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Title: Techno-economic analysis and life cycle assessment of mixed plastic waste gasification for production of methanol and hydrogen

Journal Article · · Green Chemistry
DOI:https://doi.org/10.1039/D3GC00679D· OSTI ID:1985196
ORCiD logo [1];  [1];  [2]; ORCiD logo [3]; ORCiD logo [1]; ORCiD logo [4]; ORCiD logo [4];  [3];  [5]; ORCiD logo [2]
  1. Catalytic Carbon Transformation and Scale-Up Center, National Renewable Energy Laboratory, Golden, CO, 80401 USA, BOTTLE Consortium, Golden, CO, 80401 USA
  2. BOTTLE Consortium, Golden, CO, 80401 USA, Renewable Resources and Enabling Sciences Center, National Renewable Energy Laboratory, Golden, CO, 80401 USA
  3. BOTTLE Consortium, Golden, CO, 80401 USA, Strategic Energy Analysis Center, National Renewable Energy Laboratory, Golden, CO, 80401 USA
  4. Catalytic Carbon Transformation and Scale-Up Center, National Renewable Energy Laboratory, Golden, CO, 80401 USA
  5. BOTTLE Consortium, Golden, CO, 80401 USA

Plastic waste management is an area of concern globally, given the accumulation of plastics in landfills and the natural environment. Gasification can convert mixed plastic waste (MPW) to synthesis gas (syngas), a mixture of carbon monoxide (CO) and hydrogen (H2), which can be further converted to commodity chemicals. In this work, we present techno-economic analysis (TEA) and life cycle assessment (LCA) for two gasification pathways that produce methanol and hydrogen from MPW feedstock. In particular, we modeled the gasifier as a dual fluidized bed reactor for MPW gasification in a greenfield, standalone facility. Our analysis indicates that the minimum selling price (MSP) of methanol and hydrogen produced by MPW gasification is $0.70 kg-1 and $3.41 kg-1, respectively. For comparison, we also evaluate the production of methanol and hydrogen from municipal solid waste. For MPW gasification processes, the syngas yield (kg syngas per kg plastic) and waste plastic feedstock price have the largest impact on MSP. Waste plastic feedstock prices of <$0.02 kg-1 can enable MPW-based processes to achieve cost parity with existing fossil-fuel-derived pathways. Additionally, LCA indicates that methanol and hydrogen produced from MPW gasification can reduce the total supply chain energy use by 52% and 56% respectively when compared with fossil-fuel-derived pathways. However, the greenhouse gas emissions (GHG) from MPW-gasification pathways are estimated to increase by 166% and 36% for methanol and hydrogen, respectively, compared to their current production pathways. Due to the co-product credit of steam and electricity export, MPW gasification pathways have lower levels of smog formation, acidification, non-carcinogenics, ozone depletion, eutrophication and particulates than the respective incumbent processes. Since waste streams are the feedstocks in this study, no energy burden was assigned to the upstream processes. Overall, this work identifies syngas yield and waste plastic feedstock price as the two critical variables with the largest impact on the MSP of products produced by MPW gasification. The outcomes of this work can help guide future research in MPW gasification.

Research Organization:
National Renewable Energy Laboratory (NREL), Golden, CO (United States)
Sponsoring Organization:
USDOE Office of Energy Efficiency and Renewable Energy (EERE), Energy Efficiency Office. Advanced Materials & Manufacturing Technologies Office (AMMTO); USDOE Office of Energy Efficiency and Renewable Energy (EERE), Office of Sustainable Transportation. Bioenergy Technologies Office (BETO)
Grant/Contract Number:
AC36-08GO28308
OSTI ID:
1985196
Alternate ID(s):
OSTI ID: 1992014
Report Number(s):
NREL/JA-2A00-83095; GRCHFJ
Journal Information:
Green Chemistry, Journal Name: Green Chemistry Vol. 25 Journal Issue: 13; ISSN 1463-9262
Publisher:
Royal Society of Chemistry (RSC)Copyright Statement
Country of Publication:
United Kingdom
Language:
English

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