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LIST OF ARTICLES ON THERMODYNAMICS OF POLYMERIZATION BY HIDEO SAWADA PUBLISHED IN POLYMER REVIEWS Sawada, Hideo (1969) 'Thermodynamics of Polymerization. I', Polymer Reviews, 3, 313 — 338 DOI: 10.1080/15583726908545926 URL: http://dx.doi.org/10.1080/15583726908545926 Sawada, Hideo (1969) 'Chapter 2. Heat of Polymerization', Polymer Reviews, 3, 339 — 356 DOI: 10.1080/15583726908545927 URL: http://dx.doi.org/10.1080/15583726908545927 Sawada, Hideo (1969) 'Chapter 3. Thermodynamics of Radical Polymerization', Polymer Reviews, 3, 357 — 386 DOI: 10.1080/15583726908545928 URL: http://dx.doi.org/10.1080/15583726908545928 Sawada, Hideo ((1969) 'Chapter 4. Thermodynamics of Polycondensation', Polymer Reviews, 3, 387 — 395 DOI: 10.1080/15583726908545929 URL: http://dx.doi.org/10.1080/15583726908545929 Sawada, Hideo (1970) 'Thermodynamics of Polymerization. II. Thermodynamics of Ring- Opening Polymerization', Polymer Reviews, 5, 151 — 173 DOI: 10.1080/15583727008085366 URL: http://dx.doi.org/10.1080/15583727008085366 Sawada, Hideo (1972) 'Thermodynamics of Polymerization. III', Polymer Reviews, 7, 161 — 187 DOI: 10.1080/15321797208068162 URL: http://dx.doi.org/10.1080/15321797208068162 Sawada, Hideo (1972) 'Thermodynamics of Polymerization. IV. Thermodynamics of Equilibrium Polymerization', Polymer Reviews, 8, 235 — 288 DOI: 10.1080/15321797208068172 URL: http://dx.doi.org/10.1080/15321797208068172 Sawada, Hideo (1974) 'Thermodynamics of Polymerization. V. Thermodynamics of Copolymerization. Part I', Polymer Reviews, 10, 293 — 353 DOI: 10.1080/15321797408076101 URL: http://dx.doi.org/10.1080/15321797408076101 Sawada, Hideo (1974) 'Thermodynamics of Polymerization. VI. Thermodynamics of Copolymerization. Part 2', Polymer Reviews, 11, 257 — 297 DOI: 10.1080/15583727408546025 URL: http://dx.doi.org/10.1080/15583727408546025 Table of Contents Thermodynamics of Polymerization. I 5 Chapter 1. Introductory Survey 5 I. THE CEILING TEMPERATURE CONCEPT 6 A. Thermodynamic Approach 6 B. Kinetic Approach 7 C. Determination of Ceiling Temperatures 11 II. ENTROPY AND FREE ENERGY CHANGES OF POLYMERIZATION 14 A. Entropy of Polymerization 14 B. Determination of Entropy of Polymerization 16 C. Free Energy Changes of Polymerization 22 REFERENCES 29 Chapter 2. Heat of Polymerization 31 I. GENERAL ASPECTS 31 A. Breaking a Multiple Bond 32 B. Resonance 32 C. Steric Strain 33 II. VARIATIONS IN HEATS OF POLYMERIZATION 33 A. Steric Strain in the Polymer 35 B. Conjugation and Hyperconjugation 38 C. Hydrogen Bond and Solvation 39 III. EMPIRICAL ESTIMATION OF HEAT OF POLYMERIZATION 39 REFERENCES 41 APPENDIX 42 Chapter 3. Thermodynamics of Radical Polymerization 49 I. GENERAL ASPECTS 50 A. Energetics of Radical Polymerization 50 B. Degree of Polymerization 51 C. Activation Energies of Elementary Reactions 53 II. GENERATION OF FREE RADICALS 53 III. PROPAGATION REACTION 58 A. The Polanyi Relation 58 B. Reactivity and Heat of Polymerization 60 C. Ceiling Temperature 63 IV. INTERACTION OF RADICALS 63 A. Combination and Disproportionation Reactions 63 B. Interaction of Small Hydrocarbon Radicals 64 C. Interaction of Large Hydrocarbon Radicals 65 D. Interaction of Some Large Radicals 66 V. FREE ENERGIES OF FORMATION OF POLYETHYLENE AND POLYTETRAFLUOROETHYLENE 68 A. Free Energies of Polyethylene Synthesis 68 B. Free Energies of Polytetrafluoroethylene Synthesis 73 REFERENCES 77 Chapter 4. Thermodynamics of Polycondensation 79 I. GENERAL