Open Access Article
Trang N. T.
Phan
*a,
Adèle
Ferrand
a,
Hien The
Ho
a,
Livie
Liénafa
a,
Marion
Rollet
a,
Sébastien
Maria
a,
Renaud
Bouchet
b and
Didier
Gigmes
a
aAix-Marseille Université, CNRS, Institut de Chimie Radicalaire UMR 7273, 13397, Marseille, France. E-mail: trang.phan@univ-amu.fr
bLEPMI UMR-5279 CNRS—Grenoble INP—Univ. de Savoie—Univ. Joseph Fourier, 38402 St Martin d'Hères, France
First published on 7th September 2016
A series of water-soluble styrene and propyl (meth)acrylate based monomers bearing a sulfonyl(trifluoromethane sulfonyl) imide (STFSI) group was prepared. These monomers were synthesized in good yield from the corresponding chloride sulfonyl monomer and trifluoromethanesulfonamide. Their chemical structures were further confirmed by HR-MS and NMR spectroscopy. Nitroxide-mediated polymerization of the prepared monomers was then performed in aqueous solution at 100 °C, 90 °C and 75 °C for acrylate, styrene and methacrylate derivatives, respectively. Controlled polymerization was successfully achieved as illustrated by the linearity of ln([M]0/[M]) vs. t2/3, the molar mass increase with conversion and the relatively low dispersity values for the resulting homopolymers. Compared to their neutral analogous polymers, the prepared anionic homopolymers exhibited a higher glass-transition temperature. This phenomenon was attributed to the electrostatic interactions between STFSI side groups along the polymer backbone.
In the field of solid polymer electrolytes (SPEs) designed for lithium batteries, many polymer/lithium salt systems have been considered. However, to date the most widely studied and used system consists of a mixture of LiTFSI dissolved in an aprotic polymer matrix of poly(ethylene oxide) (PEO). In such binary salt–polymer systems, the ionic conductivity could be high above the melting temperature of PEO but the Li+ transference number, that gives the proportion of the current carried by Li+ ions, remains very low (t+ < 0.2),14 leading under current to the formation of an ionic concentration gradient that limits substantially the power performances. To avoid this problem, the anions were covalently attached to the polymer backbones to form single-ion conductor copolymers with a lithium transference number close to unity.15,16 However, these solid polymer electrolytes (SPEs) exhibit a low conductivity mostly owing to the low level of ionic dissociation of carboxylates15 or borates.16 Recently, we have developed a novel family of single-ion electrolytes (SIEL) based on BAB triblock copolymers having a PEO middle block and anionic polymers based on styrene and methacrylate derivatives bearing the lithium sulfonyl(trifluoromethane sulfonyl) imide group as outer blocks.17,18 The SIEL materials containing lithium poly(styrene sulfonyl(trifluoromethane sulfonyl) imide) (denoted as PSSTFSILi) have shown outstanding performances in terms of conductivity (1.3 × 10−5 S cm−1 at 60 °C), transport number (t+ > 0.85), mechanical properties and electrochemical stability window.17 These remarkable properties build on the combination of soft PEO-rich phases that enable the conduction of Li+ with rigid PSSTFSILi phases that provide mechanical strength and act as a reservoir of cations.
The use of block copolymers as SPEs to combine in the same material the two antagonistic properties (mechanical and conductivity) was firstly proposed by Sadoway et al.19 Since this study, interest in block copolymers as SPEs for lithium batteries has continuously grown. Block copolymers can be prepared by different methods, but the living/controlled polymerization is the only way, which allows the synthesis of block copolymers with a well-defined structure. The development of reversible-deactivation radical polymerization (RDRP) techniques in the past two decades has largely promoted the synthesis of block copolymers. Furthermore, RDRP is more tolerant to protic functional monomers than anionic or group transfer polymerization techniques, and can be run in many conventional solvents over a wide range of temperatures.20–24
Taking advantage of the charge delocalization character of STFSI and the very interesting electrolytes obtained with a monomer bearing STFSI anion, we were encouraged to develop new monomer structures containing a STFSI side group, namely methacrylate and acrylate based monomers. Prior to performing the preparation of block copolymers devoted to SPEs for lithium batteries, we first investigated the aqueous-polymerization of three monomer derivatives of styrene, methacrylate and acrylate (Scheme 1) using the Nitroxide-Mediated Polymerization (NMP) technique. This investigation is crucial to ensure that the polymerization reaction is well controlled and produces well-defined water-soluble polymers. All aqueous polymerizations were carried out using an SG1-based alkoxyamine bearing a carboxylic acid function (so-called MAMA-SG1 or BlocBuilder MA, Scheme 1). In its basic form, the carboxylate function confers water solubility to the alkoxyamine and thus allows various water-soluble monomers to be polymerized by NMP in homogeneous aqueous solution.
