Marion
Helou
a,
Guillaume
Moriceau
ab,
Zhi Wei
Huang
b,
Sandrine
Cammas-Marion
b and
Sophie M.
Guillaume
*a
aLaboratoire Catalyse et Organométalliques, CNRS—Université de Rennes 1—Sciences Chimiques de Rennes (UMR 6226), Campus de Beaulieu, 35042, Rennes Cedex, France. E-mail: sophie.guillaume@univ-rennes1.fr; Fax: +33 2 2323 6939; Tel: +33 2 2323 5880
bLaboratoire Chimie Organique et Supramoléculaire, UMR 6226 CNRS, Ecole Nationale Supérieure de Chimie de Rennes (ENSCR), Avenue du Général Leclerc, CS 50837, 35 708, Rennes Cedex 7, France
First published on 12th January 2011
The “immortal” coordination–insertion ring-opening polymerization of benzyl malolactonate (MLABe) initiated by the two-component catalyst system based on the zinc amide precursor, (BDI)Zn[N(SiMe3)2] (BDI = β-diiminate ligand), and benzyl alcohol (BnOH) acting as a co-initiator and a chain transfer agent proceeds in bulk at 40 °C. Functional telechelic poly(β-benzyl malolactonate)s, H-PMLABe-OBn, are thus obtained. Sequential copolymerization with trimethylene carbonate (TMC) affords block copolymers, PTMC-b-PMLABe, which are alternatively prepared from the chemical coupling of the PMLABe-COOH and PTMC-OH homopolymers. Simultaneous copolymerization of both the lactone and the carbonate monomers offers the PTMC-co-PMLABe random copolymers. The (co)polymers have been characterized by NMR, FT-IR, SEC and DSC analyses. These represent the first examples of β-benzyl malolactonate/carbonate copolymers. More importantly, these (co)polymers could be synthesized free of metallic residues thereby making them suitable as biomedical and pharmaceutical biomaterials.
Regarding the synthesis of poly(β-alkyl malolactonate)s as well as polycarbonates, ring-opening polymerization (ROP) is usually the favored approach over polycondensation.3,9 Indeed, controlled and “living” processes are easily achieved from ROP leading to well defined high molar mass polyesters with controlled molar features (molar mass, molar mass distribution, end-group fidelity) and architectures, and with tailor-made properties.2a,3,4,8 While the synthesis of poly(malic acid) derivatives has been essentially developed via anionic ROP rather than from coordination–insertion ROP,4,5polycarbonates are preferentially prepared via coordination–insertion ROP pathways.2a,3 Among these, we have successfully used the β-diiminate zinc complex (BDI)Zn[N(SiMe3)2] (BDI = CH(CMeNC6H3-2,6-iPr2)2) for the “immortal” ROP (iROP) of TMC.10–12 In association with an alcohol (such as benzyl alcohol, BnOH; for the sake of clarity, the benzyl group “Bn” is distinguished from the benzyl group of the monomer thereafter referred to as “Be”) acting as a co-initiator and a chain transfer agent, this metalloorganic compound, used in truly minute amounts, exhibited unprecedented high activities and productivities in the preparation of well defined PTMCs void of decarboxylation sequences. Furthermore, this same catalytic system has demonstrated its versatility, being successfully applied to the iROP of β-butyrolactone, a four-membered cyclic lactone similar to β-benzyl malolactonate (MLABe) and likewise known for its rather defiant ability to undergo ROP.12,13
In comparison to the copolymers of TMC synthesized with several other cyclic esters,8b,c,14 including with a β-lactone such as the β-butyrolactone comonomer,15copolymers of MLA or its alkyl derivatives (MLARs) with other cyclic esters are quite limited and, to the best of our knowledge, do not include any carbonate moiety.4,5,16–18Block copolymer architectures composed of malic acid or malic acid ester units include poly(malic acid)/poly(lactide),16 poly(malic acid)/poly(β-butyrolactone),16a poly(malic acid)/poly(ε-caprolactone),17 and poly(malic acid)/poly(ethylene glycol).17e,18 Most of these copolymers have been prepared by sequential anionic polymerization of MLAR monomers using potassium alkanoate/18-crown-6, followed by the ROP of the comonomer using a metal-based initiating species like aluminium alkyl17a,c,d or tin (tin(II) bis(2-ethylhexanoate) = Sn(octoate)2 = Sn(oct)2) derivatives.16b,17b,e More scarcely, chain growth of dioxane-dione from poly(lactide) macroinitiators16d or direct copolymerization of both monomers (MLAR and either ε-caprolactone or lactide), using Sn(Oct)216b,17b,e or some organocatalyst(s),16a,d has been carried out. Besides these few examples, as far as we know, no other metal based catalytic system has been used, to date, for the ring-opening (co)polymerization of MLABe. In particular, no single-site metallic system bearing (an) ancillary ligand(s) has allowed the copolymerization of any malic acid based monomer with a cyclic ester (diester, lactone or carbonates).
