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Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica

BACKGROUND: Syngas fermentation is a promising option for the production of biocommodities due to its abundance and compatibility with anaerobic fermentation. Using thermophilic production strains in a syngas fermentation process allows recovery of products with low boiling point from the off-gas vi...

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Autores principales: Redl, Stephanie, Sukumara, Sumesh, Ploeger, Tom, Wu, Liang, Ølshøj Jensen, Torbjørn, Nielsen, Alex Toftgaard, Noorman, Henk
Formato: Online Artículo Texto
Lenguaje:English
Publicado: BioMed Central 2017
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5469130/
https://www.ncbi.nlm.nih.gov/pubmed/28616074
http://dx.doi.org/10.1186/s13068-017-0827-8
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author Redl, Stephanie
Sukumara, Sumesh
Ploeger, Tom
Wu, Liang
Ølshøj Jensen, Torbjørn
Nielsen, Alex Toftgaard
Noorman, Henk
author_facet Redl, Stephanie
Sukumara, Sumesh
Ploeger, Tom
Wu, Liang
Ølshøj Jensen, Torbjørn
Nielsen, Alex Toftgaard
Noorman, Henk
author_sort Redl, Stephanie
collection PubMed
description BACKGROUND: Syngas fermentation is a promising option for the production of biocommodities due to its abundance and compatibility with anaerobic fermentation. Using thermophilic production strains in a syngas fermentation process allows recovery of products with low boiling point from the off-gas via condensation. RESULTS: In this study we analyzed the production of acetone from syngas with the hypothetical production host derived from Moorella thermoacetica in a bubble column reactor at 60 °C with respect to thermodynamic and economic feasibility. We determined the cost of syngas production from basic oxygen furnace (BOF) process gas, from natural gas, and from corn stover and identified BOF gas as an economically interesting source for syngas. Taking gas–liquid mass transfer limitations into account, we applied a thermodynamics approach to derive the CO to acetone conversion rate under the process conditions. We estimated variable costs of production of 389 $/t acetone for a representative production scenario from BOF gas with costs for syngas as the main contributor. In comparison, the variable costs of production from natural gas- and corn stover-derived syngas were determined to be higher due to the higher feedstock costs (1724 and 2878 $/t acetone, respectively). CONCLUSION: We applied an approach of combining thermodynamic and economic assessment to analyze a hypothetical bioprocess in which the volatile product acetone is produced from syngas with a thermophilic microorganism. Our model allowed us to identify process metrics and quantify the variable production costs for different scenarios. Economical production of bulk chemicals is challenging, making rigorous thermodynamic/economic modeling critical before undertaking an experimental program and as an ongoing guide during the program. We intend this study to give an incentive to apply the demonstrated approach to other bioproduction processes. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (doi:10.1186/s13068-017-0827-8) contains supplementary material, which is available to authorized users.
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spelling pubmed-54691302017-06-14 Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica Redl, Stephanie Sukumara, Sumesh Ploeger, Tom Wu, Liang Ølshøj Jensen, Torbjørn Nielsen, Alex Toftgaard Noorman, Henk Biotechnol Biofuels Research BACKGROUND: Syngas fermentation is a promising option for the production of biocommodities due to its abundance and compatibility with anaerobic fermentation. Using thermophilic production strains in a syngas fermentation process allows recovery of products with low boiling point from the off-gas via condensation. RESULTS: In this study we analyzed the production of acetone from syngas with the hypothetical production host derived from Moorella thermoacetica in a bubble column reactor at 60 °C with respect to thermodynamic and economic feasibility. We determined the cost of syngas production from basic oxygen furnace (BOF) process gas, from natural gas, and from corn stover and identified BOF gas as an economically interesting source for syngas. Taking gas–liquid mass transfer limitations into account, we applied a thermodynamics approach to derive the CO to acetone conversion rate under the process conditions. We estimated variable costs of production of 389 $/t acetone for a representative production scenario from BOF gas with costs for syngas as the main contributor. In comparison, the variable costs of production from natural gas- and corn stover-derived syngas were determined to be higher due to the higher feedstock costs (1724 and 2878 $/t acetone, respectively). CONCLUSION: We applied an approach of combining thermodynamic and economic assessment to analyze a hypothetical bioprocess in which the volatile product acetone is produced from syngas with a thermophilic microorganism. Our model allowed us to identify process metrics and quantify the variable production costs for different scenarios. Economical production of bulk chemicals is challenging, making rigorous thermodynamic/economic modeling critical before undertaking an experimental program and as an ongoing guide during the program. We intend this study to give an incentive to apply the demonstrated approach to other bioproduction processes. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (doi:10.1186/s13068-017-0827-8) contains supplementary material, which is available to authorized users. BioMed Central 2017-06-12 /pmc/articles/PMC5469130/ /pubmed/28616074 http://dx.doi.org/10.1186/s13068-017-0827-8 Text en © The Author(s) 2017 Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated.
spellingShingle Research
Redl, Stephanie
Sukumara, Sumesh
Ploeger, Tom
Wu, Liang
Ølshøj Jensen, Torbjørn
Nielsen, Alex Toftgaard
Noorman, Henk
Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica
title Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica
title_full Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica
title_fullStr Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica
title_full_unstemmed Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica
title_short Thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host Moorella thermoacetica
title_sort thermodynamics and economic feasibility of acetone production from syngas using the thermophilic production host moorella thermoacetica
topic Research
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5469130/
https://www.ncbi.nlm.nih.gov/pubmed/28616074
http://dx.doi.org/10.1186/s13068-017-0827-8
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