Abstract
Keywords
Introduction
Plastics are the workhorse material of the modern economy because of their tunable and unrivaled properties. Combined with their low cost, they are an ideal choice for a wide range of applications that include packaging, transport, construction, healthcare, clothing, and electronics.1,2 The production of plastic resin has increased from 2 to 380 t/year in the last 60 years. 3 On the downside, our current linear economic model, where we simply dispose of manufactured products at the end of their life (which can be very short for single-use applications), generates large-scale pollution that causes harmful effects on human health and on the environment.4–6 The approximate total amount of plastic waste generated in 2015 was 6300 Mt, of which only 9% was recycled and 12% was incinerated.3,7
The increasing awareness about the impact of plastic pollution on ecosystems stresses the need for a transition toward a circular economy that promotes an intelligent management by reusing, recycling, and even upcycling end-of-life plastics.1,8–10 The implementation of such a circular market has been estimated to be worth $4.5 trillion by 2030. 11 Depending on the waste stream quality, the type of polymer, as well as the required purity of the recycled resin, different recycling solutions exist and are under continuous development. These include (i) separation and mechanical deconstruction, which often reduces the molecular weight and the performance of the recycled polymer; (ii) chemical depolymerization, where the polymer is converted to small molecules by chemical or enzymatic reactions; and (iii) dissolution/precipitation methods, where the polymer is purified by treatment in appropriate solvents and antisolvents. 9 For styrene-based polymers, the dissolution/precipitation approach appears as the best option considering the yield, the reachable degree of purity of the recycled resin, and the overall cost, because the polymer chains are not altered during the process.12–15 It is worth noting that among the recycling technologies, this method has the lowest environmental impact in terms of CO2 emissions. 12 Some key challenges include solvent management, the reduction of the solvent volume used for purification, and the energetic cost associated with drying the recycled resin.
This paper focuses on the optimization of a versatile recycling process of dissolution/precipitation for polystyrene (PS), developed by Polystyvert Inc.
16
As illustrated in Fig. 1, the first step consists of the dissolution of contaminated PS materials coming from various streams such as construction, food, electronics, etc. The “green” solvent used in this process is

Schematic representation of the main steps in the Polystyvert-patented 16 dissolution/precipitation PS-recycling process; Cy and H are used as the solvent and antisolvent, respectively.
As a result, knowing the amounts of Cy, H, and PS at different strategic points is essential to optimize the recycling process. For example, when washing the PS paste with H, it is necessary to remove as much Cy as possible to reduce the energy consumption and duration of the devolatilization step. Meanwhile, it is also important to minimize the amount of H used to minimize the cost of the process, both from an economic and environmental standpoint. Quantifying the residual solvents in the recycled pellets is also essential because it is a direct measure of the devolatilization process efficiency. Therefore, it is necessary to implement a rapid, direct, and easy quantification technique for residual solvents throughout the process.
While mass spectrometry provides outstanding levels of sensitivity and selectivity, it is expensive and cannot readily be implemented for routine analysis and process optimization at a production plant. Gas chromatography is a more affordable alternative, but a long elution time makes it less practical for the quality control aspect of the intended application.
Thermogravimetric analysis was also considered but the evaporation of H and Cy was poorly separated both at slow and fast scanning rates. By comparison with these various techniques, infrared spectroscopy (IR) offers several advantages such as rapid measurements and data analysis, low cost, robustness, and easy operation by nonqualified operators at the plant level.18,19 In this paper, we develop and validate calibration models allowing the rapid and accurate quantification of Cy and H in PS by IR spectroscopy. We also apply the model at the pilot plant level to representative pastes and pellets produced during the dissolution/precipitation recycling of PS waste material.
