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Polymer Synthesis CHEM 421 Chapter 3.9 (Odian). Polymer Synthesis CHEM 421 Free Radically Polymerized Monomers.

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Presentation on theme: "Polymer Synthesis CHEM 421 Chapter 3.9 (Odian). Polymer Synthesis CHEM 421 Free Radically Polymerized Monomers."— Presentation transcript:

1 Polymer Synthesis CHEM 421 Chapter 3.9 (Odian)

2 Polymer Synthesis CHEM 421 Free Radically Polymerized Monomers

3 Polymer Synthesis CHEM 421 Thermodynamics of Chain Polymerizations Relief of “strain” is the driving force –Exothermic process

4 Polymer Synthesis CHEM 421 Thermodynamics ΔG, ΔH, and ΔS ΔG = ΔH - T ΔS Chain polymerizations: »Enthalpy »Exothermic (- ΔH) »Entropy »Negative ΔS Polymer favored from enthalpic considerations but un-favored from entropic considerations

5 Polymer Synthesis CHEM 421 Thermodynamics ΔH polymerization depends upon differences in: –Resonance stabilization of polymer versus the monomer –Steric strain in monomer versus the polymer –Hydrogen bonding or dipolar interaction in monomer versus the polymer

6 Polymer Synthesis CHEM 421 Thermodynamic Trends Ethylene Styrene α-Methyl styrene or Ethylene methyl acrylate methyl methacrylate PTFE (!) –Most exothermic polymerization known (kJ/mole) (J/°K-mole)

7 Polymer Synthesis CHEM 421 Equilibrium Considerations For most polymerizations, there is a temperature where the reaction becomes reversible The position for the monomer / polymer equilibrium will be dependent on the temperature ΔG = ΔH - T ΔS –Polymerization:ΔS = –De-polymerization:ΔS = With increasing temperature the equilibrium will shift? k p k dp

8 Polymer Synthesis CHEM 421 Equilibrium Considerations When R p = R dp –Ceiling temperature

9 Polymer Synthesis CHEM 421 Thermodynamics The reaction isotherm: ΔG = ΔG° + RTlnK is applicable. Where ΔG° is the ΔG of polymerization for the monomer and the polymer in the appropriate standard states –Monomer Std. State: pure liquid –Polymer Std. State: crystalline state if possible, otherwise amorphous state

10 Polymer Synthesis CHEM 421 Thermodynamics At equilibrium, ΔG = 0 by definition: ΔG° = - RTlnK Equilibrium constant is defined by K eq = k p / k dp K eq = ————— = ——— [M n+1] [M n][M] 1

11 Polymer Synthesis CHEM 421 Thermodynamics Combine: [M] c is the equilibrium monomer concentration as a function of reaction temperature –The monomer concentration in equilibrium with the polymer increases as the temperature increases T c = ————— ΔH° ΔS° + Rln[M] c

12 Polymer Synthesis CHEM 421 Ceiling Temperature Poly(α-methyl styrene) –T g = 170 °C –T ceil = 61 °C Processing temperature?

13 Polymer Synthesis CHEM 421 Ceiling Temperature Poly(methyl methacrylate) –T g = 125 °C –T ceil = 164 °C Recycle… PMMA 99% MMA monomer 300 °C

14 Polymer Synthesis CHEM 421 Heats of Polymerization and Ceiling Temperatures MonomerHeat of Polymerization (kcal/mol) Ceiling Temperature (°C) Styrene-16235 α-Methyl styrene-761 Methyl acrylate-20---- Methyl methacrylate-13164 Ethylene-26407 Propylene-21300 Isobutene-1750

15 Polymer Synthesis CHEM 421 Polymerization Processes Solution Polymerization Bulk (Mass) Polymerization Heterogeneous Polymerizations

16 Polymer Synthesis CHEM 421 Solution Polymerizations Ingredients –Monomer –Solvent –Initiator R p = k p [M] ( k d f [ I ] / k t ) 1/2 k p [M] 2 (k t k d f [I] ) 1/2 = ————— k p [M] [M] 2 k t [M] 2 = ——— R p R i R t ٧ = — = —

17 Polymer Synthesis CHEM 421 Solution Polymerization Solvent, monomer & initiator Polymer remains soluble in the solvent Easy temperature, viscosity, MW control Free radical kinetics apply Solvent M MM M M M M M M M I I I I I hνhν or Δ Solvent M M M M I I I P P P P P P P P

18 Polymer Synthesis CHEM 421 Solution Polymerization Considerations: –Chain transfer to solvent –Purity of polymer (difficulty in removing solvent) Used for: vinyl acetate, acrylonitrile, and esters of acrylic acid

19 Polymer Synthesis CHEM 421 Bulk (Mass) Polymerizations Ingredients: Monomer and Initiator only Kinetics follows solution polymerization kinetics…R p and ٧

20 Polymer Synthesis CHEM 421 Bulk (Mass) Polymerization Considerations: –Hard to control: high activation energies, gel effect –Equipment: elaborate, strong stirring due to viscosity increase –Temperature Control: local hot spots »Can lead to degradation, discoloration, and broad MW distribution »“Runaway” reactions –Used for styrene and methyl methacrylate (Chain Growth) »Low conversion and separation/recycling of un-reacted monomer


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