Nisin production of Lactococcus lactis N8 with hemin‐stimulated cell respiration in fed‐batch fermentation system

In this study, nisin production of Lactococcus lactis N8 was optimized by independent variables of glucose, hemin and oxygen concentrations in fed‐batch fermentation in which respiration of cells was stimulated with hemin. Response surface model was able to explain the changes of the nisin production of L. lactis N8 in fed‐batch fermentation system with high fidelity (R² 98%) and insignificant lack of fit. Accordingly, the equation developed indicated the optimum parameters for glucose, hemin, and dissolved oxygen were 8 g L^?1 h^?1, 3 μg mL^?1 and 40%, respectively. While 1711 IU mL^?1 nisin was produced by L. lactis N8 in control fed‐batch fermentation, 5410 IU mL^?1 nisin production was achieved within the relevant optimum parameters where the respiration of cell was stimulated with hemin. Accordingly, nisin production was enhanced 3.1 fold in fed‐batch fermentation using hemin. In conclusion the nisin production of L. lactis N8 was enhanced extensively as a result of increasing the biomass by stimulating the cell respiration with adding the hemin in the fed‐batch fermentation. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:678–685, 2015     

Glucose metabolism determines resistance of cancer cells to bioenergetic crisis after cytochrome‐c release

Many anticancer drugs activate caspases via the mitochondrial apoptosis pathway. Activation of this pathway triggers a concomitant bioenergetic crisis caused by the release of cytochrome‐c (cyt‐c). Cancer cells are able to evade these processes by altering metabolic and caspase activation pathways. In this study, we provide the first integrated system study of mitochondrial bioenergetics and apoptosis signalling and examine the role of mitochondrial cyt‐c release in these events. In accordance with single‐cell experiments, our model showed that loss of cyt‐c decreased mitochondrial respiration by 95% and depolarised mitochondrial membrane potential ΔΨ_m from ?142 to ?88 mV, with active caspase‐3 potentiating this decrease. ATP synthase was reversed under such conditions, consuming ATP and stabilising ΔΨ_m. However, the direction and level of ATP synthase activity showed significant heterogeneity in individual cancer cells, which the model explained by variations in (i) accessible cyt‐c after release and (ii) the cell's glycolytic capacity. Our results provide a quantitative and mechanistic explanation for the protective role of enhanced glucose utilisation for cancer cells to avert the otherwise lethal bioenergetic crisis associated with apoptosis initiation.     

Cultivation of Saccharomyces cerevisiae in continuous culture

Summary Growth of Saccharomyces cerevisiae was investigated under aerobic conditions in a glucose limited chemostat. The steady state concentrations of cells, glucose and ethanol were measured in dependence of the dilution rate. The growth rate showed a biphasic dependence from the glucose concentration. A shift from respiratory to fermentative metabolism (Crabtree-effect) altering heavily the cell yield and the ethanol yield took place in the range of dilution rates between 0.3 h^-1 and 0.5 h^-1. Therefore the classical theory of continuous cultures is not applicable on aerobic growth of Saccharomyces cerevisiae under glucose limitation without introducing further premises. On the other hand the steady state cell concentration as a function of the dilution rate fits well the theoretically calculated curves, if cells are cultivated under conditions where only fermentation or respiration is possible.     

