2025 AIChE Annual Meeting
(258e) Solvent-Based Polymer Recovery and Bioethanol Production from Municipal Solid Waste: Economic and Environmental Feasibility
Authors
To address the limitations of conventional recycling methods, the Solvent-Targeted Recovery and Precipitation (STRAP) process was introduced in 2020 by Walker et al. as a selective, solvent-based approach for polymer separation.3 STRAP exploits the thermodynamic solubility differences between polymers in organic solvents to achieve targeted dissolution and subsequent recovery by temperature-driven precipitation. Previous studies have shown that STRAP could not only selectively isolate polymers like PE, PP, PET, and EVOH for a variety of industrial wastes, but could also do so with high chemical purity and minimal degradation.4–6 Given STRAP’s robustness, it may be possible to recover the most prevalent polymers, PE and PP, from MSW. Preprocessing of MSW may result in a feedstock mainly composed of biogenic material and polymers, with little to no metals and glass that would interfere with the STRAP process. The remaining nonsoluble co-product of the STRAP process will be enriched in biogenic material that can be readily converted to bioethanol. Altogether, we envision a chemical process that selectively recovers key polyolefins from MSW and produces bioethanol from the biogenic fraction.
In this study, we conducted a techno-economic analysis (TEA) and life cycle assessment (LCA) to evaluate the potential market feasibility and environmental impact of this conceptual STRAP-MSW process. Furthermore, to address the large uncertainty in MSW availability and composition, bioethanol market prices, and potential technological performance at scale, TEA/LCA was coupled with rigorous uncertainty and sensitivity analyses in BioSTEAM—an open-source simulation platform7,8—to elucidate the most salient drivers of sustainability and establish critical targets for research and development. All simulated scenarios demonstrated that the ethanol produced from the STRAP-MSW process resulted in lower carbon intensities than cellulosic ethanol production. The minimum selling price of the recovered polymer resin may be market competitive under optimistic assumptions on the tipping fee credited for MSW, the processing capacity, and the technological performance of bioethanol production.
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