Paulina Maksym-Bębeneka,
Tadeusz Bielab and
Dorota Neugebauer*a
aDepartment of Physical Chemistry and Technology of Polymers, Faculty of Chemistry, Silesian University of Technology, M. Strzody 9, 44-100 Gliwice, Poland. E-mail: dorota.neugebauer@polsl.pl
bCentre of Molecular and Macromolecular Studies, Polish Academy of Sciences, Sienkiewicza 112, 90-363 Łódź, Poland
First published on 1st December 2014
A series of well-defined amphiphilic graft copolymers based on poly(propylene glycol)methacrylate (PPGMA) extended with a polymethacrylate segment containing methacrylic acid units was successfully synthesized, combining atom transfer radical polymerization (ATRP), esterification, “grafting from” polymerization, and acidolysis. The multistep procedure yielded hydroxy-functionalized polymers (6–47 mol% of PPGMA), bromoester-functionalized copolymers as multifunctional macroinitiators (nBr = 8–25), PPGMA-based copolymers with poly(tert-butyl methacrylate) (PtBMA) segments (DPtBMA = 18–59), and copolymers varying in hydrophilic fraction content (FMAA = 0.28–0.54). After the generation of methacrylic acid units the PPGMA-based graft polymers attained a good solubility in polar solvents such as methanol and water. The particles, which were formed in aqueous solution, achieved sizes in the nanoscale range (165–230 nm) and negative zeta potentials.
The presence of pendant reactive –OH groups in polymers as substituents or at the end of side chains is an advantage for their further modification by various types of reactions; hence, these groups are useful for changing the physicochemical properties of macromolecules. One possibility is to use them directly for grafting reactions via ring-opening polymerization of cyclic monomers (for example, ε-caprolactone19,20 or lactide). Another strategy is based on the transformation of hydroxyl groups in linear polymers to halogenoesters. For example, PHEMA can be converted to poly(2-(2-bromoisobutyryloxy)ethyl methacrylate) (PBIEM), and then used as a multifunctional macroinitiator in “grafting from” polymerization.21 This strategy makes it possible to combine polymeric segments with different natures in branched structures which, similarly to linear block copolymers, can exhibit good phase separation and can be used in a variety of applications.22 However, because of their nonlinear topology they generally have lower melt viscosities, which is especially useful for processing.23 Recently, our group has reported the synthesis of well-defined amphiphilic and biocompatible polymers containing 5 mol% of PEGMA grafts extended by extra hydrophilic segments of poly(methacrylic acid) (PMAA), which significantly improved the solubility in polar solvents, including water.11 Solubility in aqueous solutions, as well as the composition and topology of polymers, is strongly recommended for biomedical applications, for example in the field of drug carriers.
Herein, we describe a versatile multistep procedure for the synthesis of another type of amphiphilic graft polymethacrylate with segments of PPG (5 units) and MAA units in the side chains, as shown in Scheme 1. ATRP provides well-defined PPGMA based copolymers with a high polymerization degree in the backbone (DPn = 100–225, including nPPGMA = 10–75) and relatively long PtBMA side chains (DPtBMA = 20–60), whereas esterification and acidolysis reactions guarantee the selective modification of hydroxyl groups to bromoester groups and the removal of tert-butoxy groups to introduce carboxyl groups, respectively. According to the literature, in the late 80’s PPGMA/MMA copolymers were prepared by conventional radical polymerization,24,25 whereas the other PPGMA copolymers mentioned above were applied as surface-engineered particles or hydrogels. Our work is focused on the first-time use of modified short-grafted PPGMA copolymers as new multifunctional macroinitiators in “side chain extension” polymerization to prepare biocompatible branched weak polyacids, which have the potential for self-assembly to form nanoparticles with drug entrapment capabilities.
