1. Introduction
Plastics have become an integral part of the operation of modern society in the past century, and they are predominantly manufactured from non-renewable fossil fuels and inevitably discarded into the environment. Most plastics are resistant to biodegradation and have resulted in the accumulation of micro- and nano-plastic particles with adverse health effects on both sea and land animals. Their resistance to biodegradation is mainly attributed to their macromolecular structure and hydrophobicity, which limit the ability of the microorganisms to transport themselves into cells for metabolic disintegration; the biodegradation relies on extracellular enzymes to achieve some limited depolymerization [
1]. This has led to the development of biodegradable plastics such as polyhydroxyalkanoates (PHAs), which structurally comprise ester linkages in the polymer backbone that are easily hydrolyzed by microorganisms to monomeric metabolites. PHAs have evolved in nature via numerous microorganisms which utilize them as storage energy sources through depolymerization [
2].
However, the emergence of commercial PHAs, such as polyhydroxy butyrate, copolymers, and other biodegradable polyester-based plastic alternatives, have had little success due to their inferior mechanical properties and higher cost compared to traditional polymers. In 2021, the production of these polyesters represented less than 0.1% of all commercial polymers [
3] and was mostly driven by government procurement policies and public awareness of sustainability [
4].
Polyurethane-based plastics are an important class, representing about 6.6% of all polymers produced globally [
3], with broad applications in construction, the automotive industry, furniture, footwear, insulation, coatings, adhesives, elastomer foams, and consumer goods. These include thermoplastic as well as rigid and flexible foams, of which the latter accounts for 67% of all polyurethane produced [
5]. Polyurethanes are produced from the polymerization reaction between polyols and diisocyanates in the presence of chain extenders, blowing agents, surfactants, fillers, plasticizers, and colorants. Blowing agents create a polyurethane foam, while surfactants control the bubble formation and, therefore, the cell formation of the foam. In general, fillers increase stiffness, plasticizers enhance malleability, and pigments add color to the material. The polyols utilized for polyurethanes are typically of low molecular weight and can be either a polyether derived from the polymerization of alkylene oxides or hydroxyl-terminated polyester resin.
As polymeric materials are subjected to differing environmental factors, including temperature changes; pH changes; exposure to water, light, and oxygen; and physical stress, they tend to undergo physical and chemical changes that discolor and fracture the bulk material. Generally, these changes affect all materials over time; however, the rate at which any one of these factors can degrade a specific polymer varies based on the material’s susceptibility to these erosive forces [
6,
7]. As an example, polyesters are formed from multiple ester bonds, which are known to be susceptible to enzyme-catalyzed hydrolysis [
8,
9]. Ultimately, polymeric materials are converted into increasingly smaller and more reactive species over time, but this process can lead to the intermediate production of microplastics which can cause harm to living species and the environment [
10]. Also, since these changes impact functional structures that comprise the backbone structures of these polymers, the degradation of these components can be visualized by infrared spectroscopic methods [
11].
Polymers and other materials can be subjected to biodegradation by decomposing microorganisms within the same environment. Enzymes, acids, and other reactive chemical species are exuded to assist in harvesting nutrients and organic molecules so that they can be used by the present microbiota [
12]. For carbon-containing polymers and materials, this ultimately results in the production of volatile carbon compounds, including carbon dioxide and methane, which results in a decrease in organic carbon within the environment over time [
13].
Our interest is in the development of a more sustainable polyurethane composite which is biodegradable and derived primarily from bioderived components, especially polyester polyols, plasticizers, and fillers, as well as colorants and diisocyanates. Determining the biodegradation of plastic materials under controlled composting conditions, can be achieved by using the ASTM D5338, where the plastic product must demonstrate a satisfactory rate of biodegradation by achieving an acceptable ratio of conversion to carbon dioxide within 180 days. However, this test is quite time-consuming and expensive to carry out on a routine basis as the set-up can only be used on an individual sample. There is another ASTM test, the ISO 20200 standard, which can more easily measure the disintegration of plastics in 45 days and allow more samples to be carried within an equipment set-up. This latter test is extremely useful when developing polyurethane formulations with various components as a screening method for an indication of biodegradation by further evaluating and characterizing disintegration components through imaging, gravimetric analysis, infrared spectroscopy, and optical microscopy. The current work examines various formulations of bioderived polyurethane–polyester foam composites to assess the drivers of easier disintegration in the composting environment and provides an accelerated methodology for identifying markers of biodegradation prior to committing to a resource-intensive full biodegradation study.
2. Materials and Methods
2.1. Biobased Polyurethane Foam Formulation
The material stocks used for samples 2 to 8 were prepared according to Example 9 of US Patent 10,934,384, titled “Polyurethane elastomer compositions, and processes thereof”.
