Continuous penicillin production by Penicillium chrysogenum immobilized in calcium alginate beads

Summary A high penicillin-producing Penicillium chrysogenum strain immobilized in calcium alginate beads was used for continuous penicillin fermentation in a bubble column and in a conical bubble fermentor. The fermentation was limited by the growth rate, dilution rates and the stability of the alginate beads. The immobilized cells lost their ability to produce penicillin in the bubble column after 48 h from beginning of the continuous fermentation. In the conical bubble fermentor the immobilized cells remained active for more than 7 days. This bioreactor ensured a good distribution of nutrients and oxygen as well as a higher mechanical stability of the alginate beads.     

Pilot-plant production of prednisolone using calcium alginate immobilized Arthrobacter simplex

The maximum conversion of hydrocortisone suspensions at initial substrate concentrations greater than 4 g/L by immobilized Arthrobacter simplex in a batch reactor was 80-85%. By feeding hydrocortisone suspensions continuously to either a fed-batch-operated stirred tank reactor or to a continuous-flow airlift loop reactor, at a rate such that the soluble hydrocortisone concentration in the reactor remained ca. 0.05 g/L, 95% conversion of substratewas obtained at final product concentrations exceeding 4 g/L.     

Cellobiose hydrolysis using Pichia etchellsii cells immobilized in calcium alginate

The rate of celluose degradation, limited due to the inhibition by cellobiose, can be increased by the hydrolysis of cellobiose to glucose using immobilized beta-glucosidase. Production of beta-glucosidase in four yeasts was studied and a maximum activity of 1.22 IU/mg cells was obtained in cells of Pichia etchellsii when grown on 3% cellobiose as the sole carbon source. A study of the immobilization of beta-glucosidase containing cells of Pichia etchellsii on various solid supports was conducted and immobilization by entrapment in calcium alginate gel beads was found to be the most simple and efficient method. A retention of 96.5% of initial activity after ten sequential batch uses of the immobilized preparation was observed. The pH and temperature optima for free and immobilized cells were the same, i.e., 6.5 (0.05M Maleate buffer) and 50 degrees C, respectively. Even though the temperature optimum was found to be 50 degrees C, the enzyme exhibits a better thermal stability at 45 degrees C. Beads stored at 4 degrees C for six months retain 80% of their activity. Kinetic studies performed on free and immobilized cells shown that glucose is a noncompetitive product inhibitor.The immobilized preparation was found to be limited by pore diffusion but exhibited no film-diffusion resistance during packed bed column indicated by a low dispersion number of 0.1348. A model for reaction with pore diffusion for a noncompetitive type of inhibited system was developed and applied to the cellobiose hydrolysis system. The rate of reaction with diffusional limitations was determined by using the model and effectiveness factors were calculated for different particle sizes. An effectiveness factor of 0.49 was obtained for a particle diameter of 2.5 mm. The modified rate expression using the effectiveness factor represented batch and packed bed reactor operation satisfactorily. The productivity in the packed bed column was found to fall rapidly with increase in conversion rate indicating that the operating conditions of the column would have to be a compromise between high conversion rates and reasonable productivity. A half-life of over seven days was obtained at the operating temperature of 45 degrees C in continuous operation of the packed bed reactor. However, the half-life in the column was found to be greatly affected by temperature, increasing to over seventeen days at a temperature of 40 degrees C and decreasing to less than two days at 50 degrees C.     

Continuous production of ethanol using immobilized growing yeast cells

Summary Immobilized growing yeast cells were prepared in kappa-carra-geenan gel. Gel beads containing a small number of cells were incubated in a complete medium. The cells grew very well in the gel and the number of living cells per ml of gel increased to over 10 times that of free cells per ml of culture medium. After growing in the gel, the cells formed a dense layer of cells near the gel surface and produced large amounts of ethanol. The conditions for continuous production of ethanol using immobilized growing yeast cells were investigated. The supply of appropriate nutrients for growth was essential for the continuous production. The living cells in the gel were maintained at the high level of 10⁹ per ml of gel and continuous production of ethanol using the complete medium containing 10% glucose was carried out with a retention time of 1 h. In this operation, a stable steady state was maintained for longer than 3 months. The ethanol concentration was 50 mg/ml and the conversion of glucose utilized to ethanol produced was almost 100% of the theoretical yield.     