No. | fPPGMA [mol%] | Time [h] | GC | NMR | GPCb | |||||
---|---|---|---|---|---|---|---|---|---|---|
xMMA [%] | nMMA | x [%] | DPn | FPPGMA [mol%] | Mn,NMR × 10−3 [g mol−1] | Mn,GPC × 10−3 [g mol−1] | Mw/Mn | |||
a CuBr/dNbPy = 0.75/1.5 as the catalytic system.b RI detector, CH2Cl2, PS standards; fPPGMA: initial PPGMA molar content in the reaction mixture; xMMA: conversion of MMA; x: overall monomer conversion; nMMA = xMMA[MMA]0/[EtBriBu]0 means the number of MMA units incorporated into the polymer; DPn = x([PPGMA]0 + [MMA]0)/[EtBriBu]0; FPPGMA: molar content of PPGMA units in the copolymer; Mn,NMR = x(375[PPGMA]0 + 100[MMA]0)/[EtBriBu]0.c PPGMA + MMA/EtBriBu/CuBr/PMDETA = 500/1/1/1; anisole = 30 vol%; T = 60 °C. | ||||||||||
I | 5 | 1 | 23 | 109 | 31 | 155 | 6.6 | 18.5 | 24.5 | 1.26 |
II | 10 | 0.2 | 21 | 93 | 23 | 116 | 13.0 | 15.7 | 18.6 | 1.25 |
III | 10 | 1 | 34 | 153 | 33 | 167 | 12.9 | 22.6 | 29.6 | 1.18 |
IVa | 10 | 0.5 | 19 | 86 | 23 | 115 | 12.8 | 15.4 | 16.0 | 1.36 |
Va | 10 | 1 | 23 | 104 | 25 | 125 | 9.3 | 16.7 | 18.5 | 1.31 |
VIa | 10 | 2 | 28 | 126 | 27 | 132 | 12.0 | 18.0 | 17.3 | 1.39 |
VII | 15 | 1 | 35 | 149 | 36 | 180 | 14.8 | 25.4 | 30.4 | 1.27 |
VIII | 25 | 0.3 | 15 | 56 | 21 | 105 | 35.9 | 21.0 | 21.5 | 1.18 |
IX | 25 | 0.6 | 36 | 135 | 34 | 170 | 23.1 | 27.8 | 34.4 | 1.22 |
X | 25 | 1 | 41 | 154 | 45 | 225 | 24.0 | 37.4 | 45.6 | 1.29 |
XIa | 50 | 1 | 45 | 113 | 32 | 160 | 47.4 | 36.7 | 28.0 | 1.19 |
The chemical structures of the PPGMA-based copolymers after purification by repeated precipitation were characterized by 1H NMR spectroscopy. As shown in Fig. 1, the characteristic peaks corresponding to the methylene (A) and methyl protons (B) in the backbone are observed at 1.81 ppm and 0.65–1.3 ppm, respectively. Additionally, the protons of the methyl groups in the PPG side chains (1.20 ppm; E) are overlapped with these signals in the latter range of chemical shifts. The content of PPGMA units in the copolymer (FPPGMA) was estimated using these signals. The other signals were assigned to the methoxy protons of the MMA units (3.60 ppm; F) as well as the methylene and methine protons in the PPG chains of PPGMA units (3.14–4.22 ppm; C, D). 1H NMR was also used for analysis of reaction mixture samples to monitor the progress of polymerization via total monomer conversion (x), whereas conversion of MMA (xMMA) was determined by GC. The conversion parameters allowed calculation of the polymerization degree of polymethacrylate chains (DPn) and the number of MMA units (nMMA) introduced into the copolymer.
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Fig. 1 1H NMR spectra of P(MMA-co-PPGMA) copolymers with varying content of PPGMA units obtained with an initial macromonomer feed in the range of 5–50 mol%. |
The P(MMA-co-PPGMA) copolymers were prepared in total monomer conversions of 21–45%. Various compositions were correlated with 10–75 units of PPGMA distributed along the polymethacrylate backbone with DPn in the range of 105–225, which yielded different grafting degrees of the short PPG chains as indicated by the content of PPGMA units (7–47 mol%). ATR copolymerization of PPGMA and MMA in the presence of 10 mol% initial feed of PPGMA was performed in two catalyst systems with different activity, CuBr/PMDETA vs. CuBr/dNbPy (II and III vs. IV–VI). A lower conversion within 1 h was obtained using the system with the latter catalyst (25% of V vs. 33% of III), indicating a reduced polymerization rate and broader molecular weight distribution (1.31 vs. 1.18). The kinetic plots in Fig. 2 confirm this observation and show some deviation from a linear relationship in the first-order time–conversion dependence. With CuBr/PMDETA, the process was well-controlled for the initial 20 min (21% conversion) and then proceeded more slowly, whereas in the second system, after 20 min the consumption of monomer was linear, but much lower.
