The effect of yeast extract supplementation on the production of lactic acid from whey permeate byLactobacillus helueticus

Summary Batch and continuous two-stage cultures have been conducted in order to determine the effect of yeast extract (YE) on the homolactic fermentation of whey permeate byLactobacillus helveticus. Supplementation with YE had a significant effet on lactic acid concentration, volumetric productivity, and substrate conversion, but not on lactic acid yield. Volumetric productivity in the first stage increased from 2 to 9 g l^–1 per hour by increasing the YE concentration from 1.5 to 25 g l^–1 At the same time conversion improved from 22% to 93% at a dilution rate of 0.2 h^–1. The second stage demonstrated the effect of YE at a lower dilution rate (0.14 h^–1. A high system conversion (97%) and a high final lactic acid concentration (40 g l^–1) were achieved with 10 g l^–1 YE.     

Lactic acid fermentation by Lactobacillus casei in free cell form and immobilised on gluten pellets

A comparative study of the fermentation of a range of carbohydrate substrates, at various temperatures, was carried out using a commercial Lactobacillus casei strain in a free cell form and immobilised on gluten pellets. This strain required yeast extract, l-cysteine HCl and Mn²⁺ at 5, 0.5 and 0.1 g l^–1, respectively, for maximum growth and lactic acid production. Sugar fermentation using free cells showed preference in the order glucose, sucrose, fructose while lactose was poorly utilised. Optimum temperature for growth and lactic acid production over (18–30 h) was 43 °C. L. casei was successfully immobilised on gluten pellets and fermented glucose and sucrose in a shorter time (18 h) with increased lactic acid production (42 and 41 g l^–1 on glucose and sucrose, respectively).     

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.     

Optimization of lactic acid production from beet molasses by Lactobacillus delbrueckii NCIMB 8130

Production of lactic acid from beet molasses by Lactobacillus delbrueckii NCIMB 8130 in static and shake flask fermentation was investigated. Shake flasks proved to be a better fermentation system for this purpose. Substitution of yeast extract with other low cost protein sources did not improve lactic acid production. The maximum lactic acid concentration was achieved without treatment of molasses. A Central Composite Design was employed to determine the maximum lactic acid concentration at optimum values for the process variables (sucrose, yeast extract, CaCO₃). A satisfactory fit of the model was realized. Lactic acid production was significantly affected both by sucrose–yeast extract and sucrose–CaCO₃ interactions, as well as by the negative quadratic effects of these variables. Sucrose and yeast extract had a linear effect on lactic acid production while the CaCO₃ had no significant linear effect. The maximum lactic acid concentration (88.0 g/l) was obtained at concentrations for sucrose, yeast extract and CaCO₃ of 89.93, 45.71 and 59.95 g/l, respectively.     

Synthesis of recombinant human interleukin-2 via controlled feed of lactose-complex media in fed-batch cultures of Escherichia coli BL21(DE3)[pT7-G3IL2]

Using lactose as an inducer, recombinant human interleukin-2 (rhIL-2) was synthesized with an N-terminus fusion partner, G3 (three tandem-arranged glucagon peptides) in fed-batch cultures at high cell concentration (60–90 g l^–1) of Escherichia coli BL21(DE3) [pT7-G3IL2]. With batch additions of lactose (4 × 13.5 g), the fusion rhIL-2 was synthesized up to 9.3 g l^–1. However, if all the lactose (54 g) was added at once to the culture, synthesized fusion rhIL-2 decreased to 5.4 g l^–1 with a decreased cell growth rate. A statistical optimization of the production medium containing glucose, yeast extract, and lactose led to fusion rhIL-2 being produced at > 9 g l^–1.     

Mixed-acid fermentation and polysaccharide production by Lactobacillus helveticus in milk cultures

Lactobacillus helveticus grown in milk with pH control at 6.2 had a slower growth rate (=0.27 h^–1) and produced less exopolysaccharide (49 mg l^–1) but increased lactic acid production (425 mM) compared to cultures without pH control (=0.5 h^–1, 380 mg exopolysaccharide l^–1, and 210 mM lactate), respectively. Both cultures displayed a mixed-acid fermentation with formation of acetate, which is linked not only to citrate metabolism, but also to alternative pathways from pyruvate.     

Inhibition of yeast by lactic acid bacteria in continuous culture: nutrient depletion and/or acid toxicity?

