Full factorial screening of human embryonic stem cell maintenance with multiplexed microbioreactor arrays

Use of human pluripotent stem cells (hPSCs) in regenerative medicine applications relies on control of cell fate decisions by exogenous factors. This control can be hindered by the use of undefined culture components, poorly understood autocrine/paracrine effects, spatiotemporal variations in microenvironmental composition inherent to static culture formats, and signal cross-talk between multiple factors. We recently described microbioreactor arrays that provide a full factorial spectrum of exogenous factors, and allow gradual accumulation of paracrine factors through serial culture chambers. We combined these with defined biochemical conditions, and in situ reporter gene- and immunofluorescence-based readouts to create an hPSC screening platform with enhanced data throughput and microenvironmental control. HES3-EOS-C(3+)-EiP reporter hESCs were screened against FGF-2, TGF-β1, and retinoic acid in a modified mTeSR-1 medium background. Differential pluripotency marker expression reflected mTeSR-1's maintenance capacity, and differentiation in response to removal of maintenance factors or addition of retinoic acid. Interestingly, pluripotency marker expression was downregulated progressively through serial chambers. Since downstream chambers are exposed to greater levels of paracrine factors under continuous flow, this effect is thought to result from secreted factors that negatively influence pluripotency. The microbioreactor array platform decodes factor interplay, and has a broad application in deciphering microenvironmental control of cell fate.     

Microbioreactor Arrays for Full Factorial Screening of Exogenous and Paracrine Factors in Human Embryonic Stem Cell Differentiation

Timed exposure of pluripotent stem cell cultures to exogenous molecules is widely used to drive differentiation towards desired cell lineages. However, screening differentiation conditions in conventional static cultures can become impractical in large parameter spaces, and is intrinsically limited by poor spatiotemporal control of the microenvironment that also makes it impossible to determine whether exogenous factors act directly or through paracrine-dependent mechanisms. We detail here the development of a continuous flow microbioreactor array platform that combines full-factorial multiplexing of input factors with progressive accumulation of paracrine factors through serially-connected culture chambers, and further, the use of this system to explore the combinatorial parameter space of both exogenous and paracrine factors involved in human embryonic stem cell (hESC) differentiation to a MIXL1-GFP⁺ primitive streak-like population. We show that well known inducers of primitive streak (BMP, Activin and Wnt signals) do not simply act directly on hESC to induce MIXL1 expression, but that this requires accumulation of surplus, endogenous factors; and, that conditioned medium or FGF-2 supplementation is able to offset this. Our approach further reveals the presence of a paracrine, negative feedback loop to the MIXL1-GFP⁺ population, which can be overcome with GSK-3β inhibitors (BIO or CHIR99021), implicating secreted Wnt inhibitory signals such as DKKs and sFRPs as candidate effectors. Importantly, modulating paracrine effects identified in microbioreactor arrays by supplementing FGF-2 and CHIR in conventional static culture vessels resulted in improved differentiation outcomes. We therefore demonstrate that this microbioreactor array platform uniquely enables the identification and decoding of complex soluble factor signalling hierarchies, and that this not only challenges prevailing strategies for extrinsic control of hESC differentiation, but also is translatable to conventional culture systems.     

Microplate‐reader compatible perfusion microbioreactor array for modular tissue culture and cytotoxicity assays

One important application of tissue engineering is to provide novel in vitro models for cell‐based assays. Perfusion microbioreactor array provides a useful tool for microscale tissue culture in parallel. However, high‐throughput data generation has been a challenge. In this study, a 4 × 4 array of perfusion microbioreactors was developed for plate‐reader compatible, time‐series quantification of cell proliferation, and cytotoxicity assays. The device was built through multilayer soft lithography. Low‐cost nonwoven polyethylene terephthalate fibrous matrices were integrated as modular tissue culture scaffolds. Human colon cancer HT‐29 cells with stable expression of enhanced green fluorescent protein were cultured in the device with continuous perfusion and reached a cell density over 5 × 10⁷ cells/mL. The microbioreactor array was used to test a chemotherapeutic drug 5‐FU for its effect on HT‐29 cells in continuous perfusion 3D culture. Compared with conventional 2D cytotoxicity assay, significant drug resistance was observed in the 3D perfusion culture. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Bioprocess considerations for T-cell therapy: Investigating the impact of agitation,dissolved oxygen,and pH on T-cell expansion and differentiation

