Xiaodong
Liu
,
Lifen
Zhang
*,
Zhenping
Cheng
* and
Xiulin
Zhu
Suzhou key Laboratory of Macromolecular Design and Precision Synthesis, Jiangsu Key Laboratory of Advanced Functional Polymer Design and Application, Department of Polymer Science and Engineering, College of Chemistry, Chemical Engineering and Materials Science, Soochow University, Suzhou 215123, China. E-mail: chengzhenping@suda.edu.cn; zhanglifen@suda.edu.cn; Fax: +86-512-65882787
First published on 26th November 2015
The development of an atom transfer radical polymerization (ATRP) system without any transition metal catalyst for electronic and biomedical applications was considered to be in pressing need. Fluorescein (FL) was used as the organic photocatalyst for the polymerization of methyl methacrylate (MMA) via the proposed photoinduced electron transfer–atom transfer radical polymerization (PET–ATRP) mechanism. In the presence of electron donors provided by triethylamine (TEA), fluorescein can activate alkyl bromide and control radical polymerizations by a reductive quenching pathway. The polymerizations could be controlled by an efficient activation and deactivation equilibrium while maintaining the attractive features of “living” radical polymerization. The number-average molecular weight Mn,GPC increased with monomer conversion, and the controllability of molecular weight distributions for the obtained PMMA could be achieved in the polymerization processes. MALDI-TOF MS, 1H NMR spectroscopy and chain extension polymerizations show reserved chain-end functionality in the synthesized polymers and further confirm the “living” feature of the metal-free ATRP methodology. All these research results support the feasibility of the visible light mediated metal-free PET–ATRP platform for the synthesis of elegant macromolecular structures.
Transition metals (e.g., iridium and ruthenium) have been previously utilized as photoredox catalysts to mediate radical polymerization under light irradiation. Ruthenium(II)polypyridine complexes (e.g., RuII(bpy)3) can activate alkyl halides through the Ru(bpy)3+ photoredox cycle under visible light irradiation;14 while the excited fac-[Ir(ppy)3]* species15 could directly reduce an alkyl bromide initiator via a PET process to provide the desired alkyl radical and subsequently initiate polymerization. Besides, organo-cobalt porphyrins,16 both as a photoinitiator and a mediator, undergo photo-cleavage of the Co–C bond to give an organic radical and a cobalt(II) porphyrin metal-central radical for chain propagation with good control over the molecular weight and polydispersity. However, these obtained products and traditional ATRP polymers are inevitably contaminated with trace metal residues that cause distress for electronic and biomedical applications. The elimination of transition metals entirely eliminates the necessary step for purification of the synthesized polymers. Photocatalysis employed under visible light is undoubtedly one of the promising strategies to meet the increasing demand for more sustainable green chemical processes, and employing visible light photoredox catalysis for controlled/“living” radical polymerization is an emerging research focus area attracting significant interest in material and biological chemistry. However, it remains a great challenge to adopt metal-free catalytic systems to ATRP with an alkyl bromide commonly used as the initiator. Outstanding work reported by Hawker,10a Miyake10b and Matyjaszewski10c provided a good demonstration for further research, and the organic photoredox catalysts, 10-phenylphenothiazine (PTH) and perylene, have generated considerable interest in this research field.
The PET–RAFT technique employed by Boyer8b,17 was effectively conducted to activate/mediate controlled/“living” radical polymerization, and the PET mechanism is believed to be an efficient process to activate thiocarbonylthio compounds to generate radicals and thereby initiate controlled free radical polymerization. For example, Boyer et al. used a series of organo-dyes (e.g., eosin Y) as the catalysts to successfully conduct PET–RAFT for a variety of functional monomers, including N,N-dimethylaminoethyl methacrylate, hydroxyl ethyl methacrylate, pentafluorophenyl methacrylate, glycidyl methacrylate, oligoethylene glycol methyl ether methacrylate (OEGMA), and methacrylic acid.8f Various organic photocatalysts have been extensively exploited as green photoredox catalysts for a series of radical-mediated organic reactions because of their easy availability, low cost and toxicity.18 We envisaged that the unique properties of these catalysts would be promising for the development of photo-controlled living radical polymerization. Recently, fluorescein (FL) has been studied as a photoredox catalyst due to its visible region absorbance (∼450 nm), chemical stability, long excited-state lifetime, and favourable redox potential.18e Upon visible light photon absorption, FL is converted to its excited state FL*, and through a reductive quenching pathway by an electron donor (e.g., trialkylamines), a powerful single-electron reductant, FL˙− (E0 = −1.22 V), was generated, which can dechlorinate organic halides to provide carbon-central radical species. In this paper, based on this theoretical research background, we reported a novel methodology of metal-free photoinduced electron transfer–atom transfer radical polymerization (PET–ATRP), using methyl methacrylate (MMA) as the model monomer conducted by using FL as an effective organic visible-light photocatalyst. The controllability of the radical polymerization of MMA was achieved by the organic-catalyzed blue light mediated process. Through a reductive quenching pathway, the photocatalytic reductive dehalogenation of ethyl α-bromophenylacetate and subsequent initiation of the radical polymerization were realized by the aforementioned single-electron reductant FL˙− under blue light irradiation, and the polymerization process could be directly activated/deactivated by “on/off” light irradiation. The effects of acid–alkali polymerization conditions, initiator, light source, solvent, catalyst concentration, polymerization degree (DP) etc. on metal-free PET–ATRP of MMA were systematically investigated to optimize the polymerization conditions. Not only was the “living” feature of polymerization further clarified, but also the metal-free PET–ATRP mechanism was proposed by our research in detail.
