alpha-Amylase production by Bacillus subtilis with dregs in an external-loop airlift bioreactor

An external-loop airlift bioreactor, with a low ratio 2.9 of height-to-diameter of the riser and a ratio 6.6 of riser-to-downcomer diameter, was used to produce alpha-amylase from fermentation with dregs by Bacillus subtilis. The effects of gas flow rate and liquid volume on alpha-amylase production were investigated. After a 36-h fermentation time, an average of 432.3U/ml alpha-amylase activity was obtained under the conditions of liquid volume 8.5l and gas flow rate 1.2vvm for the first 12h of fermentation, 1.4vvm from 12 to 27h, and 1.2vvm from 27h to the end. The activity was higher than that obtained in shaking flasks (409.0U/ml) and in a mechanically stirred tank bioreactor (397.2U/ml) under optimized operating conditions. The fermentation cycle of the airlift bioreactor was shorter than the 48h required for the shaking flasks and close to the 36h of the mechanically stirred tank bioreactor. It was demonstrated that the external-loop airlift bioreactor could substitute for the traditional mechanically stirred tank bioreactor to produce alpha-amylase from fermentation by Bacillus subtilis with dregs.     

Influence of Dissolved Oxygen Levels on Production of l-Asparaginase and Prodigiosin by Serratia marcescens

The effect of dissolved oxygen concentrations on the behavior of Serratia marcescens and on yields of asparaginase and prodigiosin produced in shaken cultures and in a 55-liter stainless-steel fermentor was studied. A range of oxygen transfer rates was obtained in 500-ml Erlenmeyer flasks by using internal, stainless-steel baffles and by varying the volume of medium per flask, and in the fermentor by high speed agitation (375 rev/min) or low rates of aeration (1.5 volumes of air per volume of broth per min), or both. Dissolved oxygen levels in the fermentation medium were measured with a membrane-type electrode. Peak yields of asparaginase were obtained in unbaffled flasks (3.0 to 3.8 IU/ml) and in the fermentor (2.7 IU/ml) when the level of dissolved oxygen in the culture medium reached zero. A low rate of oxygen transfer was accomplished by limited aeration. Production of prodigiosin required a supply of dissolved oxygen that was obtainable in baffled flasks with a high rate of oxygen transfer and in the fermentor with a combination of high-speed agitation and low-rate aeration. The fermentation proceeded at a more rapid rate and changes in pH and cell populations were accelerated by maintaining high levels of dissolved oxygen in the growth medium.     

Studies on Oxygen Transfer in Submerged Fermentations

In conventional shaken culture system, control of oxygen supply is performed by changing liquid volume in flasks and it necessarily introduces variation in the effectiveness of agitation and in the partial pressure of carbon dioxide. In jar or tank culture system, also, the changes in mechanical agitation and in the flow rate of air for control of aeration induce similar problems. It is impossible, therefore, to isolate the effects of oxygen on microbial metabolism from these accompanying ones. Hence, there is a basic requirement of making clear distinction among them, and in this paper the effects of agitation and carbon dioxide on product formation are presented in glutamic acid fermentation using the apparatus of controlling the level of dissolved oxygen throughout the fermentation.

To obtain fundamental knowledge required for attaining adequate aeration, the rate of oxygen demand in glutamic acid fermentation was discussed in connection with its fermentation rates. On the basis of specific rates, rates of change per unit mass of cells, glutamic acid fermentation was found to fall in the process pattern of Gaden’s type II, in which a constant rate of oxygen demand was sustained for a considerable time. On the basis of volumetric rates, rates of change per unit volume of broths, oxygen demand was recognized to be correlated with growth, sugar utilization and product formation, and it was pointed out particularly that the oxygen demand was closedly related with sugar utilization. In the particular cases where rapid utilization of sugar occurred, therefore, oxygen deficiency was liable to be evoked being unable to fill the growing oxygen demand. This finding might be useful for scale-up studies or process design.     