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Fig. 2 Kinetic plots of the semilogarithmic dependence of conversion vs. time for reactions III and V performed in various catalytic systems ([MMA]0/[PPGMA]0 = 90/10 mol%). |
On the other hand, polymerizations IV–VI (fPPGMA = 10 mol%) performed under the same conditions but stopped at different times (0.5–2 h) indicated insignificant progress of conversion from 23 to 27% with the change in dispersity index (1.31–1.39). Similar behavior was also observed for polymerizations VIII–X (fPPGMA = 25 mol%). However, with a larger initial feed of PPGMA the change in conversion with reaction time was more spectacular, increasing from 21–45% in 0.3–1 h. The tendency of the conversion to increase on increasing the initial feed of PPGMA, which was monitored under comparable conditions (31% at fPPGMA = 5 mol%, 33% at 10 mol%, 36% at 15 mol%, and 45% at 25 mol% after 1 h), caused us to perform the next polymerization with 50 mol% of PPGMA with the less active catalyst complex CuBr/dNbPy, to avoid too fast a reaction and to minimize the participation of side reactions. In this case, 32% of the comonomers were converted to polymer XI containing 160 repeating units in the backbone, including 75 units of PPGMA with short side chains. As can be seen in Fig. 3a, the GPC traces display unimodal and narrow peaks without any tailing. The values of Mn,GPC obtained from conventional GPC in comparison with those from 1H NMR analysis showed some discrepancies in the method error range (Fig. 4a). The additional GPC analysis with a MALLS detector confirmed good agreement of the absolute Mn,MALLS with Mn,NMR, with one significant exception for copolymer XI obtained at the highest feed of PPGMA. In that case, Mn,MALLS ∼ 2xMn,NMR (58200 vs. 36
500 g mol−1), whereas the molecular weight distribution was narrow (Mw/Mn,MALLS = 1.19), suggesting chain coupling termination.
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Fig. 3 GPC traces of copolymers with varying content of PPGMA (13–46 mol%) (a) and a series of hydroxyl-functionalized copolymers, PPGMA-based MI, and tBMA modified copolymers (b). |
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Fig. 4 Dependence of molecular weight on PPGMA content in hydroxyl-functionalized copolymers (a), polymerization degree of tBMA (b), and grafting degree (c) in graft copolymers. |
The diagram of instantaneous monomer-copolymer composition in Fig. 5 is related to the dependence of the content of PPGMA units in the copolymer (FPPGMA) vs. the initial feed of PPGMA in the polymerization mixture (fPPGMA). It shows that the composition of the copolymer is proportional to the monomer mixture, showing good agreement with a typical dependence for a “random copolymer” (solid line).
The “side chain extension” polymerizations (Scheme 1c) were conducted under ATRP conditions using a CuCl/PMDETA catalyst system and multifunctional macroinitiators based on PPGMA copolymers with active bromoester groups, obtained by the esterification of hydroxyl groups (Scheme 1b). The content of initiating sites was close to that of hydroxyl groups because the functionalization reaction proceeded with a high efficiency of 91–92% (MI I–MI VII). To avoid irreversible coupling reactions and gel formation, all polymerizations were performed in a highly diluted system (anisole/monomer = 1/1 v/v). Table 2 summarizes the molecular characteristics of the PPGMA based copolymers with side chains extended by PtBMA segments. P[MMA-co-(PPGMA-graft-PtBMA)] copolymers were obtained in monomer conversions of 5–45%, determined by GC. Various compositions were correlated with the polymerization degree of PtBMA and the grafting density of block copolymers (DPtBMA = 18–59 per graft and DGB = 6–14 mol%), which yielded varying content of tBMA in the copolymer (FtBMA = 60–92 wt%). The graft copolymers XII–XIV, based on MI I containing 9 initiating groups in the chain (nBr), which correlated with DGB = 6 mol%, had varying lengths of graft (19 vs. 29 vs. 59 units per graft, respectively) without any influence on the molecular weight distribution (Mw/Mn ≤ 1.25). However, the dispersity index increased for copolymers XV–XVII (DPtBMA = 18–56, Mw/Mn = 1.4), with a larger grafting density of the PPG-bl-PtBMA side chains (12–14 mol%). In the case of XVIII, containing the largest amount of side chains, the reaction was continued up to the highest value of monomer conversion, yielding a drastically high dispersity (Mw/Mn > 2), which led us to assume the occurrence of side reactions accompanied by steric hindrance effects.