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| Scheme 1 Chemical formulae of nitroxide (SG1), alkoxyamine (MAMA-SG1) and vinyl monomers bearing sulfonyl(trifluoromethane sulfonyl) imide. | ||
It is well known now that the NMP of methacrylate monomers using MAMA-SG1 alkoxyamine can be performed in a controlled manner by adding a small amount of co-monomer such as styrene,25,26 sodium 4-styrenesulfonate,27,28 acrylonitrile,29,30N,N-dimethylacrylamide31 or vinylbenzyl carbazole.32 In the present work, potassium methacrylate-STFSI was copolymerized with potassium styrene-STFSI as a comonomer. To illustrate the features of a controlled polymerization process, kinetic studies were performed and the molar masses of the collected samples were analyzed by size exclusion chromatography with DMF/LiBr as the eluent. The thermodynamic behavior of the prepared water-soluble polymers was also characterized by using differential scanning calorimetry (DSC).
High-resolution mass spectroscopy (HR-MS) experiments were performed in the negative ion mode on a time-of-flight mass spectrometer (Synapt-G2 HDMS, Waters) equipped with a pneumatically assisted electrospray ion source. Samples were analyzed with the following conditions: capillary voltage 2.28 kV, cone voltage 10 V, and desolvation gas (nitrogen) flow rate 100 L h−1. Poly(ethylene glycol) oligomers with m/z 325.1868 and m/z 369.2130 were used for the calibration as internal references.
Differential scanning calorimetry (DSC) was carried out on a TA DSC Q20 using a heat/cool/heat cycle from −90 °C to 250 °C. The heating and cooling rates were 10 °C min−1. The glass-transition temperature, Tg, was determined from the second heating cycle of the DSC thermograms.
Size exclusion chromatography (SEC) experiments were performed on a Varian PL-GPC 120 apparatus, which was composed of a PL-AS-MT autosampler, an Agilent 1100 series pump, a degasser, an injection valve, a column oven and a refractive index (RI) detector. The following columns were used: one pre-column and two PL Resipore columns (300 mm × 7.8 mm). The injection loop, the columns and the RI detector were in the same oven thermostated at 70 °C. The eluent was a solution of 0.1 M LiBr in N,N-dimethylformamide filtered through a 0.45 μm nylon membrane and the flow rate was fixed at 0.7 mL min−1. The samples were prepared in a mixture of eluent and toluene (0.25 vol%) as the flowmarker, filtered through a 0.2 μm nylon filter (Interchim) and placed in an autosampler preheated at 50 °C. The sample concentration was 0.25 wt%. Calibration curves were established with either polystyrene (PS) standards or poly(methyl methacrylate) (PMMA) standards, both purchased from Agilent.
1H NMR (400 MHz, DMSO-d6, δ ppm): 5.38 (CH2
CH–, d, 1H), 5.95 (CH2
CH–, d, 1H), 6.77 (CH2
CH–, dd, 1H), 7.64 (C6H4–, dd, 4H). 19F NMR (DMSO-d6, δ ppm): −77.81. 7Li NMR (DMSO-d6, δ ppm): −1.00. 13C NMR (DMSO-d6, δ ppm): 116.78 (CH2
CH–), 118.48 and 121.70 (–CF3), 126.07–126.61 (–CH2 aromatic), 135.74 (CH2
CH–), 139.77 and 144.35 (–CH aromatic).
