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Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis

[Image: see text] The two-step bubble column-photobioreactor photosynthetic biogas upgrading system can enable simultaneous production of biomethane and value-added products from microalgae. However, due to the influence of a large number of variables, including downstream processes and the presence...

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Autores principales: Bose, Archishman, O’Shea, Richard, Lin, Richen, Murphy, Jerry D.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2021
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8277169/
https://www.ncbi.nlm.nih.gov/pubmed/34276129
http://dx.doi.org/10.1021/acs.iecr.0c05974
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author Bose, Archishman
O’Shea, Richard
Lin, Richen
Murphy, Jerry D.
author_facet Bose, Archishman
O’Shea, Richard
Lin, Richen
Murphy, Jerry D.
author_sort Bose, Archishman
collection PubMed
description [Image: see text] The two-step bubble column-photobioreactor photosynthetic biogas upgrading system can enable simultaneous production of biomethane and value-added products from microalgae. However, due to the influence of a large number of variables, including downstream processes and the presence of microalgae, no unanimity has been reached regarding the performance of bubble column reactors in photosynthetic biogas upgrading. To investigate this further, the present work documents in detail, the design and commissioning of a lab-scale bubble column reactor capable of treating up to 16.3 L/h of biogas while being scalable. The performance of the bubble column was assessed at a pH of 9.35 with different algal densities of Spirulina platensis at 20 °C in the presence of light (3–5 klux or 40.5–67.5 μmol m(–2) s(–1)). A liquid/gas flow (L/G) ratio of 0.5 allowed consistent CO(2) removal of over 98% irrespective of the algal density or its photosynthetic activity. For lower concentrations of algae, the volumetric O(2) concentration in the upgraded biomethane varied between 0.05 and 0.52%, thus providing grid quality biomethane. However, for higher algal concentrations, increased oxygen content in the upgraded biomethane due to both enhanced O(2) stripping and the photosynthetic activity of the microalgae as well as clogging and foaming posed severe operational challenges.
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spelling pubmed-82771692021-07-14 Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis Bose, Archishman O’Shea, Richard Lin, Richen Murphy, Jerry D. Ind Eng Chem Res [Image: see text] The two-step bubble column-photobioreactor photosynthetic biogas upgrading system can enable simultaneous production of biomethane and value-added products from microalgae. However, due to the influence of a large number of variables, including downstream processes and the presence of microalgae, no unanimity has been reached regarding the performance of bubble column reactors in photosynthetic biogas upgrading. To investigate this further, the present work documents in detail, the design and commissioning of a lab-scale bubble column reactor capable of treating up to 16.3 L/h of biogas while being scalable. The performance of the bubble column was assessed at a pH of 9.35 with different algal densities of Spirulina platensis at 20 °C in the presence of light (3–5 klux or 40.5–67.5 μmol m(–2) s(–1)). A liquid/gas flow (L/G) ratio of 0.5 allowed consistent CO(2) removal of over 98% irrespective of the algal density or its photosynthetic activity. For lower concentrations of algae, the volumetric O(2) concentration in the upgraded biomethane varied between 0.05 and 0.52%, thus providing grid quality biomethane. However, for higher algal concentrations, increased oxygen content in the upgraded biomethane due to both enhanced O(2) stripping and the photosynthetic activity of the microalgae as well as clogging and foaming posed severe operational challenges. American Chemical Society 2021-04-08 2021-04-21 /pmc/articles/PMC8277169/ /pubmed/34276129 http://dx.doi.org/10.1021/acs.iecr.0c05974 Text en © 2021 American Chemical Society Permits the broadest form of re-use including for commercial purposes, provided that author attribution and integrity are maintained (https://creativecommons.org/licenses/by/4.0/).
spellingShingle Bose, Archishman
O’Shea, Richard
Lin, Richen
Murphy, Jerry D.
Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis
title Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis
title_full Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis
title_fullStr Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis
title_full_unstemmed Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis
title_short Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with Spirulina platensis
title_sort design, commissioning, and performance assessment of a lab-scale bubble column reactor for photosynthetic biogas upgrading with spirulina platensis
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8277169/
https://www.ncbi.nlm.nih.gov/pubmed/34276129
http://dx.doi.org/10.1021/acs.iecr.0c05974
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