Acetic Acid Production by an Electrodialysis Fermentation Method with a Computerized Control System

In acetic acid fermentation by Acetobacter aceti, the acetic acid produced inhibits the production of acetic acid by this microorganism. To alleviate this inhibitory effect, we developed an electrodialysis fermentation method such that acetic acid is continuously removed from the broth. The fermentation unit has a computerized system for the control of the pH and the concentration of ethanol in the fermentation broth. The electrodialysis fermentation system resulted in improved cell growth and higher productivity over an extended period; the productivity exceeded that from non-pH-controlled fermentation. During electrodialysis fermentation in our system, 97.6 g of acetic acid was produced from 86.0 g of ethanol; the amount of acetic acid was about 2.4 times greater than that produced by non-pH-controlled fermentation (40.1 g of acetic acid produced from 33.8 g of ethanol). Maximum productivity of electrodialysis fermentation in our system was 2.13 g/h, a rate which was 1.35 times higher than that of non-pH-controlled fermentation (1.58 g/h).     

Factors affecting lactic acid production rate in the built-in electrodialysis fermentation,an approach to high speed batch culture

To avoid cells adhering to the ion-exchange membrane and damage of the cells in electrodialysis fermentation (ED-F), ED-F with a microfiltration (MF) module, was used in lactate fermentation. In this system, after 38 h of cultivation, the dry cell weight (2.89 g/l) and the number of viable cells (4.8 × 10⁹/ml) were about 1.8 and 1.6 times more than those of the control fermentation, respectively. Lactate dehydrogenase activity in this system was maintained at a high level, resulting in reduction of fermentation time to complete batch culture within 38 h. From these results, ED-F with an MF module enabled high speed batch culture.     

Oxidative and Reductive Routes of Glycerol and Glucose Fermentation by Escherichia coli Batch Cultures and Their Regulation by Oxidizing and Reducing Reagents at Different pHs

Glycerol and glucose fermentation redox routes by Escherichia coli and their regulation by oxidizing and reducing reagents were investigated at different pHs. Cell growth was followed by decrease of pH and redox potential (E _h ). During glycerol utilization at pH 7.5 ?pH, the difference between initial and end pH, was lower compared with glucose fermentation. After 8 h growth, during glycerol utilization E _h dropped down to negative values (?150 mV) but during glucose fermentation it was positive (+50 mV). In case of glycerol H₂ was evolved at the middle log phase while during glucose fermentation H₂ was produced during early log phase. Furthermore, upon glycerol utilization, oxidizer potassium ferricyanide (1 mM) inhibited both cell growth and H₂ formation. Reducing reagents dl-dithiothreitol (3 mM) and dithionite (1 mM) inhibited growth but stimulated H₂ production. The findings point out the importance of reductive conditions for glycerol fermentation and H₂ production by E. coli.     

Novel Method of Lactic Acid Production by Electrodialysis Fermentation

In lactic acid fermentation by Lactobacillus delbrueckii, the produced lactic acid affected the lactic acid productivity. Therefore, for the purpose of alleviating this inhibitory effect, an electrodialysis fermentation method which can continuously remove produced lactic acid from the fermentation broth was applied to this fermentation process. As a result, the continuation of fermentation activity was obtained, and the productivity was three times higher than in non-pH-controlled fermentation. In electrodialysis fermentation, the amount of produced lactic acid was 82.2 g/liter, which was about 5.5 times greater than that produced in non-pH-controlled fermentation. It was concluded that these good results were obtained on account of alleviating the lactic acid inhibitory effect by electrodialysis fermentation. However, the fouling of anion-exchange membranes by cells was observed in electrodialysis fermentation.     

A new process for red pigment production by submerged culture of Monascus purpureus

Formation of red pigment by Monascus purpureus via diauxic growth on glucose and ethanol in submerged culture was optimized based on inoculum preparation and culture medium. A vegetative inoculum was prepared from spores grown on ethanol. The optimized culture medium was low in phosphates, and had an initial pH?of 5.5. The characteristics of Monascus purpureus grown on glucose and on ethanol were compared: the specific consumption rate of glucose (q_G) was higher than the specific consumption rate of ethanol (q_E), whereas the specific growth rate was greatest with ethanol. The specific production rate of red pigment (p_OD) and pigment yield (Y_OD/s) with glucose was twice that with ethanol. A novel fermentation process was developed with M. purpureus initially grown with controlled ethanol formation, and consumption of the latter during pigment formation.     