800 g mol−1, Mw/Mn = 1.27), and the macroinitiator-2 was synthesized under the molar ratio of [MMA]0/[EBPA]0/[FL]0/[TEA]0 = 200/1/0.4/12 for 2 h (Mn,GPC = 19
400 g mol−1, Mw/Mn = 1.30). The polymerization and purification processes were performed under the general conditions as previously mentioned.
In a typical experimental procedure for chain-extension polymerization of MMA, macroinitiator-1 (100 mg, 5.39 μmol, 0.19 equiv.), fluorescein (9.3 mg, 0.028 mmol, 1 equiv.), TEA (116 μL, 0.84 mmol, 30 equiv.) and MMA (1.00 mL, 9.43 mmol, 337 equiv.) were dissolved in 2.0 mL of DMSO, and the reaction was irradiated with a blue LED for 48 h before the polymer was isolated by precipitation from methanol. In chain-extension polymerization of St, macroinitiator-2 (100 mg, 5.22 μmol, 0.19 equiv.), fluorescein (9.3 mg, 0.028 mmol, 1 equiv.), TEA (116 μL, 0.84 mmol, 30 equiv.) and St (1.00 mL, 8.73 mmol, 312 equiv.) were dissolved in a mixture solution of DMSO (1.0 mL) and DMF (1.0 mL). The reaction mixture was irradiated with blue LED irradiation for 24 h before the polymer was purified as mentioned above.
Control experiments proved that omission of any single component (FL, EBPA, TEA or light source) could result in either uncontrolled or no polymeric products (Table S1,† entries 1–4). These results clearly revealed that control over polymerization results from the photocatalyst mediating with light as an external stimulus. Of particular importance is to eliminate the disruptive effects from any possible iniferter agent. In the absence of triethylamine, trace amounts of uncontrolled polymers (2.6% of monomer conversion, Mn = 62
100, Mw/Mn = 1.92) were obtained, indicating that fluorescein is proposed as an inefficient photoiniferter agent for photopolymerization reactions. While in the presence of triethylamine, no polymer was collected from the reaction system without any initiator, indicating that no obvious disadvantageous effects were generated from the photoiniferters on the polymerization. Specifically, in the synthesis of the block copolymer, this feature could prevent interference from homopolymers initiated from dye molecules. Besides, upon irradiation with blue LED light with an emission maximum at 458 nm, this xanthene-based dye was proved to be sufficiently stable under the reaction conditions.
Of particular note is that when the organic-based photoredox catalyst is employed under conditions without either TEA or acetic acid, the polymerization was absolutely out of control (entry 9 in Table S2,†Mn,GPC = 58
500, Mw/Mn = 2.54). Meanwhile, the monomer conversion (Conv. 6.4%) and initiation efficiency (I* = 2.6%) were both rather low, indicating that the initiator was almost not consumed. This further verifies that an organic catalyst in a highly reducing state is needed to activate the alkyl bromide. Within the organic catalytic cycle, as the initial recyclable electron reservoir, the oxidation of TEA provides the electron for the reductive quenching of the dye's excited state FL*, and the formed FL˙− can reduce an alkyl halide under visible light irradiation to produce the electron-deficient alkyl radical for chain propagation (Table S2,† entries 1–8). Thus the important function of TEA is not only to ensure that the chemical structure of fluorescein is in ring-opened form, but also to act as an electron donor. The following sections mainly discuss the polymerization processes performed under the condition of TEA up to 30 times the content of photocatalyst.
