TY - JOUR
T1 - Plastic Waste Upcycling for Generation of Power and Methanol: Process Simulation and Energy-Exergy-Economic (3E) Analysis
AU - Qian, Qiming
AU - Ren, Jingzheng
AU - He, Chang
N1 - Funding Information:
The work described in this paper was supported by a grant from the Research Committee of The Hong Kong Polytechnic University under student account code RKQ6, a grant from Research Grants Council of the Hong Kong Special Administrative Region, China-General Research Fund (project ID: P0042030, Funding Body ref. no: 15304222, project no. B-Q97U), a grant from the PROCORE-France/Hong Kong Joint Research Scheme sponsored by the Research Grants Council of Hong Kong and the Consulate General of France in Hong Kong (ref. no. F-PolyU501/22), and a grant from the Environment and Conservation Fund (ECF) (grant no. ECF 51/2022).
Publisher Copyright:
© 2023 American Chemical Society.
PY - 2023/11/1
Y1 - 2023/11/1
N2 - To address the global issue of plastic waste, the waste to wealth technique is under investigation. Four processes, known as INP-CC (incineration with carbon capture and power generation), GFP-CC (gasification with carbon capture and power generation), INP-ME (incineration with methanol and power cogeneration), and GFP-ME (gasification with methanol and power cogeneration), which include both traditional and innovative methods, have undergone development, simulation, and comprehensive comparison through techno-economic analysis. GFP-CC and GFP-ME are particularly favored for their energy efficiencies of 43.47 and 34.91%, respectively, in comparison to INP-CC (17.6%) and INP-ME (6.89%). Exergy flow diagrams reveal that the incinerator, gasifier, and combustion chamber account for over 50% of the exergy loss, highlighting their potential for intensification. However, from an economic standpoint, without a larger subsidy fee ($84 per ton) or higher methanol selling price ($550 per ton), processes GFP-ME and INP-ME are not economically attractive due to a negative net present value over 20 years. A sensitivity analysis of key economic parameters demonstrates that the price of methanol and hydrogen has the greatest impact on process economic performance. It appears that process INP-ME is more resilient in terms of economic performance when subjected to the same level of fluctuations in methanol and hydrogen prices, in comparison to GFP-ME.
AB - To address the global issue of plastic waste, the waste to wealth technique is under investigation. Four processes, known as INP-CC (incineration with carbon capture and power generation), GFP-CC (gasification with carbon capture and power generation), INP-ME (incineration with methanol and power cogeneration), and GFP-ME (gasification with methanol and power cogeneration), which include both traditional and innovative methods, have undergone development, simulation, and comprehensive comparison through techno-economic analysis. GFP-CC and GFP-ME are particularly favored for their energy efficiencies of 43.47 and 34.91%, respectively, in comparison to INP-CC (17.6%) and INP-ME (6.89%). Exergy flow diagrams reveal that the incinerator, gasifier, and combustion chamber account for over 50% of the exergy loss, highlighting their potential for intensification. However, from an economic standpoint, without a larger subsidy fee ($84 per ton) or higher methanol selling price ($550 per ton), processes GFP-ME and INP-ME are not economically attractive due to a negative net present value over 20 years. A sensitivity analysis of key economic parameters demonstrates that the price of methanol and hydrogen has the greatest impact on process economic performance. It appears that process INP-ME is more resilient in terms of economic performance when subjected to the same level of fluctuations in methanol and hydrogen prices, in comparison to GFP-ME.
UR - https://www.scopus.com/pages/publications/85177033090
U2 - 10.1021/acs.iecr.3c02665
DO - 10.1021/acs.iecr.3c02665
M3 - Journal article
AN - SCOPUS:85177033090
SN - 0888-5885
VL - 62
SP - 17857
EP - 17870
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 43
ER -