Continuous production ofL-isoleucine using immobilized growing Serratia marcescens cells

An immobilized growing cell system was applied to the continuous L -isoleucine production by Serratia marcescens. In the new immobilized-cell systems using the carrageenan gel method. S. marcescens cells in the gel required nutrients and oxygen for growth, and the numbers of living cells per milliliter of gel increased to the levels of that of free cells in the liquid medium. This immobilized growing cell system exhibited high and stable activity for isoleucine production under steady-state conditions. Continuous isoleucine production was carried out by feeding the nutrient medium under aeration into a fluidized bed reactor containing the immobilized cells. In the continuous operation, an efficient production was maintained by automatically controlling the pH of the reaction mixture at 7.5. The productivity of isoleucine increased using multibed reactors. In a two-bed reactor system, the effluent L -isoleucine concentration reached 4.5 mg/ml at a retention time of 10 hr, and a steady state was maintained for longer than 30 days.     

Growth and hydrocarbon production ofBotryococcus braunii immobilized in calcium alginate gel

Summary The colonial microalgaB. braunii, immobilized in calcium alginate beads, shows active photoautotrophic growth. Nevertheless, the rates of increase in cell number and, to a lesser extent, in biomass are substantially lower when compared to free cultures. Such features are related to steric contraints which occasion also the formation of large spherical colonies in the gel, showing an unsual mulberry organization. Some cracks due to the development of underlying colonies appear at the surface of the beads. Alga release remains low, however, during the cultures. EntrappedB. braunii retain the ability to produce extracellular hydrocarbons; the structure of the latter is not affected by immobilization but their relative abundances can undergo some variations. Entrapment leads to marked improvements in hydrocarbon production; decrease in growth rates is therefore associated, in alginate gel, with a still more pronounced diversion ofB. braunii metabolic activity towards hydrocarbon generation. It appears also that the improvements in hydrocarbon production, due to strain selection and to culture condition adjustment, obtained in free cultures, can be directly applied toB. braunii immobilized in alginate beads.     

Steroid transformation by living cells immobilized in calcium alginate

Summary Whole cells of Arthrobacter simplex were immobilized in a living state in calcium alginate gel. The bacteria showed steroid-¹-dehydrogenase activity and the production of prednisolone from cortisol was investigated. The ¹-dehydrogenase activity of the immobilized cells could be increased about ten-fold by incubation in nutrient media (e.g., containing 0.5% peptone abd 0.2% glucose). The reason for this activation was examined and it was found that the immobilized cells were capable of multiplying when supplied with nutrients. Furthermore, provided that an inducer, cortisol, was present, the steroid-¹-dehydrogenase activity increased in proportion to the increase in the number of cells and it was thus concluded that microbial growth was the cause of activation.Experiments on repeated, batch-wise pseudocrystallofermentation with immobilized A. simplex cells also showed that immobilized cells could be advantageously used for pseudocrystallofermentation of steroids.     

Incorporation of nisin in micro-particles of calcium alginate

Nisin was successfully incorporated into a matrix of calcium alginate and ground into micro-particles smaller than 150 μm. Formation of micro-particles and incorporation of nisin was verified by scanning electron microscopy and by the reduction in the inactivation of nisin activity with proteolytic enzymes. Incorporation efficiency was 87–93% and the nisin in the alginate-incorporated form was 100% active against an indicator culture of Lactobacillus curvatus both in MRS broth and reconstituted skim milk.     

