polysiloxanes and rely on reactive end groups for crosslinking at room temperature. • One component, or one part, packages rely on atmospheric moisture for curing and are used for thin parts or coatings • Two component systems have a catalyst and require a mixing stage and result in a small exotherm where heat is given off.
  • 25.
    25 Silicones • Properties – LSRelastomers involve low molecular weight polysiloxanes but a different curing system • Relatively high temperature (150°C) for a faster cure (10-30s) • Mixed system is largely unreactive at room temp (long pot life) • Suitable for high speed liquid injection molding of small parts. – HTV elastomers contain unsaturations that are suitable for conventional rubber processing. • Heat curable elastomers (HCE) are cross linked through high temperature vulcanization (HTV) with the use of peroxides. – Rigid silicones are cross linked into tight networks. • Non-crosslinked systems are stable only in solutions that are limited to paints, varnishes, coatings, and matrices for laminates • Cross-linking takes place when the solvent evaporates. • Post curing is recommended to complete reaction, e.g., silicone-epoxy systems for electrical encapsulation.
  • 26.
    26 Silicones Applications• Mostapplications involve elastomeric form. • Flexibility and hardness can be adjusted over a wide range – Electrical applications high voltage and high or low temperatures • Power cable insulation, high voltage leads and insulator boots, ignition cables, spark plug boots, etc.. • Semi-conductors are encapsulated in silicone resins for potting. – Mechanical applications requiring low and high-temperature flexibility and chemical inertness • ‘O-rings’, gaskets, seals for aircraft doors and windows, freezers, ovens, and appliances, diaphragms flapper valves, protective boots and bellows. – Casting molds and patterns for polyurethane, polyester, or epoxy – Sealants and caulking agents – Shock absorbers and vibration damping characteristics • “Silly-Putty”: Non-crosslinked, high molecular weight PDMS-based compound modified with fillers and plasticizers. – Biomedical field for biological inertness include prosthetic devices
  • 27.
    27 Miscellaneous Other Elastomers •Acrylic Rubber (AR) – Polyethylacrylate (PEA) copolymerized with a small amount (5%) of 2-chloro-ethyl-vinyl-ether CEVE, which is a cure site. – The Tg of PEA is about -27°C and acrylic rubber is not suitable for low temperature applications. – Polybutylacrylate (PBR) has a Tg of -45°C. – Applications • Resistant to high temperatures, lubricating oils, including sulfur-bearing oils. • Include seals, gaskets, and hoses. • Epichlorohydrin Rubber (ECHR) – Polymerization of epichlorohydrin with a repeat unit of PECH. – Excellent resistant to oils, fuels and flame resistance. (Cl presence) – Copolymer with flexible ethyleneoxide (EO) provides Tg = -40C – Applications include seals, gaskets, diaphragms, wire covers
  • 28.
    28 Miscellaneous Other Elastomers •Polysulfide Rubbers (SR) – One of the first synthetic rubbers. Tg =-27°C, PES Thiokol A – Consists of adjacent ethylene and sulfide units giving a stiff chain. – Flexibility is increased with addition of ethylene oxide for polyethylene-ether- sulfide (PEES), Thiokol B – Mechanical properties are not very good, but are used for outstanding resistance to many oils, solvents and weathering. – Applications include caulking, mastics, and putty. • Propylene rubber (PROR) – Does not crystallize in its atactic form and has a low Tg = -72°C. – Has excellent dynamic properties H C H C H S S ][ H S S C C H CH3 H H n O
  • 29.
    29 Miscellaneous Other Elastomers •Polynorborene (PNB) – Norborene polymerizes into highly molecular weight PNB. – Tg = 35°C but can be plasticized with oils and vulcanized into an elastomer with lower Tg = -65°C. – Excellent damping properties that can be adjusted. • Polyorgano-phosphazenes (PPZ) – Form an example of a new class of polymeric materials involving inorganic chains. • Atoms of Nitrogen (azo) and Phosphorous form, the chain and a variety of organic side groups, R1 and R2 can be attached to the phosphorous atom. • Side groups include halo (Cl or F), amino (NH2 or NHR), alkoxy (methoxy, ethoxy, etc.) and fluoroalkoxy groups. • High molecular weight is flexible with a low Tg • Excellent inherent fire resistance, weatherability, and water & oil repellency • Applications – coatings, fibers, and biomedical materials
  • 30.
