The urgency of the climate crisis has driven significant efforts to develop technologies that reduce greenhouse gas (GHG) emissions and remove CO2 from the atmosphere. Among the most promising opportunities is the advancement of sustainable and economically viable chemical processes, particularly given that the chemical industry is one of the largest energy consumers and the third-largest source of GHG emissions [1,2]. Potential solutions include the implementation of electrified chemical, energy conversion, and storage systems. However, there remains a need for integrated techno-economic and environmental analysis tools [3], especially for addressing the unique characteristics of electro-decarbonization technologies, along with the uncertainty inherent in their design and operations [4]. Based on that, this work presents a systematic and integrated techno-economic and environmental analysis framework to assess emerging process designs for electrified chemical, energy conversion, and storage systems. This framework can then be used for subsequent process optimization to facilitate the deployment of a net-zero carbon economy.
The proposed framework enhances conventional cost estimation methods to evaluate capital and operating expenses for deploying emerging electrified technologies on a large-scale basis [5]. This is achieved by leveraging data on costs, capacities, and operating conditions from bench- and pilot-scale studies, combined with economies of scale concepts. Such early-stage data is particularly crucial for novel technologies, as commercial-scale information is typically unavailable. Capital and operating cost estimates are further analyzed using key profitability metrics, such as levelized costs (LC), and benchmarked against conventional processes to assess the feasibility and identify trade-offs in adopting emerging process designs. Sensitivity analysis and uncertainty propagation are also explored to evaluate the impact of key variables on profitability and breakeven prices. Additionally, economy of learning concepts can be incorporated into the analysis to determine desirable experience curve behaviors [6].
Four different emerging electrified technologies are considered for application of the TEA framework: (1) Low-temperature electrochemical CO2 reduction process to produce C1 and C2 chemicals [7]; (2) Hydrogen production via solid oxide electrolysis cells (SOEC) [8]; (3) CO2 hydrogenation to methanol via plasma-assisted catalytic joule-heating [9]; and (4) Energy storage using CO2 as an active cathode material for Aluminum-CO2 batteries [10,11]. The results obtained for these case studies include cost-effectiveness trends and trade-off analyses when compared to their traditional manufacturing counterparts. The developed TEA approach in this work can accelerate the deployment and optimization of new electrified chemical process designs.
REFERENCES
[1] International Energy Agency (2021). Net Zero by 2050: A Roadmap for the Global Energy Sector (International Energy Agency).
[2] Intergovernmental Panel On Climate Change (IPCC) (Ed.), 2023. Climate Change 2022 - Mitigation of Climate Change: Working Group III Contribution to the Sixth Assessment Report of the Intergovernmental Panel on Climate Change, 1st ed. Cambridge University Press.
[3] Mahmud, R., Moni, S.M., High, K., Carbajales-Dale, M., 2021. Integration of techno-economic analysis and life cycle assessment for sustainable process design – A review. Journal of Cleaner Production 317, 128247.
[4] Mallapragada, D.S., Dvorkin, Y., Modestino, M.A., Esposito, D.V., Smith, W.A., Hodge, B.-M., Harold, M.P., Donnelly, V.M., Nuz, A., Bloomquist, C., Baker, K., Grabow, L.C., Yan, Y., Rajput, N.N., Hartman, R.L., Biddinger, E.J., Aydil, E.S., Taylor, A.D., 2023. Decarbonization of the chemical industry through electrification: Barriers and opportunities. Joule 7, 23–41.
[5] Turton, R., Shaeiwitz, J. A., Bhattacharya, D., Whiting, W. B., 2018. Analysis, synthesis, and design of chemical processes, 5th edition. ed, Prentice Hall international series in the physical and chemical engineering sciences. Prentice Hall, Boston.
[6] Gazzaneo, V., Watson, M., Ramsayer, C.B., Kilwein, Z.A., Alves, V., Lima, F.V., 2022. A techno‐economic analysis framework for intensified modular systems. J. Adv. Manuf. & Process. 4, 3.
[7] Nascimento, C. A., Lima, F. V., 2023. Application of a Developed Techno-Economic Analysis Framework to CO2 Electrochemical Reduction Processes. In Proceedings of 2023 AIChE Annual Meeting.
[8] Busam, K.M., Nascimento, C. A, Dantas, B., Li, W., Lima, F. V., 2024. Process Modeling and Operability Analysis for the Optimization of a Proton-Conducting Solid Oxide Electrolyzer for Green Hydrogen Production. In Proceedings of 2024 AIChE Annual Meeting.
[9] Dong, Q., Hu, S., Hu, L., 2024. Electrothermal synthesis of commodity chemicals. Nat Chem Eng 1, 680–690.
[10] Fetrow, C., Carugati, C., Yu, X., Zhou, X.-D., Wei, S., 2023. A Secondary Al–CO2 Battery Enabled by Aluminum Iodide as a Homogeneous Redox Mediator. ACS Appl. Mater. Interfaces 15, 12908–12914.
[11] Diaz, G., Wei, S. Gas Diffusion Electrode Improves Kinetics of Rechargeable Aluminum-CO2 Batteries. In Proceedings of AIChE 2024 Annual Meeting.