Effect of reducing agents in an aerobic amino acid fermentation

This study focuses on the effects of the reducing agents, dithiothreitol (DTT) and glutathione (GSH), on amino acid production in aerobically growing Corynebacterium glutamicum. The problem of reducing agent addition affecting the dissolved oxygen level was solved by positioning the culture at a high dissolved oxygen level and feeding the reducing agent into the fermentor. We show that it is possible to lower the redox potential even in a highly aerobic environment. The addition of DTT to the fermentation during the growth phase caused a significant increase in specific amino acid production rate and total amino acids produced, as compared with a control. In contrast, GSH had an inhibitory effect. (c) 1992 John Wiley & Sons, Inc.     

The use of culture redox potential and oxygen uptake rate for assessing glucose and glutamine depletion in hybridoma cultures

Culture redox potential (CRP) and oxygen uptake rate (OUR) were monitored on-line during glucose- and glutamine-limited batch cultures of a murine hybridoma cell line that secretes a neutralizing monoclonal antibody specific to toxin 2 of the scorpion Centruroides noxius Hoffmann. It was found that OUR and CRP can be used for assessing the viable cell concentration and growth phases of the culture. Before nutrient depletion, OUR increased exponentially with viable cell concentration, whereas CRP decreased monotonically until cell viability started to decrease. During the death phase, CRP gradually increased. A sudden decrease in OUR occurred upon glucose or glutamine depletion. CRP traced the dissolved oxygen profile during a control action or an operational eventuality, however, during nutrient depletion it did not follow the expected behavior of a system composed mainly by the O(2)/H(2)O redox couple. Such a behavior was not due to the accumulated lactate or ammonia, nor to possible intracellular redox potential changes caused by nutrient depletion, as inferred from respiration inhibition by rotenone or uncoupled respiration by 2,4-dinitrophenol. As shown in this study, operational eventualities can be erroneously interpreted as changes in OUR when using algorithms based solely on oxygen balances. However, simultaneous measurements of CRP and OUR may be used to discriminate real metabolic events from operational failures. The results presented here can be used in advanced real-time algorithms for controling glucose and glutamine at low concentrations, avoiding under- or over-feeding them in hybridoma cultures, and consequently reducing the accumulation of metabolic wastes and improving monoclonal antibody production. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 555-563, 1997.     

Intensification of β-poly(l-malic acid) production by Aureobasidium pullulans ipe-1 in the late exponential growth phase

β-Poly(malic acid) (PMLA) has attracted industrial interest because this polyester can be used as a prodrug or for drug delivery systems. In PMLA production by Aureobasidium pullulans ipe-1, it was found that PLMA production was associated with cell growth in the early exponential growth phase and dissociated from cell growth in the late exponential growth phase. To enhance PMLA production in the late phase, different fermentation modes and strategies for controlling culture redox potential (CRP) were studied. The results showed that high concentrations of produced PMLA (above 40 g/l) not only inhibited PMLA production, but also was detrimental to cell growth. Moreover, when CRP increased from 57 to 100 mV in the late exponential growth phase, the lack of reducing power in the broth also decreased PMLA productivity. PMLA productivity could be enhanced by repeated-batch culture to maintain cell growth in the exponential growth phase, or by cell-recycle culture with membrane to remove the produced PMLA, or by maintaining CRP below 70 mV no matter which kind of fermentation mode was adopted. Repeated-batch culture afforded a high PMLA concentration (up to 63.2 g/l) with a productivity of 1.15 g l(-1) h(-1). Cell-recycle culture also confirmed that PMLA production by the strain ipe-1 was associated with cell growth.     

Effect of redox potential regulation on succinic acid production by Actinobacillus succinogenes

The effects of redox potential used as a control parameter on the process of succinic acid production in batch cultures of Actinobacillus succinogenes NJ113 have been investigated. In batch fermentation, cell growth and metabolite distribution were changed with redox potential levels in the range of ?100 to ?450 mV. From the results, the ORP level of ?350 mV was preferable, which resulted in high succinic acid yield (1.28 mol mol^?1), high succinic acid productivity (1.18 g L^?1 h^?1) and high mole ratio of succinic acid to acetic acid (2.02). The mechanism of redox potential regulation was discussed by metabolic flux analysis and the ratio of NADH/NAD⁺. We expected that redox potential can be used as a valuable parameter to monitor and control much more anaerobic fermentation production.     

