Co-production of biomass and metabolites by cell retention culture of <Emphasis Type="Italic">Leuconostoc citreum</Emphasis>

Cell retention culture of lactic acid bacterium Leuconostoc citreum was carried out in a fermentor equipped with an internal ceramic filtration system to co-produce biomass and metabolites. The filtration system was composed of porous ceramic filter module with pore size of 0.1 μm and total surface area of 330 cm². High cell density cultivation of L. citreum was achieved within the fermentor, while extracellular metabolites such as mannitol and d-lactic acid were produced through the filter with high productivities. In batch culture of L. citreum using a medium containing 50 g/L of glucose and 100 g/L of fructose, the maximum optical density (OD) monitored at 660 nm was 13 with 65 g/L of mannitol and 38 g/L of lactic acid. In cell retention culture of L. citreum with dilution rate of 0.07 h⁻¹, OD increased to 75, which was 6 times higher than that in batch culture. The concentrations of mannitol and lactic acid increased to 85 and 45 g/L, respectively, and were maintained throughout the cultivation to 105 h. By increasing dilution rate to 0.13 h⁻¹, the productivities of mannitol and lactic acid increased to 8.5 and 4.2 g/L/h, respectively, which were 2.7 to 3 times higher than those in batch culture, suggesting that cell retention culture using internal filtration system is highly effective for co-production of useful cell biomass and various extracellular metabolites.     

Performance of a two-stage fermentor with cell recycle for continuous production of lactic acid

The performasnce of a recycle two-stage fermentor with cell separators after each stage is analyzed numerically for continuous production of lactic acid. In this system, the bleed broth withdrawn from the first stage is provided to the second fermentor to reuse viable cells in the bleed. Biological rate expressions and parametric values are taken from the literature. The effects of operating parameters on the concentrations of total and viable cells, substrate and product in each stage, the lactic acid productivity and the substrate conversion are examined and discussed. With respect to overall productivity and conversion, it is found that the present fermentor system is more efficient than a conventional chemostat fermentor with cell recycle.     

Effects of the ionophores monensin and tetronasin on simulated development of ruminal lactic acidosis in vitro.

A continuous coculture of four ruminal bacteria, Megasphaera elsdenii, Selenomonas ruminantium, Streptococcus bovis, and Lactobacillus sp. strain LB17, was used to study the effects of the ionophores monensin and tetronasin on the changes in ruminal microbial ecology that occur during the onset of lactic acidosis. In control incubations, the system simulated the development of lactic acidosis in vivo, with an initial overgrowth of S. bovis when an excess of glucose was added to the fermentor. Lactobacillus sp. strain LB17 subsequently became dominant as pH fell and lactate concentration rose. Both ionophores were able to prevent the accumulation of lactic acid and maintain a healthy non-lactate-producing bacterial population when added at the same time as an excess of glucose. Tetronasin was more potent in this respect than monensin. When tetronasin was added to the culture 24 h after glucose, the proliferation of lactobacilli was reversed and a non-lactate-producing bacterial population developed, with an associated drop in lactate concentration in the fermentor. Rises in culture pH and volatile fatty acid concentrations accompanied these changes. Monensin was unable to suppress the growth of lactobacilli; therefore, in contrast to tetronasin, monensin added 24 h after the addition of glucose failed to reverse the acidosis. Numbers of lactobacilli and lactate concentrations remained high, whereas pH and volatile fatty acid concentrations were low.     

Continuous cultivation ofLactobacillus rhamnosus with cell recycling using an acoustic cell settler

Continuous production of lactic acid from glucose byLactobacillus rhamnosus with cell recycling using an acoustic cell settler was carried out. The performance of the system, such as the concentration of cell and product were compared with the control experiment without recycling. The acoustic settler showed cell separation efficiency of 67% during the continuous operation and the cell concentration in the fermentor with recycle exceeded that of the control by 29%. Compared with the control, lactic acid production was increased by 40%, while glucose consumption was only increased by 8%. The higher value of lactic acid production to substrate consumption (Y _P/S, product yield coefficient) achieved by cell recycling is interpreted to indicate that the recycled cell mass consumes less substrate to produce the same amount of product than the control. Within system environmental changes due to the longer mean cell residence time induced the cells maintaining the metabolic pathways to produce less by-product but more product, lactic acid.     

