Cationic polymerization

IUPAC definition

cationic polymerization: An ionic polymerization in which the kinetic-chain carriers are cations. ^[1]

In polymer chemistry, cationic polymerization is a type of chain growth polymerization in which a cationic initiator transfers charge to a monomer, which then becomes reactive. This reactive monomer goes on to react similarly with other monomers to form a polymer. ^{[2] [3]} The types of monomers necessary for cationic polymerization are limited to alkenes with electron-donating substituents and heterocycles. Similar to anionic polymerization reactions, cationic polymerization reactions are very sensitive to the type of solvent used. Specifically, the ability of a solvent to form free ions will dictate the reactivity of the propagating cationic chain. Cationic polymerization is used in the production of polyisobutylene (used in inner tubes) and poly(N-vinylcarbazole) (PVK). ^[4]

Monomers

Monomer scope for cationic polymerization is limited to two main types: alkene and heterocyclic monomers. Cationic polymerization of both types of monomers occurs only if the overall reaction is thermally favorable. In the case of alkenes, this is due to isomerization of the monomer double bond; for heterocycles, this is due to release of monomer ring strain and, in some cases, isomerization of repeating units. Monomers for cationic polymerization are nucleophilic and form a stable cation upon polymerization. ^[5]

Alkenes

Cationic polymerization of olefin monomers occurs with olefins that contain electron-donating substituents. These electron-donating groups make the olefin nucleophilic enough to attack electrophilic initiators or growing polymer chains. At the same time, these electron-donating groups attached to the monomer must be able to stabilize the resulting cationic charge for further polymerization. Some reactive olefin monomers are shown below in order of decreasing reactivity, with heteroatom groups being more reactive than alkyl or aryl groups. Note, however, that the reactivity of the carbenium ion formed is the opposite of the monomer reactivity. ^[5]

Decreasing reactivity of alkene monomers

Heterocyclic monomers

Examples of heterocyclic monomers

Heterocyclic monomers that are cationically polymerized are lactones, lactams and cyclic amines. Upon addition of an initiator, cyclic monomers go on to form linear polymers. The reactivity of heterocyclic monomers depends on their ring strain. Monomers with large ring strain, such as oxirane, are more reactive than 1,3-dioxepane which has considerably less ring strain. Rings that are six-membered and larger are less likely to polymerize due to lower ring strain. ^[6]

Synthesis

Initiation

Initiation is the first step in cationic polymerization. During initiation, a carbenium ion is generated from which the polymer chain is made. The counterion should be non-nucleophilic, otherwise the reaction is terminated instantaneously. There are a variety of initiators available for cationic polymerization, and some of them require a coinitiator to generate the needed cationic species. ^[7]

Classical protic acids

Strong protic acids can be used to form a cationic initiating species. High concentrations of the acid are needed in order to produce sufficient quantities of the cationic species. The counterion (A⁻) produced must be weakly nucleophilic so as to prevent early termination due to combination with the protonated alkene. ^[5] Common acids used are phosphoric, sulfuric, fluoro-, and triflic acids. Only low molecular weight polymers are formed with these initiators. ^[2]

Initiation by protic acids

Lewis acids/Friedel-Crafts catalysts

Lewis acids are the most common compounds used for initiation of cationic polymerization. The more popular Lewis acids are SnCl₄, AlCl₃, BF₃, and TiCl₄. Although these Lewis acids alone are able to induce polymerization, the reaction occurs much faster with a suitable cation source. The cation source can be water, alcohols, or even a carbocation donor such as an ester or an anhydride. In these systems the Lewis acid is referred to as a coinitiator while the cation source is the initiator. Upon reaction of the initiator with the coinitiator, an intermediate complex is formed which then goes on to react with the monomer unit. The counterion produced by the initiator-coinitiator complex is less nucleophilic than that of the Brønsted acid A⁻ counterion. Halogens, such as chlorine and bromine, can also initiate cationic polymerization upon addition of the more active Lewis acids. ^[2]

Initiation with boron trifluoride (coinitiator) and water (initiator)

