Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers
The rheology of high-cell density (HCD) cultures is an important parameter for its impact on mixing and sparging, process scale-up, and downstream unit operations in bioprocess development. In this work, time-dependent rheological properties of HCD <i>Pseudomonas putida</i> LS46 cultures...
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doaj-396c7e6294d34a4583cbbe0cdb6f7d1b2020-11-25T01:33:18ZengMDPI AGBioengineering2306-53542019-10-01649310.3390/bioengineering6040093bioengineering6040093Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) PolymersWarren Blunt0Marc Gaugler1Christophe Collet2Richard Sparling3Daniel J. Gapes4David B. Levin5Nazim Cicek6Department of Biosystems Engineering, University of Manitoba, Winnipeg, MB R3T 5V6, CanadaScion Research, Te Papa Tipu Innovation Park, 49 Sala Street, Private Bag 3020, Rotorua 3046, New ZealandScion Research, Te Papa Tipu Innovation Park, 49 Sala Street, Private Bag 3020, Rotorua 3046, New ZealandDepartment of Microbiology, University of Manitoba, Winnipeg, MB R3T 2N2, CanadaScion Research, Te Papa Tipu Innovation Park, 49 Sala Street, Private Bag 3020, Rotorua 3046, New ZealandDepartment of Biosystems Engineering, University of Manitoba, Winnipeg, MB R3T 5V6, CanadaDepartment of Biosystems Engineering, University of Manitoba, Winnipeg, MB R3T 5V6, CanadaThe rheology of high-cell density (HCD) cultures is an important parameter for its impact on mixing and sparging, process scale-up, and downstream unit operations in bioprocess development. In this work, time-dependent rheological properties of HCD <i>Pseudomonas putida</i> LS46 cultures were monitored for microbial polyhydroxyalkanoate (PHA) production. As the cell density of the fed-batch cultivation increased (0 to 25 g·L<sup>−1</sup> cell dry mass, CDM), the apparent viscosity increased nearly nine-fold throughout the fed-batch process. The medium behaved as a nearly Newtonian fluid at lower cell densities, and became increasingly shear-thinning as the cell density increased. However, shear-thickening behavior was observed at shearing rates of approximately 75 rad·s<sup>−1</sup> or higher, and its onset increased with viscosity of the sample. The supernatant, which contained up to 9 g·L<sup>−1</sup> soluble organic material, contributed more to the observed viscosity effect than did the presence of cells. Owing to this behavior, the oxygen transfer performance of the bioreactor, for otherwise constant operating conditions, was reduced by 50% over the cultivation time. This study has shown that the dynamic rheology of HCD cultures is an important engineering parameter that may impact the final outcome in PHA cultivations. Understanding and anticipating this behavior and its biochemical origins could be important for improving overall productivity, yield, process scalability, and the efficacy of downstream processing unit operations.https://www.mdpi.com/2306-5354/6/4/93phaviscositynon-newtonian fluidfed-batch fermentationoxygen transfer<i>pseudomonas putida</i> |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Warren Blunt Marc Gaugler Christophe Collet Richard Sparling Daniel J. Gapes David B. Levin Nazim Cicek |
spellingShingle |
Warren Blunt Marc Gaugler Christophe Collet Richard Sparling Daniel J. Gapes David B. Levin Nazim Cicek Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers Bioengineering pha viscosity non-newtonian fluid fed-batch fermentation oxygen transfer <i>pseudomonas putida</i> |
author_facet |
Warren Blunt Marc Gaugler Christophe Collet Richard Sparling Daniel J. Gapes David B. Levin Nazim Cicek |
author_sort |
Warren Blunt |
title |
Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers |
title_short |
Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers |
title_full |
Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers |
title_fullStr |
Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers |
title_full_unstemmed |
Rheological Behavior of High Cell Density <i>Pseudomonas putida</i> LS46 Cultures during Production of Medium Chain Length Polyhydroxyalkanoate (PHA) Polymers |
title_sort |
rheological behavior of high cell density <i>pseudomonas putida</i> ls46 cultures during production of medium chain length polyhydroxyalkanoate (pha) polymers |
publisher |
MDPI AG |
series |
Bioengineering |
issn |
2306-5354 |
publishDate |
2019-10-01 |
description |
The rheology of high-cell density (HCD) cultures is an important parameter for its impact on mixing and sparging, process scale-up, and downstream unit operations in bioprocess development. In this work, time-dependent rheological properties of HCD <i>Pseudomonas putida</i> LS46 cultures were monitored for microbial polyhydroxyalkanoate (PHA) production. As the cell density of the fed-batch cultivation increased (0 to 25 g·L<sup>−1</sup> cell dry mass, CDM), the apparent viscosity increased nearly nine-fold throughout the fed-batch process. The medium behaved as a nearly Newtonian fluid at lower cell densities, and became increasingly shear-thinning as the cell density increased. However, shear-thickening behavior was observed at shearing rates of approximately 75 rad·s<sup>−1</sup> or higher, and its onset increased with viscosity of the sample. The supernatant, which contained up to 9 g·L<sup>−1</sup> soluble organic material, contributed more to the observed viscosity effect than did the presence of cells. Owing to this behavior, the oxygen transfer performance of the bioreactor, for otherwise constant operating conditions, was reduced by 50% over the cultivation time. This study has shown that the dynamic rheology of HCD cultures is an important engineering parameter that may impact the final outcome in PHA cultivations. Understanding and anticipating this behavior and its biochemical origins could be important for improving overall productivity, yield, process scalability, and the efficacy of downstream processing unit operations. |
topic |
pha viscosity non-newtonian fluid fed-batch fermentation oxygen transfer <i>pseudomonas putida</i> |
url |
https://www.mdpi.com/2306-5354/6/4/93 |
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