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1.
    
Microtiter plates with integrated optical sensing of dissolved oxygen were developed by immobilization of two fluorophores at the bottom of 96-well polystyrene microtiter plates. The oxygen-sensitive fluorophore responded to dissolved oxygen concentration, whereas the oxygen-insensitive one served as an internal reference. The sensor measured dissolved oxygen accurately in optically well-defined media. Oxygen transfer coefficients, k(L)a, were determined by a dynamic method in a commercial microtiter plate reader with an integrated shaker. For this purpose, the dissolved oxygen was initially depleted by the addition of sodium dithionite and, by oxygen transfer from air, it increased again after complete oxidation of dithionite. k(L)a values in one commercial reader were about 10 to 40 h(-1). k(L)a values were inversely proportional to the filling volume and increased with increasing shaking intensity. Dissolved oxygen was monitored during cultivation of Corynebacterium glutamicum in another reader that allowed much higher shaking intensity. Growth rates determined from optical density measurement were identical to those observed in shaking flasks and in a stirred fermentor. Oxygen uptake rates measured in the stirred fermentor and dissolved oxygen concentrations measured during cultivation in the microtiter plate were used to estimate k(L)a values in a 96-well microtiter plate. The resulting values were about 130 h(-1), which is in the lower range of typical stirred fermentors. The resulting maximum oxygen transfer rate was 26 mM h(-1). Simulations showed that the errors caused by the intermittent measurement method were insignificant under the prevailing conditions.  相似文献   

2.
3.
This reports on the determination of the overall oxygen transfer coefficient in a mechanically agitated vessel using a randomly pulsed dynamic method. This method consists in exciting the system by randomly switching the inlet gas stream with air or nitrogen with an identical volumetric flow rate. A pseudo-random binary sequence was used. This procedure is routinely used in process control for the identification of system's transfer function. The pulsed dynamic method gives good reliability (as compared with the traditional gassing-out method) and reproducibility in water. However, further improvement is needed before it can be used to monitor on-line the k(L)a during a fermentation.  相似文献   

4.
The overall oxygen mass transfer coefficient (KLa) is often used as scale-up factor of fermentation systems. In fermenter scale-up, it is desired to achieve the same KLa values at the larger scale than the one that was obtained at a smaller scale during the development stage. It is therefore important to be able to measure KLa in situ during fermentation and to also determine the action to be taken to maintain its value at its design set point. These objectives can be obtained by measuring KLa using the dynamic method and enhancing the KLa information by immediately conducting a series of changes in agitation speed and/or aeration rate to determine the influence of these variables on KLa. This enhanced dynamic method is demonstrated with two filamentous microorganisms: Trichoderma reesei for the production of cellulase and Aspergillus niger for the production of citric acid. Two different types of bioreactor were used: a reciprocating plate bioreactor and a stirred (Rushton) bioreactor. It is shown that the proposed method can provide a simple way to measure the local variation of KLa and to adjust its value to its set point during the course of fermentation.  相似文献   

5.
The concentration of dissolved oxygen in waters 0.5–0.6 m above the bottom of Lake Hibara, a dimictic lake, was zero in early spring of 1994 and 1997. The concentrations in early spring of 1992, 1993, 1995, 1996, and 1998 ranged from 3.75 to 10.1 mg l−1. The depth profiles of water temperature suggest that water had not circulated prior to the sample collections of 1994 and 1997, but it had done so in the cases of the other years, suggesting that winter conditions were well preserved in the former years. On the other hand, the dissolved oxygen in the same strata decreased severely in summer. However, more or less titratable amounts of dissolved oxygen still remained (0.01–0.73 mg l−1) at the final stages of summer stratification from 1992 to 1998. These facts show that a completely anoxic condition is not formed in this lake in summer but is sometimes formed in winter. It is interesting to note that in spite of unfavorable winter conditions for oxygen consumption, i.e., shorter duration and lower water temperature, oxygen is exhausted. These facts suggest that ventilation to the depths is much greater in summer than in winter. Received: March 5, 1999 / Accepted: October 18, 1999  相似文献   

6.
7.
    
This communication proposes a mechanistic modification to a recently published method for analyzing oxygen mass transfer in two-phase partitioning bioreactors (Nielsen et al., 2003), and corrects an oversight in that paper. The newly proposed modification replaces the earlier empirical approach, which treated the two liquid phases as a single, homogeneous liquid phase, with a two-phase mass transfer model of greater fundamental rigor. Additionally, newly developed empirical models are presented that predict the mass transfer coefficient of oxygen absorption in both aqueous medium and an organic phase (n-hexadecane) as a function of bioreactor operating conditions. Experimental values and theoretical predictions of mass transfer coefficients in two-phase dispersions, k(L)a(TP), are compared. The revised approach more clearly demonstrates the potential for oxygen mass transfer enhancement by organic phase addition, one of the motivations for employing a distinct second phase in a partitioning bioreactor.  相似文献   

8.
    
