A pH-controlled fed-batch process can overcome inhibition by formate in NADH-dependent enzymatic reductions using formate dehydrogenase-catalyzed coenzyme regeneration

The NAD-dependent, formate dehydrogenase-catalyzed oxidation of formate anion into CO2 is known as the method for the regeneration of NADH in reductive enzymatic syntheses. Inhibition by formate and inactivation by alkaline pH-shift that occurs when oxidation of formate is carried out at pH approximately 7.0 may, however, hamper the efficient application of this NADH recycling reaction. Here, we have devised a fed-batch process using pH-controlled feeding of formic acid that can overcome enzyme inhibition and inactivation. The reaction pH is thus kept constant by addition of acid, and formate dehydrogenase is supplied continuously with substrate as required, but the concentration of formate is maintained at a constant, non- or weakly inhibitory level throughout the enzymatic conversion, thus enabling a particular NADH-dependent dehydrogenase to operate stably and at high reaction rates. For xylitol production from xylose using yeast xylose reductase (Ki,Formate 182 mM), a fed-batch conversion of 0.5M xylose yielded productivities of 2.8 g (L h)-1 that are three-fold improved when contrasted to a conventional batch reaction that employed equal initial concentrations of xylose and formate.     

Absence of diauxie during simultaneous utilization of glucose and Xylose by Sulfolobus acidocaldarius

Sulfolobus acidocaldarius utilizes glucose and xylose as sole carbon sources, but its ability to metabolize these sugars simultaneously is not known. We report the absence of diauxie during growth of S. acidocaldarius on glucose and xylose as co-carbon sources. The presence of glucose did not repress xylose utilization. The organism utilized a mixture of 1 g/liter of each sugar simultaneously with a specific growth rate of 0.079 h(-1) and showed no preference for the order in which it utilized each sugar. The organism grew faster on 2 g/liter xylose (0.074 h(-1)) as the sole carbon source than on an equal amount of glucose (0.022 h(-1)). When grown on a mixture of the two carbon sources, the growth rate of the organism increased from 0.052 h(-1) to 0.085 h(-1) as the ratio of xylose to glucose increased from 0.25 to 4. S. acidocaldarius appeared to utilize a mixture of glucose and xylose at a rate roughly proportional to their concentrations in the medium, resulting in complete utilization of both sugars at about the same time. Gene expression in cells grown on xylose alone was very similar to that in cells grown on a mixture of xylose and glucose and substantially different from that in cells grown on glucose alone. The mechanism by which the organism utilized a mixture of sugars has yet to be elucidated.     

A simple and novel method for radiometric analysis of glucose utilization by adrenal chromaffin cells

Glucose utilization by cells and tissues can be followed by measuring the release of [³H]H₂O from added -[5-³H]glucose, and we have developed a method whereby the whole reaction and assay can be performed in a single scintillation vial. The basic principle behind our new assay is that the released tritiated hydrogen ion in water can be quantitatively exchanged with the hydroxyl proton of simple alcohols such as isoamyl alcohol. The radiolabeled alcohol can then be extracted into an organic solvent to which 2,5-diphenyloxazole and p-bis[2-(5-phenyloxazoyl)]benzene have been previously added. Using this new assay we studied isolated chromaffin cells and found them to utilize glucose at a linear rate for at least 30 min. The assay was precise and reproducible enough to allow detailed analysis of various inhibitors of glycolysis and of oxidative phosphorylation. The new method is simple and rapid, can be done in open test tubes, requires no complex equipment, and is intrinsically highly accurate.     

Online automatic tuning and control for fed-batch cultivation

Performance of controllers applied in biotechnological production is often below expectation. Online automatic tuning has the capability to improve control performance by adjusting control parameters. This work presents automatic tuning approaches for model reference specific growth rate control during fed-batch cultivation. The approaches are direct methods that use the error between observed specific growth rate and its set point; systematic perturbations of the cultivation are not necessary. Two automatic tuning methods proved to be efficient, in which the adaptation rate is based on a combination of the error, squared error and integral error. These methods are relatively simple and robust against disturbances, parameter uncertainties, and initialization errors. Application of the specific growth rate controller yields a stable system. The controller and automatic tuning methods are qualified by simulations and laboratory experiments with Bordetella pertussis.     

Accumulation of CdS nanoparticles by yeasts in a fed-batch bioprocess

The yeasts Schizosaccharomyces pombe and Candida glabrata were successfully cultivated in a fed-batch process at cadmium levels up to 100 mg l(-1). S. pombe incorporated 20 mg C dg(-1) dry biomass within 24h. C. glabrata accumulated 8 mg C dg(-1) dry biomass in 24h. The higher Cd uptake from S. pombe cells correlate with the elevated glucose concentrations during and at the end of the cultivation. Analysis of the cells with energy-filtering transmission electron microscopy-element specific imaging (EFTEM-ESI) revealed that cadmium is not precipitated outside the cells or at the cell wall but evenly distributed inside the cell plasma. As Cd is highly toxic this indicates that Cd is immobilized by an intracellular detoxification mechanism. Size exclusion chromatography showed that Cd is associated to a protein fraction between 25 and 67 kDa which corresponds to the theoretical molecular weight of CdS nanoparticles of 35 kDa coated with phytochelatins. This structure has been proposed in literature.     

