Here, we describe protocols for the preparation of trans-cyclobutane fused cyclooctenes (tCBCO), their polymerization to prepare depolymerizable olefinic polymers, and the depolymerization of these polymers under mild conditions. Additionally, protocols for the preparation of depolymerizable networks and compression molding of rigid linear plastics based on this system are described.
The growing consumption of synthetic polymers and the accumulation of polymer waste have led to a pressing need for new routes to sustainable materials. Achieving a closed-loop polymer economy via chemical recycling to monomer (CRM) is one such promising route. Our group recently reported a new CRM system based on polymers prepared by ring-opening metathesis polymerization (ROMP) of trans-cyclobutane fused cyclooctene (tCBCO) monomers. This system offers several key advantages, including the ease of polymerization at ambient temperatures, quantitative depolymerization to monomers under mild conditions, and a broad range of functionalities and thermomechanical properties. Here, we outline detailed protocols for the preparation of tCBCO-based monomers and their corresponding polymers, including the preparation of elastic polymer networks and compression molding of linear thermoplastic polymers. We also outline the preparation of high ring strain E-alkene tCBCO monomers and their living polymerization. Finally, the procedures for the depolymerization of linear polymers and polymer networks are also demonstrated.
The versatile and robust nature of synthetic polymers has made them a ubiquitous fixture of modern human existence. On the flip side, the same robust and environmentally resistant properties make polymer waste exceedingly persistent. This, together with the fact that a large fraction of all synthetic polymers ever made has ended up in landfills1, has raised legitimate concerns about their environmental effects2. Additionally, the open-loop nature of the traditional polymer economy has caused a steady consumption of petrochemical resources and a mounting carbon footprint3. Promising routes to a closed-loop polymer economy are, thus, highly sought after.
Chemical recycling to monomer (CRM) is one such route. The advantage of CRM over traditional recycling is that it leads to the regeneration of monomers that can be used to manufacture pristine polymers, as opposed to mechanical recycling of materials with deteriorating properties over multiple processing cycles. Polymers based on ring-opening polymerizations have appeared as especially attractive routes to CRM materials4. The thermodynamics of polymerization is typically an interplay between two opposing factors: the enthalpy of polymerization (ΔHp, which is typically negative and favors polymerization) and the entropy of polymerization (ΔSp, which is also typically negative but disfavors polymerization), with the ceiling temperature (Tc) being the temperature at which these two factors balance each other out5. For a polymer to be capable of CRM under practical and economically beneficial conditions, the right balance of ΔHp and ΔSp must be achieved. Cyclic monomers allow a convenient means to tune these factors via the selection of the appropriate ring size and geometry, since here, ΔHp is primarily determined by the ring strain of the cyclic monomers4,5. As a result, CRM polymers with a wide variety of monomers have been reported of late6,7,8,9,10,11. Out of these systems, ROMP polymers prepared from cyclopentenes are particularly promising due to the rather cheap starting material required and the hydrolytic and thermal stability of the polymers. Additionally, in the absence of a metathesis catalyst, the depolymerization is kinetically unfeasible, affording high thermal stability despite a low Tc12. However, cyclopentenes (and other monomers based on small cyclic structures) pose a key challenge-they cannot be readily functionalized, as the presence of functional groups on the backbone can affect the thermodynamics of polymerization in drastic, and sometimes unpredictable, ways13,14.
Recently, we reported a system that overcomes some of these challenges15. Inspired by examples of low-strain fused ring cyclooctenes in the literature16,17, a new CRM system was designed based on ROMP polymers of trans-cyclobutane fused cyclooctenes (tCBCO) (Figure 1A). The tCBCO monomers could be prepared at a gram scale from the [2+2] photo cycloadduct of maleic anhydride and 1,5-cyclooctadiene, which could be readily functionalized to achieve a diverse set of substituents (Figure 1B). The resulting monomers had ring strains comparable to cyclopentene (~5 kcal·mol−1, as calculated using DFT). Thermodynamic studies revealed a low ΔHp (−1.7 kcal·mol−1 to −2.8 kcal·mol−1), which was offset by a low ΔSp (−3.6 kcal·mol−1·K−1 to −4.9 kcal·mol−1·K−1), allowing the preparation of high molecular weight polymers (at high monomer concentrations) and near quantitative depolymerization (>90%, under dilute conditions) at ambient temperatures in the presence of Grubbs II catalyst (G2). It was also demonstrated that materials with diverse thermomechanical properties could be obtained while preserving the ease of polymerization/depolymerization. This ability was further exploited to prepare a soft elastomeric network (which could also be readily depolymerized), as well as a rigid thermoplastic (with tensile properties comparable to polystyrene).