Herein, we report the homopolymerization of MLABe and its copolymerization with TMC according to an innovative coordination–insertion ROP approach based on the (BDI)Zn[N(SiMe3)2]/BnOH catalytic system. Poly(β-benzyl malolactonate) homopolymers, PMLABe, and poly(β-benzyl malolactonate-b/co-trimethylene carbonate) copolymers, PMLABe-b/co-PTMC, are thus synthesized according to Scheme 1.
![]() | ||
Scheme 1 Schematic representation of the synthesis of H-PMLA-OR from the (BDI)Zn[(N(SiMe3)2)]/BnOH or Al(OTf)3/BnOH mediated “immortal” ROP of MLAR. |
Average molar mass (n) and molar mass distribution (
w/
n) values were determined by size-exclusion chromatography (SEC) in THF at 30 °C (flow rate = 1.0 mL min−1) on a Polymer Laboratories PL50 apparatus equipped with a refractive index detector and a PLgel 5 Å Mixed-C column. The polymer samples were dissolved in THF (2 mg mL−1). All elution curves were calibrated with polystyrene standards.
nSEC values of PTMCs were calculated using the average correction coefficient previously reported (
nSEC =
nSEC raw data × 0.73; 0.73 = average of the coefficients determined from low molar mass PTMCs (0.57;
n < 5000 g mol−1) and from high molar mass PTMCs (0.88;
n > 10
000 g mol−1) by using MALDI-ToF-MS and viscosimetry analyses, respectively).8b
nSEC values of all other (co)polymers are uncorrected for possible difference in hydrodynamic volume vs.polystyrene standards. The molar mass values of short-chain H-PMLAHe-ORs were determined by 1H NMR analysis from the relative intensities of the signals of PMLAHe chains methylene protons (–CH2OC(O), δ = 3.02 ppm) to those of the chain-end benzyl (OCH2C6H5, δ = 7.38 ppm).
Monomer conversions were calculated from FTIR spectra (for PMLABe homopolymers) or from 1H NMR spectra of the crude polymer samples by using the integration (Int.) ratio Int.PMLABe/[Int.PMLABe + Int.MLABe] of the methylene group in α-position of the carbonyl (CH2C(O), δ ≈ 2.85 ppm) and Int.PTMC/[Int.PTMC + Int.TMC] using the methylene group in α-position of the carbonate (CH2OC(O), δ ≈ 4.25 ppm).
FTIR spectra of the polymers were acquired on a FTIR Fourier Nicolet 250 apparatus using KBr plates.
Differential scanning calorimetry (DSC) analyses were performed on a Setaram DSC 131 apparatus calibrated with indium at a rate of 10 °C min−1, under a continuous flow of helium (25 mL min−1), using aluminium capsules. Typically, 10 mg of the (co)polymer was weighted in the capsules. The thermograms were recorded according to the following cycles: −40 °C to +180 °C at 10 °C min−1; +180 °C to −40 °C at 10 °C min−1; −40 °C to +180 °C at 10 °C min−1.