HR-MS (C9H7NO4S2F3K): m/z = [M − K+]found = 313.9775 g mol−1, [M − K+]cal = 313.9769 g mol−1.
1H NMR (400 MHz, DMSO-d6, δ ppm): 6.34 (CH2
CH–, d, 1H), 6.18 (CH2
CH–, dd, 1H), 5.95 (CH2
CH–, d, 1H), 4.19 (–O–CH2–, t, 2H), 3.05 (–CH2–SO2–, t, 2H), 2.01 (–CH2–, m, 2H). 13C NMR (DMSO-d6, δ ppm): 165.87 (C
O), 132.00 (CH2
CH–), 128.71 (CH2
CH–), 125.41–115.74 (–CF3), 63.01 (–COOCH2–), 51.72 (–CH2SO2–), 23.97 (–COOCH2–). 19F NMR (DMSO-d6, δ ppm): −77.54.
HR-MS (C7H9NO6S2F3K): m/z = [M − K+]found = 323.9832 g mol−1, [M − K+]cal = 323.9829 g mol−1.
1H NMR (400 MHz, DMSO-d6, δ ppm): 6.04 (CH2
C, s, 1H), 5.68 (CH2
C, s, 1H), 4.17 (–O–CH2–, t, 2H), 3.06 (–CH2–SO2–, t, 2H), 2.01 (–CH2–, m, 2H), 1.88 (–CH3, s, 3H). 13C NMR (DMSO-d6, δ ppm): 166.42 (C
O), 135.81 (CH2
CH–), 125.75 (CH2
CH–), 123.10–115.26 (–CF3), 62.07 (–COOCH2–), 51.25 (–CH2SO2–), 23.53 (–COOCH2–), 17.94 (–CH3). 19F NMR (DMSO-d6, δ ppm): −77.53.
HR-MS (C8H11NO6S2F3): m/z = [M − K+]found = 337.9985 g mol−1, [M − K+]cal = 337.9985 g mol−1.
| Entry | Monomer | T (°C) | m monomer (g) | molMAMA-SG1 (mmol) | r (%) | [Monomer] wt% in water | Target Mn b at full conversion (g mol−1) |
|---|---|---|---|---|---|---|---|
| a r = 100 × [SG1]0/[MAMA-SG1]0. b Theoretical number-average molar mass, calculated according to Mn = MM(MAMA-SG1) + conversion × initial weight of the monomer/initial mol number of MAMA-SG1, with conversion = 1 and molar mass of the initiator, MM(MAMA-SG1) = 381 g mol−1. | |||||||
| 1 | SSTFSILi | 90 | 0.975 | 26.2 | 5 | 10 | 40 000 |
| 2 | MASTFSIK/SSTFSIK | 75 | 0.81/0.19 | 47.2 | 10 | 20 | 30 000 |
| 3 | ASTFSIK | 100 | 1.3 | 47.2 | 7 | 30 | 30 000 |
Because of the poor solubility of SSTFSIK in water, this monomer was converted to the lithium salt and then polymerized in diluted solution at 10 wt%. For the polymerizations of acrylate-STFSIK and methacrylate-STFSIK, targeted molar masses (Mn) of anionic polymers at 100% conversion were targeted at 30
000 g mol−1, while that of styrene-STFSILi was targeted at 40000 g mol−1.
The synthesis of SSTFSIK was first described by Armand35 and readapted by other authors.8,34,36 4-Vinylbenzenesulfonyl chloride, as an intermediate compound, was synthesized and reacted in situ with trifluoromethanesulfonamide in the presence of triethylamine to yield a viscous liquid. Cation exchange of the liquid with an excess of LiOH in methanol yields the lithium styrene-STFSI derivative. A high purity product can be obtained after washing the solid with n-pentane and cold dichloromethane. The formation of the lithium styrene-STFSI monomer was proven by 19F NMR with a singlet at −77.81 ppm, to be compared with the signal of the starting compound trifluoromethanesulfonamide CF3SO2NH2, which is at −79.32 ppm. 1H, 7Li and 13C NMR were also used to characterize the structure of SSTFSILi (Fig. S1–S3†).