    30 Commercial Elastomers • Characteristics NameChemical Name Vucanization agent Natural rubber cis polyisoprene sulfur Polyisoprene cis polyisoprene sulfur Polybutadiene Polybutadiene sulfur SBR Polybutadiene-styrene sulfur Nitrile Polybutadiene-acrylonitrile sulfur Butyl Poly isobutylene-isoprene sulfur EPR (EPDM) Poly ethylene propylene- diene Peroxies or sulfur Neoprene Polychloroprene MgO Silicone Polydimethylsiloxane peroxides Thiokol Polyslkylenesulfide ZnO Urethanes Polyester or polyether urethanes Diisocycanates
  • 31.
    31 Commercial Elastomers • Costs NameConsumption 1983 (metric tons) $/lb Type Natural rubber 676,267 $0.44 General Purpose Polyisoprene $0.72 General Purpose Polybutadiene 335,541 $0.74 General Purpose SBR 887,005 $0.66 General Purpose Nitrile 57,239 $1.10 Solvent Resistant Butyl $0.76 General Purpose EPR (EPDM) 141,490 $1.01 General Purpose Neoprene 85,096 $1.29 Solvent Resistant Silicone $4.40 Heat Resistant Thiokol Psulfides $1.83 Solvent Resistant Urethanes $3.70 Solvent Resistant
  • 32.
    32 Polymerization Mechanisms • Step-wise(Condensation) Polymerization – Monomers combine to form blocks 2 units long – 2 unit blocks form 4, which intern form 8 and son on until the process is terminated. – Results in by-products (CO2, H2O, Acetic acid, HCl etc.) • Chain Growth (Addition) Polymerization – Polymerization begins at one location on the monomer by an initiator – Instantaneously, the polymer chain forms with no by- products
  • 33.
    33 Condensation Polymerization Example •Polyamides – Condensation Polymerization • Nylon 6/6 because both the acid and amine contain 6 carbon atoms NH2(CH2)6NH2 + COOH(CH2)4COOH Hexamethylene diamene Adipic acid n[NH2(CH2)6NH2 ·CO(CH2)4COOH] (heat) Nylon salt [NH(CH2)4NH·CO(CH2)4CO]n + nH2O Nylon 6,6 polymer chain
  • 34.
    34 Condensation Polymerization Example •Polyurethane – Reaction of isocyanate and polyether-alcohol (polyol) • Polyester – Polymerization of acid and and alcohol • Polycarbonate – Polycarbonates are linear, amorphous polyesters because they contain esters of carbonic acid and an aromatic bisphenol (C6H5OH) Phenol + Acetone Bisphenol-A + water 2 OH + H2O+ C CH2CH3 O C CH2 CH2 OHOH
  • 35.
    35 Other Condensation Polymers •Thermoplastic Polyesters – Saturated polyesters (Dacron). • Linear polymers with high MW and no crosslinking. • Polyethylene Terephthalate (PET). Controlled crystallinity. • Polybutylene Terephthalate (PBT). – Aromatic polyesters (Mylar) O C O R O C O R C O C O R R
  • 36.
    36 Step-Growth Polymerization Condensation Polymerizatio •Main feature is that all molecular species in the system can react with each other to form higher molecular weight species. – Step-growth polymerization reactions fall into two classes • A-R1-A + B-R2-B => A-R1-R2-B + AB • A-R1-A + B-R2-B => A-R1-AB-R2-B – where A and B are repeat polymer groups which react with each other; » Example, for polyurethanes A = Isocyanate and B = Polyol and the by-product is water. – and R1 and R2 are long chain polymers
  • 37.