Experimental
Materials and Methods
High-performance liquid chromatography grade H (≥96%), Cy (99%), 1,2-dichloroethane (DCE; anhydrous, 99.8%), and PS (
To test the applicability of the models in real-life conditions, PS samples were extracted at different stages of the recycling process in a pilot-scale plant. This plant can produce about 5 kg of recycled resin per hour. It consists of several modules of dissolution, purification, precipitation, washing, and extrusion. A weighted amount of each sample was dissolved in an appropriate mass of DCE to approximate the PS concentration used in the calibration standards. Three replicates were used for each sample.
For convenience, the models were built using either a spectrometer located in the university laboratory or one located at the pilot plant. Efforts were made to make the sampling and measurement parameters as similar as possible between the two instruments, but no attempt was made to transfer calibration models from one instrument to the other. Rather, samples were systematically quantified by measuring their spectrum with the same instrument that was used to create the calibration model. More specifically, the single-solvent (Cy-only and H-only) models were created using a Vertex 70 Fourier transform infrared (FT-IR) spectrometer (Bruker Optics) equipped with a deuterated L-alanine doped tri-glycine sulfate detector and a single reflection ZnSe attenuated total reflection (ATR) accessory (MIRacle, Pike Technologies), while the mixed-solvent (Cy + H) model was created using a Thermo Scientific Nicolet iS10 FT-IR spectrometer equipped with a deuterated triglycine sulfate detector and a single reflection diamond ATR accessory. To minimize the risk of solvent evaporation during the analysis, a large (at least 1 mm thick) droplet of the highly viscous solution was deposited on the ATR element. Spectra were recorded with a 4 cm−1 resolution by averaging scans for 1 min for the samples and 2 min for the backgrounds. This acquisition time was selected as a compromise between the need for a good signal-to-noise ratio and the avoidance of a bias due to problematic solvent evaporation.
ATQ Analyst 9 (Thermo Nicolet Corporation) was used for spectral processing and multivariate analysis. The performance of the multivariate models was evaluated in terms of root mean square error of calibration (RMSEC), root mean square error of prediction (RMSEP), root mean square error of cross-validation (RMSECV), and determination coefficient (
Results and Discussion
Attenuated total reflection (ATR) was selected as the sampling method of choice because it can be readily used by operators at the plant level. Ideally, the PS samples would be analyzed directly in their solid (for pellets) or viscoelastic (for pastes) state to allow for a faster and more sensitive quantification of the Cy and H content. However, this direct sample presentation method makes the analytical outcome prone to random or systematic errors if there is heterogeneity in the bulk distribution of the solvents because ATR only probes the surface of the sample, with a penetration depth on the order of 0.6–2.3 µm over the spectral range of interest when using a diamond ATR element. Notably, a partial evaporation of the Cy or H at the surface of the samples would result in a systematic underestimation of their true content in the bulk sample. In view of this, we decided to dissolve the samples in a common solvent for all three components (PS, Cy, and H) to ensure a homogeneous distribution and unbiased results. This solvent must be minimally volatile during analysis, and it should interfere as little as possible with the characteristic bands of the compounds of interest. Several candidates were considered and DCE was selected as a good compromise in terms of volatility and spectral interference (see Fig. 2a). A concentration of 30 wt% of PS in DCE was used throughout as a compromise between the need for sensitivity, which improves at higher PS concentration, and a sufficiently low viscosity to enable homogenization of the sample solutions.

(a) Infrared spectra of the pure components Cy, H, PS, and DCE. Shaded areas indicate the spectral regions used for multivariate analysis. (b) Infrared spectra of representative compositions in the selected spectral regions. The numerical values in the legend indicate the approximate Cy and H percentage in the mixture.