皮状丝孢酵母同步利用葡萄糖/木糖的糖转运动力学简

皮状丝孢酵母（ Trichosporon cutaneum）能够同步利用葡萄糖和木糖生产油脂。以2脱氧葡萄糖（2 DOG）为底物,考察皮状丝孢酵母糖跨膜运输的转运动力学。结果表明：2 DOG转运符合米氏方程,表观米氏常数Km为0.19 mmol/L,最大转运速率Vmax为14.1 nmol/（ min＆#183;mg）。葡萄糖和木糖均竞争性抑制2 DOG转运,葡萄糖表观抑制常数Ki远低于木糖,表明存在一个共用转运体系,且该转运体系对葡萄糖亲和力更高。大量木糖与2 DOG同时转运到胞内,进一步说明木糖与葡萄糖共运输。代谢抑制剂和pH对糖转运有明显影响,说明质子/底物同向运输系统是该酵母的主要糖转运系统。     

A polarographic method for the simultaneous determination of total glucosinolates and free glucose of cruciferous material

A rapid method for the simultaneous analysis of total free glucose and total glucosinolates in aqueous extracts of cruciferous material is described. The technique, which appears suitable for plant-breeding programs as it allows the processing of more than 100 samples per day, involves the polarographic determination of O2 uptake of free glucose by a system of double-coupled enzymes, such as myrosinase-glucose oxidase. The method has advantages over current methods, because it is very rapid (4 min per analysis), allows two determinations for each analysis, and appears to be very reproducible, accurate, and sensitive.     

The utilization of aromatic compounds by yeasts

Yeasts belonging to 6 genera were isolated from sewage and tested for their ability to use 15 hydroxy derivatives of phenol and benzoic acid as carbon source. The majority were able to produce colonies on at least 10 of the simple monophenol derivatives tested. Salicylic acid,p-hydroxybenzoic acid and gentisic acid were the most commonly used benzoic acid derivatives and resorcinol and phloroglucinol the most frequently metabolized phenols. However, there was no obvious relationship between the utilization of these compounds and the generic classification of the yeasts.Summer student, 1967. Graduate Student, Department of Microbiology, University of Alberta, Edmonton, Alberta, Canada.The authors wish to acknowledge the capable assistance of Mrs. C. Knapp and Mr. N. R. Gardner.     

Sequential utilization of mixed monosaccharides by yeasts

Four yeasts (Saccharomyces cerevisiae, Schizosaccharomyces pombe, Candida utilus, and Rhodotorula toruloides) were tested for their ability to grow and consume D-glucose, D-xylose, D-xylulose, and D-xylitol. Sequential utilization of substrates was observed when D-glucose as mixed with D-xylulose as the carbon source. Catabolite inhibition was tentatively concluded to be responsible for this regulatory mechanism. D-Glucose was also found to inhibit the utilization of D-xylose and D-xylitol in C. utilus and R. toruloides. D-Xylose, D-xylitol, and D-xylulose were consumed simultaneously by R. toruloides and C. utilus.     

Improvement of Y-values of Hansenula polymorpha growth on methanol by simultaneous utilization of glucose

The simultaneous utilization of methanol and glucose by Hansenula polymorpha MH20 was investigated in chemostat (C-limited) cultivation. The mixed-substrate utilization results in biomass yields which are greater up to 20 to 25% as expected assuming an additive growth on both substrates. This is referred to as an auxiliary-substrate effect. Additionally, methanol can be utilized at higher growth rates in the presence of glucose compared to those obtained on this substrate alone. The extend of the auxiliary-substrate effect and the optimum ratio of substrates to reach this effect depend on dilution rate. The greatest stimulation in yield is obtained at D approximately 0.1 h-1, after raising the dilution rate this effect diminishes. At a rate of 0.1 h-1 the optimum mixed-substrate ratio of methanol: glucose is 7:1 (g). By increasing the growth rate the ratio changes toward glucose and reached a value of 1:1 (g) at D = 0.3 h-1. This change in the optimum ratio correlates with diminution in yield coefficient of methanol accompanying an increase in growth rate greater than 0.15 h-1. Energy balances of the utilization of the single substrates are used for interpretation of these results. From this it is evident that methanol does not play the role of an energy-rich substrate in the metabolism of yeast. Rather glucose is the energy-providing substrate in this combination.     

A simplified routine method for determining carbohydrate fermentation by yeasts

The use of commercially available materials in a minimal medium contributes to the simplicity, reliability, and reproducibility of a method described to demonstrate carbohydrate fermentation reactions by yeasts. The medium consists of 1% yeast extract and 2% test carbohydrate in distilled water, dispensed in a modified Durham fermentation tube. Carbohydrate fermentation patterns can usually be obtained within a period of 7 days. The ability of yeasts to ferment carbohydrates is determined strictly on the basis of gas production from the substrate. The method proved reliable in reproducing established fermentation patterns for 112 different yeast strains representing 13 separate genera.