    37 Formation of Polymers •Condensation Polymerization – Step-growth polymerization proceeds by several steps which result in by-products. • Step-wise (Condensation) Polymerization – Monomers combine to form blocks 2 units long – 2 unit blocks form 4, which intern form 8 and son on until the process is terminated. – Results in by-products (CO2, H2O, Acetic acid, HCl etc.)
  • 38.
    38 Chain Growth (Addition) Polymerization •Chain Growth (Addition) Polymerization by Free Radical Mechanism – Involves three primary steps • Initiation- formation of free radicals through homolytic dissociation of weak bonds (e.g., peroxides). Results in opening up unsaturated (C=C) bonds to saturated (C-C) bonds) • Propagation- formation of long chain polymers of the now free C-C bonds • Termination- reactions at the ends of the polymer cause C-C to terminate with a functional group that does not have any free electrons to bond with and results in unsaturated end group (C- C=CX)
  • 39.
    39 Chain Growth (Addition) Polymerization •Special case of Diene polymerization – Very important in elastomers- mostly addition – Polydienes are the backbone of the synthetic rubber are produced by free radical polymerization – Early attempts of polymerization was slow and produced low molecular weight polymers (oils) – Emulsion polymerization (1930s) was introduced to speed up polymerization and higher Molecular weights
  • 40.
    40 Polymerization Methods • 4Methods to produce polymers – Some polymers have been produced by all four methods • PE, PP and PVC are can be produced by several of these methods • The choice of method depends upon the final polymer form, the intrinsic polymer arrangement (isotactic, atactic, etc), and the yield and throughput of the polymer desired. – Bulk Polymerization – Solution Polymerization – Suspension Polymerization – Emulsion Polymerization
  • 41.
    41 Formation of Polymers •Polymers from Addition reaction – LDPE HDPE PP – PVC PS C C H H H H n C C H H H H n C C H CH3 H H n C C H Cl H H n C C H H H n
  • 42.
    42 Other Addition Polymers •Vinyl- Large group of addition polymers with the formula: – Radicals (X,Y) may be attached to this repeating vinyl group as side groups to form several related polymers. • Polyvinyls – Polyvinyl chloride – Polyvinyl dichloride (polyvinylidene chloride) – Polyvinyl Acetate (PVAc) C C H X H Y or C C H X H H CC H Cl H H C C H Cl H Cl C C H OCOCH3 H H
  • 43.
    43 Manufacturing of EmulsionSBR • Free-radical emulsion process – Developed in 1930s and still in use – Typical process (Figure) • Soap stabilized water emulsion of two monomers is converted in a train of 10 continuous reactors (4000 gallons each) • Water, butadiene, styrene, soaps, initiators, buffers, and modifier are fed continuously • Temp is 5 to 10°C and conversion proceeds until 60% of the reactants have polymerized in the last reactor. • Shortstop is added in the emulsion to stop the conversion at 60% • Unreacted butadiene is flashed off with steam and recycled • Unreacted styrene is stripped off in a distillation column that separates liquid rubber emulsion from the gas styrene. • Rubber is recovered from the latex in a series of operations. – Introduction of antioxidants, blending with oils, dilution with brine, coagulation, dewatering, drying, and packaging the rubber
  • 44.
    44 Manufacturing of EmulsionSBR • Polymerization – Cold SBR: at 5 to 10°C is called the cold process, • Better abrasion resistant, treadwear, and dynamic properties. – Hot SBR: at about 50°C is called the hot process. • Conversion is allowed to proceed to 70% • Higher branching occurs and incipient gelation. – Typical SBR recipes, Table from Morton’s Rubber technology
  • 45.
