
Understanding Modeling and Simulation of Polymerization Reactions
Description
Alles über E-Books | Antworten auf Fragen rund um E-Books, Kopierschutz und Dateiformate finden Sie in unserem Info- & Hilfebereich.
Model and simulate chemical reactions that create plastics and polymers
Understanding Modeling and Simulation of Polymerization Reactions fills a critical gap in existing literature by teaching the science behind polymer design using advanced mathematical and computational methods and providing tools to predict and control how polymers are formed. The book covers both traditional and cutting-edge polymerization methods and uses four powerful modeling techniques: z-transform, method of moments, Markov chains, and Monte Carlo simulations.
The book emphasizes hands-on, equation-driven approaches that help readers understand the underlying chemistry and physics and relate reaction conditions to specific polymer properties. Real-world examples and practice problems are included to reinforce learning, with an online solutions manual available for adopting professors.
Written by an experienced teaching professor, Understanding Modeling and Simulation of Polymerization Reactions discusses:
- Mechanisms of chain formation from monomers including addition, step-growth, and their combinations
- Theoretical models for predicting composition of propagating species for several types of polymerization reactions including conventional radical, reversible deactivation radical, anionic, and cationic polymerization
- Stochastic models of chain distribution, based on the Markovian process, for addition and step-growth polymerization
- Theoretical models to relate viscosity of the reaction medium to monomer conversion, chain diffusivity, and polymer molecular weight
- Copolymer sequences, monomer sequence distributions, and copolymer randomness
Understanding Modeling and Simulation of Polymerization Reactions is an ideal high-level academic textbook for advanced undergraduate and graduate courses on polymer engineering, polymer science, and polymer materials. With its broad scope, the book is also valuable for practicing professionals in the polymer and materials industries.
More details
Other editions
Additional editions

Person
Esmaiel Jabbari, PhD is Professor of Chemical and Biomedical Engineering at the University of South Carolina. His research focuses on the application of resorbable polymeric biomaterials in medicine for drug delivery and regenerative medicine. He was elected a Fellow of the American Institute of Medical and Biological Engineering in 2013.
Content
Preface xvii
Acknowledgment xxi
About the Companion Website xxii
1 Mechanisms and Methods of Polymerization 1
1.1 Introduction 1
1.2 Mechanisms of Polymerization 2
1.3 Living Polymerization 17
1.4 Copolymerization 21
1.5 Architecture of Polymer Chains 22
1.6 Summary 23
1.7 List of Symbols and Abbreviations 24
1.8 Practice Problems 27
2 Elementary Reactions in Polymerization 43
2.1 Introduction 43
2.2 Initiation Reaction 44
2.3 Propagation Reaction 52
2.4 Termination Reactions 52
2.5 Chain Transfer Reactions to Small Molecules 54
2.6 Chain Backbiting Reaction 57
2.7 Chain Combination Reactions 58
2.8 Chain Dissociation Reactions 63
2.9 Summary 64
2.10 List of Symbols and Abbreviations 65
2.11 Practice Problems 69
3 Functions with Distributed Variables 85
3.1 Introduction 85
3.2 Moments of a Distribution 86
3.3 Relating Molar-based Distribution of Polymer Chains to Weight-based Distribution 88
3.4 Relating Molar-based Moments of Polymer Chains to Weight-based Moments 89
3.5 Relating Number-average, Weight-average, and z-average Degree of Polymerization of Polymer Chains to Molar-based Moments of Chain Distribution 92
3.6 Relating Viscosity-average Degree of Polymerization of Polymer Chains to Molar-based Moments of Chain Distribution 94
3.7 Variance and Polydispersity of a Polymer Chain Distribution 97
3.8 Skewness and Kurtosis of a Polymer Chain Distribution 98
3.9 Standard Distribution Functions Used in Polymerization Reactions 101
3.10 Summary 111
3.11 List of Symbols and Abbreviations 111
3.12 Practice Problems 113
4 Z-transform in Polymerization Reactions 121
4.1 Introduction 121
4.2 Definition of Z-transform 122
4.3 Moments of a Distributed Function in Z Domain 122
4.4 Properties of a Function in the Z Domain 124
4.5 Inverse Z-transform 126
4.6 Application of Z-transform in Addition Polymerization 128
4.7 Application of Z-transform in Step-growth Polymerization 130
4.8 Summary 141
4.9 List of Symbols and Abbreviations 142
4.10 Practice Problems 145
5 Conservation of Moments of Distribution of Chains in Polymerization 153
5.1 Introduction 153
5.2 Elementary Reactions in Polymerization in a Differential Time Interval 153
