Metabolic transition step from ethanol consumption to sugar/ethanol

The metabolic pathway shift between only ethanol consumption to both sugar/ethanol consumption was measured by on-line analysis of respiratory quotient of a Saccharomyces cerevisiae. The experiments were carried out in a fed-batch culture under aerobic conditions. During the transition phase, respiratory quotient (RQ) profile shows that sugar can be metabolized through the fermentative pathway even to values of RQ lower than 1.Revisions requested; Revisions received 9 September 2004     

Effect of changes in the pH and carbon dioxide evolution rate on the measured respiratory quotient of fermentations

The total concentration of dissolved carbon dioxide in fermentation broths is one to two orders of magnitude greater than that of oxygen for pH > 6.5. The rate of change in this total concentration can be sufficiently large to produce a discrepancy between the carbon dioxide transfer rate (CTR) across the gas-liquid interface, available from gas analyses, and the carbon dioxide evolution rate (CER) of biomass in the fermentor. The CER is the variable of most interest to fermentation technologists but cannot be measured directly. The CTR is commonly used to yield the measured respiratory quotient (called here the TQ, or transfer quotient). Evaluation of the real underlying respiratory quotient (RQ), however, requiures the unmeasureable CER. Equations defining the problem are presented and are found to accurately predict the discrepancy between the TQ and the RQ in fed-batch fermentations of Escherichia coli. During the exponential growth phase, the TQ is less than the RQ. A changing pH can cause the TQ to be bigger or smaller than the RQ, while pH fluctuations associated with on-off pH controller action make the CTR and hence the TQ noisy. The RQ is estimated on-line during an E. coli fermentation and is shown to be constant during the fermentation, even though the TQ varies greatly. (c) 1992 John Wiley & Sons, Inc.     

Computer-aided on-line monitoring of physiological variables in suspended cell cultures of Perilla frutescens in a bioreactor

A computer-aided on-line real-time monitoring system for plant cell bioprocesses was established and applied to the cultivation of Perilla frutescens plant cells in a bioreactor. This system calculated several informative process variables which were useful for the identification of the physiological states of the plant cells during cultivation. Some variables, such as the respiratory quotient (RQ), pH, and specific carbon dioxide evolution rate (SCER), could be used for the identification of the growing phase of cell cultures. The results also suggest that the oxygen uptake rate (OUR) and the specific OUR (SOUR) may depend on the accumulation of anthocyanin (a secondary metabolite) in P. frutescens cell cultures.     

Biochemical and physiological characterization of the efrotomycin fermentation

Summary An efrotomycin fermentation was characterized through physical, chemical and biochemical studies. Growth of the actinomycete,Nocardia lactamdurans occurred during the first 50 h of the fermentation cycle at the expense of glucose, protein, and triglycerides. The initiation of efrotomycin biosynthesis was observed when glucose dropped to a low concentration. Upon glucose depletion, cell growth ceased and a switch in the respiratory quotient occurred. Efrotomycin biosynthesis was supported by the utilization of soybean oil and starch. Analysis of triglyceride metabolism showed that no diglycerides or monoglycerides accumulated during the fermentation. The activity of extracellular enzymes (lipase, protease, and amylase) increase during the cell growth phase and decreased significantly after 150 h. The concentrations of DNA, tetrahydro-vitamin K₂ (a membrane component), and free amino acids in the supernatant increased dramatically late in the fermentation cycle (225 h), indicating massive cell lysis. During this same time period, a reduction in cellular respiratory activity and efrotomycin biosynthesis were observed.     

Metabolic transition step from ethanol consumption to sugar/ethanol

The metabolic pathway shift between only ethanol consumption to both sugar/ethanol consumption was measured by on-line analysis of respiratory quotient of a Saccharomyces cerevisiae. The experiments were carried out in a fed-batch culture under aerobic conditions. During the transition phase, respiratory quotient (RQ) profile shows that sugar can be metabolized through the fermentative pathway even to values of RQ lower than 1.     

On-line estimation of viable biomass of a microaerobic culture using exit gas analysis

Summary A method is proposed to estimate the concentration of metabolically active cells of a microaerobic culture on-line from the measurement of oxygen uptake rate (OUR) and respiratory quotient (RQ). With the cultivation ofEnterobacter aerogenes in a fedbatch mode the estimated active cell concentration agrees well with the viable cell concentration determined by microscopic count and agar plate incubation.     

Glucose metabolism in the yeast Schwanniomyces castellii: role of phosphorylation site I and an alternative respiratory pathway.

