Koichi
Nakaoka
,
Satoshi
Muranaka
,
Io
Yamamoto
and
Tadashi
Ema
*
Division of Applied Chemistry, Graduate School of Natural Science and Technology, Okayama University, Tsushima, Okayama 700-8530, Japan. E-mail: ema@cc.okayama-u.ac.jp
First published on 31st January 2024
Terpolymerization of cyclohexene oxide (CHO), CO2, and aryl isothiocyanates produced poly(carbonate–thioimidocarbonate)s with gradient character, while that of CHO, CO2, and aryl isocyanates furnished poly(carbonate–urethane)s with random sequences. The former underwent partial degradation upon acid treatment or UV irradiation, while the latter was stable under the same conditions.
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Scheme 1 (a) Previous work on terpolymerization of epoxides, CO2, and comonomers. (b) Our previous work. (c) This work. |
In 2020, two groups independently achieved the first epoxide/isocyanate ROCOP (without CO2) to obtain new polyurethanes (PUs) with tertiary carbamate linkages,10a,b which are almost inaccessible via the conventional synthetic method with diisocyanates and diols. There are only several reports on this type of ROCOP partly because of the difficulty in using highly reactive isocyanates,10 which readily trimerize into isocyanurates.11 On the other hand, the epoxide/isothiocyanate ROCOP for the synthesis of poly(thioimidocarbonate)s (PTICs) was reported by three groups independently in 2021, and strong bases were used to activate isothiocyanates with poor reactivity as compared with isocyanates.12 These pioneering works suggest that the terpolymerizations of epoxides, CO2, and isocyanates or isothiocyanates might be difficult to achieve especially with a single catalyst because the ideal reaction conditions for the epoxide/CO2 ROCOPs are quite different from those for the epoxide/iso(thio)cyanate ROCOPs.
Previously, bifunctional MgII or ZnII porphyrin catalysts showed high activity for the synthesis of cyclic carbonates from epoxides and CO2,13 while bifunctional AlIII porphyrin catalysts 1 promoted the ROCOP of epoxides and CO2 efficiently to produce polycarbonates (Scheme 1b).14,15 The cooperative actions of the metal center and the quaternary ammonium halides led to the high activity and selectivity in both cases.16 More recently, we have also succeeded in the selective conversions of oxetanes and CO2 into trimethylene carbonates or poly(trimethylene carbonate)s with 1d.17 We envisioned that isocyanates or isothiocyanates could be used as comonomers in our catalytic system. Here we report the terpolymerizations of epoxide, CO2, and isocyanates or isothiocyanates for the first time (Scheme 1c). The terpolymerization of cyclohexene oxide (CHO), CO2 (2 MPa), and aryl isothiocyanates produced poly(carbonate–thioimidocarbonate)s with gradient character, while that of CHO, CO2 (1 atm), and aryl isocyanates afforded poly(carbonate–urethane)s with random sequences. The former underwent partial degradation upon acid treatment or UV irradiation to give polycarbonates, while the latter was stable under the same conditions.
