Low-cost propionate salt as road deicer: evaluation of cheese whey and other media constituents

Propionate and acetate salts are environmentally friendly, effective road deicer substitutes for widely used sodium chloride. A low-cost medium, using raw cheese whey and hydrolyzed whey permeate/whey permeate powder as substrates, and corn-steep liquor as a nutrient supplement, was studied for lactic acid production, replacing synthetic lactose and other high-cost nutrients. A non-sterile stage-I fermentation process for improved lactate productivity using an inexpensive commercial medium was performed at a 20-L fermenter level. A lactate yield of 0.98 g/g lactose and a productivity of 1.1 g/L/h was obtained with complete lactose utilization. When synthetic lactate and glucose were used as substrates in propionate and acetate fermentation, a total acid yield of 0.55 g/g glucose and lactate consumed and a batch productivity of 0.22 g/L/h was obtained. A stage-II fermentation process to produce propionate and acetate salts from cheese whey-derived lactate (stage-I fermentation broth) resulted in 1.6%( w/v) propionate after a total of 161 h (stages I and II).     

Optimization of the production of the lantibiotic mutacin 1140 in minimal media

Mutacin 1140 is produced by Streptococcus mutans and belongs to the type A lantibiotic family. Experiments were done to optimize production of mutacin 1140 in minimal media enabling a more cost efficient downstream purification method. The development of a small volume fermentation method enabled a rapid screen of several variables in a standard shaking incubator. This method provided a fast approach for determining components that promote mutacin 1140 production in minimal media broth. Lactose was determined to be the optimal carbon source for mutacin 1140 production. High concentrations of CaCl₂ (0.3%, w/v) and MgSO₄ (0.77%, w/v) promoted an increase in mutacin 1140 production, while ZnCl₂ and FeCl₃ appeared to impair production. Optimization of mutacin 1140 production in minimal media resulted in more than a 100-fold increase in production compared to the base medium used to begin our optimizations. The yield has been estimated by RP-HPLC to be ∼10 mg/L.     

Fed-batch fermentation to produce oligonucleotides from Kluyveromyces marxianus grown on whey

Oligonucleotides (ON) extracted from yeasts are used as antiviral agents, immunostimulators, and flavour enhancers. Fed-batch fermentation of cheese whey by Kluyveromyces marxianus was carried out to produce high biomass yields to extract ON. K marxianus was grown for 20 h in medium containing 5% (w/v) dehydrated whey, at 30°C (pH 4.5), with agitation (350 rpm), and under aeration (1.0–2.0 vvm). After 20 h, media containing 10–15% (w/v) of dehydrated whey were added at different flow rates (180–230 ml/h). Samples were analyzed at 6–8 h intervals for cell count, lactose consumption, and ethanol production. Maximum production of biomass (28.13 g/l), yield (0.58 g/g), productivity (2.42 g/l per h), and specific growth rate (0.63 1/h) were obtained when medium containing 15% (w/v) of whey was added at 180 ml/h under 2 vvm aeration. Fed-batch fermentation converted 95% of whey lactose into biomass.     

Alcohol production from cheese whey permeate using genetically modified flocculent yeast cells.

Alcoholic fermentation of cheese whey permeate was investigated using a recombinant flocculating Saccharomyces cerevisiae, expressing the LAC4 (coding for beta-galactosidase) and LAC12 (coding for lactose permease) genes of Kluyveromyces marxianus enabling for lactose metabolization. Data on yeast fermentation and growth on cheese whey permeate from a Portuguese dairy industry is presented. For cheese whey permeate having a lactose concentration of 50 gL(-1), total lactose consumption was observed with a conversion yield of ethanol close to the expected theoretical value. Using a continuously operating 5.5-L bioreactor, ethanol productivity near 10 g L(-1) h(-1) (corresponding to 0.45 h(-1) dilution rate) was obtained, which raises new perspectives for the economic feasibility of whey alcoholic fermentation. The use of 2-times concentrated cheese whey permeate, corresponding to 100 gL(-1) of lactose concentration, was also considered allowing for obtaining a fermentation product with 5% (w/v) alcohol.     

