Investigation of Shelf Life of Potency and Activity of the Lactobacilli Produced Bacteriocins Through Their Exposure to Various Physicochemical Stress Factors

Three Lactobacilli strains, Lactobacillus casei NCIMB 11970, Lactobacillus plantarum NCIMB 8014, Lactobacillus lactis NCIMB 8586 have been used for the production of bacteriocins. Though, their production phase, their biochemical nature, their mode of activity even their genetic structure have been widely investigated, there are hardly any studies investigating their potency and activity in depth of time, in other words their shelf life under several physicochemical conditions that may occur during their production in large scale. As such, the effect of several factors influencing the activity and the potency of bacteriocins when produced in large scale was examined as due to bacteriocins peptide nature degradation or denaturation might occur, under extreme physicochemical conditions. During scale-up process, differences between the output data may occur, such as concerning biomass, metabolic by-products and limiting substrate concentrations. These may affect negatively the activity and the potency of the bacteriocins. For investigating these effects and minimizing them, numerous studies were conducted, which were related to the exact phase of the production of these substances, the effect of dilution and temperature changes. These studies could be used in order to minimize the scaling-up effect when decided to produce these peptides in large scale.     

Partially chemically defined liquid medium development for intensive propagation of industrial fermentation lactobacilli strains

An economic liquid growth medium was synthesised for high-rate production of cellular mass, lactic acid and bacteriocin in lactobacilli. Three lactobacilli that are applied extensively in industry—Lactobacillus casei NCIMB 11970, Lactobacillus plantarum NCIMB 8014, Lactobacillus lactis NCIMB 8586—were chosen to test the medium’s efficiency. These bacteria are chemoorganotrophs requiring rich, complex media for optimum growth. Contrary to the current practice of formulating a strain-specific medium, we attempted to prepare a universal broth that would allow easy formulation and optimisation. Man de Rogosa Sharp (MRS) medium, which can support the growth of lactobacilli, was found unsuitable for use in large quantities due to its high cost of preparation and its use of beef extract and peptone from poultry as nitrogen sources, which are not environmentally friendly and have potential health risks. The developed medium supported the growth of all the three bacteria equally, offering good maximum yields and incorporating only the chemical compounds needed, resulting in an improvement in the growth rate of the bacilli of between 50 % and 241 % compared to the same strains grown on MRS. Lactic acid production was between 28.6 and 35.74 g L^?1 and bacteriocin production ranged from 110 to 130 IU mL^?1.     

Separation of lactobacilli bacteriocins from fermented broths using membranes

Current separation, isolation and purification techniques to obtain highly potent purified lactobacilli and lactococci bacteriocins include chemical precipitation, separation employing solvents and chromatographic techniques. These methods are arduous, costly, with limited scalability, offering low bacteriocin yields (<20%). To address these challenges, the alternatives of ultrafiltration and nanofiltration, as separation methods were tested. Three promising bacteriocin producing strains, Lactobacillus casei NCIMB 11970, Lactobacillus plantarum NCIMB 8014 and Lactococcus lactis NCIMB 8586 were selected to investigate the applicability and feasibility of the method.To facilitate separation, the microorganisms were grown on specially developed low molecular weight medium (LMWM) mainly containing nutritive sources up to 4 kDa molecular weight. Bacterial cells were removed by centrifugation. The clarified broths were filtered using 4 and 1 kDa MWCO. Bacteriocin activity was determined by an antimicrobial activity test using nisin, which has an inhibitory effect on the growth of susceptible microorganisms. Recovery yields using filtration were found to range between 53 and 68%, a high recovery performance.The bacteriocin activity of crude extracts of all the three lactobacilli were between 95 and 105 IU ml^?1. When the substances were separated using ultrafiltration membrane (4 kDa MWCO) their activity was enhanced to 145–150 IU ml^?1, achieving a total potency yield of 44–53%. Further enhancement of yields up to 36% was attained employing nanofiltration (1 kDa MWCO) membranes with an activity increased up to 200 IU ml^?1.Bacteriocin isolation from crude extracts using filtration was found to be effective, offering high recovery yields, optimising their activity as well as presenting a realistic option towards the formulation of these as commercially available antibacterial agents.     

Modelling and simulation of cell growth dynamics, substrate consumption, and lactic acid production kinetics of Lactococcus lactis

Lactococcus lactis species have been and still are extensively investigated due to their significant commercial importance. Current scientific research focuses on strains utilized in food industry, due to their multiple uses in food and beverages fabrication. Biomass of Lactococcus lactis is of great interest as well as the end products of its metabolism such as lactic acid and nisin. However their production is constantly challenged due to end product inhibition occurring during intensive propagation of the coccus in reactor systems. To successfully predict the behavior of the culture, the approach of combining mathematics with biology, ergo the development of an unstructured mathematical model, was taken. Although Luedeking and Piret is the model that has been extensively used to demonstrate growth in end-product inhibition cultures, its applicability is limited due to its dependance on the specific growth and product coefficients, particularly related to the culturing conditions used. To overcome these hurdles, a combination of the non competitive single product end inhibition Taylor and Hinselwood models was used, with the significance of this model laying in the fact that it offers a feasible alternative to the commonly used model of Luedeking and Piret for describing fermentation kinetics governed by end-product inhibitions. The fitting with the experimental values, in batch mode, was tested in terms of the coefficient of determination (R²), having values 0.97 ～ 0.99 and suggesting a very good fitting with the experimental data. The model was further developed to achieve theoretical predictions of volumetric cell productivity in continuous and fed-batch mode of substrate feed in different culturring systems.