Entry | 2 | S/Cb | Conv.c (%) | TONc | 3 | 4 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
CHO | 2 | n![]() ![]() |
M
n![]() |
PDIe | Yieldc (%) | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
a Reaction conditions: CHO (12.5 mmol), 2 (3.1 mmol), 1b (quantity indicated above), CO2 (2.0 MPa), 90 °C, 24 h, in an autoclave. b Ratio of CHO to 1b. c Determined by 1H NMR analysis of the crude reaction mixture. TON for the formation of 3. The yields of 4 were calculated based on 2. d Determined by 1H NMR analysis of the purified polymer. e Determined by SEC analysis of the purified polymer using THF as an eluent and polystyrene as a molecular-weight standard. Peaks had bimodal shapes. f CO2 (1.0 MPa). g CO2 (0.5 MPa). | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
1 | 2a | 6250 | 94 | 75 | 5400 | 4![]() ![]() |
83/34 | 1.1/1.1 | 6 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
2 | 2a | 20![]() |
93 | 46 | 12![]() |
5![]() ![]() |
164/63 | 1.0/1.3 | 3 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
3f | 2a | 20![]() |
83 | 71 | 15![]() |
3![]() ![]() |
167/55 | 1.1/1.3 | 7 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
4g | 2a | 20![]() |
80 | 85 | 9000 | 2![]() ![]() |
85/22 | 1.1/1.4 | 10 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
5 | 2a | 40![]() |
87 | 30 | 31![]() |
8![]() ![]() |
183/57 | 1.1/1.5 | 3 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
6 | 2b | 40![]() |
89 | 39 | 29![]() |
9![]() ![]() |
121/41 | 1.1/1.4 | 0 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
7 | 2c | 40![]() |
90 | 71 | 27![]() |
3![]() ![]() |
74/25 | 1.1/1.3 | 0 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
8 | 2d | 40![]() |
91 | 77 | 23![]() |
4![]() ![]() |
132/45 | 1.1/1.4 | 0 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
9 | 2e | 40![]() |
80 | >99 | 33![]() |
2![]() ![]() |
164/59 | 1.1/1.2 | 0 |
The reaction conditions were optimized. Higher temperature promoted the formation of byproduct 4a, while lower temperature resulted in a lower conversion of 2a; 90 °C was optimal (Table S1, entries 1–3, ESI†). When the molar ratio of CHO to 2a was set to 4:
1, both the molecular weight of the polymer and the conversion of 2a were high (entries 2, 4–6). When the amount of catalyst 1b decreased from 0.016 to 0.0025 mol% (S/C = 40
000), turnover numbers (TONs) increased from 5400 to 31
600 to give high-molecular-weight polymers, and both the conversion of 2a and the PTIC content (n
:
m) decreased (Table 1, entries 1, 2 and 5). Interestingly, lower CO2 pressure led to a higher PTIC content (entries 2–4). These results suggest that although the formation of the PTIC units is slower than that of the PCHC units, the former becomes favorable as CO2 is consumed. This trend is consistent with the electrophilicity parameters reported for heteroallenes; isothiocyanates are less electrophilic than CO2.18 The linker length of catalysts 1 had a significant effect on the catalytic activity, and 1b exhibited the best result (Table S2, entries 1–4, ESI†). We consider that catalysts 1c and 1d have longer linkers that may hinder the polymer elongation owing to steric bulkiness, while catalyst 1a has shorter linkers that cannot assist well the ring-opening of CHO and/or the insertion of CO2 or 2a. In sharp contrast, a binary catalytic system composed of Al(TPP)Br and tetrabutylammonium bromide (TBAB) showed little or no activity for the PTIC formation under otherwise the same conditions (entry 5), which clearly demonstrates the importance of cooperative catalysis with bifunctional catalyst 1b.13–17
The scope of aryl isothiocyanates 2 was explored under the optimized conditions with 1b. Isothiocyanate 2b with the methyl group at the para position was modestly incorporated to form terpolymer 3b (Table 1, entry 6). In contrast, isothiocyanates 2c–e with electron-withdrawing groups showed much higher reactivity, and terpolymers 3c–e with higher PTIC contents were successfully obtained (entries 7–9).
We next examined the reactivity of aryl isocyanates 5. In view of the facile conversion of 5a into isocyanurate 9a, we employed a syringe-pump for the slow dropwise addition of 5avia syringe under atmospheric CO2 pressure (balloon), which allowed us to optimize the reaction conditions for the terpolymerization of CHO, CO2, and 5a (Table S3, ESI†). Terpolymer 6a containing both the PCHC and PU units was obtained most efficiently with a catalyst loading of 0.016 mol% (S/C = 6250) (entries 1–3). The formation of byproduct 9a was minimal at 90 °C, although the formation of cyclohexene carbonate (7) and 2-oxazolidone 8a was suppressed at 80–100 °C (entries 2, 4 and 5). A faster dropwise addition of 5a resulted in the formation of a significant amount of 9a (entry 6). The use of 10 equiv. of CHO relative to 5a was better than that of 5 or 15 equiv. of CHO (entries 2, 7 and 8). The linker length of 1 had a crucial effect on the catalytic activity; 1b was the best catalyst (Table S4, entries 1–4, ESI†). In sharp contrast, a binary catalytic system composed of Al(TPP)Br and TBAB showed poor polymerization activity (entry 5), which demonstrates the advantage of bifunctional catalyst 1b.