Enhanced Conversion of Lactose to Glycerol by Kluyveromyces fragilis Utilizing Whey Permeate as a Substrate

Kluyveromyces fragilis (CBS 397) is a nonhalophilic yeast which is capable of lactose utilization from whey permeate and high glycerol production under anaerobic growth conditions. However, the optimum yields of glycerol (11.6 mg/ml of whey permeate medium) obtained in this study occurred only in the presence of 1% Na₂SO₃ as a steering agent. The use of other concentrations of Na₂SO₃, as well as 5% NaCl and 1% ascorbic acid, had no or detrimental effects on cell growth, lactose utilization, and glycerol production. Glycerol yields were greater in cultures grown from a light inoculum of K. fragilis than in cultures in which a resuspended mass of cells was introduced into the medium. The results of this study suggest that this strain of K. fragilis may be useful commercially in the utilization of cheese whey lactose and the concomitant production of glycerol.     

Development of a low-cost medium for production of nisin from Lactococcus lactis subsp. lactis

The goal of this project was to develop a lower-cost medium for nisin production, so this bacteriocin could be used in a broader range of industrial fermentation processes. The objectives included: (1) evaluating methods for controlling the inhibitory effect of lactic acid produced during fermentation, and (2) comparing two inexpensive complex media for nisin production. Lactococcus lactis subsp. lactis was cultured in shake flasks on Laurel–Tryptose broth to evaluate a range of buffers for pH control. NaHCO₃ proved to be an effective buffer for increasing nisin production. Subsequent trials then evaluated condensed corn soluble (CCS, a fuel ethanol production byproduct) and cheese whey as inexpensive growth media. CCS was shown to be an efficient, low-cost medium for high nisin titers and yields. These modifications reduced the medium costs for nisin production from $600/kg nisin (based on Laurel–Tryptose broth medium) to $35–40/kg nisin for the corn solubles medium.     

A novel recycle batch immobilized cell bioreactor for propionate production from whey lactose

Recycle batch fermentations using immobilized cells of Propionibacterium acidipropionici were studied for propionate production from whey permeate, de-lactose whey permeate, and acid whey. Cells were immobilized in a spirally wound fibrous sheet packed in a 0.5-L column reactor, which was connected to a 5-L stirred tank batch fermentor with recirculation. The immobilized cells bioreactor served as a breeder for these recycle batch fermentations. High fermentation rates and conversions were obtained with these whey media without nutrient supplementation. It took approximately 55 h to ferment whey permeate containing approximately 45 g/L lactose to approximately 20 g/L propionic acid. Higher propionate concentrations can be produced with various concentrated whey media containing more lactose. The highest propionic acid concentration obtained with the recycle batch reactor was 65 g/L, which is much higher than the normal maximum concentration of 35 to 45 g/L reported in the literature. The volumetric productivity ranged from 0.22 g/L . h to 0.47 g/L . h, depending on the propionate concentration and whey medium used. The corresponding specific cell productivity was 0.033 to 0.07 g/L . g cell. The productivity increased to 0.68 g/L . h when whey permeate was supplemented with 1% (w/v) yeast extract. Compared with conventional batch fermentation, the recycle batch fermentation with the immobilized cell bioreactor allows faster fermentation, produces a higher concentration of product, and can be run continually without significant downtime. The process also produced similar fermentation results with nonsterile whey media. (c) 1995 John Wiley & Sons, Inc.     

Production of ethanol from the mixture of beet molasses and cheese whey by a 2-deoxyglucose-resistant mutant of Kluyveromyces marxianus

Fourteen lactose-fermenting strains of Kluyveromyces marxianus , including its anamorph, Candida kefyr , were grown in two media containing 20% (w/v) sugar as either beet molasses or cheese whey. Strain NBRC 1963 of K. marxianus converted sucrose and lactose to ethanol in both media most efficiently. However, ethanol was produced from sucrose and not from lactose by strain NBRC 1963 in the medium containing equal amounts of sugar from beet molasses and cheese whey. The spontaneous mutants resistant to 2-deoxyglucose in the minimal medium composed of galactose as the sole carbon source were isolated from strain NBRC 1963. Among them, strain KD-15 vigorously produced ethanol in the media containing beet molasses, cheese whey, or both. The mutant strain KD-15 was insensitive to catabolite repression, as shown by the observation that β-galactosidase was not repressed in the presence of sucrose from beet molasses.     