A three-phase pattern in growth, monoclonal antibody production, and metabolite exchange in a hybridoma bioreactor culture

The use of partial cubic spline data interpolation for the calculation of volumetric metabolite exchange rates suggested the existence of three distinct metabolic phases during bioreactor culture of a hybridoma cell line. During phase 1, a rapid amino acid uptake rate and ammonia release rate were observed. The growth rate was low and glutamine synthetase activity fell. In phase 2, maximum growth rate and minimum glutamine assimilation and ammonium production rates were observed. Attempts to corroborate the apparent ammonia assimilation in this phase using (15)NH(4)Cl resulted in low incorporation rates into alanine and glutamine. Maximum glutamine synthetase activity took place during this period. Maximum antibody production rate was observed during phase 3 during which peaks in glutamine assimilation, ammonia release, and glutamine synthetase activity were observed. The apparent existence of the three phases prompted us to carry out Northern blot analysis of glutamine synthetase RNA at appropriate times during the process. This revealed a pattern of appearance and dis-appearance of mRNA consistent with the three phases indicated by the fermentation parameters. (c) 1993 John Wiley & Sons, Inc.     

In vivo 15N NMR studies of regulation of nitrogen assimilation and amino acid production by Brevibacterium lactofermentum

Glutamic acid producer Brevibacterium lactofermentum intact cells were used to demonstrate the feasibility of in vivo 15N NMR to follow nitrogen assimilation and amino acid production throughout the growth cycle. The induction of glutamic acid production by different growth conditions was studied. Intracellular and extracellular levels of free metabolites were estimated as function of oxygen supply and biotin concentration. 15N NMR enabled us to distinguish two phases during the fermentation. At the early stage of fermentation, glutamic acid was accumulated intracellularly independent of oxygen supply and no product was excreted. In the late growth phase, the permeability of the cells developed and L-glutamic acid was excreted. The effect of aeration and biotin concentration on cellular contents and excretion was also studied by 15N NMR. Glutamate, N-acetylglutamine, and glutamine were the main nitrogenous pools independent of cell culture conditions. Free ammonia was not accumulated intracellularly although glutamic acid fermentation can be characterized as the process of nitrogen assimilation and the uptake of ammonia is the key step. In conclusion, the application of in vivo 15N NMR spectroscopy unraveled various problems of nitrogen metabolism, in a rapid and nondestructive manner.     

On-line assessment of metabolic activities based on culture redox potential and dissolved oxygen profiles during aerobic fermentation.

We report here on the utility of on-line culture redox potential and dissolved oxygen measurements to identify metabolic changes in fermentation by Corynebacterium glutamicum under aerobic conditions. Metabolic changes were identified by observing discrepancies in the profile of culture redox potential and dissolved oxygen. On the basis of these measurements, we can identify the end of the lag phase, threonine exhaustion, and glucose exhaustion during fermentation.     

Stimulation of the rate of l-lactate fermentation using Lactococcus lactis IO-1 by periodic electrodialysis

Lactic acid fermentation in glucose medium with periodic electrodialysis by Lactococcus lactis IO-1 was examined. The fermentation time was reduced considerably, compared with the time required for ordinary built-in electrodialysis fermentation with a microfilter module (ED-MF). Fermentation with an initial glucose concentration of 80 g/l was completed within 18 h, about 50% of the time required with an ED-MF. The maximum productivity of this novel system was about two-fold that of the ordinary ED-MF system even when the lactate concentration in broth was higher than in the ED-MF. The H₂ gas produced from the ED-MF made the culture redox potential (CRP) lower than in the novel system. Online culture redox potential was monitored and higher CRP indicated a higher fermentation rate.     

Fermentative ability of Zymomonas mobilis under various oxygen supply conditions in batch culture

The performance of Zymomonas mobilis under various oxygen supply conditions in batch culture was quantitatively investigated. Although both the cell growth rate and ethanol productivity decreased with increases in the oxygen supply, the production of by-products such as acetaldehyde and acetic acid increased. The ethanol productivity was more sensitive to oxygen supply than the growth rate. Oxygen supply also affected the morphology of the cells and an increase in oxygen supply resulted in the elongation of the cells. It was also found that both metabolic activity and fermentation balance were largely affected by changes in the dissolved oxygen concentration during the steady state in oxygen concentration.     