Pure terpolymer 6a was obtained by reprecipitation (chloroform/methanol), and 6a was characterized by 1H NMR spectroscopy (Fig. S20a, ESI†). In addition to the broad signals at 4.6 ppm for the methine groups of the PCHC units, broad signals appeared at 6.9–7.5 ppm, which clearly indicates the incorporation of 5a. The 13C NMR spectrum showed the signals for the carbonyl groups of the PCHC and PU units at 153–154 ppm (Fig. S20b, ESI†). The IR spectrum showed two peaks for the CO stretching vibrations of the PU and PCHC units at 1707 and 1749 cm−1, respectively (Fig. S20d, ESI†). The structure of 6a was also analyzed by MALDI-TOF mass spectroscopy (Fig. S22a, ESI†); m/z intervals of 142 and 217 corresponding to the PCHC and PU units, respectively, were observed. DOSY also supported the formation of 6a (Fig. S21, ESI†). The analysis of hydrolysis products as well as the comparison of the NMR spectra between 6a and a model compound also supported the existence of the PCHC and PU units (Fig. S26 and S27, ESI†). Because 6a was prepared by the dropwise addition of 5a and because no systematic changes were seen in the ratios between the PCHC and PU units of 6a over the reaction time (data not shown), we consider that 6a had random sequences.
The scope of aryl isocyanates 5 was examined (Table 2). Isocyanate 5b with the methyl group at the para position was incorporated into terpolymer 6b accompanied with 9b. 4-Chlorophenyl isocyanate (5c) was successfully used to make 6c, while 4-(trifluoromethyl)phenyl isocyanate (5d) led to the formation of 6d with a larger molecular weight; byproduct 8d seems to result from the backbiting of the highly electrophilic carbonyl group of the PU unit by the adjacent terminal alkoxide ion. We also challenged the quaterpolymerizations of CHO, CO2, 2c or 2d, and 5c (Scheme 2 and Fig. S28–S33, ESI†). A mixture of 5c and CHO was added dropwise with the syringe-pump to a mixture of CHO, 2c or 2d, and 1b under CO2 (1 atm); as a result, quaterpolymers 10a with a Mn of 4.7 kg mol−1 and 10b with a Mn of 4.5 kg mol−1 were produced with the quantitative conversions of the comonomers (2c, 2d, and 5c). NMR, DOSY, IR, and mass spectra of the purified polymers indicated that the PCHC, PTIC, and PU units were contained in the polymer chains. When alkyl isocyanates were used instead of aryl isocyanates, the corresponding terpolymers 6 could not be obtained efficiently (data not shown). This is partly due to the rapid formation of the corresponding isocyanurates 9.
Entry | 5 | Conv.b (%) | TONb | 6 | Byproductb (%) | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
CHO | 5 | n![]() ![]() |
M
n![]() |
PDId | 7 | 8 | 9 | ||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
a A mixture of CHO (1.2 mmol) and 5 (1.2 mmol) was added dropwise to a mixture of CHO (11.2 mmol) and 1b (S/C = 6250 for CHO, 0.016 mol%) at 15 μL h−1 with a syringe-pump under CO2 (1 atm, balloon) at 90 °C, and the mixture was then stirred at 90 °C for 2 h. b Determined by 1H NMR analysis of the crude reaction mixture. TON for the formation of 6. The yields of 7 were calculated based on CHO, and those of 8 and 9 were calculated based on 5. c Determined by 1H NMR analysis of the purified polymer. d Determined by SEC analysis of the purified polymer using THF as an eluent and polystyrene as a molecular-weight standard. e Addition at 24 μL h−1. | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
1 | 5a | 81 | >99 | 3200 | 6![]() ![]() |
7.1 | 1.4 | 3 | 0 | 8 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
2 | 5b | 85 | >99 | 1900 | 2![]() ![]() |
4.2 | 1.4 | 1 | 0 | 29 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
3e | 5c | 79 | >99 | 3100 | 3![]() ![]() |
7.4 | 1.5 | 3 | 0 | 2 | |||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
4e | 5d | 80 | >99 | 4200 | 9![]() ![]() |
14 | 1.3 | 4 | 8 | 12 |