One drawback with this system was the need for high monomer concentrations to access high molecular weight polymers. At the same time, due to extensive chain transfer and cyclization reactions, the polymerization was uncontrolled in nature. This was addressed in a subsequent work via photochemical isomerization of the Z-alkene in the tCBCO monomers to prepare highly strained E-alkene tCBCO monomers18. These monomers could be rapidly polymerized in a living manner at low initial monomer concentrations (≥25 mM) in the presence of Grubbs I catalyst (G1) and excess triphenylphosphine (PPh3). The polymers could then be depolymerized to yield the Z-alkene form of the monomers. This has created opportunities to access new depolymerizable polymer architectures, including block copolymers and graft/bottlebrush copolymers.
In this work, detailed protocols are outlined for the synthesis of tCBCO monomers with different functional groups and their polymerization, as well as the depolymerization of the resulting polymers. Additionally, protocols for the preparation of dogbone samples of a soft elastomeric network and their depolymerization, as well as compression molding of the N-phenylimide substituted rigid thermoplastic polymer, are also described. Finally, protocols for the photoisomerization of a tCBCO monomer to its strained E-alkene tCBCO form and its subsequent living ROMP are also discussed.
NOTE: The protocols outlined below are detailed forms of experimental procedures reported previously15,18,19. Characterization of the small molecules and polymers has been reported previously15,18. Additionally, syntheses of monomers and polymers and depolymerization of polymers should be performed inside a fume hood with appropriate personal protective equipment (PPE), including nitrile gloves, safety glasses, and a lab coat.
1. tCBCO monomer preparation15
2. Column chromatography
NOTE: The following is a general procedure for column chromatography as performed for the compounds described herein.
3. Photochemical Isomerization18
NOTE: The photoisomerization was adapted from a literature procedure22.
4. Polymer synthesis
5. Depolymerization
6. Preparation of tensile testing specimens for P315
Discussed here are representative results previously published15,18,19. Figure 5 shows the GPC traces for polymer P1 prepared by conventional ROMP with G2 (red curve)15 and living ROMP of EM1 with G1/PPh3 (black)18. The polymer prepared by living ROMP has a much narrower molecular weight distribution (Mn = 114.9 KDa, Ð = 1.17) versus the rather broad distribution seen for the polymer prepared by conventional ROMP with G2 (Mn = 142 KDa, Ð = 1.55).
1H NMR spectra for the depolymerization of linear (P1) and crosslinked (PN1) polymers are given in Figure 6. The extent of depolymerization of P1 is measured by calculating the ratio of the integral of the peaks corresponding to monomeric olefinic protons with respect to the sum of the peak integrals of the monomer and residual oligomer olefinic protons (as indicated in Figure 6A). Under the dilute conditions and in the presence of 1 mol% G2, P1 is depolymerized nearly quantitatively (~93%). The extent of depolymerization of PN1 is calculated similarly and amounts to ~94% (Figure 6B). It must be noted here that, for PN1, "monomers" refers to the mixture of monofunctional monomer and crosslinkers (M2 and XL, respectively) obtained after depolymerization.
Figure 7 shows the representative tensile curves (these data are from previously published work15) for polymer P3 and networks PN1. The presence of the flexible butyl chains in M2 causes PN1 to be a soft, elastomeric material with an ultimate tensile strain of ~0.64 MPa, modulus of ~ 0.76 MPa, and strain at break of ~226%.