Glucose metabolism in a Crabtree-negative yeast, Schwanniomyces castellii, and a cytochrome b-deficient mutant of this strain was investigated in chemostat culture. The wild-type and mutant strains exhibited the same behavior. Oxidative metabolism was observed when the substrate uptake rate (qS) was low. Fermentative metabolites were excreted when the qS value was higher than 0.40 g.g-1.h-1, indicating the occurrence of a respirofermentative metabolism; however, the respiratory quotient (RQ) remained near 1. When fermentation occurred, the cytochrome pathway was repressed but not the salicylhydroxamic acid (SHAM)-sensitive pathway. The presence of an alternative SHAM-sensitive respiratory pathway and the presence of phosphorylation site I in all metabolic conditions explained the RQ value of 1 and accounted for high biomass yields in oxidative metabolism conditions (0.62 g.g-1 for the wild-type strain and 0.31 g.g-1 for the cytochrome b-deficient mutant strain).     

Model identification and physiological control of xylitol production using Debaryomyces hansenii

The control of xylitol production from xylose-grown Debaryomyces hansenii yeast, which is a very complex biological process, usually requires accurate and demanding analytical HPLC measurements. For this reason, estimating relationships of the main variables of the fermentation process-concentration of xylitol, biomass and xylose-are suggested and studied in this article. The volume of added base for maintaining pH at the prescribed level has been shown to be important for approximate assessment of the biomass concentration and, therefore, for all estimation relationships. Furthermore, replacement of expensive off-line HPLC analyses of xylose by an on-line determined respiratory quotient RQ for control purposes is discussed. On the basis of this, physiological control of xylitol production which takes advantage of on-line classification of the different metabolic states of the culture from easily and cheaply measured variables, has been developed. Data and knowledge obtained from several experiments were evaluated for this reason and results are presented.     

Sucrose utilization and mineral nutrient uptake during hairy root growth of red beet (Beta vulgaris L.) in liquid culture

Information concerning the sugar status of plant cells is of greatimportance during all stages of the plant life cycle. The aim of this work wasto study primary carbohydrate metabolism in hairy roots of red beet. Growth ofhairy roots of red beet in vitro and changes in concentration of major nutrientsand sugar in the media were measured over a growth cycle of 16 days. We havealso determined the levels of key enzymes in the pathways of sucrose metabolism.Sucrose concentration decreased as hairy root growth proceeded while no changein glucose and fructose levels in the medium was found during the first 3 daysindicating that external sucrose is preferably taken to the cell before it ishydrolyzed by extracellular invertase. The increase in glucose and fructoselevels in the media after 5 days of culture indicates extracellular hydrolysisof sucrose which was further supported by the activity of acid invertaseobserved during that time in the culture medium. The uptake of mineral nutrientsby hairy root of red beet was monitored continuously during the culture cycle.The preferential use of NH₄ ⁺ overNO₃ ^– at the beginning of the culture andacidification of culture media were the two most notable results concerningnitrogen nutrition during hairy root growth of red beet.     

Regulatory aspects of bakers' yeast metabolism in aerobic fed-batch cultures

A highly instrumented computer-coupled bioreactor is used to investigate metabolic changes of Saccharomyces cerevisiae in aerobic fed-batch systems which are generally applied in bankers' yeast manufacture. The four types of metabolism (oxidation of glucose, aerobic fermentation, oxidation of glucose and ethanol, and oxidation of ethanol) appearing in such systems are characterized by four significant fermentation parameters: Respiratory quotient (RQ), glucose uptake rate (Q_g), ethanol turnover rate (Q_EtOH), and growth yield on glucose (Y_g). Below the critical glucose concentration glucose and ethanol are utilized simultaneously. The shift from aerobic fermentation to nondiauxic growth on glucose and ethanol is not only dependent on glucose concentration. but also on the precultivation on cells. The uptake of ethanol is controlled by the glucose supply except in the case when ethanol is limiting; the oxygen uptake rate (Q_o2), however, is unaffected by the ratio of Q_g and Q_EtOH. Critical glucose concentration is not a constant value for a particular strain, but varies corresponding to the nutritional state of the cells.     

Studies on on-line bioreactor identification. IV. Utilization of pH measurements for product estimation

Relationships between the total rate of biomass growth and the rate of ammonia addition to a fermentor for pH control are presented. These equations make use of the concept of reaction invariants and provide the additional information needed for bioreactor identification. They are especially useful when the RQ measurement is not sufficient for this purpose, such as when sensitivities arise with the measured values of the respiratory quotient or when fermentation products are formed. The cases of batch, fed-batch and continuous fermentations, forming products with or without acidic/basic properties are considered. The derived relationships were successfully tested with nonbiological acid-base continuous flow reaction systems and subsequently applied to the identification of the continuous yeast fermentation of glucose to ethanol. Results of these experimental studies are also presented.     