Recently, degradable polymers have attracted much attention from the viewpoint of the promotion of chemical recycling and the mitigation of plastic pollution.19 Although sulfur-containing polymers are known to be susceptible to UV light or chemicals,19a there are no reports on the degradability of PTICs to our knowledge. We envisioned that terpolymers 3 containing the PTIC units might be degradable upon acid treatment or UV light irradiation. To our delight, 3 did undergo partial degradation by acid exposure or UV irradiation (Fig. 1a–c). Reprecipitation (chloroform/methanol) of the degradation mixtures and spectroscopic characterizations indicated that pure PCHCs were formed by the selective degradation of the PTIC linkages in both cases (Fig. S35 and S39, ESI†). Interestingly, Fig. 1b and c strongly suggests that terpolymers 3 have gradient character in composition (ratio of the PTIC to PCHC units);203c–e with electron-withdrawing groups showed larger decrease in molecular weight upon acid treatment or UV light irradiation than 3a and 3b. Accordingly, kinetic studies indicated that 2d was converted into the terpolymers faster than 2a (Fig. S14, ESI†). For comparison, block copolymer PCHC-b-PTIC (3e′) was synthesized in a one-pot two-step manner, which was confirmed to exhibit the selective degradation of the PTIC moiety (Fig. 1d, e and S42–S44, ESI†), while copolymer PTIC that was synthesized from CHO and 2e and purified in a similar manner was completely degraded (Fig. S49, ESI†). In sharp contrast, both PCHC and terpolymer 6a showed little or no degradability under the same conditions, which indicates that the PCHC and PU linkages are more robust (Fig. S37 and S41, ESI†).
Plausible catalytic cycles for the 1b-catalyzed polymerizations of CHO, CO2, and isothiocyanates/isocyanates are shown in Scheme 3. The nucleophilic attack of the counter anion on CHO activated by the Al center of 1b makes a new PCHC/PTIC/PU linkage, generating the alkoxide intermediate shown in the center. The subsequent insertion of CO2/isothiocyanate/isocyanate into the Al–O bond gives the carbonate/thioimidocarbonate/imidocarbonate anion, which then forms an ion pair with the quaternary ammonium ion of 1b upon CHO coordination. The S and N atoms of the thioimidocarbonate and carbamate anions, respectively, are more nucleophilic because the negatively charged atom with less electronegativity is more labile, which is the key determinant for the selective formation of the PTIC or PU linkage. In the PTIC cycle, the reaction of the alkoxide anion with isothiocyanate 2 is considered to be the rate-determining step, judging from the substituent effect of 2 on the ratio of the PTIC to PCHC units (Table 1), degradation behaviors with gradient character (Fig. 1), and kinetic studies (Fig. S14, ESI†). In the PU cycle, the PU linkage formation may be the rate-determining step, although the situation is complicated owing to the side reactions such as the formation of 9. Cyclic byproducts 7, 4, and 8 are formed by the backbiting of the terminal alkoxide ions just after the construction of the PCHC, PTIC, and PU linkages, respectively.
![]() | ||
Scheme 3 Plausible catalytic cycles, where P simply represents a part of a polymer chain that may differ in each step. |
The molecular weights of terpolymers 6 and quaterpolymers 10 synthesized at 1 atm CO2 pressure (Table 2 and Scheme 2) were much smaller than those of terpolymers 3 synthesized at 2.0 MPa CO2 pressure (Table 1). In the synthesis of 6 and 10, isocyanates 5 were added dropwise to minimize the formation of byproducts 9. It is likely that 6 and 10 growing at 1 atm CO2 pressure have the alkoxide anions at the ends, which may experience backbiting and protonation. In contrast, 3 growing at the high CO2 pressure can undergo the rapid addition of CO2 to the alkoxide anions to form the carbonate anions, which leads to the smooth ring-opening of CHO rather than backbiting or protonation. If 5 could be added dropwise at the high CO2 pressure, 6 and 10 with higher molecular weights would be obtained.
Footnote |
† Electronic supplementary information (ESI) available: Experimental procedures and compound characterizations. See DOI: https://doi.org/10.1039/d3py01165h |
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