Enhancing bioethanol production from delactosed whey permeate by upstream desalination techniques

Industrial cheese whey processing comprises generally the isolation of proteins and lactose, but the economic use for the residual molasses, the so‐called delactosed whey permeate (DWP), is still to be improved. One possibility to maximize valorization and to minimize waste water treatment is the conversion of the remaining lactose in the DWP to ethanol by the yeast Kluyveromyces marxianus. This fermentation process depends strongly on the total ash content of the DWP, as high salt concentrations inhibit yeast metabolism. Here, three different approaches were tested to lower the DWP salt content: (i) simple dilution; (ii) nanofiltration; and (iii) electrodialysis. Lactose consumption, ethanol production and time‐dependent yields were compared between the three methods. A dilution of DWP to 60% v/v led to fermentation taking less than 80 h and yield above 7% AbV (alcohol by volume). After nanofiltration, 7.5% AbV was produced in about 80 h, and after electrodialysis, 11% AbV was produced in about 52 h. On the one hand the technical treatments (nanofiltration and electrodialysis) led to enhanced productivity in the fermentations, but, on the other hand, elaborate and extensive preprocessing is needed. Overall, ethanol production from DWP could be enhanced by prior partial desalination.     

Production of β-carotene from deproteinized waste whey filtrate using Mucor azygosporus MTCC 414 in submerged fermentation

The cheese whey, a by-product of dairy industry proved to be an attractive substrate for production of β-carotene. The β-carotene production from Mucor azygosporus MTCC 414 by using deproteinized waste whey filtrate under submerged fermentation was investigated. Various fermentation variables, such as lactose content in whey, initial pH, production temperature, incubation time, and carbon and nitrogen sources played significant role on β-carotene production. Maximum β-carotene production (385 μg/g dcw) was obtained with the whey (pH 5.5) containing 3.5% (w/v) lactose supplemented with soluble starch at (1.0%, w/v) at 30°C after a 5 days incubation. Moreover, unlike other microorganisms which utilize pre-hydrolyzed lactose, this Mucor azygosporus MTCC 414 was found to be capable of utilizing unhydrolyzed lactose present in the whey.     

Fermentation of deproteinized cheese whey powder solutions to ethanol by engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>: effect of supplementation with corn steep liquor and repeated-batch operation with biomass recycling by flocculation

The lactose in cheese whey is an interesting substrate for the production of bulk commodities such as bio-ethanol, due to the large amounts of whey surplus generated globally. In this work, we studied the performance of a recombinant Saccharomyces cerevisiae strain expressing the lactose permease and intracellular ß-galactosidase from Kluyveromyces lactis in fermentations of deproteinized concentrated cheese whey powder solutions. Supplementation with 10 g/l of corn steep liquor significantly enhanced whey fermentation, resulting in the production of 7.4% (v/v) ethanol from 150 g/l initial lactose in shake-flask fermentations, with a corresponding productivity of 1.2 g/l/h. The flocculation capacity of the yeast strain enabled stable operation of a repeated-batch process in a 5.5-l air-lift bioreactor, with simple biomass recycling by sedimentation of the yeast flocs. During five consecutive batches, the average ethanol productivity was 0.65 g/l/h and ethanol accumulated up to 8% (v/v) with lactose-to-ethanol conversion yields over 80% of theoretical. Yeast viability (>97%) and plasmid retention (>84%) remained high throughout the operation, demonstrating the stability and robustness of the strain. In addition, the easy and inexpensive recycle of the yeast biomass for repeated utilization makes this process economically attractive for industrial implementation.     

Lactic acid production from whey permeate by immobilized Lactobacillus casei

Two matrices have been assessed for their ability to immobilize Lactobacillus casei cells for lactic acid fermentation in whey permeate medium. Agar at 2% concentration was found to be a better gel than polyacrylamide in its effectiveness to entrap the bacterial cells to carry out batch fermentation up to three repeat runs. Of the various physiological parameters studied, temperature and pH were observed to have no significant influence on the fermentation ability of the immobilized organism. A temperature range of 40–50°C and a pH range of 4.5–6.0 rather than specific values, were found to be optimum when fermentation was carried out under stationary conditions. In batch fermentation ～90% conversion of the substrate (lactose) was achieved in 48 h using immobilized cell gel cubes of 4 × 2 × 2 mm size, containing 400 mg dry bacterial cells per flask and 4.5% w/v (initial) whey lactose content as substrate. However, further increase in substrate levels tested (>4.5% w/v) did not improve the process efficiency. Supplementation of Mg²⁺ (1 mM) and agricultural by-products (mustard oil cake, 6%) in the whey permeate medium further improved the acid production ability of the immobilized cells under study.     

