Physico-chemical properties of alginate gel beads

Alginate gel beads are used in many applications as matrices for release or immobilisation. Until now, the parameters (such as type and concentration of cation, ionic strength and pH) of the beads formation solution in which the Na-alginate solution was dropped were not deeply studied. Therefore, in this paper, the gel formation of alginate beads and their behavior in demineralized water has been investigated carefully. The results obtained in the present study about the gel formation showed that (1) the type and the concentration of the cation play a determinant role in the gel formation phenomenon giving beads of different volumes and characteristics; (2) the weight and volume losses occurring in the ‘syneresis’ are essentially by water elimination; (3) NaCl, which gives the ionic strength of the beads formation solution, plays two roles: a competitor with calcium and a screen in the electrostatic repulsion; and (4) finally, the pH controls the gel formation process as regulator in the dissociation of the alginate and in the complexation of the calcium cations. A study by weight change dynamic analysis was also carried out. The results showed that the transfer of a bead from its formation solution into demineralized water provokes a modification of its volume, weight and stability. These results are important to understand the behavior of beads in their utilization medium.     

Direct observation of frits and dynamic air bubble formation in capillary electrochromatography using confocal fluorescence microscopy

Confocal fluorescence microscopy has been used to study the capillary electrochromatography (CEC) frits and dynamic air bubble formation under real chromatographic conditions. Confocal fluorescence microscopy provides a nondestructive way to view the three-dimensional structure of the frits with high spatial resolution. Frits prepared with four different procedures were studied: (1) sintering bare silica beads with sodium silicate; (2) sintering bare silica beads wetted with water; (3) sintering C18 beads wetted with water; and (4) sintering C18 beads wetted with water and then surfaced-recovered with C18. Frits prepared with sintering silicate-wetted beads have a high degree of heterogeneity, while the other three types of frits have similar, more homogeneous packing structures. Confocal fluorescence microscopy also provides sufficient temporal resolution for in situ observation of the dynamic processes in air bubble formation. In this study, air bubble formation is imaged during the reorganization process of the packing bed and is shown to occur close to the border between the packing bed and the outlet frit. Confocal fluorescence microscopy opens a new avenue in studying dynamic processes in situ in CEC separations.     

Extended release of Gliclazide from highly stabilized calcium alginate/poly(acrylamide) beads for diabetes management

In the present work, stability of calcium alginate beads has been remarkably improved by a novel strategy which consists of in situ formation of poly (acrylamide) within the calcium ions cross-linked sodium alginate beads. The resulting beads have been found to be stable for more than 48 h, in the physiological fluid (PF) of pH 7.4, while the plain alginate beads disintegrated within a couple of hours. The release of the anti-diabetic drug Gliclazide (Glz) from the beads was investigated under physiological conditions. The enhanced stability and prolonged release was also confirmed by an in vivo study on Albino Wistar rats.     

Encapsulation of living cells with polymeric systems

Microencapsulation of cells producing recombinant proteins or hormones leads to immunoprotection and immobilization in culture or in vivo. We are investigating three different strategies for the production of calcium cross-linked alginate beads of a small size with immobilized and immunoprotected mammalian cells: a) the AirJet technology (coaxial gas flow extrusion), b) the vibrating nozzle technology, and c) the JetCutter technology. A alginate/poly-L-lysine/alginate complexation was used as the polymeric system. All three methods may be used for production of homogeneous beads with a diameter of approximately 350 μm. While the vibrating nozzle technique was limited to an alginate viscosity of 0.2 Pa·s or less, the AirJet and JetCutter technology were less sensitive to higher viscosities. High frequency Scanning Acoustic Microscopy is used for mechanical characterization of the microspheres as well as for investigation of surface properties.     