L-丙氨酸厌氧发酵关键技术及产业化

传统氨基酸制造主要是通过化学合成或好氧发酵实现。相对于化学合成,微生物发酵可以实现以可再生资源为原料直接生产氨基酸,减少了对石油基原料的依赖,解决了化学合成高污染、高能耗等问题。好氧发酵具有生长快、产量高等特点,但好氧发酵中大量碳源用于细胞生长容易造成糖酸转化率低、能耗高等问题。厌氧发酵是近年来新出现的氨基酸生产模式,具有操作简单、无需通氧、糖酸转化率高容易接近理论最大值等优势。L-丙氨酸是国际上首个实现厌氧发酵产业化生产的氨基酸。本文以L-丙氨酸为例,综述了氨基酸厌氧发酵过程中的关键问题及其在产业化实施中的应用。未来,随着厌氧发酵关键技术在更多化合物生物制造技术中的突破,这种低成本、高效、低碳环保型发酵方式将会带来更大的经济价值和社会效益。     

Effects of dissolved oxygen on hybridoma cell growth, metabolism, and antibody production kinetics in continuous culture.

The effects of dissolved oxygen concentration (DO) on hybridoma cell physiology were examined in a continuous stirred tank bioreactor with a murine hybridoma cell line (167.4G5.3). Dissolved oxygen concentration was varied between 0% and 100% air saturation. Cell growth and viability, carbohydrate, amino acid, and energy metabolism, oxygen uptake, and antibody production rates were investigated. Cell growth was inhibited at both high and low DO. Cells could grow at 0% DO and maintain viability under a nitrogen atmosphere. Cell viability was higher at low DO. Glucose, glutamine, and oxygen consumption rates changed little at DO above 1% air saturation. However, the metabolic uptake rates changed below 1% DO, where growth became oxygen limited, and a Km value of 0.6% DO was obtained for the specific oxygen uptake rate. The metabolic rates of glucose, glutamine, lactate, and ammonia increased 2-3-fold as the DO dropped from 1% to 0%. Amino acid metabolism followed the same general pattern as that of glutamine and glucose. Alanine was the only amino acid produced. The consumption rates of amino acids changed little above 1% DO, but under anaerobic conditions the consumption rates of all amino acids increased severalfold. Cells obtained most of their metabolic energy from glutamine oxidation except under oxygen limitation, when glucose provided most of the energy. The calculated ATP production rate was only slightly influenced by DO and rose at 0% DO. Antibody concentration was highest at 35% DO, while the specific antibody production rate was insensitive to DO.     

胞内氧化还原水平对嗜热厌氧乙醇菌 发酵代谢的影响

辅酶NADH/NAD+在细胞内氧化还原反应中起着重要的作用,是细胞生长和能量代谢必不可少的辅因子。调节微生物胞内NADH/NAD+的比率是定向改变微生物代谢,高效获得目标代谢产物的有效手段。嗜热厌氧乙醇菌(Thermoanaerobacter ethanolicus)是高温厌氧菌中乙醇产量较高的代表性菌株,本文利用不同氧化还原态的碳源改变T.ethanolicus的胞内NADH/NAD+含量和比例,进而研究了其对细胞生长、代谢产物分布的影响。以不同比例的葡萄糖/甘露醇作为混合碳源发酵,胞内氧化还原水平、细胞的生长特性、代谢产物都发生了不同程度的差异,以葡萄糖作为唯一碳源进行培养时,T.ethanolicus生长良好,乙醇产量为0.79g/L,但胞内NADH/NAD+比值和乙醇/乙酸的比值都比较低,分别为0.47和4.82;随着葡萄糖在混合碳源中比例的下降,NADH/NAD+比值增高,发酵产物中乙醇/乙酸比值也呈现上升的趋势。而以甘露醇作为唯一碳源时,发酵产物中乙醇浓度为0.389g/L,NADH/NAD+比值和乙醇/乙酸的比值分别为1.04和16.0。     

Inhibition of fermentation and growth in batch cultures of the yeast Brettanomyces intermedius upon a shift from aerobic to anaerobic conditions (Custers effect)