    45 Manufacturing of EmulsionSBR • Compounding and Processing – Similar to natural rubber – Materials for large scale use, e.g., tires, based on • Rubber, fillers (carbon black), extending oils, zinc oxide, sulfur, accelerators, antioxidants, antiozonants, and waxes. – Materials are mixed in a mill or twin rollers or calendered – Processing into smooth compounds that can be quickly pressed, sheeted, calendered, or extruded • Recipes – Large parts, e.g., tires and hoses, are given in Tables 7.6, 7.7, 7.8, and 7.9
  • 46.
    46 Polymerization of Elastomers •Butadiene-Acrylonitrile (Nitrile) Rubber – Produced by emulsion polymerization – Nitrile rubbers have nitrile contents from 10 to 40%. • Chloroprene rubber – Produced by emulsion polymerization – Produced as a homopolymer that has a high trans 1,4 chain structure and is susceptible to strain-induced crystallization, much like natural rubber. • Leads to high tensile strength – Does not lead itself to copolymerization
  • 47.
    47 Polymerization of Elastomers •Butyl Rubber- – Only important commercial rubber prepared by cationic polymerization • Processes with AlCl at –98 to –90°C – Copolymer of isobutene and isoprene with isoprene used in 1.5 % quantities • The isoprene is introduced to provide sufficient unsaturations for sulfur vulcanization. – MW is in the range of 300,000 to 500,000
  • 48.
    48 Processing of Elastomers •Rubber Products – 50% of all rubber produced goes into automobile tires; – 50% goes into mechanical parts such as • mountings, gaskets, belts, and hoses, as well as • consumer products such as shoes, clothing, furniture, and toys • Elastomers and Rubbers – Thermoset rubbers • Compounding the ingredients in recipe into the raw rubber with a mill, calender, or Banbury (internal) mixer • Compression molding of tires – Thermoplastic elastomers • Compression molding, extrusion, injection molding, casting.
  • 49.
    49 Processing of Elastomers •Rubber Processors – Mills and Banbury mixers
  • 50.
    50 Compression Molding Process •Materials •Elastomers: •Thermoplastic •Thermoplastic Olefin (TPO), Thermoplastic Elastomer (TPE), Thermoplastic Rubber (TPR) •Thermoset rubbers •Styrene Butadiene Rubber, isoprene Thermoplastic: Heat Plastic prior to molding Thermosets: Heat Mold during molding
  • 51.
    51 Polyurethane Processing • Polyurethanecan be processed by – Slow process: Casting or foaming, or – Fast process: Reaction Injection Molding (RIM)
  • 52.
    52 Injection Molding GlassElastomers • Plastic pellets with copolymer elastomers. – Similar processing requirements as with injection molding of commodity and engineering plastics • Injection pressures, tonnage, pack pressure, shrinkage
  • 53.
    53 Transfer Molding ofRubbers • Transfer molding is a process by which uncured rubber compound is transferred from a holding vessel (transfer pot) to the mold cavities using a hydraulically operated piston. Transfer molding is especially conducive to multicavity designs and can produce nearly flashless parts.
  • 54.
    54 Calendering of Rubbers •Calendering is the process for producing long runs of uniform thickness sheets of rubber either unsupported or on a fabric backing. A standard 3 or 4 roll calender with linear speed range of 2 to 10 feet/minute is typical for silicone rubber. Firm compound with good green strength and resistance to overmilling works the best for calendering.
  • 55.
    55 Curing of Rubbers •Extruded profile may be cured by hot air vulcanization (HAV), steam vulcanization (CV) or liquid-medium cure. HAV consists of a heated tunnel through which the profile is fed continuously on a moving conveyor. Air temperature reaches 600°F to 1200°F, and cure times are usually short, on the order of 3 to 12 seconds. The recommended curing agents are DCBP-50 or addition cure, both of which provide rapid cure with no porosity. • Steam cure commonly refers to the steam curing systems used by the wire and cable industry and consists of chambers 4” – 6” in diameter and 100 – 150 feet in length. Steam pressure varies from 50 psig to 225 psig depending on wall thickness of the insulation. • For liquid-medium cure, continuous lengths of extruded profile are fed into a bath of moltenmaterial (salt or lead) which cures the extrudate.