Preparation of calcium alginate microgel beads in an electrodispersion reactor using an internal source of calcium carbonate nanoparticles

An electrodispersion reactor has been used to prepare calcium alginate (Ca-alginate) microgel beads in this study. In the electrodispersion reactor, pulsed electric fields are utilized to atomize aqueous mixtures of sodium alginate and CaCO3 nanoparticles (dispersed phase) from a nozzle into an immiscible, insulating second liquid (continuous phase) containing a soluble organic acid. This technique combines the features of the electrohydrodynamic force driven emulsion processes and externally triggered gelations in microreactors (the droplets) ultimately to yield soft gel beads. The average particle size of the Ca-alginate gels generated by this method changed from 412 +/- 90 to 10 +/- 3 microm as the applied peak voltage was increased. A diagram depicting structural information for the Ca-alginate was constructed as a function of the concentrations of sodium alginate and CaCO3 nanoparticles. From this diagram, a critical concentration of sodium alginate required for sol-gel transformation was observed. The characteristic highly porous structure of Ca-alginate particles made by this technique appears suitable for microencapsulation applications. Finally, time scale analysis was performed for the electrodispersion processes that include reactions in the microreactor droplets to provide guidelines for the future employment of this technique. This electrodispersion reactor can be used potentially in the formation of many reaction-based microencapsulation systems.     

Entrapment of ethyl vanillin in calcium alginate and calcium alginate/poly(vinyl alcohol) beads

Electrostatic extrusion was applied to the encapsulation of 3-ethoxy-4-hydroxybenzaldehyde (ethyl vanillin) in calcium alginate and calcium alginate/poly(vinyl alcohol) beads. The calcium alginate/poly(vinyl alcohol) hydrogel spheres were formed after contact with the cross-linker solution of calcium chloride, followed by the freeze-thaw method for poly(vinyl alcohol) gel formation. The entrapment of aroma in beads was investigated by FTIR and thermal analysis (thermogravimetry/differential thermal gravimetry; TGA/DTG). The mass loss in the temperature range of 150?C300°C is related to degradation of the matrix and the release of ethyl vanillin. According to the DTG curve, the release of ethyl vanillin occurs at about 260°C. TGA measurements of the stored samples confirmed that formulations were stable for a period of one month. FTIR analysis provides no evidence for chemical interactions between flavour and alginate that would alter the nature of the functional groups in the flavour compound.     

Removal of Toxic As (V) Ions by Adsorption onto Alginate and Carboxymethyl Cellulose Beads

The removal of arsenic ions from dilute aqueous solutions using biopolymeric beads of crosslinked sodium alginate and carboxymethyl cellulose (CMC) as the adsorbent is reported in this paper. The biopolymeric alginate and carboxymethyl cellulose beads were prepared and characterized by FTIR spectra. On the surfaces of the prepared beads were performed static and dynamic adsorption studies of arsenic ions at fixed pH and ionic strength of the aqueous metal ion solutions. The adsorption data were applied to Langmuir and Freundlich isotherm equations and various static parameters were calculated. The dynamic nature of adsorption was quantified in terms of several kinetic constants such as rate constant for adsorption (k₁) and Lagergreen rate constant (K_ad). The influence of various experimental parameters such as solid to liquid ratio, pH, temperature, presence of salts and chemical composition of biopolymeric beads were investigated on the adsorption of arsenic ions.     

Taxonomic Identification and Use of Free and Entrapped Cells of a New <Emphasis Type="Italic">Mycobacterium</Emphasis> sp., Strain Spyr1 for Degradation of Polycyclic Aromatic Hydrocarbons (PAHs)

A polycyclic aromatic hydrocarbon (PAH)-degrading bacterial strain Spyr1 was isolated from Greek creosote polluted soil by an enrichment method using pyrene as sole carbon and energy source. Spyr1 was identified as Mycobacterium sp. based on 16S rDNA analysis and it was capable of degrading pyrene, fluoranthene, fluorene, anthracene, and acenaphthene. The effect of entrapment in glass beads and alginate/starch mixtures on the survival and pyrene degradation ability of Spyr1 cells in liquid suspensions and soil microcosms was tested and compared with that of freely suspended cells. In general, free cells showed higher degradation of pyrene and other PAH than immobilized cells. However, immobilized cells could better tolerate PAH and they maintained their viability and PAH degradation capability for at least 1 year after storage at 4 °C. Entrapped cells in glass beads exhibited better pyrene biodegradation performance than alginate/starch entrapped cells in liquid suspensions and could be used effectively for at least ten repeated cycles. Alginate/starch entrapped cells exhibited better yields than glass beads entrapped cells for removing pyrene as well as mixtures of PAH in soil microcosms.     