000 g mol−1, Mw/Mn = 1.57) in the situation of yellow LED irradiation for 22 h deviated considerably from the theoretical value (Mn,th = 3970 g mol−1). While under blue LED irradiation, the polymerization was relatively well-controlled with high initiation efficiency (entries 5–7 in Table S1†). Thus in the following discussion, the polymerization was performed by exposure to blue LED irradiation.
calculated from the slopes showed that the polymerization in DMSO (kappp = 6.78 × 10−5 s−1) was much faster than in DMF (kappp = 3.76 × 10−5 s−1), thus DMSO was selected as the most suitable solvent for this polymerization system.
Subsequently, the effect of solvent volume of DMSO on polymerization was further studied, and the results are shown in Tables S5 and S6,† respectively. The polymerization rate decreased with the increase of solvent volume. In the molar ratio of [MMA]0
:
[EBPA]0
:
[FL]0
:
[TEA]0 = 200/1/0.3/9, the monomer conversion reached up to 68.6% under 8 h irradiation in 1.0 mL of DMSO (entry 2 in Table S5†), whereas 38.9% and 77.2% of conversion for the cases with 2.0 mL of DMSO could be obtained after 7 h (entry 4 in Table S5†) and 35 h (entry 5 in Table S5†), respectively. However, as the volume of DMSO in the polymerization system was 4.0 mL, the reaction rate seemed to be higher than that in the case of 2.0 mL. This phenomenon was similar to the situation at the molar ratio of [MMA]0
:
[EBPA]0 = 200/1 with different photocatalyst contents as discussed in the following section, in which the polymerization rate would be faster in the system of lower photocatalyst concentration. Meanwhile, the growth trend of molecular weight seems to be modest. When 1.0 mL of DMSO was used as the solvent, the molecular weight at 68.6% conversion (Mn,GPC = 23
500, Mw/Mn = 1.51) was lower than that at 34.4% conversion (Mn,GPC = 25
100, Mw/Mn = 1.39). The possible reason is that under this condition the activation of bromide at polymer chain end was slightly less efficient, and continuous initiation activities were conducted throughout the whole polymerisation process. In the later polymerization period when most of monomers were consumed, the later growing polymers of low molecular weight took their share of the monomer conversion and the averaged molecular weight. Only in the case of 2.0 mL of solvent does the number-average molecular weight clearly increase, and initiation efficiency was also raised along with increasing conversion. Unfortunately, the molecular weights of the polymers determined by GPC deviated from the theoretical ones, and the molecular weight distributions become relatively broader with the increase of monomer conversion. At the molar ratio of [MMA]0
:
[EBPA]0
:
[FL]0
:
[TEA]0 = 400
:
1
:
0.4
:
12, similar experimental results were obtained as well (entries 3–9 in Table S6†). Therefore, we focused our attention on the polymerization of MMA in 2.0 mL of DMSO in the following investigation.
:
[EBPA]0 = 200
:
1
:
[EBPA]0
:
[FL]0
:
[TEA]0 = 200
:
1:x
:
y (x = 0.1–0.3, x
:
y = 1
:
30), the kinetic plots and the evolution of Mn,GPC and Mw/Mn with conversion at this polymerization degree were studied as illustrated in Fig. 1 and S1.† The molecular weights increased with conversion throughout the polymerization, and the experimentally measured molecular weights (Mn,GPC) were relatively greater than the theoretical ones, giving a slight low initiator efficiency (I*) probably caused by the low deactivator concentration and deactivation rate constants. When increasing the proportion of fluorescein ([MMA]0
:
[EBPA]0
:
[FL]0
:
[TEA]0) from 200/1/0.1/3 to 200/1/0.3/9, improved control over Mn,GPC could be achieved with molecular weight much closer to the theoretical values. In addition, as the first-order kinetic plot showed a downward curvature, the higher fluorescein proportion greatly decelerated the polymerization processes with a much lower polymerization rate than that of systems with lower dosage and ratio of the catalyst, and this was also accompanied by an increase in molecular weight distribution (Mw/Mn) to around 1.6. The calculated kappp values were 6.12 × 10−5 s−1, 1.77 × 10−5 s−1 and 1.12 × 10−5 s−1 corresponding to x = 0.1, 0.25 and 0.3, respectively, which further demonstrated that the polymerization rate decreased as the amount of fluorescein increased. One possible explanation would be related to the radical concentration; the high load of catalyst leads to higher concentration of polymer-end radicals which leads to more termination reaction.
