Open Access Article
Chao
Chen
,
Yves
Gnanou
* and
Xiaoshuang
Feng
*
Physical Sciences and Engineering Division, King Abdullah University of Science and Technology (KAUST), Thuwal 23955, Saudi Arabia. E-mail: yves.gnanou@kaust.edu.sa; fxs101@gmail.com
First published on 26th May 2022
This work reports how to efficiently utilize carbon disulfide (CS2) as a sulfur-containing C1 resource for the purpose of synthesizing both linear poly(trithiocarbonate)s and cyclic trithiocarbonates. When initiated by PPNCl or phosphazene benzoxide, the copolymerization of CS2 with episulfides affords perfectly alternating poly(trithiocarbonate)s in the absence of any catalyst. In contrast, when initiated by tetrabutylammonium halide, the same coupling reaction of CS2 with episulfides results in the formation of cyclic trithiocarbonates. The role played by initiating onium salts in the linear/cyclic selectivity as well as reaction conditions such as the temperature, the type of solvent, and the feeding ratio of CS2 to episulfides was investigated. Lastly, when placed in the presence of a radical source or treated with UV irradiation, poly(trithiocarbonate)s undergo complete unzipping to produce cyclic trithiocarbonates. This remarkable feature has been harnessed to prepare degradable polymers using oligotrithiocarbonates as self-immolating linkers between dithiol alkyl precursors.
S in CS2 is indeed equal to 105.3 kcal mol−1, compared to 127.2 kcal mol−1 of C
O in CO2) of C
S compared to C
O, a higher energy is required to activate CS2, rendering its copolymerization more challenging.
In 2007, Nozaki and co-workers first reported the successful copolymerization of CS2 with propylene sulfide (PS) resulting in the formation of a well-defined alternating poly(trithiocarbonate) when initiated by PPNCl and activated by a chromium salen complex.37 The polymerization could be optimized to obtain poly(trithiocarbonate)s up to 42.6 kg mol−1 molar mass with a 92% linear/cyclic selectivity. Zhang et al. on the other hand used an asymmetrical Schiff base chromium complex for such copolymerizations and obtained poly(trithiopropylene carbonate)s with molar masses limited to 10 kg mol−1, a linear/cyclic selectivity of 88% and increased yields.38 Recently, Silvano et al.39 reported the copolymerization of cyclohexene sulfide with CS2, and used the same (salen) CrCl complex as the one reported by Nozaki. In the latter case, poly(trithiocyclohexenecarbonate)s were obtained with a lower linear/cyclic selectivity (76%) and a broader polydispersity. Because of the high thiophilicity of the transition metal used, chances are high for the produced poly(trithiocarbonate)s to be contaminated with metallic residues, which may prevent their use in biomedical applications or as optical materials. In addition, such an approach requires a multistep synthesis of organometallic catalysts.
In this work, we investigate the potential of truly metal-free initiators and wish to demonstrate that such an approach is viable to selectively produce either poly(trithiocarbonate)s or cyclic trithiocarbonates (Scheme 1) through the coupling of CS2 with episulfides. When either PPNCl or phosphazenium benzoxide was used as an initiator, fully alternating poly(trithiocarbonate)s could be indeed obtained with a linear/cyclic selectivity up to 95% under conditions different from those considered by Nozaki and without resorting to a transition metal-based activator. On the other hand, when tetrabutylammonium fluoride was used at high temperatures, only cyclic trithiocarbonates were produced with very high selectivity. Lastly, the self-immolative behavior of the obtained poly(trithiocarbonate)s was demonstrated for the first time, a process triggered by a radical source or UV irradiation resulting in the degradation of linear poly(trithiocarbonate)s into cyclic trithiocarbonates.