Entry |
[MLABe]0![]() ![]() ![]() ![]() |
Reaction timeb/h | Conv.c (%) |
![]() |
![]() |
![]() ![]() |
TOF g/h−1 |
---|---|---|---|---|---|---|---|
a Monomer and alcohol equiv. relative to [(BDI)Zn[Si(Me3)2]]0. b Reaction times were not necessarily optimized. c Monomer conversion determined by 1H NMR. d Theoretical molar mass value calculated from [MLABe]0/[BnOH]0 × monomer conversion × MMLABe + MBnOH, with MMLABe = 206 g mol−1 and MBnOH = 108 g mol−1. e Experimental molar mass value determined by SECvs.polystyrene standards. f Molar mass distribution value determined from SEC chromatogram traces. g Non-optimized turnover frequency expressed in mol(MLABe) × mol[(BDI)Zn[N(SiMe3)2]]/h−1. h Experiment performed with MLAHe (MMLAHe = 200 g mol−1; MnNMR = 2900 g mol−1). All data are representative of at least duplicated experiments. | |||||||
1 | 100![]() ![]() ![]() ![]() |
6 | 78 | 16![]() |
1760 | 1.46 | 13.0 |
2 | 100![]() ![]() ![]() ![]() |
3 | 54 | 11![]() |
1400 | 1.27 | 18.0 |
3 | 100![]() ![]() ![]() ![]() |
6 | 67 | 13![]() |
1550 | 1.20 | 11.2 |
4 | 100![]() ![]() ![]() ![]() |
6 | 100 | 4230 | 900 | 1.17 | 16.7 |
5h | 100![]() ![]() ![]() ![]() |
6 | 80 | 3310 | 2850 | 1.13 | 13.3 |
6 | 200![]() ![]() ![]() ![]() |
7.5 | 52 | 21![]() |
1500 | 1.23 | 13.9 |
7 | 200![]() ![]() ![]() ![]() |
15 | 78 | 32![]() |
1500 | 1.33 | 10.4 |
8 | 200![]() ![]() ![]() ![]() |
15 | 15 | 1340 | 1000 | 1.11 | 2.0 |
9 | 200![]() ![]() ![]() ![]() |
24 | 30 | 2580 | 2100 | 1.12 | 2.5 |
10 | 200![]() ![]() ![]() ![]() |
15 | 40 | 1760 | 1150 | 1.24 | 5.3 |
11 | 200![]() ![]() ![]() ![]() |
24 | 45 | 1970 | 1500 | 1.28 | 3.8 |
12 | 200![]() ![]() ![]() ![]() |
63 | 70 | 2990 | 1300 | 1.21 | 2.2 |
13 | 500![]() ![]() ![]() ![]() |
36 | 39 | 40![]() |
1000 | 1.33 | 5.4 |
14 | 500![]() ![]() ![]() ![]() |
72 | 68 | 70![]() |
1200 | 1.25 | 4.7 |
15 | 500![]() ![]() ![]() ![]() |
72 | 5 | — | — | — | 0.3 |
Metal-amide derivatives, such as the homoleptic [Zn(N(SiMe3)2)3] compound, are known to polymerize lactones, yet in a non-controlled process11–13,21 like the behavior observed in the present work for the ROP of MLABe initiated by [(BDI)Zn(N(SiMe3)2)] (Table 1, entry 1). In the absence of any added alcohol, whereas the β-diiminate zinc precursor showed a moderate activity (78 turnovers in 6 h), the polymerization featured a very broad molar mass distribution value (w/
n = 1.46) indicative of significant side reactions and/or of a slow initiation process.
In the presence of one equivalent of BnOH (vs. Zn), the [(BDI)Zn(N(SiMe3)2)] complex thus generated a more active alkoxide species that allowed the conversion of 67 equivalents of the 100 of MLABe introduced within 6 h (Table 1, entry 3). Increasing the MLABe content to 200 equivalents then afforded 78% monomer conversion within 15 h (Table 1, entry 7), an activity (156 turnovers in 15 h) thus comparable to that obtained with half less MLABe (Table 1, entry 3; 67 turnovers in 6 h). At much larger monomer loadings (500 equivalents vs. Zn), 72 h were required to convert 68% of MLABe thereby highlighting a decrease of the activity (Table 1, entry 14; 340 turnovers in 72 h).