:
[EBPA]0 = 400
:
1
:
[EBPA]0
:
[FL]0
:
[TEA]0) of 400
:
1
:
0.3
:
9 and 400
:
1
:
0.4
:
12. The linearity of the kinetic plots in both cases indicated that the polymerization was approximately in a first order relationship with respect to the monomer concentration, and the propagation radicals kept constant during the polymerization process. When the conversion was less than 50%, the molecular weight (Mn,GPC) increased with monomer conversion and was higher than the theoretical values. The gap between molecular weights determined by GPC and theoretical ones was probably ascribed to the low initiation efficiency and lagging establishment of the dynamic equilibrium between active and dormant species. The photocatalytic reductive dehalogenation of initiator and polymer chain propagation always existed throughout the whole polymerization process, and molecular weights seem to approach theoretical values in more than about 50% conversion, suggesting the tendency of complete initiation with the increase of monomer conversion. Both at molar ratios ([MMA]0
:
[EBPA]0
:
[FL]0
:
[TEA]0) of 400
:
1
:
0.3
:
9 and 400
:
1
:
0.4
:
12 (entries 6–7 in Table S1†), the initiation efficiency was as high as 91% during the late period of polymerization (>85% Conv.). Yet, at the same time, the molecular weight distributions (Mw/Mn) become slightly broader than that in conversion less than 50%. By comparing the experimental results at 400
:
1
:
0.3
:
9 (kappp = 3.12 × 10−5 s−1) and at 400
:
1
:
0.4
:
12 (kappp = 1.98 × 10−5 s−1), polymerization regularity, that the reaction rate is reduced as the concentration of FL increases while bringing the molecular weights closer to theoretical values, was also discovered.
Table S6† also shows the effect of the photocatalyst concentration on metal-free PET–ATRP of MMA at [MMA]0
:
[EBPA]0 = 400
:
1 in 2.0 mL or 4.0 mL of DMSO. In the polymerization system with 2.0 mL of solvent, the molecular weight Mn,GPC at the molar ratio ([MMA]0
:
[EBPA]0
:
[FL]0
:
[TEA]0) of 400
:
1
:
0.2
:
6 was higher than that of 400
:
1
:
0.4
:
12. For instance, the molecular weight was calculated to be 37
500 g mol−1 at the monomer conversion of 85.2% (entry 7 in Table S6†) in the case of 400
:
1
:
0.4
:
12; while at the molar ratio of 400
:
1
:
0.2
:
6, the molecular weight reached up to 46
500 g mol−1 when the monomer conversion was 86.3% (entry 2 in Table S6†). In the polymerization system containing 4.0 mL of solvent (entries 8–13 in Table S6†), the molecular weights provided under various conditions seem to show relatively few differences with each other, and by increasing the usage of catalyst, the polymerization rate would be slowed down, but the change of molecular weight along with monomer conversion was not distinct.
In order to expand the scope and access of the applicability of this polymerization strategy to other functional monomers, the polymerization of styrene (St), poly(ethylene glycol) monomethyl ether methacrylate (PEGMA), acrylonitrile (AN), tert-butyl acrylate (tBA), glycidyl methacrylate (GMA) or benzyl methacrylate (BnMA) was also investigated as summarized in Table S8.† However, the extent of control over polymerization was inferior compared with that of PMMA. Further improvements for this metal-free method to enhance initiation efficiencies and provide polymers with controlled molecular weights, lower polydispersities as well as regular sequences and architectures are ongoing by our research group.