  • 56.
    56 Polymer Length • PolymerLength – Polymer notation represents the repeating group • Example, -[A]-n where A is the repeating monomer and n represents the number of repeating units. • Molecular Weight – Way to measure the average chain length of the polymer – Defined as sum of the atomic weights of each of the atoms in the molecule. • Example, – Water (H2O) is 2 H (1g) and one O (16g) = 2*(1) + 1*(16)= 18g/mole – Methane CH4 is 1 C (12g) and 4 H (1g)= 1*(12) + 4 *(1) = 16g/mole – Polyethylene -(C2H4)-1000= 2 C (12g) + 4H (1g) = 28g/mole * 1000 = 28,000 g/mole
  • 57.
    57 Molecular Weight • AverageMolecular Weight – Polymers are made up of many molecular weights or a distribution of chain lengths. • The polymer is comprised of a bag of worms of the same repeating unit, ethylene (C2H4) with different lengths; some longer than others. • Example, – Polyethylene -(C2H4)-1000 has some chains (worms) with 1001 repeating ethylene units, some with 1010 ethylene units, some with 999 repeating units, and some with 990 repeating units. – The average number of repeating units or chain length is 1000 repeating ethylene units for a molecular weight of 28*1000 or 28,000 g/mole .
  • 58.
    58 Molecular Weight • AverageMolecular Weight – Distribution of values is useful statistical way to characterize polymers. • For example, – Value could be the heights of students in a room. – Distribution is determined by counting the number of students in the class of each height. – The distribution can be visualized by plotting the number of students on the x-axis and the various heights on the y-axis. Histogram of Heights of Students 0 5 10 15 20 25 60 70 80 Height, inches Frequency Series1
  • 59.
    59 Molecular Weight • MolecularWeight Distribution – Count the number of molecules of each molecular weight – The molecular weights are counted in values or groups that have similar lengths, e.g., between 100,000 and 110,000 • For example, – Group the heights of students between 65 and 70 inches in one group, 70 to 75 inches in another group, 75 and 80 inches in another group. • The groups are on the x-axis and the frequency on the y-axis. • The counting cells are rectangles with the width the spread of the cells and the height is the frequency or number of molecules • Figure 3.1 • A curve is drawn representing the overall shape of the plot by connecting the tops of each of the cells at their midpoints. • The curve is called the Molecular Weight Distribution (MWD)
  • 60.
    60 Molecular Weight • AverageMolecular Weight – Determined by summing the weights of all of the chains and then dividing by the total number of chains. – Average molecular weight is an important method of characterizing polymers. – 3 ways to represent Average molecular weight • Number average molecular weight • Weight average molecular weight • Z-average molecular weight
  • 61.
    61 Gel Permeation Chromatography •GPC Used to measure Molecular Weights – form of size-exclusion chromatography – smallest molecules pass through bead pores, resulting in a relatively long flow path – largest molecules flow around beads, resulting in a relatively short flow path – chromatogram obtained shows intensity vs. elution volume – correct pore sizes and solvent critical
  • 62.
  • 63.
    63 Number Average MolecularWeight, Mn • • where Mi is the molecular weight of that species (on the x-axis) • where Ni is the number of molecules of a particular molecular species I (on the y-axis). – Number Average Molecular Weight gives the same weight to all polymer lengths, long and short. • Example, What is the molecular weight of a polymer sample in which the polymers molecules are divided into 5 categories. – Group Frequency – 50,000 1 – 100,000 4 – 200,000 5 – 500,000 3 – 700,000 1 ... ... 321 332211 +++ +++ == ∑ ∑ NNN MNMNMN N MN M i ii n 000,260 )13541( )700(1)500(3)200(5)100(4)50(1 ... ... 321 332211 = ++++ ++++ = +++ +++ == ∑ ∑ n n i ii n M KKKKK M NNN MNMNMN N MN M
  • 64.