Biotechnological production of ethanol: Biochemistry,processes and technologies

The majority of environmental problems arise from the use of conventional energy sources. The liability of such problems along with the reduction of fossil energy resources has led to the global need for alternative renewable energy sources. Using renewable biofuels as energy sources is of remarkable and continuously growing importance. Producing bioethanol through conversion of waste and residual biomass can be a viable and important perspective. In the first part of this review, general concepts, approaches and considerations concerning the utilization of the most important liquid biofuels, namely biodiesel and bioethanol, are presented. Unlike biodiesel (specifically first generation biodiesel), the production of bioethanol is exclusively based on the utilization of microbial technology and fermentation engineering. In the second part of this review, the biochemistry of ethanol production, with regards to the use of hexoses, pentoses or glycerol as carbon sources, is presented and critically discussed. Differences in the glycolytic pathways between the major ethanol‐producing strains (Saccharomyces cerevisiae and Zymomonas mobilis) are presented. Regulation between respiration and fermentation in ethanol‐producing yeasts, viz. effects “Pasteur”, “Crabtree”, “Kluyver” and “Custers”, is discussed. Xylose and glycerol catabolism related with bioethanol production is also depicted and commented. The technology of the fermentation is presented along with a detailed illustration of the substrates used in the process and in pretreatment of lignocellulosic biomass, and the various fermentation configurations employed (separate hydrolysis and fermentation, simultaneous saccharification and fermentation, simultaneous saccharification and co‐fermentation and consolidated bioprocessing). Finally, the production of bioethanol under non‐aseptic conditions is presented and discussed.     

Revisiting the Crabtree/Warburg effect in a dynamic perspective: a fitness advantage against sugar-induced cell death

The mechanisms behind the Warburg effect in mammalian cells, as well as for the similar Crabtree effect in the yeast Saccharomyces cerevisiae, are still a matter of debate: why do cells shift from the energy-efficient respiration to the energy-inefficient fermentation at high sugar concentration?

This review reports on the strong similarities of these phenomena in both cell types, discusses the current ideas, and provides a novel interpretation of their common functional mechanism in a dynamic perspective. This is achieved by analysing another phenomenon, the sugar-induced-cell-death (SICD) occurring in yeast at high sugar concentration, to highlight the link between ATP depletion and cell death.

The integration between SICD and the dynamic functioning of the glycolytic process, suggests that the Crabtree/Warburg effect may be interpreted as the avoidance of ATP depletion in those conditions where glucose uptake is higher than the downstream processing capability of the second phase of glycolysis. It follows that the down-regulation of respiration is strategic for cell survival allowing the allocation of more resources to the fermentation pathway, thus maintaining the cell energetic homeostasis.     

Pilot production of Clonostachys rosea conidia in a solid‐state fermentor optimized using response surface methodology

The nonpathogenic, saprophytic fungus Clonostachys rosea is one of the most powerful fungal biological control agents (BCAs). However, the production of fungal BCAs is still a major constraint for their large‐scale use and commercialization. Here, we developed a novel solid‐fermentation reactor that is light transparent and ventilated both at the top and the bottom, and optimized C. rosea cultivation conditions in solid‐state fermentation using response surface methodology. The growth area of spores provided by the novel fermentor was two times that of the traditional one. A quadratic polynomial model was developed, which indicated the effects of variables on the conidia yield. The greatest spore production of 3.50 × 10¹⁰ spores/g‐dry‐matter was obtained after 11 days at the initial moisture content of 69.2% w/w, the medium thickness of 3.84 cm, and the porosity of 0.37%. The optimized spore yield was increased by one order of magnitude. The fermentation time was shortened from 15 to 11 days. With the novel solid‐fermentation reactor, increase in C. rosea spores production and decrease in fermentation time were achieved. Current data imply that both the novel solid‐fermentation reactor designed and the optimized fermentation conditions are suitable for industrial‐scale C. rosea spore production.     

Trade‐offs to flight capability in Gryllus firmus: the influence of whole‐organism respiration rate on fitness

Wing dimorphism, where some macropterous long‐winged (LW) individuals can fly whereas micropterous short‐winged (SW) individuals cannot, is common in insects and believed to be maintained in part by trade‐offs between flight capability and reproductive traits. In this paper we examine differences in whole‐organism respiration rate between wing morphs of the sand cricket Gryllus firmus. We hypothesized that maintenance of the flight apparatus would result in elevated CO₂ respired because of the high metabolic cost of these tissues, which, in turn, constrain resources available for egg production in females. As the trade‐off involves calling behaviour in males, we predicted no equivalent constraint on organ development in this sex. We found female macropters (particularly older crickets) had significantly higher residual respiration rates than micropters. In males, we found only marginal differences between wing morphs. In both sexes there was a highly significant effect of flight muscles status on residual respiration rate, individuals with functional muscles having higher respiration rates. Both female and male macropters had significantly smaller gonads than micropters. Whole‐organism residual respiration rate was negatively correlated with fecundity: macropterous females with high respiration rates had smaller gonads compared with macropterous females with lower respiration rates.     