Carbenium ion salts

Stable carbenium ions are used to initiate chain growth of only the most reactive alkenes and are known to give well defined structures. These initiators are most often used in kinetic studies due to the ease of measuring the disappearance of the carbenium ion absorbance. Common carbenium ions are trityl and tropylium cations. ^[5]

Initiation with trityl carbenium ion

Ionizing radiation

Ionizing radiation can form a radical-cation pair that can then react with a monomer to start cationic polymerization. Control of the radical-cation pairs is difficult and often depends on the monomer and reaction conditions. Formation of radical and anionic species is often observed. ^[5]

Initiation using ionizing radiation

Propagation

Propagation proceeds by addition of monomer to the active species, i.e. the carbenium ion. The monomer is added to the growing chain in a head-to-tail fashion; in the process, the cationic end group is regenerated to allow for the next round of monomer addition. ^[6]

General propagation pathway

Effect of temperature

The temperature of the reaction has an effect on the rate of propagation. The overall activation energy for the polymerization (${\displaystyle {\mathit {E}}}$) is based upon the activation energies for the initiation (${\displaystyle {\mathit {E_{i}}}}$), propagation (${\displaystyle {\mathit {E_{p}}}}$), and termination (${\displaystyle {\mathit {E_{t}}}}$) steps:

${\displaystyle \textstyle E=E_{i}+E_{p}-E_{t}}$

Generally, ${\displaystyle {\mathit {E_{t}}}}$ is larger than the sum of ${\displaystyle {\mathit {E_{i}}}}$ and ${\displaystyle {\mathit {E_{p}}}}$, meaning the overall activation energy is negative. When this is the case, a decrease in temperature leads to an increase in the rate of propagation. The converse is true when the overall activation energy is positive. ^[6]

Chain length is also affected by temperature. Low reaction temperatures, in the range of 170–190 K, are preferred for producing longer chains. ^[6] This comes as a result of the activation energy for termination and other side reactions being larger than the activation energy for propagation. ^{[5] [6]} As the temperature is raised, the energy barrier for the termination reaction is overcome, causing shorter chains to be produced during the polymerization process. ^[6]

Effect of solvent and counterion

The solvent and the counterion (the gegen ion) have a significant effect on the rate of propagation. The counterion and the carbenium ion can have different associations according to intimate ion pair theory; ranging from a covalent bond, tight ion pair (unseparated), solvent-separated ion pair (partially separated), and free ions (completely dissociated). ^{[2] [6]}

〰〰RXcovalent     〰〰R⁺
X⁻
tight ion pair     〰〰R⁺
/X⁻
solvent-separated
ion pair     〰〰R⁺
+X⁻
free ions

Range of associations between the carbenium ion (${\displaystyle {\ce {R+}}}$) and gegen ion (${\displaystyle {\ce {X-}}}$)

The association is strongest as a covalent bond and weakest when the pair exists as free ions. ^[6] In cationic polymerization, the ions tend to be in equilibrium between an ion pair (either tight or solvent-separated) and free ions. ^[2] The more polar the solvent used in the reaction, the better the solvation and separation of the ions. Since free ions are more reactive than ion pairs, the rate of propagation is faster in more polar solvents. ^{[6] [8]}

The size of the counterion is also a factor. A smaller counterion, with a higher charge density, will have stronger electrostatic interactions with the carbenium ion than will a larger counterion which has a lower charge density. ^[2] Further, a smaller counterion is more easily solvated by a polar solvent than a counterion with low charge density. The result is increased propagation rate with increased solvating capability of the solvent. ^[6]

Termination

Termination generally occurs by unimolecular rearrangement with the counterion. In this process, an anionic fragment of the counterion combines with the propagating chain end. This not only inactivates the growing chain, but it also terminates the kinetic chain by reducing the concentration of the initiator-coinitiator complex. ^{[2] [6]}

Termination by combination with an anionic fragment from the counterion

Chain transfer

Chain transfer can take place in two ways. One method of chain transfer is hydrogen abstraction from the active chain end to the counterion. ^{[6] [8] [9]} In this process, the growing chain is terminated, but the initiator-coinitiator complex is regenerated to initiate more chains. ^{[5] [6]}

