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The halophilic bacterium Halomonas elongata DSM 2581supT/supgenerally adapts well to high level of salinity by biosynthesizing ectoine, which functions as an important compatible solute protecting the cell against external salinity environment. Halophilic bacteria have specific metabolic activities under high-salt conditions and are gradually applied in various industries. The present study focuses on investigating the physiological and metabolic mechanism of H. elongata DSM 2581supT/supdriven by the external salinity environment. The physiological metabolic dynamics under salt stress were investigated to evaluate the effect of NaCl stress on the metabolism of H. elongata. The obtained results demonstrated that ectoine biosynthesis transited from a nongrowth-related process to a growth-related process when the NaCl concentration varied from 1% to 13% (w/v). The maximum biomass (Xsubm/sub = 41.37 g/L), and highest ectoine production (Psubm/sub = 12.91 g/L) were achieved under 8% NaCl. Moreover, the maximum biomass (Xsubm/sub) and the maximum specific growth rates (μsubm/sub) showed a first rising and then declining trend with the increased NaCl stress. Furthermore, the transcriptome analysis of H. elongata under different NaCl concentrations demonstrated that both 8% and 13% NaCl conditions resulted in increased expressions of genes involved in the pentose phosphate pathway, Entner-Doudoroff pathway, flagellar assembly pathway, and ectoine metabolism, but negatively affected the tricarboxylic acid cycle and fatty acid metabolism. At last, the proposed possible adaptation mechanism under the optimum NaCl concentration in H. elongata was described.

Metabolic reprogramming has been coined as a hallmark of cancer, accompanied by which the alterations in metabolite levels have profound effects on gene expression, cellular differentiation and the tumor environment. Yet a systematic evaluation of quenching and extraction procedures for quantitative metabolome profiling of tumor cells is currently lacking. To achieve this, this study is aimed at establishing an unbiased and leakage-free metabolome preparation protocol for Hela carcinoma cell. We evaluated 12 combinations of quenching and extraction methods from three quenchers (liquid nitrogen, -40°C 50% methanol, 0.5°C normal saline) and four extractants (80% methanol, methanol: chloroform: water (1:1:1, v/v/v), 50% acetonitrile, 75°C 70% ethanol) for global metabolite profiling of adherent Hela carcinoma cells. Based on the isotope dilution mass spectrometry (IDMS) method, gas/liquid chromatography in tandem with mass spectrometry was used to quantitatively determine 43 metabolites including sugar phosphates, organic acids, amino acids, adenosine nucleotides and coenzymes involved in central carbon metabolism. Among 12 combinations, cells that washed twice with phosphate buffered saline (PBS), quenched with liquid nitrogen, and then extracted with 50% acetonitrile was found to be the most optimal method to acquire intracellular metabolites with minimal loss during sample preparation. Furthermore, a case study was carried out to evaluate the effect of doxorubicin (DOX) on both adherent cells and 3D tumor spheroids using quantitative metabolite profiling. Based on this, quantitative time-resolved metabolite data can serve to the generation of hypotheses on metabolic reprogramming to reveal its important role in tumor development and treatment.