General procedure: 35 g of (1,3-propylene-succinate) was combined with 10.5 g of tributyl citrate, 0.19 g of TEGOSTAB
® (Evonik, Essen, Germany), 1.03 g of molten 1,3-propanediol, 0.37 g of 1,4-diazabicyclo[2.2.2]octane solution (DABCO 33-LV; Evonik), 0.32 g of water, 0.035 g of diethanolamine, and 1.24 g of FATE® dye (Bao Shen Polyurethane Tech, Hong Kong, China) within a 200 mL plastic container under overhead stirring and was heated to 50 °C. To this container, 11.9 mL of methylene-diphenyl diisocyanate (Suprasec 2379; Huntsman Corp., Arlington, TX, USA)was quickly added to the mixture and allowed to stir for 5 s before removing the container from the mixer and allowing the reaction to proceed (
Scheme 1). After 6 min of resting, the hardened foam was demolded from the container and evaluated to determine whether the foam conformed to a density of 0.15 g/cm
3 and had an Asker C hardness of 17. [
14] The weight percent additions of kraft lignin (West Frazer Mill Ltd, Vancouver, Canada), coconut charcoal (Sigma-Adrich, St.Louis, MO, USA), biobased 1.5-pentamethylnendiisocyanate (Mitsui Chemical Corp., Tokyo, Japan), glycerol (Bio Basic Inc, Markham, Canada), and
Bacillus spp. probiotics (Evoco Ltd., Toronto, Canada) are listed in
Table 1. Additional information regarding the included bacterial adducts can be found under PCT WO2021102589 [
15] and the biobased additives can be found under PCT WO2022126242 [
16].
2.2. Sample Preparation
These samples were made in accordance with the ISO 20200 specifications [
17]. The polyurethane material stocks required to make each set of samples were supplied by Evoco Ltd. Many of these polyurethane foam compositions were derived from biobased poly (1,3-propylene-succinate), biobased tributyl citrate plasticizer, and methylene diphenyl diisocyanate, as described in Example 9 of US Patent 10,934,384; the fillers, colorant, and bacteria are listed in
Table 1 [
14]. A commercially sourced thermoplastic polyurethane, WHT-8885 (Wanhua Chemical Group Co. Ltd.; Yantai, China), which consists of an MDI-polyether backbone, was used for comparison [
18]. These materials were cut with a stainless steel razor blade into 15 mm × 15 mm × 5 mm. The samples were weighed into 10 g batches, placed into a Model 48 Fisher vacuum oven (Fisher Scientific Co.; Hampton, NH, USA), and allowed to dry over a 24-h period before reweighing. Thirty seconds before placing the samples into their respective composting reactors, the reweighted sample batches were dipped and soaked in a container filled with distilled water. Extended trial samples were cut into larger 15 mm × 15 mm × 15 mm cubes and split into 2 5 g batches and are included in the
Supplementary Materials.
2.3. Synthetic Waste Preparation
The synthetic waste used to degrade the foam samples under thermophilic composting conditions was made immediately before use with the sets of prepared samples. In a large pail, 1 kg of synthetic waste was combined, prepared, and mixed for each reactor used during the trial. An additional 0.5 kg of excess synthetic waste was also made per trial. This was completed by adding the corresponding dry components in the following percentages: 40% sawdust/animal bedding (Pet Valu Canada Inc.; Markham, ON, Canada); 30% alfalfa rabbit feed pellets (Martin Mills Inc., Elmira, ON, Canada); 10% municipal compost (All Treat Farms Ltd.; Arthur, ON, Canada); 10% cornstarch (ACH Food Companies, Inc.; Oakbrook Terrace, IL, USA); 5% sugar (Redpath Sugar Ltd.; Toronto, ON, Canada); 4% corn oil (Mazola Corn Oil; ACH Food Companies, Inc.; Oakbrook Terrace, IL, USA); and 1% urea (Alpha Chemicals; Cape Giradeau, MO, USA). After the addition of the dry components, distilled water was added until it constituted 55% of the total synthetic solid waste mass, and the components were mixed by mechanical agitation of the pail for 15 min. Prior to use, the pH and nitrogen content were measured using a pH meter (cat# STARA2117, Thermo Fisher Scientific; Waltham, MA, USA) and a coulometric soil testing kit (Lustre Leaf Products, Inc.; Atlanta, GA, USA). If the nitrogen was determined to be deficient, the urea addition was doubled and mixed into the synthetic waste 1 h before retesting the nitrogen content. Synthetic waste samples were taken from the initial excess waste and from the individual reactors following the trials by individually labelling and filling 50 mL conical polypropylene tubes and storing them at −4 °C until analysis could be performed after the trial.