Effects of the ionophores monensin and tetronasin on simulated development of ruminal lactic acidosis in vitro

A continuous coculture of four ruminal bacteria, Megasphaera elsdenii, Selenomonas ruminantium, Streptococcus bovis, and Lactobacillus sp. strain LB17, was used to study the effects of the ionophores monensin and tetronasin on the changes in ruminal microbial ecology that occur during the onset of lactic acidosis. In control incubations, the system simulated the development of lactic acidosis in vivo, with an initial overgrowth of S. bovis when an excess of glucose was added to the fermentor. Lactobacillus sp. strain LB17 subsequently became dominant as pH fell and lactate concentration rose. Both ionophores were able to prevent the accumulation of lactic acid and maintain a healthy non-lactate-producing bacterial population when added at the same time as an excess of glucose. Tetronasin was more potent in this respect than monensin. When tetronasin was added to the culture 24 h after glucose, the proliferation of lactobacilli was reversed and a non-lactate-producing bacterial population developed, with an associated drop in lactate concentration in the fermentor. Rises in culture pH and volatile fatty acid concentrations accompanied these changes. Monensin was unable to suppress the growth of lactobacilli; therefore, in contrast to tetronasin, monensin added 24 h after the addition of glucose failed to reverse the acidosis. Numbers of lactobacilli and lactate concentrations remained high, whereas pH and volatile fatty acid concentrations were low.     

High cell density culture of a recombinant Escherichia coli producing penicillin acylase in a membrane cell recycle fermentor

A recombinant Escherichia coli HB101(pPAKS2) producing penicillin acylase was cultured in a membrane cell recycle fermentor. The strain was very stable throughout the whole experiment. The main inhibitory by-product was acetic acid, and cell growth ceased when its concentration was above 14 g/L Cell density could be increased up to 145 g/L dry weight without experiencing by-product inhibition by regulating glucose concentration in the fermentor and by using total membrane recycle. Acetic acid formation was negligible not only when cells were cultured in medium containing no glucose but also when glucose was limited. Dissolved oxygen control as well as glucose limitation was an indispensable condition for minimizing acetic acid formation when the medium contained glucose. Low concentrations of accumulated acetic acid were reused when glucose was limited. Use of highly concentrated medium reduced the membrane surface area required for cell recycle greatly. The recycle fermentor could be operated in various operational modes including partial bleed and repeated recycle culture to give high productivity. Productivity of a repeated recycle system was over 10 times higher than that of a simple batch system.     

米根霉发酵生产L-乳酸

报道了Ｌ－乳酸菌株的分离与筛选,探讨了不同碳源、氮源、通气量、温度等发酵条件对产Ｌ－乳酸的影响,从７８株米根霉中筛选出１３株产Ｌ－乳酸较高的菌株,其中米根霉（Ｒｈｉｚｏｐｕｓ ｏｒｙｚａｅ）Ｒｓ９２８产Ｌ－乳酸最高,产酸最稳定。试验结果表明,该菌株最适发酵培养组成（％）：淀粉水解糖１６,ＭｇＳＯ４ ０．０８,ＫＨ２ＰＯ４ ０．０５,ＺｎＳＯ４ ０．０１,ＣａＣＯ３ ７,ｐＨ自然。在６０ｔ发酵罐中,     

Direct fermentation of starch to lactic acid byLactobacillus amylovorus

Summary Fermentation production of lactic acid directly from starch was studied in a batch fermentor usingLactobacillus amylovorus. At an initial concentration of 120 g/L starch, 96.2 g/L of lactic acid was produced from liquefied starch in 20 hours while 92.5 g/L of lactate was produced from the raw starch in 39 hours. High initial glucose levels (100 g/L) in the medium inhibited the organism, unless it had been adapted by growing it in a low-glucose medium. The direct production of lactic acid from starch could reduce overall production costs significantly.     

Inhibitory effects of H2 on growth of Clostridium cellobioparum.