Identification of cell culture conditions to control N‐glycosylation site‐occupancy of recombinant glycoproteins expressed in CHO cells

The effect of different cell culture conditions on N‐glycosylation site‐occupancy has been elucidated for two different recombinant glycoproteins expressed in Chinese hamster ovary (CHO) cells, recombinant human tissue plasminogen activator (t‐PA) and a recombinant enzyme (glycoprotein 2—GP2). Both molecules contain a N‐glycosylation site that is variably occupied. Different environmental factors that affect the site‐occupancy (the degree of occupied sites) of these molecules were identified. Supplementing the culture medium with additional manganese or iron increased the fraction of fully occupied t‐PA (type I t‐PA) by approximately 2.5–4%. Decreasing the cultivation temperature from 37 to 33°C or 31°C gradually increased site‐occupancy of t‐PA up to 4%. The addition of a specific productivity enhancer, butyrate, further increased site‐occupancy by an additional 1% under each cultivation temperature tested. In addition, the thyroid hormones triiodothyronine and thyroxine increased site‐occupancy of t‐PA compared to control conditions by about 2%. In contrast, the addition of relevant nucleoside precursor molecules involved in N‐glycan biosynthesis (e.g., uridine, guanosine, mannose) either had no effect or slightly reduced site‐occupancy. For the recombinant enzyme (GP2), it was discovered that culture pH and the timing of butyrate addition can be used to control N‐glycan site‐occupancy within a specific range. An increase in culture pH correlated with a decrease in site‐occupancy. Similarly, delaying the timing for butyrate addition also decreased site‐occupancy of this molecule. These results highlight the importance of understanding how cell culture conditions and media components can affect the product quality of recombinant glycoproteins expressed in mammalian cell cultures. Furthermore, the identification of relevant factors will enable one to control product quality attributes, specifically N‐glycan site‐occupancy, within a specific range when applied appropriately. Biotechnol. Bioeng. 2009;103: 1164–1175. © 2009 Wiley Periodicals, Inc.     

Physiological characterization of starch-utilizing <Emphasis Type="Italic">Saccharomyces</Emphasis> sp. SK0704 isolated from kimchi

Saccharomyces sp. SK0704 (further defined as SK0704) isolated from long-term-ripening kimchi was identified by a biochemical method with an API kit; its physiology was found to be very similar to that of S. cerevisiae ATCC 26603 (further defined as ATCC 26603), except in terms of starch utilization. SK0704 did not excrete extracellular glucoamylase, but utilized starch as a sole carbon source under only aerobic conditions. Crude enzyme excreted from SK0704 catalyzed the saccharification of starch to glucose, but ATCC 26603 did not. The PCR product obtained using the chromosomal DNA of SK0704 and the primers designed on the basis of the extracellular glucoamylase-coding gene of S. diastaticus was homologous with the intracellular sporulation-specific glucoamylase of S. cerevisiae. SDS-PAGE pattern of soluble protein extracted from yeast cells grown on glucose was greatly different from that on starch. From these results, we proposed that the SK0704 may have a specific physiological function for starch catabolism such as membrane transport system and intracellular sac-charification of starch.     