Adoptive T-cell therapy (ACT) has emerged as a promising new way to treat systemic cancers such as acute lymphoblastic leukemia. However, the robustness and reproducibility of the manufacturing process remains a challenge. Here, a single-use 24-well microbioreactor (micro-Matrix) was assessed for its use as a high-throughput screening tool to investigate the effect and the interaction of different shaking speeds, dissolved oxygen (DO), and pH levels on the growth and differentiation of primary T cells in a perfusion-mimic process. The full factorial design allowed for the generation of predictive models, which were used to find optimal culture conditions. Agitation was shown to play a fundamental role in the proliferation of T cells. A shaking speed of 200 rpm drastically improved the final viable cell concentration (VCC), while the viability was maintained above 90% throughout the cultivation. VCCs reached a maximum of 9.22 × 10⁶ cells/ml. The distribution of CD8+ central memory T cells (T_CM), was found to be largely unaffected by the shaking speed. A clear interaction between pH and DO (p < .001) was established for the cell growth and the optimal culture conditions were identified for a combination of 200 rpm, 25% DO, and pH of 7.4. The combination of microbioreactor technology and Design of Experiment methodology provides a powerful tool to rapidly gain an understanding of the design space of the T-cell manufacturing process.     

Controlling the time evolution of mAb N‐linked glycosylation,Part I: Microbioreactor experiments

N‐linked glycosylation is of key importance for the efficacy of many biotherapeutic proteins such as monoclonal antibodies (mAbs). Media components and cell culture conditions have been shown to significantly affect N‐linked glycosylation during the production of glycoproteins using mammalian cell fed‐batch cultures. These parameters inevitably change in modern industrial processes with concentrated feed additions and cell densities beyond 2 × 10⁷ cells/mL. In order to control the time‐dependent changes of protein glycosylation, an automated microbioreactor system was used to investigate the effects of culture pH, ammonia, galactose, and manganese chloride supplementation on nucleotide sugars as well as mAb N‐linked glycosylation in a time‐dependent way. Two different strategies comprising of a single shift of culture conditions as well as multiple media supplementations along the culture duration were applied to obtain changing and constant glycosylation profiles. The different feeding approaches enabled constant glycosylation patterns throughout the entire culture duration at different levels. By modulating the time evolution of the mAb glycan pattern, not only the endpoint but also the ratios between different glycosylation structures could be modified. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1123–1134, 2016     

Optimization of extracellular xylanase production by Dictyoglomus sp. B1 in continuous culture

The thermophilic, xylanolytic, anaerobic organism, Dictyoglomus sp. B1, was cultivated in batch and continuous cultures in media containing insoluble beech-wood xylan. The extracellular xylanase activity levels obtained for the two cultivation methods were compared. Experiments were performed separately to determine the optimum substrate concentration, dilution rate, pH and temperature for xylanase production. Maximum xylanase activity was found at a substrate concentration of 1.5 g xylan/l, a dilution rate of 0.112 h^–1, pH 8.0 and at 7°C. Different combinations of these optimum values were used in a 2³ factorial experiment to investigate whether an increase in the xylanase production/activity could be achieved. A maximum xylanase activity of 2312 U/l was found when fermentors were operated at 73°C with a substrate concentration of 1.5 g xylan/l, pH 8.0, and a dilution rate of 0.112 h^–1. Thus, the optimum xylanase activity in the factorial experiment was obtained when the conditions that gave the maximum xylanase activities in the individual experiments were combined. Optimum xylanase activity obtained in the 2³ factorial experiment was 6.2 times higher than the activity found in the initial batch culture (373 U/l) and 3.0 times higher than the activity of a batch culture (783 U/l) grown at the same optimum conditions as the factorial experiment. The higher specific xylanase activity (217 U/mg protein) found in the 2³ factorial experiment was 4.1 times higher than the specific activity in the initial batch culture (53 U/mg protein).     