Hydrogen inhibits the growth of hydrogen-producing Clostridium cellobioparum, but not of Escherichia coli or Bacteroides ruminicola. The inhibition is reversible. When hydrogen was removed either by palladium black or by gassing out the tube, glucose utilization increased as did optical density and hydrogen production of C. cellobioparum. Removal of the H2 by methanogenic bacteria favors the growth of C. cellobioparum. Grown with Methanobacterium ruminantium in various concentrations of glucose, the Clostridium reaches a higher optical density and produces more H2 and a higher viable cell count. The cell yield is also higher than in pure culture. In mixed culture, C. cellobioparum produces more acetic acid and less lactic acid, ethanol, and butyric acid than in pure culture. The significance of this metabolic shift and hydrogen utilization in methanogenesis is discussed.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from a mixture of xylose and glucose by co-cultivation of lactic acid bacteria

The production of optically pure lactic acid in a high yield from xylose or a mixture of xylose and glucose, which is a model hydrolysate of lignocellulose, is described. In a single cultivation, Enterococcus casseliflavus produced 38 g/l of lactic acid with an optical purity of 96% enantiomeric excess (ee) and 6.4 g/l of acetic acid from 50 g/l of xylose when MRS medium was used. When a mixture of 50 g/l of xylose and 100 g/l of glucose was used as the carbon source in a cultivation of E. casseliflavus alone, glucose was converted to lactic acid in the early phase of the cultivation but xylose was hardly consumed. In a co-cultivation where E. casseliflavus and Lactobacillus casei specific for glucose were simultaneously inoculated, little or no lactic acid was produced after the glucose was almost consumed. A co-cultivation with two-stage inoculation (in which E. casseliflavus was added at a cultivation time of 40 h after L. casei cells were inoculated) resulted in complete consumption of 50 g/l of xylose and 100 g/l of glucose. In the co-cultivation, 95 g/l of lactic acid with a high optical purity of 96% ee was obtained at 192 h. Such a co-cultivation using two microorganisms specific for each sugar is considered to be one promising cultivation technique for the efficient production of lactic acid from a sugar mixture derived from lignocellulose.     

昆虫细胞(Sf9)培养中葡萄糖、乳酸的影响

昆虫细胞培养已经在小儿灰髓炎、乙肝表面抗原等研究中得到系统应用,此外,许多高值的治疗性蛋白药物,如tPA、白细胞介素-2、β-干扰素和促红细胞生成素等的研究过程中昆虫细胞及杆状病毒的培养已成为新的生物工程手段。在美国、荷兰等国已成功地得到了外源基因大量表达的药物。在我国也已成功构建了人-α干扰素的昆虫细胞/杆状病毒表达系统。同时昆虫杆状病毒本身可以制备成各种专一性较强的广谱、无公害、无毒性的的农用杀虫剂。但是昆虫细胞及其杆状病毒的大规模培养对     

Production of L(+)-lactic acid from glucose and starch by immobilized cells of Rhizopus oryzae in a rotating fibrous bed bioreactor

A rotating fibrous-bed bioreactor (RFB) was developed for fermentation to produce L(+)-lactic acid from glucose and cornstarch by Rhizopus oryzae. Fungal mycelia were immobilized on cotton cloth in the RFB for a prolonged period to study the fermentation kinetics and process stability. The pH and dissolved oxygen concentration (DO) were found to have significant effects on lactic acid productivity and yield, with pH 6 and 90% DO being the optimal conditions. A high lactic acid yield of 90% (w/w) and productivity of 2.5 g/L.h (467 g/h.m(2)) was obtained from glucose in fed-batch fermentation. When cornstarch was used as the substrate, the lactic acid yield was close to 100% (w/w) and the productivity was 1.65 g/L.h (300 g/h.m(2)). The highest concentration of lactic acid achieved in these fed-batch fermentations was 127 g/L. The immobilized-cells fermentation in the RFB gave a virtually cell-free fermentation broth and provided many advantages over conventional fermentation processes, especially those with freely suspended fungal cells. Without immobilization with the cotton cloth, mycelia grew everywhere in the fermentor and caused serious problems in reactor control and operation and consequently the fermentation was poor in lactic acid production. Oxygen transfer in the RFB was also studied and the volumetric oxygen transfer coefficients under various aeration and agitation conditions were determined and then used to estimate the oxygen transfer rate and uptake rate during the fermentation. The results showed that the oxygen uptake rate increased with increasing DO, indicating that oxygen transfer was limited by the diffusion inside the mycelial layer.     