The synthetic route for potassium methacrylate-STFSI and potassium acrylate-STFSI is depicted in Scheme 2. The corresponding 3-sulfopropyl (meth)acrylate potassium salts are commercially available and were converted into sulfonyl chloride derivatives upon reaction with oxalyl chloride in the presence of DMF as the catalyst (Vilsmeier–Haack reaction). The intermediate chloride products were then reacted with trifluoromethanesulfonamide in the presence of an excess of triethylamine. The use of an excess of triethylamine ensures the obtention of all monomers in their triethylammonium salt form avoiding the obtention of a mixture of salt and acid forms. The last step consisted of an ionic exchange of the triethylammonium ion with the potassium ion. This step was performed by using K2CO3 instead of Li2CO3 or LiOH used in the synthesis of SSTFSILi. Indeed, the basicity of the latter is too strong and may induce the hydrolysis of the (meth)acrylate ester bond. The global yield was typically close to 60%. Each compound was characterized by 1H, 19F, 13C NMR and HRMS. The 19F NMR spectra of the purified monomers (Fig. S4†) showed a shift of the characteristic signal of the trifluoromethyl group before and after the reaction. The combination of this result and those of other analyses indicates the formation of the right products. 1H and 13C NMR spectra are shown in the ESI (Fig. S5–S8†).
| Polymer | Target Mn a at full conversion (g mol−1) |
Polymerization time (min) | Total conversion (NMR) (%) |
M
n b (th) (g mol−1) |
M n (SEC) (g mol−1) | Dispersity |
|---|---|---|---|---|---|---|
| M n, the number-average molar mass, calculated according to the equation Mn = MM(MAMA-SG1) + conversion × initial weight of monomer/initial mol number of MAMA-SG1, MM(MAMA-SG1) = 381 g mol−1.a Values calculated with conversion of 100%.b Values calculated with conversion determined by 1H NMR. | ||||||
| PSSTFSILi | 40 000 |
300 | 55 | 22 000 |
45 000 |
1.09 |
| P(MASTFSIK-SSTFSIK) | 30 000 |
80 | 59 | 17 700 |
23 500 |
1.19 |
| PASTFSIK | 30 000 |
380 | 57 | 17 100 |
24 000 |
1.17 |
000 g mol−1 at full conversion was performed. Fig. 1 gives the kinetic plots of ln([M]0/[M]) vs. reaction time (t and t2/3). The linearity of the kinetic plots when plotted as ln([M]0/[M]) vs. t2/3 rather than t lies in the radical persistent effect. According to Fischer's43 and Fukuda's44 work, the minimization of the irreversible termination in the NMP process is governed by the persistent radical effect. Considering an alkoxyamine compound (RY) that decomposes into a transient radical (R˙) and a persistent radical (Y˙), this persistent radical effect leads to two unusual rate laws for R˙ and Y˙ during the intermediate regimes:
and
, where kd, kc and kt are the rate constants of the decomposition reaction, the combination reaction of RY and the termination reaction between two R˙, respectively. Consequently, the kinetic law of monomer concentration is thus given by
; hence, the plots of ln([M]0/[M]) versus time should show a downward curvature while the plots of ln([M]0/[M]) versus t2/3 should be linear. This persistent radical effect was experimentally validated in the NMP of styrene and acrylates by different groups.45–47 On the other hand, in the case of high propagation rate constant monomers, an initial excess of persistent radicals is added at the beginning of the polymerization process to slow down its rate and improve the polymerization control.33,48 Under these conditions, the concentration of the transient radicals reaches the stationary value [R˙]stationary = K[RY]0/[Y˙]0 (with K = kd/kc) and the linear evolution of the polymerization index ln([M]0/[M]) with time is generally observed.49,50 However, since the self-termination of the propagating radicals increases with the polymerization time and causes an additional Y˙ amount, when this released nitroxide concentration [Y˙] exceeds the initial one [Y˙]0, the behavior of the system turns to that observed without the initial persistent species. Fischer et al.50 theoretically demonstrated that if [Y˙]0 > (3[ln(10)]K[RY]0kt/kp)1/2, the polymerization index ln([M]0/[M]) varies linearly with time. On the contrary, if [Y˙]0 < (3K[RY]0kt/kp)1/2, the initial presence of the persistent species has no influence, and the polymerization index ln([M]0/[M]) increases linearly with t2/3.