An investigation of the pure component spectra, shown in Fig. 2a, was conducted to evaluate the possibility of a univariate analysis of the Cy and H contents in PS using isolated bands of sufficient intensity. For simple systems, the Beer–Lambert law can be used directly to quantify the species of interest. In practice, the spectral information is often obscured, even for moderately complex systems, due to the overlap of bands originating from different components. This was particularly the case for H: although it presents very intense C–H stretching bands between 2800 and 3000 cm−1, the overlap with the C–H stretching bands of both PS and Cy led to strong nonlinearity for univariate calibrations. On the other hand, good candidate bands can be identified for Cy. A spectrally isolated band is also needed for PS to serve as an internal standard because, while its concentration is well controlled in the calibration standards, it is unknown for samples collected at the pilot plant. The best univariate calibration was obtained using the intensity ratio of the 813 cm−1 Cy band (shifted to 818 cm−1 in DCE) and 1601 cm−1 PS bands but, as can be seen in Fig. S1 (Supplemental Material), a nonlinear trend was obtained (see the nonrandom residuals). Univariate analysis of Cy in PS thus provides a quick general guidance for the recycling process optimization, but it cannot provide accurate results. In particular, the presence of a large H content provoked systematic errors due to the partial overlap of the baseline points. Recording spectra with a better spectral resolution led to worse calibration results due to a lower signal-to-noise ratio and the higher prevalence of water vapor rovibrational lines interfering with the PS band.
A multivariate model is thus necessary to quantify H in PS and to provide better predictive power for Cy in PS. Multivariate data analysis methods include classical least squares, multiple linear regression, principal component regression, and PLS regression.21,23–27 PLS is arguably the most common approach for IR because bands associated with the components to quantify are often severely overlapped. Indeed, PLS models provided better determination coefficients than the other methods for Cy and H in PS. The calibration range for the standards was based on the expected Cy and H mass percentages relative to the total mass, Cywt% and Hwt%, at the various stages of the dissolution/precipitation recycling process. Figure 2b shows spectra obtained for mixtures representative of those that could be obtained. This includes samples that mimic a PS solution in Cy before precipitation (18% of Cy and 0% of H), pastes, and pellets. The precipitated PS paste may contain up to 40% of H and 10% of Cy. Washing the paste with H gradually reduces the Cy content. Finally, the devolatilization process reduces the residual solvent content as low as possible in the final pellets. In other words, there are steps during the process where either Cy or H is the dominant solvent present and other steps where both solvents are present simultaneously.
Two separate calibration models were first prepared for Cy-only and H-only conditions. Figure 3 shows the correlation between the predicted and real concentrations of the prepared samples. A linear regression is observed with

Performance of the separate PLS models for the quantification of either Cy-only or H-only in PS.
These calibration models were then used to determine the residual solvent in samples representative of the recycling process, that is, the precipitated paste, the washed paste, and the pellets. To evaluate the washing step efficiency, two different washing conditions, W1 and W2, were tested. The Cy-only model was used for the precipitated paste and pellets, where it should be the dominant solvent, while the H-only model was used for the washed pastes. The results are presented in Table I in terms of wt% of the relevant solvent and percentage of spectrum fit, a parameter that indicates how well the experimental sample spectrum is reconstructed based on the model. An acceptable spectrum fit value above 97% was found only for the pellets, in which a minute quantity of H is indeed expected to be present. The Cy content is lower in the washed pellets obtained from W2 (1.1%) than from its W1 counterpart (1.8%), consistent with more drastic washing conditions for W2. On the other hand, the Cy-only model completely fails to estimate the Cy content in the precipitated paste, where the spectrum fit is very poor (54%) and the sum of the percentages of Cy, PS, and DCE is far from 100%. Observation of the paste spectra indicates that this is due to the presence of H that makes the Cy-only model inapplicable. Similarly, the H-only model fails to properly describe the washed pastes, with spectrum fit values typically <70%, due to the unaccounted presence of Cy. Such single-solvent models are therefore not reliable except for the pellets, leading to the need for a model combining both Cy and H.
Determination of the Cy or H content in PS samples collected at specific steps of the recycling process as determined using the individual cymene or H PLS models.
A PLS calibration model was thus built to describe the four components (PS, Cy, H, and DCE) over the concentration range relevant to a PS dissolution/precipitation recycling process. A very good correlation (

Performance of the combined (Cy + H) PLS model for the quantification of Cy and H in PS.