In the presence of an excess of BnOH (1 < x = up to 10 equiv. vs. Zn) acting as a chain transfer agent, the [(BDI)Zn(N(SiMe3)2)]/BnOH catalytic system allowed the polymerization of MLABe at various monomer-to-zinc and zinc-to-alcohol ratios with high to quantitative monomer conversions being reached within 6–72 h (Table 1, entries 2–15). Monitoring the progress of the polymerization by 1H NMR spectroscopy showed the decrease of the methylene resonance of the malate unit of the monomer at δ 5.30 ppm, and the concomitant appearance of the corresponding broad singlet of the PMLABe at δ 5.53 ppm.
Analysis of the PMLABes by SEC showed traces all exhibiting a unimodal and symmetrical peak. The molar mass distribution values (w/
n) ranging from 1.11 to 1.33 were quite narrow, taking into account that the polymerizations were performed in bulk.20,22 In comparison, typical values obtained from anionic ROP (in bulk or in solution) vary from 1.01 to 1.80 depending on the initiating system.5,16–18,23 The molar mass distribution values reported in Table 1 probably reflected an initiation slower than the propagation and/or the occurrence of some side processes (transfer and/or inter- and intramolecular transesterification reactions) all along the propagation step, more likely to occur under the solvent-free operating conditions used in the present work as compared to solution process.22 Theoretical molar mass values (
ntheo) have been calculated assuming that all the added alcohol molecules contribute to the “immortal” polymerization. The molar mass values determined by SEC (
nSEC), although uncorrected for the difference in hydrodynamic radius vs. the polystyrene standards used for the calibration (as generally found in the literature for the related poly(β-butyrolactone)s),13,19 remained lower than the expected values. A similar behavior was already observed for PMALBes synthesized by anionic ROP of MLABe (
ntheo = 5500; 9300; 11
300 g mol−1vs.
nSEC = 6600; 8300; 5200 g mol−1).17a,d,23a Determination of the molar mass of PMLABes by NMR was not possible because of the overlap of the resonances of the chain-end methylene group (OCH2Ph; δ = 5.16 ppm) with that of the side chain methylene groups (CHC(O)OCH2Ph; δ = 5.04 ppm). However, the use of the hexyl substituted malolactonate (MLAHe) allowed the determination of the molar mass by NMR (
nNMR = 2900 g mol−1, refer to Experimental section) which was in good agreement with the calculated value established from the MLAHe-to-BnOH ratio (
ntheo = 3310 g mol−1, Table 1, entry 5, Fig. 3).
A second feed experiment supported the “living” character of the ROP of MLABe (Fig. 1). Indeed, a PMLABe (nSEC = 1650 g mol−1,
w/
n = 1.19) was first prepared (40 °C, 4 h; 90% monomer conversion,
ntheo = 1550 g mol−1) by ROP of 25 equiv. of MLABe initiated with [(BDI)Zn(N(SiMe3)2)] (1 equiv.) in the presence of 3 equiv. of BnOH. Resuming the polymerization by addition of 25 equiv. of monomer afforded (40 °C, 4 h; 78% monomer conversion,
ntheo = 2900 g mol−1) a PMLABe of greater molar mass (
nSEC = 2600 g mol−1) and still narrow molar mass distribution (
w/
n = 1.22).