Depending on the polymerization system, the propagation can take place in the first mode or could happen in both modes and in certain cases; the presence of the persistent species has no influence and the kinetics vary with time as t2/3. There are relatively few experimental studies that have investigated the effect of free nitroxide concentration on the NMP. Becer et al.51 in a systematic kinetic screening have studied the influence of the concentration of free nitroxide SG1 (0–10 mol% with respect to the initiator) on the NMP of styrene and tert-butyl acrylate. They found no significant effect of the introduction of a slight excess of free nitroxide for the styrene polymerization; however, the polymerization rate of tert-butyl acrylate was reduced with the increasing SG1 concentration. For an initial concentration of SG1 introduced in the polymerization medium ≥1 mol% with respect to the initiator, the polymerization index ln([M]0/[M]) varies linearly with time for both monomers.
In our case, as no values of kp and kt are available in the literature for lithium styrene-STFSI and the two other monomers studied in the present work, it is difficult for us to estimate precisely if the initial SG1 concentration introduced in the polymerization medium was higher than (3[ln(10)]K[MAMA-SG1]0kt/kp)1/2 or lower than (3K[MAMA-SG1]0kt/kp)1/2. For the NMP of lithium styrene-STFSI in the presence of 5 mol% of SG1 with respect to MAMA-SG1, we found a linear fit of ln([M]0/[M]) with t2/3 rather than with time. This suggests that the initial concentration of SG1 used was not enough to suppress the persistent radical effect conditions due probably to the fast activation step in the polar medium. The similar phenomenon was also observed in the Atom Transfer Radical Polymerization (ATRP) system by Zhang et al.52 They demonstrated through a full kinetic analysis of the CuBr-mediated ATRP of methyl methacrylate that when [Cu(II)]0/[Cu(I)]0 ≤ 0.1, the reaction kinetics fits quite well Fischer's equation with ln([M]0/[M]) as a function of t2/3 and when [Cu(II)]0/[Cu(I)]0 ≥ 0.1, the reaction kinetics fits quite well with ln([M]0/[M]) as a function of t. In this case, the addition of at least 10 mol% of Cu(II) in the initial mixture is needed to neglect the persistent radical effect.
To further characterize the control of the chain growth polymerization, evolution of the theoretical and experimental Mn values was plotted (Fig. 2a). The experimental Mn values increased linearly with monomer conversion and the molar mass distributions were narrow as attested by the dispersity values. However, the experimental Mn values evaluated from the SEC calibration curve established with polystyrene standards were considerably higher than the expected ones. According to the principle of the SEC technique, the determination of the polymer molecular weight is based on the hydrodynamic volume of the polymer in the mobile phase. DMF used for the SEC mobile phase is considered as a “poor” solvent for PS but as a “good” solvent for poly(styrene-STFSI), it means that PS is poorly solvated and poly(styrene-STFSI) is well solvated in DMF. Considering the two polymers with a similar length, the hydrodynamic volume of PS will be smaller than that of poly(styrene-STFSI). This explains why we obtained the experimental Mn values for poly(styrene-STFSI) which were higher than the expected values. The SEC traces (Fig. 2b) show the continuous shift to smaller retention volumes with the increasing reaction time and are all unimodal with no evidence of the presence of high molecular weight polymers that may be indicative of uncontrolled polymerization and/or termination reactions. These data show clearly the controlled nature of the aqueous NMP of lithium styrene-STFSI using MAMA-SG1 as the initiator. However, some tailing is observed at high elution volume of the SEC chromatograms, probably coming from the interactions between the polymer chains and stationary phase.