Addendum to Issue 1 - ENZITEC 2012 Cheese whey and passion fruit rind flour as substrates for protease production by Bacillus sp. SMIA-2 strain isolated from Brazilian soil

Abstract

Application of wastes from the food processing industry as carbon sources in enzyme production processes reduces the cost of production, and also helps in solving problems of their disposal. In this work, we demonstrated that sweet cheese whey, in combination with passion fruit rind flour, can be successfully used for the production of protease by Bacillus sp. SMIA-2, opening perspectives for the use of these agricultural byproducts as novel and cost-effective culture media for the production of protease. The maximum production of the enzyme was observed in a sweet cheese whey-based culture medium preparation (0.5%, w/v) containing 0.25% (w/v) passion fruit rind flour and supplemented with different metal salts at an initial pH of 7.5–8.0, incubated at 50°C for 48 h. Studies on enzymatic characterization revealed that crude protease showed maximum activity at pH 9.0 and 70°C. These characteristics presented by the protease produced by Bacillus sp. SMIA-2 could be very useful when thinking about biotechnological applications.     

Whey for mass production of Beauveria bassiana and Metarhizium anisopliae

Spore production of Beauveria bassiana and Metarhizium anisopliae was studied in a novel whey-based culture media. Spore yield and viability were determined for two B. bassiana (GHA-726 and CA-603) and two M. anisopliae (CA-1 and IMI 330189) isolates following production in three whey-based systems: solid, liquid, and a diphasic production system. Our study indicated that whey permeate can be used effectively for production of spores of entomopathogenic fungi. However, spore yield and viability were significantly influenced by fungal isolate, whey concentration, and the type of production process used. Under the conditions defined in the present study, spore yields ranging from 1.3 × 10⁹–10 × 10¹¹ spores l⁻¹ of whey medium could be obtained depending on the strain and production process used. Our study revealed that spores produced by all strains in whey-based solid and liquid media showed between 73–99 % viability; germination rates were comparable with those obtained using the standard SDA medium. In the two-stage production process, the viabilities of conidia produced by GHA-726, CA-603, and CA-1 were 35–86, 32–98, and 6–29 %, respectively; viability was correlated with whey concentration and isolates. Whey permeate can be used as a growth substrate for mass production of biocontrol fungi. We hypothesize that spore yield and viability could be improved by careful selection of whey content in the medium, incorporation of critical additives and optimization of culture conditions.     

Acetate production from whey lactose using co-immobilized cells of homolactic and homoacetic bacteria in a fibrous-bed bioreactor

Acetate was produced from whey lactose in batch and fed-batch fermentations using co-immobilized cells of Clostridium formicoaceticum and Lactococcus lactis. The cells were immobilized in a spirally wound fibrous sheet packed in a 0.45-L column reactor, with liquid circulated through a 5-L stirred-tank fermentor. Industrial-grade nitrogen sources, including corn steep liquor, casein hydrolysate, and yeast hydrolysate, were studied as inexpensive nutrient supplements to whey permeate and acid whey. Supplementation with either 2.5% (v/v) corn steep liquor or 1.5 g/L casein hydrolysate was adequate for the cocultured fermentation. The overall acetic acid yield from lactose was 0.9 g/g, and the productivity was 0.25 g/(L h). Both lactate and acetate at high concentrations inhibited the homoacetic fermentation. To overcome these inhibitions, fed-batch fermentations were used to keep lactate concentration low and to adapt cells to high-concentration acetate. The final acetate concentration obtained in the fed-batch fermentation was 75 g/L, which was the highest acetate concentration ever produced by C. formicoaceticum. Even at this high acetate concentration, the overall productivity was 0.18 g/(L h) based on the total medium volume and 1.23 g/(L h) based on the fibrous-bed reactor volume. The cells isolated from the fibrous-bed bioreactor at the end of this study were more tolerant to acetic acid than the original culture used to seed the bioreactor, indicating that adaptation and natural selection of acetate-tolerant strains occurred. This cocultured fermentation process could be used to produce a low-cost acetate deicer from whey permeate and acid whey.     

