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Open AccessArticle
Process Design and Simulation of Biodimethyl Ether (Bio-DME) Production from Biomethane Derived from Agave sisalana Residues
by
Rozenilton de J. Rodrigues
Rozenilton de J. Rodrigues 1,
Carine T. Alves
Carine T. Alves 1,2,3
,
Alison B. Vitor
Alison B. Vitor 2
,
Ednildo Andrade Torres
Ednildo Andrade Torres 1,3 and
Felipe A. Torres
Felipe A. Torres 1,3,4,*
1
Industrial Engineering Postgraduation Program, Polytechnic School, Federal University of Bahia, Salvador 40210-630, Brazil
2
Energy Engineering Department, Center of Science and Technology in Energy and Sustainability, Federal University of Recôncavo of Bahia, Feira de Santana 44042-280, Brazil
3
Interdisciplinary Center in Energy and Environment, Federal University of Bahia, Salvador 40210-630, Brazil
4
Mechanical Systems Department, Center of Exact and Technological Sciences, Federal University of Recôncavo of Bahia, Cruz das Almas 44380-000, Brazil
*
Author to whom correspondence should be addressed.
Processes 2025, 13(11), 3451; https://doi.org/10.3390/pr13113451 (registering DOI)
Submission received: 19 September 2025
/
Revised: 14 October 2025
/
Accepted: 20 October 2025
/
Published: 27 October 2025
Abstract
This study presents the design and simulation of an integrated pathway to produce Biodimethyl ether (Bio-DME) from biomethane derived from Agave sisalana residues, focusing on the downstream sections such as: (i) steam reforming of biogas and water-gas shift to generate syngas and (ii) indirect methanol synthesis followed by methanol dehydration to Bio-DME, including separation and recycle steps. The modeled scope excludes the anaerobic digestion stage. Benchmarking against the literature was used to validate model fidelity. The simulation delivered a single-pass methanol conversion of 81.8%, a Bio-DME reactor conversion of 44.6 mol%, and a Bio-DME yield/selectivity of ≈99 mol%; product purities reached ≈99.99 mol% Bio-DME at the first distillation column and ≈99.9 mol% MeOH in the recycle, indicating efficient separation. Compared to the literature, Bio-DME conversion in this study is slightly below the reported values (0.446 vs. 0.499, Δ = 0.053), while yield is very close to literature (0.99 vs. 0.9979, Δ = 0.0079). Incomplete methanol conversion emerges as the primary optimization lever, pointing to adjustments in operating conditions (T, p), recycle/purge strategy, and H2/CO control. Overall, the results confirm the technical feasibility of the simulated sections and support the development of a sisal-based, low-carbon Bio-DME route relevant to Northeast Brazil.
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MDPI and ACS Style
Rodrigues, R.d.J.; Alves, C.T.; Vitor, A.B.; Torres, E.A.; Torres, F.A.
Process Design and Simulation of Biodimethyl Ether (Bio-DME) Production from Biomethane Derived from Agave sisalana Residues. Processes 2025, 13, 3451.
https://doi.org/10.3390/pr13113451
AMA Style
Rodrigues RdJ, Alves CT, Vitor AB, Torres EA, Torres FA.
Process Design and Simulation of Biodimethyl Ether (Bio-DME) Production from Biomethane Derived from Agave sisalana Residues. Processes. 2025; 13(11):3451.
https://doi.org/10.3390/pr13113451
Chicago/Turabian Style
Rodrigues, Rozenilton de J., Carine T. Alves, Alison B. Vitor, Ednildo Andrade Torres, and Felipe A. Torres.
2025. "Process Design and Simulation of Biodimethyl Ether (Bio-DME) Production from Biomethane Derived from Agave sisalana Residues" Processes 13, no. 11: 3451.
https://doi.org/10.3390/pr13113451
APA Style
Rodrigues, R. d. J., Alves, C. T., Vitor, A. B., Torres, E. A., & Torres, F. A.
(2025). Process Design and Simulation of Biodimethyl Ether (Bio-DME) Production from Biomethane Derived from Agave sisalana Residues. Processes, 13(11), 3451.
https://doi.org/10.3390/pr13113451
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