Aerobic growth of the yeast Brettanomyces intermedius CBS 1943 in batch culture on a medium containing glucose and yeast extract proceeded via a characteristic pattern. In the first phase of growth glucose was fermented to nearly equal amounts of ethanol and acetic acid. After glucose depletion, growth continued while the ethanol produced in the first phase was almost quantitatively converted to acetic acid. Finally, after a long lag phase, growth resumed with concomitant consumption of acetic acid.When the culture was made anaerobic during the first phase, growth, glucose consumption and metabolite production stopped immediately. This Custers effect (inhibition of alcoholic fermentation as a result of anaerobic conditions) was transient. After 7–8 h the culture was adapted to anaerobiosis, and growth and ethanol production resumed. The lag phase could be shortened at will by the introduction of hydrogen acceptors, such as oxygen or acetoin, into the culture. Glycerol production was not observed during any phase of growth. These results support the hypothesis that the Custers effect in this yeast is due to a disturbance of the redox balance, resulting from the tendency of the organism to produce acetic acid, and its inability to restore the balance by production of glycerol.     

High viable cell concentration fed-batch cultures of hybridoma cells through on-line nutrient feeding

A hybridoma cell line was cultivated in fed-batch cultures using a low-protein, serum-free medium. On-line oxygen uptake rate (OUR) measurement was used to adjust the nutrient feeding rate based on glucose consumption, which was estimated on-line using the stoichiometric relations between glucose and oxygen consumption. Through on-line control of the nutrient feeding rate, not only sufficients were supplied for cell growth and antibody production, but also the concentrations of glucose and other important nutrients such as amino acids were maintained at low levels during the cell growth phase. During the cultivation, cell metabolism changed from high lactate production and low oxygen consumption to low lactate production and high oxygen consumption. As a result the accumulation of lactate was reduced and the growth phase was extended. In comparison with the batch cultures, in which cells reached a concentration of approximately 2 x 10(6) cells/mL, a very high concentration of 1.36 x 10(7) cells/mL with a high cell viability (>90%) was achieved in the fed-batch culture. By considering the consumption of glucose and amino acids, as well as the production of cell mass, metabolites, and antibodies, a well-closed material balance was established. Our results demonstrate the value of coupling on-line OUR measurement and the stoichiometric realations for dynamic nutrient feeding in high cell concentration fed batch cultures. (c) 1995 John Wiley & Sons, Inc.     

Genome-scale modeling for Bacillus coagulans to understand the metabolic characteristics

Lactic acid is widely used in many industries, especially in the production of poly-lactic acid. Bacillus coagulans is a promising lactic acid producer in industrial fermentation due to its thermophilic property. In this study, we developed the first genome-scale metabolic model (GEM) of B. coagulans iBag597, together with an enzyme-constrained model ec-iBag597. We measured strain-specific biomass composition and integrated the data into a biomass equation. Then, we validated iBag597 against experimental data generated in this study, including amino acid requirements and carbon source utilization, showing that simulations were generally consistent with the experimental results. Subsequently, we carried out chemostats to investigate the effects of specific growth rate and culture pH on metabolism of B. coagulans. Meanwhile, we used iBag597 to estimate the intracellular metabolic fluxes for those conditions. The results showed that B. coagulans was capable of generating ATP via multiple pathways, and switched among them in response to various conditions. With ec-iBag597, we estimated the protein cost and protein efficiency for each ATP-producing pathway to investigate the switches. Our models pave the way for systems biology of B. coagulans, and our findings suggest that maintaining a proper growth rate and selecting an optimal pH are beneficial for lactate fermentation.     

溶氧对变溶菌素发酵的影响

变溶菌素是由球孢链霉菌产生的一种胞外溶菌酶群。它包括几种不同类型的溶菌酶,有着广阔的用途和良好的应用前景。许多研究结果[1,2]表明,它比卵清溶菌酶有更为广泛的溶菌谱,应用范围更广,尤其是在预防和治疗龋齿[3]方面有其独特的优点。在医药上可用作灭菌剂,也可用其作?..     

