Enhanced degradation of phenanthrene in a solid–liquid two‐phase partitioning bioreactor via sonication

The current article examined the feasibility of inducing improved delivery and degradation of phenanthrene in a solid–liquid partitioning bioreactor system at bench scale by means of ultrasonic energy input. Initial degradation rates of phenanthrene by a microbial consortium, delivered from Desmopan, were improved 2.7‐fold in the presence of sonication relative to unsonicated controls. Results demonstrated that an operating window involving on/off sonication cycling improved substrate delivery and rational selection of ultrasound cycling profiles could lead to even further enhancements. Additionally, all results were obtained in a conventional bioreactor with commercial ultrasonic equipment and a commercially available polymer. Subsequent DGGE analysis demonstrated that the sonication cycles selected maintained consortium compositions, relative to control cases, and suggest that exposure would not reduce degradative capabilities under the periods of irradiation examined. Finally, consortium members were identified as belonging to the Pandoraea, Sphingobium, and Pseudoxanthomonas genera. Comparison of genetic sequences in the Ribosomal Database Project revealed that some of the bacterial members, identified at the strain level, had been previously observed in PAH degradations, while others have been reported only in the degradation of other aromatics, such as pesticides. Biotechnol. Bioeng. 2010;105: 997–1001. © 2009 Wiley Periodicals, Inc.     

Scaled-up production of mammalian neural precursor cell aggregates in computer-controlled suspension bioreactors

The clinical use of neural precursor cells (NPCs) for the treatment of neurological diseases, such as Parkinson's disease and Huntington's disease, requires overcoming the scarcity of these cells through controlled expansion. The main objective of the present study was to develop a large-scale computer-controlled bioprocess for the expansion of mammalian NPCs in suspension culture by scaling up existing reactor protocols. In order to support the oxygen demands of the maximum cell densities achieved, the volumetric mass transfer coefficient was kept above 1.10/h while scaling-up from small-scale 125 mL vessels to large-scale 500 mL bioreactors. In addition, the maximum shear stress at the impeller tip was maintained between 0.30 and 0.75 Pa to reduce damage to the cells. The resulting large-scale bioprocess achieved maximum viable cell densities of 1.2 x 10(6) cells/mL and a batch multiplication ratio of 9.1. Moreover, the process successfully maintained the NPC characteristics observed in small-scale studies.     

Coenzyme Q<Subscript>10</Subscript> production by <Emphasis Type="Italic">Rhodobacter sphaeroides</Emphasis> in stirred tank and in airlift bioreactor

A higher Coenzyme Q₁₀ (CoQ₁₀) concentration of 25.04 mg/l was found in airlift bioreactor than the value of 18.11 mg/l obtained in stirred tank under the aerobic-dark cultivation of Rhodobacter sphaeroides. Aeration rate didn’t show obvious impact to CoQ₁₀ production in airlift bioreactor. The fed-batch operation in airlift bioreactor could increase the biomass concentration and led to the maximum CoQ₁₀ concentration of 33.91 mg/l measured, but a lower CoQ₁₀ cell content (3.5 mg CoQ₁₀/DCW) was observed in the fed-batch operation as compared to the batch operation. To enhance the CoQ₁₀ content, an aeration-change strategy was proposed in the fed-batch operation of airlift bioreactor. This strategy led to the maximum CoQ₁₀ concentration of 45.65 mg/l, a 35% increase as compared to the simple fed-batch operation. The results of this study suggested that a fed-batch operation in airlift bioreactor accompanying aeration-change could be suitable for CoQ₁₀ production.     

The baffled microtiter plate: Increased oxygen transfer and improved online monitoring in small scale fermentations