Treatment of coffee waste by slurry-state anaerobic digestion

Slurries containing 20% (w/v) coffee waste solids were treated anaerobically in one- and two-phase thermophilic methane fermentation systems (53°C) with or without pH control. In one-phase methane fermentation using a roller bottle reactor, the maximum gas evolution rate of 0.87 l/l·d was achieved during treatment for 91 d. However, this one-phase methane fermentation did not yield reproducible data. In a two-phase methane fermentation system consisting of a completely stirred tank reactor type (CSTR-type) liquefaction reactor without pH control and an anaerobic fluidized bed type gasification reactor, three-repetitions of treatment were conducted. Each treatment was very stable and the average gas evolution rate per volume of the gasification reactor was about 2.4 l/l·d. Two-repetitions of treatment were then done while controlling pH in the liquefaction at more than 6. The average gas evolution rate per volume of gasification reactor was found to have increased to 10.2 l/l·d, a value which corresponded to 0.84 l/l·d per total volume, including the liquefaction reactor. It was observed that treatment in a two-phase methane fermentation could be repeated in a stable fashion even in the closed system without discharging anything but the coffee waste residues.     

Growth monitoring of <Emphasis Type="Italic">Fibrobacter succinogenes</Emphasis> by pressure measurement

In life support systems, such as the MELiSSA (Micro-Ecological Life Support Alternative) project, developed by the European Space Agency, the aim is to understand and assemble artificial ecosystems for ensuring human subsistence in space. Fibrobacter succinogenes, an anaerobic bacterium, was used for the degradation of vegetable wastes produced in higher plants chambers, but the process does not allow the monitoring of biomass concentration and degradation rates. This study proposes a growth and a degradation monitoring technique using pressure measurements. First, volatile fatty acids (VFA) production was compared with biomass growth and with CO₂ production. The experiments were carried out in batch and fed-batch processes on glucose and on vegetables. The results have shown that a link could be established between VFA production, degradation rate and gas pressure measurements. Thus, the pressure could be used both as a relevant variable for online evaluation of biomass growth and of degradation of complex vegetable wastes.     

Analysis of glucose catabolites by using head-space gas chromatography for differentiation of some Gram-negative species

Volatile products from the degradation of glucose by a total of 66 strains ofEnterobacter cloacae, Escherichia coli, Klebsiella pneumoniae, Proteus mirabilis, Proteus vulgaris, andPseudomonas aeruginosa were analyzed by head-space gas chromatography. The bacteria were incubated for 1 h in a glucose-containing buffer solution before being analyzed by gas chromatography, using manual, semiautomatic, and automatic head-space injection. From the chromatographic patterns obtained, all strains could be differentiated as to species, with the exception of two strains ofProteus mirabilis, which gave chromatograms similar to those produced byProteus vulgaris. The gas chromatographic head-space technique developed provides a rapid and easily performed means for identification of bacteria, particularly when using an automatic injection unit, as exemplified in this study on some of the Gram-negative species commonly encountered in urinary tract infections.     

Process-engineering characterization of small-scale bubble columns for microbial process development

Volumetric oxygen transfer rates and power inputs were estimated by a model of the formation of primary gas bubbles at the static sparger (sinter plate) of small-scale bubble columns and a common mass-transfer correlation for bubbles rising in a non-coalescent Newtonian electrolyte solution of low viscosity. Estimations were used to assess the dimensioning and possibilities of small-scale bubble column application with an height/diameter ratio of about 1. Estimations of volumetric oxygen transfer rates (<0.16 s^-1) and power inputs (<100 W m^-3) with a mean pore diameter of the static sparger of 13 µm were confirmed as function of the superficial air velocity (<0.6 cm s^-1) by measurements using an Escherichia coli fermentation medium. Small-scale bubble columns are thus to be classified between shaking flasks and stirred-tank reactors with respect to the oxygen transfer rate, but the maximum volumetric power input is more than one magnitude below the power input in shaking flasks, which is of the same order of magnitude as in stirred-tank reactors. A small-scale bubble columns system was developed for microbial process development, which is characterized by handling in analogy to shaking flasks, high oxygen transfer rates and simultaneous operation of up to 16 small-scale reactors with individual gas supply in an incubation chamber.     