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Fig. 3 (a) pH-dependent equilibrium between the spirolactone form and the ring-opened form of fluorescein (FL) and optical properties of fluorescein in ring-opened structure.25 (b) Proposed mechanism of metal-free PET–ATRP photo-mediated with fluorescein as an organic photocatalyst. (c) Plot of monomer conversion versus time demonstrating the effect of blue light on the control over polymerization propagation through repeated “on-off” cycling of irradiation (blue regions) and light source removal (shaded regions); number-average molecular weight (Mn,GPC) and molecular weight distribution (Mw/Mn) versus conversion (d) and ln([M]0/[M]) as a function of exposure time (e) for metal-free PET–ATRP of MMA in the “on/off” light irradiation experiment. Polymerization conditions: [MMA]0 : [EBPA]0 : [FL]0 : [TEA]0 = 200 : 1 : 0.15 : 4.5, VMMA = 1.0 mL, VDMSO = 2.0 mL; samples were irradiated by a blue LED at rt. | ||
Fluorescence quenching studies demonstrated the reductive quenching effect. Fluorescence intensity of FL in DMSO solution decreased over time under blue light irradiation (Fig. S3a†), then the fluorescence – provided instantly with treatment of light avoidance in the dark environment – would recover within 30 min (Fig. S3b†); while for the solution of FL (0.1 mM) and TEA (30 equiv.) in DMSO, the quenched fluorescence caused by blue light irradiation (Fig. S3c†) was not recoverable even after being kept out of light for an adequate time (Fig. S3d†). This illustrates that an effective and irreversible fluorescence quenching effect had taken place in the presence of TEA. Meanwhile, the fluorescence of the polymerization system still had not been quenched throughout the whole reaction period (Fig. S2†), indicating that the initial ground state photocatalyst was regenerated after an electron transferred from FL˙− to the alkyl bromide of the initiator, and these results further confirmed the reversed catalysed cycle as illustrated in Scheme 1. Furthermore, the fluorescence intensity of FL with TEA (30 equiv.) in DMSO solution was much stronger than FL at the same concentration, illustrating that the chemical structure of fluorescein treated with TEA was maintained in the ring-opened form.
To confirm the necessity of light and the efficient nature of photocatalyst for reversible activation and deactivation of the polymerization process, an intermittent light irradiation sequence was introduced to investigate the temporal control. A repeated circulation of 1 h of irradiation followed by the same period of “dark” conditions was performed by using a parallel-group comparison trial method. The polymerization system was at first subject to the dark environment for 1 h, and the parallel sample 1 indicated that no polymer was obtained. The reaction mixture was then exposed to blue LED light, reaching 13.5% and 24.4% conversion after 0.5 h and 1 h light exposure, respectively (Fig. 3c). After the subsequent removal of irradiation from the system during the course of 1 h, the polymerization was suspended as demonstrated by parallel sample 2 with almost no monomer consumption and molecular weight Mn,GPC change observed during the “dark” periods. Upon re-exposure to light, as displayed in Fig. 3d, the polymerization process was reactivated, and the molecular weight reached up to 31
800 g mol−1 after 4 h, along with the monomer conversion changing to 43.6%, proving that polymer chain termination did not occur when the light was turned off. This “on–off” light switching could be recycled multiple times, indicating that in the absence of light irradiation, the polymerization paused with the chain end resting as the dormant alkyl bromide, and the dormant species were protected from any irrelevant radical reaction but were available to be reactivated upon re-exposure to light. These experimental achievements confirmed that the polymerization processes were strictly driven by the light stimulus and only occurred during irradiation time, and stagnant conversion and molecular weight could be detected in the absence of light. Particularly, a proportionality relationship between molecular weight and monomer conversion was expressed up to a high conversion (>85%) even with three on/off cycles (Fig. 3d). Furthermore, a linear relationship between ln([M]0/[M]) and time of light exposure indicated a constant propagation radical concentration throughout the whole polymerization process (Fig. 3e) and illustrated the light-stimulus responsibility and “living” feature of the photocatalyst mediated metal-free polymerization.