Selective production of bikaverin in a fluidized bioreactor with immobilized Gibberella fujikuroi

The best culture medium composition for the production of bikaverin by Gibberella fujikuroi in shake-flasks, i.e. 100 g glucose l^–1; 1 g NH₄Cl l^–1; 2 g rice flour l^–1; 5 g KH₂PO₄ l^–1 and 2.5 g MgSO₄ l^–1, was obtained through a fractional factorial design and then scaled-up to a fluidized bioreactor. The effects of carbon and nitrogen concentrations, inoculum size, aeration, flow rate and bead sizes on batch bikaverin production using immobilized G. fujikuroi in a fluidized bioreactor were determined by an orthogonal experimental design. Concentrations of up to 6.83 g bikaverin l^–1 were obtained when the medium contained 100 g glucose l^–1 and 1 g NH₄Cl l^–1 with an inoculum ratio of 10% v/v, an aeration rate of 3 volumes of air per volume of medium min^–1, and a bead size of 3 mm. Based on dry weight, the bikaverin production was 30–100 times larger than found in submerged culture and approximately three times larger than reported for solid substrate fermentation.     

On-line growth measurements in bioreactors by titrating metabolic proton exchange

Recording the amount of titrant required to maintain constant pH in a bioreactor where cell metabolism causes acidity changes allows on-line determinations of growth kinetics in computer-controlled batch cultures. A system for making such measurements is described and its performance is investigated. Transient bicarbonate accumulation occurs if the culture produces CO₂ at high pH values and low gas transfer rates. We have developed a mathematical model for the titrant requirement as a function of the cell growth rate, the gas transfer properties of the bioreactor and the culture pH. According to this model, bicarbonate accumulation affects the stoichiometry between titrant and biomass but does not prevent determination of growth rate constants. These predictions are confirmed using model experiments and measurements during batch growth of microbial cultures.     

Optimization of pro-urokinase secretion from recombinant Saccharomyces cerevisiae

Secretion of a nonglycosylated form of human pro-urokinase, also known as single-chain urinary plasminogen activator (scu-PA), from Saccharomyces cerevisiae is described. A "supersecreting" yeast strain harboring multiple copies of integrated plasmids was grown batchwise and at constant respiratory quotient (RQ) in 20-L fermenters. Because the promoters used to drive expression of the pro-urokinase genes are not tightly regulated, secretion into the culture supernatant was growth associated. Although the final cell density achieved in the perturbed-batch fermentation (45 g dry wt/L) was less than that observed in the RQ-controlled culture (77 g dry wt/L), the scu-PA titer in the perturbed-batch fermentation (1863 IU/mL) was nearly twice that attained at constant RQ (1108 IU/mL). The effects on cell growth and scu-PA titer of other process variables (pH, temperature, phosphate concentration, and medium composition) are also discussed.     

Some comments on respiratory quotient (RQ) determination from the analysis of exit gas from a fermentor

Recently, the respiratory quotient (RQ) of microbes measured in situ in a fermentor by exit-gas analysis has been used successfully, for instance, in a fed-batch culture of baker's yeast as a criterion to control the feeding rate.(1-3) It is significant here to keep RQ values close to unity throughout; any deviations of RQ from unity give rise to deterioration of the cell growth yield.However easy it might be to keep RQ values around unity by controlling the feeding rate, the question of whether or not RQ values determined by gas analysis at the fermentor exit could generally represent those in vivo deserves attention. Indeed, for a fermentation carried out at an alkaline side, gas analysis would give RQ values that differ remarkably from true values because of the medium's "storage" of CO(2) released from microbes. The purpose of this communication is to make clear those factors that would affect true RQ values in the analysis of exit gas from a fermentor.     

以葡萄糖为生长相基质的重组毕赤酵母表达植酸酶发酵

甲醇营养型毕赤酵母表达外源蛋白是在醇氧化酶（alcohol oxidase,AOX）启动子（PAOXI）严格调控下进行的,然而这种启动子在转录水平受到葡萄糖的阻遏。本文研究了毕赤酵母在葡萄糖替代甘油为生长相碳源时表达重组植酸酶蛋白的发酵特征。结果表明：初始葡萄糖浓度为20dL的细胞得率高,为0．39g[DCW]／g。通过基于实时参数（溶氧和呼吸商）调控的葡萄糖补料策略,生长相40h后细胞密度达到100g[DCW]／L,甲醇诱导100h后植酸酶产量达到2200FTUphytase／mL,甲醇得率系数为0．25FTU phytase／gmethnol。因此,在毕赤酵母高表达重组蛋白培养中葡萄糖能够用作生长相基质,并能实现重组蛋白的高效表达。     

Non-invasive methods for determination of cellular growth inPodophyllum hexandrum suspension cultures

