Effective Bead Preparation of Coimmobilized Methanogenic and Methanotrophic Bacteria for Tetrachloroethene Degradation

Three types of coimmobilized methanogenic and methanotrophic bacterial beads – Ca-alginate, Ba-alginate, and Ca-alginate chitosan – were used for tetrachloroethene (PCE) degradation. For the purpose of effective preparation of coimmobilized bacterial beads, the diameter and broken-loading of beads were measured. The activity tests to find the optimal bacteria concentration in the bead were performed. It was found that Ba-alginate beads had superiority in bacterial growth and the degree of strength of beads from the diameter and broken-loading tests. Also, it was shown that it is most effective to add 200 mL of methanogens into 500 mL of 2% alginate solution and 20 mL of methanotrophs into 500 mL to 2% alginate solution. When methanogens and methanotrophs were applied with the Ba-alginate bead in the actual dechlorination of PCE, the biological PCE dechlorination rate was 92%, and there was highly effective degradation of PCE based on the coimmobilized bead. Additionally, relation to the diameter (X) and broken-loading (Y) of the Ba-alginate bead was derived following equation, Y = 438.02 exp(–1.4815 X).     

Relevance of rheological properties of gel beads for their mechanical stability in bioreactors

The mechanical stability of biocatalyst particles in bioreactors is of crucial importance for applications of immobilized-cell technology in bioconversions. The common methods for evaluation of the strength of polymer beads (mostly force-to-fracture or tensile tests) are, however, not yet proven to be relevant for the assessment of their mechanical stability in bioreactors. Therefore, we tested fracture properties of gel materials and investigated their relevance for abrasion in bioreactors. Abrasion of gel beads was assumed to be a continuous fracturing of the bead surface. At first, three rheological properties were considered: stress at fracture; strain at fracture; and the total fracture energy. If stress at fracture is the most important property, beads having a similar fracture energy, but a smaller stress at fracture, would abrade faster in a bioreactor than beads with a larger stress at fracture; if fracture energy the determining factor, beads that require less energy to fracture would abrade faster than those having a larger fracture energy for the same fracture stress. To determine this, beads of kappa-carrageenan and agar (at two different polymer concentrations) were tested for abrasion in four identical bubble columns under the same operating conditions. Agar beads were expected to abrade faster than those of carrageenan because agar had either a lower stress at fracture or a lower fracture energy. However, no correlation between fracture properties and abrasion rate was found in any of the combinations tested. Carrageenan beads abraded faster than those of agar in all combinations. Furthermore, both the stress and strain at fracture of agar and carrageenan beads decreased during the run and those of carrageenan decreased faster, suggesting that the gels are liable to fatigue in different ways. This hypothesis was confirmed by oscillating experiments in which gel samples were subjected to repeated compressions below their fracture levels. Their resistance to compression clearly decreased with the number of oscillations. Fatigue is probably related to the development of microcracks and microfracture propagation within the material. We concluded that: (a) the use of tests based on bead rupture do not provide relevant information on the mechanical stability of gel beads to abrasion; and (b) abrasion of polymer beads is likely to be related to fatigue of the gel materials. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 517-529, 1997.     

Alginate beads provide a beneficial physical barrier against native microorganisms in wastewater treated with immobilized bacteria and microalgae

When the freshwater microalga Chlorella sorokiniana and the plant growth-promoting bacterium Azospirillum brasilense were deployed as free suspensions in unsterile, municipal wastewater for tertiary wastewater treatment, their population was significantly lower compared with their populations in sterile wastewater. At the same time, the numbers of natural microfauna and wastewater bacteria increased. Immobilization of C. sorokiniana and A. brasilense in small (2–4 mm in diameter), polymer Ca-alginate beads significantly enhanced their populations when these beads were suspended in normal wastewater. All microbial populations within and on the surface of the beads were evaluated by quantitative fluorescence in situ hybridization combined with scanning electron microscopy and direct measurements. Submerging immobilizing beads in wastewater created the following sequence of events: (a) a biofilm composed of wastewater bacteria and A. brasilense was created on the surface of the beads, (b) the bead inhibited penetration of outside organisms into the beads, (c) the bead inhibited liberation of the immobilized microorganisms into the wastewater, and (d) permitted an uninterrupted reduction of ammonium and phosphorus from the wastewater. This study demonstrated that wastewater microbial populations are responsible for decreasing populations of biological agents used for wastewater treatment and immobilization in alginate beads provided a protective environment for these agents to carry out uninterrupted tertiary wastewater treatment.     