No. | MI (nBr) | [tBMA]0/[MI]0 | Time [h] | GC | NMR | GPCa | |||
---|---|---|---|---|---|---|---|---|---|
xtBMA [%] | DPtBMA | Mn,calc × 10−3 [g mol−1] | FtBMA | Mn,GPC × 10−3 [g mol−1] | Mw/Mn | ||||
a RI detector, CH2Cl2, PS standards; MI are bromoester-functionalized P(MMA-co-PPGMA) copolymers, based on PPGMA copolymers I–III and VII; nBr = DPn × FPPGMA × EfE, where nBr is the number of bromine functional groups obtained by esterification of the hydroxyl groups of PPGMA units in the copolymer, DPn is the polymerization degree of the backbone, FPPGMA is the PPGMA content in the copolymer, EfE is the efficiency of esterification, equal to 91–92%; DPtBMA = xtBMA[tBMA]0/[MI]0; Mn,calc = Mn,NMR + 150 nBr + 142 DPtBMA, where Mn,NMR is the molecular weight of the hydroxyl-functionalized copolymer and 150 is the molecular weight of the bromoester group (–COC(CH3)2Br–1H).b [MI]0/[CuCl]0/[PMDETA]0 = 1/1/1; anisole = 100 vol%; T = 60 °C. | |||||||||
XII | MI I (9) | 450 | 1 | 5 | 19 | 44.7 | 0.60 | 26.2 | 1.23 |
XIII | MI I (9) | 400 | 2 | 8 | 29 | 58.4 | 0.72 | 29.0 | 1.25 |
XIV | MI I (9) | 275 | 3 | 22 | 59 | 87.5 | 0.77 | 35.3 | 1.24 |
XV | MI II (14) | 175 | 5 | 23 | 40 | 96.2 | 0.89 | 27.2 | 1.37 |
XVI | MI III (19) | 150 | 2 | 39 | 56 | 179.3 | 0.93 | 36.1 | 1.44 |
XVII | MI VII (25) | 50 | 2 | 34 | 18 | 91.6 | 0.74 | 44.9 | 1.38 |
XVIII | MI VII (25) | 100 | 4 | 45 | 47 | 195.2 | 0.92 | 59.0 | 2.06 |
The values of Mn,GPC obtained from conventional GPC were lower than those from the 1H NMR analysis. This discrepancy considerably increased with the length (Fig. 4b) and the number of PtBMA segments in the side chains (Fig. 4c). Both structural parameters of branching could be responsible for a gradual decrease in the hydrodynamic volume of the macromolecules, causing a difference in relation to the linear polymer standards used for calibration in the GPC method.
The tert-butyl groups of the PtBMA segments in the side chains were cleaved by treatment with TFA in dichloromethane, to yield amphiphilic P[MMA-co-(PPGMA-graft-PMAA)] copolymers with acidic groups (FMAA = 28–54 wt%). The modification of hydrophobic polymers to give carboxyl-functionalized ones (Scheme 1d) was observed by significant changes in solubility. Both hydroxyl-functionalized PPGMA copolymers and the copolymers with PtBMA segments in the side chains were completely insoluble in polar solvents, but after acidolysis, the copolymers did not dissolve in methylene chloride, while retaining good solubility in THF, but they could also be dissolved in methanol and in water.