The endosomal sorting complex required for transport complex negatively regulates Erg6 degradation under specific glucose restriction conditions

Lipid droplets (LDs) are cytosolic fat storage organelles that play roles in lipid metabolism, trafficking and signaling. Breakdown of LDs in Saccharomyces cerevisiae is mainly achieved by lipolysis and lipophagy. In this study, we found that the endosomal sorting complex required for transport (ESCRT) in S. cerevisiae negatively regulated the turnover of a LD marker, Erg6, under both simplified glucose restriction (GR) and acute glucose restriction (AGR) conditions by monitoring the localization and degradation of Erg6. Loss of Vps27, Snf7 or Vps4, representative subunits of the ESCRT machinery, facilitated the delivery of Erg6‐GFP to vacuoles and its degradation depending on the lipophagy protein Atg15 under simplified GR. Additionally, the lipolysis proteins Tgl3 and Tgl4 were also involved in the enhanced vacuolar localization and degradation of Erg6‐GFP in vps4Δ cells. Furthermore, we found that Atg14, which is required for the formation of putatively liquid‐ordered (Lo) membrane domains on the vacuole that act as preferential internalization sites for LDs, abundantly localized to vacuolar membranes in ESCRT mutants. Most importantly, the depletion or overexpression of Atg14 correspondingly abolished or promoted the observed Erg6 degradation in ESCRT mutant cells. We propose that Atg14 together with other proteins promotes Erg6 degradation in ESCRT mutant cells under specific glucose restriction conditions. These results shed new light on the regulation of ESCRT on LD turnover.     

Potential action of copper surfaces on meticillin-resistant Staphylococcus aureus

Aims: Studies to date have shown rapid killing of bacterial cells when exposed to copper surfaces. The mechanistic action of copper on bacterial cells is so far unknown. Methods and Results: To investigate potential mechanisms involved, meticillin‐resistant Staphylococcus aureus (MRSA) cells (10⁷ CFU) were inoculated onto coupons of copper or stainless steel and stained with either the viability fluorophore 5‐cyano‐2,3‐ditolyl tetrazolium (CTC), to detect respiration, or BacLight? (SYTO9/propidium iodide), to determine cell wall integrity. Coupons were then observed in‐situ using epifluorescence microscopy. In addition, DNA from cells inoculated onto either copper or stainless steel surfaces was isolated and analysed by agarose gel electrophoresis. An effect on cellular respiration with CTC reduction was evident but no effect on cell membrane integrity (BacLight?) was observed. Results from the DNA isolation indicated a copper‐induced detrimental effect on MRSA genomic material as no bands were observed after exposure to copper surface. Conclusions: The results indicate that exposure to copper surfaces rapidly kills MRSA by compromising cellular respiration and damaging DNA, with little effect on cell membrane integrity. Significance and Impact of the study: This research provides a mechanistic explanation in support of previous suggestions that although copper surfaces do not affect membrane integrity of cells, there is still a rapid antimicrobial effect.     

Activation of the small GTPase Rac1 by a specific guanine-nucleotide-exchange factor suffices to induce glucose uptake into skeletal-muscle cells

Background information. Insulin‐stimulated glucose uptake into skeletal muscle is crucial for glucose homoeostasis, and depends on the recruitment of GLUT4 (glucose transporter 4) to the plasma membrane. Mechanisms underlying insulin‐dependent GLUT4 translocation, particularly the role of Rho family GTPases, remain controversial. Results. In the present study, we show that constitutively active Rac1, but not other Rho family GTPases tested, induced GLUT4 translocation in the absence of insulin, suggesting that Rac1 activation is sufficient for GLUT4 translocation in muscle cells. Rac1 activation occurred in dorsal membrane ruffles of insulin‐stimulated cells as revealed by a novel method to visualize activated Rac1 in situ. We further identified FLJ00068 as a GEF (guanine‐nucleotide‐exchange factor) responsible for this Rac1 activation. Indeed, constitutively active FLJ00068 caused Rac1 activation in dorsal membrane ruffles and GLUT4 translocation without insulin stimulation. Down‐regulation of Rac1 or FLJ00068 by RNA interference, on the other hand, abrogated insulin‐induced GLUT4 translocation. Basal, but not insulin‐stimulated, activity of the serine/threonine kinase Akt was required for the induction of GLUT4 translocation by constitutively active Rac1 or FLJ00068. Conclusion. Collectively, Rac1 activation specifically in membrane ruffles by the GEF FLJ00068 is sufficient for insulin induction of glucose uptake into skeletal‐muscle cells.     

