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Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors
This paper investigates the scaling‐up of cyanobacterial biomass cultivation and biohydrogen production from laboratory to industrial scale. Two main aspects are investigated and presented, which to the best of our knowledge have never been addressed, namely the construction of an accurate dynamic m...
Autores principales: | , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
John Wiley and Sons Inc.
2015
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4975697/ https://www.ncbi.nlm.nih.gov/pubmed/26041472 http://dx.doi.org/10.1002/bit.25661 |
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author | Zhang, Dongda Dechatiwongse, Pongsathorn del Rio‐Chanona, Ehecatl Antonio Maitland, Geoffrey C. Hellgardt, Klaus Vassiliadis, Vassilios S. |
author_facet | Zhang, Dongda Dechatiwongse, Pongsathorn del Rio‐Chanona, Ehecatl Antonio Maitland, Geoffrey C. Hellgardt, Klaus Vassiliadis, Vassilios S. |
author_sort | Zhang, Dongda |
collection | PubMed |
description | This paper investigates the scaling‐up of cyanobacterial biomass cultivation and biohydrogen production from laboratory to industrial scale. Two main aspects are investigated and presented, which to the best of our knowledge have never been addressed, namely the construction of an accurate dynamic model to simulate cyanobacterial photo‐heterotrophic growth and biohydrogen production and the prediction of the maximum biomass and hydrogen production in different scales of photobioreactors. To achieve the current goals, experimental data obtained from a laboratory experimental setup are fitted by a dynamic model. Based on the current model, two key original findings are made in this work. First, it is found that selecting low‐chlorophyll mutants is an efficient way to increase both biomass concentration and hydrogen production particularly in a large scale photobioreactor. Second, the current work proposes that the width of industrial scale photobioreactors should not exceed 0.20 m for biomass cultivation and 0.05 m for biohydrogen production, as severe light attenuation can be induced in the reactor beyond this threshold. Biotechnol. Bioeng. 2015;112: 2429–2438. © 2015 The Authors. Biotechnology and Bioengineering Published by Wiley Peiodicals, Inc. |
format | Online Article Text |
id | pubmed-4975697 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2015 |
publisher | John Wiley and Sons Inc. |
record_format | MEDLINE/PubMed |
spelling | pubmed-49756972016-08-17 Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors Zhang, Dongda Dechatiwongse, Pongsathorn del Rio‐Chanona, Ehecatl Antonio Maitland, Geoffrey C. Hellgardt, Klaus Vassiliadis, Vassilios S. Biotechnol Bioeng Articles This paper investigates the scaling‐up of cyanobacterial biomass cultivation and biohydrogen production from laboratory to industrial scale. Two main aspects are investigated and presented, which to the best of our knowledge have never been addressed, namely the construction of an accurate dynamic model to simulate cyanobacterial photo‐heterotrophic growth and biohydrogen production and the prediction of the maximum biomass and hydrogen production in different scales of photobioreactors. To achieve the current goals, experimental data obtained from a laboratory experimental setup are fitted by a dynamic model. Based on the current model, two key original findings are made in this work. First, it is found that selecting low‐chlorophyll mutants is an efficient way to increase both biomass concentration and hydrogen production particularly in a large scale photobioreactor. Second, the current work proposes that the width of industrial scale photobioreactors should not exceed 0.20 m for biomass cultivation and 0.05 m for biohydrogen production, as severe light attenuation can be induced in the reactor beyond this threshold. Biotechnol. Bioeng. 2015;112: 2429–2438. © 2015 The Authors. Biotechnology and Bioengineering Published by Wiley Peiodicals, Inc. John Wiley and Sons Inc. 2015-12 2015-07-14 /pmc/articles/PMC4975697/ /pubmed/26041472 http://dx.doi.org/10.1002/bit.25661 Text en © 2015 The Authors. Biotechnology and Bioengineering Published by Wiley Peiodicals, Inc. This is an open access article under the terms of the Creative Commons Attribution (http://creativecommons.org/licenses/by/4.0/) License, which permits use, distribution and reproduction in any medium, provided the original work is properly cited. |
spellingShingle | Articles Zhang, Dongda Dechatiwongse, Pongsathorn del Rio‐Chanona, Ehecatl Antonio Maitland, Geoffrey C. Hellgardt, Klaus Vassiliadis, Vassilios S. Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
title | Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
title_full | Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
title_fullStr | Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
title_full_unstemmed | Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
title_short | Dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
title_sort | dynamic modelling of high biomass density cultivation and biohydrogen production in different scales of flat plate photobioreactors |
topic | Articles |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4975697/ https://www.ncbi.nlm.nih.gov/pubmed/26041472 http://dx.doi.org/10.1002/bit.25661 |
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