Chain transfer by hydrogen abstraction to the counterion

The second method involves hydrogen abstraction from the active chain end to the monomer. This terminates the growing chain and also forms a new active carbenium ion-counterion complex which can continue to propagate, thus keeping the kinetic chain intact. ^[6]

Chain transfer by hydrogen abstraction to the monomer

Cationic ring-opening polymerization

Cationic ring-opening polymerization follows the same mechanistic steps of initiation, propagation, and termination. However, in this polymerization reaction, the monomer units are cyclic in comparison to the resulting polymer chains which are linear. The linear polymers produced can have low ceiling temperatures, hence end-capping of the polymer chains is often necessary to prevent depolymerization. ^[6]

Cationic ring-opening polymerization of oxetane involving (a and b) initiation, (c) propagation, and (d) termination with methanol

Kinetics

The rate of propagation and the degree of polymerization can be determined from an analysis of the kinetics of the polymerization. The reaction equations for initiation, propagation, termination, and chain transfer can be written in a general form:

${\displaystyle {\begin{aligned}{\ce {{I+}+M}}\ &{\ce {->[{k_{i}}]M+}}\\{\ce {{M+}+M}}\ &{\ce {->[{k_{p}}]M+}}\\{\ce {M+}}\ &{\ce {->[{k_{t}}]M}}\\{\ce {{M+}+M}}\ &{\ce {->[{k_{tr}}]{M}+M+}}\end{aligned}}}$

In which I⁺ is the initiator, M is the monomer, M⁺ is the propagating center, and ${\displaystyle {\mathit {k_{i}}}}$, ${\displaystyle {\mathit {k_{p}}}}$, ${\displaystyle {\mathit {k_{t}}}}$, and ${\displaystyle {\mathit {k_{tr}}}}$ are the rate constants for initiation, propagation, termination, and chain transfer, respectively. ^{[5] [6] [10]} For simplicity, counterions are not shown in the above reaction equations and only chain transfer to monomer is considered. The resulting rate equations are as follows, where brackets denote concentrations:

${\displaystyle {\begin{aligned}{\text{rate(initiation)}}&=k_{i}[{\ce {I+}}][{\text{M}}]\\{\text{rate(propagation)}}&=k_{p}[{\ce {M+}}][{\text{M}}]\\{\text{rate(termination)}}&=k_{t}[{\ce {M+}}]\\{\text{rate(chain transfer)}}&=k_{tr}[{\ce {M+}}][{\text{M}}]\end{aligned}}}$

Assuming steady-state conditions, i.e. the rate of initiation = rate of termination: ^{[6] [10]}

${\displaystyle [{\ce {M+}}]={k_{i}[{\ce {I+}}][{\ce {M}}] \over k_{t}}}$

This equation for [M⁺] can then be used in the equation for the rate of propagation: ^{[6] [10]}

${\displaystyle {\text{rate(propagation)}}={k_{p}k_{i}[{\ce {M}}]^{2}[{\ce {I+}}] \over k_{t}}}$

From this equation, it is seen that propagation rate increases with increasing monomer and initiator concentration.

The degree of polymerization, ${\displaystyle {\mathit {X_{n}}}}$, can be determined from the rates of propagation and termination: ^{[6] [10]}

${\displaystyle X_{n}={{\text{rate(propagation)}} \over {\text{rate(termination)}}}={k_{p}[{\text{M}}] \over k_{t}}}$

If chain transfer rather than termination is dominant, the equation for ${\displaystyle {\mathit {X_{n}}}}$ becomes ^{[6] [10]}

${\displaystyle X_{n}={{\text{rate(propagation)}} \over {\text{rate(chain transfer)}}}={k_{p} \over k_{tr}}}$