Transport limitation of chlorine disinfection of Pseudomonas aeruginosa entrapped in alginate beads

An artificial biofilm system consisting of Pseudomonas aeruginosa entrapped in alginate and agarose beads was used to demonstrate transport limitation of the rate of disinfection of entrapped bacteria by chlorine. Alginate gel beads with or without entrapped bacteria consumed chlorine. The specific rate of chlorine consumption increased with increasing cell loading in the gel beads and decreased with increasing bead radius. The value of an observable modulus comparing the rates of reaction and diffusion ranged from less than 0.1 to 8 depending on the bead radius and cell density. The observable modulus was largest for large (3-mm-diameter) beads with high cell loading (1.8 x 10(9) cfu/cm(3)) and smallest for small beads (0.5 mm diameter) with no cells added. A chlorine microelectrode was used to measure chlorine concentration profiles in agarose beads (3.0 mm diameter). Chlorine fully penetrated cell-free agarose beads rapidly; the concentration of chlorine at the bead center reached 50% of the bulk concentration within approximately 10 min after immersion in chlorine solution. When alginate and bacteria were incorporated into an agarose bead, pronounced chlorine concentration gradients persisted within the gel bead. Chlorine did gradually penetrate the bead, but at a greatly retarded rate; the time to reach 50% of the bulk concentration at the bead center was approximately 46 h. The overall rate of disinfection of entrapped bacteria was strongly dependent on cell density and bead radius. Small beads with low initial cell loading (0.5 mm diameter, 1.1 x 10(7) cfu/cm(3)) experienced rapid killing; viable cells could not be detected (<1.6 x 10(5) cfu/cm(3)) after 15 min of treatment in 2.5 mg/L chlorine. In contrast, the number of viable cells in larger beads with a higher initial cell density (3.0 mm diameter, 2.2 x 10(9) cfu/cm(3)) decreased only about 20% after 6 h of treatment in the same solution. Spatially nonuniform killing of bacteria within the beads was demonstrated by measuring the transient release of viable cells during dissolution of the beads. Bacteria were killed preferentially near the bead surface. Experimental results were consistent with transport limitation of the penetration of chlorine into the artificial biofilm arising from a reaction-diffusion interaction. The methods reported here provide tools for diagnosing the mechanism of biofilm resistance to reactive antimicrobial agents in such applications as the treatment of drinking and cooling waters. (c) 1996 John Wiley & Sons, Inc.     

Enhanced Tethered-Particle Motion Analysis Reveals Viscous Effects

Tethered-particle motion experiments do not require expensive or technically complex hardware, and increasing numbers of researchers are adopting this methodology to investigate the topological effects of agents that act on the tethering polymer or the characteristics of the polymer itself. These investigations depend on accurate measurement and interpretation of changes in the effective length of the tethering polymer (often DNA). However, the bead size, tether length, and buffer affect the confined diffusion of the bead in this experimental system. To evaluate the effects of these factors, improved measurements to calibrate the two-dimensional range of motion (excursion) versus DNA length were carried out. Microspheres of 160 or 240 nm in radius were tethered by DNA molecules ranging from 225 to 3477 basepairs in length in aqueous buffers containing 100 mM potassium glutamate and 8 mM MgCl₂ or 10 mM Tris-HCl and 200 mM KCl, with or without 0.5% Tween added to the buffer, and the motion was recorded. Different buffers altered the excursion of beads on identical DNA tethers. Buffer with only 10 mM NaCl and >5 mM magnesium greatly reduced excursion. Glycerol added to increase viscosity slowed confined diffusion of the tethered beads but did not change excursion. The confined-diffusion coefficients for all tethered beads were smaller than those expected for freely diffusing beads and decreased for shorter tethers. Tethered-particle motion is a sensitive framework for diffusion experiments in which small beads on long leashes most closely resemble freely diffusing, untethered beads.     