Lactic acid was added to batch very high gravity (VHG) fermentations and to continuous VHG fermentations equilibrated to steady state with Saccharomyces cerevisiae. A 53% reduction in colony-forming units (CFU) ml^–1 of S. cerevisiae was observed in continuous fermentation at an undissociated lactic acid concentration of 3.44% w/v; and greater than 99.9% reduction was evident at 5.35% w/v lactic acid. The differences in yeast cell number in these fermentations were not due to pH, since batch fermentations over a pH range of 2.5–5.0 did not lead to changes in growth rate. Similar fermentations performed in batch showed that growth inhibition with added lactic acid was nearly identical. This indicates that the apparent high resistance of S. cerevisiae to lactic acid in continuous VHG fermentations is not a function of culture mode. Although the total amount of ethanol decreased from 48.7 g l^–1 to 14.5 g l^–1 when 4.74% w/v undissociated lactic acid was added, the specific ethanol productivity increased ca. 3.2-fold (from 7.42×10^–7 g to 24.0×10^–7 g ethanol CFU^–1 h^–1), which indicated that lactic acid stress improved the ethanol production of each surviving cell. In multistage continuous fermentations, lactic acid was not responsible for the 83% (CFU ml^–1) reduction in viable S. cerevisiae yeasts when Lactobacillus paracasei was introduced to the system at a controlled pH of 6.0. The competition for trace nutrients in those fermentations and not lactic acid produced by L. paracasei likely caused the yeast inhibition.     

Fed-batch fermentation of Lactobacillus lactis for hyper-production of l-lactic acid

A fed-batch fermentation of Lactobacillus lactis to produce l-lactic acid was developed in which the residual glucose concentration in the culture was used to control a continuous feeding strategy. Up to 210 g l-lactic acid l^–1 (97% yield) was obtained. The maximal dry cell was 2.7 g l^–1 and the average l-lactic acid productivity was 2.2 g l^–1 h^–1.     

Influence of an initial addition of lactic acid on growth, acid production and their coupling for batch cultures of Lactobacillus helveticus

Growth and production coupling for L. helveticus growing at constant pH?on a medium largely supplemented with yeast extract and peptons has been examined as a function of initial lactic acid addition: these conditions allowed to avoid side effects of cultivation pH?and nitrogen source deficiency on coupling. Growth of L. helveticus strain milano was reduced by half for a free lactic acid concentration of 0.34?g.l^?1; both growth and production were fully inhibited for a critical end-product concentration of 83?g.l^?1, despite the fact that lactose was still available. The extent of autolysis 8?h after growth ceased was practically independent of initial lactic acid concentration: the same conclusion held for the part played by a growth-associated mechanism in total acid production. During the slowing down phase of growth, production was non-growth-associated: production rate remained close to its maximal value, while growth rate declined.     

Lactic acid production by aggregated continuous cultures of Lactobacillus acidophilus under aerobic conditions

Summary The ability of Lactobacillus acidophilus to aggregate, to produce lactic acid for a long term continuous fermentation process and to exist as aggregate cell cultures in a gas-lift reactor under aerobic conditions was studied. The main product of fermentation was lactic acid and only the traces of other end-products were determined. The highest fermentation efficiency of lactic acid was 98.6% and the highest productivity was 9.6 g.l^–1.h^–1 of lactic acid.     

Influence of growth supplements on lactic acid production in whey ultrafiltrate by Lactobacillus helveticus

Summary Investigations have been carried out on lactic acid production by Lactobacillus helveticus CNRZ 303 in whey ultrafiltrate. Addition of beet molasses was investigated with good results, although yeast extract proved to be more effective. The size of inoculum and the preculture medium also played a significant role in determining the amount of lactic acid produced during the fermentation process. High lactose consumption (94.09%), together with good lactic acid production (26.09 g/l) and yield (0.90%), were obtained in whey ultrafiltrate supplemented with 1% (w/v) beet molasses (WUM), with a 10% (w/v) inoculum and peptonized milk as preculture medium. Although these results were similar to those obtained when yeast extract was used as supplement, the maximum volumetric productivities proved to be quite different, and were definitely higher with yeast extract. Offprint requests to: L. Chiarini     

Fermentative production of lactic acid from biomass: an overview on process developments and future perspectives

The concept of utilizing excess biomass or wastes from agricultural and agro-industrial residues to produce energy, feeds or foods, and other useful products is not necessarily new. Recently, fermentation of biomass has gained considerable attention due to the forthcoming scarcity of fossil fuels and also due to the necessity of increasing world food and feed supplies. A cost-effective viable process for lactic acid production has to be developed for which several attempts have been initiated. Fermentation techniques result in the production of either d (−) or l (+) lactic acid, or a racemic mixture of both, depending on the type of organism used. The interest in the fermentative production of lactic acid has increased due to the prospects of environmental friendliness and of using renewable resources instead of petrochemicals. Amylolytic bacteria Lactobacillus amylovorus ATCC 33622 is reported to have the efficiency of full conversion of liquefied cornstarch to lactic acid with a productivity of 20 g l⁻¹ h⁻¹. A maximum of 35 g l⁻¹ h⁻¹ was reported using a high cell density of L. helveticus (27 g l⁻¹) with a complete conversion of 55- to 60-g l⁻¹ lactose present in whey. Simultaneous saccharification and fermentation is proved to be best in the sense of high substrate concentration in lower reactor volume and low fermentation cost. In this review, a survey has been made to see how effectively the fermentation technology explored and exploited the cheaply available source materials for value addition with special emphasis on lactic acid production.     

