Chemically recyclable alternating copolymers with low polydispersity from

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Electronic Supplementary Information Chemically recyclable alternating copolymers with low polydispersity from conjugated/aromatic aldehydes with vinyl ethers: selective degradation to another monomer at ambient temperature Yasushi Ishido, Arihiro Kanazawa, Shokyoku Kanaoka, and Sadahito Aoshima*. Department of Macromolecular Science, Graduate School of Science, Osaka University, Toyonaka, Osaka, 560-0043, Japan. *Corresponding author. E-mail: aoshima@chem.sci.osaka-u.ac.jp Contents: Experimental Section Figure S1. Copolymerization of CinA with IBVE Figure S2. 1 H NMR spectrum of hydrolysis products of poly(cina-co-ibve) Figure S3. 13 C NMR spectrum of hydrolysis products of poly(cina-co-ibve) Figure S4. Copolymerization of PPDE with IBVE in the absence of DTBP Figure S5. Copolymerization of PPDE with IBVE in the presence of DTBP Figure S6. 13 C NMR spectrum of hydrolysis products of poly(ppde-co-ibve) Figure S7. MWD curves of a model reaction of acid hydrolysis S1

Experimental Section Materials. trans-cinnamaldehyde (CinA; Aldrich, 99%) and 2,6-di-tert-butylpyridine (DTBP; Aldrich, 97.0%) were distilled over calcium hydride twice under reduced pressure before use. (E,E)-5-Phenylpenta-(2,4)-dienal (PPDE) was synthesized by acid hydrolysis of alternating poly(cina-co-ibve) and distilled over calcium hydride twice under reduced pressure before use. Isobutyl vinyl ether (IBVE; TCI, >99.0%) was distilled twice over calcium hydride. 1,4-Dioxane (Wako, >99.5%) was distilled over calcium hydride and then lithium aluminum hydride. EtSO 3 H (Aldrich, 95%) was used as received. Toluene (Wako, >99.5%) was dried using solvent purification columns (Glass Contour). Dichloromethane (DCM) was distilled twice over calcium hydride (for the reagent from Nacalai, 99%) or dried using solvent purification columns (Glass Contour) (for the reagent from Wako, 99.0%). For GaCl 3, a stock solution in hexane was prepared from anhydrous GaCl 3 (Aldrich, >99.999%). Hydrochloric acid (Nacalai Tesque) and tetrahydrofuran (THF; Wako, >99.5%) were used as received. All reagents except for toluene, DCM, THF, and hydrochloric acid were stored in brown ampules under dry nitrogen. Polymerization Procedures. Polymerization was carried out under a dry nitrogen atmosphere in a glass tube equipped with a three-way stopcock. The tube was carefully dried using a heat gun (Ishizaki; PJ-206A; blow temperature ~450 C) under dry nitrogen before polymerization reactions. A prechilled initiator solution (0.40 ml) was added to a prechilled mixture solution of a monomer, an added base, and a solvent (3.20 ml) at 0 C by a dry medical syringe. The polymerization reaction was started by the addition of a prechilled Lewis acid solution (0.40 ml) to the prechilled mixture (3.60 ml) at a certain polymerization temperature. The reaction mixture was stirred with a magnetic stir bar throughout the polymerization. The S2