Metabolomics aims to address what and how regulatory mechanisms are coordinated to achieve flux optimality, different metabolic objectives as well as appropriate adaptations to dynamic nutrient availability. Recent decades have witnessed that the integration of metabolomics and fluxomics within the goal of synthetic biology has arrived at generating the desired bioproducts with improved bioconversion efficiency. Absolute metabolite quantification by isotope dilution mass spectrometry represents a functional readout of cellular biochemistry and contributes to the establishment of metabolic (structured) models required in systems metabolic engineering. In industrial practices, population heterogeneity arising from fluctuating nutrient availability frequently leads to performance losses, that is reduced commercial metrics (titer, rate, and yield). Hence, the development of more stable producers and more predictable bioprocesses can benefit from a quantitative understanding of spatial and temporal cell-to-cell heterogeneity within industrial bioprocesses. Quantitative metabolomics analysis and metabolic modeling applied in computational fluid dynamics (CFD)-assisted scale-down simulators that mimic industrial heterogeneity such as fluctuations in nutrients, dissolved gases, and other stresses can procure informative clues for coping with issues during bioprocessing scale-up. In previous studies, only limited insights into the hydrodynamic conditions inside the industrial-scale bioreactor have been obtained, which makes case-by-case scale-up far from straightforward. Tracking the flow paths of cells circulating in large-scale bioreactors is a highly valuable tool for evaluating cellular performance in production tanks. The "lifelines" or "trajectories" of cells in industrial-scale bioreactors can be captured using Euler-Lagrange CFD simulation. This novel methodology can be further coupled with metabolic (structured) models to provide not only a statistical analysis of cell lifelines triggered by the environmental fluctuations but also a global assessment of the metabolic response to heterogeneity inside an industrial bioreactor. For the future, the industrial design should be dependent on the computational framework, and this integration work will allow bioprocess scale-up to the industrial scale with an end in mind.

In a 54 m3 large-scale penicillin fermentor, the cells experience substrate gradient cycles at the timescales of global mixing time about 20–40 s. Here, we used an intermittent feeding regime (IFR) and a two-compartment reactor (TCR) to mimic these substrate gradients at laboratory-scale continuous cultures. The IFR was applied to simulate substrate dynamics experienced by the cells at full scale at timescales of tens of seconds to minutes (30 s, 3 min and 6 min), while the TCR was designed to simulate substrate gradients at an applied mean residence time ((Formula presented.)) of 6 min. A biological systems analysis of the response of an industrial high-yielding P. chrysogenum strain has been performed in these continuous cultures. Compared to an undisturbed continuous feeding regime in a single reactor, the penicillin productivity (qPenG) was reduced in all scale-down simulators. The dynamic metabolomics data indicated that in the IFRs, the cells accumulated high levels of the central metabolites during the feast phase to actively cope with external substrate deprivation during the famine phase. In contrast, in the TCR system, the storage pool (e.g. mannitol and arabitol) constituted a large contribution of carbon supply in the non-feed compartment. Further, transcript analysis revealed that all scale-down simulators gave different expression levels of the glucose/hexose transporter genes and the penicillin gene clusters. The results showed that qPenG did not correlate well with exposure to the substrate regimes (excess, limitation and starvation), but there was a clear inverse relation between qPenG and the intracellular glucose level.

Background Sophorolipids (SLs) are regarded as one of the most promising biosurfactants. However, high production costs are the main obstacle to extended SLs application. Semi-continuous fermentation, which is based on in-situ separation, is a promising technology for achieving high SLs productivity. Methods and results In this study, the sedimentation mechanism of SLs was analyzed. The formation of a hydrophobic mixture of SLs and rapeseed oil was a key factor in sedimentation. And the hydrophobicity and density of the mixture determined SLs sedimentation rate. On this basis, ultrasonic enhanced sedimentation technology (UEST) was introduced, by which the sedimentation rates were increased by 46.9% to 485.4% with different ratio of rapeseed oil to SLs. UEST-assisted real-time in-situ separation and semi-continuous fermentation were performed. SLs productivity and yield were 2.15 g/L/h and 0.58 g/g, respectively, simultaneously the loss ratio of cells, glucose, and rapeseed oil were significantly reduced. Conclusions This study provides a new horizon for optimization of the SLs fermentation process. This article is protected by copyright. All rights reserved.