On the other hand, polymer P3 with the rigid phenyl imide substituent behaves like a rigid glassy material with an ultimate tensile strength of ~41.4 MPa and strain at break of ~3.4%. Tensile testing was performed for P3 with an Instron Universal Testing Frame, while that for PN1 was performed with a homemade tensile tester, both at a crosshead speed of 5 mm·min−1.
Figure 1: tCBCO monomers for depolymerizable olefinic polymers. (A) tCBCO monomers for chemically recyclable polymers. (B) Synthesis of tCBCO monomers. Photochemical [2 + 2] cycloaddition of 1,5-cyclooctadiene and maleic anhydride affords the anhydride 1, which can be readily converted to M1 and XL, M2, and M3 through conditions (i), (ii), and (iii), respectively. (i) M1: MeOH, reflux; MeOH, EDC, DMAP, DCM; XL: 1,4-butanediol, EDC, DMAP, DCM. (ii) M2: NaOH, H2O, 60 °C; 1-butanol, EDC, DMAP, DCM. (iii) M3: aniline, acetone; sodium acetate, acetic anhydride, 100 °C. Please click here to view a larger version of this figure.
Figure 2: Reaction schemes for small molecule and polymer synthesis outlined in this work. (A) Synthesis of tCBCO small molecules and monomers. (B) Synthesis of P1 by conventional ROMP. (C) Synthesis of P1 by living ROMP. Please click here to view a larger version of this figure.
Figure 3. Reaction setup for photochemical isomerization of M1. The photoisomerization of M1 到 EM1 involves irradiation under flow conditions, and the setup consists of a photoreactor housing the quartz reaction tube, a column packed with AgNO3-impregnated silica (to trap the product), and a metering pump to enable the flow of the reaction mixture. Please click here to view a larger version of this figure.
Figure 4: Molds used for compression molding of P3 and preparation of PN1. (A) Steel mold for compression molding of P3 and (B) PTFE mold for curing elastomer network PN1. Please click here to view a larger version of this figure.
Figure 5: GPC traces for polymer. GPC traces for polymer P1 prepared by living ROMP in the presence of G1 and PPh3 (black) and conventional ROMP in the presence of G2 (red). This figure has been prepared from previously published data (red trace from Sathe et al.15, black trace from Chen et al.18). Please click here to view a larger version of this figure.
Figure 6: Depolymerization of tCBCO based polymers. (A) Depolymerization reaction scheme and stacked partial 1H NMR spectra of (B) polymer P1 after depolymerization (black), polymer P1 before depolymerization (blue), and monomer M1 (red) and (C) network PN1 after depolymerization (black), crosslinker XL (blue), and monomer M2 (red). This figure has been prepared from previously published data (data for B are from Sathe et al.19, data for C are from Sathe et al.15). Please click here to view a larger version of this figure.
Figure 7: Stress vs. strain curves. (A) Polymer network PN1 and (B) polymer P3. This figure has been prepared from previously published data from Sathe et al.15. Please click here to view a larger version of this figure.
The tCBCO monomers can be prepared from a common precursor: the [2+2] photocycloadduct of maleic anhydride and 1,5-cyclooctadiene, anhydride 1. Since the crude anhydride 1 is difficult to purify but can be hydrolyzed readily, the crude photoreaction mixture is subjected to methanolysis conditions to yield the readily isolable methyl ester-acid 2. The recrystallization of 2 after column chromatography is key to obtaining the pure trans-cyclobutane isomer of 2. 2 can be readily derivatized to prepare several different tCBCO monomers as outlined here, including the diester monomers M1 and M2, imide monomer M3, and ester crosslinker XL. Additionally, the final esterification step in the preparation of M2 and XL can lead to the formation of a side product that, we hypothesize, differs only in the relative stereochemistry of the ester groups (cis- for M2 and XL vs. trans- for the side products). Being only slightly lower in polarity than the desired products, care must be taken during the purification of M2 and XL so as to ensure efficient separation and minimize the loss of product. Typically, performing column chromatography under gravity (instead of flash chromatography) yields satisfactory results in this case.