000 g mol−1 at full conversion, we observed that the reaction was fast. Indeed, conversions close to 100% were reached within 100 min (Fig. 3a). ln([M]0/[M]) of individual monomers was also plotted versus t2/3 with the aim to check the controlled character of the polymerization (Fig. 3b). As can be seen in Fig. 3b, ln([M]0/[M]) versus t2/3 was almost linear for potassium styrene-STFSI and potassium methacrylate-STFSI at least until 70 min. However, at this time, the conversion of SSTFSI-K was quasi-complete (>92%) and about 60% for the overall monomer conversions. After the complete disappearance of the styrene monomer in the polymerization mixture, the control of methacrylate polymerization was lost. Indeed, to ensure good control of the methacrylate monomer the polymerization mixture must always contain at least 7–10 mol% of comonomer.25,56 Below 60% overall monomer conversions, the Mn increased linearly with monomer conversion (Fig. 4a) and dispersity values were low (Đ < 1.2). Like for the polymerization of SSTFSI-Li discussed above, the experimental Mn values, derived from the calibration curve established with PMMA standards, were above the expected data. However, the difference between the experimental Mn values and the expected ones is now considerably reduced compared to the case of poly(styrene-STFSI) since DMF is considered as a “theta” (quite good) solvent of PMMA. The controlled character of the polymerization was further attested by the shift of the SEC chromatograms with the polymerization time (Fig. 4b). The SEC peaks corresponding to the polymerization time of 100 min and 130 min were superimposed with the large distributions of molar masses indicating the loss of polymerization control.
From these results, it undoubtedly appeared that the SG1-mediated copolymerization of potassium methacrylate-STFSI and potassium styrene-STFSI under the employed conditions was fast and ill-controlled above 60% overall monomer conversion.
000 g mol−1, a monomer concentration of 30 wt% in water and in the presence of 7 mol% of free SG1 to initiator. In all cases, the polymerization reactions proceeded smoothly with reaction kinetics following ln([M]0/[M]) as a function of t2/3 (Fig. 5b). Monomer conversion was lower compared to styrene and methacrylate derivatives although the reaction temperature and monomer content were higher (Fig. 5a). The SEC chromatograms of the produced polymer shifted steadily to a lower elution volume with increasing monomer conversion (Fig. 6a). The evaluation of the molar masses from the calibration established with PMMA standards indicated low dispersity values (Đ < 1.2) and molar masses increased linearly with conversion (Fig. 6b). However, the apparent Mn values are higher than the theoretical values based on conversion, as the polymer standard is not appropriate and also because of the difference of solvation between the polymer standard and the analyzed polymer in the mobile phase as well as the possible interactions between the polymer chain and the stationary phase.
000 g mol−1.42 The poly(SSTFSIK-co-MASTFSIK) copolymer exhibits two Tg values at 132 °C and 174 °C with a high heat flow amplitude for the first Tg. The observation of two Tg values suggests that the copolymer is not random but rather a gradient copolymer with a rich part of methacrylate and a rich part of styrene. Thus, the first Tg was attributed to PMASTFSIK and the second, close to the Tg value observed for PSSTFSILi previously, to PSSTFSIK. As expected for the polyacrylate backbone, the Tg value of the PASTFSIK homopolymer was much lower than those observed for styrene and methacrylate based polymers, which was 17 °C. However, one can note that thermal transition took place on a very large temperature domain. By comparison with the corresponding polystyrene and poly(propyl (meth)acrylate), all the studied water-soluble polymers bearing a sulfonyl(trifluoromethane sulfonyl) imide group exhibit higher Tg values (50 °C to 80 °C) due to strong electrostatic interactions between the potassium or lithium STFSI groups. These anionic polymers with their interesting thermodynamic behavior will probably give rise to the good block copolymer electrolytes for lithium battery when they associate with a ionic conductor block.
Footnote |
| † Electronic supplementary information (ESI) available: The 1H, 19F, 13C NMR spectra of hydrophilic monomers bearing the STFSI anion and the DSC thermograms of their corresponding homopolymers. See DOI: 10.1039/c6py01004k |
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