Complex responses to culture conditions in Pseudomonas syringae pv. tomato DC3000 continuous cultures: The role of iron in cell growth and virulence factor induction

The growth of a model plant pathogen, Pseudomonas syringae pv. tomato DC3000, was investigated using a chemostat culture system to examine environmentally regulated responses. Using minimal medium with iron as the limiting nutrient, four different types of responses were obtained in a customized continuous culture system: (1) stable steady state, (2) damped oscillation, (3) normal washout due to high dilution rates exceeding the maximum growth rate, and (4) washout at low dilution rates due to negative growth rates. The type of response was determined by a combination of initial cell mass and dilution rate. Stable steady states were obtained with dilution rates ranging from 0.059 to 0.086 h^?1 with an initial cell mass of less than 0.6 OD₆₀₀. Damped oscillations and negative growth rates are unusual observations for bacterial systems. We have observed these responses at values of initial cell mass of 0.9 OD₆₀₀ or higher, or at low dilution rates (<0.05 h^?1) irrespectively of initial cell mass. This response suggests complex dynamics including the possibility of multiple steady states. Iron, which was reported earlier as a growth limiting nutrient in a widely used minimal medium, enhances both growth and virulence factor induction in iron‐supplemented cultures compared to unsupplemented controls. Intracellular iron concentration is correlated to the early induction (6 h) of virulence factors in both batch and chemostat cultures. A reduction in aconitase activity (a TCA cycle enzyme) and ATP levels in iron‐limited chemostat cultures was observed compared to iron‐supplemented chemostat cultures, indicating that iron affects central metabolic pathways. We conclude that DC3000 cultures are particularly dependent on the environment and iron is likely a key nutrient in determining physiology. Biotechnol. Bioeng. 2010;105: 955–964. © 2009 Wiley Periodicals, Inc.     

Role of vascular endothelial growth factor in the communication between human osteoprogenitors and endothelial cells

Proper bone remodeling requires an active process of angiogenesis which in turn supplies the necessary growth factors and stem cells. This tissue cooperation suggests a cross‐talk between osteoblasts and endothelial cells. This work aims to identify the role of paracrine communication through vascular endothelial growth factor (VEGF) in co‐culture between osteoblastic and endothelial cells. Through a well defined direct contact co‐culture model between human osteoprogenitors (HOPs) and human umbilical vein endothelial cells (HUVECs), we observed that HUVECs were able to migrate along HOPs, inducing the formation of specific tubular‐like structures. VEGF₁₆₅ gene expression was detected in the HOPs, was up‐regulated in the co‐cultured HOPs and both Flt‐1 and KDR gene expression increased in co‐cultured HUVECs. However, the cell rearrangement observed in co‐culture was promoted by a combination of soluble chemoattractive factors and not by VEGF₁₆₅ alone. Despite having no observable effect on endothelial cell tubular‐like formation, VEGF appeared to have a crucial role in osteoblastic differentiation since the inhibition of its receptors reduced the co‐culture‐stimulated osteoblastic phenotype. This co‐culture system appears to enhance both primary angiogenesis events and osteoblastic differentiation, thus allowing for the development of new strategies in vascularized bone tissue engineering. J. Cell. Biochem. 106: 390–398, 2009. © 2009 Wiley‐Liss, Inc.     

Optimization of chimeric HIV‐1 virus‐like particle production in a baculovirus‐insect cell expression system