![]() | ||
Fig. 1
SEC chromatograms of a PMLABe (![]() ![]() ![]() ![]() ![]() ![]() |
This [(BDI)Zn(N(SiMe3)2)]0/[BnOH] catalytic system, which proved efficient for the (i)ROP of other cyclic esters such as lactide19 or trimethylene carbonate,11,12 as well as the related four membered ring β-butyrolactone (BBL),12,13 was, however, quite less active for the (i)ROP of MLABe. The activity of the catalytic system was, under the same operating conditions, much larger in the case of BBL than with MLABe: at a ratio [monomer]0/[(BDI)Zn(N(SiMe3)2)]0/[BnOH]0 = 200:
1
:
5, TOFMLABe = 2.5 h−1vs.TOFBBL = 600 h−1.13 Substitution of the β-lactone by the benzyl ester group Be = C(O)OBn rather than by a methyl group thus significantly influenced the polymerization. The presence, on the β-lactone, of a functional group bulkier than Me with a different electronic influence most likely greatly altered the interaction between the catalyst system and the incoming monomer. The anionic ROP of β-substituted β-lactones such as MLABe is classically operated in the presence of a weak base such as tetraalkylammonium benzoate as an initiator.5b,c,g,23 This latter system afforded, upon appropriate purification of MLABe, high molar mass polymers (
nSEC up to 174
000 g mol−1vs.polystyrene standards in dioxane) with broad molar mass distribution values (1.7 <
w/
n < 3.3) within 72 h with almost complete monomer conversion (80%).5g In comparison, the present metalloorganic zinc catalytic system showed slightly higher activities (TONzinc up to 18 h−1, Table 1, entry 2, vs. TONanionic = 11 h−1 (ref. 5g)) and significantly narrower molar mass distribution values (
w/
n ≈ 1.22). This zinc initiator, which operated through a coordination–insertion route,12,13 thus clearly minimized the occurrence of side reactions as supported by NMR analyses (vide infra). This underlines the greater advantages and potential of this new zinc-based catalytic system for the ROP of MLARs.
Some of us recently reported the controlled iROP of TMC from of a two-component catalyst system based on a metal Lewis acid such as a metal triflate Al(OTf)3 (OTf = CF3SO3−) and an alcohol as a co-initiator and a chain transfer agent.24 Similar evaluation of this same catalytic system on the iROP of MLABe and MLAHe in bulk at 40 °C successfully afforded the corresponding PMLARs (Scheme 1). Selected results are reported in Table 2. Both monomers were effectively polymerized under “classical” (1 equiv. of BnOH as a co-initiator) and “immortal” (5 equiv. of BnOH as a co-initiator and chain transfer agent) operating conditions with quite similar to slightly higher activities (100 turnovers in 3–6 h, Table 2) as observed with the above organometallic zinc system (54–100 turnovers in 3–6 h, Table 1, entries 2–5). With this catalytic system, under the operating conditions presently investigated, functionalization of the β-lactone with either a benzyl (Be) or hexyl (He) group does not significantly affect the activities (Table 2). However, this seemed beneficial when compared to the pendant naked β-butyrolactone, BBL, for which significant crotonisation side reactions were observed by NMR analyses under similar bulk conditions12,13 whereas no side reaction was detected in the present case from NMR investigations. The polymerization mechanism in the case of Al(OTf)3/BnOH, based on the activation of the monomer, differs from the coordination–insertion one taking place with the (BDI)Zn[N(SiMe3)2]/BnOH catalytic system, as previously reported.11,12,24
Entry | Monomer |
[MLAR]0![]() ![]() ![]() ![]() |
Reaction timeb/h | Conv.c (%) |
![]() |
![]() |
![]() |
![]() ![]() |