:
2
:
3 and the absence of thioether linkages from 2.6–3.0 ppm (ref. 40) confirmed the perfectly alternating structure. As interestingly noted by Nozaki, changing the feeding ratio of PS to CS2 in favor of the latter compound resulted in a higher selectivity (entries 3–6, Table 1). Molar masses of PPSC reaching values as high as 45.4 kg mol−1 with 67% linear/cyclic selectivity (entry 3, Table 1) could be obtained for the PPSC sample corresponding to entry 3 in Table 1. With a ratio of 1
:
5 between PS and CS2, a linear/cyclic selectivity of 79% could be obtained (entry 5, Table 1); in contrast, only CTC could be isolated for a ratio of 2
:
1 between PS and CS2 (entry 6, Table 1). Besides the nature of the anion initiating the polymerization – here Cl− – the above results show that thioanions are mainly responsible for the production of CTCs. Upon using an excess amount of CS2 with respect to PS, the addition of CS2 by growing ether thioanions is favored over back-biting reactions. On the other hand, the trithiocarbanions formed being less nucleophilic than ether thioanions do not cause back-biting by reaction with trithiocarbonate functions.37 Increasing further the amount of CS2 improved slightly the linear vs. cyclic selectivity but slowed down the overall copolymerization. Carrying out copolymerization in a non-coordinating solvent such as toluene which is unable to solvate ion pairs also helped to increase the linear vs. cyclic selectivity up to 87% (entry 7, Table 1). Finally the addition of hydroxyl or thiol-ended transfer agents that can serve as initiating species was also beneficial for the production of linear polymeric trithiocarbonates against cyclic trithiocarbonates. As indicated above, the initiation by Cl− generates halide-terminated chains that favor back-biting reactions because of the electronegativity of the terminal Cl. Upon using thio-terminated transfer agents, such back-biting occurring at the very early stage of the polymerization could almost be avoided. In the presence of thiols, the linear/cyclic selectivity indeed reached up to 84% (entries 10–12 in Table 1); the 1H NMR characterization results confirm that 1-dodecanethiol (DoSH) acted as a transfer agent and thus as a chain initiator, being effectively incorporated at the α-end of the produced PPSC (Fig. S5†) and the 1H NMR calculated molar mass (5.6 kg mol−1) is in agreement with the one obtained with SEC (6.0 kg mol−1); in contrast, alcohols such as benzyl alcohol (BnOH) and tert-butyl alcohol (tBuOH) were less effective than DoSH at initiating chains probably due to the lower basicity of thioanions and their inability to abstract protons from alcohols (entries 8 and 9 in Table 1) and generate oxanions. In the latter case, the molar masses of the generated chains were little affected by the presence of BnOH or tBuOH. Further investigation of the copolymerization of CS2 with another episulfide, ethylene sulfide (ES), under the same conditions as above (entry 13 in Table 1) afforded a polymer which is insoluble in common organic solvents. Upon characterization of the crude polymerization mixture by IR and gravimetry, the conversion appeared to be almost complete with a yield of 90% for poly(trithioethylene carbonate); the linear/cyclic selectivity reached 95%, which is a much higher value than that obtained for poly(trithiocarbonate) generated from PS (67%, entry 2 in Table 1). The higher reactivity of ES compared to PS and the insolubility of the polymer generated have favored propagation over back-biting.
a
| Entry | PS : CS2 : I |
CTA : I |
Conv.b (%) | Sel.b (%) |
M
n(theo.) b (kg mol−1) |
M
n(SEC) c (kg mol−1) |
Đ |
|---|---|---|---|---|---|---|---|
| a The polymerizations were performed at 25 °C for 12 h unless otherwise noted; PPNCl was used as the initiator (I). b Determined by 1H NMR spectroscopy. c Determined by GPC in THF and with linear polystyrene as the standard. d Not analyzed. e Toluene (equal volume to monomers) was used as the solvent. f Ethylene sulfide was used as the monomer; conversion and selectivity were calculated by gravimetry. | |||||||