2.4. Composting Reactor Setup
Lidded plastic polypropylene containers measuring 346 mm (l) × 210 mm (w) × 124 mm (h) were used (cat# 16428012, Sterilite; Townsend, MA, USA) as sample reactor vessels. To these containers, 2 5 mm holes were drilled 65 mm from the container bottom, vertically centered on the 200 mm (w) sides. These containers were filled with 1000.0 g of premixed synthetic waste. The prepared samples were then mixed in weighted batches into the synthetic waste reactors. The initial reactor weights were recorded and then loaded into a 58 °C incubator (cat# 51030515, Thermo Fisher Scientific; Waltham, MA, USA) equipped with a 1 L/min external aquarium air pump (cat# 77846, Spectrum Brands Pet, LLC.; Blacksburg, VA, USA) to provide fresh air. Within 30 days, the sample reactors were mixed and rehydrated to 100% initial weight following a standard schedule, as specified in ISO 20200. Thirty days after the incubation started, the reactors were mixed and rehydrated to 80% initial weight according to the schedule. Throughout the trial, the reactor vessels were repositioned within the incubator to prevent localized variations within the incubator from affecting reactor decomposition.
2.5. Sample Collection and Evaluation
After 45 days of reactor upkeep and incubation, the sample batches were individually sifted and removed from the composted synthetic waste. The collected materials were exhaustively rinsed with distilled water until there was an absence of floating particulate matter. The sample batches were then placed in a vacuum oven at 60 °C to dry until the sample mass change was less than 1% of the initial weight, with a drying time of around 3–5 days. Clean, dried sample batches were then weighed to determine the degree of disintegration of each set compared to the composting period. Additionally, the samples were imaged using a Nikon Eclipse E200 upright microscope (Nikon Co., Ltd.; Tokyo, Japan) at 40× magnification and characterized by Fourier transform infrared spectroscopy using an Agilent Cary 630 equipped with a diamond attenuated total reflectance accessory (Agilent Technologies, Inc.; Santa Clara, CA, USA). For an additional extended-period trial, a 10 g batch of samples was split into 3 identical 5 g sets, where 1 experienced the standard 45-day trial and the other 2 were maintained in composting conditions until 75 and 90 days of composting had elapsed, respectively.
2.6. Soil Analysis
Soil samples were taken from the synthetic solid waste when it was first prepared and from each reactor immediately following sample collection. These soil samples underwent thermogravimetric analysis (TGA) using the TA Instruments TGA55 (Waters Corporation; Milford, MA, USA), which is equipped to determine the decrease in volatile organic solid components, indicating composting activity. Approximately 10 mL of frozen synthetic waste sample was placed into a pestle and mortar before being cryogenically frozen with liquid nitrogen and crushed into a fine powder. An excess of 50 mg of powdered synthetic waste was then loaded onto a 100 μL platinum pan and placed into the TGA sampler. The thermal profile used to test the volatile organic solids content included a 20 °C/min ramp to 105 °C, which was maintained for 1 h before ramping by 20 °C/min up to 550 °C and holding for 6 h. Both isotherm periods were set to abort and to proceed if the change in mass of the sample was less than 0.5%/min to reduce excessive heating.
4. Conclusions
Considered that most synthetic polymeric materials place a large burden on the environment in terms of petrochemical resource extraction and end-of-use pollution, biobased polyester polyurethanes appear as a path towards a more sustainable alternative. Biobased polyurethanes can be formulated that require fewer petrochemical materials in their production, and the goal of producing a petrochemical-free polymeric material is seen as viably achievable in the near term. For this study, biobased polyester polyurethanes consisting of a poly(1,3-propylene-succinate)-co-methylenediphenyl diisocyanate backbone were subjected to ISO 20200, which evaluated degradation under composting conditions, followed by ATR-FTIR analysis of the degraded foams. Compared to the results obtained by Kupka et al. [
19], the biobased polyester-backboned polyurethanes also appear to have an average mass loss of 24.3 ± 4.0% when subjected to composting conditions for 45 days, which suggests that these materials are less likely to persist in the environment when compared to other types of commodity plastics. [
23] Additionally, the disappearance of FTIR peaks at 3300, 1720, 1650, and 1150 cm
−1 in degraded foams suggests enzymatic degradation of key backbone polymeric linkages. [
8,
9] Ideally, society will benefit from the development and use of bio-sustainable polymeric materials, and additional testing and evaluation of these materials will contribute to that goal.