Spermicidal bacteriocins: lacticin 3147 and subtilosin A

Spermicidal compounds that also exhibit antimicrobial properties would be extremely attractive agents as they could be used to not only prevent unwanted pregnancy but also to combat the growing prevalence of sexually transmitted infections (STI). One class of compounds that are potential candidates for development of dual-acting contraceptive products are antimicrobial peptides (AMPs). Herein, we report preliminary studies carried out to investigate the spermicidal activity of two bacteriocins, lacticin 3147 and subtilosin A, on bovine, horse/pony, boar and rat sperm.     

Continuous production of bacteriocins, brevicin, nisin and pediocin, using calcium alginate-immobilized bacteria

Bacteriocins including brevicin 286, nisin and pediocin PO2 have been produced successfully with immobilized cells of Lactobacillus brevis VB286, Lactococcus lactis subsp. lactis and Pediococcus acidilactici PO2 respectively encapsulated in calcium alginate beads. The beads encapsulating the bacteriocin-producing cells were loaded into a column, and continuously supplied with fresh medium at a flow rate of 1 bed volume per 20 min. The concentrations of the three bacteriocins produced in the eluents were at least as high as those obtained from conventional free-cell batch fermentations.     

Generation of food-grade lactococcal starters which produce the lantibiotics lacticin 3147 and lacticin 481

Transconjugant lactococcal starters which produce both lantibiotics lacticin 3147 and lacticin 481 were generated via conjugation of large bacteriocin-encoding plasmids. A representative of one of the resultant strains proved more effective at killing Lactobacillus fermentum and inhibiting the growth of Listeria monocytogenes LO28H than either of the single bacteriocin-producing parental strains, demonstrating the potential of these transconjugants as protection cultures for food safety applications.     

Nitrite uptake by Chlamydomonas reinhardtii cells immobilized in calcium alginate

When an initial cell loading of about 30–40 µg chlorophyll (Chl)·g^–1 gel and alginate suspension of 3% (w/v) were used for immobilization of Chlamydomonas reinhardtii, the resulting cell beads showed optimum nitrite uptake rate, at 30° C and pH 7.5, of 14 µmol NO _inf2 ^sup– ·mg^–1 Chl·h^–1, the photosynthetic and respiratory activities being about 120 µmol O₂ produced·mg^–1 Chl·h^–1, and 40 µmol O₂ consumed ·mg^–1 Chl·h^–1, respectively. The nitrite uptake activity required CO₂ in the culture and persisted after 8 days of cells immobilization, or in the presence of 0.2 mm ammonium in the medium. Our data indicate that alginate-entrapped C, reinhardtii cells may provide a stable and functional system for removing nitrogenous contaminants from waste-waters.Correspondence to: C. Vílchez     

Continuous production of gibberellic acid in a fixed-bed reactor by immobilized mycelia of Gibberella fujikuroi in calcium alginate beads

Summary The continuous production of gibberellic acid with immobilized mycelia of Gibberella fujikuroi was maintained over a hundred days in a tubular fixed-bed reactor. Free mycelium at the beginning of the storage phase was harvested from G. fujikuroi shake-flask culture and was immobilized by ionotropic gelation in calcium alginate beads.The continuous recycle production system consisted of a fixed-bed reactor, a container in which the culture medium was heated, stirred and aerated, and valves for sample withdrawal or reactant addition during the first 1320 h (55 days). A two-phase continuous extractor was then added for the last 960 hours (40 days). Free and immobilized mycelium shake-flask cultures with the same strain used in the continuous culture system were also realized to compare growth, maintenance and production parameters. The results show about the same gibberellic acid productivity in both free and immobilized mycelium shakeflask cultures: 0.384 and 0.408 mgGA₃·gBiomass^-1 ·day^-1, respectively, whereas in the continuous system the gibberellic acid production is about twice as large for a similar biomass: 0.768 mgGA₃·gBiomass^-1·day^-1. Several factors affecting the overall productivity of the immobilized systems were found to be: the quality and the quantity of mycelia in the biocatalyst beads and the immobilization conditions.     