| 1 | 100 : 0 : 1 |
5 | — | — | NA | NAd | |
| 2 | 500 : 500 : 1 |
67 | 59 | 29.6 | 35.0 | 1.4 | |
| 3 | 500 : 1000 : 1 |
49 | 67 | 24.6 | 45.4 | 1.4 | |
| 4 | 500 : 1500 : 1 |
40 | 74 | 22.2 | 31.0 | 1.3 | |
| 5 | 500 : 3000 : 1 |
9 | 79 | — | NA | NA | |
| 6 | 1000 : 500 : 1 |
62 | 0 | — | NA | NA | |
| 7e | 500 : 500 : 1 |
45 | 87 | 29.4 | 28.0 | 1.4 | |
| 8 | 500 : 1000 : 1 |
BnOH (10/1) | 32 | 79 | 20.0 | 37.5 | 1.4 |
| 9 | 500 : 1000 : 1 |
tBuOH (10/1) | 47 | 75 | 26.4 | 34.6 | 1.5 |
| 10 | 500 : 1000 : 1 |
DoSH (1/1) | 57 | 80 | 17.1 | 21.3 | 1.5 |
| 11 | 500 : 1000 : 1 |
DoSH (5/1) | 52 | 82 | 5.3 | 9.3 | 1.5 |
| 12 | 500 : 1000 : 1 |
DoSH (10/1) | 64 | 84 | 3.7 | 6.0 | 1.6 |
| 13f | 500 : 1000 : 1 |
90 | 95 | — | NA | NA | |
Besides increasing the ratio of CS2 to PS and using appropriate transfer agents, we considered another factor, namely the temperature of the polymerization to favor propagation over back-biting. Using phosphazenium alkoxide obtained by deprotonation of benzyl alcohol with the superbase P4, we carried out the copolymerization of CS2 with PS at various temperatures. At 60 °C only cyclic trithiocarbonates were produced whereas at 0 °C and below (entries 3 and 6 Table 2) the level of linear vs. cyclic selectivity reached values (90%) comparable to those claimed in Nozaki's work where a salen chromium complex was used as an activator. However, lower temperatures caused a slower rate of polymerization. All the PPSC samples obtained at low temperatures exhibited narrow molar distributions with molar masses around 10 kg mol−1. Because of the slow rate of polymerization at 0 °C, we did not attempt to obtain samples of higher molar masses.
a
| Entry | T (°C) | PS : CS2 : I |
Conv.b (%) | Selectivityb (%) |
M
n, theo. b (kg mol−1) |
M
n c (kg mol−1) |
Đ |
|---|---|---|---|---|---|---|---|
a The polymerizations were performed under neat conditions for 12 h and the ratio of P4 to BnOH was set as 1 : 1 unless otherwise noted.
b Determined by 1H NMR spectroscopy.
c Determined by GPC in THF and with linear polystyrene as the standard.
d The polymerizations were performed for 24 h.
|
|||||||
| 1 | 30 | 100 : 600 : 1 |
80 | 77 | 9.2 | 10.1 | 1.4 |
| 2 | 60 | 100 : 600 : 1 |
100 | 0 | |||
| 3 | 0 | 100 : 600 : 1 |
53 | 90 | 7.2 | 8.2 | 1.3 |
| 4 | −10 | 100 : 600 : 1 |
45 | 92 | 6.1 | 7.3 | 1.3 |
| 5 | −20 | 100 : 600 : 1 |
21 | 90 | 2.8 | 3.2 | 1.3 |
| 6 | −40 | 100 : 600 : 1 |
9 | 92 | |||
| 7d | 0 | 200 : 1200 : 1 |
84 | 83 | 20.9 | 21.5 | 1.4 |
A kinetic study (Fig. 2) of the copolymerization of CS2 with PS was performed under the following conditions: a feeding ratio of 600
:
100 for CS2
:
PS at −10 °C with BnOH/P4 as the initiator. The ln([M0]/[M]) vs. time plot (Fig. 2A) shows a first order character in the studied range of conversions. The molar masses of PPSC samples (Fig. 2B) increase linearly with monomer conversion with narrow polydispersity indexes (Đ ≤ 1.3), indicating a “living” character. The in situ FT-IR (Fig. S6†) real-time online monitoring at 1180 cm−1, assigned to the C
S bond, allowed us to follow the buildup of trithiocarbonate functions. The adsorption vs. time plot (Fig. 2C) showed an exponential fit that also demonstrated a first order polymerization character. Based on the in situ FT-IR monitoring results at different temperatures (0, −10, −20, −30 °C, Fig. 2D), the enthalpy and entropy of the copolymerization of PS and CS2 could be derived (ΔH = 7.48 kcal mol−1, ΔS = −53.37 cal mol−1 K−1) and an activation energy for the formation of linear PPSC equal to 21.5 kJ mol−1 was deduced. This value of the activation energy is much lower than the one determined by Darensbourg et al. for the copolymerization of CO2 with epoxides when catalyzed by the salen Cr catalyst (67.6 kJ mol−1).41 This confirms that the formation of linear poly(trithiocarbonate)s is easier than that of linear polycarbonates and that it can be carried out at lower temperatures.