The preparation of the highly strained monomer with the trans-cyclooctene, EM1, provides access to depolymerizable polymers with controlled molecular weight distribution. To achieve this, a photochemical isomerization method employing flow chemistry is utilized. This method shows higher yield and functional group tolerance compared to conventional batch-type photoisomerization. In this flow system, silver nitrate is used to immobilize EM1 in a column. The constant removal of EM1 drives the equilibrium in the irradiated reaction mixture toward EM1 and prevents its photodegradation. Active silver nitrate and proper polarity of the solvent mixture are critical for optimal results. Additionally, the pressure buildup can cause leakages; thus, pre-circulation before irradiation is necessary to locate any leakages. Due to the silver nitrate silica gel and Et2O/hexane solvent mixture, this method is limited to compounds with relatively low polarity and sufficiently high solubility in Et2O/hexane. Further, the trans-olefins in these monomers are reactive and prone to dimerization/decomposition in the presence of acidic impurities23. Additionally, if the monomer is not isolable as a solid, it may be stored as a dilute solution or with a small amount of BHT (~3%-5%) added to prevent radical-induced side reactions; these trans-olefin monomers may also be refrigerated to further prevent degradation24.
The tCBCO monomers can be polymerized to high molecular weights at ambient temperatures by ring-opening metathesis polymerization (ROMP) in the presence of G2. A rather high monomer concentration (~2 M) is needed to achieve this, owing to the low ring strain of the tCBCO monomers. If the monomers prove difficult to dissolve in the solvent at such high concentrations, sonication in an ultrasound bath may be helpful. Under these conditions, the polymerization can be performed to conversions >80% and high molecular weights (Mn > 100 kDa), albeit with broad dispersities (Đ > 1.5)15.
Monomer EM1, on the other hand, can be polymerized to a high conversion in a short time, even at low initial monomer concentrations. We attribute this to the high ring strain in EM1, resulting in a higher driving force for its polymerization. Depolymerization and cross-metathesis are suppressed by using an excess amount of PPh3 with respect to G1, allowing polymerization to proceed to high conversions while maintaining low Đ (<1.2). The polymerization shows a living character and can be applied for the synthesis of block copolymers18. The technique is fairly straightforward and robust enough that it can be conducted under ambient conditions by the simple addition of stock solutions. One important note, however, is that PPh3 must be purified (to remove oxidized PPh3 and other impurities) and stored under nitrogen (the purification may be done by recrystallization from ethyl acetate); additionally, care should be taken to dry the glassware before performing this polymerization.
The depolymerization of linear and crosslinked polymers based on this system under mild conditions is also demonstrated. It is interesting that this depolymerization is not restricted to linear polymers only-polymer networks prepared with this system can also be readily depolymerized. This is likely because, while the local concentrations of olefinic groups in the swollen network may be high, chain scission events in the presence of catalyst aid in the degradation and dissolution of the network, following which the fragments further undergo depolymerization. It is critical to quench the catalyst with ethyl vinyl ether after depolymerization prior to evaporating the solvent since the extent of depolymerization may be affected if the active catalyst is still present in the system.
The versatility of this system is further cemented by the range of properties accessible. Here, the preparation of a soft rubbery network, as well as a rigid glassy plastic with the same depolymerizable core, is demonstrated. The preparation of network PN1 may be challenging since it is rather fragile in the swollen state, requiring careful handling when removing it from the mold. Additionally, when performing Soxhlet extraction, highly volatile solvents (like dichloromethane) should be avoided since the rapid evaporation of such solvents may lead to warping and fracture of the sample. Additionally, to avoid such fracture, the swollen network should be allowed to dry in a covered container to slow the evaporation of the solvent. If the dissolution of P3 in DCM during the preparation of dogbone samples proves difficult, an additional solvent may be added in small increments. Further, to avoid defects while preparing dogbone samples with P3, the underfilling of mold cavities should be avoided. High-temperature processing of P3 can also lead to oxidative degradation due to the presence of olefinic groups in the backbone. To prevent this, butylated hydroxytoluene (BHT) may be added to the polymer.
The versatile nature of the tCBCO system lends itself to a diverse range of thermomechanical properties through facile functionalization, which can facilitate the introduction of chemical recyclability to areas where it has been as yet limited, like high-performance thermosets and composites. Additionally, the ability to access living polymerization with this system drastically expands the scope of depolymerizable polymer architectures that can be prepared, including block copolymers and bottlebrush and graft polymers.