An In‐situ glucose‐stimulated insulin secretion assay under perfusion bioreactor conditions

Perfusion bioreactors, unlike traditional in vitro cell culture systems, offer stringent control of physiological parameters such as pH, flow, temperature, and dissolved oxygen concentration which have been shown to have an impact on cellular behaviour and viability. Due to the relative infancy and the growing interest in these in vitro culture systems, detection methods to monitor cell function under dynamic perfusion bioreactor conditions remains one of the main challenges. In this study, INS‐1 cells, a cell line which exhibit glucose‐stimulated insulin secretion, were embedded in fibrin and cultured under perfusion bioreactor conditions for 48 h and then exposed to either a high‐, or low‐glucose concentration for 24 h. These cultures were compared to non‐bioreacted controls. Bioreacted cultures exposed to a high‐glucose concentration showed the highest glucose‐stimulated insulin secretion when compared to those in a low‐glucose environment. The stimulation index, a marker for insulin secretion functionality, increased over time. A lower incidence of apoptotic cells was observed in the bioreacted cultures when compared to non‐bioreacted ones, as evaluated by a TUNEL assay. Immunofluorescence staining of Ki67 and insulin was performed and showed no differences in the incidence of proliferative cells between conditions (bioreacted and non‐bioreacted), where all cells stained positive for insulin. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:454–462, 2017     

Growth of Saccharomyces cerevisiae in a chemostat under high glucose conditions

Saccharomyces cerevisiae was grown in a chemostat under high glucose conditions (up to 300 g l^–1). The results support the view that higher glucose feed favors higher ethanol production regardless of the existence of osmotic stress. A low glucose utilization and yield coefficient provides an opportunity to improve continuous fermentation performance in the fuel alcohol industry. The possibility exists of reusing yeast cells and subsequently lower operating costs, and by using an optimal glucose feeding concentration between 100 and 200 g l^–1.     

Dilution rates influence ammonia-assimilating enzyme activities and cell parameters of Selenomonas ruminantium strain D in continuous (glucose-limited) culture

Aims: The objective of this study was to examine the effect of dilution rates (Ds, varying from 0·05 to 0·42 h^?1) in glucose‐limited continuous culture on cell yield, cell composition, fermentation pattern and ammonia assimilation enzymes of Selenomonas ruminantium strain D. Methods and Results: All glucose‐limited continuous culture experiments were conducted under anaerobic conditions. Except for protein, all cell constituents including carbohydrates, RNA and DNA yielded significant cubic responses to Ds with the highest values at Ds of either 0·10 or 0·20 h^?1. At Ds higher than 0·2 h^?1, fermentation acid pattern shifted primarily from propionate and acetate to lactate production. Succinate also accumulated at the higher Ds (0·30 and 0·42 h^?1). Glucose was most efficiently utilized by S. ruminantium D at 0·20 h^?1 after which decreases in glucose and ATP yields were observed. Under energy limiting conditions, glutamine synthetase (GS) and glutamate dehydrogenase (GDH) appeared to be the major enzymes involved in nitrogen assimilation suggesting that other potential ammonia incorporating enzymes were of little importance in ammonia assimilation in S. ruminantium D. GS exhibited lower activities than GDH at all Ds, which indicates that the bacterial growth rate is not a primary regulator of their activities. Conclusions: Studied dilution rates influenced cell composition, fermentation pattern and nitrogen assimilation of S. ruminantium strain D grown in glucose‐limited continuous culture. Significance and Impact of the Study: Selenomonas ruminantium D is an ecologically and evolutionary important bacterium in ruminants and is present under most rumen dietary conditions. Characterizing the growth physiology and ammonia assimilation enzymes of S. ruminantium D during glucose limitation at Ds, which simulate the liquid turnover rates in rumen, will provide a better understanding of how this micro‐organism responds to differing growth conditions.     