5.3 Mixing Theory of Polymer Chains 154
5.4 Conservation of kth Order Moment of Polymer Chains in a Reaction 158
5.5 Derivation of the General Conservation Equation for kth Order Moment of Polymer Chains in a Reaction 162
5.6 Formation of Reactive Species in Conventional Radical Polymerization and the Quasi-steady State Assumption 174
5.7 Initiation and Formation of Reactive Species in Polymerization 176
5.8 Summary 184
5.9 List of Symbols and Abbreviations 185
5.10 Practice Problems 187
6 Moments of Elementary Reactions in Addition Polymerization 205
6.1 Introduction 205
6.2 Instantaneous kth Order Moments of Propagating Chains After Propagation in Terms of Propagating Chains Prior to Propagation 205
6.3 Instantaneous kth Order Moments of Chains Produced by Termination in Terms of kth Order Moments of Propagating Chains 207
6.4 Instantaneous kth Order Moments of Chains Produced by Transfer Reactions in Terms of kth Order Moments of Propagating Chains 208
6.5 Instantaneous kth Order Moments of Chains Produced by Chain Scission 213
6.6 Summary 218
6.7 List of Symbols and Abbreviations 218
6.8 Practice Problems 221
7 Conservation of Moments Applied to Polymerization Reactions 229
7.1 Introduction 229
7.2 General Conservation Equations for kth Order Moment of Propagating, Dormant, and Terminated Chains 229
7.3 Modeling Radical Polymerization with Termination by Disproportionation in the Absence of Chain Transfer 230
7.4 Modeling Radical Polymerization with Chain Transfer Agent 251
7.5 Modeling Radical Polymerization with Chain Transfer to the Terminated Polymer Chains 256
7.6 Modeling Radical Polymerization with ;;2 Chain Scission 259
7.7 Modeling Radical Polymerization with Photoinitiation 263
7.8 Modeling Reversible-deactivation Radical Polymerization by Atom transfer Radical Polymerization 271
7.9 Modeling Ionic Polymerization 281
7.10 Summary 287
7.11 List of Symbols and Abbreviations 288
7.12 Practice Problems 294
8 Diffusion Controlled Polymerization Reactions 307
8.1 Introduction 307
8.2 Relating Diffusion Coefficient and Viscosity to Molecular Weight 308
8.3 Role of Diffusion in Bulk Polymerization of Methyl Methacrylate 313
8.4 Termination Rate Constant in Diffusion-limited Polymerization Reactions 321
8.5 Quasi Steady State in Diffusion-limited Polymerization Reactions 328
8.6 Modeling Diffusion-limited Radical Polymerization with Termination by Disproportionation and Combination
and Chain Transfer to Monomer 330
8.7 Modeling Diffusion-limited Bulk Radical Polymerization of Methyl Methacrylate 338
8.8 Summary 347
8.9 List of Symbols and Abbreviations 348
8.10 Practice Problems 356
9 Markov Chain Modeling of Polymerization Reactions 367
9.1 Introduction 367
9.2 Definition of a Markov Chain 367
9.3 State Space of a Markov Chain 368
9.4 Initial Probability Vector 368
9.5 One-step Uniform Transition Probability Matrix 368
9.6 n-step Uniform Transition Probability Matrix 369
9.7 n-step Absolute Probability Vector 370
9.8 Types of States in State Space of a Markov Chain 370
9.9 n-step Probability of Reaching an Absorbing State 371
9.10 Matrix Operations 372
9.11 Application of Markov Chains to Radical Polymerization 375
9.12 Application of Markov Chain to Condensation Polymerization 383
9.13 Summary 389
9.14 List of Symbols and Abbreviations 390
9.15 Practice Problems 393
10 Markov Chain Modeling of Copolymerization Reactions 399
10.1 Introduction 399
10.2 Number Representation of Copolymer Sequences 399
10.3 Order of Copolymerization 400
10.4 State Space of Copolymerization Reaction 402
10.5 Conditional Probability Matrix for Copolymerization Reaction 403
10.6 Composition of Copolymer 403
10.7 Copolymer Sequence Distribution 404
10.8 Modeling Terminal Copolymerization of Two Monomers 409
10.9 Modeling Terminal Terpolymerization of Three Monomers 418
10.10 Summary 427
10.11 List of Symbols and Abbreviations 428
10.12 Practice Problems 430
11 Monte Carlo Simulation of Polymerization Reactions 439
11.1 Introduction 439
11.2 Theory of Monte Carlo Simulation 439
11.3 Estimation of an Integral Function with Monte Carlo Method 440
11.4 Probability Distributions of Random Numbers in Monte Carlo Simulation 441
11.5 Error Estimation in Monte Carlo Simulation 443
11.6 Testing Uniformity of Random Numbers 445
11.7 Monte Carlo Simulation of Initiator Dissociation 451
11.8 Monte Carlo Simulation of Methyl Methacrylate Polymerization 452
11.9 Monte Carlo Simulation of Branching in Butadiene Emulsion Polymerization 457
11.10 Summary 467
11.11 List of Symbols and Abbreviations 468
11.12 Practice Problems 472
References 474
Index 481
Chapter 1
Mechanisms and Methods of Polymerization
1.1 Introduction