The authors have nothing to disclose.
We acknowledge funding support from the University of Akron and the National Science Foundation under grant DMR-2042494.
1 and 3 dram vials | VWR | 66011-041, 66011-100 | |
1,4-butanediol | Sigma-Aldrich | 240559-100G | |
1,5-cyclooctadiene | ACROS | AC297120010 | |
1-butanol | Fisher | A399-1 | |
20 mL scintillation vials | VWR | 66022-081 | |
Acetic Anhydride | Alfa-Aesar | AAL042950B | |
Acetone | Fisher | A18-20 | |
Aluminum backed TLC plates | Silicycle | TLA-R10011B-323 | |
Ammonium hydroxide | Fisher | A669-212 | |
Aniline | TCI | A0463500G | |
BD precisionglide (18 G) | Fisher | ||
Chloroform | Fisher | C298-4 | |
Column for circulation (to be packed with silver nitrate treated silica gel) | Approximately 1 cm radius and 25 cm long, with inner thread on either end | ||
d-Chloroform | Cambridge Isotopes | DLM-7-100 | |
Dichloromethane | VWR | BDH1113-19L | |
EDC.HCl; 3-(3-dimethylaminopropyl)-1-ethyl-carbodiimide hydrochloride | Chemimpex | 00050 | |
Ethyl Acetate | Fisher | E145-20 | |
Ethyl Vinyl Ether | Sigma-Aldrich | 422177-250ML | |
Glass chromatography columns | Fabricated in-house | D = 20 mm, L= 450 mm and D = 40 mm, L = 450 mm | The columns are fitted with a teflon stopcock at one end and a 24/40 ground glass joint to accommodate a solvent reservoir if needed. |
Grubbs Catalyst 1st Generation (M102) | Sigma-Aldrich | 579726-1G | |
Grubbs Catalyst 2nd Generation (M204) | Sigma-Aldrich | 569747-100MG | |
Hexanes | Fisher | H292-20 | |
Hydraulic press | Carver Instruments | #3912 | Coupled with temperature control modules (see below) |
Hydrochloric acid | Fisher | AA87617K4 | |
Maleic Anhydride | ACROS | AC125240010 | |
Methanol | Fisher | A412-20 | |
Micro essential Hydrion pH paper (1-13 pH) | Fisher | 14-850-120 | |
Normject Luer Lock syringes (1, 3 and 10 mL) | VWR | 89174-491, 53547-014 and 53547-010 | |
Photoreactor chamber | Rayonet | RPR-100 | |
QuadraPure TU (catalyst scavenger) | Sigma-Aldrich | 655422-5G | |
Quartz tubes | Favricated in-house | D=2", L=12.5" and D=1.5", L=10.5" | |
Rotavap | Buchi | ||
SciLog Accu Digital Metering Pump MP- 40 | Parker | 500 mL capacity | |
Siliaflash Irregular Silica, F60 | Silicycle | R10030B-25KG | |
Silver Nitrate | ACROS | AC197680050 | |
Sodium hydroxide | VWR | BDH9292-2.5KG | |
Steel Mold | Fabricated in-house | Overall dimensions of mold cavity: length 20 mm, width 7 mm and depth 1 mm; gauge dimensions: length 10 mm, width 3 mm) | |
Steel Plates | Fabricated in-house | 100 mm x 150 mm x 1 mm | |
Teflon Mold (6-cavities) | Fabricated in-house | Overall cavity dimensions: length 25 mm, width 8.35 mm and depth 0.8 mm; gauge dimensions: length 5 mm, width 2 mm) | |
Teflon Sheets (0.005" thick) | McMaster-Carr | 8569K61 | |
Temperature Control Modules | Omega | C9000A and C9000 | °C units (two modules, one for top and one for bottom) |
Triphenyl Phosphine | TCI | T0519500G | |
UV lamps | Rayonet | RPR2537A and RPR3000A | |
Vacuum pump | Welch Duoseal | ||
Whatman Filter Paper (grade 2) | VWR | 09-810F | filter paper |