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Living polymerization

From Wikipedia, the free encyclopedia
Chain-growth polymerization without the ability to terminate

Inpolymer chemistry,living polymerization is a form ofchain growth polymerization where the ability of a growingpolymer chain toterminate has been removed.[1][2] This can be accomplished in a variety of ways.Chain termination andchain transfer reactions are absent and the rate ofchain initiation is also much larger than the rate ofchain propagation. The result is that the polymer chains grow at a more constantrate than seen in traditional chainpolymerization and their lengths remain very similar (i.e. they have a very lowpolydispersity index). Living polymerization is a popular method for synthesizingblock copolymers since the polymer can be synthesized in stages, each stage containing a differentmonomer. Additional advantages are predeterminedmolar mass and control overend-groups.

IUPAC definition

Living polymerization: A chain polymerization from which chain transfer and chain termination are absent.

Note: In many cases, the rate of chain initiation is fast compared with the rate of chain propagation, so that the number of kinetic-chain carriers is essentially constant throughout the polymerization.[3]

Living polymerization is desirable because it offers precision and control in macromolecular synthesis. This is important since many of the novel/useful properties of polymers result from their microstructure and molecular weight. Sincemolecular weight anddispersity are less controlled in non-living polymerizations, this method is more desirable for materials design[4][5]

In many cases, living polymerization reactions are confused or thought to be synonymous with controlled polymerizations. While these polymerization reactions are very similar, there is a distinction between the definitions of these two reactions. While living polymerizations are defined as polymerization reactions where termination or chain transfer is eliminated, controlled polymerization reactions are reactions where termination is suppressed, but not eliminated, through the introduction of a dormant state of the polymer.[4][5] However, this distinction is still up for debate in the literature.

The main living polymerization techniques are:

History

[edit]

Living polymerization was demonstrated byMichael Szwarc in 1956 in the anionic polymerization ofstyrene with analkali metal /naphthalene system intetrahydrofuran (THF). Szwarc showed thatelectron transfer occurred fromradical anion ofnaphthalene tostyrene. The initial radical anion of styrene converts to adianion (or equivalently disodio-) species, which rapidly added styrene to form a "two – ended living polymer." An important aspect of his work, Szwarc employed theaprotic solventtetrahydrofuran, which dissolves but is otherwise unreactive toward the organometallic intermediates. After initial addition of monomer to the initiator system, theviscosity increased (due to increased polymer chain growth), but eventually cease after depletion of monomer concentration. However, he found that addition ofmore monomer caused an increase in viscosity, indicating growth of the polymer chain, and thus concluded that the polymer chains had never been terminated.[6] This was a major step in polymer chemistry, since control over when the polymer was quenched, or terminated, was generally not a controlled step. With this discovery, the list of potential applications expanded dramatically.[7]

Today, living polymerizations are used widely in the production of many types of polymers or plastics. For instance,poly(phthalaldehyde) polymer, first developed in 1967, can be synthesized via bothliving cationic andliving anionic polymerization reactions producing both the cyclic or linear form of the polymer respectively. The approach offers control of the chemical makeup of the polymer and, thus, the structural and electronic properties of the material. This level of control rarely exists in non-living polymerization reactions.[5][8]

Fast rate of initiation: low polydispersity

[edit]
Figure 1: Rate of initiation is slower than the rate of propagation, leading to the formation of active species at different points in time during the polymerization.
Figure 2: Rate of initiation is instantaneous in comparison to the rate of propagation, causing all the active species to form simultaneously, and chain growth to occur at the same rate.

One of the key characteristics of a living polymerization is that the chain termination and transfer reactions are essentially eliminated from the four elementary reactions ofchain-growth polymerization leaving onlyinitiation and (chain) propagation reactions.

A key characteristic of living polymerization is that the rate of initiation (meaning the dormant chemical species generates the active chain propagating species) is much faster than the rate of chain propagation. Thus all of the chains grow at the same rate (the rate of propagation).

