Batch fermentation with entrapped growing cells ofLactobacillus casei

Summary Growing cells ofLactobacillus casei were entrapped in-carrageenan/locust bean gum (LBG) (2:1 or 2.75%:0.25% w/w respectively) mixed gel beads (two ranges of diameter: 0.5–1.0 and 1.0–2.0 mm) to fermentLactobacillus Selection (LBS) medium and produce biomass. The results showed significant influence of initial cell loading of the beads and bead size on the fermentation rate. The highest cell release rates were obtained with 2.75%:0.25%-carrageenan/LBG small diameter gel beads. However, 17 h fermentation of LBS medium with immobilized cells resulted in substantial softening of the gel matrix, prohibiting reuse of immobilized biocatalysts as inoculum in subsequent batch fermentation. A dynamic shear rheological study showed that the gel weakness was related to chemical interactions with the medium. Results indicated that part of the matrix-stabilizing K⁺ ions diffused back to the medium. Stabilization of the gel was obtained by adding potassium ions to the LBS medium;L. casei growth was not altered by this supplementation. Fermentation of LBS medium supplemented with KCl byL. casei showed higher cell counts in the broth medium with immobilized cells than with free cells, reaching 10¹⁰ cells/ml after about 10 h with entrapped cells in 0.5–1.0 mm diameter beads and 17 h with free cells. Counts in the gel beads after fermentation were higher than 10¹¹ cells/ml and bead integrity was maintained throughout fermentation.     

Performance of an external loop air-lift bioreactor for the production of monoclonal antibodies by immobilized hybridoma cells

Summary The performance of an external loop air-lift bioreactor was investigated by assessing the inter-relationships between various hydrodynamic properties and mass transfer. The feasibility of using this bioreactor for the production of monoclonal antibodies by mouse hybridoma cells immobilized in calcium alginate gel beads and alginate/poly-l-lysine microcapsules was also examined. When the superficial gas velocity, V _g , in the 300 ml reactor was varied from 2 to 36 cm/min, the average liquid velocity increased from 3 to 14 cm/sec, the gas hold-up rose from 0.2 to 3.0%, and the oxygen mass transfer coefficient, k _L a, increased from 2.5 to 18.1 h^-1. A minimum liquid velocity of 4 cm/s was required to maintain alginate gel beads (1000 m diameter, occupying 3% of reactor volume) in suspension. Batch culture of hybridoma cells immobilized in alginate beads followed logarithmic growth, reaching a concentration of 4×10⁷ cells/ml beads after 11 days. Significant antibody production did not occur until day 9 into the culture, reaching a value of 100 g/ml of medium at day 11. On the other hand, bioreactor studies with encapsulated hybridoma cells gave monoclonal antibody concentrations of up to 800 g/ml capsules (the antibody being retained within the semipermeable capsule) and maximum cell densities of 2×10⁸ cells/ml capsule at day 11. The volumetric productivities of the alginate gel immobilized cell system and the encapsulated cell system were 9 and 3 g antibody per ml of reactor volume per day, respectively. The main advantage of the bioreactor system is its simple design, since no mechanical input is required to vary the hydrodynamic properties.     

Production of glutamine by micro-gel bead-immobilized Corynebacterium glutamicum 9703-T cells in a stirred tank reactor

The effectiveness of using micro-gel bead-immobilized cells for aerobic processes was investigated. Glutamine production by Corynebacterium glutamicum, 9703-T, cells was used as an example. The cells were immobilized in Sr-alginate micro-gel beads 500 m in diameter and used for fermentation processes in a stirred tank reactor with a modified impeller at 400 min^–1. Continuous production of glutamine was carried out for more than 220 h in this reactor and no gel breakage was observed. As a result of the high oxygen transfer capacity of this system, the glutamine yield from glucose was more than three times higher, while the organic acid accumulation was more than 24 times lower than those obtained with 3.0 mm-gel bead-immobilized cells in an airlift fermentor under similar experimental conditions. During the continuous fermentations there was evolution and proliferation of non-glutamine producing strains which led to a gradual decrease in the productivity of the systems. Although a modified production medium which suppresses cell growth during the production phase was effective in maintaining the productivity, the stability of the whole system was shortened due to high cell deactivation rate in such a medium.List of Symbols C kg/m³ glutamine concentration - C _A mol/m ³ local oxygen concentration inside the gel beads - C _AS mol/m ³ oxygen concentration at the surface of the gel beads - De m²/h effective diffusion coefficient of oxygen in the gel bead - DO mol/m³ dissolved oxygen concentration - F dm³/h medium flow rate - K h^–1 glutamine decomposition rate constant - Km mol/m³ Michaelis Menten constant - QO _2max mol/(kg · h) maximum specific respiration rate - R m radius of the gel beads - r m radial distance - t h time - V _C dm ³ volume of the gel beads - V _L dm ³ liquid volume in the reactor - Vm mol/(m³ · h) maximum respiration rate - X kg/m³ cell concentration - x r/R - y C _A /C_AS - h^–1 cell deactivation rate constant - Thiele modulus defined by R(Vm/De Km) ^1/2 - C _AS /Km - _C kg/(m³-gel · h) specific glutamine formation rate - _c dm³-gel/dm³ V _C /V _L      