An empirical correlation, based on conventional forms, has been developed to represent the oxygen mass transfer coefficient as a function of operating conditions and organic fraction in two-phase, aqueous-organic dispersions. Such dispersions are characteristic of two-phase partitioning bioreactors, which have found increasing application for the biodegradation of toxic substrates. In this work, a critical distinction is made between the oxygen mass transfer coefficient, k(L)a, and the oxygen mass transfer rate. With an increasing organic fraction, the mass transfer coefficient decreases, whereas the oxygen transfer rate is predicted to increase to an optimal value. Use of the correlation assumes that the two-phase dispersion behaves as a single homogeneous phase with physical properties equivalent to the weighted volume-averaged values of the phases. The addition of a second, immiscible liquid phase with a high solubility of oxygen to an aqueous medium increases the oxygen solubility of the system. It is the increase in oxygen solubility that provides the potential for oxygen mass transfer rate enhancement. For the case studied in which n-hexadecane is selected as the second liquid phase, additions of up to 33% organic volume lead to significant increases in oxygen mass transfer rate, with an optimal increase of 58.5% predicted using a 27% organic phase volume. For this system, the predicted oxygen mass transfer enhancements due to organic-phase addition are found to be insensitive to the other operating variables, suggesting that organic-phase addition is always a viable option for oxygen mass transfer rate enhancement.  相似文献   

9.
We show the application of a novel optical on-line sensor fixed in spinner flasks for the online monitoring of dissolved O2 concentrations during mammalian cell growth. Using this sensor that requires only minute changes to the flask to be made, we could determine the volumetric O2 transfer coefficient as well as O2 consumption rates. Under normal growth conditions the cells did not undergo O2 limitation. Also, the transfer of O2 from the atmosphere to the spinner flasks is influenced by the use of screw caps. The on-line measurement was further applied to determine the O2 uptake rates which can then be used to monitor the metabolic state of the cells and also for online process monitoring.  相似文献   

10.
    
Shake flasks are ubiquitous in cell culture and fermentation. However, conventional devices for measuring oxygen concentrations are impractical in these systems. Thus, there is no definitive information on the oxygen supply of growing cells. Here we report the noninvasive, nonintrusive monitoring of dissolved oxygen (DO) in shake flasks using a low-cost optical sensor. The oxygen-sensitive element is a thin, luminescent patch affixed to the inside bottom of the flask. The sensitivity and accuracy of this device is maximal up to 60% DO, within the range that is critical to cell culture applications. By measuring actual oxygen levels every 1 or 5 min throughout the course of yeast and E. coli fermentations, we found that a modest increase in shaker speed and a decrease in culture volume slowed the onset of oxygen limitation and reduced its duration. This is the first time that in situ oxygen limitation is reported in shake flasks. The same data is unattainable with a Clark type electrode because the presence of the intrusive probe itself changes the actual conditions. Available fiber optic oxygen sensors require cumbersome external connections and recalibration when autoclaved.  相似文献   

11.
    
Bioprocess optimization for cell-based therapies is a resource heavy activity. To reduce the associated cost and time, process development may be carried out in small volume systems, with the caveat that such systems be predictive for process scale-up. The transport of oxygen from the gas phase into the culture medium, characterized using the volumetric mass transfer coefficient, kLa, has been identified as a critical parameter for predictive process scale-up. Here, we describe the development of a 96-well microplate with integrated Redbud Posts to provide mixing and enhanced kLa. Mixing in the microplate is characterized by observation of dyes and analyzed using the relative mixing index (RMI). The kLa is measured via dynamic gassing out method. Actuating Redbud Posts are shown to increase rate of planar homogeneity (2 min) verse diffusion alone (120 min) and increase oxygenation, with increasing stirrer speed (3500-9000 rpm) and decreasing fill volume (150-350 μL) leading to an increase in kLa (4-88 h−1). Significant increase in Chinese Hamster Ovary growth in Redbud Labs vessel (580,000 cells mL-1) versus the control (420,000 cells mL-1); t(12.814) = 8.3678, p ≤ .001), and CD4+ Naïve cell growth in the microbioreactor indicates the potential for this technology in early stage bioprocess development and optimization.  相似文献   