Culture conductivity and on-line NADH fluorescence were used to measure cellular growth in plant cell suspension cultures ofPodophyllum hexandrum. An inverse correlation between dry cell weight and medium conductivity was observed during shake flask cultivation. A linear relationship between dry cell weight and culture NADH fluorescence was obtained during the exponential phase of batch cultivation in a bioreactor under the pH stat (pH 6) conditions. It was observed that conductivity measurement were suitable for biomass characterisation under highly dynamic uncontrolled shake flask cultivation conditions. However, if the acid/alkali feeding is done for pH control the conductivity measurement could not be applied. On the other hand the NADH fluorescence measurement allowed online-in situ biomass monitoring of rather heterogenous plant cell suspension cultures in bioreactor even under the most desirable pH stat conditions.     

Relationships of respiratory quotient to microbial biomass and hydrocarbon contaminant degradation during soil bioremediation

This work focused on monitoring respiratory quotient, RQ (defined as a ratio of CO₂ production to O₂ uptake rates), microbial growth and residual hydrocarbon concentration during bioremediation experiments performed on laboratory soil microcosms. The aim of the study was to determine if the time course biodegradation profile of the contaminant can be related to the RQ evolution and to investigate the effect of the water content on RQ measurements. A natural soil was artificially contaminated with hexadecane and adjusted with inorganic nutrients to stimulate biodegradation. Microbial growth, CO₂ production, O₂ uptake and residual hexadecane were periodically monitored at different soil water contents ranging from 0.15 to 0.35 g water g⁻¹ of dry soil. Results showed that microbial activity and contaminant degradation were strongly dependent on soil water content. Maximal growth and hexadecane depletion were obtained at a water content of 0.20 g water g⁻¹ of dry soil, which corresponded to 46.6% of the water holding capacity. Hexadecane degradation was considerably reduced with increasing soil water content. RQ values fluctuated as a function of the hexadecane biodegradation phases. The lowest RQs corresponded to the highest hexadecane depletion and microbial growth. The water content variation did not significantly affect the shape of the RQ evolution curves as a function of time. It only modified the magnitude of RQ values. This study indicates that additional biological and chemical analyses are needed to support RQ data when monitoring contaminant degradation to have an accurate understanding of all the biotic processes, which may occur simultaneously.     

Production of 2-Ketogluconic Acid by Serratia marcescens

Production of 2-ketogluconic acid from glucose by fermentation with Serratia marcescens NRRL B-486 was studied in 20-liter stainless-steel fermentors. Conditions for 2-ketogluconic acid production included the following: glucose-salt medium, aeration rate of 0.75 volumes per volume per minute, agitation rate of 400 rev/min, temperature of 30 C, CaCO₃ to neutralize the acid formed, and a 5% (v/v) inoculum. Foaming was controlled with an antifoam agent added at intervals during the fermentation. When 120 g per liter of glucose were supplied, 95 to 100% yields of 2-ketogluconic acid were obtained in 16 hr. Larger amounts of glucose could be used in the fermentation provided that the carbohydrate was fed continuously. Continuous feeding of glucose to a total amount of 180 g per liter gave 95 to 100% yields of 2-ketogluconic acid in 24 hr; feeding glucose to a total amount of 240 g per liter gave 85 to 90% yields in 32 to 40 hr.     

Constitutive expression of human angiostatin in <Emphasis Type="Italic">Pichia pastoris</Emphasis> by high-density cell culture

A high-density cell culture method to produce human angiostatin has been successfully established by constitutive expression of the protein in Pichia pastoris. The fermentation was carried out in a 20 l bioreactor with a 10 l working volume, using a high-density cell culture method by continuously feeding with 50% glycerol−0.8% PTM4 to the growing culture for 60 h at 30°C. Dissolved oxygen level was maintained at 25–30% and pH was controlled at 5 by the addition of 7 M NH₄OH. Angiostatin was constitutively expressed during the fermentation by linking its expression to the P. pastoris constitutive GAP promoter (pGAP). But after 36 h of fermentation, the peak biomass growth was 305 as measured by absorption of 600 nm, while the peak angiostatin expression was 176 mg/l. Similar to the product expressed from inducible system [24], angiostatin produced from constitutive system also inhibited the angiogenesis on the CAM and suppressed the growth of B16 melanoma in C57BL/6J mouse. The above results suggest that GAP promoter is more efficient than AOX1 promoter for the expression of angiostatin in P. pastoris by shake flask culture or high-density cell fermentation and is likely to be an alternative to AOX1 promoter in large-scale expression of angiostatin and other heterologous proteins. Supported by the Natural Science Foundation of China (39670013) and “225” Science and Technology Program of Guangzhou Municipal Government of China (99-Z-004-001).