Measurement of oxygen concentration gradients in gel-immobilized recombinantEscherichia coli

Summary In this study, an oxygen microsensor was used to measure oxygen concentration profiles in carrageenan gel particles containing growing, immobilizedEcherichia coli B (pTG201). Profiles, which were measured at intervals during continuous culture of gel slabs and beads, became increasingly steep with time. The oxygen penetration depth in the gel decreased with time, eventually reaching a steady state value of approximately 100 m for both gel beads and slabs. A reaction-diffusion model employing zero-order cell growth kinetics was found to provide an excellent fit to the experimental concentration data. Growth rates estimated from profiles obtained during the first few hours of culture were 0.24h^–1 (gel slabs) and 0.18 h^–1 (beads), compared to a value of 0.30 h^–1 measured in free-cell suspensions at 25° C.     

Plant regeneration from patchouli protoplasts encapsulated in alginate beads

Mesophyll protoplasts were isolated from leaves of in vitro grown patchouli (Pogostemon cablin Benth.). The protoplasts were encapsulated in alginate beads, approximately 2–3×10³ protoplasts per 25 l bead. Successful colony formation was induced when the protoplast beads were inoculated into a liquid medium supplemented with 10^-6 M NAA and 10^-5 M BA. The frequency of colony formation was improved greatly by the inclusion of several beads per ml medium. To induce high colony formation for a single bead, it was essential to culture protoplasts in the presence of nurse beads containing actively-growing cells of the same species. Rapid regeneration of plants from protoplast-derived calluses was accomplished by a two-step culture procedure with liquid and then solid media. Gas-chromatographic analyses showed that regenerated plants produced an essential oil comprising a full-set of patchouli sesquiterpenes.Abbreviations BA 6-benzylaminopurine - 2,4-D 2,4-dichlorophenoxyacetic acid - f. wt. fresh weight - GC gas chromatography - MES 2-(N-morpholino)ethanesulfonic acid - NAA 1-naphthaleneacetic acid     

Direct measurement of pH profiles in gel beads immobilizing Lactobacillus helveticus using a pH sensitive microelectrode

A H⁺-selective liquid membrane microelectrode was prepared and used to measure the pH profile evolution during colonization of gel beads immobilizing Lactobacillus helveticus in a whey permeate medium. A large pH gradient was observed in a highly active periferal layer thickness that decreased from 500 to 300 m for an immobilized cell population that increased from 5.8 × 10⁹ to 3.1 × 10¹⁰ CFU/g. The flat pH profile (pH 4.4) in the central part of the bead was attributed to a high concentration of the inhibitory undissociated form of lactic acid.     

Determination of the effective diffusion coefficient of oxygen in gel materials in relation to gel concentration

Summary The effective diffusion coefficient of oxygen, ID_e, was determined in different gel support materials (calcium alginate, -carrageenan, gellan gum, agar and agarose) which are generally used for immobilization of cells. The method used was based upon fitting Crank's model on the experimental data. The model describes the solute diffusion from a well-stirred solution into gel beads which are initially free of solute. The effect of the gel concentration on ID_e of oxygen in the gel was investigated. The results showed a decreasing ID_e for both agar and agarose at increasing gel concentration. In case of calcium alginate and gellan gum, a maximum in ID_e at the intermediate gel concentration was observed. It is hypothesized that this phenomenon is due to a changing gelpore structure at increasing gel concentrations. The ID_e of oxygen in calcium alginate, -carrageenan and gellan gum varied from 1.5^*10^–9 to 2.1^*10^–9 m²s^–1 in the gel concentration range of 0.5 to 5% (w/v).     