Glucose utilization, pH reduction and density dependent inhibition in cultures of chick embryo fibroblasts.

The multiplication rate of sparse cultures of chick embryo cells is only slightly lower at pH 6.9 than at pH 7.4. There is, however, a marked reduction in the multiplication rate of the pH 6.9 cultures before they reach confluency. Cultures at pH 7.4 continue to multiply beyond confluency with only a slight decrease in the multiplication rate. Eighty to ninety percent of the glucose taken up by the cells growing at each pH is converted to lactic acid which is released into the medium. Metabolic reduction in pH of the medium is almost entirely accounted for by the amount of lactic acid produced by the cells. Neither the intracellular nor extracellular accumulation of lactic acid nor the accompanying reduction in pH is sufficient to explain density dependent inhibition of the rate of multiplication of chick cells. The rate of lactic acid production and the multiplication rate of chick cells are independent of glucose concentration in the range of 2--16 mM. In view of the kinetic parameters for the uptake of glucose, this shows that glycolysis is not limited by the rate of glucose uptake and that depletion of glucose from the medium cannot account for the onset of density dependent inhibition of multiplication. However, when cells reach very high population densities, conventional glucose concentrations of 5 mM can be depleted overnight by chick cells. Since the multiplication rate of cells is dependent on glucose concentration when it falls below 2 mM, depletion of glucose may cause some growth inhibition in crowded cultures supplied with conventional medium.     

Liquid phase volumetric mass transfer coefficient in dairy effluent stream

The effluent from a dairy cold storage plant was studied for the levels of dissolved oxygen saturation. The effluent to the aerobic digester mainly contains lactose, milk fat, protein and lactic acid. The study was conducted at five different temperatures in a two litre laboratory fermentor. The volumetric liquid phase mass transfer coefficient was correlated to temperature with an average absolute deviation of 6.2%.     

在不同碳源培养条件下酿酒酵母的蛋白质组解析

为了分析酿酒酵母在不同培养条件下的代谢调控过程的差异,采用固相pH梯度-SDS聚丙烯酰胺双向凝胶电泳对其利用不同碳源时细胞的总蛋白进行了分离,银染显色,使用2D蛋白质图像分析系统Image Master-2D Elite对双向电泳图谱进行分析,查询SWISS-2D-PAGE蛋白质组数据库,识别了约500个蛋白质点。对与糖酵解途径、磷酸戊糖途径、三羧酸循环和几种回补反应相关的大部分关键的蛋白质进行了差异分析。探讨了酿酒酵母利用不同碳源时及生长的不同阶段代谢机理的变化和在蛋白质水平的调控。     

Batch fermentation of whey ultrafiltrate by Lactobacillus helveticus for lactic acid production

Summary Cheese whey ultrafiltrate (WU) was used as the carbon source for the production of lactic acid by batch fermentation with Lactobacillus helveticus strain milano. The fermentation was conducted in a 400 ml fermentor at an agitation rate of 200 rpm and under conditions of controlled temperature (42° C) and pH. In the whey ultrafiltrate-corn steep liquor (WU-CSL) medium, the optimal pH for fermentation was 5.9. Inoculum propagated in skim milk (SM) medium or in lactose synthetic (LS) medium resulted in the best performance in fermentation (in terms of growth, lactic acid production, lactic acid yield and maximum productivity of lactic acid), as compared to that propagated in glucose synthetic (GS) medium. The yeast extract ultrafiltrate (YEU) used as the nitrogen/growth factor source in the WU medium at 1.5% (w/v) gave the highest maximum productivity of lactic acid of 2.70 g/l-h, as compared to the CSL and the tryptone ultrafiltrate (TU). L. helveticus is more advantageous than Streptococcus thermophilus and Lactobacillus delbrueckii for the production of lactic acid from WU. The L. helveticus process will provide an alternative solution to the phage contamination in dairy industries using Lactobacillus bulgaricus.     