The high rate of initiation (together with absence of termination) results in low (or narrow) polydispersity index (PDI), an indication of the broadness in the distribution of polymer chains.[9] The extended lifetime of the propagating chain allowing for co-block polymer formation and end group functionalization to be performed on the living chain. These factors also allow predictable molecular weights, expressed as the number average molecular weight (Mn). For an ideal living system, assuming efficiency for generating active species is 100%, where each initiator generates only one active species theKinetic chain length (average number of monomers the active species reacts with during its lifetime) at a given time can be estimated by knowing the concentration of monomer remaining. The number average molecular weight,Mn, increases linearly with percent conversion during a living polymerization

 v=[M]0[M][I]0{\displaystyle \ v={\frac {[M]_{0}-[M]}{[I]_{0}}}}[5]

Techniques

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Living anionic polymerization

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Main article:Living anionic polymerization

As early as 1936,Karl Ziegler proposed that anionic polymerization of styrene and butadiene by consecutive addition of monomer to an alkyl lithium initiator occurred without chain transfer or termination. Twenty years later, living polymerization was demonstrated by Szwarc through theanionic polymerization ofstyrene inTHF usingsodium naphthalene as an initiator.[10][6][11]

The naphthalene anion initiates polymerization by reducing styrene to its radical anion, which dimerizes to the dilithiodiphenylbutane, which then initiates the polymerization. These experiments relied on Szwarc's ability to control the levels of impurities which would destroy the highly reactive organometallic intermediates.

Living α-olefin polymerization

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α-olefins can be polymerized through an anionic coordination polymerization in which the metal center of the catalyst is considered the counter cation for theanionic end of the alkyl chain (through a M-R coordination). Ziegler-Natta initiators were developed in the mid-1950s and are heterogeneous initiators used in the polymerization of alpha-olefins. Not only were these initiators the first to achieve relatively high molecular weight poly(1-alkenes) (currently the most widely produced thermoplastic in the world PE(Polyethylene) and PP (Polypropylene)[12] but the initiators were also capable of stereoselective polymerizations which is attributed to thechiralCrystal structure of the heterogeneous initiator.[5] Due to the importance of this discovery Ziegler and Natta were presented with the1963 Nobel Prize in chemistry. Although the active species formed from the Ziegler-Natta initiator generally have long lifetimes (on the scale of hours or longer) the lifetimes of the propagating chains are shortened due to several chain transfer pathways (Beta-Hydride elimination and transfer to the co-initiator) and as a result are not considered living.[5]

Metallocene initiators are considered as a type of Ziegler-Natta initiators due to the use of the two-component system consisting of atransition metal and a group I-III metal co-initiator (for examplemethylalumoxane (MAO) or other alkyl aluminum compounds). Themetallocene initiators form homogeneous single sitecatalysts that were initially developed to study the impact that the catalyst structure had on the resulting polymers structure/properties; which was difficult for multi-site heterogeneous Ziegler-Natta initiators.[12] Owing to the discrete single site on the metallocene catalyst researchers were able to tune and relate how the ancillary ligand (those not directly involved in the chemical transformations) structure and the symmetry about the chiral metal center affect the microstructure of the polymer.[13] However, due to chain breaking reactions (mainly Beta-Hydride elimination) very few metallocene based polymerizations are known.[5]

By tuning the steric bulk and electronic properties of the ancillary ligands and theirsubstituents a class of initiators known aschelate initiators (or post-metallocene initiators) have been successfully used forstereospecific living polymerizations of alpha-olefins. The chelate initiators have a high potential for living polymerizations because the ancillary ligands can be designed to discourage or inhibit chain termination pathways. Chelate initiators can be further broken down based on the ancillary ligands; ansa-cyclopentyadienyl-amido initiators, alpha-diimine chelates and phenoxy-imine chelates.[5]

  • Ansa-cyclopentadienyl-amido (CpA) initiators
a.) Shows the general form of CpA initiators with one Cp ring and a coordinated Nitrogen b.) Shows the CpA initiator used in the living polymerization of 1-hexene (5)

CpA initiators have onecyclopentadienyl substituent and one or more nitrogen substituents coordinated to the metal center (generally a Zr or Ti) (Odian). The dimethyl(pentamethylcyclopentyl)zirconium acetamidinate in figure___ has been used for a stereospecific living polymerization of 1-hexene at −10 °C. The resulting poly(1-hexene) wasisotactic (stereochemistry is the same between adjacent repeat units) confirmed by13C-NMR. The multiple trials demonstrated a controllable and predictable (from catalyst tomonomer ratio) Mn with low Đ. The polymerization was further confirmed to be living by sequentially adding 2 portions of the monomer, the second portion was added after the first portion was already polymerized, and monitoring the Đ and Mn of the chain. The resulting polymer chains complied with the predicted Mn (with the total monomer concentration = portion 1 +2) and showed low Đ[14] suggesting the chains were still active, or living, as the second portion of monomer was added (5).

