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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...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American Chemical
Society
2021
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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. |
format | Online Article Text |
id | pubmed-8277169 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2021 |
publisher | American Chemical
Society |
record_format | MEDLINE/PubMed |
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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