Production of alginate beads by emulsification/internal gelation. I. Methodology

Summary Small diameter alginate beads (microspheres) were formed via internal gelation of alginate solution emulsified within vegetable oil. Gelation was initiated by addition of an oil-soluble acid thereby reducing the pH of the alginate solution and releasing soluble Ca²⁺ from the citrate complex. Smooth, spherical, micron-sized beads were formed. The mean diameter ranged from 200 to 1000 m, controlled by the reactor impeller design and rotational speed. The technique has potential for large-scale and continuous applications in immobilization.Correspondence to: R. J. Neufeld     

Production of alginate beads by emulsification/internal gelation. II. Physicochemistry

Alginate microspheres were produced by emulsification/internal gelation of alginate sol dispersed within vegetable oil. Gelification was initiated within the alginate sol by a reduction in pH (7.5 to 6.5), releasing calcium from an insoluble complex. Smooth, spherical beads with the narrowest size dispersion were obtained when using low-guluronic-acid and low-viscosity alginate and a carbonate complex as the calcium vector. A more finely dispersed form of the complexed calcium within the alginate sol promotes a more homogeneous gelification. Microsphere mean diameters ranging from 50 m to 1000 m were obtained with standard deviations ranging from 35% to 45% of the mean.     

Characterization of calcium alginate and chitosan-treated calcium alginate gel beads entrapping allyl isothiocyanate

Calcium alginate (CA), chitosan-coated calcium alginate (CCA-I), and chitosan–calcium alginate complex (CCA-II) gel beads, in which an oil-in-water emulsion containing allyl isothiocyanate (AITC) was entrapped, were prepared and characterized for efficient oral delivery of AITC. The AITC entrapment efficiency was 81% for CA gel beads, whereas about 30% lower values were determined for the chitosan-treated gel beads. Swelling studies showed that all the gel beads suddenly shrunk in simulated gastric fluid (pH 1.2). In simulated intestinal fluid (pH 7.4), CA and CCA-I gel beads rapidly disintegrated, whereas CCA-II gel beads highly swelled without degradation probably due to the strong chitosan–alginate complexation. Release studies revealed that most entrapped AITC was released during the shrinkage, degradation, or swelling of the gel beads, and the chitosan treatments, especially the chitosan–alginate complexation, were effective in suppressing the release. CCA-II gel beads showed the highest bead stability and AITC retention under simulated gastrointestinal pH conditions.     

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.     

Conjugal transfer of plasmid DNA between streptococci immobilized in calcium alginate gel beads

A rapid and simple technique was developed for conjugation between group N and group D streptococci by using cells entrapped within calcium alginate gel beads. With this method, the frequencies of transfer of lactose metabolism from Streptococcus lactis ME2 to S. lactis LM2302 were comparable to those achieved with agar surface matings. Conjugal transfer of the chloramphenicol and erythromycin resistance plasmid pVA797::Tn917 from S. faecalis V1229 to S. faecalis V1102 in alginate beads occurred at frequencies comparable to those achieved with filter matings. The results demonstrated efficient conjugal transfer of plasmid DNA among alginate-immobilized streptococcal cells and suggested that this method could be used as an alternative to conventional solid-surface and filter matings with these organisms.     

Diffusion of proteases in calcium alginate beads.

Diffusion of proteases from Bacillus subtilis and Serratia marcescens within calcium alginate beads has been assayed, and the experimental data fitted into a mathematical model for diffusion into a finite volume liquid medium. Values of effective diffusivity were calculated for the studied proteases and compared with the available data in the literature for molecules of lower molecular weight.     

Optimization of alpha-amylase immobilization in calcium alginate beads

alpha-Amylase enzyme was produced by Aspergillus sclerotiorum under SSF conditions, and immobilized in calcium alginate beads. Effects of immobilization conditions, such as alginate concentration, CaCl(2) concentration, amount of loading enzyme, bead size, and amount of beads, on enzymatic activity were investigated. Optimum alginate and CaCl(2) concentration were found to be 3% (w/v). Using a loading enzyme concentration of 140 U mL(-1), and bead (diameter 3 mm) amount of 0.5 g, maximum enzyme activity was observed. Beads prepared at optimum immobilization conditions were suitable for up to 7 repeated uses, losing only 35% of their initial activity. Among the various starches tested, the highest enzyme activity (96.2%) was determined in soluble potato starch hydrolysis for 120 min at 40 degrees C.     