A baculovirus‐insect cell expression system potentially provides the means to produce prophylactic HIV‐1 virus‐like particle (VLP) vaccines inexpensively and in large quantities. However, the system must be optimized to maximize yields and increase process efficiency. In this study, we optimized the production of two novel, chimeric HIV‐1 VLP vaccine candidates (GagRT and GagTN) in insect cells. This was done by monitoring the effects of four specific factors on VLP expression: these were insect cell line, cell density, multiplicity of infection (MOI), and infection time. The use of western blots, Gag p24 ELISA, and four‐factorial ANOVA allowed the determination of the most favorable conditions for chimeric VLP production, as well as which factors affected VLP expression most significantly. Both VLP vaccine candidates favored similar optimal conditions, demonstrating higher yields of VLPs when produced in the Trichoplusia ni Pro? insect cell line, at a cell density of 1 × 10⁶ cells/mL, and an infection time of 96 h post infection. It was found that cell density and infection time were major influencing factors, but that MOI did not affect VLP expression significantly. This work provides a potentially valuable guideline for HIV‐1 protein vaccine optimization, as well as for general optimization of a baculovirus‐based expression system to produce complex recombinant proteins. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Optimal culture conditions for keratinase production by a novel thermophilic Myceliophthora thermophila strain GZUIFR‐H49‐1

Aims: To investigate the effect of medium compositions and culture conditions on keratinase production by a novel thermophilic fungus Myceliophthora thermophila (Apinis) Oorschot strain GZUIFR‐H49‐1. Methods and Results: The thermophilic strain GZUIFR‐H49‐1 with keratinolytic ability was characterized and identified as a strain of M. thermophila on the basis of its morphological characters and molecular analysis of ITS1‐5.8S‐ITS2 rDNA sequence. Among the medium compositions tested, the soluble starch (SS), urea, sodium thiosulfate and CaCl₂ were the most effective C‐source, N‐source, S‐source and mineral ion, respectively, by employing the single‐factor experiment. The urea and pH value were the significant factors (P < 0·05) for the keratinase production in this experiment condition using Plackett–Burman factorial design. The conditions of keratinase production were further optimized by Box–Behnken design. Consequently, there was a 6·4‐fold increase (5100 U l^?1) in the keratinase activity than the initial value (800 U l^?1) by this optimal process. Conclusions: This study indicated that the optimization design proved a useful and powerful tool for the development of optimal medium compositions and culture conditions. Myceliophthora thermophila strain GZUIFR‐H49‐1 was a promising fungus strain for keratinase production. Significance and Impact of the Study: This study characterized a novel thermophilic M. thermophila strain GZUIFR‐H49‐1 with potential applications for keratinase production. These conditions of keratinase production obtained by means of optimization design will be accumulated as potential information for exploration and utilization to the new fungus isolate.     

Optimization of primary culture condition for mesenchymal stem cells derived from umbilical cord blood with factorial design

Mesenchymal stem cells (MSCs) can not only support the expansion of hematopoietic stem cells in vitro, but also alleviate complications and accelerate recovery of hematopoiesis during hematopoietic stem cell transplantation. However, it proved challenging to culture MSCs from umbilical cord blood (UCB) with a success rate of 20–30%. Many cell culture parameters contribute to this outcome and hence optimization of culture conditions is critical to increase the probability of success. In this work, fractional factorial design was applied to study the effect of cell inoculated density, combination and dose of cytokines, and presence of serum and stromal cells. The cultured UCB‐MSC‐like cells were characterized by flow cytometry and their multilineage differentiation potentials were tested. The optimal protocol was identified achieving above 90% successful outcome: 2 × 10⁶ cells/mL mononuclear cells inoculated in Iscove's modified Dulbecco's medium supplied with 10% FBS, 15 ng/mL IL‐3, and 5 ng/mL Granulocyte‐macrophage colony‐stimulating factor (GM‐CSF). Moreover, the UCB‐MSC‐like cells expressed MSC surface markers of CD13, CD29, CD105, CD166, and CD44 positively, and CD34, CD45, and human leukocyte antigens‐DR (HLA‐DR) negatively. Meanwhile, these cells could differentiate into osteoblasts, chondrocytes, and adipocytes similarly to MSCs derived from bone marrow. In conclusion, we have developed an efficient protocol for the primary culture of UCB‐MSCs by adding suitable cytokines into the culture system. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

A novel scale-down mimic of perfusion cell culture using sedimentation in an automated microbioreactor (SAM)