Diversity and activity of enriched ruminal cultures of anaerobic fungi and methanogens grown together on lignocellulose in consecutive batch culture

Consecutive batch cultures (CBC), involving nine serial transfers at 3, 5 and 7 d intervals (21, 45 and 63 d, respectively) were established to enrich for plant fibre degrading co-cultures of anaerobic fungi and methanogens from rumen digesta. Microbial diversity and fermentation end-products were measured at appropriate intervals over each CBC time-course. While methanogenic populations remained diverse, anaerobic fungal diversity was related to transfer interval and appeared to decrease with increasing transfer number. Acetate was the principal aqueous fermentation end-product with minimal quantities of lactate and formate detected. Methane and carbon dioxide were detected in the gaseous head-space of all co-cultures and the total amounts of gas generated per transfer was greater with transfer intervals of 5 and 7 d compared with a 3 d interval, although the 3 d interval tended to be more efficient per unit time. In conclusion, rapidly growing, methane producing co-cultures of anaerobic fungi and methanogens from rumen digesta were easy to establish on lignocellulose (barley straw) and maintain over considerable time periods. These results suggest such co-cultures have potential in industrial scale anaerobic digestion (AD) of highly fibrous substrates, which are resistant to degradation in conventional AD plants.     

Ranking the significance of fermentation conditions on the volatile organic compounds of Tuber melanosporum fermentation system by combination of head-space solid phase microextraction and chromatographic fingerprint similarity analysis

Tuber melanosporum is highly appreciated in culinary contexts due to its unique and characteristic aroma. T. melanosporum fermentation has been established as a promising alternative for fruiting bodies to produce volatile organic compounds (VOCs). In this work, a technique using a combination of chromatographic fingerprint similarity analysis, head-space solid phase microextraction and gas chromatography was developed to rank the significance of fermentation conditions on the VOCs profile during T. melanosporum fermentation. Omission tests indicated that the absence of major carbon source (i.e., sucrose) in the fermentation media had the most significant effect on the profile of VOCs, followed by the absence of yeast extract or peptone. Consideration of the culture conditions revealed that VOCs produced was the most significantly affected by temperature. These results indicated that it is possible to adjust the aroma of truffles via fermentation process control.     

Expression level of heterologous proteins in Pichia pastoris is influenced by flask design

The yeast Pichia pastoris is a convenient production system that enables expression of heterologous proteins in high amounts. As a fermentation method, shaking flasks are very popular because of their simplicity of handling and their low cost. We compared the expression level of the enzyme acetylcholinesterase in a transformed strain of P. pastoris grown in different flasks, presenting various designs but all with the same volume. A several-thousand-fold difference appeared in the expression levels; and the results could not be explained by differences between the flasks in the oxygenation of the medium. The data show that flask design is an important factor to consider for optimising fermentation processes.     

Reassessing the out-of-phase phenomenon in shake flasks by evaluating the angle-dependent liquid distribution relative to the direction of the centrifugal acceleration

Shake flasks are still the most relevant experimental tool in the development of viscous fermentation processes. The phase number, which defines the onset of the unfavorable out-of-phase (OP) phenomenon in shake flasks, was previously defined via specific power input measurements. In the OP state, the bulk liquid no longer follows the orbital movement of the imposed centrifugal force, which is for example, detrimental to oxygen transfer. In this study, an optical fluorescence technique was used to measure the three-dimensional liquid distribution in shake flasks. Four new optically derived evaluation criteria for the phase transition between the in-phase and OP condition were established: (a) thickness of the liquid film left on the glass wall by the rotating bulk liquid, (b) relative slope of the leading edge of bulk liquid (LB) lines, (c) trend of the angular position of LB, and (d) very high angular position of the leading edge. In contrast to the previously applied power input measurements, the new optical evaluation criteria describe the phase transition in greater detailed. Instead of Ph = 1.26, a less conservative value of Ph = 0.91 is now suggested for the phase transfer, which implies a broader operating window for shake flask cultivations with higher viscosities.     

On-line measurement of gas production rates

Gas evolution rates represent an important variable to track in biological and certain electrochemical processes. Accurate gas flow rate sensors exist for gas streams possessing a pressure head, such as when pressurized air or oxygen is delivered to a fermentation process. However, these devices impose pressure heads that can inhibit gas production and, therefore, yield false measurements. Examples of effected processes would include electrochemical production of a gas at the electrode (e.g., electrolysis) or anaerobic fermentation (e.g., anaerobic production of methane). In this work, we present an on-line gas measurement technique that measures on-line gas production from an anaerobic microbial process that is continuously fed simulated food waste over a 6-month period. Commentary is given on the sensor's accuracy and ease of use within the context of long-term operation, ability to measure both low and high gas production rates, as well as its potential for process control and system-health monitoring.     