Most experiments in screening and process development are performed in shaken bioreactors. Today, microtiter plates are the preferred vessels for small‐scale microbial cultivations in high throughput, even though they have never been optimized for this purpose. To interpret the experimental results correctly and to obtain a base for a meaningful scale‐up, sufficient oxygen supply to the culture liquid is crucial. For shaken bioreactors this problem can generally be addressed by the introduction of baffles. Therefore, the focus of this study is to investigate how baffling and the well geometry affect the maximum oxygen transfer capacity (OTR_max) in microtiter plates. On a 48‐well plate scale, 30 different cross‐section geometries of a well were studied. It could be shown that the introduction of baffles into the common circular cylinder of a microtiter plate well doubles the maximum oxygen transfer capacity, resulting in values above 100 mmol/L/h (k_La > 600 1/h). To also guarantee a high volume for microbial cultivation, it is important to maximize the filling volume, applicable during orbital shaking. Additionally, the liquid height at the well bottom was examined, which is a decisive parameter for online‐monitoring systems such as the BioLector. This technology performs fiber‐optical measurements through the well bottom, therefore requires a constant liquid height at all shaking frequencies. Ultimately, a six‐petal flower‐shaped well geometry was shown to be the optimal solution taking into account all aforementioned criteria. With its favorable culture conditions and the possibility for unrestricted online monitoring, this novel microtiter plate is an efficient tool to gain meaningful results for interpreting and scaling‐up experiments in clone screening and bioprocess development. Biotechnol. Bioeng. 2009;103: 1118–1128. © 2009 Wiley Periodicals, Inc.     

A case study in converting disposable process scouting devices into disposable bioreactors as a future bioprocessing tool

In this study, we perform mass transfer characterization (k_La) on a novel mechanically driven/stirred Process Scouting Device, PSD, (SuperSpinner D 1000®, SSD) and demonstrate that this novel device can be viewed as disposable bioreactor. Using patch‐based optical sensors, we were able to monitor critical cell culture environmental conditions such as dissolved oxygen (DO) and pH in SSD for comparison to a 1 L standard spinner (SS) flask. We also coupled these mass transfer studies with mixing time studies where we observed relative high mixing times (5.2 min) that are typically observed in production scale bioreactors. Decreasing the mixing time 3.5‐fold resulted in 30% increase in k_La (from 2.3 to 3.0 h^?1) and minimum DO level increased from 0% to 20% for our model hybridoma cell line. Finally, maximum viable cell density and protein titer stayed within ±20% of historical data, from our standard 5 L stirred bioreactor (Biostat®) operated under active DO control. Biotechnol. Bioeng. 2012; 109: 2790–2797. © 2012 Wiley Periodicals, Inc.     

A shaken disposable bioreactor system for controlled insect cell cultivations at milliliter‐scale

While wave‐mixed and stirred bag bioreactors are common devices for rapid, safe insect cell culture‐based production at liter‐scale, orbitally shaken disposable flasks are mainly used for screening studies at milliliter‐scale. In contrast to the two aforementioned bag bioreactor types, which can be operated with standard or disposable sensors, shaker flasks have not been instrumented until recently. The combination of 250 mL disposable shake flasks with PreSens's Shake Flask Reader enables both pH and dissolved oxygen to be measured, as well as allowing characterization of oxygen mass transfer. Volumetric oxygen transfer coefficients (k_La‐values) for PreSens 250 mL disposable shake flasks, which were determined for the first time in insect cell culture medium at varying culture volumes and shaker frequencies, ranged between 4.4 and 37.9/h. Moreover, it was demonstrated that online monitoring of dissolved oxygen in shake flasks is relevant for limitation‐free growth of insect cells up to high cell densities in batch mode (1.6×10⁷ cells/mL) and for the efficient expression of an intracellular model protein.     

Purity,cell viability,expression of GFAP and bystin in astrocytes cultured by different procedures

Primary astrocyte cultures are the most commonly used in vitro model for neurobiological studies. We speculated that different protocols might induce differences not only in the percentage of astrocytes but also in their biological characteristics. In this study, we investigated the effects of four major protocols on the purity of astrocytes, cell viability, expression of glial fibrillary acidic protein (GFAP) and bystin of cultured astrocytes using MTT assay, immunocytochemical staining, and Western blot analysis. We demonstrated that the purity of astrocytes (98.9%) generated by the subculture (SC) procedure is significantly higher than those generated by primary culture (PC), shaken once culture (SK‐1) or shaken twice culture (SK‐2). We also showed that expressions of GFAP and bystin in astrocytes that are purified by the SK‐2 or SK‐1 procedures are significantly higher than those in astrocytes prepared by PC or SC. In addition, astrocytes cultured by SK‐2 or SK‐1 have a higher level of cell viabilities at most time points after ischemia compared with astrocytes cultured by PC or SC. These suggested that physical stimulation induced by “shaken” or culture operation might be able to activate astrocytes and implied that different procedures induce differences not only in the purity but also in the biological characteristics of astrocytes, such as the percentage of activated astrocytes, GFAP, and bystin expressions and responses to ischemia. A more detailed analysis about the effect of “culture protocol factor” on the biological characteristics of astrocytes is absolutely needed. J. Cell. Biochem. 109: 30–37, 2010. © 2009 Wiley‐Liss, Inc.     

