(314d) Optimization of Biorefinery Production Chains and Decision-Making through Sustainability Evaluation: A Biojet Fuel Case Study
AIChE Annual Meeting
2017
2017 Annual Meeting
Sustainable Engineering Forum
Sustainable Management of Post Consumption/Use Biomaterials
Tuesday, October 31, 2017 - 9:15am to 9:40am
Previous contributions have addressed the production of biojet fuel; as examples Crawford et al. (4) and Klein-Marcuschamer et al. (5) have analyzed the economic viability of biojet fuel production under different geographical and technological contexts, while Klein-Marcuschamer et al. (5) have studied the air emissions for its production. Going a step forward, Agusdinata et al. (6) have recognized that multiple actors/ stakeholders (e.g. national/international policymakers, biorefineries, farmers) are involved in the development of biojet-fuels, each of which has differents objectives to consider in their decision-making.
In this work, we combine mathematical programming tools (optimization) and the GREENSCOPE approach developed by the U.S. Environmental Protection Agency (7) to assess the sustainability of production of biojet fuels from the perspective of the different actors that participate in the overall production chain. The GREENSCOPE approach allows for the quantification of process sustainability in four main areas: Efficiency, Energy, Economics, and Environment; in here, each E is characterized by a series of metrics that indicates the performance of a particular process. Optimization is applied to find the processing pathways that provide the best performance for each E, and for clusters of the indicators that represent the preferences of the different stakeholders. Multi-objective optimization is then used to find the Pareto frontier that describes the trade-offs among their optimal solutions.
As a case study, we consider the production of biojet fuels from three different organic material sources: eucalyptus, pine, and macauba, through three main technological pathways: fast pyrolysis, hydrothermal liquefaction, and gasification followed by Fischer-Tropsch synthesis. In all cases, the benefits of adding a follow-up cracking step of long-chain (hydrocarbon) residues, is also considered.
The views expressed in this presentation are those of the authors and do not necessarily represent the views or policies of the U.S. Environmental Protection Agency.
References
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