Development of in vitro procedures for regeneration of petiole and leaf expiants and production of protoplast-derived callus in Tanacetum vulgare L. (Tansy)

Tanacetum vulgare (Tansy) was established in vitro on Murashige and Skoog (MS) medium supplemented with naphthaleneacetic acid (NAA) and 6-benzylaminopurine (BAP) using shoot tips and embryos. From petiole expiants 93% formed callus, and 27% produced shoots on MS medium containing 4.5 mg l^-1 NAA and BAP. NAA alone induced root formation from leaf expiants. Up to 7 ×10⁶ viable protoplasts were obtained by macerating 1 g of leaves in 0.5 % Macerozyme R-10, 1.0% Cellulase R10, and 1.0% Cellulysin. Cell division was observed 3–4 days after protoplast isolation at the optimum plating density of 0.2-0.4×10⁶ cells ml^-1. A total of 350 protoplast-derived calluses were produced on which nodules with meristematic zones developed. Roots regenerated on MS medium supplemented with BAP 3.0 mg 1^-1, NAA 2.0 mg l^-1, and 250 mg l^-1 casein hydrolysate, however no shoots have been obtained yet.Abbreviations BAP 6-benzylaminopurine - CH casein enzymatic hydrolysate - 2.4 D dichlorophenoxyacetic acid - FDA fluorescein diacetate - GA₃ gibberellic acid - IBA indole butyric acid - IPA 6-dimethylallylamino purine - KIN Kinetin - MS Murashige and Skoog medium - NAA -naphthaleneacetic acid     

Immobilized growing lactic acid bacteria with κ-carrageenan — locust bean gum gel

Summary A cell entrapment process using -carrageenan — locust bean gum gel is presented. Streptococcus thermophilus, Lactobacillus bulgaricus and S. lactis were immobilized in small gel beads (0.5–1.0 mm and 1.0–2.0 mm diameter) and fermentations in bench bioreactors were conducted. Viability of entrapped cells, lactose utilization, lactic acid production and cell release rates were measured during fermentation. The procedure was effective for S. thermophilus, L. bulgaricus and S. lactis, and the viability of these bacteria remained very high throughout entrapment steps and subsequent storage. Bead diameter influenced the fermentation rate: smaller beads (0.5–1.0 mm) permitted an increase in release rates, lactose utilization and acid production by entrapped cells, approximating values attained with free cells.     

Biotransformation of cephalosporin C to 7-aminocephalosporanic acid with coimmobilized biocatalyst in a batch bioreactor

The permeabilized cells of Trigonopsis variabilis CCY 15-1-3 having D-amino acid oxidase (DAAO) activity were used to convert cephalosporin C (CPS-C) into 7-(-ketoadipyl amido) cephalosporanic acid (CO-GL-7-ACA) in a batch bioreactor with good aeration and stirring during the process. The deacylation of 7--(4-carboxybutanamido)-cephalosporanic acid (GL-7-ACA) to 7-cephalosporanic acid (7-ACA) by permeabilized cells of Pseudomonas species 3635 having 4--(4-carboxybutamido)-cephalosporanic acid acylase (GL-7-ACA acylase) activity was performed in a batch bioreactor. A spectrophotometric method for the determination of CO-GL-7-ACA and 7-ACA was proposed. Experimental data were fitted by non-linear regression with parameters optimization. The sorption method (without reaction) was applied for the determination of cephalosporin effective diffusion coefficients in Ca-pectate gel beads. These beads were prepared by dropping a potassium pectate gel suspension of inactive permeabilized cells of Trigonopsis variabilis and Pseudomonas species, crosslinked with glutaraldehyde, into a stirred 0.2 M calcium chloride solution. Concentrations of appropriate cephem components were measured by the refractive method. Values of effective diffusion coefficients were calculated by the Fibbonacci optimization method.List of Symbols c _L mol/dm³ concentration on the surface of a bead - c _L0 mol/dm³ initial cephalosporin concentration - c _L mol/dm³ equilibrium cephalosporin concentration in the solution - c _s1 mol/dm³ concentration of CPS-C - c _s2 mol/dm³ concentration of GL-7-ACA - D _ei m²/s effective diffusion coefficient of the components - K _i mol/dm³ inhibition parameter in Eq. (2) - K _{m i} mol/dm³ Michaelis constant in Eq. (1) - K _{m 2} mol/dm³ Michaelis constant in Eq. (2) - n number of beads - q _n nonzero positive roots in Eq. (7) - r ₁ mol/(dm³·s) rate of the conversion of CPS-S to CO-GL-7-ACA - r ₂ mol/(dm³·s) rate of the conversion of GL-7-ACA to 7-ACA - R m radius of the bead - S( ) symbol for total residual sum of squares in Eq. (1) - t s time - V _{m 1} mol/(dm³·s) max. reaction rate in Eq. (1) - V _{m 2} mol/(dm³·s) max. reaction rate in Eq. (2) - V _L dm³ volume of the solution excluding the space occupied by beads - V _s dm³ volume of beads - y _i mol/(dm³ · s) symbol for experimental data in Eq. (1) - _i mol/(dm³· s) symbol for calculated data in Eq. (1) - _P porosity, defined by Eq. (5) - dimensionless parameter, defined by Eq. (6) The authors wish to thank Dr. P. Gemeiner of Slovak Academy of Sciences for rendering of pectate gel. This work is supported by Ministry of Education (Grant No. 1/990 935/93)     