Utility of culture redox potential for identifying metabolic state changes in amino acid fermentation

We investigated the relationship of dissolved oxygen and culture redox potential (CRP) on amino acid production. Corynebacterium glutamicum ATCC 14296 was used for all experiments. The fermentation can be divided into a growth phase and a production phase. Our results indicate that in order to get higher amino acid production, a lower oxygen supply during the exponential phase is favored. A higher oxygen supply rate appears to be necessary during the production phase. Culture redox potential (CRP) was used to monitor the fermentation. CRP readings were observed to drop to a characteristic minimum value as the metabolic state changed from a growth to production phase. This was evidenced by the commencement of amino acid production and a simultaneous uptake of lactate. Upon lactate exhaustion, the CRP increased abruptly. At the same time, maximal amino acid yields were observed. By the use of minimum CRP as an indication of metabolic phase changes, the agitation rate was changed to increase oxygen supply during the production phase. This significantly increased amino acid production. These results show that culture redox potential measurements can be used to monitor and optimize amino acid production by process manipulation.     

Optimization of Fermentation Conditions and Properties of an Exopolysaccharide from Klebsiella sp. H-207 and Application in Adsorption of Hexavalent Chromium

The novel exopolysaccharide HZ-7 is produced by Klebsiella sp. H-207, and its fermentation conditions were optimized by response surface methodology (RSM). In this study, the optimized medium consisted of sucrose 31.93 g/L, KNO₃ 2.17 g/L and K₂HPO₄ 5.47 g/L; while the optimized culture conditions consisted of seed age 13 h, with an inoculum size of 10.6% and incubation temperature of 28.9°C. A maximum HZ-7 yield of about 15.05 g/L was achieved under the optimized conditions using RSM and single-factor experiments. Next the exopolysaccharide HZ-7 was partially purified and characterized. The resulting product showed good properties, such as high concentration of uronic acid (41.67%), low average molecular weight (about 1.94×10⁵ Da) and porous surface structure, were very advantageous to biosorption. Therefore HZ-7 was applied to absorb hexavalent chromium (Cr(VI)). The maximum adsorption efficiency (99.2%) which was obtained at an initial pH of 1.0 along with an initial Cr(VI) concentration of 20 mg/L, was not affected by ordinary metal ions and temperature. These data suggest Klebsiella sp. H-207 exopolysaccharide will be promising potential for industrial application.     

Production and recovery of propionic and acetic acids in electrodialysis culture of Propionibacterium shermanii

The simultaneous production and recovery of propionic and acetic acids in cultures of Propionibacterium shermanii were examined while maintaining the concentrations of these acids in the fermentation broth at low values with electrodialysis to alleviate end product inhibition. By this method, maximum cell concentration increased 1.36 fold and the average productivities of propionic and acetic acids increased 1.4 fold and 1.31 fold, respectively, compared to cultures without electrodialysis. The mass ratio of propionic and acetic acids recovered was the same as that for the acids produced by fermentation. The inhibitory effect of propionic acid was more significant on the growth of cells than on the production of propionic acid. Some kinetic equations are presented for simulating the dry cell concentration in the fermentor and the concentrations of propionic and acetic acids in the permeate solution of an electrodialysis culture.     

End product inhibition in methane fermentations: Effects of carbon dioxide on fermentative and acetogenic bacteria

Summary The rates of glucose utilization by fermentative bacteria and propionate and butyrate utilization by acetogenic bacteria were studied and their dependence of pCO₂ in the interval 0–1 bar was determined. A batch fermentation method was used permitting good control of fermentation parameters and rapid experiments.The rate of glucose fermentation to acids, CO₂ and H₂ was in the order of 12,000 mg glucose/l · day which was about two orders of magnitude faster than the utilization of propionic and butyric acid by acetogenic bacteria. The rate of glucose utilization was about 30% greater at low values of pCO₂ compared with 1 bar CO₂.Propionate degradation was strongly affected by pCO₂; rates were 60 mg/l · day at pCO₂=1 bar and 200 mg/l · day at pCO₂=0.2 bar. Some CO₂ was required since the rate of propionate utilization dropped rapidly below pCO₂=0.2 bar. The rate of butyric acid utilization was constant at 170 mg/l · day; slightly lower at pCO₂=1 bar.Yields of methane from glucose or acids were close to the theoretical value 50% of degraded substrate-carbon. Yields were 20–30% higher at low values of pCO₂ compared with 1 bar CO₂.The redox potential was usually between –200 and –250 mV, slowly increasing to between –150 and –200 mV during fermentation. No clear connection between rates of substrate utilization, pCO₂ and E_h was detected.     

