Lactococcus lactis release from calcium alginate beads.

Cell release during milk fermentation by Lactococcus lactis immobilized in calcium alginate beads was examined. Numbers of free cells in the milk gradually increased from 1 x 10(6) to 3 x 10(7) CFU/ml upon successive reutilization of the beads. Rinsing the beads between fermentations did not influence the numbers of free cells in the milk. Cell release was not affected by initial cell density within the beads or by alginate concentration, although higher acidification rates were achieved with increased cell loading. Coating alginate beads with poly-L-lysine (PLL) did not significantly reduce the release of cells during five consecutive fermentations. A double coating of PLL and alginate reduced cell release by a factor of approximately 50. However, acidification of milk with beads having the PLL-alginate coating was slower than that with uncoated beads. Immersing the beads in ethanol to kill cells on the periphery reduced cell release, but acidification activity was maintained. Dipping the beads in aluminum nitrate or a hot CaCl2 solution was not as effective as dipping them in ethanol. Ethanol treatment or heating of the beads appears to be a promising method for maintaining acidification activity while minimizing viable cell release due to loosely entrapped cells near the surface of the alginate beads.     

Production ofLactococcus lactis biomass by immobilized cell technology

Summary Calcium alginate beads containingLactococcus lactis cells were used for three batch fermentations of milk or a commercially available growth medium (Gold Complete, Nordica) with the aim of producing concentrated cultures. Repeated fermentations did not significantly increase bead CFU counts which were between 3.3–7.8×10¹⁰ CFU/g. During the second and third fermentations, which lasted 6 h each, the bead populations decreased if the incubation was extended over 2 h. There was cell release from the beads. Fermentation media and fermentation time all had an effect on free cell counts, but none of these factors statistically interacted. Free cell counts were higher at the end of fermentations 2 and 3 than in the first fermentation and approximately 50% of the population was in the free state. Free cell counts were higher when the beads were incubated in Gold complete than in milk. Although the total bacterial population of a standard free cell fermentation was always higher than those having immobilized cells, immobilized cell technology did enable the production of dense cultures.     

Growth of yeast contaminants in an immobilized lactic acid bacteria system

Calcium alginate-immobilized lactic acid bacteria (LAB) were used to acidify milk and re-utilized for five successive fermentations. The yeast Kluyveromyces marxianus was added to the milk in order to simulate contamination of the bioreactor. Growth of the yeast was studied over the successive re-utilizations of the immobilized LAB. When the system was contaminated only in the first fermentation, the yeast population decreased in the successive re-utilizations; rinsing of the system following each fermentation was effective in further reducing yeast contamination. Yeast population increased only when contaminants were added at the beginning of each fermentation. Presence of yeast in the system did not influence acidification rate of the immobilized LAB or cell release from the alginate beads.     

Bacteriophage development in an immobilized lactic acid bacteria system

Summary Bacteriophages were added to milk fermented byStreptococcus raffinolactis cells immobilized in calcium alginate. Beads containing the immobilized streptococci were used for five consecutive fermentations; pH, free cell and bacteriophage counts were estimated. Free cells increased from 5×10⁶ to 3×10⁸ per mL of milk, over the successive fermentations. Addition of bacteriophages reduced the free cell count by almost 1000 after 3 fermentations, but a gradual increase occurred subsequently. Bacteriophages were inoculated at 100 per mL and gradually attained 5×10⁹ per mL in the system. Rinsing of the system did not have a substantial influence on free cell or phage counts. Presence of bacteriophage reduced slightly the acidification rate in the system.Bacteriophage numeration by two layer agar method gave better results than by most probable number (MPN). MPN counts were greatly influenced byS. raffinolactis inoculation level.Contribution # 099     