The model was applied to the same series of recycled PS samples recovered at the pilot plant (Table II). The spectrum fit percentages are systematically improved with values ≥98.8%. This is particularly the case for the pastes for which the single-solvent models failed badly. This is easily understood when noting that the Cy and H contents were substantial in all types of pastes, leading to the breakdown of the single-solvent models. The Cy content decreases from a large value of 11.4% in the precipitated pastes to 3.1% or 2.5% after washing the paste with H. Meanwhile, the H content increases up to ∼22% for the washed paste W2, slightly more than for W1. The results obtained for the pellets are consistent, within quantification error, between the Cy-only model (Table I) and the Cy + H model (Table II). This is understood when noting that the H content in the pellets is indeed within the determination uncertainty of the Cy + H model, so the Cy-only model was indeed applicable. When considering the propagation of the errors on all components of the system, the limit of detection of the model is estimated to be 0.5% for Cy and 1% for H, even though the sample-to-sample replicability is better. These limits of detection are not competitive with mass spectrometry for an accurate determination of the residual solvent content in pellets. Nevertheless, IR spectroscopy allows quantification of large solvent contents, up to 60% for H and 20% for Cy, with relative errors on the order of 2-3% and reproducibility on the order of <0.6% for triplicate samples. It is therefore a useful tool for a rapid determination of the solvent content in pastes for quality control purposes, as well as for the optimization of the precipitation and washing steps in view of a more sustainable and economical PS-recycling process.
Determination of the Cy and H content in PS samples collected at specific steps of the recycling process as determined using the combined PLS model.
Conclusion
Infrared spectroscopy (IR) was applied as a rapid and reliable tool to determine the solvent content in PS at various stages of a dissolution/precipitation recycling process. The application of PLS regression allows quantifying simultaneously the mass percentages of the dissolution solvent, Cy, and the precipitation antisolvent, H, over a large concentration range and with limits of quantifications of ∼0.5%. In its current implementation, the method is not sufficiently sensitive to determine if the solvent content in the recycled pellets is low enough to respect the regulatory limits for commercial-grade applications. It may be possible to compress the pellets into a film form and to probe them by transmission IR spectroscopy, thereby substantially increasing the detection limit compared to the ATR sampling approach used here. Nevertheless, the broad quantification range, fast measurement turnaround time, demonstrated implementation at the plant level, and simplicity for application by minimally trained operators, make ATR-IR a sampling mode of choice for the day-to-day surveillance of a PS-recycling process. It can also be a valuable tool to process engineers seeking to optimize solvent usage during the different stages of the dissolution/precipitation process. While the model reported here is restricted to the specific combination of Cy and H in PS, the approach is applicable to other polymer/solvent/antisolvent combinations. Considering the environmental benefits of the dissolution/precipitation recycling process, it is predictable that other thermoplastic polymers will be recycled by this approach in the future and would benefit from a similar IR-based solvent/antisolvent management tool.
Supplemental Material
sj-docx-1-app-10.1177_27551857231179982 - Supplemental material for Quantification of p -Cymene and Heptane in a Solvent-Based Green Process of Polystyrene Recycling
Supplemental material, sj-docx-1-app-10.1177_27551857231179982 for Quantification of
Footnotes
Acknowledgments
The authors thank the Polystyvert team for their contribution at different stages of this investigation.
Author Contributions
The manuscript was written through contributions of all authors. All authors have approved the final version of the manuscript.
Declaration of Conflicting Interests
The authors declared no potential conflicts of interest with respect to the research, authorship, and/or publication of this article.
Funding
The authors disclosed receipt of the following financial support for the research, authorship, and/or publication of this article: This research was supported by the Natural Science and Engineering Research Council of Canada (grant no. RGPIN-05098-2020) and cofinanced by MITACS (grant no. IT20169).
Supplemental Material
All supplemental material mentioned in the text is available in the online version of the journal.
References
Supplementary Material
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