The effect of immobilization on recombinant protein production in plant cell culture

The effects of encapsulation on the production of recombinant human proteins by Nicotiana tabacum cells were investigated using alginate, carrageenan, and agar as immobilization matrices. Experiments showed that cell encapsulation in alginate increased the production of human granulocyte-macrophage colony-stimulating factor (GM-CSF) in tobacco cells by approximately 50%. Alginate also yielded the highest quality beads and the most reproducible growth results. The most likely cause for this increased protein production is the altered growth conditions within the alginate beads resulting in a prolonged exponential growth phase. To characterize these effects, we compared growth performance and protein production for various gel geometries, bead sizes, and volume fractions of beads.     

Influence of processing parameters on disintegration of Chlorella cells in various types of homogenizers

The following bead mills used for disruption of the microalga Chlorella cells were tested: (1) Dyno-Mill ECM-Pilot, grinding chamber volume 1.5 L; KDL-Pilot A, chamber volume 1.4 L; KD 20 S, chamber volume 18.3 L; KD 25 S, chamber volume 26 L of Willy A. Bachofen, Basel, Switzerland, (2) LabStar LS 1, chamber volume 0.6 L of Netzsch, Selb, Germany, (3) MS 18, chamber volume 1.1 L of FrymaKoruma, Neuenburg, Germany. Amount of disrupted cells decreased with increasing Chlorella suspension feed rate and increased up to about 85% of the beads volume in the grinding chamber of the homogenizers. It also increased with agitator speed and number of passes of the algae suspension through the chamber. The optimum beads diameter was 0.3–0.5 mm in the homogenizers Dyno-Mill and LabStar LS 1 and 0.5–0.7 mm in the homogenizer MS 18. While the degree of the cell disruption decreased with increasing cell density in Dyno-Mill and LabStar, the cell disruption in the MS 18 increased. Depending on processing parameters, more than 90% of algae cells were disrupted by passing through the bead mills and bacteria count in algae suspension was reduced to about two orders.     

Protein separation and identification using magnetic beads encoded with surface-enhanced Raman spectroscopy

This article presents a prototype of a surface-enhanced Raman spectroscopy (SERS)-encoded magnetic bead of 8 μm diameter. The core part of the bead is composed of a magnetic nanoparticle (NP)-embedded sulfonated polystyrene bead. The outer part of the bead is embedded with Ag NPs on which labeling molecules generating specific SERS bands are adsorbed. A silica shell is fabricated for further bioconjugation and protection of SERS signaling. Benzenethiol, 4-mercaptotoluene, 2-naphthalenethiol, and 4-aminothiophenol are used as labeling molecules. The magnetic SERS beads are used as substrates for protein sensing and screening with easy handling. As a model application, streptavidin-bound magnetic SERS beads are used to illustrate selective separation in a flow cytometry system, and the screened beads are spectrally recognized by Raman spectroscopy. The proposed magnetic SERS beads are likely to be used as a versatile solid support for protein sensing and screening in multiple assay technology.     

Encapsulation of adult human mesenchymal stem cells within collagen-agarose microenvironments

Reliable control over the process of cell differentiation is a major challenge in moving stem cell-based therapies forward. The composition of the extracellular matrix (ECM) is known to play an important role in modulating differentiation. We have developed a system to encapsulate adult human mesenchymal stem cells (hMSC) within spherical three-dimensional (3D) microenvironments consisting of a defined mixture of collagen Type I and agarose polymers. These protein-based beads were produced by emulsification of liquid hMSC-matrix suspensions in a silicone fluid phase and subsequent gelation to form hydrogel beads, which were collected by centrifugation and placed in culture. Bead size and size distribution could be varied by changing the encapsulation parameters (impeller speed and blade separation), and beads in the range of 30-150 microns in diameter were reliably produced. Collagen concentrations up to 40% (wt/wt) could be incorporated into the bead matrix. Visible light and fluorescence microscopy confirmed that the collagen matrix was uniformly distributed throughout the beads. Cell viability post-encapsulation was in the range of 75-90% for all bead formulations (similar to control slab gels) and remained at this level for 8 days in culture. Fluorescent staining of the actin cytoskeleton revealed that hMSC spreading increased with increasing collagen concentration. This system of producing 3D microenvironments of defined matrix composition therefore offers a way to control cell-matrix interactions and thereby guide hMSC differentiation. The bead format allows the use of small amounts of matrix proteins, and such beads can potentially be used as a cell delivery vehicle in tissue repair applications.     