Protoplast isolation, culture, and fusion protocols for kenaf (Hibiscus cannabinus)

Protoplast isolation and culture protocols were developed for ten cultivars of Hibiscus cannabinus L. (kenaf). Leaves from seedling lines maintained in vitro were used as donor tissues. Optimal cell wall digestions were achieved with a combination of cellulysin (1.0%) and macerase (0.5%). Average yields ranged from 0.9×10⁵ to 5.9×10⁶ protoplasts g fw^-1 leaf tissue with viability estimates ranging from 53% to 87%. This protocol was ineffective for leaf tissue taken from plants grown in vivo. Protoplasts harvested from plantlets maintained in vitro produced rapidly growing calluses when plated in semi-solid medium after an initial culture in liquid medium. First cell divisions were observed within four to six days after initial culture in medium containing plant growth regulators 2,4-dichlorophenoxyacetic acid (1.4 M) and kinetin (13.8 M). An electrofusion protocol which did not significantly reduce protoplast viabilities was developed for kenaf protoplasts. The maximum fusion frequency (4.6%) was obtained with an electrofusion voltage of 2.0 kV cm^-1.Abbreviations 2,4-d 2,4-dichlorophenoxyacetic acid - BA 6-benzylaminopurine - FDA fluorescein diacetate - MS Murashige and Skoog - NAA 1-naphthaleneacetic acid - PGRs plant growth regulators - SCL seed clonal line     

Production of the triterpenoid quassin in callus and cell suspension cultures of Picrasma quassioides Bennett

Plant cell and suspension cultures have been established from stem cuttings of Picrasma quassioides Bennett. The effect of 244 different types/concentrations of plant growth regulators on growth and quassin accumulation in callus tissue was investigated. Best growth, in terms of wet/dry weight after four weeks growth, was obtained on B5 media supplemented with 2% glucose, 10% coconut milk, 0.5 mg.l^–1 zeatin riboside and 1.5 mg.l^–1 IBA. The highest yields of quassin (0.014–0.018%) were detected on this same media supplemented with 1.0 mg.l^–1 IBA and varying concentrations of zeatin riboside. Suspension cultures were easily established on B5 media supplemented with 2% glucose, 1.0 mg.l^–1 2,4-D and 0.5 mg.l^–1 kinetin. The carbon source had a marked effect on quassin accumulation with 0.32% quassin being detected when cells were grown in 2% galactose. This is comparable to the highest reported quassin yield for the whole plant.Abbreviations IAA indole-3-acetic acid - IBA indolebutyric acid - IpA N⁶-(-isopentenyl) adenine - IpAR N-(-isopentenyl) adenine riboside - NAA naphthalene acetic acid - 2,4-D 2,4-dichlorophenoxyacetic acid - 6BA 6-benzyladenine     

Epizooic ciliates (Vorticella sp.) compete for food with their host Daphnia longispina in a small polyhumic lake

Summary Clearance rates of epizooic ciliates (Vorticella sp.) were measured together with their host, a planktonic cladoceran Daphnia longispina by using fluorescent latex beads as tracers of food. Vorticellans and their host graze on food of same size range (nanoplanktonic algae and bacteria). Individual clearance rates of Vorticella averaged 6.9 and 7.0 l ind^-1 h^-1 and those of Daphnia 463 and 708 l ind^-1 h^-1 for beads with diameter 2.00 and 3.92 m. On the average, epizooic vorticellans together on the carapace of Daphnia cleared particles with rates representing 25–33% of that the host cleared, the maximum rates being 50–80%. In a steeply stratified polyhumic lake vorticellans take advantage of following Daphnia to food patches and they can severely compete for food with their host.     