Batch and repeated batch production of l(+)-lactic acid by Enterococcus faecalis RKY1 using wood hydrolyzate and corn steep liquor

Lactic acid production was investigated for batch and repeated batch cultures of Enterococcus faecalis RKY1, using wood hydrolyzate and corn steep liquor. When wood hydrolyzate (equivalent to 50 g l⁻¹ glucose) supplemented with 15–60 g l⁻¹ corn steep liquor was used as a raw material for fermentation, up to 48.6 g l⁻¹ of lactic acid was produced with, volumetric productivities ranging between 0.8 and 1.4 g l⁻¹ h⁻¹. When a medium containing wood hydrolyzate and 15 g l⁻¹ corn steep liquor was supplemented with 1.5 g l⁻¹ yeast extract, we observed 1.9-fold and 1.6-fold increases in lactic acid productivity and cell growth, respectively. In this case, the nitrogen source cost for producing 1 kg lactic acid can be reduced to 23% of that for fermentation from wood hydrolyzate using 15 g l⁻¹ yeast extract as a single nitrogen source. In addition, lactic acid productivity could be maximized by conducting a cell-recycle repeated batch culture of E. faecalis RKY1. The maximum productivity for this process was determined to be 4.0 g l⁻¹ h⁻¹.     

Production of xylitol in cell recycle fermentations of Candida tropicalis

Xylitol was produced a in two-substrate, batch fermentation with cell recycling of Candida tropicalis ATCC 13803. A series of cell-recycle experiments showed that the feeding of xylose, glucose and yeast extract in the xylitol production phase was most effective in enhancing xylitol productivity. The optimized cell recycle fermentation resulted in 0.82 g xylitol/g xylose yield, 4.94 g xylitol l^–1 h^–1 productivity, and final xylitol concentration of 189 g l^–1. These results were 1.3 times higher in volumetric xylitol productivity and 2.2 times higher in final product concentration compared with the corresponding values of the optimized two-substrate batch culture.     

Lactic acid production from cellulosic waste by immobilized cells of Lactobacillus delbrueckii

Industrial waste corn cob residue (from xylose manufacturing) without pretreatment was hydrolyzed by cellulase and cellobiase. The cellulosic hydrolysate contained 52.4 g l⁻¹ of glucose and was used as carbon source for lactic acid fermentation by cells of Lactobacillus delbrueckii ZU-S2 immobilized in calcium alginate gel beads. The final concentration of lactic acid and the yield of lactic acid from glucose were 48.7 g l⁻¹ and 95.2%, respectively, which were comparative to the results of pure glucose fermentation. The immobilized cells were quite stable and reusable, and the average yield of lactic acid from glucose in the hydrolysate was 95.0% in 12 repeated batches of fermentation. The suitable dilution rate of continuous fermentation process was 0.13 h⁻¹, and the yield of lactic acid from glucose and the productivity were 92.4% and 5.746 g l⁻¹ h⁻¹, respectively. The production of lactic acid by simultaneous saccharification and fermentation (SSF) process was carried out in a coupling bioreactor, the final concentration of lactic acid was 55.6 g l⁻¹, the conversion efficiency of lactic acid from cellulose was 91.3% and the productivity was 0.927 g l⁻¹ h⁻¹. By using fed-batch technique in the SSF process, the final concentration of lactic acid and the productivity increased to 107.6 g l⁻¹ and 1.345 g l⁻¹ h⁻¹, respectively, while the dosage of cellulase per gram substrate decreased greatly. This research work should advance the bioconversion of renewable cellulosic resources and reduce environmental pollution.     

Continuous lactic acid fermentation with concentrated product recovery by ultrafiltration and electrodialysis

Lactose of sweet whey permeate was converted into sodium lactate byLactobacillus helveticus. To increase the, productivity of the lactic acid fermentation and to reduce the amounts of effluents, the bioreactor was coupled with an ultrafiltration module and an electrodialysis unit. Without the electrodialyzer, with total cell recycling and at a dilution rate of 0.88 h^–1, a cellular concentration of 64 gl^–1 and a productivity of 22 gl^–1 h^–1 were obtained. When the electrodialysis unit is coupled, the outlet concentration of lactate was stabilized at 85±5 gl^–1.     