耐盐性毒死蜱降解菌HY-1 的产酶培养基及发酵条件优化

为了明确生化处理和微生物降解的关系,通过增加耐盐菌的比例可以提高农药废水生化处理效果。从农药厂废水中分离到1株耐盐性毒死蜱降解菌——蜡状芽孢杆菌(Bacillus cereus HY-1),以从该菌中提取到的降解酶比活力为指标,进行产酶培养基和发酵条件的优化研究。通过单一因素试验和正交试验,对细菌HY-1的产酸培养基和发酵条件进行了优化。运用SPSS软件进行结果分析,所获优化培养基配方为:葡萄糖6.0 g/L,胰蛋白胨2.2 g/L,K2HPO4 2.0 g/L,KH2PO4 0.2 g/L,MgSO4.7H2O 0.1 g/L,NaCl 0.1 g/L和微量元素溶液2 mL/L。得到菌株发酵培养的最佳优化条件为:种子液培养时间为16 h,发酵培养时间为18 h,接种量为1%(V/V),发酵培养基初始pH值为7.0。氯化钠浓度为0?30 g/L时降解酶比活力不受影响,这是已报道的耐盐性最强的一株毒死蜱降解菌。     

Effects of culture redox potential on succinic acid production by Corynebacterium crenatum under anaerobic conditions

During mixed-acid fermentation by Corynebacterium crenatum under anaerobic conditions, two moles of NADH are required to synthesize 1 mol of succinic acid. In this work, four controlled culture redox potentials and different carbon sources with different oxidation states were used to investigate the possibility of enhancing the succinic acid production by increasing the availability of NADH. When the culture redox potential was ?300 mV, the yield of succinic acid was 0.31 g/g, representing a 72% increase compared with the yield when the culture redox potential was ?40 mV. Meanwhile, the molar ratio of succinic acid/lactic acid increased from 0.27 to 0.48. When 0.1% neutral red was added to the acid production medium, the yield of succinic acid was 0.25 g/g, and the molar ratio of succinic acid/lactic acid was 0.38. Both values were higher than those obtained from glucose only (0.19 g/g, 0.26) or gluconate (0.05 g/g, 0.18). A higher NADH/NAD⁺ ratio and increased enzymatic activity could be achieved to enhance the succinic acid production by manipulating the culture to a more reductive environment.     

Production of acetic acid by Clostridium thermoaceticum in electrodialysis culture using a fermenter equipped with an electrodialyser

Electrodialysis culture of Clostridium thermoaceticum increased the yield of acetate by its continuous removal. In normal batch cultures without pH control the yield was 4.2 g acetic acid/800 ml, while in pH-controlled culture it was 16.8 g/800 ml. Although electrodialysis cultures gave almost the same yield (15.4 g/800 ml) as that in pH-controlled cultures, sparging CO₂ into the broth in electrodialysis culture increased the amount of acetic acid to 22.3 g/800 ml. CO₂ sparging into normal cultures with or without pH control did not significantly increase the amount of acetate produced but yields, in terms of amounts of glucose consumed, were higher than without sparging. The theoretical yield was almost obtained in pH-controlled, electrodialysis cultures with CO₂ sparging.The authors are with the Department of Applied Microbial Technology, Kumamoto Institute of Technology, Ikeda 4-22-1, Kumamoto 860, Japan     

Some growth peculiarities and membrane characteristics of probiotic strains of Escherichia coli

It is found that the probiotic strains of Escherichia coli, G35 N 59 isolated from “Okarin” and from “ASAP” drug formulas, and the commensal strain 5–1 isolated from healthy human intestine, manifest higher specific growth rates, lower acidifying capacity during glucose fermentation in the external medium, and lower rates of decrease in redox potential in comparison with the wild-type strain (MC4100). At the same time, despite similar values of their membrane potentials, these bacteria differ essentially in total and N,N′-dicyclohexylcarbodiimide-sensitive rates of energy-dependent transmembrane H⁺ and K⁺ transport and display a low level of H₂ production. It is suggested that the difference between their membrane characteristics reflects changes in the activity of proton-translocating F₀F₁-ATPase and is crucial for bacterial growth and probiotic activity of E. coli.     