  • α-diimine chelate initiators

α-diimine chelate initiators are characterized by having adiimine chelating ancillary ligand structure and which is generally coordinated to a late transition (i.e. Ni and Pd) metal center.

Brookhart et al. did extensive work with this class of catalysts and reported living polymerization for α-olefins[15] and demonstrated living α-olefin carbon monoxide alternating copolymers.[16]

Living cationic polymerization

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Main article:Living cationic polymerization

Monomers for living cationic polymerization are electron-rich alkenes such as vinyl ethers,isobutylene,styrene, and N-vinylcarbazole. The initiators are binary systems consisting of an electrophile and a Lewis acid. The method was developed around 1980 with contributions from Higashimura, Sawamoto and Kennedy. Typically, generating a stable carbocation for a prolonged period of time is difficult, due to the possibility for the cation to be quenched by a β-protons attached to another monomer in the backbone, or in a free monomer. Therefore, a different approach is taken[4][5][17]

This is an example of a controlled/living cationic polymerization. Note that the "termination" step has been placed in equilibrium with an "initiation" step in either direction. Nu: is a weak nucleophile that can reversibly leave, while the MXn is a weak Lewis acid M bound to a halogen X to generate the carbocation.
This is an example of a controlled/living cationic polymerization. Note that the "termination" step has been placed in equilibrium with an "initiation" step in either direction. Nu: is a weak nucleophile that can reversibly leave, while the MXn is a weak Lewis acid M bound to a halogen X to generate the carbocation.

In this example, the carbocation is generated by the addition of a Lewis acid (co-initiator, along with the halogen "X" already on the polymer – see figure), which ultimately generates the carbocation in a weak equilibrium. This equilibrium heavily favors the dormant state, thus leaving little time for permanent quenching or termination by other pathways. In addition, a weak nucleophile (Nu:) can also be added to reduce the concentration of active species even further, thus keeping the polymer "living".[4][5][17] However, it is important to note thatby definition, the polymers described in this example are not technically living due to the introduction of a dormant state, as termination has only been decreased, not eliminated (though this topic is still up for debate). But, they do operate similarly, and are used in similar applications to those of true living polymerizations.

Living ring-opening metathesis polymerization

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Given the right reaction conditionsring-opening metathesis polymerization (ROMP) can be rendered living. The first such systems were described byRobert H. Grubbs in 1986 based onnorbornene andTebbe's reagent and in 1978 Grubbs together withRichard R. Schrock describing living polymerization with atungsten carbene complex.[18]

Generally, ROMP reactions involve the conversion of a cyclic olefin with significant ring-strain (>5 kcal/mol), such as cyclobutene, norbornene, cyclopentene, etc., to a polymer that also contains double bonds. The important thing to note about ring-opening metathesis polymerizations is that the double bond is usually maintained in the backbone, which can allow it to be considered "living" under the right conditions.[19]

For a ROMP reaction to be considered "living", several guidelines must be met:[19]

  1. Fast and complete initiation of the monomer. This means that the rate at which an initiating agent activates the monomer for polymerization, must happen very quickly.
  2. How many monomers make up each polymer (the degree of polymerization) must be related linearly to the amount of monomer you started with.
  3. Thedispersity of the polymer must be < 1.5. In other words, the distribution of how long your polymer chains are in your reaction must be very low.

With these guidelines in mind, it allows you to create a polymer that is well controlled both in content (what monomer you use) and properties of the polymer (which can be largely attributed to polymer chain length). It is important to note that living ring-opening polymerizations can be anionicor cationic.

The catalytic cycle of a living ring-opening metathesis polymerization with a metal catalyst. Note that the ring can be any size, but should contain some significant ring strain on the alkene.
The catalytic cycle of a living ring-opening metathesis polymerization with a metal catalyst. Note that the ring can be any size, but should contain some significant ring strain on the alkene.