Influence of yeast extract concentrationon batch cultures of Lactobacillus helveticus: growth and production coupling

Lactobacillus helveticus was cultivated batchwise on whey permeate supplemented with 2–30g yeast extract l^-1. For low supplementation levels, growth was slow, and a long maintenance phase in the absence of any cell autolysis was observed. When the yeast extract concentration was increased, growth time increased slightly; under these circumstances, a large increase of maximum biomass concentration was recorded, indicating a clear nitrogen source starvation at low supplement concentration. At the same time the length of the maintenance phase decreased; for a 30gl^-1 supplementation, it vanished and a death phase was observed instead: this behaviour highlighted a shift from nitrogen to carbon source starvation. For more and more supplemented media, the final lactic acid concentration was constant, while fermentation time decreased significantly; a growth-associated production phase was followed by a maintenance production phase. The part played by the former mecha nism was under tight control of yeast extract concentration: for 30gl^-1 supplementation, 83% of total lactic acid was provided by a growth-linked production process.     

Optimization of probiotic and lactic acid production by Lactobacillus plantarum in submerged bioreactor systems

Biomass and lactic acid production by a Lactobacillus plantarum strain isolated from Serrano cheese, a microorganism traditionally used in foods and recognized as a potent probiotic, was optimized. Optimization procedures were carried out in submerged batch bioreactors using cheese whey as the main carbon source. Sequential experimental Plackett–Burman designs followed by central composite design (CCD) were used to assess the influence of temperature, pH, stirring, aeration rate, and concentrations of lactose, peptone, and yeast extract on biomass and lactic acid production. Results showed that temperature, pH, aeration rate, lactose, and peptone were the most influential variables for biomass formation. Under optimized conditions, the CCD for temperature and aeration rate showed that the model predicted maximal biomass production of 14.30 g l⁻¹ (dw) of L. plantarum. At the central point of the CCD, a biomass of 10.2 g l⁻¹ (dw), with conversion rates of 0.10 g of cell g⁻¹ lactose and 1.08 g lactic acid g⁻¹ lactose (w/w), was obtained. These results provide useful information about the optimal cultivation conditions for growing L. plantarum in batch bioreactors in order to boost biomass to be used as industrial probiotic and to obtain high yields of conversion of lactose to lactic acid.     

Production of poly(3-hydroxybutyrate) from whey by cell recycle fed-batch culture of recombinant Escherichia coli

A new fermentation strategy using cell recycle membrane system was developed for the efficient production of poly(3-hydroxybutyrate) (PHB) from whey by recombinant Escherichia coli strain CGSC 4401 harboring the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes. By cell recycle, fed-batch cultivation employing an external membrane module, the working volume of fermentation could be constantly maintained at 2.3 l. The final cell concentration, PHB concentration and PHB content of 194 g l^–1, 168 g l^–1 and 87%, respectively, were obtained in 36.5 h by the pH-stat cell recycle fed-batch culture using whey solution concentrated to contain 280 g lactose l^–1 as a feeding solution, resulting in a high productivity of 4.6 g PHB l^–1 h^–1.     

Generalized model of the effect of pH on lactate fermentation and citrate bioconversion in Lactococcus lactis ssp. Lactis biovar. diacetylactis

An aroma-imparting mesophilic lactic starter (Lactococcus lactis ssp. lactis biovar. diacetylactis) was studied in batch culture in medium with 50 g·l^–1 lactose and 2 g·l^–1 citrate. The effect of pH on the physiology of growth and the production of flavour compounds was investigated with a mathematical model. The specific rates of growth and of lactose fermentation obeyed a law of non-competitive inhibition by lactic acid produced, inhibition increasing as the pH of the medium decreased. The pH thus acted indirectly by increasing the proportion of non-dissociated lactic acid, identified as the inhibiting form of lactic acid. The generalized model, taking into account the effect of pH, was tested using fermentations at pH controlled at different values (4.5–6.5), as well as with a fermentation conducted at non-regulated pH. These simulations supported the working hypotheses. The effect of pH on the fermentation of citric acid resulted in an increase in the maximal specific rate of citrate utilization, in the bioconversion yield, and in the constant of diacetyl and acetoin reduction at acid pH. The production of flavour compounds is a complex phenomenon resulting from the interaction of pH, citric acid concentration, and the physiological state of the cells. These results are discussed with respect to the use of this strain in the preparation of manufactured dairy products.