Continuous upstream processing in mammalian cell culture for recombinant protein production holds promise to increase product yield and quality. To facilitate the design and optimization of large-scale perfusion cultures, suitable scale-down mimics are needed which allow high-throughput experiments to be performed with minimal raw material requirements. Automated microbioreactors are available that mimic batch and fed-batch processes effectively but these have not yet been adapted for perfusion cell culture. This article describes how an automated microbioreactor system (ambr15) can be used to scale-down perfusion cell cultures using cell sedimentation as the method for cell retention. The approach accurately predicts the viable cell concentration, in the range of about 1 × 10⁷ cells/mL for a human cell line, and cell viability of larger scale cultures using a hollow fiber based cell retention system. While it was found to underpredict cell line productivity, the method accurately predicts product quality attributes, including glycosylation profiles, from cultures performed in bioreactors with working volumes between 1 L and 1,000 L. The spent media exchange method using the ambr15 was found to predict the influence of different media formulations on large-scale perfusion cultures in contrast to batch and chemostat experiments performed in the microbioreactor system. The described experimental setup in the microbioreactor allowed an 80-fold reduction in cell culture media requirements, half the daily operator time, which can translate into a cost reduction of approximately 2.5-fold compared to a similar experimental setup at bench scale.     

A Two‐stage CSTR Cascade for Studying the Effect of Inhibitory and Toxic Substances in Bioprocesses

In some biotechnological processes like wastewater treatment and biotransformation, substances are involved which are inhibitory or even toxic to the microorganisms. Their presence changes the cell physiology or even acts lethal on the cells so that the process breaks down completely. For studying such processes, a two‐stage continuous‐flow stirred tank reactor (CSTR) cascade was developed where the toxic substance is only supplied to the second reactor. Mathematical modeling of the system showed that identical steady‐state conditions can be established in both bioreactors of the two‐stage CSTR cascade when the dilution rate of the second reactor is twice as high as the dilution rate in the first reactor, provided that both reactors are fed with the same culture medium and possess an identical working volume. The theoretically derived concept was verified by cultivating Saccharomyces cerevisiae CBS 8066 under glucose‐limited aerobic conditions. Independently of the dilution rates established (D₁ in the range of 0.26 to 0.38 h^–1 and D₂ = 2·D₁), the steady‐state values of the biomass, glucose and ethanol concentration were almost identical in both reactors. Moreover, the dynamic behavior after each stepwise change of the dilution rates was also identical in both reactors, which was detected by dissolved‐oxygen measurements. Finally, the system was applied to the whole‐cell biotransformation of ethyl 2‐chloro‐3‐oxo‐butanoate as an example.     

Analysis of secondary structure and self‐assembly of amelogenin by variable temperature circular dichroism and isothermal titration calorimetry

Amelogenin is a proline‐rich enamel matrix protein known to play an important role in the oriented growth of enamel crystals. Amelogenin self‐assembles to form nanospheres and higher order structures mediated by hydrophobic interactions. This study aims to obtain a better insight into the relationship between primary–secondary structure and self‐assembly of amelogenin by applying computational and biophysical methods. Variable temperature circular dichroism studies indicated that under physiological pH recombinant full‐length porcine amelogenin contains unordered structures in equilibrium with polyproline type II (PPII) structure, the latter being more populated at lower temperatures. Increasing the concentration of rP172 resulted in the promotion of folding to an ordered β‐structured assembly. Isothermal titration calorimetry dilution studies revealed that at all temperatures, self‐assembly is entropically driven due to the hydrophobic effect and the molar heat of assembly (ΔH_A) decreases with temperature. Using a computational approach, a profile of domains in the amino acid sequence that have a high propensity to assemble and to have PPII structures has been identified. We conclude that the assembly properties of amelogenin are due to complementarity between the hydrophobic and PPII helix prone regions. Proteins 2009. © 2009 Wiley‐Liss, Inc.     