Increase of xylitol production rate by controlling redox potential in Candida parapsilosis

The effect of redox potential on xylitol production by Candida parapsilosis was investigated. The redox potential was found to be useful for monitoring the dissolved oxygen (DO) level in culture media, especially when the DO level was low. An increase in the agitation speed in a 5 L fermentor resulted in an increased culture redox potential as well as enhanced cell growth. Production of xylitol was maximized at a redox potential of 100 mV. As the initial cell concentration increased from 8 g/L to 30 g/L, the volumetric productivity of xylitol increased from 1.38 g/L. h to 4.62 g/L. h. A two-stage xylitol production strategy was devised, with stage 1 involving rapid production of cells under well-aerated conditions, and stage 2 involving cultivation with reduced aeration such that the culture redox potential was 100 mV. Using this technique, a final xylitol concentration of 180 g/L was obtained from a culture medium totally containing 254.5 g/L xylose in a 3,000 L pilot scale fermentor after 77 h fermentation. The volumetric productivity of xylitol during the fermentation was 2.34 g/L. h.     

Homofermentative lactate production cannot sustain anaerobic growth of engineered Saccharomyces cerevisiae: possible consequence of energy-dependent lactate export

Due to a growing market for the biodegradable and renewable polymer polylactic acid, the world demand for lactic acid is rapidly increasing. The tolerance of yeasts to low pH can benefit the process economy of lactic acid production by minimizing the need for neutralizing agents. Saccharomyces cerevisiae (CEN.PK background) was engineered to a homofermentative lactate-producing yeast via deletion of the three genes encoding pyruvate decarboxylase and the introduction of a heterologous lactate dehydrogenase (EC 1.1.1.27). Like all pyruvate decarboxylase-negative S. cerevisiae strains, the engineered strain required small amounts of acetate for the synthesis of cytosolic acetyl-coenzyme A. Exposure of aerobic glucose-limited chemostat cultures to excess glucose resulted in the immediate appearance of lactate as the major fermentation product. Ethanol formation was absent. However, the engineered strain could not grow anaerobically, and lactate production was strongly stimulated by oxygen. In addition, under all conditions examined, lactate production by the engineered strain was slower than alcoholic fermentation by the wild type. Despite the equivalence of alcoholic fermentation and lactate fermentation with respect to redox balance and ATP generation, studies on oxygen-limited chemostat cultures showed that lactate production does not contribute to the ATP economy of the engineered yeast. This absence of net ATP production is probably due to a metabolic energy requirement (directly or indirectly in the form of ATP) for lactate export.     

基于途径分析的L-异亮氨酸发酵溶氧控制研究

利用途径分析方法对黄色短杆菌（Brevibacterium flavum）TC-21 生产L-异亮氨酸的途径进行了分析,确定了黄色短杆菌TC-21生产L-异亮氨酸的最佳途径的通量分布,根据途径分析的结果,TCA循环的代谢流量对L-异亮氨酸产量有明显影响,而TCA循环与发酵过程中的溶氧密切相关,因此可以通过控制溶氧来提高L-异亮氨酸产量。在发酵过程的不同阶段,根据菌体生长和产酸的需求,改变TCA代谢流量,可以有效提高产酸率。实验证明,通过溶氧分阶段控制发酵生产L-异亮氨酸,比溶氧恒定控制方式发酵产率提高了15.77％。实验结果说明,用途径分析的结果指导发酵过程中的溶氧可以大幅度提高L-异亮氨酸的产量。     

酿酒酵母对数生长后期代谢重构的全基因组表达谱芯片分析

为了探讨酵母进入对数生长后期以后酒精生产速度降低的原因,我们利用酵母表达谱芯片技术对酿酒酵母细胞从对数生长中期进入对数生长后期时的全基因组表达谱进行了分析,发现酵母在对数生长中期的表达谱非常稳定,而一旦进入对数生长后期.则出现明显的代谢重构现象.许多氨基酸合成和代谢相关的基因、离子转移以及与能量的生成和储存等功能相关的基因出现了不同程度的上调;而许多涉及酵母转座和DNA重组的基因则表达下调;一些中心代谢途径也发生了代谢重构.包括:琥珀酸和α-酮戊二酸生成途径基因的一致上调,都与氨基酸合成和代谢相关基因表达的结果相吻合.结果表明:由于氨基酸合成的需求量增加,进入对数生长后期酵母的代谢转向TCA循环和乙醛酸循环,导致酒精的生产速率降低.