    64 Molecular Weight • NumberAverage Molecular Weight. Figure 3.2 – The data yields a nonsymmetrical curve (common) – The curve is skewed with a tail towards the high MW – The Mn is determined experimentally by analyzing the number of end groups (which permit the determination of the number of chains) – The number of repeating units, n, can be found by the ratio of the Mn and the molecualr weight of the repeating unit, M0, for example for polyethylene, M0 = 28 g/mole – The number of repeating units, n, is often called the degree of polymerization, DP. – DP relates the amount of monomer that has been converted to polymer. 0M M n n =
  • 65.
    65 Weight Average MolecularWeight, Mw • Weight Average Molecular Weight, Mw – Favors large molecules versus small ones – Useful for understanding polymer properties that relate to the weight of the polymer, e.g., penetration through a membrane or light scattering. – Example, • Same data as before would give a higher value for the Molecular Weight. Or, Mw = 420,000 g/mole ... ... 332211 2 33 2 22 2 11 2 +++ +++ == ∑ ∑ MNMNMN MNMNMN MN MN M ii ii w
  • 66.
    66 Z- Average MolecularWeight – Emphasizes large molecules even more than Mw – Useful for some calculations involving mechanical properties. – Method uses a centrifuge to separate the polymer ... ... 2 33 2 22 2 11 3 33 3 22 3 11 2 3 +++ +++ == ∑ ∑ MNMNMN MNMNMN MN MN M ii ii z
  • 67.
    67 Molecular Weight Distribution •Molecular Weight Distribution represents the frequency of the polymer lengths • The frequency can be Narrow or Broad, Fig 3.3 • Narrow distribution represents polymers of about the same length. • Broad distribution represents polymers with varying lengths • MW distribution is controlled by the conditions during polymerization • MW distributions can be symmetrical or skewed.
  • 68.
    68 Physical and MechanicalProperty Implications of MW and MWD • Higher MW increases • Tensile Strength, impact toughness, creep resistance, and melting temperature. – Due to entanglement, which is wrapping of polymer chains around each other. – Higher MW implies higher entanglement which yields higher mechanical properties. – Entanglement results in similar forces as secondary or hydrogen bonding, which require lower energy to break than crosslinks.
  • 69.
    69 Physical and MechanicalProperty Implications of MW and MWD • Higher MW increases tensile strength • Resistance to an applied load pulling in opposite directions • Tension forces cause the polymers to align and reduce the number of entanglements. If the polymer has many entanglements, the force would be greater. • Broader MW Distribution decreases tensile strength • Broad MW distribution represents polymer with many shorter molecules which are not as entangled and slide easily. • Higher MW increases impact strength • Impact toughness or impact strength are increased with longer polymer chains because the energy is transmitted down chain. • Broader MW Distribution decreases impact strength • Shorter chains do not transmit as much energy during impact
  • 70.
    70 Thermal Property Implicationsof MW & MWD • Higher MW increases Melting Point • Melting point is a measure of the amount of energy necessary to have molecules slide freely past one another. • If the polymer has many entanglements, the energy required would be greater. • Low molecular weights reduce melting point and increase ease of processing. • Broader MW Distribution decreases Melting Point • Broad MW distribution represents polymer with many shorter molecules which are not as entangled and melt sooner. • Broad MW distribution yields an easier processed polymer Mechanical Properties Melting Point * Decomposition
  • 71.
    71 Example of HighMolecular Weight • Ultra High Molecular Weight Polyethylene (UHWMPE) • Modifying the MWD of Polyethylene yields a polymer with – Extremely long polymer chains with narrow distribution – Excellent strength – Excellent toughness and high melting point. • Material works well in injection molding (though high melt T) • Does not work well in extrusion or blow molding, which require high melt strength. • Melt temperature range is narrow and tough to process. • Properties improved if lower MW polyethylene – Acts as a low-melting lubricant – Provides bimodal distributions, Figure 3.5 – Provides a hybrid material with hybrid properties