Growth and morphology of thermophilic dairy starters in alginate beads

The aim of this research was to produce concentrated biomasses of thermophilic lactic starters using immobilized cell technology (ICT). Fermentations were carried out in milk using pH control with cells microentrapped in alginate beads. In the ICT fermentations, beads represented 17% of the weight. Some assays were carried out with free cells without pH control, in order to compare the ICT populations with those of classical starters. With Streptococcus thermophilus, overall populations in the fermentor were similar, but maximum bead population for (8.2 x 10(9) cfu/g beads) was 13 times higher than that obtained in a traditional starter (4.9 x 10(8) cfu/ml). For both Lactobacillus helveticus strains studied, immobilized-cell populations were about 3 x 10(9) cfu/g beads. Production of immobilized Lb. bulgaricus 210R strain was not possible, since no increases in viable counts occurred in beads. Therefore, production of concentrated cell suspension in alginate beads was more effective for S. thermophilus. Photomicrographs of cells in alginate beads demonstrated that, while the morphology of S. thermophilus remained unchanged during the ICT fermentation, immobilized cells of Lb. helveticus appeared wider. In addition, cells of Lb. bulgaricus were curved and elongated. These morphological changes would also impair the growth of immobilized lactobacilli.     

Studies of the mechanical properties and the fermentation behavior of double layer alginate–chitosan beads,using <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> entrapped cells

Double layer alginate beads coated with chitosan were constructed for the entrapment of yeast cells used in alcoholic fermentations. Several construction parameters of the beads were studied. Among these parameters were the composition of the inner and the outer layer, the initial cell loading, the concentration of chitosan in the coating solution. Improved bead behavior was noticed by the use of chitosan as a coating agent to double layer alginate beads. The mechanical strength and the stability of the beads were enhanced. The polyelectrolyte complex membrane of alginate–chitosan reduced significantly the leakage of the entrapped cells into the medium. The aim of this work was to define the optimal conditions for the construction of the double layer alginate beads coated with chitosan with the purpose of using them for the fermentation of carbohydrates. This paper is based on a presentation at the “International Congress on Bioprocesses in Food Industries – ICBF 2006” conference, Patras 2006     

Spectrophotometric quantification of lactic bacteria in alginate and control of cell release with chitosan coating

Lactococcus lactis ssp. cremoris was entrapped within a Ca-alginate matrix, and an in situ spectrophotometric method for monitoring cell population in calcium alginate beads described. The intracapsular cell population can be estimated by measuring the optical density of beads containing cells, using cell-free beads as reference, or by measuring absorbance of a liquified bead suspension. Alginate beads, and beads coated with chitosan type I, II, and I and II mixtures, were examined for cell release. Lower viscosity chitosan (type I) coatings reduced cell release by a factor of 100 from10⁵ cfu ml⁻¹ to 10³ cfu ml⁻¹ after 6 h of fermentation. Reuse of chitosan I coated alginate beads also showed a reduction in cell release by a factor of 100. Cell loading and initial cell growth within the beads greatly affected cell release. Reducing the initial cell release would lower the overall levels of cell release throughout the fermentation. Compared to non-immobilized cultures, a 20–40% reduction in the lactic acid production rate was observed for alginate beads and chitosan I coated alginate beads, respectively. This reduction can be compensated for by increasing the intracapsular cell loading during immobilization, or before the onset of fermentation.     

Membrane formation by interfacial cross-linking of chitosan for microencapsulation of Lactococcus lactis

Lactic acid bacteria were microencapsulated within cross-linked chitosan membranes formed by emulsification/interfacial polymerization. The technique was modified and optimized to provide biocompatible conditions during encapsulation involving the use of mineral oils as the continuous phase and chitosan as the membrane material. Chitosan cross-linked with hexamethylene diisocyanate or glutaraldehyde resulted in strong membranes, with a narrow size distribution about a mean diameter of 150 mum. Cell viability and activity was demonstrated by the acidification of milk. Loss of acidification activity during microencapsulation was recovered in subsequent fermentations to levels similar to that of free cell fermentations. (c) 1993 John Wiley & Sons, Inc.     