Because living polymers have had their termination ability removed, this means that once your monomer has been consumed, the addition of more monomer will result in the polymer chains continuing to grow until all of the additional monomer is consumed. This will continue until the metal catalyst at the end of the chain is intentionally removed by the addition of a quenching agent. As a result, it may potentially allow one to create ablock orgradient copolymer fairly easily and accurately. This can lead to a high ability to tune the properties of the polymer to a desired application (electrical/ionic conduction, etc.)[5][19]

"Living" free radical polymerization

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Main article:Reversible-deactivation radical polymerization

Starting in the 1970s several new methods were discovered which allowed the development of living polymerization usingfree radical chemistry. These techniques involvedcatalytic chain transfer polymerization, iniferter mediated polymerization, stable free radical mediated polymerization (SFRP),atom transfer radical polymerization (ATRP),reversible addition-fragmentation chain transfer (RAFT) polymerization, and iodine-transfer polymerization.

In "living" radical polymerization (or controlled radical polymerization (CRP)) the chain breaking pathways are severely depressed when compared to conventional radical polymerization (RP) and CRP can display characteristics of a living polymerization. However, since chain termination is not absent, but only minimized, CRP technically does not meet the requirements imposed by IUPAC for a living polymerization (see introduction for IUPAC definition). This issue has been up for debate the view points of different researchers can be found in a special issue of the Journal of Polymer Science titledLiving or Controlled ?. The issue has not yet been resolved in the literature so it is often denoted as a "living" polymerization, quasi-living polymerization, pseudo-living and other terms to denote this issue.

There are two general strategies employed in CRP to suppress chain breaking reactions and promote fast initiation relative to propagation. Both strategies are based on developing a dynamic equilibrium amongst an active propagating radical and a dormant species.[20]

The first strategy involves a reversible trapping mechanism in which the propagating radical undergoes an activation/deactivation (i.e.Atom-transfer radical-polymerization) process with a species X. The species X is a persistent radical, or a species that can generate a stable radical, that cannot terminate with itself or propagate but can only reversibly "terminate" with the propagating radical (from the propagating polymer chain) P*. P* is a radical species that can propagate (kp) and irreversibly terminate (kt) with another P*. X is normally a nitroxide (i.e.TEMPO used inNitroxide Mediated Radical Polymerization) or an organometallic species. The dormant species (Pn-X) can be activated to regenerate the active propagating species (P*) spontaneously, thermally, using a catalyst and optically.[20][21]

The second strategy is based on a degenerative transfer (DT) of the propagating radical between transfer agent that acts as a dormant species (i.e.Reversible addition−fragmentation chain-transfer polymerization). The DT based CRP's follow the conventional kinetics of radical polymerization, that is slow initiation and fast termination, but the transfer agent (Pm-X or Pn-X) is present in a much higher concentration compared to the radical initiator. The propagating radical species undergoes a thermally neutral exchange with the dormant transfer agent through atom transfer, group transfer or addition fragment chemistry.[20]

Living chain-growth polycondensations

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Chain growth polycondensation polymerizations were initially developed under the premise that a change in substituent effects of the polymer, relative to the monomer, causes the polymers end group to be more reactive this has been referred to as "reactive intermediate polycondensation". The essential result is monomers preferentially react with the activated polymer end groups over reactions with other monomers. This preferred reactivity is the fundamental difference when categorizing a polymerization mechanism as chain-growth as opposed tostep-growth in which the monomer and polymer chain end group have equal reactivity (the reactivity is uncontrolled). Several strategies were employed to minimize monomer-monomer reactions (or self-condensation) and polymerizations with low D and controllable Mn have been attained by this mechanism for small molecular weight polymers.[22] However, for high molecular weight polymer chains (i.e. small initiator to monomer ratio) the Mn is not easily to controlled, for some monomers, since self-condensation between monomers occurred more frequently due to the low propagating species concentration.[22]

Catalyst-transfer polycondensation

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Main article:Living chain-growth polycondensation

Catalyst transfer polycondensation (CTP) is a chain-growth polycondensation mechanism in which the monomers do not directly react with one another and instead the monomer will only react with the polymer end group through a catalyst-mediated mechanism.[22] The general process consists of the catalyst activating the polymer end group followed by a reaction of the end group with a 2nd incoming monomer. The catalyst is then transferred to the elongated chain while activating the end group (as shown below).[23]

