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Bioreactor

About: Bioreactor is a research topic. Over the lifetime, 9980 publications have been published within this topic receiving 192690 citations. The topic is also known as: bioreactors.


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Journal ArticleDOI
TL;DR: An Anaerobic Membrane Bioreactor (AnMBR) pilot plant was studied to improve certain operational conditions of AnMBRs that treat high oil and grease wastewaters discharged from a snacks factory.

55 citations

Journal ArticleDOI
TL;DR: In this article, the performance of sequential sulfate-reducing anaerobic and sulfide-oxidizing aerobic membrane bioreactors (MBRs) for the treatment of synthetic textile wastewater was evaluated under varying concentrations of COD (1000-2000 µmg/L), NaCl (500-1000 µm/L) and sulfate (500 −1500 µm /L), but keeping dye (Remazol Brilliant Violet 5R) concentration constant at 200 −200 µm.

55 citations

Journal ArticleDOI
TL;DR: The aerobic treatment of refinery wastewater in a three-phase (gas–liquid–solid) fluidised bed bioreactor with a low density (matrix particle density smaller than that of water) biomass support was studied and the reduction in COD in the wastewater treated in a bioreactors with KMT® particles used as biomassSupport was investigated.

55 citations

Journal ArticleDOI
TL;DR: These results demonstrate that trickle‐bed reactor systems can sustain tissue concentrations, growth rates and volumetric biomass productivities substantially higher than other reported bioreactor configurations.
Abstract: Trickle-bed root culture reactors are shown to achieve tissue concentrations as high as 36 g DW/L (752 g FW/L) at a scale of 14 L. Root growth rate in a 1.6-L reactor configuration with improved operational conditions is shown to be indistinguishable from the laboratory-scale benchmark, the shaker flask (mu=0.33 day(-1)). These results demonstrate that trickle-bed reactor systems can sustain tissue concentrations, growth rates and volumetric biomass productivities substantially higher than other reported bioreactor configurations. Mass transfer and fluid dynamics are characterized in trickle-bed root reactors to identify appropriate operating conditions and scale-up criteria. Root tissue respiration goes through a minimum with increasing liquid flow, which is qualitatively consistent with traditional trickle-bed performance. However, liquid hold-up is much higher than traditional trickle-beds and alternative correlations based on liquid hold-up per unit tissue mass are required to account for large changes in biomass volume fraction. Bioreactor characterization is sufficient to carry out preliminary design calculations that indicate scale-up feasibility to at least 10,000 liters.

55 citations

Journal ArticleDOI
TL;DR: The decision as to which cell culture system should be chosen, whether batch or continuous processes should be applied essentially is based on the capital investment, the amount of material to be produced, genetic stability of the production cell line, reliability of sterile technology and the flexibility required in the production plant.

55 citations


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Performance
Metrics
No. of papers in the topic in previous years
YearPapers
20241
2023726
20221,549
2021388
2020401
2019413