Effect of glucose on xylose utilization in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> harboring the xylose reductase gene

We have constructed recombinant Saccharomyces cerevisiae JH1 harboring a xylose reductase gene (xyl1) isolated from Pichia stipitis. However, JH1 still utilizes glucose more easily than xylose. Therefore, in this study, we characterized the effect of a glucose supplement on xylose utilization, the expression level of xylose reductase as a recombinant gene in JH1, and the expression levels of two hexose transporters (Hxt4 and Hxt7) due to co-fermentation of different concentrations of glucose and xylose. Co-fermentation using 20 g/l of glucose increased xylose consumption up to 11.7 g/l, which was 7.9-fold that of xylose fermentation without a glucose supplement. In addition, we found xyl1 mRNA levels dramatically increased as cells grew under co-fermentation conditions with supplementary glucose; this result is consistent with a significant decrease in the xylose concentration 48 h after cultivation. In addition, the expression levels of Hxt4 and Hxt7 were strongly activated by the presence of glucose and xylose; in particular, Hxt7 showed a 2.9-fold increased expression relative to that of recombinant S. cerevisiae JHM with only a backbone vector, pYES2. The results of this study suggest that xylose utilization would be improved by activation of hexose transporters induced by glucose (rather than xylose) reductase expression.     

A C6/C5 co‐fermenting Saccharomyces cerevisiae strain with the alleviation of antagonism between xylose utilization and robustness

During second‐generation bioethanol production from lignocellulosic biomass, the desired traits for fermenting microorganisms, such as Saccharomyces cerevisiae, are high xylose utilization and high robustness to inhibitors in lignocellulosic hydrolysates. However, as observed previously, these two traits easily showed the antagonism, one rising and the other falling, in the C6/C5 co‐fermenting S. cerevisiae strain. In this study, LF1 obtained in our previous study is an engineered budding yeast strain with a superior co‐fermentation capacity of glucose and xylose, and was then mutated by atmospheric and room temperature plasma (ARTP) mutagenesis to improve its robustness. The ARTP‐treated cells were grown in 50% (v/v) leachate from lignocellulose pretreatment with high inhibitors content for adaptive evolution. After 30 days, the generated mutant LF1‐6 showed significantly enhanced tolerance, with a six‐fold increase in cell density in the above leachate. Unfortunately, its xylose utilization dropped markedly, indicating the recurrence of the negative correlation between xylose utilization and robustness. To alleviate this antagonism, LF1‐6 cells were iteratively mutated with ARTP mutagenesis and then anaerobically grown using xylose as the sole carbon source, and xylose utilization was restored in the resulting strain 6M‐15. 6M‐15 also exhibited increased co‐fermentation performance of xylose and glucose with the highest ethanol productivity reported to date (0.525 g g^?1 h^?1) in high‐level mixed sugars (80 g L^?1 glucose and 40 g L^?1 xylose) with no inhibitors. Meanwhile, its fermentation time was shortened by 8 h compared to that of LF1. During the fermentation of non‐detoxified lignocellulosic hydrolysate with high inhibitor concentrations at pH ~3.5, 6M‐15 can efficiently convert glucose and xylose with an ethanol yield of 0.43 g g^?1. 6M‐15 is also regarded as a potential chassis cell for further design of a customized strain suitable for production of second‐generation bioethanol or other high value‐added products from lignocellulosic biomass.     