Polymers are chain-like molecules consisting of smaller repeat units. They are synthesized from smaller molecules that are chemically linked together. The smaller molecules are called monomers, and the repeat units on a long polymer chain are called monomer residues. Polymers are divided into natural polymers and synthetic polymers. Natural polymers or biopolymers are made by nature as part of living organisms, including microorganisms, plants, animals, and humans. They include polysaccharides from smaller saccharide or sugar monomers, proteins from smaller amino acid monomers, and polynucleotides from smaller nucleotide monomers. Biopolymers, due to having different types of repeat units in their molecular structure, like 20 different amino acids in proteins, display multiple and specific functions in living organisms. Synthetic polymers are designed and produced by mankind by linking small molecules with at least two reactive functional groups to form long chains. Unlike natural polymers, synthetic polymers are made of one, two, or at most three different types of monomers. Most synthetic polymers are homopolymers, that is, they are made of one monomer, like polyethylene and polymethylmethacrylate. Examples of copolymers include polyethylene-vinyl acetate and polystyrene-methyl methacrylate. An example of a terpolymer is polyacrylonitrile-butadiene-styrene or ABS terpolymer. There are very few, if any, synthetic polymers made up of four different monomers. Another difference between biologic and synthetic polymers is that biopolymer chains are, in general, monodisperse, whereas chains in synthetic polymers are polydisperse. For example, the chains in a sample of albumin protein have identical molecular weights, whereas chains in a polyethylene sample have a distribution of molecular weights with a specified average value and a specified polydispersity. The unique property that distinguishes polymeric materials from other man-made materials like metals and ceramics is the aspect ratio of the molecules making up the material. The aspect ratio of a molecule is defined as the ratio of its contour length to its diameter. The aspect ratio for materials made of small molecules is between 1 and 10. Conversely, the aspect ratio of polymer molecules is generally greater than one thousand. The high aspect ratio imparts unique properties to polymers. For example, unlike metals and ceramics, polymers do not exhibit a boiling point with increasing temperature because the long chains in a polymer degrade prior to gaining sufficient energy to evaporate. Instead, polymers exhibit a glassy temperature below which the chains in the polymer sample are frozen with no translational diffusion, even though the polymer is above its melting temperature. As a result of their high aspect ratio, polymers possess unique physical, mechanical, chemical, and biological properties. The aspect ratio of polymers is characterized by the number of monomeric repeat units or degree of polymerization , chain length , which is or multiplied by the length of a repeat unit, or molecular weight , which is N or DP multiplied by molecular weight of the repeat unit. As chains in a sample have a distribution of or , polymers are characterized by their average number of repeat units , average degree of polymerization , average chain length , or average molecular weight . The of a polymer depends on reaction conditions for polymerization. These include temperature, pressure, pH, ionic strength, concentrations of monomers, solvent, initiator, co-initiator, catalyst, activating agent, crosslinker, chain transfer agent, chain terminating agent, retarder and inhibitor, impurities and oxygen, ratios of monomers and solvents, among others. Reaction conditions not only affect molecular weight and its distribution but also density of short and long branching, chain-end functional groups, unsaturated groups along the chain in multifunctional monomers, intra- and inter-molecular branching, and their distributions. Reaction conditions also affect chain architecture (linear, short-branch, long-branch, star-like, comb-like), distribution of monomers in copolymers (ideal, random, alternate, block), and polymer tacticity. As there is a wide range of reaction conditions affecting properties, there is a need to develop theoretical models and simulation methods to relate molecular weight and its distribution to reaction conditions. As the first step, this chapter covers mechanisms and methods of polymerization, which include addition and step-growth polymerization. Addition polymerization further includes conventional and reversible-deactivation radical polymerization (RDRP), anionic and cationic polymerization, ring-opening, and group transfer polymerization.