Microbial production of d‐lactic acid from dried distiller's grains with solubles

d ‐Lactic acid production is gaining increasing attention due to the thermostable properties of its polymer, poly‐d ‐lactic acid . In this study, Lactobacillus coryniformis subsp. torquens, was evaluated for its ability to produce d ‐lactic acid using Dried Distiller's Grains with Solubles (DDGS) hydrolysate as the substrate. DDGS was first subjected to alkaline pretreatment with sodium hydroxide to remove the hemicellulose component and the generated carbohydrate‐rich solids were then subjected to enzymatic hydrolysis using cellulase mixture Accellerase® 1500. When comparing separate hydrolysis and fermentation and simultaneous saccharification and fermentation (SSF) of L. coryniformis on DDGS hydrolysate, the latter method demonstrated higher d ‐lactic acid production (27.9 g/L, 99.9% optical purity of d ‐lactic acid), with a higher glucose to d ‐lactic acid conversion yield (84.5%) compared to the former one (24.1 g/L, 99.9% optical purity of d ‐lactic acid). In addition, the effect of increasing the DDGS concentration in the fermentation system was investigated via a fed‐batch SSF approach, where it was shown that the d ‐lactic acid production increased to 38.1 g/L and the conversion yield decreased to 70%. In conclusion, the SSF approach proved to be an efficient strategy for the production of d ‐lactic acid from DDGS as it reduced the overall processing time and yielded high d ‐lactic acid concentrations.     

Kinetic studies of the lactic acid fermentation in batch and continuous cultures

The fermentation kinetics of the homofermentative organism Lactobacillus delbrueckii in a glucose-yeast extract medium is studied in both batch and continuous culture under conditions of controlled pH. From a graphical analysis of the batch data, a mathematical model of the process is derived which relates bacterial growth, glucose utilization, and lactic acid formation. The parameters in the model represent the activity of the organism and are a function of pH, having a maximum value at about 5.90. In a continuous stirred tank fermentor (CSTF), the effect of pH, feed concentration, and residence time is observed. The feed medium is a constant ratio of two parts glucose to one part yeast extract plus added mineral salts. An approximate prediction of the steady-state behavior of the CSTF can be made using a method based on the kinetic model derived for the batch case. In making step changes from one steady state to another, the transient response is observed. Using the kinetic model to simulate the transient period, the calculated behavior qualitatively predicts the observed response.     

Extractive lactic acid fermentation using ion-exchange resin

Lactic acid fermentation is an end-product-inhibited reaction. The restriction imposed by lactic acid on its fermentation can be avoided by extractive fermentation techniques. Studies were performed by attaching an ion-exchange resin packed column with a 2-L fermentor for separation of lactic acid. The fermentation, in a conventional batch mode, resulted in a lactic acid yield of 0.828 g . g(-1) and a lactic acid productivity of 0.313 g . L(-1) . h(-1). However, these could be further enhanced to 0.929 g . g(-1) and 1.665 g . L(-1) . h(-1) by extractive fermentation techniques. The effect of temperature on extractive fermentation was remarkable and has been included in this work.     

Effect of Corn steep liquor supplementation and scale up on Lactococcus starter production

Summary Three Lactococcus strains (Lactococcus ssp. lactis var. diacetylactis, Lactococcus ssp. lactis cremoris and Lactococcus ssp. lactis var. lactis) isolated from the Tunisian lben were grown at constant pH on CSL medium in stirred fermentors for lactic starters production. The agitation required to homogenate alkali used to pH control should be low because it affects the Lactococcus growth. Scale up from 20-liter fermentor to 400-liter fermentor was carried out at constant impeller tip speed below 150 cm s^у. The CSL supplementation and fed-batch with glucose increased the yield in the upper 10¹⁰ cfu/ml. The consumed glucose during fermentation was converted into lactic acid and cell. Before fed-batch, the maximum specific growth rate of Lactococcus ssp. lactis var. diacetylactis was around 1 h^у and the number of cells increased 20 to 40 times according to inoculum size. After fed-batch, the glucose consumption rate remains constant but specific growth rate decreased and number of cell trebled only.