:
[EBPA]0
:
[FL]0
:
[TEA]0 = 200
:
1
:
0.3
:
9 in 2.0 mL of DMSO for 5 h, PMMA obtained via the metal-free PET–ATRP mechanism was analyzed by 1H NMR spectroscopy in CDCl3 (Fig. 4a) and in DMSO-d6 (Fig. 4b). The ethyl phenylacetate and bromine end groups are observable in the 1H NMR spectrum scanned in CDCl3 solution. The aromatic protons He (around δ 7.35 ppm) and ethyl groups Hf (δ 4.09 ppm) were assigned to the initiator EBPA segment, as indicated in the chemical structure. The chemical shift Hd at δ 3.72 ppm is attributed to the methyl ester group at the end of the polymer chain, deviated from other methyl ester groups in PMMA due to the electron-attracting impact of the ω-bromide atom. The 1H NMR spectrum obtained in DMSO-d6 was used to calculate the molecular weight Mn,1H NMR by comparison of the integral area of the phenyl unit from EBPA (He) with the methyl groups in the polymer backbone (Ha) and methyl ester groups (Hc). However, the chemical shift of the methyl ester group at the polymer chain end observed in this situation is overlapped by other methyl ester groups (Fig. 4b, peak c). The polymerization degree (DP) and the molecular weight Mn,1H NMR were calculated as follows:| DP = [Area (Ha) − Area (Ha,EBPA) + Area (Hc)]/6 = 195; |
Mn,1H NMR = MEBPA + DP × MMMA = 19 800 g mol−1. |
The molecular weight (Mn,1H NMR = 19
800 g mol−1) calculated by the 1H NMR spectrum was very close to the molecular weight obtained by GPC analysis (Mn,GPC = 19
900 g mol−1, Mw/Mn = 1.30), indicating that the obtained PMMA was end-capped by EBPA segments with high fidelity. To further confirm the initiation mechanism of the polymerization process, a polystyrene (PS) (entry 6 in Table S8,†Mn,GPC = 6200 g mol−1, Mw/Mn = 1.35) was analyzed by MALDI-TOF MS (Fig. 5). A series of main peaks is separated by an interval corresponding to a St repeating unit (104 mass units). This major set of peaks in the spectrometry indicated the existence of ethyl 2-phenyl acetate and bromide groups at the end of the polymer chains, suggesting that reversible activation and deactivation occurred effectively within this system. A PMMA sample (entry 2 in Table S4,†Mn,GPC = 13
800 g mol−1, Mw/Mn = 1.53) was also analyzed by MALDI-TOF MS as shown in Fig. 6. The interval of the main series of peaks by a m/z ratio of 100.04–100.06 was assigned to a MMA repeating unit. This set of peaks belonging to PMMA demonstrated the existence of an ethyl 2-phenyl acetate group at the chain end but missing the bromide functional groups (Fig. 6), the absence of bromide chain-end groups was probably due to the fact that they could be obliterated from polymers during MALDI-TOF MS analysis as usually observed in polymers produced by traditional ATRP.26
000 g mol−1) and polydispersity (Mw/Mn ∼ 1.30). Initially, as the employed content of FL was 1.73 equiv., there was an obvious increase of Mn,GPC of PMMA with a relatively wide distribution (Mn,GPC = 37
400 g mol−1, Mw/Mn = 1.62) after the 48 h chain extension reaction (Fig. S4a†). When the chain extension photocatalyzed reaction was conducted using 3.46 equiv. fluorescein, GPC traces illustrated a peak shift from the macroinitiator (Mn,GPC = 19
400 g mol−1, Mw/Mn = 1.30) to the obtained PMMA (Mn,GPC = 31
000 g mol−1, Mw/Mn = 1.60) as observed in Fig. S4b.† The GPC elution curve exhibited that some starting macroinitiators remained in the extended polymers, which may be perhaps caused by the difficulty in activating the bromide groups in the long polymer chain ends.
Chain extension of macroinitiator-1 (Mn,GPC = 18
800 g mol−1, Mw/Mn = 1.27) with MMA was carried out with 5.2 equiv. fluorescein at rt under blue LED irradiation for 48 h (Fig. 7a), providing a well-defined polymer (Mn,GPC = 29
000, Mw/Mn = 1.44). The GPC elution trace clearly shifted to the higher molecular species, suggesting the sufficient alkyl bromine chain-end functionality and high propagation efficiency of the macroinitiator. The effects of fluorescein content found in these experiments were quite significant, which suggests that in order to gain control over polymers in chain extension polymerization, it is necessary to increase the dosage of photocatalyst in the polymerization system to establish the equilibrium between the activation of the dormant bromide chain terminated polymer and the deactivation of the propagating radical chain.
In Fig. 7b, the chain extension employing styrene as the fresh monomer resulted in a block copolymer of macroinitiator-2 (Mn,GPC = 19
400 g mol−1, Mw/Mn = 1.30) P(MMA-b-St) (Mn,GPC = 33
900 g mol−1, Mw/Mn = 1.55) with an obvious GPC peak shift. Moreover, as shown in Fig. 7, the chemical shifts at δ 6.37–7.08 ppm assigned to the aromatic protons in PS segments indicated the successful synthesis of the block copolymer. The molecular weight of such a block copolymer measured by 1H NMR is 32
000 g mol−1, and the calculated DP of the PS segment was 121. The difference between Mn,GPC and 1H NMR data was probably attributed to the use of linear PMMA as the GPC standard. All these results exemplify the photocatalytic nature of FL via the metal-free PET–ATRP mechanism, and indicate that the macroinitiator with bromide chain-end groups can be used to reinitiate polymerization under external visible light stimulation to construct block copolymers.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c5py01765c |
| This journal is © The Royal Society of Chemistry 2016 |