Characterization of alginate lyase activity on liquid, gelled, and complexed states of alginate

A study of alginate lyase was carried out to determine if this enzyme could be used to remove alginate present in the core of alginate/poly-L-lysine (AG/PLL) microcapsules in order to maximize cell growth and colonization. A complete kinetic study was undertaken, which indicated an optimal activity of the enzyme at pH 7-8, 50 degrees C, in the presence of Ca2+. The buffer, not the ionic strength, influenced the alginate degradation rate. Alginate lyase was also shown to be active on gelled forms of alginate, as well as on the AG/PLL complex constituting the membrane of microcapsules. Batch cultures of CHO cells in the presence of alginate showed a decrease of the growth rate by a factor of 2, although the main metabolic flux rates were not modified. The addition of alginate lyase to cell culture medium increased the doubling time 5-7-fold and decreased the protein production rate, although cell viability was not affected. The addition of enzyme to medium containing alginate did not improve growth conditions. This suggests that alginate lyase is probably not suitable for hydrolysis of microcapsules in the presence of cells, in order to achieve high cell density and high productivity. However, the high activity may be useful for releasing cells from alginate beads or AG/PLL microcapsules.     

pH-controlled cell release and biomass distribution of alginate-immobilized Lactococcus lactis subsp. lactis

AIMS: To investigate the growth and release of Lactococcus lactis subsp. lactis in gel beads and to affect rates of cell release by changing the growth conditions. METHODS AND RESULTS: The rate of release and the distribution of immobilized L. lactis subsp. lactis in alginate beads were studied in continuous fermentations for 48 h. A change in operating pH from 6.5 to 9.25 initially reduced the ratio of the rates of cell release to lactate production by almost a factor of 105. Compared with fermentations at pH 6.5, growth at pH 9.25 also increased the final internal bead biomass concentration by a factor of 5 and increased the final rate of lactate production by 25%. After 48 h, the ratio of the rates of cell release to lactate production was still 10 times lower than in fermentations at pH 6.5. CONCLUSIONS: A change in the operating pH from 6.5 to 9.25 reduced rates of cell release throughout 48 h of fermentation and increased the final rates of lactate production and internal bead biomass concentration. SIGNIFICANCE AND IMPACT OF THE STUDY: These data illustrate that diffusional limitations and corresponding pH gradients can be exploited in affecting the distribution of immobilized growing cells and their concomitant release.     

Enhanced production of bioethanol and ultrastructural characteristics of reused Saccharomyces cerevisiae immobilized calcium alginate beads

Yeast immobilized on alginate beads produced a higher ethanol yield more rapidly than did free yeast cells under the same batch-fermentation conditions. The optimal fermentation conditions were 30 °C, pH 5.0, and 10% initial glucose concentration with 2% sodium alginate beads. The fermentation time using reused alginate beads was 10-14 h, whereas fresh beads took 24 h, and free cells took 36 h. All bead samples resulted in nearly a 100% ethanol yield, whereas the free cells resulted in an 88% yield. Transmission electron microscopy (TEM) showed that the shortened time and higher yield with the reused beads was due to a higher yeast population per bead as well as a higher porosity. The ultrastructure of calcium alginate beads and the alginate matrix structure known as the “egg-box” model were observed using TEM.     

Nutrient-enhanced survival of and phenanthrene mineralization by alginate-encapsulated and freePseudomonas sp. UG14Lr cells in creosote-contaminated soil slurries

The effects of nutrient amendment and alginate encapsulation on survival of and phenanthrene mineralization by the bioluminescentPseudomonas sp. UG14Lr in creosote-contaminated soil slurries were examined. UG14Lr was inoculated into creosote-contaminated soil slurries either as a free cell suspension or encapsulated in alginate beads prepared with montmorillonite clay and skim milk. Additional treatments were free-cell-inoculated slurries amended with sterile alginate beads, free-cell-inoculated and uninoculated slurries amended with skim milk only, and uninoculated, unamended slurries. Mineralization was determined by measuring¹⁴CO₂ released from radiolabelled phenanthrene. Survival was measured by selective plating and bioluminescence. Inclusion of skim milk was found to enhance both survival of and phenanthrene mineralization by free and encapsulated UG14Lr cells.     