ASPECTS 79 II. DEGREE OF POLYMERIZATION 80 III. EQUILIBRIUM CONSTANT 81 IV. RING FORMATION IN POLYCONDENSATION 86 ACKNOWLEDGMENTS 87 References 87 Thermodynamics of Polymerization. II. Thermodynamics of Ring-Opening Polymerization 88 I. GENERAL ASPECTS 88 II. HOMOCYCLIC COMPOUNDS 89 A. Angle Strain 89 B. Conformational and Transannular Strain 99 C. Steric Effect of Side Group 100 III. HETEROCYCLIC COMPOUNDS 102 A. Cyclic Ethers 103 B. Lactams 105 C. Lactones 107 D. Miscellaneous Heterocyclic Compounds 107 IV. SUMMARY 109 ACKNOWLEDGMENTS 109 References 109 Thermodynamics of Polymerization. III (Cationic Polymerization) 111 I. GENERAL ASPECTS 112 II. FORMATION OF CARBONIUM ION 114 A. Ionization Potential 114 B. Proton Affinity 115 C. Acidity 118 D. Free Energy Change of Formation of Carbonium Ion 119 E. Ions and Ion Pairs 121 F. Energetics of Salvation 122 III. INITIATION OF CATIONIC POLYMERIZATION 124 A. Energetic Consideration of Initiation Reaction by Halogen Acid 124 B. Catalytic Activity in Cationic Polymerization by Lewis Acids 126 IV. PROPAGATION OF CATIONIC POLYMERIZATION 127 A. Energetics 127 B. Heats of Reaction of Cations with Olefins 129 C. Activation Entropy Changes of Propagation 132 D. Thermodynamics of Formation of Zwitterions 134 V. CHAIN TRANSFER AND TERMINATION 136 Acknowledgments 136 References 136 Thermodynamics of Polymerization. IV. Thermodynamics of Equilibrium Polymerization 138 I. POSSIBLE TYPES OF EQUILIBRIUM POLYMERIZATION 139 II. SOME CASE STUDIES OF EQUILIBRIUM POLYMERIZATION 146 A. Vinyl Polymerizations 147 B. Ring-Opening Polymerizations 150 C. Polymerization of Aldehydes 165 III. TRANSITION PHENOMENA IN EQUILIBRIUM POLYMERIZATION 167 IV. MOLECULAR WEIGHT DISTRIBUTION 173 A. Equilibrium Polymerization 173 B. Living Polymerization 179 V, THERMODYNAMICS OF EQUILIBRIUM POLYMERIZATION 183 Acknowledgment 188 References 189 Thermodynamics of Polymerization. V. Thermodynamics of Copolymerization. Part I 192 I. THE GENERAL THEORY OF BINARY COPOLYMERIZATION 193 A. Heat of Copolymerization 193 B. Entropy of Copolymerization 200 C. Equilibrium Sequence Distribution 203 D. Free Energy Change in Binary Copolymerization System 209 E. Equilibrium Monomer Concentration 217 F. Penultimate Unit Effect 222 II. DEGREE OF POLYMERIZATION AND COPOLYMER COMPOSITION OF BINARY COPOLYMERIZATION SYSTEM 224 A. Degree of Polymerization 224 B. Copolymer Composition Equation 228 III. MULTICOMPONENT COPOLYMERIZATION 243 A. Heat of Terpolymerization 243 B. General Theory of Multicomponent Copolymerization 248 Acknowledgment 250 References 251 Thermodynamics of Polymerization. VI. Thermodynamics of Copolymerization. Part 2 253 I. RADICAL COPOLYMERIZATION 254 A. Heat of Copolymerization 254 B. Ceiling Temperature 259 C. Q-e Scheme 263 D. Substituent Effect 265 E. Effect of Polymerization Temperature 268 F. Effect of Solvent 272 II. IONIC COPOLYMERIZATION 274 A. Energetic Characteristics 274 B. Reactivity 279 C. Effect of Polymerization Temperature 280 III. OTHER COPOLYMERIZATIONS 282 A. Ring-Opening Copolymerization 282 B. Miscellaneous Copolymerizations 284 Acknowledgment 290 References 290 Thermodynamics of Polymerization. I HIDEO SAWADA Central Research Laboratory Daicel Ltd. Tsunigaoka, Oi, Intmagwi Saitama, Japan Chapter 1. Introductory Survey I. THE CEILING TEMPERATURE CONCEPT 314 A. Thermodynamic Approach ; 314 B. Kinetic Approach 315 C. Determination of Ceiling Temperatures 319 II. ENTROPY AND FREE ENERGY CHANGES OF POLYM- ERIZATION 322 A. Entropy of Polymerization 322 B. Determination of Entropy of Polymerization 324 C. Free Energy Changes of Polymerization 330 REFERENCES 337 313 314 HIDEO SAWADA I. THE CEILING TEMPERATURE CONCEPT A. Thermodynamic Approach The Gib'bs free energy of a system at temperature T is defined as G = H - TS (1) where H is the enthalpy and S the entropy of the system. The free energy change for any polymerization will be, therefore, AG = Gpoiymer ~ G monomer = "polymer ~ H — T^Spoiyj^ej.