Nanoliter scale microbioreactor array for quantitative cell biology

A nanoliter scale microbioreactor array was designed for multiplexed quantitative cell biology. An addressable 8 x 8 array of three nanoliter chambers was demonstrated for observing the serum response of HeLa human cancer cells in 64 parallel cultures. The individual culture unit was designed with a "C" shaped ring that effectively decoupled the central cell growth regions from the outer fluid transport channels. The chamber layout mimics physiological tissue conditions by implementing an outer channel for convective "blood" flow that feeds cells through diffusion into the low shear "interstitial" space. The 2 microm opening at the base of the "C" ring established a differential fluidic resistance up to 3 orders of magnitude greater than the fluid transport channel within a single mold microfluidic device. Three-dimensional (3D) finite element simulation were used to predict fluid transport properties based on chamber dimensions and verified experimentally. The microbioreactor array provided a continuous flow culture environment with a Peclet number (0.02) and shear stress (0.01 Pa) that approximated in vivo tissue conditions without limiting mass transport (10 s nutrient turnover). This microfluidic design overcomes the major problems encountered in multiplexing nanoliter culture environments by enabling uniform cell loading, eliminating shear, and pressure stresses on cultured cells, providing stable control of fluidic addressing, and permitting continuous on-chip optical monitoring.     

Application of response surface methodology in medium optimization for spore production of <Emphasis Type="Italic">Coniothyrium minitans</Emphasis> in solid-state fermentation

Summary Spore production of Coniothyrium minitans was optimized by using response surface methodology (RSM), which is a powerful mathematical approach widely applied in the optimization of fermentation process. In the first step of optimization, with Plackett–Burman design, soluble starch, urea and KH²PO⁴ were found to be the important factors affecting C. minitans spore production significantly. In the second step, a 2³ full factorial central composite design and RSM were applied to determine the optimal concentration of each significant variable. A second-order polynomial was determined by the multiple regression analysis of the experimental data. The optimum values for the critical components for the maximum were obtained as follows: soluble starch 0.643 (36.43 g. l⁻¹), urea −0.544 (3.91 g l⁻¹) and KH²PO⁴ 0.049 (1.02 g l⁻¹) with a predicted value of maximum spore production of 9.94 × 10⁹ spores/g IDM. Under the optimal conditions, the practical spore production was 1.04 × 10¹⁰ spores/g IDM. The determination coefficient (R²) was 0.923, which ensure an adequate credibility of the model.     

In situ cell retention of a CHO culture by a reverse‐flow diafiltration membrane bioreactor

Heterogeneities occur in various bioreactor designs including cell retention devices. Whereas in external devices changing environmental conditions cannot be prevented, cells are retained in their optimal environment in internal devices. Conventional reverse‐flow diafiltration utilizes an internal membrane device, but pulsed feeding causes temporal heterogeneities. In this study, the influence of conventional reverse‐flow diafiltration on the yeast Hansenula polymorpha is investigated. Alternating 180 s of feeding with 360 s of non‐feeding at a dilution rate of 0.2 h^?1 results in an oscillating DOT signal with an amplitude of 60%. Thereby, induced short‐term oxygen limitations result in the formation of ethanol and a reduced product concentration of 25%. This effect is enforced at increased dilution rate. To overcome this cyclic problem, sequential operation of three membranes is introduced. Thus, quasi‐continuous feeding is achieved reducing the oscillation of the DOT signal to an amplitude of 20% and 40% for a dilution rate of 0.2 h^?1 and 0.5 h^?1, respectively. Fermentation conditions characterized by complete absence of oxygen limitation and without formation of overflow metabolites could be obtained for dilution rates from 0.1 h^?1 – 0.5 h^?1. Thus, sequential operation of three membranes minimizes oscillations in the DOT signal providing a nearly homogenous culture over time. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1348–1355, 2014     

Cultures of cells from fetal rat brain: Methods to control composition,morphology, and biochemical activity