Diffusion-mediated in situ alginate encapsulation of cell spheroids using microscale concave well and nanoporous membrane

Here, we present a novel and simple process of spheroid formation and in situ encapsulation of the formed spheroid without intervention. A hemispherical polydimethylsiloxane (PDMS) micromold was employed for the formation of uniform sized spheroids and two types of nano-porous membrane were used for the control of the crosslinking agent. We characterized the transport properties of the membrane, and the selection of alginate hydrogel as a function of gelation time, alginate concentration, and membrane type. Using the developed process and micromold, HepG2 cell spheroids were successfully formed and encapsulated in alginate without replating. This method allows spheroid encapsulation with minimal damage to the spheroid while maintaining high cell viability. We demonstrate the feasibility of this method in developing a bio-artificial liver (BAL) chip by evaluating viability and function of encapsulated HepG2 spheroids. This method may be applied to the encapsulation of several aggregating cell types, such as β-cells for islet formation and stem cells for embryonic body preservation, or as a model for tumor cell growth and proliferation in a 3D hydrogel environment.     

Dynamic Release of Riboflavin from Ethyl Cellulose Coated Barium Alginate Beads for Gastrointestinal Drug Delivery: An in vitro Study

The present work describes the dynamic release of model drug riboflavin form uncoated and ethyl cellulose coated barium alginate beads in the media of continuous varying pH at the physiological temperature 37°C. The drug release behavior has been studied in the simulating gastric fluid (SGF, pH 1.2) for 0–2 h and then in the simulating intestinal fluid (SIF pH 6.8) for 2–48 h. In addition to the traditional dissolution test (TDT, the dynamic release has also been studied by a newly developed method, called ‘flow through diffusion cell’ (FTDC). The release profiles, obtained by using these two methods have been found to differ appreciably from each other. Moreover, the nature of the solid mass surrounding the beads in the FTDC method also influences the release behavior of beads. The uncoated beads demonstrated faster drug release of drug in the medium of lower pH (i.e., 1.2) as compared to that in the medium of pH 6.8 and the release process was found to be diffusion controlled.     

Ionically crosslinked alginate/carboxymethyl chitin beads for oral delivery of protein drugs

Complex beads composed of alginate and carboxymethyl chitin (CMCT) were prepared by dropping aqueous alginate-CMCT into an iron(III) solution. The structure and morphology of the beads were characterized by IR spectroscopy and scanning electron microscopy (SEM). IR confirmed electrostatic interactions between iron(III) and the carboxyl groups of alginate as well as CMCT, and the binding model was suggested as a three-dimensional structure. SEM revealed that CMCT had a porous morphology while alginate and their complex beads had a core-layer structure. The swelling behavior, encapsulation efficiency, and release behavior of bovine serum albumin (BSA) from the beads at different pHs were investigated. The BSA encapsulation efficiency was fairly high (>90%). It was found that CMCT disintegrated at pH 1.2 and alginate eroded at pH 7.4 while the complex beads could effectively retain BSA in acid (>85%) and reduce the BSA release at pH 7.4. The results suggested that the iron(III)-alginate-CMCT bead could be a suitable polymeric carrier for site-specific protein drug delivery in the intestine.     

Magnetic switchable alginate beads

Calcium alginate beads are enclosed in a wide range of products including food, pharmaceuticals, and cosmetic formulations. The biopolymer matrix is often used to stabilize active ingredients and to provide a controlled release under well-defined conditions. In this context, it is of high interest to study the magnetic-induced attraction, elongation, and rupture of capsules or beads. In this work, we synthesized new types of magnetic switchable alginate beads. The magnetic sensitivity was achieved by incorporation of magnetic nanoparticles (MNPs) within the alginate gel. We measured the mechanical properties of single alginate beads in squeezing experiments, the evaporation of water and the magnetic sensitivity by stimulation of these beads in external fields. In all these measurements, the alginate and the nanoparticle concentration were systematically varied. We could show that the incorporation of MNPs generates a magnetic response of the beads and reduces the evaporation of water but has no influence on the mechanical stability of the beads during compression. Calculations of the shear modulus by means of the squeezing data result in good agreement in comparison to the shear moduli measured by rheological frequency sweep tests. With scanning electron microscopy, we could analyze the molecular structure of such composite systems, and we observed a homogeneous distribution of the MNPs within the gel matrix.     