— S ) (2) monomer monomer = AH -T AS p When the polymer has a lower free energy than the initial mono- mer, a polymerization can occur spontaneously, and the sign of AG is negative. A positive sign for AG signifies, therefore, that the polymerization is not spontaneous. When the system is in equilib- rium at a certain critical temperature, there is no tendency for polymerization, and, hence, AG = 0 [1-3]. This temperature is known as the ceiling temperature. These three possible conditions for free energy change of polymerization may be summarized as follows: monomer — polymer AG = - (spontaneous) monomer — polymer AG = + (nonspontaneous) monomer — polymer AG = 0 (equilibrium) At the ceiling temperature, T , AG is zero, so that c T = AHp/AS (3) c p where AHp and ASp are the enthalpy and entropy changes per mono- mer unit. When the polymer chains are long these quantities are identical with the heat and entropy changes of polymerization. If the standard state refers to unit concentration and the monomer behaves ideally, AS = AS° + R In [M]; thus T AS° + R In [M] (4) THERMODYNAMICS OF POLYMERIZATION. I 315 where AS0 is the entropy change accompanying polymerization at the standard state when the concentration of monomer is unity. There- fore, T can be raised by increasing the concentration of monomer c when a solvent is present. Equation (4) emphasizes that T is char- c acteristic of monomer-polymer equilibrium only and is quite inde- pendent of the monomer or the nature of the active centers in the system; for a given value of [M], the ceiling temperature should, therefore, be the same whether the active centers are radicals or ions. Many polymers are stable even above the ceiling temperature only because of the difficulty of initiating degradative centers on the polymer molecule. In practice, terminated polymer appears stable at temperatures above the ceiling temperature, being in a state of metastable equilibrium. Therefore, the polymer cannot depolymerize spontaneously but can do so under appropriate conditions. Catalyst residues that are not removed during the purification of a polymer may also cause depolymerization reaction. There are four important possibilities of polymerization as follows: a. In addition polymerization, AH and AS are usually both nega- tive, and so AG becomes positive above the ceiling temperature of the system. Thus, the high polymer cannot be formed above the ceil- ing temperature. b. If the polymerization is endothermic (AH > 0) and AS is greater than zero, no polymer can exist below a floor temperature, above which AG becomes negative. The phenomenon of floor temperature is exhibited by the polymerization of S rings. 