With the increasing importance in the application of the molecular biological detection technology in the field of food safety, strengthening education in molecular biology experimental techniques is more necessary for the culture of the students in food quality and safety major. However, molecular biology experiments are not always in curricula of Food quality and safety Majors. This paper introduced a project "competition of molecular biological detection technology for food safety among undergraduate sophomore students in food quality and safety major", students participating in this project needed to learn the fundamental molecular biology experimental techniques such as the principles of molecular biology experiments and genome extraction, PCR and agarose gel electrophoresis analysis, and then design the experiments in groups to identify the meat species in pork and beef products using molecular biological methods. The students should complete the experimental report after basic experiments, write essays and make a presentation after the end of the designed experiments. This project aims to provide another way for food quality and safety majors to improve their knowledge of molecular biology, especially experimental technology, and enhances them to understand the scientific research activities as well as give them a chance to learn how to write a professional thesis. In addition, in line with the principle of an open laboratory, the project is also open to students in other majors in East China University of Science and Technology, in order to enhance students in other majors to understand the fields of molecular biology and food safety. © 2017 by The International Union of Biochemistry and Molecular Biology, 45(4):343-350, 2017.

Aspergillus niger is one of the most important cell factories for industrial enzymes and organic acids production. A comprehensive genome-scale metabolic network model (GSMM) with high quality is crucial for efficient strain improvement and process optimization. The lack of accurate reaction equations and gene-protein-reaction associations (GPRs) in the current best model of A. niger named GSMM iMA871, however, limits its application scope. To overcome these limitations, we updated the A. niger GSMM by combining the latest genome annotation and literature mining technology. Compared with iMA871, the number of reactions in iHL1210 was increased from 1,380 to 1,764, and the number of unique ORFs from 871 to 1,210. With the aid of our transcriptomics analysis, the existence of 63% ORFs and 68% reactions in iHL1210 can be verified when glucose was used as the only carbon source. Physiological data from chemostat cultivations, 13 C-labeled and molecular experiments from the published literature were further used to check the performance of iHL1210. The average correlation coefficients between the predicted fluxes and estimated fluxes from 13 C-labeling data were sufficiently high (above 0.89) and the prediction of cell growth on most of the reported carbon and nitrogen sources was consistent. Using the updated genome-scale model, we evaluated gene essentiality on synthetic and yeast extract medium, as well as the effects of NADPH supply on glucoamylase production in A. niger. In summary, the new A. niger GSMM iHL1210 contains significant improvements with respect to the metabolic coverage and prediction performance, which paves the way for systematic metabolic engineering of A. niger. Biotechnol. Bioeng. 2017;114: 685-695. © 2016 Wiley Periodicals, Inc.

BACKGROUND Oxygen metabolism plays an important role in cell growth, metabolism and survival of microorganism. This report describes the effects of different oxygen metabolism levels on L-lactic acid production by Lactobacillus paracasei, and then a new oxygen uptake rate (OUR) strategy is proposed based on integrated process physiological and metabolic analyses. RESULTS Physiological parameter, OUR, was introduced to quantitatively characterize oxygen metabolism in a microaerobic bioprocess for the first time, and 0.14 mmol L−1 h−1 was adopted as control to simulate industrial lactic acid production. During the growth phase, moderate to high OUR (0.43 mmol L−1 h−1) could promote cell growth, glucose consumption and L-lactic acid production with little decrease in yield. However, when cells entered the stationary phase, significant glycolysis inhibition and pyruvate metabolism shift from lactic acid to acetoin occurred with 0.43 and 0.85 mmol L−1 h−1, both of which led to further L-lactic acid production limitation. Through a new two-step OUR control strategy with 0.43 mmol L−1 h−1 during the growth phase and 0.14 mmol L−1 h−1 during the stationary phase, productivity was enhanced 12.7% and the same yield was achieved as in the control. CONCLUSIONS OUR was identified to be a feasible process control parameter for microaerobic lactic acid production, and the OUR control strategy efficiently improved L-lactic acid production. © 2015 Society of Chemical Industry