An on-line technique for monitoring propionic acid fermentation

An on-line technique, based on measuring the increase in pressure due to CO₂ release in a closed air-tight reactor, was used to evaluate the fermentation of lactate by propionibacteria. The method was applied to batch cultures of Propionibacterium shermanii grown in yeast extract/sodium lactate medium containing lactate as a carbon source under micro-aerophilic conditions. Gas pressure evolution was compared both with substrate consumption and metabolites production and with acidification and growth. Linear relationships were found between gas pressure variation, lactate consumption and propionate and acetate production. The technique also enabled the evaluation of total CO₂ produced, by taking account of pressure, oxygen and pH measurements. These results tend to show that this simple and rapid method could be useful to monitor propionic acid bacteria growth.     

溶氧对Blakeslea trispora分批发酵生产β-胡萝卜素的影响

在摇瓶和5 L发酵罐中研究了溶氧 (DO) 对Blakeslea trispora分批发酵生产β-胡萝卜素的影响,总结了5 L发酵罐中β-胡萝卜素发酵过程中溶氧的变化规律.结果表明,当500 mL摇瓶装液量为50 mL,转速为240 r/min条件下发酵生产β-胡萝卜素产量最大,达到3.416 g/L; 5 L发酵罐中,在搅拌转速为1 000 r/min,通气量为1.5 vvm的条件下,β-胡萝卜素的产量可达到3.712 g/L,略高于摇瓶,这可能是由于5 L发酵罐中的气液传递和混合状况好于摇瓶,促进了产物的合成.     

培养幽门螺旋杆菌的发酵工艺研究

采用摇瓶微需氧培养技术,模拟发酵条件,探讨不同因素（pH、转速、种子菌接种量）对幽门螺旋杆菌（Helicobacter pylori,Hp）生长的影响,优化工艺参数,并级联放大到10L发酵罐发酵,经多次实验,建立了稳定的Hp发酵工艺,24h发酵细菌的最大吸光度A600达3.89,收获菌体湿重达5.2g／L。     

Studies on Oxygen Transfer in Submerged Fermentations

The unsteady-state gas analysis method for the determination of oxygen transfer rate in shaken cultures was applied to the glutamic acid fermentation. This method was essentially based on the measurement of oxygen tension of gas phase in flasks. Major intentions of this application were to clarify the problems of oxygen transfer, to establish the measure of aeration effectiveness and to design the best aeration condition in the glutamic acid fermentation. Correlations of the fermentation to the level of dissolved oxygen, the rate of oxygen transfer, overall oxygen transfer coefficient and oxygen demand of cells were examined. As a measure of aeration effectiveness, the rate of oxygen transfer actually occurring in the fermentation seemed to be preferable, and was found to be above 7 × 10^?7 mol/ml-min for attaining the maximum productivity. Extremely high or low oxygen supply resulted in less productivity.     

Application of process mass spectroscopy to the detection of metabolic changes in plant tissue culture

There is a clear need in the area of plant cell culture for methods of on-line estimation of culture parameters. The introduction of plant cells into culture can result in a loss of their photoautotrophic character so that they are largely heterotrophic. As a result, fermentation off-gas analysis may not be confounded by photosynthetically-related O₂ production. In this study performance of a suspension culture of Syringa vulgaris, in a pneumatically agitated bioreactor of in-house design, was investigated. The effect of light on growth, carbohydrate metabolism and the respiratory quotient (RQ), determined by process mass spectroscopy, was studied. Yield coefficients for cells grown in the light and dark were similar although the patterns of carbohydrate uptake were quite different. Maximum biomass yields were higher in this bioreactor than normally observed in shake flasks. The RQ was dynamic during the course of the fermentation, peaking during the transition from the lag phase to the growth phase. It is suggested that the RQ may prove useful as an on-line parameter for monitoring transitions in cellular metabolism during plant cell culture fermentations.Abbreviations RQ respiratory quotient - v.v.m. volume of gas fed to fermenter per unit volume per minute - Y_X/S growth yield coefficient based on total carbohydrate     

Comparison of protein fermentation characteristics in rumen fluid determined with the gas production technique and the nylon bag technique

