Ring-opening polymerization

History

Ring-opening polymerization has been used since the beginning of the 1900s to produce polymers. Synthesis of polypeptides which has the oldest history of ROP, dates back to the work in 1906 by Leuchs. Subsequently, the ROP of anhydro sugars provided polysaccharides, including synthetic dextran, xanthan gum, welan gum, gellan gum, diutan gum, and pullulan. Mechanisms and thermodynamics of ring-opening polymerization were established in the 1950s. The first high-molecular weight polymers (M_n up to 10⁵) with a repeating unit were prepared by ROP as early as in 1976.

New research shows that ROP can be completed with cyclic esters with minimal to no use of solvents by using resonant acoustic mixing.

An industrial application is the production of nylon-6 from caprolactam.

Mechanisms

Ring-opening polymerization can proceed via radical, anionic, or cationic polymerization as described below. Additionally, radical ROP is useful in producing polymers with functional groups incorporated in the backbone chain that cannot otherwise be synthesized via conventional chain-growth polymerization of vinyl monomers. For instance, radical ROP can produce polymers with ethers, esters, amides, and carbonates as functional groups along the main chain.

Anionic ring-opening polymerization (AROP)

Anionic ring-opening polymerizations (AROP) involve nucleophilic reagents as initiators. Monomers with a three-member ring structure - such as epoxides, aziridines, and episulfides - undergo anionic ROP.

A typical example of anionic ROP is that of ε-caprolactone, initiated by an alkoxide. Silicones are produced by AROP starting with cyclic siloxanes. A representative reaction is shown with hexamethyltrisiloxane:

n[Si(CH₃)₂O]₃ → [Si(CH₃)₂O]_3n

Cationic ring-opening polymerization

Cationic initiators and intermediates characterize cationic ring-opening polymerization (CROP). Examples of cyclic monomers that polymerize through this mechanism include lactones, lactams, amines, and ethers. CROP proceeds through an S_N1 or S_N2 propagation, chain-growth process. The mechanism is affected by the stability of the resulting cationic species. For example, if the atom bearing the positive charge is stabilized by electron-donating groups, polymerization will proceed by the S_N1 mechanism. The cationic species is a heteroatom and the chain grows by the addition of cyclic monomers thereby opening the ring system.

The monomers can be activated by Bronsted acids, carbenium ions, onium ions, and metal cations.

CROP can be a living polymerization and can be terminated by nucleophilic reagents such as phenoxy anions, phosphines, or polyanions. When the amount of monomers becomes depleted, termination can occur intra or intermolecularly. The active end can "backbite" the chain, forming a macrocycle. Alkyl chain transfer is also possible, where the active end is quenched by transferring an alkyl chain to another polymer.

Ring-opening metathesis polymerization

Ring-opening metathesis polymerisation (ROMP) produces unsaturated polymers from cycloalkenes or bicycloalkenes. It requires organometallic catalysts.

The mechanism for ROMP follows similar pathways as olefin metathesis. The initiation process involves the coordination of the cycloalkene monomer to the metal alkylidene complex, followed by a [2+2] type cycloaddition to form the metallacyclobutane intermediate that cycloreverts to form a new alkylidene species.

Commercially relevant unsaturated polymers synthesized by ROMP include polynorbornene, polycyclooctene, and polycyclopentadiene.

Thermodynamics

The formal thermodynamic criterion of a given monomer polymerizability is related to a sign of the free enthalpy (Gibbs free energy) of polymerization: $${\displaystyle \mathrm{\Delta }{G}_p(xy)=\mathrm{\Delta }{H}_p(xy)-T\mathrm{\Delta }{S}_p(xy)}$$ where:

x and y indicate monomer and polymer states, respectively (x and/or y = l (liquid), g (gaseous), c (amorphous solid), c' (crystalline solid), s (solution));

ΔH_p(xy) is the enthalpy of polymerization (SI unit: joule per kelvin);

ΔS_p(xy) is the entropy of polymerization (SI unit: joule);

T is the absolute temperature (SI unit: kelvin).

The free enthalpy of polymerization (ΔG_p) may be expressed as a sum of standard enthalpy of polymerization (ΔG_p°) and a term related to instantaneous monomer molecules and growing macromolecules concentrations: $${\displaystyle \mathrm{\Delta }{G}_p=\mathrm{\Delta }{G}_p^{\circ }+RT\ln \frac{[\dots -(\text{m}{)}_{i+1}{\text{m}}^{\ast }]}{[\text{M}][\dots -(\text{m}{)}_i{\text{m}}^{\ast }]}}$$ where:

R is the gas constant;

M is the monomer;

(m)_i is the monomer in an initial state;

m^* is the active monomer.