a
| Entry | Catalyst | Monomer | T (°C) | PS : CS2 : Cat |
Conv.b (%) | TOFc (h−1) | Selectivityb (%) |
|---|---|---|---|---|---|---|---|
| a The coupling reaction was performed under neat conditions for 12 h. b Determined by 1H NMR spectroscopy. c Turnover frequency (TOF) = (mole of episulfide consumed)/(mole of ammonium × h). TBAF, TBABr, TBAI, and TBAAc are tetraammonium fluoride, bromide, iodide, and acetate, respectively; PS: propylene sulfide, ES: ethylene sulfide, CHS: cyclohexene sulfide, AES: allyl ether episulfide, PES: phenyl ether episulfide, iBS: isobutylene sulfide. | |||||||
| 1 | TBABr | PS | 25 | 500 : 500 : 1 |
<1 | <1 | |
| 2 | TBAI | PS | 25 | 500 : 500 : 1 |
<1 | <1 | |
| 3 | TBAF | PS | 25 | 500 : 500 : 1 |
45 | 18.8 | 80 |
| 4 | TBAAc | PS | 25 | 500 : 500 : 1 |
78 | 32.5 | 63 |
| 5 | TBAF | PS | 60 | 500 : 500 : 1 |
>99 | 41.7 | >99 |
| 6 | TBAF | PS | 60 | 5000 : 5000 : 1 |
91 | 379 | >99 |
| 7 | TBAF | PS | 80 | 10 000 : 10 000 : 1 |
83 | 691 | >99 |
| 8 | TBAF | PS | 80 | 20 000 : 20 000 : 1 |
57 | 950 | >99 |
| 9 | TBAF | ES | 80 | 20 000 : 20 000 : 1 |
>99 | 1667 | >99 |
| 10 | TBAF | CHS | 80 | 5000 : 5000 : 1 |
90 | 375 | >99 |
| 11 | TBAF | AES | 80 | 5000 : 5000 : 1 |
32 | 133 | >99 |
| 12 | TBAF | PES | 80 | 5000 : 5000 : 1 |
30 | 125 | >99 |
| 13 | TBAF | iBS | 80 | 5000 : 5000 : 1 |
92 | 383 | >99 |
Unlike polycarbonates that can be chemically degraded or depolymerized only under anionic or enzymatic conditions,44,45 poly(trithiocarbonate)s are vulnerable to radical attack. Yet attempts at utilizing poly(trithiocarbonate)s as RAFT platforms to grow under controlled conditions polymer chains or blocks by radical means are scarce.46,47 The examples found of such polymeric RAFT agents that were used to control radical polymerization of vinyl monomers were all prepared by polycondensation through the coupling of ditrithiocarbonate anions with a difunctional electrophilic reagent. With these works in mind, we subjected our poly(trithiocarbonate)s to radical reactions. In the presence of 2,2′-azobis(2-methylpropionitrile) (AIBN) used as a radical source, poly(trithiocarbonate)s undergo complete unzipping that proceeded via radical mechanisms, resulting in the formation of cyclic trithiocarbonates (CTC). As shown in Fig. 3, PPSC degraded very fast in the presence of 5% (wt/wt) of AIBN at 70 °C and almost fully degraded into CTC in 24 h. As a comparison, PPSC remains unchanged in a control experiment under the same conditions in the absence of AIBN. Knowing that PPSC can be radically degraded by AIBN, we further explored its degradation under UV irradiation. As shown in Fig. S20,† PPSC also undergoes degradation under UV irradiation but at a much slower rate than that observed in the presence of AIBN: under UV irradiation, 75% of PPSC was decomposed into CTC after 60 h.
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| Fig. 3 1H NMR monitoring degradation of PPSC using AIBN at 70 °C and a plausible radical induced degradable process. | ||
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| Scheme 2 Trithiocarbonates as degradable linkers for the preparation of degradable polymers (m + n = 4). | ||
Footnote |
| † Electronic supplementary information (ESI) available: Experimental, 1H and 13C NMR, FTIR, DSC, TGA and GPC characterization data Fig. S1–S24. See DOI: https://doi.org/10.1039/d2py00405d |
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