Process parameters for the high-scale production of alginate-encapsulated stem cells for storage and distribution throughout the cell therapy supply chain

With the ever-increasing clinical application of cell-based therapies, it is considered critical to develop systems that facilitate the storage and distribution of cell therapy products (CTPs) between sites of manufacture and the clinic. For such systems to be realized, it is essential that downstream bioprocessing strategies be established that are scalable, reproducible and do not influence the viability or function of the living biologic. To this end, we examined alginate-encapsulation as a method to heighten the preservation of human adipose-derived stem cells (hASCs) during hypothermic storage, and establish a scalable process for high-volume production. A drop-wise method for scalable alginate bead generation, using calcium as the cross-linker, was modified to enable the yield of up to 3500 gelled beads per minute. The effect of alginate concentration on the viscosity of non-gelled sodium alginate and the mechanical properties and internal structure of calcium-crosslinked alginate in response to different alginate and calcium concentrations were investigated. Mechanical strength was chiefly dependent on alginate concentration and 1.2% alginate cross-linked with 100 mM calcium chloride could withstand stress in the order of 35 kPa. Upon selection of appropriate parameters, we demonstrated the suitability of using this method for immobilizing human stem cells. Encapsulated hASCs demonstrated no loss in cell viability, and had a uniform distribution after high-volume production. Following storage, released cells were able to attach and recover a normal morphology upon return to culture conditions. Thus we present a scalable method for stem cell encapsulation and storage for application within the cell therapy supply chain.     

Preparation and characterization of epoxy-functionalized magnetic chitosan beads: laccase immobilized for degradation of reactive dyes

Cross-linked magnetic chitosan beads were prepared by phase-inversion technique in the presence of epichlorohydrin under alkaline condition, and used for covalent immobilization of laccase. The activity of the immobilized laccase on the magnetic chitosan was about 260 U (g/dry beads) with an enzyme loading of about 16.33 ± 0.39 mg [(g/dry beads) mg/g]. Kinetic parameters, V _max and K _m values were determined as 21.7 U/mg protein and 9.4 μM for free enzyme, and 15.6 U/mg protein and 19.7 μM for the immobilized laccase, respectively. The operational and thermal stabilities of the immobilized laccase were improved compared to free counterpart. The immobilized laccase was operated in a batch reactor for the decolorization of reactive dyes from aqueous solution. The laccase immobilized on magnetic chitosan beads was very effective for removal of textile dyes from aqueous solution which creates an important environmental problem in the discharged textile dying solutions.     

Development of Gelucire 43/01 Beads of Metformin Hydrochloride for Floating Delivery

The objective of this study was to prepare and characterize beads of Gelucire 43/01 for floating delivery of metformin hydrochloride (MH). The beads were evaluated for particle size, surface morphology, percent drug entrapment, percent yield, differential scanning calorimetry (DSC), in vitro floating ability, and in vitro drug release. Aging effect on storage was evaluated using hot stage microscopy (HSM), DSC, scanning electron microscopy, and in vitro floating ability. The formed beads were sufficiently hard and spherical in shape. Photomicrographs show that the surface was porous in nature. The average particle diameter of beads was found to be in the size range of 3.85 to 3.95 mm, and percent entrapment was 83.07% to 86.13%. The beads demonstrated favorable in vitro floating ability. The analysis of DSC thermograms revealed no physical interaction between the lipid and the drug in the prepared beads. Prepared formulations showed better controlled release behavior when compared with its conventional dosage form and comparable release profile with marketed sustained release product. HSM photomicrograph showed presence of some unmelted portion even at 43°C and completely melts on 51°C in aged sample. It was found that there was no significant effect on floating ability of aged beads since it remains floats up to 8 h study period. Thus, it is concluded that beads of Gelucire 43/01 could be serve as an effective carrier for highly water-soluble antihyperglycemic drugs like MH for the controlled delivery.     