---|---|---|---|---|---|---|---|---|
a Monomer and alcohol equiv. relative to [Al(OTf)3]0. b Reaction times were not necessarily optimized. c Monomer conversion determined by 1H NMR. d Theoretical molar mass value calculated from [MLAR]0/[BnOH]0 × monomer conversion × MMLAR + MBnOH, with MMLABe = 206 g mol−1, MMLAHe = 200 g mol−1 and MBnOH = 108 g mol−1. e Experimental molar mass value determined by SECvs.polystyrene standards. f Molar mass distribution value determined from SEC chromatogram traces. All data are representative of at least duplicated experiments. | ||||||||
1 | MLABe | 100![]() ![]() ![]() ![]() |
6 | 100 | 20![]() |
— | 1300 | 1.24 |
2 | MLABe | 100![]() ![]() ![]() ![]() |
6 | 100 | 4230 | — | 1100 | 1.21 |
3 | MLAHe | 100![]() ![]() ![]() ![]() |
6 | 100 | 4110 | 6560 | 6400 | 1.20 |
4 | MLAHe | 100![]() ![]() ![]() ![]() |
3 | 100 | 4110 | 5600 | 5400 | 1.20 |
![]() | ||
Scheme 2 Schematic representation of the syntheses of PMLA-b-/co-PTMC copolymers either from (i and ii) the sequential or (iii) simultaneous copolymerization of MLABe and TMC. |
Entry |
[TMC]0![]() ![]() ![]() ![]() ![]() ![]() |
TMC![]() ![]() |
Reaction timec | Conv. TMCd (%) | Conv. MLABed (%) | Comp.NMRTMC![]() ![]() |
![]() |
![]() |
![]() ![]() |
---|---|---|---|---|---|---|---|---|---|
a Monomer and alcohol equiv. relative to [(BDI)Zn[Si(Me3)2]]0. b Weight fraction of TMC and MLABe units in the feed and relative percentage of TMC and MLABe units in the feed. c Reaction times were not necessarily optimized. d Monomer conversion determined by 1H NMR. e Composition of the precipitated copolymer expressed as weight fraction of TMC and MLABe units in the copolymer; relative percentage of TMC and MLABe units in the copolymer, taking into account the TMC and MLABe conversions determined from 1H NMR analysis. f Theoretical molar mass value calculated from {([TMC]0/[BnOH]0 × Conv.TMC × MTMC) + ([MLABe]0/[BnOH]0 × Conv.MLABe × MMLABe) + MBnOH}, with MTMC = 102 g mol−1, MMLABe = 206 g mol−1 and MBnOH = 108 g mol−1. g Experimental molar mass value determined by SECvs.polystyrene standards. h Molar mass distribution value determined from SEC chromatogram traces. All data are representative of at least duplicated experiments. | |||||||||
1 | 200![]() ![]() ![]() ![]() ![]() ![]() |
50![]() ![]() |
MLABe—6 h + TMC—16 h | 2 | 85 | 2![]() ![]() |
3700 | 960 | 1.42 |
67![]() ![]() |
4![]() ![]() |
||||||||
2 | 200![]() ![]() ![]() ![]() ![]() ![]() |
50![]() ![]() |
TMC—3 min + MLABe—16 h | 99 | 88 | 53![]() ![]() |
7770 | 7600 | 1.29 |
67![]() ![]() |
69![]() ![]() |
||||||||
3 | 100![]() ![]() ![]() ![]() ![]() ![]() |
19![]() ![]() |
TMC—110 min + MLABe—40 h | 100 | 26 | 49![]() ![]() |
4290 | 4850 | 1.37 |
33![]() ![]() |
67![]() ![]() |
||||||||
4 | 100![]() ![]() ![]() ![]() ![]() ![]() |
19![]() ![]() |
TMC—110 min + MLABe—72 h | 100 | 96 | 21![]() ![]() |
10![]() |
6200 | 1.53 |
33![]() ![]() |
35![]() ![]() |
||||||||
5 | 200![]() ![]() ![]() ![]() ![]() ![]() |
50![]() ![]() |
TMC and MLABe 16 h | 70 | 90 | 44![]() ![]() |
6670 | 2450 | 1.62 |
67![]() ![]() |
61![]() ![]() |
||||||||
6 | 100![]() ![]() ![]() ![]() ![]() ![]() |
19![]() ![]() |
TMC and MLABe 48 h | 33 | 93 | 8![]() ![]() |
8440 | 2470 | 1.30 |
33![]() ![]() |
16![]() ![]() |
||||||||
7 | 100![]() ![]() ![]() ![]() ![]() ![]() |
19![]() ![]() |
TMC and MLABe 96 h | 78 | 99 | 16![]() ![]() |
9860 | 4250 | 1.35 |
33![]() ![]() |
29![]() ![]() |