Physiological effects of the addition of n-dodecane as an oxygen vector during steady-state Bacillus licheniformis thermophillic fermentations perturbed by a starvation period or a glucose pulse

The effect of the presence of n-dodecane as a potential oxygen vector during oxygen-limited continuous cultures of a Bacillus strain was studied, under extreme nutrient supply conditions: glucose excess, limitation and starvation. The addition of n-dodecane to the aqueous phase of a mechanically agitated and aerated fermentation increased the k_La by up to 35%. The n-dodecane additions to Bacillus licheniformis cells during starvation (oxygen limitation with concomitant glucose starvation) caused a severe detrimental progressive change in cell physiological state with respect to cytoplasmic membrane polarisation and permeability which was mitigated against by alleviating either the oxygen limitation (by increasing the mean energy dissipation rate or by the addition of n-dodecane as an oxygen vector) or by alleviating the carbon limitation (by resuming the carbon feed or by the addition of a glucose pulse). Further that during periods of excess glucose (glucose pulse) a much higher k_La was required to prevent the onset of anaerobic mixed acid fermentation than could be provided by the addition of n-dodecane alone. n-Dodecane can be used to increase the k_La when added in sufficient quantities to the aqueous phase of a mechanically agitated and aerated bioreactor but the magnitude of this increase is process and vessel geometry specific.     

Control of Flavor Development in Wine during and after Malolactic Fermentation by Oenococcus oeni

During malolactic fermentation in wine by Oenococcus oeni, the degradation of citric acid was delayed compared to the degradation of malic acid. The maximum concentration of diacetyl, an intermediary compound in the citric acid metabolism with a buttery or nutty flavor, coincided with the exhaustion of malic acid in the wine. The maximum concentration of diacetyl obtained during malolactic fermentation was strongly dependent on the oxygen concentration and the redox potential of the wine and, to a lesser extent, on the initial citric acid concentration. The final diacetyl concentration in the wine was also dependent on the concentration of SO₂. Diacetyl combines rather strongly with SO₂ (K_f = 7.2 × 10³ M⁻¹ in 0.1 M malate buffer [pH 3.5] at 30°C). The reaction is exothermic and reversible. If the concentration of SO₂ decreases during storage of the wine, the diacetyl concentration increases again.     

Overproduction of poly(β-malic acid) (PMA) from glucose by a novel Aureobasidium sp. P6 strain isolated from mangrove system

After over 100 strains of Aureobasidium spp isolated from mangrove system were screened for their ability to produce poly(β-malic acid) (PMA), it was found that Aureobasidium sp. P6 strain among them could produce high level of Ca²⁺-PMA. Fourteen percent glucose and 6.5 % CaCO₃ in the medium were the most suitable for Ca²⁺-PMA production. Then, 100.7 g/l of Ca²⁺-PMA was produced using Aureobasidium sp. P6 strain within 168 h at flask level. During 10-l batch fermentation, when the medium contained 12.0 % glucose, 98.7 g/l of Ca²⁺-PMA in the culture and 14.7 g/l of cell dry weight were obtained within 156 h, leaving 0.34 % reducing sugar in the fermented medium. When glucose concentration in the fermentation medium was 14.0 %, 118.3 g/l of Ca²⁺-PMA in the culture and 16.4 g/l of cell dry weight were obtained within 168 h, leaving 0.4 % reducing sugar in the fermented medium. After purification of Ca²⁺-PMA from the culture and acid hydrolysis of the pure Ca²⁺-PMA, analysis of HPLC showed that Aureobasidium sp. P6 strain only produced two main components of Ca²⁺-PMA and minor amount of calcium malate and that the hydrolysate of PMA was mainly composed of calcium malate. This is the first time to report that the novel yeast strain Aureobasidium sp. P6 strain isolated from the mangrove systems can produce such high amount of Ca²⁺-PMA.     