Conjugal transfer of plasmid DNA between streptococci immobilized in calcium alginate gel beads.

A rapid and simple technique was developed for conjugation between group N and group D streptococci by using cells entrapped within calcium alginate gel beads. With this method, the frequencies of transfer of lactose metabolism from Streptococcus lactis ME2 to S. lactis LM2302 were comparable to those achieved with agar surface matings. Conjugal transfer of the chloramphenicol and erythromycin resistance plasmid pVA797::Tn917 from S. faecalis V1229 to S. faecalis V1102 in alginate beads occurred at frequencies comparable to those achieved with filter matings. The results demonstrated efficient conjugal transfer of plasmid DNA among alginate-immobilized streptococcal cells and suggested that this method could be used as an alternative to conventional solid-surface and filter matings with these organisms.     

Culture of neural stem cells in calcium alginate beads

Neural stem cells (NSCs) with the capacity of extensive self-renewal and multilineage differentiation have attracted more and more attention in research as NSCs will play an important role in the nerve disease treatment and nerve injury repair. The shortage of NSCs, both their sources and their numbers, however, is the biggest challenge for their clinic application, and hence, in vitro culture and expansion of NSCs is vitally important to realize their potentials. In this work, mouse-derived NSCs were cultured in three-dimensional calcium alginate beads (Ca-Alg-Bs). Gelling conditions, cell density, and cell harvest were determined by the exploration of formation and dissociation parameters for Ca-Alg-Bs. Additionally, the recovered and the subsequent induced cells were identified by immunofluorescence staining of Nestin, beta-tubulin, and GFAP. The results show that the 2-mm diameter Ca-Alg-Bs, prepared with 1.5% sodium alginate solution and 3.5% CaCl2 solution and with gelling for 10 min, is suitable for the NSCs culture. The seeding density of 0.8 x 10(5) cells x mL-1 for the encapsulation of NSCs resulted in the most expansion, and the NSCs almost doubled during the experiment. The average cell recovery rate is over 88.5%, with the Ca-Alg-Bs dissolving in 55 mM sodium citrate solution for 10 min. The recovered cells cultured in the Ca-Alg-Bs still expressed Nestin and had the capacity of multilineage differentiation into neurons and glial cells and, thus, remained to be NSCs. These results demonstrate that NSC expansion within Ca-Alg-Bs is feasible and provides further possibilities for NSC expansion in bioreactors of the scale of clinical relevance.     

The evolution of the structure of calcium alginate beads and cell leakage during protease production

Cells of Serratia marcescens, immobilized by entrapment in calcium alginate beads, were cultivated in two different media: a dairy waste (whey) and a complex medium (TYE). A study of the stabilization of the support employed was carried out after establishing the relationship existing between the degree of leakage from the support and the internal biomass, as well as the possible interactions between the substrate and the gel. In order to ascertain these facts, visual methods had to be developed to evaluate the number of breakages and relate these with the culture characteristics. Finally, repeated cycle cultures were carried out, establishing the evolution of product yields and the number of breakages on the support surface, showing the behaviour on whey in relation to the complex medium.     

A new principle for immobilized yeast reactors based on internal gelation of alginate

Summary Internal gelation of alginate byin situ liberation of Ca²⁺ ions permitted production of a one-piece continuous immobilized yeast cell reactor unit having vertical internal flow channels. The reactor showed good characteristics with respect to gel stability, gas-release and fermentation stability over the 3.5 month test period.     

Diffusivity of Cu2+ in calcium alginate gel beads

The diffusivity of Cu(2+) in calcium alginate beads calculated by the shrinking core model (SCM) was reevaluated in this work. The results obtained in this work were significantly different than those by the original authors. There were excellent agreements between the results obtained by the SCM in this work and those by the more rigorous linear absorption model (LAM) by the original authors. (c) 1994 John Wiley & Sons, Inc.     