Effects of dietary carbohydrates on mutacin production and activity

Although mutacins (bacteriocins produced by Streptococcus mutans) were shown to be active in vivo, their ecological role in the oral cavity is still controversial. In the present paper, the effect of dietary carbohydrates, one of the ecological parameters which influences oral bacterial populations, on the activity and the production of mutacins from four S. mutans strains (C67-1, Ny257, Ny266 and T8) is described. Results obtained by the deferred antagonism test in solid media and by the mixed cultivation of the mutacinogenic strains with a sensitive indicator strain in liquid batch cultures, indicate that a minimal fermentable sugar concentration is needed for mutacin production. Among all the fermentable carbohydrates tested (fructose, glucose, lactose, mannitol and sucrose), none significantly affected the production and the activity of the four mutacinogenic strains used, in concentrations up to 5%. Although the results do not discount the possibility of mutacin inactivation in vivo, they indicate that they are not affected by dietary carbohydrates.     

Role of amino acids, betaine and choline in vitamin B12 biosynthesis by strains of Propionibacterium

This paper reports the role of amino acids, betaine and choline on vitamin B₁₂ biosynthesis in Propionibacterium shermanii 566, P. shermanii and Propionibacterium arl AKU 1251. l-Glutamic acid supplemented at the 0.05% (w/v) level in whey permeate stimulated vitamin B₁₂ production in the three organisms, whereas the influence of other amino acids differed in the three strains. A uniform increase in product formation in Propionibacterium cultures with increasing doses of betaine and choline was recorded, but with variable relative effectiveness. However, no significant difference at the 0.50 and 0.75% (w/v) levels of these two compounds was observed. The addition of betaine at 0.5% (w/v) concentration was considered optimal for maximum fermentation efficiency in the cultures. An increase of 2.8–25.7% and 5.1–40.8% in vitamin B₁₂ yield as compared to the control was observed by supplementing whey permeate medium with l-glutamic acid and betaine, respectively, at their optimum values in the organisms studied.     

Production of propionic acid by mixed cultures ofPropionibacterium shermanii andLactobacillus casei in autoclave-sterilized whey

Summary Pure cultures ofPropionibacterium freudenreichii ss.shermanii did not grow in autoclave-sterilized cheese whey (121°C, 15 psi, 20 min) at whey concentrations greater than 2% (w/v) spray-dried sweet dairy whey. Propionic acid was produced from autoclave-sterilized whey by growingP. shermanii in mixed culture withLactobacillus casei. In medium containing 5–12% autoclaved whey solids and 1% yeast extract, the mixed culture produced 1.3–3.0% propionic acid, 0.5–1.0% acetic acid, and 0.05–0.80% lactic acid. All the lactose was consumed. Using pH-controlled fermentors (pH=7.0), mixed cultures produced at least 30% more propionic acid than cultures in which pH was not controlled.     

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     

Influence of growth conditions on the production of lactocin 705, a bacteriocin produced by Lactobacillus casei CRL 705

G.M. VIGNOLO, M.N. DE KAIRUZ, A.P. DE RUIZ HOLGADO AND G. OLIVER. 1995. The effect of growth parameters on the production of lactocin 705 by Lactobacillus casei CRL 705 isolated from dry sausages was studied. The antimicrobial compound was produced during the growth cycle at temperatures between 15 and 30°C. Maximal activity in MRS broth was achieved at pH 6.5-7.5. Investigation into the influence of supplementation and/or replacement of nutrients on lactocin 705 production demonstrated that large quantities of the bacteriocin could be obtained by addition of Tween 80 (0.5-2.0%), glucose (2.0%), tryptone (1.0%) and yeast extract (2.0%). Bacteriocin production did not decrease in the presence of (w/v) 3% NaC1 and 0.02% NaNO₂ in the culture medium. High titres of the antimicrobial compound were obtained in whey permeate supplemented with 2.0% yeast extract and 1.0% Tween 80. Lactocin 705, proved to be stable to pH and temperature at ripening conditions (pH 5.0-6.0 and 15°C) of dry cured sausages.