Batch fermentations with a mixed culture of lactic acid bacteria immobilized separately in κ-carrageenan locust bean gum gel beads

Summary Streptococcus salivarius subsp. thermophilus and Lactobacillus delbrueckii subsp. Bulgaricus were immobilized separately in -carrageenan-locust bean gum gel beads. The beads were prepared by a dispersion process in a two-phase system (water in oil) and two ranges of bead diameter selected by sieving (0.5–1.0 mm and 1.0–2.0 mm). Fermentations with the two strains were conducted in bench bioreactors in a supplemented whey permeate medium. Free and entrapped cells (two ranges of bead diameter and two levels of initial bead cell load) were grown in mixed culture, and carbohydrate utilization, acid production and cell growth or cell release rate measured. Fermentation rates were influenced by bead diameter and initial cell load of the beads. Beads with high initial cell density increased fermentation rates compared to low cell density beads or free cells. Smaller diameter beads (0.5–1.0 mm) showed a stable tendency (not statistically significant p _a > 0.05) towards higher cell release rates, lactose utilization, galactose accumulation and lactic acid production than did larger diameter beads (1.0–2.0 mm). Immobilization of S. salivarius subsp. thermophilus and L. delbrueckii subsp. bulgaricus in separate beads did not seem to affect protocooperation during batch fermentation, and allowed for high cell release rates into the medium.     

Microscopic mechanisms influencing the volume amplified magnetic nanobead detection assay

The volume amplified magnetic nanobead detection assay [Str?mberg, M., G?ransson, J., Gunnarsson, K., Nilsson, M., Svedlindh, P., Str?mme, M., 2008. Nano Letters 8, 816-821] was investigated with respect to bead size, bead surface coverage of probe oligonucleotides, bead concentration and rolling circle amplification (RCA) time, with the objective to improve the understanding of the microscopic mechanisms influencing the assay. The most important findings for future biosensor development were the following: (i) small beads exhibit a much reduced tendency to cross-link several RCA products, thus enabling use of both complex magnetisation turn-on and turn-off detection strategies, whereas larger beads only allow for turn-off detection; (ii) small beads exhibit faster immobilisation kinetics, thus reducing the time for diagnostic test completion, and also immobilise in larger numbers than larger beads. Finally, (iii) by demonstrating qualitative dual-target detection of bacterial DNA sequences using 130 and 250nm beads, the bioassay was shown to allow for multiplexed detection.     

Evaluation of Chitosan/Alginate Beads Using Experimental Design: Formulation and <Emphasis Type="Italic">In Vitro</Emphasis> Characterization

Bovine serum albumin-loaded beads were prepared by ionotropic gelation of alginate with calcium chloride and chitosan. The effect of sodium alginate concentration and chitosan concentration on the particle size and loading efficacy was studied. The diameter of the beads formed is dependent on the size of the needle used. The optimum condition for preparation alginate–chitosan beads was alginate concentration of 3% and chitosan concentration of 0.25% at pH 5. The resulting bead formulation had a loading efficacy of 98.5% and average size of 1,501 μm, and scanning electron microscopy images showed spherical and smooth particles. Chitosan concentration significantly influenced particle size and encapsulation efficiency of chitosan–alginate beads (p < 0.05). Decreasing the alginate concentration resulted in an increased release of albumin in acidic media. The rapid dissolution of chitosan–alginate matrices in the higher pH resulted in burst release of protein drug.     

Measurement of phagocytosis using fluorescent latex beads

Fluorescent monodisperse latex beads and a computer-centered spectrofluorimeter were used to devise a sensitive new assay for phagocytosis. LM fibroblasts, a transformed cell line with a high endocytic rate, were exposed to fluoresbrite beads and the following parameters were investigated: incubation time, incubation temperature and bead/cell ratio. The bead uptake was linear for 60 min over a wide range of bead/cell ratios up to 130 beads/cell. Phagocytosis was inhibited at 4 degrees C, by incubation in the presence of colchicine, and by glucose deprivation. Scanning and transmission electron microscopy were used to confirm that at 37 degrees C both bead adsorption and internalization occurred while at 4 degrees C only bead adsorption but not endocytosis occurred. Large bead sizes (0.86 and 1.72 micrometer diameter) were most useful due to higher fluorescence and higher signal to noise ratios than smaller beads (0.25 and 0.57 micrometer diameter). Beads (0.86 micrometer diameter) were taken up at a rate of 4.4 beads/cell/h at 37 degrees C when a bead/cell ratio of 70 was used. The uptake was zero when assayed at zero time. These criteria establish that fluoresbrite beads provide a useful new fluorimetric assay for phagocytosis.     