Dynamic Release of Propranolol HCl from Cationic Ion–Exchanger–Loaded Calcium Alginate Beads

The dynamic release of drug propranolol HCl from the propranolol HCl–resin complex (PRC) loaded calcium alginate beads has been studied in the buffer media of pH 1.2 at the physiological temperature 37°C. The PRC encapsulated beads demonstrated nearly 58.04% release while naked PRC particles released 98.00% drug in 24 h in the gastric fluid. The amount of drug released was found to increase with and decrease in the amount of sodium alginate in the beads. Similarly, with the increase in the amount of entrapped PRC particles within the beads, the quantity of drug released was also observed to increase. The degree of crosslinking of beads also affected the release kinetics. Interestingly, the release from naked PRC particles followed ‘first‐order’ kinetics while PRC particles, entrapped in calcium–alginate beads, exhibited ‘diffusion controlled’ release behavior as indicated by liner nature of fractional release vs. √t plot.     

Preparation and property of layer-by-layer alginate hydrogel beads based on multi-phase emulsion technique

Layer-by-layer (LbL) alginate beads, which were prepared by multi-phase emulsion technique, had been fabricated via the ionic crosslinking between calcium ion (Ca²⁺) and the carboxylic group of alginate. The prepared beads were spherical, smooth-surfaced and non-aggregated. The SEM analysis displayed the LbL structure of the beads clearly. It had been demonstrated that the size of the beads was controllable and had a correlation with concentration of sodium alginate (SA) and CaCl₂, ratio of water phase and oil phase (W/O), stirring speed, pH value of the water phase, viscosity of SA as well as the temperature for solidification. Stability studies showed that the beads degraded slowly in simulated gastric fluid and simulated intestinal fluid but degraded sharply when they were moved to simulated colonic fluid. Cytotoxicity study by MTT assay indicated that the prepared beads are slightly toxic. It is hoped that this kind of novel beads could be used in pharmaceutical area and cell culture area.     

Removal of Rhodamine-B from Aqueous Solution by Adsorption onto Crosslinked Alginate Beads

The biosorption of rhodamine-B from aqueous solution using crosslinked alginate beads was studied by contact method at fixed pH ?3 and room temperature (28 ± 0.2°C). Both the Freundlich and Langmuir isotherm models could describe the adsorption equilibrium of the rhodamine-B onto crosslinked alginate beads. The influence of various experimental parameters such as pH, temperature, effect of concentration and time were evaluated. It was observed that the adsorption capacity of rhodamine-B onto alginate beads decreased with increase in pH and temperature above room temperature.     

Comparison of different technologies for alginate beads production

This paper describes the results of the round robin experiment “Bead production technologies” carried out during the COST 840 action “Bioencapsulation Innovation and Technologies” within the 5th Framework Program of the European Community. In this round robin experiment, calcium alginate hydrogel beads with the diameter of (800 ± 100) μm were produced by the most common bead production technologies using 0.5–4 mass % sodium alginate solutions as starting material. Dynamic viscosity of the alginate solutions ranged from less than 50 mPa s up to more than 10000 mPa s. With the coaxial air-flow and electrostatic enhanced dropping technologies as well as with the JetCutter technology in the soft-landing mode, beads were produced from all alginate solutions, whereas the vibration technology was not capable to process the high-viscosity 3 % and 4 % alginate solutions. Spherical beads were generated by the electrostatic and the JetCutter technologies. Slightly deformed beads were obtained from high-viscosity alginate solutions using the coaxial airflow and from the 0.5 % and 2 % alginate solutions using the vibration technology. The rate of bead production using the JetCutter was about 10 times higher than with the vibration technology and more than 10000 times higher than with the coaxial air-flow and electrostatic technology. In memory of our colleague Stefan Rosinski     

Inorganic–organic hybrid alginate beads with LCST near human body temperature for sustained dual‐sensitive drug delivery