Microbial production of a biofuel (acetone–butanol–ethanol) in a continuous bioreactor: impact of bleed and simultaneous product removal

Acetone butanol ethanol (ABE) was produced in an integrated continuous one-stage fermentation and gas stripping product recovery system using Clostridium beijerinckii BA101 and fermentation gases (CO₂ and H₂). In this system, the bioreactor was fed with a concentrated sugar solution (250–500 g L^?1 glucose). The bioreactor was bled semi-continuously to avoid accumulation of inhibitory chemicals and products. The continuous system was operated for 504 h (21 days) after which the fermentation was intentionally terminated. The bioreactor produced 461.3 g ABE from 1,125.0 g total sugar in 1 L culture volume as compared to a control batch process in which 18.4 g ABE was produced from 47.3 g sugar. These results demonstrate that ABE fermentation can be operated in an integrated continuous one-stage fermentation and product recovery system for a long period of time, if butanol and other microbial metabolites in the bioreactor are kept below threshold of toxicity.     

The effect of salts in fermenting mashes on the microbiological assay ofl-lysine

During a study of the effects of high concentrations of NaCl, NaNO₃ and KC1 on the production of lysine bySaccharomyces cerevisiae during the fermentation of glucose (Richmond 1980) it was learned that amounts of salt greater than 0.6 M in the microbiological assay sample could change the apparent concentration of lysine in the sample. This could be corrected by adding to the lysine assay broth sufficient salt to match the concentration in the sample tube and then developing a revised standard curve. The additional salt, in turn, required that the microbiological assay time be lengthened.     

Three-liquid-phase extraction of diosgenin and steroidal saponins from fermentation of Dioscorea zingibernsis C. H. Wright

Diosgenin is an important starting material in the steroidal hormone industry. The yield of diosgenin obtained from the fermentation of Dioscorea zingibernsis C. H. Wright (DZW) by Trichoderma harzianum is higher than that typically obtained from acid hydrolysis. In this paper, the extraction of steroids in the culture broth was studied. A novel three-liquid-phase system (TLPS) consisted of petroleum ether, ethanol, ammonium sulphate and water was used to separate diosgenin and steroidal saponins in the culture broth. The partition behaviors of various steroidal saponins, diosgenin and glucose were investigated. From this, an optimized TLPS was obtained, which composed of 30% ethanol (w/w), 17% (NH₄)₂SO₄ (w/w) and 40% (w/w) petroleum ether. In the optimized TLPS, almost all of the diosgenin was extracted into the top phase giving a recovery of 97.24%, whereas the steroidal saponins were mainly extracted into the middle phase, with recoveries of zingibernsis newsaponin, deltonin and diosgenin-diglucoside reaching almost 100%. The recoveries of trillin and diosgenin-triglucoside were 96.03% and 98.82%, respectively. Glucose tended to remain in the bottom phase, giving a recovery of 72.01%. The three-liquid-phase extraction (TLPE) successfully resulted in the simultaneous separation of diosgenin, untransformed steroidal saponins and glucose.     

Production of Cellobionate from Cellulose Using an Engineered Neurospora crassa Strain with Laccase and Redox Mediator Addition

We report a novel production process for cellobionic acid from cellulose using an engineered fungal strain with the exogenous addition of laccase and a redox mediator. A previously engineered strain of Neurospora crassa (F5∆ace-1∆cre-1∆ndvB) was shown to produce cellobionate directly from cellulose without the addition of exogenous cellulases. Specifically, N. crassa produces cellulases, which hydrolyze cellulose to cellobiose, and cellobiose dehydrogenase (CDH), which oxidizes cellobiose to cellobionate. However, the conversion of cellobiose to cellobionate is limited by the slow re-oxidation of CDH by molecular oxygen. By adding low concentrations of laccase and a redox mediator to the fermentation, CDH can be efficiently oxidized by the redox mediator, with in-situ re-oxidation of the redox mediator by laccase. The conversion of cellulose to cellobionate was optimized by evaluating pH, buffer, and laccase and redox mediator addition time on the yield of cellobionate. Mass and material balances were performed, and the use of the native N. crassa laccase in such a conversion system was evaluated against the exogenous Pleurotus ostreatus laccase. This paper describes a working concept of cellobionate production from cellulose using the CDH-ATBS-laccase system in a fermentation system.