Production of alginate beads by a rotative atomizer

Summary The use of a rotative flat disc atomizer for the production of biocatalysts immobilized in alginate gel was investigated. The influence of viscosity (0.28 to 1.53 Pa · s), disc diameter (5 to 20 cm), flow rate (0.5 to 2 L/min) and rotational speed (1.6 to 5 rev/s) on drop formation mechanisms, bead diameter and their distributions were investigated. Bead diameters ranging from 1 to 3 mm were been obtained. Flow rate and viscosity increases resulted in higher bead diameters but increasing disc diameter and rotational speed had a decreasing effect. A viscosity of 0.65 Pa · s would prove best for production of beads with good size distribution and mechanical strength. Predictive equations for the mean volumetric bead diameter were determined.     

Development of pH-sensitive tamarind seed polysaccharide-alginate composite beads for controlled diclofenac sodium delivery using response surface methodology

The present study deals with the development of novel pH-sensitive tamarind seed polysaccharide (TSP)-alginate composite beads for controlled diclofenac sodium delivery using response surface methodology by full 3² factorial design. The effect of polymer-blend ratio (sodium alginate:TSP) and cross-linker (CaCl₂) concentration on the drug encapsulation efficiency (DEE, %) and drug release from diclofenac sodium loaded TSP-alginate composite beads prepared by ionotropic gelation was optimized. The observed responses were coincided well with the predicted values by the experimental design. The DEE (%) of these beads containing diclofenac sodium was within the range between 72.23 ± 2.14 and 97.32 ± 4.03% with sustained in vitro drug release (69.08 ± 2.36-96.07 ± 3.54% in 10 h). The in vitro drug release from TSP-alginate composite beads containing diclofenac sodium was followed by controlled-release pattern (zero-order kinetics) with case-II transport mechanism. Particle size range of these beads was 0.71 ± 0.03-1.33 ± 0.04 mm. The swelling and degradation of the developed beads were influenced by different pH of the test medium. The FTIR and NMR analyses confirmed the compatibility of the diclofenac sodium with TSP and sodium alginate used to prepare the diclofenac sodium loaded TSP-alginate composite beads. The newly developed TSP-alginate composite beads are suitable for controlled delivery of diclofenac sodium for prolonged period.     

In vivo production of scFv-displaying biopolymer beads using a self-assembly-promoting fusion partner

Recombinant production and, in particular, immobilization of antibody fragments onto carrier materials are of high interest with regard to diagnostic and therapeutic applications. In this study, the recombinant production of scFv-displaying biopolymer beads intracellularly in Escherichia coli was investigated. An anti-beta-galactosidase scFv (single chain variable fragment of an antibody) was C-terminally tagged with the polymer-synthesizing enzyme PhaC from Cupriavidus necator by generating the respective hybrid gene. The functionality of the anti-beta-galactosidase scFv-PhaC fusion protein was assessed by producing the respective soluble fusion protein in an Escherichia coli AMEF mutant strain. AMEF (antibody-mediated enzyme formation) strains contain an inactive mutant beta-galactosidase, which can be activated by binding of an anti-beta-galactosidase antibody. In vivo activation of AMEF beta-galactosidase indicated that the scFv is functional with the C-terminal fusion partner PhaC. It was further demonstrated that polymer biosynthesis and bead formation were mediated by the scFv-PhaC fusion protein in the cytoplasm of recombinant E. coli when the polymer precursor was metabolically provided. This suggested that the C-terminal fusion partner PhaC acts as a functional insolubility partner, providing a natural cross-link to the bead and leading to in vivo immobilization of the scFv. Overproduction of the fusion protein at the polymer bead surface was confirmed by SDS-PAGE and MALDI-TOF/MS analysis of purified beads. Antigen binding functionality and specificity of the beads was assessed by analyzing the binding of beta-galactosidase to scFv-displaying beads and subsequently eluting the bound protein at pH 2.7. A strong enrichment of beta-galactosidase suggested the functional display of scFv at the bead surface as well as the applicability of these beads for antigen purification. Binding of beta-galactosidase to the scFv-displaying beads was quantitatively analyzed by enzyme-linked assays measuring beta-galactosidase activity. These indicated that the anti-beta-galactosidase scFv-displaying beads bound a maximum of 38 ng of beta-galactosidase per 1 microg of bead protein, showing an apparent equilibrium dissociation constant ( KD) of 12 x 10 (-7) M. This study clearly demonstrated that anti-beta-galactosidase scFv-displaying polymer beads can be produced in engineered E. coli in a one-step process by using PhaC as a self-assembly-promoting fusion partner.