In order to obtain dual‐stimuli‐responsive (temperature/pH) alginate beads that exhibit LCST close to human body temperature for sustained drug release applications, poly (NIPAAm‐co‐AAm) hydrogel (with LCST 37.5°C) were selected and associated with calcium alginate to prepare inorganic–organic hybrid biomineralized polysaccharide alginate beads via a one‐step method in this paper. Scanning electron microscopy (SEM) and energy dispersive X‐ray spectrometer (EDS) results demonstrated that calcium phosphate could not only be found in the surface but also in the cross‐section of biomineralized polysaccharide beads. Both equilibrium swelling and indomethacin release behavior were found to be pH‐ and thermo‐responsive. In addition, indomethacin release profile could be sustained with a inorganic–organic hybrid membrane: the release amount reached 96% within 4 hr for the unmineralized beads, while a drug release of only 64% obtained after subjecting the biomineralized polysaccharide beads to the same treatment. These results indicate that the biomineralized polysaccharide membrane could prevent the permeability of the encapsulated drug and reduce the drug release rate effectively. The studied system has the potential to be used as an effective smart sustainable delivery system for biomedical applications. Copyright © 2008 John Wiley & Sons, Ltd.     

In vitro angiogenesis assay for the study of cell-encapsulation therapy

Cell encapsulation within alginate beads has potential as a sustained release system for delivering therapeutic agents in vivo while protecting encapsulated cells from the immune system. There is, however, no in vitro model for cell-encapsulation therapy that provides a suitable platform for quantitative assessment of physiological responses to secreted factors. Here we introduce a new microfluidic system specifically designed to evaluate and quantify the pro-angiogenic potential of factors secreted from human fetal lung fibroblasts encapsulated in beads on an intact endothelial cell monolayer. We confirmed that cell-encapsulating beads induced an angiogenic response in vitro, demonstrated by a strong correlation between the encapsulated cell density in the beads and the length of the vascular lumen formed in vitro. Conditions established by in vitro tests were then further shown to exert a pro-angiogenic response in vivo using a subcutaneous mouse model, forming an extensive network of functional luminal structures perfused with red blood cells.     

Production of low-density sodium silicate-based hydrophobic silica aerogel beads by a novel fast gelation process and ambient pressure drying process

We report a method to synthesize low-density transparent mesoporous silica aerogel beads by ambient pressure drying (APD). The beads were prepared by acid–base sol–gel polymerization of sodium silicate in aqueous ammonia solution via the ball dropping method (BDM). To minimize shrinkage during drying, wet silica beads were initially prepared; their surfaces were then modified using trimethylchlorosilane (TMCS) via simultaneous solvent exchange and surface modification. The effects of the volume percentage (%V) of TMCS on the physical and textural properties of the beads were investigated. The specific surface area and cumulative pore volume of the silica aerogel beads increased with an increase in the %V of TMCS. Silica aerogel beads with low packing bed density (0.081 g/cm³), high surface area (917 m²/g), and large cumulative pore volume (2.8 cm³/g) was obtained when 10%V TMCS was used. Properties of the final product were examined by FE-SEM, TEM, BET, and TG–DT analyses. Surface chemical modifications were confirmed by FTIR spectroscopy. The hydrophobic silica aerogel beads were thermally stable up to 411 °C. We discuss our results and compare our findings for modified versus unmodified silica beads.     

Immobilization of penicillin acylase in porous beads of polyacrylamide gel

A procedure is described for the immobilization of benzylpenicillin acylase from Escherichia coli within uniformly spherical, porous polyacrylamide gel beads. Aqueous solutions of the enzyme and sodium alginate and of acrylamide monomer, N,N'-methylene-bis-acrylamide, N,N,N,N'-tetramethylethylenediamine (TEMED) and sodium alginate are cooled separately, mixed, and dropped immediately into ice-cold, buffered calcium formate solution, pH 8.5, to give calcium alginate-coated beads. The beads are left for 30-60 min in the cold calcium formate solution for polyacrylamide gel formation. The beads are then treated with a solution of glutaraldehyde and the calcium alginate subsequently leached out with a solution of potassium phosphate. Modification of the native enzyme with glutaraldehyde results in a slight enhancement in the rate of hydrolysis of benzylpenicillin at pH 7.8 and 0.05M substrate concentration. The enzyme entrapped in porous polyacrylamide gel beads shows no measurable diffusional limitation in stirred reactors, catalyzing the hydrolysis of the substrate at a rate comparable to that of the glutaraldehyde-modified native enzyme. The immobilized enzyme preparation has been used in batch mode over 90 cycles without any apparent loss in hydrolytic activity.