A novel nonwoven hybrid bioreactor (NWHBR) for enhancing simultaneous nitrification and denitrification

This study proposed a nonwoven hybrid bioreactor (NWHBR) in which the nonwoven fabric played dual roles as a biofilm carrier and membrane‐like separation of the flocculent sludge in the reactor. The results of long‐term monitoring demonstrated that the NWHBR could achieve simultaneous nitrification and denitrification (SND), with nearly complete ammonium removal and 80% removal of total nitrogen. The biofilm attached to the nonwoven fabric removed 27% of the chemical oxygen demand (COD) and 36% of the nitrate in the reactor, an enhanced elimination of nutrients that was attributed to the increased mass transfer within the biofilm due to permeate drag. The results of batch experiments showed that the flocculent sludge played a more dominant role in nitrification and denitrification (79% and 61%, respectively) than the biofilm (21% and 36%, respectively). The batch experiments also revealed that the enforced mass transfer, with an effluent recirculation rate of 4.3 L/m²h (which was the same as the flux during the reactor's long‐term operation), improved the denitrification rate by 58% (i.e., from 9.0 to 14.2 mg‐NO‐N/h). Pyrosequencing of the 16S rRNA gene amplification revealed a high microbial diversity in both the flocculent sludge and biofilm, with Proteobacteria, Bacteroidetes and Chloroflexi as the dominant groups. A phylogenetic (P) test indicated that the NWHBR contained phylogenetically distinct microbial communities: those in the biofilm differed from those in the flocculent sludge. However, the communities on the exterior and interior of the biofilm were more similar to each other. Due to its good SND performance, low physical back‐washing frequency and low air‐to‐water ratio, the NWHBR represents an attractive alternative for the wider application of either low‐cost membrane bioreactors or biofilm reactors. Biotechnol. Bioeng. 2013; 110: 1903–1912. © 2013 Wiley Periodicals, Inc.     

Performance Of A Membrane Bioreactor For Enzymatic Transesterification: Characterization And Comparison With A Batch Stirred Tank Reactor

A membrane bioreactor containing cutinase microencapsulated in reversed micelles of AOT/isooctane was used to perform the alcoholysis of butyl acetate with hexanol. The membrane used was a tubular ceramic membrane with a cut-off of 15, 000 Da. Membrane characterization involved two parts: structure definition and operational properties. The former included membrane imaging to define the average membrane pore size. With the values obtained, characterization proceeded through the prediction of permeability and number of pores. The separation properties of the membrane were evaluated with the determination of rejection coefficients, based on transmission experiments, for all system components, including the substrates, products and the biocatalyst. The performance of the membrane bioreactor (MBR) was compared with the results obtained in a batch stirred tank reactor (BSTR) using the normalized residence time concept. The MBR operated as a differential reactor as theoretical treatment of experimental data demonstrated.     

Strategies for the design and operation of enzymatic reactors for the degradation of highly and poorly soluble recalcitrant compounds

The presence of recalcitrant compounds in both wastewaters and soils is an important environmental problem. Oxidative enzymes from white-rot fungi have been successfully utilised for the in vitro degradation of xenobiotics, such as the azo dye Orange II and the polycyclic aromatic hydrocarbon anthracene (compounds with high and low solubilities, respectively). Two different reactor configurations are proposed: (i) an enzymatic membrane reactor for the treatment of soluble compounds, consisting of a continuous stirred tank reactor coupled to an ultrafiltration membrane to facilitate the retention and recycling of enzyme; and (ii) a two-phase enzymatic reactor for the degradation of poorly soluble compounds, consisting of an immiscible solvent, which contains the contaminant at high concentrations, and the aqueous phase containing the enzyme and cofactors involved in the catalytic cycle. In this paper, factors affecting the design and operation of both systems are discussed, and experimental results concerning the efficiency and stability of the processes are presented.