Protease production by immobilized growing cells of Serratia marcescens and Myxococcus xanthus in calcium alginate gel beads

Summary Serratia marcescens and Myxococcus xanthus cells were immobilized in calcium alginate gel beads. Immobilization under various conditions had no effect on the extracellular proteolytic activity of S. marcescens cells. Protease production seemed rather to depend on the free cells in the medium. However, the stability over time of enzyme production was enhanced, as immobilization increased protease production half-life from 5 to 12 days. On the other hand, Myxococcus xanthus produced proteases inside the gel beads which could diffuse into the medium. The proteolytic activity increased as a function of the initial cell content of the beads and of the bead inoculum. Compared to free cells, immobilized cells of Myxococcus xanthus could produce 8 times more proteolytic activity, with a very low free-cell concentration in the medium.     

Production of glucoamylase using Aspergillus phoenicus immobilized in calcium alginate beads

Summary As a means of better exploiting the growth-dissociated nature of glucoamylase synthesis, a production process in which the growth phase was separated from the enzyme synthesis phase has been developed. Immobilized mycelia arising from a 6-day-old culture of conidia immobilized in calcium alginate beads could be subsequently used repeatedly to produce glucoamylase in a second step using a Dextran T-10 medium. Glucoamylase production was sustained over five sequential batches in a 19-day period and immobilized mycelia remained confined to the subsurface of the beads. Offprint requests to: C. Kuek     

Continuous production of ethanol using yeast cells immobilized in preformed cellulose beads

 Saccharomyces cerevisiae cells were immobilized on preformed cellulose beads by adsorption. The fermentation capacity of the immobilized yeast cells was found to be practically independent of the hydrogen ion concentration between pH 3.1 and 6.25. The fermentation capacity was maximal at 30 °C. The immobilized yeast cells were used for continuous production of ethanol in a fluidized-bead reactor. The average values characteristic for the process were an ethanol concentration of 41.9±0.1 g l^-1, a fermentation efficiency of 82.9±2.1% and a volumetric productivity of 3.94±0.52 g l^-1 h^-1. Received: 9 October 1995/Accepted: 22 April 1996     

Continuous production of ethanol in high concentration using immobilized growing yeast cells

Summary Application of an immobilized growing yeast cell system to continuous production of ethanol in high concentration (10%) was investigated using Saccharomyces cerevisiae IFO 2363. When a medium containing 25% glucose was fed, the growth of yeast cells in gel was inhibited. The inhibitory effect was found to be reduced by a stepwise increase in concentration of glucose in the feed medium. The stepwise operation resulted in constant growth of cells in the gel even in the medium containing 25% glucose. By this stepwise feeding system, continuous production of ethanol of 114 mg/ml was maintained at a retention time of 2.6 h for over 2 months and a conversion rate of glucose to ethanol of over 95% of theoretical, was achieved.     

Continuous ethanol production from pineapple cannery waste using immobilized yeast cells

The cells of Saccharomyces cerevisiae ATCC 24553, were immobilized in k-carrageenan and packed in a tapered glass column reactor for ethanol production from pineapple cannery waste at temperature 30 degrees C and pH 4.5. The maximum productivity was 42.8 g ethanol 1(-1) h(-1) at a dilution rate of 1.5 h(-1). The volumetric ethanol productivity of the immobilized cells was ca. 11.5 times higher than the free cells. The immobilized cell reactor was operated over a period of 87 days at a dilution rate of 1.0 h(-1), without any loss in the immobilized cell activity. The maximum specific ethanol productivity and specific sugar uptake rate of the immobilized cells were 1.2 g ethanol g(-1) dry wt. cell h(-1) and 2.6 g sugar g(-1) dry wt. cell h(-1), respectively, at a dilution rate of 1.5 h(-1).     

The production of ethanol by Saccharomyces cerevisiae immobilized in polycation-stabilized calcium alginate gels

Summary Polycation treatment of preformed calcium alginate beads produced a matrix with higher resistance to phosphate ions. The treatment of immobilized Saccharomyces cerevisiae in the calcium alginate beads inhibited respiration of the entrapped cells but did not reduce ethanol production.