The production of freeze-dried immobilized cultures of Streptococcus thermophilus and their acidification properties in milk

The aim of this study was to prepare alginate-immobilized freeze-dried cultures of Streptococcus thermophilus and to compare the acidifying activities of these rehydrated cultures with classical free cell liquid inoculants. Streptococcus thermophilus BT1 grew in alginate beads and the population reached 10(10) cfu g(-1) after 6 h incubation. Re-inoculation of the beads in fresh medium with a further 6 h incubation did not improve the biomass level, but extending the incubation at 42 degrees C to 24 h caused significant death. The rehydrated immobilized cell technology (ICT) starter contained 13% free cells. In acidifying activity tests, the ICT culture had a similar acidification curve to that of a classical milk-grown free cell culture, except that it reached lower final pH values. Although the differences between the ICT and liquid cultures were not important, there were significant effects of inoculation level on lag time, maximum acidification rate and on the pH and time at which the acidification rate was at its highest.     

Confining mycelial growth to porous microbeads: a novel technique to alter the morphology of non-newtonian mycelial cultures

In an effort to alter the filamentous morphology of Penicillium chrysogenum cells, a technique was developed to confine the growth of the mycelia to porous celite beads. The pore matrix of these beads was found to be very effective for entrapping mycelial cells and spores. The entrapped spores were used to initiate the fermentations in shake flask cultures. Significant increases in final cell densities were obtained in the confined cell cultures reaching up to 60 g/L cells. This is nearly double the cell concentration attainable in free cell cultures grown in the absence of beads. Cell loadings up to 0.55 g cells per bead were obtained in the confined cell cultures. In the later stages of the fermentations, the specific oxygen uptake rates in the confined cell cultures were found to decrease with respect to free cell cultures.     

Visualization of alginate-poly-L-lysine-alginate microcapsules by confocal laser scanning microscopy

Confocal laser scanning microscopy (CLSM) was used to study the distribution of polymers and cross-linking ions in alginate-poly-L-lysine (PLL) -alginate microcapsules made by fluorescent-labeled polymers. CLSM studies of Ca-alginate gel beads made in the presence and absence of non-gelling sodium ions revealed a more inhomogeneous distribution of alginate in beads formed in the absence of non-gelling ions. In the formation of alginate-PLL capsules, the polymer gradients in the preformed gel core were destabilized by the presence of non-gelling ions in the washing step and in the PLL solution. Ca-alginate gels preserved the inhomogeneous structure by exposure to ion-free solution in contrast to exposure to non-gelling ions (Na(+)). By exchanging Ca(2+) with Ba(2+) (10 mM), extremely inhomogeneous gel beads were formed that preserved their structure during the washing and exposure to PLL in saline. PLL was shown to bind at the very surface of the alginate core, forming a shell-like membrane. The thickness of the PLL-layer increased about 100% after 2 weeks of storage, but no further increase was seen after 2 years of storage. The coating alginate was shown to overlap the PLL layer. No difference in binding could be observed among coating alginates of different composition. This paper shows an easy and novel method to study the distribution of alginate and PLL in intact microcapsules. As the labeling procedures are easy to perform, the method can also be used for a variety of other polymers in other microencapsulation systems.     

Calcium alginate beads as a slow-release system for delivering angiogenic molecules in vivo and in vitro.

A method previously used in this laboratory for entrapment of tumor cells in alginate beads has been extended to provide a slow release delivery system for growth factors with known in vivo angiogenic activity. Protein growth factors were entrapped in alginate beads in amounts sufficient to cause incorporation of 3H-thymidine by COMMA-D cells in vitro, and in vivo neovascularization when injected subcutaneously into Balb/c mice. Entrapment of 125I-labelled growth factors showed that the amount of molecule entrapped in alginate beads may vary with the charge of the molecule. In vitro cell proliferation studies showed that entrapment in alginate beads may provide a slow-release system or a stabilizing environment for the protein. In some cases biological activity of the growth factor in solution was increased by the presence of control alginate beads. When alginate-entrapped growth factors were injected into Balb/c mice, induction of new blood vessels could be monitored qualitatively by macroscopic photography and assessed quantitatively by measuring the pooling of radiolabelled red blood cells at the experimental site. Subcutaneous injection of purified angiogenic factors not entrapped in alginate beads did not cause neovascularization. Diffusion of 125I-labelled growth factors from alginate beads in the animal showed that release in vivo may depend on the charge of the protein molecule. These results indicate that injection of purified molecules entrapped in alginate beads provides an effective localized and slow-release delivery of biologically active molecules. This delivery system may extend the time of effectiveness of biologically active molecules in vivo compared to direct injection without alginate entrapment. The method of entrapment and injection has potential for identifying active factors in tumor-induced angiogenesis and testing new compounds as modulators of neovascularization.     