Sequential copolymerization of MLABe with TMC has been carried out upon introducing both monomers in different order thereby resulting in copolymers with various chain end functions (Scheme 2). Addition of MLABe first followed by TMC (Table 3, entry 1, Scheme 2i) revealed the very slow copolymerization ability of TMC (only 2% conversion of TMC in 16 h) within experimental conditions and especially within the reaction time suitable for complete TMC homopolymerization (100% conversion of 200 equiv. of TMC by [(BDI)Zn[N(SiMe3)2]]0/[BnOH]0 = 1:
5 at 60 °C within 5 min).11,12 Under such operating conditions, MLABe/PMLABe thus inhibited the polymerization of TMC. The reverse addition sequence of comonomers, namely the introduction of the benzyl malolactonate once the complete conversion of the carbonate was achieved (i.e., within a few minutes), allowed the synthesis of the desired block copolymer PMLABe-b-PTMC (Table 3, entries 2–4, Scheme 2ii). When TMC was used in excess relative to MLABe (Table 3, entry 2), both monomers were almost fully converted within reaction times close to those expected from their behavior in the corresponding homopolymerizations; TMC was fully converted within 3 min as previously observed11 whereas MLABe was converted slightly more slowly when sequentially copolymerized with TMC (88% within 16 h, Table 3, entry 2) than when present just on its own (100% within 6 h; Table 1, entry 4). When the initial loading of MLABe was increased—to an amount larger than that of TMC (200
:
100, respectively, Table 3, entries 3 and 4)—the polymerization of the β-substituted β-lactone was slower with only 52 turnovers in 40 h or 192 turnovers in 72 h (Table 3, entries 3 and 4), as expected from the corresponding behavior of MLABe in homopolymerization (60 turnovers in 24 h for 200 equiv. MLABe, Table 1, entry 9, vs. 100 turnovers in 6 h for 100 equiv. MLABe, Table 1, entry 4). SEC analysis of the copolymers showed the increase in molar mass upon going from the PTMC first formed to the subsequent PMLABe-b-PTMC copolymer (Table 3, entry 4; Fig. 2). Such double monomer addition experiments further highlighted the “living” feature of the iROP exemplified above (Fig. 1).
![]() | ||
Fig. 2
SEC chromatograms of a PTMC (![]() ![]() ![]() ![]() ![]() ![]() |
Simultaneous MLABe and TMC addition allowed the synthesis of random copolymers in quite good yields (Table 3, entries 5–7, Scheme 2iii). Whichever the ratio of the comonomers in the feed (TMC/MLABe = 100:
200 or 200
:
100), MLABe always polymerized to a greater extent than TMC, reaching almost quantitative conversions (>90%). TMC, which under similar operating conditions would be fully homopolymerized,11 displayed partial conversion (<78%). The presence of MLABe/PMLABe in the reaction medium thus impeded the polymerization of the carbonate in agreement with the behavior observed in the sequential copolymerization above (Table 3, entry 1). MLABe (200 equiv.) polymerized significantly faster in the presence of TMC (100 equiv.) (Table 3, entry 6; 186 turnovers in 48 h) as compared to its homopolymerization (60 turnovers in 24 h, Table 1, entry 9). TMC was successfully copolymerized with MLABe with high conversion upon increasing the relative ratio of TMC-to-MLABe (Table 3, entry 6 vs. 5) or upon increasing the reaction time (Table 3, entry 6 vs. 7).
The molar composition of the isolated copolymers (Comp.NMR), determined from the integration of the characteristic 1H resonance of PTMC (CH2CH2CH2, δ ≈ 2.05 ppm) and PMLABe (CHC(O)OBe, δ ≈ 5.52 ppm) relative to the corresponding monomer, remained in agreement with the feed ratio (TMC:
MLABe). In addition, whatever the composition feed in monomers and the order of their addition, both block and random copolymers exhibited monomodal SEC traces and relatively narrow molar mass distributions (
w/
n < 1.62).