Fetal tissue transplantation is a promising new approach for the treatment of neurodegenerative diseases, but the optimal conditions for preparing cells for transplantation have not been defined. The growth of a population of septal brain cells, primarily containing cholinergic neurons and glia, was characterized after seeding at densities from 5 × 10⁴ to 6 × 10⁵ cells/cm², on polystyrene‐, collagen‐, laminin‐, and fibronectin‐coated surfaces, in the presence of serum and/or serum‐free medium. Differentiated glial cells were selected by culture on fibronectin or laminin surfaces, in the presence of low amounts of serum (2.5% FBS) and G5, a soluble factor containing EGF and insulin. Differentiated neuronal cells were selected by culture on laminin, in the presence of low amounts of serum (2.5% FBS) and N2, a soluble factor containing supplemental hormones. In each case, a minimum seeding density of 1 × 10⁵ cells/cm² was required. Neuronal growth could be maintained long term (21 days) with high levels of neuronal activity (ChAT activity). © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 62: 461–467, 1999.     

Optimization of medium composition for the production of antimicrobial activity by Bacillus subtilis B38

An antimicrobial activity produced by Bacillus subtilis B38 was found to be effective against several bacteria, including pathogenic and spoilage microorganisms such as, Listeria monocytogenes, Salmonella enteridis, and clinical isolates of methicillin‐resistant Staphylococcus species. Nutrients such as carbon, nitrogen sources, and inorganic salts enhanced the production level of the antibacterial activity by B. subtilis B38. A first screening step showed that lactose, ammonium succinate, and manganese most influenced both cell growth and antibacterial activity production. These three factors varied at two levels in eight experiments using full factorial design. Results indicated that maximum cell growth (OD = 10.2) and maximum production of antibacterial activity (360 AU/mL) were obtained in a modified medium containing 1.5% (w/v) lactose, 0.15% (w/v) ammonium succinate, and 0.3 mg/L manganese. Depending on the indicator strain used, the antibacterial activity was 2‐ to 4‐fold higher in the modified culture medium than in TSB medium under the same conditions. Thin layer chromatography‐bioautography assay showed the presence of three active spots with R_f values of 0.47, 0.7, and 0.82 in TSB medium. However, the inhibition zone of two spots (R_f values of 0.7 and 0.82) was slightly larger in the modified medium. Moreover, a large zone of inhibition with an R_f value of 0.3, was observed in this modified medium, instead of the spot having an R_f value of 0.47. These results suggest that the nutrients act as environmental factors, quantitatively and qualitatively affecting the production of antibacterial compounds by B. subtilis B38. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Design of a cytochrome P450BM3 reaction system linked by two‐step cofactor regeneration catalyzed by a soluble transhydrogenase and glycerol dehydrogenase

A cytochrome P450BM3‐catalyzed reaction system linked by a two‐step cofactor regeneration was investigated in a cell‐free system. The two‐step cofactor regeneration of redox cofactors, NADH and NADPH, was constructed by NAD⁺‐dependent bacterial glycerol dehydrogenase (GLD) and bacterial soluble transhydrogenase (STH) both from Escherichia coli. In the present system, the reduced cofactor (NADH) was regenerated by GLD from the oxidized cofactor (NAD⁺) using glycerol as a sacrificial cosubstrate. The reducing equivalents were subsequently transferred to NADP⁺ by STH as a cycling catalyst. The resultant regenerated NADPH was used for the substrate oxidation catalyzed by cytochrome P450BM3. The initial rate of the P450BM3‐catalyzed reaction linked by the two‐step cofactor regeneration showed a slight increase (approximately twice) when increasing the GLD units 10‐fold under initial reaction conditions. In contrast, a 10‐fold increase in STH units resulted in about a 9‐fold increase in the initial reaction rate, implying that transhydrogenation catalyzed by STH was the rate‐determining step. In the system lacking the two‐step cofactor regeneration, 34% conversion of 50 μM of a model substrate (p‐nitrophenoxydecanoic acid) was attained using 50 μM NADPH. In contrast, with the two‐step cofactor regeneration, the same amount of substrate was completely converted using 5 μM of oxidized cofactors (NAD⁺ and NADP⁺) within 1 h. Furthermore, a 10‐fold dilution of the oxidized cofactors still led to approximately 20% conversion in 1 h. These results indicate the potential of the combination of GLD and STH for use in redox cofactor recycling with catalytic quantities of NAD⁺ and NADP⁺. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009