2. Polymer Synthesis
CHEM 421
Emulsion Polymerizations
• Economically important
• Western countries 108
tons/year
• 30% of all polymers made by free radical
methods
–emulsion polymers accounts for 40-50% of
this
• First employed during WWII for
production of synthetic rubber
• Today: MMA, VC, vinylidene chloride,
styrene, fluoropolymers, vinyl acetate,
EVA, SA, SBR, chloroprene, etc
10. Polymer Synthesis
CHEM 421
Before Initiation
I
I
I
I
I
I
I I
I
M
M
M
M
M
M
M
M
M M
MM
M
M
M
M
M
M
M
Monomer Droplet
ca. 1 micron diameter
conc = 1011
/mL
stabilized by soap
Micelle Containing
Monomer
ca. 75 Å diameter
conc = 1018
/mL
Relative surface area
1 : 560
Initiation of micelles
statistically favored
11. Polymer Synthesis
CHEM 421
Interval One:
0 – 15 % Conversion
I •
I
I
I
I
I
I • I
I
M
M
M
M
M
M M
M
M
M
MM
M
PP••
PP••
M M
Micelles
Containing
Monomer
Active
latex particle
Micelles
Containing
Monomer
Micelles
Containing
Monomer
Active
latex particles
Inactive
latex particles
Inactive
latex particles
12. Polymer Synthesis
CHEM 421
Qualitative Details
Conversion Micelles Monomer
Droplets
Particle
Number
Particle
Size
Comments
I
0 – 15% present present increases increases
Nucleation
period,
Increasing
Rp
II
III
13. Polymer Synthesis
CHEM 421
Interval Two:
15 – 80% Conversion
I
I
I
I
I • I
I
M
M
M
M
M
M
MM
M
PP••
PP•• I •
I
M
M
PP••
Inactive
latex particles
Inactive
latex particles
Inactive
latex particles
Active
latex particles
Active
latex particles
I •
I
M
PP••
Active
latex particles
No
micelles
Number of
particles
constant,
therefore
Rp = constant
15. Polymer Synthesis
CHEM 421
Qualitative Details
Conversion Micelles Monomer
Droplets
Particle
Number
Particle
Size
Comments
I
0 – 15% present present increases increases
Nucleation
period,
Increasing
Rp
II
15 – 80% absent present constant increases
Constant #
of particles,
Cp =
constant
III
16. Polymer Synthesis
CHEM 421
Interval Three:
80 – 100% Conversion
I
I
I
I
I • I
M
M
M
M
M
M
M
PP••
PP••
I
M
M
PP••
I •
M
PP••
M
PP••
M
PP••
I •
No
monomer
droplets
No
micelles
17. Polymer Synthesis
CHEM 421
Qualitative Details
Conversion Micelles Monomer
Droplets
Particle
Number
Particle
Size
Comments
I
0 – 15% present present increases increases
Nucleation
period,
Increasing
Rp
II
15 – 80% absent present constant increases
Constant #
of particles,
Cp =
constant
III
80 – 100% absent absent constant roughly
constant
Constant #
of particles,
Cp =
decreasing
18. Polymer Synthesis
CHEM 421
Emulsion Polymerization Kinetics
• Once inside a particle, radical propagates
as rp = kp[M]
• Overall rate: Rp = kp[M][P.
]
• [P.
] = N’ñ (where N’ = the sum of micelle
and particle concentrations and
ñ = average # of radicals per particle)
• Therefore,
–Increase N’ to increase rate!
][' MknNR pp =
19. Polymer Synthesis
CHEM 421
Emulsion Kinetics, cont.
• Smith-Ewart Kinetics:
–Case 2: ñ = 0.5 (MOST CASES!)
» 1 radical per particle
» Half of the particles active, half not active
–Case 1: ñ<0.5
» Radical can diffuse out of the particle
» Monomer with higher water solubility
–Case 3: ñ>0.5
» Termination constant is low
» High viscosity, initiator; large particles
20. Polymer Synthesis
CHEM 421
Emulsion Polymerization Kinetics
• How to increase Rp?
–Increase N’ to increase rate
»Increase surfactant concentration to increase N’
][' MknNR pp =
21. Polymer Synthesis
CHEM 421
Molecular Weight in Emulsion
Polymerizations
• Molecular weight determined by rate of growth
of a chain divided by rate of radical entry (ri)
–How to increase molecular weight?
DP
rp
= ——ri
Ri
= ——
N
ri = kp[M]rp
N kp [M]
Ri
= ———DP
22. Polymer Synthesis
CHEM 421
Free Radical Solution
Polymerizations
• Recall
– To increase molecular weight…
» Increase monomer concentration
» Decrease initiator concentration
– To increase Rate of Polymerization
» Increase monomer concentration
» Increase initiator concentration
٧ =
kp [M]
2 (kt kd f [I])1/2
= —————
Can’t do
both!
Rp = kp [M] (kd f [I] / kt)1/2