Accumulation of cadmium by immobilizedZoogloea ramigera 115

Summary Zoogloea ramigera 115 was immobilized into beads of calcium-alginate and placed into batch air-bubbled column reactors. In the absence of any added nutrients the immobilized bacterium adsorbed Cd from solutions containing levels of 2 and 20 g ml^–1 per day, over a period of 21 and 20 days, respectively. Adsorption of Cd from solutions containing 20 g ml^–1 Cd was better than 90% for 16 days. Beads treated with Cd at 2 g ml^–1 never adsorbed less than 95% of the metal. Alginate adsorbed Cd as well, but inclusion of cells changed the effectiveness of adsorption. Of a 250 g ml^–1 Cd solution, alginate adsorbed 70.4% Cd in 60 min whereas alginate plus cells adsorbed 90.5% in the same time span. Temperature had no effect on adsorption by immobilized cells at levels of 2 and 10 g ml^–1 Cd. However at higher concentrations, binding was enhanced as temperature increased.Z. ramigera beads were stable during all treatments and for prolonged periods of time (21 days).     

Malate degradation by Schizosaccharomyces yeasts included in alginate beads

Schizosaccharomyces yeasts can be used for deacidification of grape musts. To this aim, we studied malic acid degradation by yeasts included in double layer alginate beads in a bubble column reactor. Use of immobilized micro-organisms allowed a continuous process with high dilution rates giving a deacidification capacity of 0.032 g of malate/hour/dm³/g of beads. The pneumatic agitation was very convenient in this case.List of Symbols D h^–1 Dilution rate for continuous culture - h Residence time for continuous culture - dM/dt kg/(m³ · h) Rate of degradation of malic acid - dS/dt kg/(m³ · h) Rate of consumption of glucose - _max h^–1 Maximal specific rate of growth     

Hybridoma cells in a protein-free medium within a composite gel perfusion bioreactor

A composite gel system has been developed combining the chemical and physical properties of calcium alginate and agarose gels. The results of growing composite gel immobilized hybridoma SPO1 cells in a protein-free medium within a fluidized-bed perfusion bioreactor are presented in this paper. During the continuous operation of this system, the total cell density reached 3.9×10⁷ cells per ml of beads (viability 79.6%). The specific productivity of monoclonal antibody of the immobilized hybridoma cells reached more than 1.5 g per 10⁶ viable cells per hour, compared with 0.5 for non-immobilized viable cells grown in a one liter agitated bioreactor with the same medium. Significant increases in cell metabolic activities, including substrate utilization and byproduct formation, were also observed. Leaching of materials from the beads was evident and the major fraction of released materials was alginate.     

Purification of theN-acetylglucosaminide α(1–3/4) fucosyltransferase of human milk

TheN-acetylglucosaminide (1–3/4)fucosyltransferase has been purified 1.8×10⁶-fold from human milk by ion-exchange chromatography, affinity chromatography of GDP-agarose and HPLC. The (1–3/4)fucosyltransferase behaves in gel filtration-HPLC as a molecule of M_r 98 000, and differs from the (1–3)fucosyltransferase which behaves like a molecule of about M_r 47 000. The enzyme is a glycoprotein, and the purified preparation appears in SDS polyacrylamide gel electrophoresis as a band of M_r 44 000. The results present the first purification of human milk (1–3/4)fucosyltransferase to apparent homogeneity, and suggest that the (1–3/4)- and (1–3)fucosyltransferases of human milk differ in their native molecular sizes, the former being a dimer of two subunits.     

Purification and preliminary characterization of an extracellular pullulanase from Thermoanaerobium Tok6-B1

Summary Extracellular pullulanase (pullulan 6-glucanohydrolase, EC 3.2.1.41) was purified from cell free culture supernatants of Thermoanaerobium Tok6-B1 by ammonium sulphate precipitation, affinity precipitation, gel exclusion and ion exchange chromatography. A final purification factor of over 1600 was achieved. A molecular weight of 120 kD was determined by steric exclusion HPLC. Enzyme activity was specifically directed towards the 1–6 glucosidic linkages of pullulan resulting in 100% conversion to maltotriose and also possessed activity towards 1–4 linkages of starch, amylopectin and amylose producing maltooligosaccharides (DP2-DP4) as products. Maltotetraose was slowly hydrolysed to maltose. Values of K _m (% w/v) were 7.3×10^-3 for pullulan, 2.7×10^-3 for amylopectin and 4.7×10^-3 for Lintner's starch. Pullulanase activity was resistant to 6 M urea and was thermostable at temperatures up to 80°C (t _1/2 in the order of hours). Above 80°C thermal denaturation was significant (t _1/2=17 min at 85°C; 5 min at 90°C) but became less so in the presence of substrate (pullulan or starch). Thermostability was greatest at the pH activity optimum (pH 5.5) and was promoted by Ca²⁺ ions.Abbreviations BSA bovine serum albumin - EDTA ethylenediamine tetracetic acid - HPLC high performance liquid chromatography - MES 2-[N-Morpholino] ethanesulphonic acid - MOPS 3-[N-Morpholino] propanesulphonic acid - Tris tris-(hydroxymethyl)methylamine     