Alternatively, the block copolymers could be synthesized from the chemical coupling of both pre-synthesized homopolymers, namely carboxylic acid end-capped PMLABe5g and hydroxyl-end-functionalized PTMC11a,b (Scheme 3). A typical esterification between C6H5C(O)O-PMLABe-C(O)OH and H-PTMC-OBn, performed in CH2Cl2 using dicyclohexylcarbodiimide (DCC) as a coupling agent and 4-(dimethylamino)pyridine (DMAP) as a catalyst, as commonly encountered for polyesters,25 afforded after purification and precipitation the block copolymers C6H5C(O)O-PMLABe-b-PTMC-OBn (Table 4). 1H NMR spectrum clearly showed the presence of both blocks (vide infra); yet, it could not demonstrate the effective coupling of these two blocks. This was, however, evidenced from comparative SEC investigations of each homopolymers, of a mixture of both homopolymers and of the coupled homopolymers, i.e. the copolymer itself. Indeed, the chromatogram of a mixture of PMLABe and of PTMC gave two peaks corresponding to each homopolymer (Fig. S1†). Also, the chromatogram of the purified product resulting from their coupling was composed of a unique and distinct peak displaying a quite narrow molar mass distribution (Fig. S1†). This result demonstrated, in combination with NMR data, that the coupling reaction effectively gave access to the expected block copolymer PMLABe-b-PTMC, and not to a mixture of the two homopolymers. The combined NMR, SEC and DSC (vide infra) analyses thus supported the block structure of the copolymer. In addition, such results underlined the availability of both the carboxylic and the hydroxyl-end-functional groups on each homopolymers, for further chemical reaction. Besides they validate such a coupling as an alternative method for the preparation of PMLABe-b-PTMC block copolymers. Noteworthy, this coupling approach to the copolymers also allows the introduction of a selected biologically active molecule at the free chain end of the previously synthesized PMLABe block, this molecule being introduced during the initial anionic ROP of MLABe.5,6
![]() | ||
Scheme 3 Schematic representation of the synthesis of C6H5C(O)O-PMLABe-b-PTMC-OBn from the direct coupling of C6H5C(O)O-PMLA-C(O)OH and H-PTMC-OBn upon esterification. |
Entry | PMLABe | PTMC | PMLABe-b-PTMC | |||
---|---|---|---|---|---|---|
![]() |
![]() ![]() |
![]() |
![]() ![]() |
![]() |
![]() ![]() |
|
a Experimental molar mass value determined by SECvs.polystyrene standards. b Molar mass distribution value determined from SEC chromatogram traces. c Experimental molar mass value determined by SECvs.polystyrene standards and corrected by 0.73.8b | ||||||
1 | 9300 | 1.40 | 5700 | 1.60 | 9230 | 1.46 |
2 | 11![]() |
1.34 | 5500 | 1.48 | 6300 | 1.58 |
![]() | ||
Fig. 3 1H NMR (500 MHz, CDCl3, 23 °C) spectrum of a PMLAHe synthesized from the (BDI)Zn(N(SiMe3)2)/BnOH system (Table 1, entry 5). |
![]() | ||
Fig. 4 1H NMR (200 MHz, CDCl3, 23 °C) spectrum of a PMLABe-b-PTMC synthesized from the (BDI)Zn(N(SiMe3)2)/BnOH system (Table 3, entry 4) (* refers to residual MLA). |
Differential scanning calorimetry (DSC) thermograms of block copolymers exhibit two glass transitions corresponding to each block as illustrated with PMLABe40-b-PTMC20 (Table 3, entry 4; Tg +47.9 °C, −10.5 °C, Fig. 5). No melting temperature was observed in agreement with the racemic feature of the MLABe used and with the amorphous nature of PTMC. These data confirm the block structure of the copolymers prepared from either sequential copolymerization or coupling of the homopolymers. As illustrated with PMLABe40-co-PTMC16, DSC analysis of copolymers obtained through simultaneous copolymerization exhibits a unique glass transition temperature (Tg +19 °C, Table 3, entry 7) intermediate between those of PMLABe (Tg ≈ +29.6 °C, n = 7900 g mol−1)17d and PTMC (Tg ≈ −15 °C,
n = 10
000 g mol−1)8b in close agreement with the Fox equation, thereby supporting the random structure of the copolymers (Fig. 5).
![]() | ||
Fig. 5 DSC traces of a PMLABe-b-PMTC and PMLABe-co-PMTC (Table 3, entries 4 and 7, respectively; heat flow expressed in mW as a function of temperature expressed in °C; second run). |
Footnote |
† Electronic supplementary information (ESI) available: 1H and 13C NMR data of H-PMLABe-OBn, H-PTMC-b-PMLABe-OBn, and C6H5CH2C(O)O-PMLABe-b-PTMC-OBn, and SEC chromatograms of a mixture of a PMLABe and a PTMC and of the PMLABe-b-PTMC block copolymer obtained by their coupling. See DOI: 10.1039/c0py00368a |
This journal is © The Royal Society of Chemistry 2011 |