Chemical and Biomolecular Engineering, Department of
Department of Chemical and Biomolecular Engineering: Faculty Publications
Accessibility Remediation
If you are unable to use this item in its current form due to accessibility barriers, you may request remediation through our remediation request form.
ORCID IDs
Demirel 0000-0002-8183-0991
Date of this Version
2015
Document Type
Article
Citation
Energy (2015) 93: 343–353
doi: 10.1016/j.energy.2015.09.043
Abstract
This study is for the technoeconomic analysis of an integral facility consisting of wind energy-based electrolytic hydrogen production, bioethanol-based carbon dioxide capture and compression, and direct methanol synthesis. ASPEN Plus was used to simulate the facility producing 97.01 mt (metric tons) methanol/day using 138.37 mt CO2/day and 18.56 mt H2/day. A discounted cash flow diagram for the integral facility is used for the economic analysis at various hydrogen production costs and methanol selling prices. The feasibility analysis is based on a multi-criteria decision matrix consisting of economic and sustainability indicators comparing renewable and non-renewable methanol productions. The overall energy efficiency for the renewable methanol is around 58%. Fixation of carbon reduces the CO2 equivalent emission by around –1.05 CO2e/kg methanol. The electrolytic hydrogen production cost is the largest contributor to the economics of the integral facility. The feasibility analysis based on multi-criteria shows that renewable methanol production may be feasible.
Included in
Industrial Engineering Commons, Other Engineering Commons, Process Control and Systems Commons
Comments
Copyright © 2015, Elsevier. Used by permission