Catalyst transfer polycondensation allows for the living polymerization of π-conjugated polymers and was discovered by Tsutomu Yokozawa in 2004[23] and Richard McCullough.[24] In CTP the propagation step is based on organic cross coupling reactions (i.e.Kumada coupling,Sonogashira coupling,Negishi coupling) top form carbon carbon bonds between difunctional monomers. When Yokozawa and McCullough independently discovered the polymerization using a metal catalyst to couple aGrignard reagent with an organohalide making a new carbon-carbon bond. The mechanism below shows the formation of poly(3-alkylthiophene) using a Ni initiator (Ln can be 1,3-Bis(diphenylphosphino)propane (dppp)) and is similar to the conventional mechanism forKumada coupling involving anoxidative addition, atransmetalation and areductive elimination step. However, there is a key difference, following reductive elimination in CTP, an associative complex is formed (which has been supported by intra-/intermolecular oxidative addition competition experiments[8]) and the subsequent oxidative addition occurs between the metal center and the associated chain (an intramolecular pathway). Whereas in a coupling reaction the newly formed alkyl/aryl compound diffuses away and the subsequent oxidative addition occurs between an incoming Ar–Br bond and the metal center. The associative complex is essential to for polymerization to occur in a living fashion since it allows the metal to undergo a preferred intramolecular oxidative addition and remain with a single propagating chain (consistent with chain-growth mechanism), as opposed to an intermolecular oxidative addition with other monomers present in the solution (consistent with a step-growth, non-living, mechanism).[25][26] The monomer scope of CTP has been increasing since its discovery and has included poly(phenylene)s, poly(fluorine)s, poly(selenophene)s and poly(pyrrole)s.[25][26]

Living group-transfer polymerization

[edit]

Group-transfer polymerization also has characteristics of living polymerization.[27] It is applied to alkylatedmethacrylate monomers and the initiator is asilyl ketene acetal. New monomer adds to the initiator and to the active growing chain in aMichael reaction. With each addition of a monomer group the trimethylsilyl group is transferred to the end of the chain. The activechain-end is not ionic as in anionic or cationic polymerization but is covalent. The reaction can be catalysed by bifluorides and bioxyanions such astris(dialkylamino)sulfonium bifluoride ortetrabutyl ammonium bibenzoate. The method was discovered in 1983 byOwen Webster[28] and the name first suggested byBarry Trost.

Applications

[edit]

Living polymerizations are used in the commercial synthesis of many polymers.

Copolymer synthesis and applications

[edit]

Copolymers are polymers consisting of multiple different monomer species, and can be arranged in various orders, three of which are seen in the figure below.

Various common forms of copolymers. Here, the two different colored circles represent two different monomers.
Various common forms of copolymers. Here, the two different colored circles represent two different monomers.

While there exist others (alternating copolymers, graft copolymers, and stereoblock copolymers), these three are more common in the scientific literature.[4] In addition, block copolymers can exist as many types, including triblock (A-B-A), alternating block (A-B-A-B-A-B), etc.

Of these three types, block and gradient copolymers are commonly synthesized through living polymerizations, due to the ease of control living polymerization provides. Copolymers are highly desired due to the increased flexibility of properties a polymer can have compared to their homopolymer counterparts. The synthetic techniques used range from ROMP to generic anionic or cationic living polymerizations.[4][5]

Copolymers, due to their unique tunability of properties, can have a wide range of applications. One example (of many) is nano-scalelithography using block copolymers. One used frequently is a block copolymer made of polystyrene and poly(methyl methacrylate) (abbreviated PS-b-PMMA). This copolymer, upon proper thermal and processing conditions, can form cylinders on the order of a few tens of nanometers in diameter of PMMA, surrounded by a PS matrix. These cylinders can then be etched away under high exposure to UV light and acetic acid, leaving a porous PS matrix.[29][30][31]

The unique property of this material is that the size of the pores (or the size of the PMMA cylinders) can be easily tuned by the ratio of PS to PMMA in the synthesis of the copolymer. This can be easily tuned due to the easy control given by living polymerization reactions, thus making this technique highly desired for various nanoscale patterning of different materials for applications to catalysis, electronics, etc.

References

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  29. ^In, Insik; La, Young-Hye; Park, Sang-Min;Nealey, Paul F.; Gopalan, Padma (August 2006). "Side-Chain-Grafted Random Copolymer Brushes as Neutral Surfaces for Controlling the Orientation of Block Copolymer Microdomains in Thin Films".Langmuir.22 (18):7855–7860.doi:10.1021/la060748g.PMID 16922574.
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