Fast dynamic response of the fermentative metabolism of Escherichia coli to aerobic and anaerobic glucose pulses

The response of Escherichia coli cells to transient exposure (step increase) in substrate concentration and anaerobiosis leading to mixed‐acid fermentation metabolism was studied in a two‐compartment bioreactor system consisting of a stirred tank reactor (STR) connected to a mini‐plug‐flow reactor (PFR: BioScope, 3.5 mL volume). Such a system can mimic the situation often encountered in large‐scale, fed‐batch bioreactors. The STR represented the zones of a large‐scale bioreactor that are far from the point of substrate addition and that can be considered as glucose limited, whereas the PFR simulated the region close to the point of substrate addition, where glucose concentration is much higher than in the rest of the bioreactor. In addition, oxygen‐poor and glucose‐rich regions can occur in large‐scale bioreactors. The response of E. coli to these large‐scale conditions was simulated by continuously pumping E. coli cells from a well stirred, glucose limited, aerated chemostat (D = 0.1 h^?1) into the mini‐PFR. A glucose pulse was added at the entrance of the PFR. In the PFR, a total of 11 samples were taken in a time frame of 92 s. In one case aerobicity in the PFR was maintained in order to evaluate the effects of glucose overflow independently of oxygen limitation. Accumulation of acetate and formate was detected after E. coli cells had been exposed for only 2 s to the glucose‐rich (aerobic) region in the PFR. In the other case, the glucose pulse was also combined with anaerobiosis in the PFR. Glucose overflow combined with anaerobiosis caused the accumulation of formate, acetate, lactate, ethanol, and succinate, which were also detected as soon as 2 s after of exposure of E. coli cells to the glucose and O₂ gradients. This approach (STR‐mini‐PFR) is useful for a better understanding of the fast dynamic phenomena occurring in large‐scale bioreactors and for the design of modified strains with an improved behavior under large‐scale conditions. Biotechnol. Bioeng. 2009; 104: 1153–1161. © 2009 Wiley Periodicals, Inc.     

Molecular crowding defines a common origin for the Warburg effect in proliferating cells and the lactate threshold in muscle physiology

Aerobic glycolysis is a seemingly wasteful mode of ATP production that is seen both in rapidly proliferating mammalian cells and highly active contracting muscles, but whether there is a common origin for its presence in these widely different systems is unknown. To study this issue, here we develop a model of human central metabolism that incorporates a solvent capacity constraint of metabolic enzymes and mitochondria, accounting for their occupied volume densities, while assuming glucose and/or fatty acid utilization. The model demonstrates that activation of aerobic glycolysis is favored above a threshold metabolic rate in both rapidly proliferating cells and heavily contracting muscles, because it provides higher ATP yield per volume density than mitochondrial oxidative phosphorylation. In the case of muscle physiology, the model also predicts that before the lactate switch, fatty acid oxidation increases, reaches a maximum, and then decreases to zero with concomitant increase in glucose utilization, in agreement with the empirical evidence. These results are further corroborated by a larger scale model, including biosynthesis of major cell biomass components. The larger scale model also predicts that in proliferating cells the lactate switch is accompanied by activation of glutaminolysis, another distinctive feature of the Warburg effect. In conclusion, intracellular molecular crowding is a fundamental constraint for cell metabolism in both rapidly proliferating- and non-proliferating cells with high metabolic demand. Addition of this constraint to metabolic flux balance models can explain several observations of mammalian cell metabolism under steady state conditions.     

光镊拉曼光谱分析酿酒活性干酵母的活化与生长

应用光镊拉曼光谱新技术(LTRS)对酿酒活性干酵母复水活化与生长进行动态观察, 探索从分子光谱角度窥视胞内糖类、核酸、蛋白等生物大分子的变化过程, 及葡萄糖消耗和乙醇生成的动态过程。结果显示, 酿酒活性干酵母复水活化后, 第6小时和9小时, 即酵母对数生长中期及乙醇产生前期, 是调控酵母细胞生理变化的2个重要的时间点。核酸类物质在细胞活化后迅速增加, RNA在第6小时达到最大值; 而蛋白质和脂类物质从第6小时开始快速增加, 在第9小时达 到最大值, 而后呈下降趋势; 胞内乙醇则是在9 h开始出现, 在9