BACKGROUND In this study, the performance of aerobic batch fermentation with Aspergillus niger producing sodium gluconate under different oxygen supply levels through adjusting the agitation rate were investigated. The response of glucose metabolism in A. niger to different oxygen uptake rate (OUR) levels has been studied in the present work. RESULTS Metabolic flux analysis demonstrated that the high oxygen supply condition was favorable for cell growth and initial sodium gluconate synthesis during the early fermentation phases. However, during the late stable phase, metabolic flux analysis indicated that a high yield of sodium gluconate production could be achieved at a medium OUR level of 55 ± 2.5 mmol L−1 h−1 as less flux was required for glucolysis and the TCA cycle. With a two-stage OUR control strategy, the final sodium gluconate yield of the batch fermentation was enhanced and reached 93.7% (mol vs mol), which was higher than those obtained using a high oxygen supply level throughout the whole fermentation process. CONCLUSIONS Metabolic flux analysis was successfully used in the present work, and the two-stage OUR control strategy increased the yield of sodium gluconate production to 93.7%. © 2015 Society of Chemical Industry

rAAV (recombinant adeno-associated virus) has become a very useful gene-delivery vector for gene therapy. However, it is very difficult to generate rAAV using triple transfection on a commercial scale, owing to its low transfection efficiency. An optimal procedure for transfection in suspension-culture mode was developed for rAAV-LacZ production in suspension-cultured HEK-293 (human embryonic kidney-293) cells mediated by PEI (polyethyleneimine)-DNA complexes in combination with transient severe hypothermia at 4 degrees C for 1 h in the present study (LacZ is the product of the reporter gene lacZ, which codes for beta-D-galactosidase). It showed that the PEI/DNA ratio, cell density at the beginning of transfection and cell-cycle arrest in G2/M-phase were key factors affecting suspension-culture triple-transfection efficiency and rAAV-LacZ productivity. After incubation at 4 degrees C for 1 h and re-warming at 37 degrees C for 18 h, HEK-293 cells at 1x10(6) cells/ml were transfected with PEI-DNA complexes at a PEI/DNA ratio of 5:1 (w/w) with final concentrations of 30 mug/ml 25 kDa linear PEI and 6 mug/ml plasmid DNA in culture. After 6 h incubation for transfection, an equal volume of medium was added to the culture for additional 48 h growth until harvest. Finally, the high transfection efficiency of some 75% and rAAV-LacZ titre of (7.48+/-0.59)x10(11) physical particles or 1.86+/-0.96x10(10) infectious particles were achieved in 250 ml shake flasks with 60 ml working volume, indicating a promising application for scale-up.

rAAV (recombinant adeno-associated virus) has become a very useful gene-delivery vector for gene therapy. However, it is very difficult to generate rAAV using triple transfection on a commercial scale, owing to its low productivity and inconveniently adhesive nature of its culture. An optimal suspension-culture transfection procedure was developed for rAAV-LacZ production in suspended HEK-293 cells mediated by calcium phosphate (lacZ, a reporter gene, codes for beta-galactosidase). The study showed that cytotoxicity of transfection complexes and cell aggregation in suspension culture were two key factors affecting high suspension-culture transfection efficiency. Cytotoxicity of transfection complexes was influenced effectively by mixture of Ca(2+) and plasmid DNA when their concentrations were decreased from 300 to 150 mM and from 3.0 to 1.5 microg/ml respectively, as manifested by a relatively higher cell viability after suspension-culture transfection. Moreover, the transfection efficiency was still less than 15%. In addition, we explored the disruption of cell aggregation and the control of transfection-complex size with 2.0 mM EGTA treatment for 30 min before transfection and the addition of 100 mM Mg(2+) during transfection respectively, procedures which enhanced transfection efficiency significantly, owing to more contact and endocytosis between cells and transfection complexes. Finally, the high transfection level and rAAV-LacZ titre achieved under optimized suspension-culture transfection conditions, namely 40% and 5 x 10(11) v.g. (vector genomes)/60 ml of medium respectively, is promising for the technique's application in the large-scale production of rAAV.