The modification steps starting from hydroxyl-functionalized PPGMA copolymers, including preparation of the multifunctional macroinitiator, “side chain extension” polymerization and acidolysis, were confirmed by spectroscopic analyses. In the 1H NMR spectra (Fig. 6a), the peak assigned to the methyl protons in the bromoester group at 1.94 ppm (G) and the peaks characteristic of the protons of the tert-butyl group at 1.25–1.31 ppm (H), which dramatically decreased after the cleavage of tert-butyl groups during acidolysis, demonstrate the formation of the multifunctional MI, then the grafted copolymer, and the modified copolymer with a fraction of MAA units. In the FT-IR spectra (Fig. 6b), the asymmetric double peak characteristic of the tert-butyl group at 1360–1390 cm−1 for the graft copolymer with PtBMA segments in the side chains significantly diminished after modification. Additionally, the GPC traces of P(MMA-co-PPGMA), P(MMA-co-PPGMA)-Br and P[MMA-co-(PPGMA-graft-PtBMA)] in Fig. 3b show the progressive increase in molecular weight due to the introduction of bromoester groups and the extension of the side chains by PtBMA segments, which is observed by the peak shifting towards a lower elution volume, while narrow dispersities are maintained.
The results of hydrodynamic diameter (dh) measurements, which were performed at 25 °C in deionized water, are summarized in Table 3. The smallest particles, reaching sizes around 165 nm, were formed by XIIIA, with a low grafting degree and medium length of side chains. They became larger for longer grafts at the same graft number (XIIIA vs. XIVA and XVIIA vs. XVIIIA), whereas the latter pair of copolymers exhibited larger diameters due to a higher grafting degree. A representative histogram is presented in Fig. 7a. Another correlation of increasing particle diameter was observed with respect to the content of the hydrophilic fraction in the copolymers, in the following order: XIIIA > XVIA > XVIIIA. According to this relation, the sample XVIIA should give larger aggregates than actually resulted, but this can be explained by short grafts in combination with another important parameter, the efficiency of acidolysis, which in this case yielded almost full transformation of tert-butoxyl groups into carboxyl ones (89%), whereas for the other copolymers the efficiency was significantly lower (52–64%). The amount of MAA units in XVIIA was lower than for XVIA and XVIIIA, which correlated with the result of the zeta potential (ζ-potential, Table 3, Fig. 7b) showing a negative value close to zero, and almost neutral nanoparticle surface. The measurements were performed in an environment of deionized water at 25 °C. The negative values are typical for carboxyl-functionalized copolymers, which are generally well known for pH-sensitivity.
No. | Ngraft | DGB [%] | NMR | DLS | Zeta potential [mV] | |||
---|---|---|---|---|---|---|---|---|
EfA | nMAA/ntBMA | FMAA | dh [nm] | PDI | ||||
a Ngraft: number of side chains equal to nBr; DGB: percentage degree of grafting based on the content of PPGMA grafts; EfA: efficiency of acidolysis; nMAA: number of MAA units after acidolysis; ntBMA: number of tBMA units before acidolysis; FMAA: content of MAA units in the graft copolymer; dh and PDI: hydrodynamic diameter of particles and polydispersity of sizes; nd – not determined. | ||||||||
XIIA | 9 | 6 | 0.64 | 12/19 | 0.28 | nd | nd | nd |
XIIIA | 9 | 6 | 0.55 | 16/29 | 0.29 | 166 | 0.445 | −41 |
XIVA | 9 | 6 | nd | nd/59 | nd | 203 | 0.336 | nd |
XVA | 14 | 12 | nd | nd/40 | nd | 231 | 0.549 | nd |
XVIA | 19 | 12 | 0.52 | 29/56 | 0.37 | 221 | 0.358 | −8 |
XVIIA | 25 | 14 | 0.89 | 16/18 | 0.54 | 183 | 0.309 | −3 |
XVIIIA | 25 | 14 | 0.61 | 29/47 | 0.44 | 224 | 0.140 | −26 |
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Fig. 7 Size distribution by intensity for XVIIIA (left), and zeta potential distribution (right) in deionized water at 25 °C. |
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