8 c. When AH is positive and AS negative, AG is always positive; therefore, polymer cannot exist at any temperature. d. When AH is negative and AS positive, AG is always negative; therefore, polymer can exist at any temperature. B. Kinetic Approach It is interesting to consider the ceiling temperature phenomenon from a kinetic point of view [1,3]. At ordinary temperatures the rate constant for depolymerization is small. However, the activation energy of this rate constant is quite high (10-26 kcal/mole) compared to that for propagation, and at high temperature the depolymerization can become important compared with the polymerization. Let us consider the propagation reaction p k^ AAAARn*i 316 HIDEO SAWADA The rate constants for propagation and depropagation reactions can be expressed as k = A exp(-E /RT), k = A exp(-E /RT) p p p d d d where A and A are the collision frequency factors which approxi- p d mate to the entropy of activation, and E and E are the activation p d energies for polymerization and depolymerization, respectively. If the degree of polymerization is large, E - E = AHp. For long p d chains, AHp is equal to the heat of the overall polymerization. The rate of propagation is essentially the same as the overall rate of disappearance of monomer, since the number of monomers used in chain transfer and initiation must be small compared to that used in propagation if the polymer chains are long. Therefore, ^I (5) where [M*] is the concentration of propagating species, and [M] is the concentration of monomer. Depolymerization may now be considered to be the reverse of propagation, then vd = kdtMnl (6 Thus the overall rate of polymerization is The degree of polymerization is given by the rate of polymerization divided by the rate of termination, i.e., _ (k -k [M])[M d p n] (8) f([M ]) n where f([M*]) is a function of the number of active centers, M*, present. AHp is usually negative (the polymerization is exothermic), and so E is usually much larger than E . Therefore, although k may d p d be negligible compared with kp[M] at ordinary temperature, it will increase more rapidly with increasing temperature. At the ceiling temperature T the rate of depropagation becomes c THERMODYNAMICS OF POLYMERIZATION. equal to that of propagation, regardless of the variations of [MJ^] and ) with temperature, k [M*][M] = p which can also be written in the form: A exp(-E /RT )[M] = A exp(-E /RT ) (9) p p c d d c and, therefore, Ep - E AH d p Tc - R In (A [M]/A ) ~ R In (A [M]/A ) U0) p d p d At this temperature, the extrapolated Rp vs T and DP vs T curves will cut the temperature axis. This is illustrated in Fig. 1.1. At temperatures that are not far below the ceiling temperature, only polymers of low molecular weight form. It seems to be impossible to predict the variations of Rp and DP with temperature right up to T from Eqs. (7) and (8). When k ap- c d proaches kp[M ], DP becomes small and consumption of monomer x in the initiation process is no longer negligible. Then, k and k p d may show a dependence on DP. Nevertheless the limiting slope of dRp/dT as T approaches T may be numerically so large that such c effects are of very minor importance and operate only over the last fraction of a degree below T . The limiting slope for the rate vs c temperature curve can be obtained by differentiating Eq. (7) with respect to temperature: dR /dT = [M*](k [M]E /RT*-k E /RT2) p p p d d + (k [M]-k )d[M*]/dT p d and substituting k [M] = k when T = T : p d c lim (dR /dT) = k [M][M*] (E - E )/RT T c p p p d C (n) = k [M][M*]AH /RT p p c Then k[M][Mj![] is the rate that would have been observed at T in p c the absence of depropagation. From transition state theory the frequency factor is given by A = (kT/h) exp(AS*/R). Therefore,

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