Following Flory–Huggins solution theory that the reactivity of an active center, located at a macromolecule of a sufficiently long macromolecular chain, does not depend on its degree of polymerization (DP_i), and taking in to account that ΔG_p° = ΔH_p° − TΔS_p° (where ΔH_p° and ΔS_p° indicate a standard polymerization enthalpy and entropy, respectively), we obtain:

${\displaystyle \mathrm{\Delta }{G}_p=\mathrm{\Delta }{H}_p^{\circ }-T(\mathrm{\Delta }{S}_p^{\circ }+R\ln [M])}$

At equilibrium (ΔG_p = 0), when polymerization is complete the monomer concentration ([M]_eq) assumes a value determined by standard polymerization parameters (ΔH_p° and ΔS_p°) and polymerization temperature: $${\displaystyle \begin{array}{cc}[\text{M}{]}_{\mathrm{e}\mathrm{q}}& =\exp \left(\frac{\mathrm{\Delta }{H}_p^{\circ }}{RT}-\frac{\mathrm{\Delta }{S}_p^{\circ }}{R}\right)\\ \ln \frac{D{P}_n}{D{P}_n-1}[\text{M}{]}_{\mathrm{e}\mathrm{q}}& =\frac{\mathrm{\Delta }{H}_p^{\circ }}{RT}-\frac{\mathrm{\Delta }{S}_p^{\circ }}{R}\\ [\text{M}{]}_{\mathrm{e}\mathrm{q}}& =\frac{D{P}_n-1}{D{P}_n}\exp \left(\frac{\mathrm{\Delta }{H}_p^{\circ }}{RT}-\frac{\mathrm{\Delta }{S}_p^{\circ }}{R}\right)\end{array}}$$ Polymerization is possible only when [M]₀ > [M]_eq. Eventually, at or above the so-called ceiling temperature (T_c), at which [M]_eq = [M]₀, formation of the high polymer does not occur. $${\displaystyle \begin{array}{cc}{T}_c& =\frac{\mathrm{\Delta }{H}_p^{\circ }}{\mathrm{\Delta }{S}_p^{\circ }+R\ln [\text{M}{]}_0};(\mathrm{\Delta }{H}_p^{\circ }<0,\mathrm{\Delta }{S}_p^{\circ }<0)\\ T_f& =\frac{\mathrm{\Delta }{H}_p^{\circ }}{\mathrm{\Delta }{S}_p^{\circ }+R\ln [\text{M}{]}_0};(\mathrm{\Delta }{H}_p^{\circ }>0,\mathrm{\Delta }{S}_p^{\circ }>0)\end{array}}$$ For example, tetrahydrofuran (THF) cannot be polymerized above T_c = 84 °C, nor cyclo-octasulfur (S₈) below T_f = 159 °C. However, for many monomers, T_c and T_f, for polymerization in the bulk, are well above or below the operable polymerization temperatures, respectively. The polymerization of a majority of monomers is accompanied by an entropy decrease, due mostly to the loss in the translational degrees of freedom. In this situation, polymerization is thermodynamically allowed only when the enthalpic contribution into ΔG_p prevails (thus, when ΔH_p° < 0 and ΔS_p° < 0, the inequality |ΔH_p| > −TΔS_p is required). Therefore, the higher the ring strain, the lower the resulting monomer concentration at equilibrium.

Additional reading

• Luck, Russel M.; Sadhir, Rajender K., eds. (1992). Expanding Monomers: Synthesis, Characterization, and Applications. Boca Raton, Florida: CRC Press. ISBN 978-0-8493-5156-3.
• Nahrain E. Kamber; Wonhee Jeong; Robert M. Waymouth; Russell C. Pratt; Bas G. G. Lohmeijer; James L. Hedrick (2007). "Organocatalytic Ring-Opening Polymerization". Chemical Reviews. 107 (12): 5813–5840. doi:10.1021/cr068415b. PMID 17988157.
• Dubois, Philippe; Coulembier, Olivier; Raquez, Jean-Marie, eds. (2009). Handbook of Ring-Opening Polymerization. Wiley. doi:10.1002/9783527628407. ISBN 9783527628407.