In this study, a modified version of the gas production technique was used to determine protein fermentation characteristics in rumen fluid of 19 feedstuffs. Performing the incubations in a N-free environment, and with an excess of rapidly fermentable carbohydrates, made N the limiting factor to microbial growth, and so gas production profiles reflected the availability of N from the feed samples. Results showed that fermentation of protein in rumen fluid can be determined with this modified gas production technique, and that there were distinct differences in protein fermentation between the feed samples. Availability of protein for fermentation was highest in wheat, potato pieces and lupin, and lowest in Rumiraap, a formaldehyde treated rapeseed meal, palm kernel expeller and brewery grains. The protein degradation characteristics of the 19 feed ingredients were also determined with the in situ nylon bag technique. With the obtained results, the amount of rumen escape protein (REP) was calculated for each feedstuff. The results showed that the rate of degradation ranged from 0.010/h for Rumiraap to 0.151/h for wheat. The amount of REP ranged from 197 g/kg CP for lupin to 840 g/kg CP for Rumiraap. Comparing the gas production results with the results obtained with the nylon bag technique showed that there was a good relationship between the gas production after 12–25 h of incubation and the calculated amount of REP (r² = 0.83–0.85). The results show that the adapted gas production technique, being depleted of N and using an excess of rapidly fermentable carbohydrates, is suitable to recognize differences in N availability between feed samples and can be used as an alternative to the nylon bag technique and other in vitro techniques.     

Gas Exchange of Algae: II. Effects of Oxygen, Helium, and Argon on the Photosynthesis of Chlorella pyrenoidosa

Changes in the oxygen partial pressure of air over the range of 8 to 258 mm of Hg did not adversely affect the photosynthetic capacity of Chlorella pyrenoidosa. Gas exchange and growth measurements remained constant for 3-week periods and were similar to air controls (oxygen pressure of 160 mm of Hg). Oxygen partial pressures of 532 and 745 mm of Hg had an adverse effect on algal metabolism. Carbon dioxide consumption was 24% lower in the gas mixture containing oxygen at a pressure 532 mm of Hg than in the air control, and the growth rate was slightly reduced. Oxygen at a partial pressure of 745 mm of Hg decreased the photosynthetic rate 39% and the growth rate 37% over the corresponding rates in air. The lowered metabolic rates remained constant during 14 days of measurements, and the effect was reversible after this time. Substitution of helium or argon for the nitrogen in air had no effect on oxygen production, carbon dioxide consumption, or growth rate for 3-week periods. All measurements were made at a total pressure of 760 mm of Hg, and all gas mixtures were enriched with 2% carbon dioxide. Thus, the physiological functioning and reliability of a photosynthetic gas exchanger should not be adversely affected by: (i) oxygen partial pressures ranging from 8 to 258 mm of Hg; (ii) the use of pure oxygen at reduced total pressure (155 to 258 mm of Hg) unless pressure per se affects photosynthesis, or (iii) the inclusion of helium or argon in the gas environment (up to a partial pressure of 595 mm of Hg).     

添加剂对水稻秸秆实地混合厌氧发酵产甲烷系统的作用

为提高水稻秸秆利用效率,改进水稻秸秆实地混合厌氧发酵产甲烷技术,本研究开展了添加剂在混合厌氧发酵系统的应用研究。试验选取水稻秸秆和猪粪作为发酵原料,通过分别添加不同的浓度的吐温20和腐植酸,测定甲烷的产气量和浓度、秸秆的降解和土壤肥力的变化,以揭示添加剂类型及其浓度对水稻田实地甲烷生产系统的影响。结果表明:添加剂的掺入并未影响产气的动态变化趋势,但显著地促进产气和提高产气浓度,整体效果由高到低为腐植酸吐温20对照,其中经腐植酸处理的产气量和产气浓度对照相比分别提高了50. 73%和24. 55%。添加剂的掺入有利于水稻秸秆纤维素和半纤维素的降解,但对木质素没有显著影响;其中以0. 15 g/L腐植酸和0. 30 g/L吐温20的降解率最高,相较于对照其纤维素降解率均提高了22. 11%,半纤维素降解率分别提高了107. 13%和98. 39%。添加剂的掺入能显著增加土壤肥力,以0. 15 g/L腐植酸和0. 30 g/L吐温20处理水平的效果最优,相较于对照,其土壤有机质分别增加了29. 63%和23. 72%,全氮分别增加了52. 32%和42. 38%,全磷分别增加了83. 33%和57. 14%。