polymerization was quenched with prechilled methanol containing a small amount of aqueous ammonia solution (2.50 ml; 0.1%). The quenched reaction mixture was diluted with DCM and then washed with water to remove the catalyst residues. The volatiles were evaporated under reduced pressure and the residue was vacuum-dried for at least 6 h at 60 C. The monomer conversion was determined by the gravimetric method and/or 1 H NMR analysis Acid Hydrolysis. Obtained copolymers were purified by reprecipitation in alcohols at least twice to remove low MW oligomers. The purified copolymer (30 mg) was dissolved in THF (5.0 ml), then the reaction was started by the addition of an aqueous HCl-THF (1.0 M; 5.0 ml) solution at 30 C. The reaction mixture was stirred with a magnetic stir bar throughout the hydrolysis. The hydrolysis was quenched with aqueous sodium hydroxide (1.0 M). The quenched reaction mixture was diluted with DCM, washed with water to remove the resulting salt and evaporated under reduced pressure. The residue was vacuum-dried at room temperature. Characterization. The MWD of the polymers was measured by gel permeation chromatography (GPC) in chloroform at 40 C with three polystyrene gel columns (TSK gel G-4000H XL, G-3000H XL, and G-2000H XL ; 7.8 mm internal diameter 300 mm; flow rate = 1.0 ml/min) connected to a Tosoh DP-8020 pump, a CO-8020 column oven, a UV-8020 ultraviolet detector, and an RI-8020 refractive index detector. The number-average molecular weight (M n ) and polydispersity ratio [weight-average molecular weight/number-average molecular weight (M w /M n )] were calculated from the chromatographs with respect to 16 polystyrene standards (Tosoh; 577 1.09 10 6 or 292 1.09 10 6, M w /M n 1.1). NMR spectra were recorded at 30 C in CDCl 3 or CD 2 Cl 2 using a Varian Mercury 300 spectrometer (300 MHz for 1 H), a JEOL JNM-LA 500 spectrometer (500 MHz for 1 H), or a JEOL ECA 500 spectrometer (500 MHz for 1 H). Differential Scanning Calorimetry (DSC EXSTER-6000, Seiko Instruments Inc.) was S3

used to determine the glass transition temperature (T g ) of product copolymers. The heating and cooling rates were 10 C/min. The T g of the copolymers was defined as the temperature of the midpoint of a heat capacity change on the second heating scan. Thermogravimetric analysis was performed under nitrogen atmosphere at a heating rate of 10 C/min using EXSTAR 6000 TG/DTA 6200 (Seiko Instruments, Inc.) S4

Figure S1. (A) Conversion vs. time curves and (B) MWD curves of products obtained by copolymerization of CinA with IBVE ([CinA] 0 = 0.60 M, [IBVE] 0 = 0.60 M, [EtSO 3 H] 0 = 4.0 mm, [GaCl 3 ] 0 = 4.0 mm, [1,4-dioxane] = 1.0 M, in toluene at 78 C). a For polymerization. b For polymer. c Cyclic trimer ratio in products. Figure S2. 1 H NMR spectrum of the hydrolysis products of poly(cina-co-ibve) (500.16 MHz in CDCl 3 at 30 C). S5

Figure S3. 13 C NMR spectrum of the hydrolysis products of poly(cina-co-ibve) (125.77 MHz in CDCl 3 at 30 C). Figure S4. (A) Conversion vs. time curves, (B) M n and M w /M n for polymer peaks, and (C) MWD curves of products obtained by copolymerization of PPDE and IBVE in the absence of DTBP ([PPDE] 0 = 0.45 M, [IBVE] 0 = 0.45 M, [EtSO 3 H] 0 = 4.0 mm, [GaCl 3 ] 0 = 4.0 mm, [1,4-dioxane] = 1.0 M, in toluene at 78 C). a For polymerization. b For polymer. c Cyclic trimer ratio in products. S6

Figure S5. (A) Conversion vs. time curves and (B) MWD curves of products obtained by copolymerization of PPDE and IBVE in the presence of DTBP ([PPDE] 0 = 0.45 M, [IBVE] 0 = 0.45 M, [EtSO 3 H] 0 = 4.0 mm, [GaCl 3 ] 0 = 4.0 mm, [1,4-dioxane] = 1.0 M, [DTBP] = 4.0 mm, in toluene at 78 C). a For polymerization. b For polymer. c Cyclic trimer ratio in products. Figure S6. 13 C NMR spectrum of the hydrolysis products of poly(ppde-co-ibve) (125.77 MHz in CDCl 3 at 30 C). S7

Figure S7. MWD curves of original polymers and hydrolysis products for poly(p-methoxybza-co-ibve) [M n (GPC) = 2.70 10 4, M w /M n (GPC) = 1.25, pmeobza content: 45%] (hydrolysis conditions: 0.50 M aqueous HCl-THF at 30 C). S8