Effect of pH on the preparation of poly-L-lysine-stabilized calcium alginate beads for immobilization of aminoacylase

Summary The preparations of calcium alginate beads stabilized with poly-L-lysine and encapsulating aminoacylase were conducted at different pH conditions. The interaction of poly-L-lysine and alginate beads proceeds readily. The beads prepared at pH 7.0 exhibited high operational and storage stability with the elimination of enzyme leakage and the immobilized aminoacylase possessed high biological activity.     

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     

Diffusivity of Cu(2+) in calcium alginate gel beads

A linear absorption model (LAM) is used to describe the process of metal binding to spherically shaped biopolymers particles. The LAM was solved using a numerical algorithm which calculates diffusivities of metal ion in biopolymer gels. It assumes attainment of rapid metal-biopolymer binding equilibrium accompanied by rate limiting diffusion of the metal ions through the gel. The model was tested using batch experiments in which copper (Cu(2+)) binding with calcium alginate beads was investigated. Biopolymer density in the beads was varied between 2% and 5%. The diffusion coefficient of Cu(2+) calculated from the LAM ranged from 1.19 x 10(-9) to 1.48 x 10(-9) m(2) s(-1) (average 1.31 +/- 0.21 x 10(-9) m(2) s(-1)), independent of biopolymer density. The LAM has theoretical advantages over the shrinking core model (shell progressive model). The latter calculated an unreasonable exponential increase in the diffusion coefficient as density of alginate polymer in the bead increased. (c) 1993 John Wiley & Sons, Inc.     

Biosorption of no-carrier-added radionuclides by calcium alginate beads using 'tracer packet' technique

The aim of this study was to determine the adsorption behaviour of various micronutrient elements e.g., (61)Cu, (62,63)Zn, (66,67,68)Ga, (66,67,69)Ge, (71,72)As present in no-carrier-added state, with calcium alginate (CA) using 'tracer packet' technique. High Ge and Ga and moderate Cu removal were achieved at pH 7 and pH 5, respectively. Results on the studies to recover all the three radionuclides from the calcium alginate beads using desorbing reagents, HCl, thiourea, ammonium oxalate and sodium nitrite showed that 0.1 M HCl and 0.1 M ammonium oxalate removed Cu and Ge moderately. The amount of Ga desorbed by all the washing liquids was almost negligible, except sodium nitrite.     

Diffusivity of Cu2+ in calcium alginate gel beads: recalculation

Calculations of the diffusivity of Cu(2+) in calcium alginate gel beads using the shrinking core model were checked by us. Corrected results are reported here. Diffusivity was still found to increase with increasing alginate concentration, but at a lower rate than reported in the cited paper. The diffusivity increased by a factor of 2 over the range of alginate concentrations studied rather than 10. The original data is included with sample calculations. (c) 1994 John Wiley & Sons, Inc.     

Diffusion of Cu2+ in calcium alginate gel beads: further analyses

The diffusivity of Cu(2+), as determined by previous authors from analysis of experimental data in terms of the shrinking core (SCM) and linear absorption (LAM) models, is examined in light of the ability of the models to curve fit all the data. It is concluded from this further analysis that previous conclusions depicting the LAM to have an advantage over the SCM for predictive value are not justified. It is also shown that equally good curve fits can be obtained with a recent absorption/desorption model of diffusion which considers directly, through distribution theory, the effect of heterogeneity of material properties on the rate of diffusion. (c) 1995 John Wiley & Sons, Inc.     

Characterization of dextransucrase immobilized on calcium alginate beads from Leuconostoc mesenteroides PCSIR-4

Immobilization of dextransucrase from Leuconostoc mesenteroides PCSIR-4 on alginate is optimized for application in the production of dextran from sucrose. Dextransucrase was partially purified by ethanol upto 2.5 fold. Properties of dextransucrase were less affected by immobilization on alginate beads from soluble enzyme. Highest activities of both soluble and immobilized dextransucrase found to be at 35 degrees C and optimum pH for activity remain 5.00. Substrate maxima for immobilized enzyme changed from 125 mg/ml to 200 mg/ml. Incubation time for enzyme-substrate reaction for maximum enzyme activity was increased from 15 minutes to 60 minutes in case of immobilized enzyme. Maximum stability of immobilized dextransucrase was achieved at 25 degrees C with respect to time.