Significance of the surface of immobilized Saccharomyces cerevisiae cells in ethanolic fermentation

S. cerevisiae cells immobilized in alginate beads show in many cases an increase of mean single cell volume during long-time fermentations (successive batch cycles). The biomass loading capacity of the gel beads is characterized by a maximum volume but not by a maximum number of cells occupying the gel volume. In our system this loading capacity, i.e. the maximum volume fraction of cells per volume of beads, amounted to about 0.54. As a more important result it must be stated that the specific product formation rate in the case of fermentations negligibly influenced by diffusion hindrance is related to the total surface of the viable cells but not to their total number, total volume or total dry weight.     

Elucidation of optimum conditions for immobilization of viable cells by using calcium alginate

Different factors which affect the stability of calcium alginate gel beads entrapping viable cells during fermentation were investigated. It was found that among others, the initial population of cells per ml of gel beads, the length of period of incubation in CaCl₂ solution, and the concentration of sodium alginate used for the immobilization were the most important factors affecting the stability of the gel beads during fermentation. By using an initial cell population of about 10⁵ cells per ml of 2.0% sodium alginate, and incubating the beads for at least 22 h in a CaCl₂ solution after immobilization, the percentage of beads which developed cracks during fermentation was highly reduced. Also, without the addition of CaCl₂ into the fermenting broth, the gel beads were stable for nine consecutive batch fermentations.     

Biodegradable polymer based encapsulation of neem oil nanoemulsion for controlled release of Aza-A

Azadirachtin a biological compound found in neem have medicinal and pesticidal properties. The present work reports on the encapsulation of neem oil nanoemulsion using sodium alginate (Na-Alg) by cross linking with glutaraldehyde. Starch and polyethylene glycol (PEG) were used as coating agents for smooth surface of beads. The SEM images showed beads exhibited nearly spherical shape. Swelling of the polymeric beads reduced with coating which in turn decreased the rate of release of Aza-A. Starch coated encapsulation of neem oil nanoemulsion was found to be effective when compared to PEG coated encapsulation of neem oil nanoemulsion. The release rate of neem Aza-A from the beads into an aqueous environment was analyzed by UV-visible spectrophotometer (214nm). The encapsulated neem oil nanoemulsion have the potential for controlled release of Aza-A. Neem oil nanoemulsion encapsulated beads coated with PEG was found to be toxic in lymphocyte cells.     

Characterization of an encapsulation device for the production of monodisperse alginate beads for cell immobilization

An encapsulation device, designed on the basis of the laminar jet break-up technique, is characterized for cell immobilization with different types of alginate. The principle of operation of the completely sterilizable encapsulator, together with techniques for the continuous production of beads from 250 microm to 1 mm in diameter, with a size distribution below 5%, at a flow rate of 1-15 mL/min, is described. A modification of the device, to incorporate an electrostatic potential between the alginate droplets and an internal electrode, results in enhanced monodispersity with no adverse effects on cell viability. The maximum cell loading capacity of the beads strongly depends on the nozzle diameter as well as the cells used. For the yeast Phaffia rhodozyma, it is possible to generate 700 microm alginate beads with an initial cell concentration of 1 x 10(8) cells/mL of alginate whereas only 1 x 10(6) cells/ml could be entrapped within 400 microm beads. The alginate beads have been characterized with respect to mechanical resistance and size distribution immediately after production and as a function of storage conditions. The beads remain stable in the presence of acetic acid, hydrochloric acid, water, basic water, and sodium ions. The latter stability applies when the ratio of sodium: calcium ions is less than 1/5. Complexing agents such as sodium citrate result in the rapid solubilization of the beads due to calcium removal. The presence of cells does not affect the mechanical resistance of the beads. Finally, the mechanical resistance of alginate beads can be doubled by treatment with 5-10 kDa chitosan, resulting in reduced leaching of cells.