12.
以摇瓶所得摄氧率为基准进行发酵放大   总被引:2,自引:0,他引:2       下载免费PDF全文
通过设计特殊摇瓶,用亚硫酸盐法测出摇瓶口纱布层氧通透率的基础上,在实际发酵情况下通过测定瓶内气、液相氧的变化得出其发酵过程中的摄氧率(OUR)及氧传递系数(KLa)。以特制摇瓶取得的菌体CUR为基准进行发酵过程和发酵罐的放大。通过质谱仪在线检测及采样分析,研究了3种不同供气流量及搅拌转速下的放大结果。摇瓶与发酵罐在菌体OUR、菌体产量方面吻合很好,而在整个放大过程中,发现摇瓶与发酵罐内的氧传递系数(KLa)、溶解氧(CL)差异较大。  相似文献   

13.
Hypoxia is common in freshwater, estuarine, and shallow or enclosed marine systems. Research on the sub-lethal effects of hypoxia on feeding and growth includes both field and laboratory studies. Extended regulation of dissolved oxygen (DO) is difficult to precisely control in the laboratory. Here we describe a device that is capable of simultaneously monitoring and controlling DO at multiple treatment levels, in replicate experimental tanks, for indefinite periods of time. Each treatment level may be static or fluctuate on a diel cycle. The device consists of a series of independent aquarium systems, each of which is monitored and adjusted by a computer program. A data file and chart of DO levels in each treatment level is recorded. A computer program that repeatedly measures and adjusts DO controls the device. Because this apparatus is software-controlled, the user has the flexibility of altering treatment parameters at any time without interrupting experiments.  相似文献   

14.
A new online monitoring technique to measure the physiological parameters, dissolved oxygen (DO) and pH of microbial cultures in continuously shaken 24-well microtiter plates (MTP) is introduced. The new technology is based on immobilised fluorophores at the bottom of standard 24-well MTPs. The sensor MTP is installed in a sensor dish reader, which can be fixed on an orbital shaker. This approach allows real online measurements of physiological parameters during continuous shaking of cultures without interrupting mixing and mass transfer like currently available technologies do. The oxygen transfer conditions at one constant shaking frequency (250 1/min) and diameter (25 mm) was examined with the chemical sulphite oxidation method. Varied filling volumes (600–1,200 μL) of Escherichia coli cultures demonstrated the importance of sufficient oxygen transfer to the culture. Cultures with higher filling volumes were subjected to an oxygen limitation, which influenced the cell metabolism and prolongated the cultivation time. The effects could be clearly monitored by online DO and pH measurements. A further study of different media in an E. coli fermentation elucidated the different growth behaviour in response to the medium composition. The MTP fermentations correlated very well with parallel fermentations in shake flasks. The new technique gives valuable new insights into biological processes at a very small scale, thus enabling parallel experimentation and shorter development times in bioprocessing.  相似文献   

15.
Xie K  Zhang XW  Huang L  Wang YT  Lei Y  Rong J  Qian CW  Xie QL  Wang YF  Hong A  Xiong S 《Cytotechnology》2011,63(4):345-350
A novel, optical sensor was fixed in a new type of disposable bioreactor, Tubespin, for the on-line (real-time) monitoring of dissolved oxygen concentrations during cell culture. The cell density, viability and volumetric mass transfer coefficient were also determined to further characterize the bioreactors. The kLa value of the Tubespin at standard conditions was 24.3 h−1, while that of a spinner flask was only 2.7 h−1. The maximum cell density in the Tubespin bioreactor reached 6 × 106 cells mL−1, which was two times higher than the cell density in a spinner flask. Furthermore, the dynamic dissolved oxygen level was maintained above 90% air-saturation in the Tubespin, while the value was only 1.9% in a spinner flask. These results demonstrate the competitive advantage of using the Tubespin system over spinner flasks for process optimization and scale-down studies of oxygen transfer and cell growth.  相似文献   

16.
    
Oxygen mass transfer in shake flasks is an important aspect limiting the culture of aerobic microorganisms. In this work, mass transfer of oxygen through a closure and headspace of shake flasks is investigated. New equations for prediction of kGa in shake flasks with closures are introduced. Using Pseudomonas putida, microbial growth on glucose (fast metabolism) and phenol (slow metabolism) in shake flasks with closures were studied, considering both substrate and oxygen restrictions. A combined model for oxygen mass transfer and microbial growth is shown to accurately predict experimental oxygen concentrations and oxygen yield factors during growth experiments more accurately than previous models.  相似文献   