1.2 Mechanisms of Polymerization
1.2.1 Addition Polymerization
In the addition polymerization, monomer molecules react with active species formed by initiator dissociation to form propagating chains [1, 2]. Polymerizations in which the active species on propagating chains is a radical are called radical polymerization, whereas those with an anion or cation are called anionic polymerization and cationic polymerization, respectively [3-6].
1.2.1.1 Conventional Radical Polymerization
Monomers with unsaturated vinyl groups like styrene, methyl methacrylate, ethylene, propylene, vinyl alcohol, vinyl chloride, and alkyl vinyl ethers, as well as monomers with unsaturated triple bonds, polymerize by addition polymerization according to the following reaction:
(1.1)where is the rate constant for the propagation reaction. In the above reaction, the radical attached to the terminal carbon atom of the propagating chain reacts with a vinyl monomer by dissociating the -bond of the vinylic carbon. Following the reaction, the radical is transferred to the terminal carbon atom of the added monomer to increase the number of monomer residues on the propagating chain radical by one residue. The radical on the propagating chain is normally positioned on the carbon atom with a side group, shown by "X" in the above reaction, as the side group increases the stability of the radical by resonance stabilization [7]. Radical polymerization requires an initiator to form the primary reactive species. Common reactions in addition polymerization are chain initiation, chain propagation, and chain termination. In the initiation step, the initiator dissociates by the addition of a reducing or oxidizing agent, or by a change in temperature, pH, or other external factors like ultraviolet radiation to form one or more reactive species [8, 9]. The initiation reaction for a typical temperature-activated initiator like benzoyl peroxide (BPO) is as follows [10]:
(1.2)In the above reaction, the weak bond of BPO dissociates upon raising the reaction temperature to 80-100 °C, with a rate constant to generate two benzoyloxy radicals. As the benzoyloxy radical is highly unstable, it further disintegrates into a more stable but transient benzyl radical with the liberation of a molecule of carbon dioxide [10]. Some initiators dissociate into two active species while others dissociate into one active species and an inactive fragment [9]. Prior to escaping the dissociation cage, the benzyl radicals may recombine to form an inactive biphenyl compound as follows [11-14]:
(1.3)In the chain initiation step, the generated radical reacts with a vinyl monomer in the reaction mixture to form a 1-mer propagating radical as follows [11-13]:
(1.4)where is the rate constant for initiation of a propagating radical. In the propagation step, vinyl monomers react with a 1-mer propagating chain in propagation reaction steps, as shown in Rxn. 1.1, to generate a propagating chain radical with repeat units [15]. As the propagating chain radical is transient, it ultimately abstracts a hydrogen from a chain or combines with another propagating chain to terminate the propagating radical, and forms one or two terminated chains as follows [16, 17]:
(1.5)where is the rate constant for termination. The termination reaction may take place by termination by disproportionation or termination by combination (shown above), or transfer reactions, which will be discussed in Chapter 2. The defining feature of radical polymerization is that the molecular weight of the synthesized polymer is relatively independent of the extent of polymerization or monomer conversion [18]. Conventional radical polymerization is not a living polymerization unless termination reactions are suppressed, as will be discussed in the reversible deactivation radical polymerization section [19, 20]. Initiation in radical polymerization is generally not instantaneous; that is, initiator dissociation is time-dependent, which leads to time-dependent chain initiation/termination reactions and a relatively broad chain molecular weight distribution.
1.2.1.2 Anionic Polymerization
Vinyl monomers with electrophilic or polar groups that stabilize a propagating anion undergo anionic polymerization [21-23]. Examples include styrene, butadiene, and isoprene with electrophilic groups and acrylonitrile, methyl methacrylate, and cyanoacrylate with polar groups [24]. A commonly used anionic polymerization initiator is butyl lithium [25, 26]. The carbon-lithium bond in...
System requirements
File format: ePUB
Copy protection: Adobe-DRM (Digital Rights Management)
System requirements:
- Computer (Windows; MacOS X; Linux): Install the free reader Adobe Digital Editions prior to download (see eBook Help).
- Tablet/smartphone (Android; iOS): Install the free app Adobe Digital Editions or the app PocketBook before downloading (see eBook Help).
- E-reader: Bookeen, Kobo, Pocketbook, Sony, Tolino and many more (not Kindle).
The file format ePub works well for novels and non-fiction books – i.e., „flowing” text without complex layout. On an e-reader or smartphone, line and page breaks automatically adjust to fit the small displays.
This eBook uses Adobe-DRM, a „hard” copy protection. If the necessary requirements are not met, unfortunately you will not be able to open the eBook. You will therefore need to prepare your reading hardware before downloading.
Please note: We strongly recommend that you authorise using your personal Adobe ID after installation of any reading software.
For more information, see our ebook Help page.