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Hydrogen from Waste Plastics: Integrated Pyrolysis–Reforming Simulation and Techno-Economic Insights for a Circular Economy
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An integrated pyrolysis-steam reforming process for waste polyethylene, polypropylene, and polystyrene can produce approximately 651 kg of hydrogen per hour with a 39% internal rate of return and under 6-year payback, demonstrating economic viability for plastic-to-energy conversion. This chemical recycling pathway offers a scalable route for diverting plastic waste that would otherwise fragment into environmental microplastics, addressing pollution at the source.
Plastic waste poses a major environmental issue because it persists in nature for long durations and recycling facilities are not readily available. The conversion of waste materials into hydrogen creates two beneficial effects that help decrease pollution levels and establish hydrogen as a clean energy source for sustainable low-carbon systems. In this study, an integrated process for plastic-to-hydrogen conversion was developed using Aspen HYSYS v14. The system uses pyrolysis, steam reforming, and the water–gas shift (WGS) reaction, through pseudo-components of polyethylene, polypropylene and polystyrene to model decomposition processes. Following optimization, the hydrogen fraction in the syngas rose from 0.664 to 0.733. At this stage, the process produced roughly 651 kg of hydrogen per hour in steady operation. In addition, char and pyrolysis oil were produced as co-products that can be valorized in circular economy applications The implementation of heat integration achieved an 8% reduction in utility demand that proves that internal energy recovery stands as a vital element for sustainable design. The techno-economic analysis showed that the project would achieve a 39% internal rate of return and payback period of 5.95 years, thus proving its financial stability. The research demonstrates how modern process modeling techniques enable the creation of clean technology systems that address plastic pollution problems while producing low-carbon hydrogen.
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Researchers used Aspen Plus process simulation to optimize pyrolysis of mixed plastic waste, finding that fuel production peaks at 460°C and 1 bar while hydrogen production via integrated steam reforming peaks at 700°C, with heat integration substantially cutting external energy demand—though economic viability remained tightly dependent on feedstock throughput.
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Thermochemical plastic waste conversion to hydrogen via pyrolysis, steam reforming, and gasification achieves 45–60% energy efficiency without heat integration, compared to 65–75% for conventional steam methane reforming, with heat recovery being the critical gap. Converting plastic waste to hydrogen rather than allowing it to fragment into microplastics represents a promising circular economy approach that addresses both energy recovery and upstream plastic pollution prevention.
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