17.
摇瓶的体积氧传递系数和氧通透率的测定   总被引:6,自引:2,他引:6       下载免费PDF全文
通过设计特殊摇瓶,用亚硫酸钠法测出摇瓶的体积氧传递系数和氧透过纱布层的通透率。以氧电极测其内外氧的分压降后,可以算出摇瓶表观体积氧传递系数(kLa)app及真实体积氧传递系数kLa,并进一步求出氧通透率。由实验得出:氧分压降低6.1%,氧传递系数增加一倍;在37c、220r/min、500m1摇瓶(内盛液50m1)8层纱布的氧通透率Pm=43.7moI/m2·h·arm;并且关联出摇瓶容积V、装液量VL、转速n、摄氏温度t之间的模型式:(kLa)app=1.84×10-7[t]1.8479·[n]2.3906.(VLV]-0.6360(kLa)=2.02×10-7[t]1.8525·[n]2.39441·[VLV]-0.6370  相似文献   

18.
In vitro zygotic and somatic embryogenesis procedures for wheat have been improved by simulating in ovulo nutritional, hormonal and dissolved oxygen (dO2) conditions. However, diurnal fluctuations in these conditions during early embryony are not well characterized. In this study, dO2 and water-soluble carbohydrate levels in wheat kernels were determined after 8 h of light and 8 h of dark at approximately 6, 12 and 18 day post anthesis (DPA). Clark style O2 microelectrodes, having a tip diameter of approximately 115 μm, were inserted into intact kernels immediately distil to the developing embryo, and dO2 levels were recorded at 50 μm intervals into the center of kernels. High-performance anion exchange chromatography with pulsed amperometric detection was used to quantify carbohydrate levels in endosperm sap. dO2 levels in the chlorophyllous layer of the pericarp reached 190 mmol m−3 during the day, which probably represents, because of photosynthesis, a supersaturated O2 condition relative to the external environment (21% O2). At the embryo surface, dO2 levels at 6 DPA ranged from 135 to 170 mmol m−3. At 12 and 18 DPA, dO2 levels at the embryo axis ranged from 100 to 150 mmol m−3. At all three stages, dO2 levels in the center of the endosperm were below 13 mmol m−3. Extreme fluctuations in carbohydrate levels were observed diurnally during rapid seed fill (12 DPA). Levels of sucrose and short-chain fructans were much higher during the day than during the night. In contrast, fructose, glucose, and myo-inositol levels were much higher during the night than during the day. By 18 DPA (hard dough stage), carbohydrate levels tended to be similar during the day and night. These dynamic fluctuations may assist in regulating embryony in ovulo, and their simulation might improve the development of somatic and zygotic embryos in vitro.  相似文献   

19.
    
Yarrowia lipolytica is able to secrete large amounts of citric acid (CA), which is greatly affected by the dissolved oxygen concentration (DOC) in the fermentation medium. In this study, oleic acid was selected as oxygen‐vector to improve DOC during CA fermentation. When 2% (v/v) of oleic acid was added to the culture broth, higher DOC (>42.1%) was determined throughout the CA synthesis phase. The yield of CA reached a maximum of 32.1 g/L (25.4% higher than the control) and the biomass was 8.8 g/L. The substrate uptake rate, products formation rate and key enzyme activities were also determined, and the results indicated that CA synthesis was strengthened with oleic acid addition. Furthermore, it was detected that oleic acid could be assimilated by the cells, which means that oleic acid could be served both as oxygen‐vector and co‐substrate for CA synthesis by Y. lipolytica. In a bioreactor with working volume of 3 L, the highest concentration of CA reached to 36. 4 g/L in the presence of 2% (v/v) oleic acid after 192 h of fermentation. These results confirmed that oleic acid could be applied in the large‐scale production of CA by Y. lipolytica.  相似文献   

20.
Twenty-four Hansenula polymorpha transformants were passaged and stabilised in glucose medium and screened in glycerol medium for recombinant phytase in shaken test tubes. The cultivations were performed under either limited or non-limited oxygen supply. Maximum oxygen transfer capacities of test tubes were assessed by sulfite oxidation. Oxygen-limited glucose cultures resulted in a partially anaerobic metabolism and formation of 4.1 g ethanol l(-1), which was subsequently aerobically metabolised. Non-limited oxygen supply led to overflow metabolism and to accumulation of 2.1 g acetic acid l(-1), reducing the biomass yield. The use of glycerol in the screening main cultures prevented by-product formation irrespective of oxygen supply. Preculturing in glucose medium under non-limited oxygen supply resulted in a 20-h lag phase of the screening main culture. This lag phase was not observed when preculturing was performed under oxygen limitation. Phytase activity was on average 25% higher in cultures passaged, stabilised and screened under limited oxygen supply than in cultures under non-limited oxygen supply.  相似文献   

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