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Zusammenfassung Der Gebrauch von handelsüblichen Grundbestandteilen in einem geringen Medium trägt zu der Einfachheit, Zuverlässigkeit und Reproduzierbarkeit der beschriebenen Methode, um die Gärungsreaktionen der Karbohydrate durch Hefen zu veranschaulichen, bei. Das Medium besteht aus einem 1 prozent. Hefenauszug und aus einem 2 prozentigen Testkarbohydrat in destilliertem Wasser, die auf modifiziertes Durham Gärungsreagensglas verteilt sind. Das Karbohydrat-Gärungsmodell kann gewöhnlich innerhalb einer Periode von sieben Tagen erhalten werden. Die Fähigkeit von Hefen, Karbohydrate zu vergären, ist ausschließlich auf Grund der Gasentwicklung aus den Produkten bestimmt. Die Methode erwies sich zuverlässig in der Erzeugung festgestellter Gärungsmodelle aus 112 Hefen, die 13 verschiedene Gattungen darstellten.

     

On-line multi-analyzer monitoring of biomass, glucose and acetate for growth rate control of a Vibrio cholerae fed-batch cultivation

In situ near-infrared (NIR) spectroscopy and in-line electronic nose (EN) mapping were used to monitor and control a cholera-toxin producing Vibrio cholerae fed-batch cultivation carried out with a laboratory method as well as with a production method. Prediction models for biomass, glucose and acetate using NIR spectroscopy were developed based on spectral identification and partial-least squares (PLS) regression resulting in high correlation to reference data (standard errors of prediction for biomass, glucose and acetate were 0.20 gl(-1), 0.26 gl(-1) and 0.28 gl(-1)). A compensation algorithm for aerated bioreactor disturbances was integrated in the model computation, which in particular improved the prediction by the biomass model. First, the NIR data were applied together with EN in-line data selected by principal component analysis (PCA) for generating a trajectory representation of the fed-batch cultivation. A correlation between the culture progression and EN signals was demonstrated, which proved to be beneficial in monitoring the culture quality. It was shown that a deviation from a normal cultivation behavior could easily be recognized and that the trajectory was able to alarm a bacterial contamination. Second, the NIR data indicated the potential of predicting the concentration of formed cholera toxin with a model prediction error of 0.020 gl(-1). Third, the on-line biomass prediction based on the NIR model was used to control the overflow metabolism acetate formation of the V. cholerae culture. The controller compared actual specific growth rate as estimated from the prediction with the critical acetate formation growth rate, and from that difference adjusted the glucose feed rate.     

Kalman filter based glucose control at small set points during fed-batch cultivation of Saccharomyces cerevisiae

A glucose control system is presented, which is able to control cultivations of Saccharomyces cerevisiae even at low glucose concentrations. Glucose concentrations are determined using a special flow injection analysis (FIA) system, which does not require a sampling module. An extended Kalman filter is employed for smoothing the glucose measurements as well as for the prediction of glucose and biomass concentration, the maximum specific growth rate, and the volume of the culture broth. The predicted values are utilized for feedforward/feedback control of the glucose concentration at set points of 0.08 and 0.05 g/L. The controller established well-defined conditions over several hours up to biomass concentrations of 13.5 and 20.7 g/L, respectively. The specific glucose uptake rates at both set points were 1.04 and 0.68 g/g/h, respectively. It is demonstrated that during fed-batch cultivation an overall pure oxidative metabolism of glucose is maintained at the lower set point and a specific ethanol production rate of 0.18 g/g/h at the higher set point.     

Sequential utilization of mixed monosaccharides by yeasts.

Four yeasts (Saccharomyces cerevisiae, Schizosaccharomyces pombe, Candida utilus, and Rhodotorula toruloides) were tested for their ability to grow and consume D-glucose, D-xylose, D-xylulose, and D-xylitol. Sequential utilization of substrates was observed when D-glucose as mixed with D-xylulose as the carbon source. Catabolite inhibition was tentatively concluded to be responsible for this regulatory mechanism. D-Glucose was also found to inhibit the utilization of D-xylose and D-xylitol in C. utilus and R. toruloides. D-Xylose, D-xylitol, and D-xylulose were consumed simultaneously by R. toruloides and C. utilus.     

The control of glucose concentration during yeast fed-batch cultivation using a fast measurement complemented by an extended Kalman filter

In this contribution results are presented from the control of glucose during a yeast fed-batch cultivation. For glucose measurements a special flow injection analysis (FIA) system was employed, which uses a glucose oxidase solution instead of immobilized enzymes. To avoid the large delay time caused by probing systems samples containing cells, i.e., samples containing the ordinary culture broth, are injected into the FIA system. Based on a special evaluation method the glucose concentration can be measured with a delay time of about 60 s. Employing an extended Kalman filter, the biomass, the glucose concentration as well as the w_max (Monod model) are estimated. Based on the estimation a feed forward and a PI-control with a set point of 0.5 g/l was carried out. The mean deviation of the set point and the estimated value as well as the set point and the measured value were 0.05 and 0.11 g/l respectively for a control period of 8 h producing a cell dry mass of more than 6 g/l.