Living polymerization

Main article: Living cationic polymerization

In 1984, Higashimura and Sawamoto reported the first living cationic polymerization for alkyl vinyl ethers. This type of polymerization has allowed for the control of well-defined polymers. A key characteristic of living cationic polymerization is that termination is essentially eliminated, thus the cationic chain growth continues until all monomer is consumed. ^[11]

Commercial applications

The largest commercial application of cationic polymerization is in the production of polyisobutylene (PIB) products which include polybutene and butyl rubber. These polymers have a variety of applications from adhesives and sealants to protective gloves and pharmaceutical stoppers. The reaction conditions for the synthesis of each type of isobutylene product vary depending on the desired molecular weight and what type(s) of monomer(s) is used. The conditions most commonly used to form low molecular weight (5–10 x 10⁴ Da) polyisobutylene are initiation with AlCl₃, BF₃, or TiCl₄ at a temperature range of −40 to 10 °C. ^[2] These low molecular weight polyisobutylene polymers are used for caulking and as sealants. ^[2] High molecular weight PIBs are synthesized at much lower temperatures of −100 to −90 °C and in a polar medium of methylene chloride. ^[5] These polymers are used to make uncrosslinked rubber products and are additives for certain thermoplastics. Another characteristic of high molecular weight PIB is its low toxicity which allows it to be used as a base for chewing gum. The main chemical companies that produce polyisobutylene are Esso, ExxonMobil, and BASF. ^[12]

Butyl rubber gloves

Butyl rubber, in contrast to PIB, is a copolymer in which the monomers isobutylene (~98%) and isoprene (2%) are polymerized in a process similar to high molecular weight PIBs. Butyl rubber polymerization is carried out as a continuous process with AlCl₃ as the initiator. Its low gas permeability and good resistance to chemicals and aging make it useful for a variety of applications such as protective gloves, electrical cable insulation, and even basketballs. Large scale production of butyl rubber started during World War II, and roughly 1 billion pounds/year are produced in the U.S. today. ^[2]

Polybutene is another copolymer, containing roughly 80% isobutylene and 20% other butenes (usually 1-butene). The production of these low molecular weight polymers (300–2500 Da) is done within a large range of temperatures (−45 to 80 °C) with AlCl₃ or BF₃. Depending on the molecular weight of these polymers, they can be used as adhesives, sealants, plasticizers, additives for transmission fluids, and a variety of other applications. These materials are low-cost and are made by a variety of different companies including BP Chemicals, Esso, and BASF. ^[5]

Other polymers formed by cationic polymerization are homopolymers and copolymers of polyterpenes, such as pinenes (plant-derived products), that are used as tackifiers. In the field of heterocycles, 1,3,5-trioxane is copolymerized with small amounts of ethylene oxide to form the highly crystalline polyoxymethylene plastic. Also, the homopolymerization of alkyl vinyl ethers is achieved only by cationic polymerization. ^[2]

References

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3. Mark, Herman F.; Bikales, Norbert; Charles G. Overberger; Menges, Georg; Kroschwitz, Jacqueline I. (1990). Encyclopedia of Polymer Science and Engineering (2nd ed.). Wiley-Interscience. ISBN   978-0-471-80950-0.
4. Robello, Douglas R. (2002). "Chem 421: Introduction to Polymer Chemistry – Cationic Polymerization". Department of Chemistry, University of Rochester. Archived from the original on 20 July 2011. Retrieved 20 March 2011.
5. Matyjaszewski, Krzysztof (1996). Cationic Polymerizations: Mechanisms, Synthesis, and Applications. New York, New York: Marcel Dekker, Inc. ISBN   978-0-8247-9463-7.
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9. Fahlman, Bradley D. (2008). Materials Chemistry. Springer. ISBN   978-1-4020-6119-6.
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11. Sawamoto, M. (1991). "Modern Cationic Vinyl Polymerization". Progress in Polymer Science. 16: 111–172. doi:10.1016/0079-6700(91)90008-9.
12. Chanda, Manas; Roy, Salil K. (2007). Plastics Technology Handbook: Plastics Engineering Series (4th ed.). Boca Raton, FL: CSC Press. ISBN   978-0-8493-7039-7.