Biotransformation of cephalosporin C to 7-aminocephalosporanic acid with coimmobilized biocatalyst in a batch bioreactor

Biotransformation of cephalosporin C (CPS-C) to 7-aminocephalosporanic acid (7-ACA) was carried out with coimmobilized permeabilized cells of Trigonopsis variabilis and Pseudomonas species entrapped in Ca-pectate gel beads. Good aeration and stirring during the process was assured. The analysis of this complicated biochemical process in a heterogeneous system was based on the identification of individual effects (internal diffusion, reaction) running simultaneously. A spectrophotometric method was proposed for the determination of 7-(-ketoadipyl amido) cephalosporanic acid (CO-GL-7-ACA) and 7-ACA. The reaction-diffusion model containing dimensionless partial differential equations was solved by using the orthogonal collocation method. A good agreement between experimental values and values predicted by the mathematical model was obtained. Numerical simulations were performed on the basis of following the two assumptions:- several times higher activity of both cells,- hydrogen peroxide was continuously supplied in the bioreactor.List of Symbols A m² surface of the bead - c _i mol/dm³ concentration of component in the bead and/or in the solution - c _i0 mol/dm³ initial concentration of component in the solution - c _l0 mol/dm³ initial concentration of CPS-C in the solution - C _jl orthogonal collocation weights of the first derivation - D _ei m²/s effective diffusion coefficient of the components - D _jl orthogonal collocation weights of the second derivation - k ₅ dm³/(mol · s) kinetic parameter of non-enzyme reaction - K _inh mol/dm³ inhibition parameter for the first enzyme reaction - K _i dimensionless Michaelis constant for the first and second enzyme reaction, defined in Eq. (7) - K _l dimensionless inhibition parameter for the first enzyme reaction, defined in Eq. (7) - K _mi mol/dm³ Michaelis constant for the first and second enzyme reaction - n number of beads - P( _i ) symbol of dimensionless reaction rate, defined in Eq. (13) - r m radial coordinate inside the bead - R m radius of the bead - R(c _i ) mol/(dm³ · s) symbol for reaction rate, defined in Eq. (6) - t s time - V _max mol/(dm³ · s) max. reaction rate for the first and second enzyme reaction - V _L dm³ volume of solution excluding the space occupied by beads - voidage in batch bioreactor - _P porosity of the bead - i dimensionless effective diffusion coefficient of the components, defined in Eq. (7) - dimensionless time, defined in Eq. (7) - _mi Thiele modulus, defined in Eq. (7) - _i dimensionless concentration, defined in Eq. (7) - dimensionless radial position inside the bead, defined in Eq. (7) - _l0 initial dimension concentration of CPS-C, defined in Eq. (9), (10) - _i0 initial dimension concentration of component, defined in Eq. (9), (10) The authors wish to thank Dr. P. Gemeiner of Slovak Academy of Sciences for rendering of pectate gel. This work is supported by Ministry of Education (Grant No. 1/990 935/93).     

Production of citric acid with immobilized Yarrowia lipolytica

Summary Citric acid was produced with immobilized Yarrowia lipolytica yeast in repeated batch-shake-flask and air-lift fermentations. In active and passive immobilization methods calcium alginate, -carrageenan, polyurethane gel, nylon web and polyurethane foams were tested as carriers in repeated-batch fermentations. The highest citric acid productivity of 155 mg l^–1 h^–1 was reached with alginate-bead-immobilized cells in the first batch. A decrease in bead diameter from 5–6 mm to 2–3 mm increased the volumetric citric acid productivity threefold. In an air-lift bioreactor the highest citric acid productivity of 120 mg l^–1 h^–1 with a product concentration of 16.4 g l^–1 was obtained with cells immobilized in -carrageenan beads. Offprint requests to: H. Kautola