Reaction and diffusion in a gel membrane reactor containing immobilized cells

To investigate the effect of diffusional limitations and heterogeneous cell distribution in a gel-immobilized cell system, a gel membrane reactor has been constructed. The reactor consists essentially of a gel layer with immobilized cells, flanked by two well-mixed chambers. Through one chamber substrate is pumped, and this chamber is the equivalent of the outside of a spherical gel bead. The second closed measuring chamber contains a small quantity of liquid that can equilibrate with the inside surface of the membrane, eventually after a long transient. Analysis of the liquid in this chamber can give direct information on substrate and product concentrations at the gel surface, and is and indication of the situation in the center of a gel bead. The gel membrane reactor appears to be an excellent tool to study diffusion and reaction in a gel-containing immobilized cells. A mathematical model with time- and position-dependent cell concentration and diffusion coefficient is described. Experimental data show the effective diffusion coefficient of glucose in an alginate gel to decrease with yeast cell concentration. Moreover, kinetic parameters could be determined, using the mathematical model. Microscopic analysis confirmed the proliferation of the gel-entrapped microorganisms in the outer layer of the matrix, as predicted by the model. Potentially, this type of reactor has a clear potential to study the physiology of gel-immobilized cells. (c) 1992 John Wiley & Sons, Inc.     

Mass transfer effects in fermentations using immobilized whole cells

The immobilization of whole cells for fermentation processes has many potential advantages over fermentation with free cells, including higher cell concentrations, higher productivites and a higher level of operational stability. Most of the research reported in the literature has been directed towards demonstrating the feasibility of using these systems for various fermentations. The ultimate goal of research in this area is to bring the understanding of immobilized whole cells to the level of heterogeneous catalysis. Immobilized whole cell systems are examined from a mass transfer perspective. Evidence for external and internal mass transfer limitations is presented. Procedures for quantifying these effects in terms of effectiveness factors and determining the reaction kinetics in their presence are reviewed. Development of the reactor design equations and the reactor performance results for fermentations with immobilized cells are also discussed.     

Effects of diffusion limitation on immobilized nitrifying microorganisms at low temperatures

Activation energies of suspended and immobilized nitrifying bacteria were determined and compared to determine if diffusion limitation results in decreased sensitivity for temperature. The activation energy for the respiration activity of suspended Nitrosomonas europaea and Nitrobacter agilis was found to be 86.4 and 58.4 kJ mol(-1), respectively. The activation energy for oxygen diffusion in the support material, kappa-carrageenan, determined from the effect of temperature on the effective diffusion coefficient (D), was 17.2 kJ mol(-1). Consequently, the apparent actvation energy of diffusion limited cells should be lower. It was indeed shown that due to the effect of diffusion limitation and to temperature effects on the Monod constant K(s), the immobilized-cell activity was less sensitive to temperature. The apparent activation energy for immobilized Ns. europaea was between 28.6 and 94.2 kJ mol(-1) and for immobilized Nb. agilis between 1.4 and 72.9 kJ mol(-1), depending on the oxygen concentration and temperature. (c) 1995 John Wiley & Sons, Inc.     

Cultureof bovine mammary epithelial cells on collagen gels

A method for the isolation of lobules of acini from bovine mammary gland and their storage in liquid nitrogen is described. After further dissociation of freshly prepared or frozen lobules, clumps of cells are obtained which attach to collagen gels and give rise to colonies which, on morphological criteria, appear predominantly epithelial. Storage for up to 6 months did not adversely affect viability. Increase in colony area involved cell division, was more rapid in air than in 95% oxygen and was enhanced by fetal calf serum.     

New application of single and mixed immobilized cells for furfural biodegradation

In this study, a new application of immobilized microbial cells for biodegradation of furfural in aqueous solution was investigated using spouted bed bioreactor. Pseudomonas sp., as a single type specie as well as activated sludge as mixed cultures were individually immobilized in 3 different bio-carrier matrices which were prepared by reinforcement of natural polysaccharides including sodium alginate, guar-gum and agar-agar with polyvinyl alcohol. The results demonstrated a complete removal (100%) of furfural from aqueous solutions using immobilized cells (IC) of Pseudomonas sp., and mixed cultures as well. Recycling of used IC for furfural removal in successive treatment cycles provided significant removal rates up to 96%. In general, results revealed that IC exhibited better performance compared to free cells in regard with the removal rate of furfural, duration of biodegradation process, as well as the ability for recycling and sustaining the high concentrations of furfural.     

Examination of immobilized cells in a rotating packed drum reactor for the production of ethanol from d-glucose

A rotating packed drum reactor has been proposed as an immobilized whole cell reactor and its performance for ethanol production has been studied with yeast cells immobilized in calcium alginate gel. In a continuous operation with synthetic d-glucose medium containing 125 g d-glucose l^?1, ethanol productivity was 20 g l^?1 h^?1 at a space velocity of 0.38 l (l gel)^?1 h^?1. With intermittent aeration the viability of yeast cells after 270 h of operation remained above 65%. CO₂ removal was easy, but d-glucose conversion was low at a high space velocity.     

Phenotypic stability of mouse mammary tumor cells cultured on collagen gels

Summary This study demonstrates that phenotypic characteristics of androgen-responsive (AR) Shionogi mouse mammary tumors and androgen-independent (AI) derivatives can be maintained in culture. Cells were seeded onto collagen gels in medium containing 2% dextran-characoal-treated fetal bovine serum with or without 0.01 μg/ml dihydrotestosterone (DHT). Androgen-responsive tumors grew more rapidly than AI tumors in vivo and consequently, cells from AR tumors cultured in DHT-containing medium grew faster than cells in DHT-deprived medium and cells from AI tumors. Androgen-responsive tumors had a sheetlike growth pattern; AI tumors formed clumps or irregular cords of cells. Cells from AR tumors cultured in the presence of DHT formed confluent pavements, whereas cells maintained in the absence of DHT and cells from AI tumors formed clusters or cords of cells. Ultrastructurally, cells of AR tumors were elongated; cells of AI tumors were smaller and rounder. These cellular morphologies persisted in culture. Tumorigenicity of cells was assayed by injecting cells s.c. into host mice. Tumors arising from cells of freshly dissociated AR tumors and cells of AR tumors cultured in the presence of DHT appeared more rapidly and grew faster in intact males than in castrated males and intact females. Tumors arising from cells cultured in the absence of DHT and from freshly dissociated or cultured cells of AI tumors had identical rates of appearance and growth in all hosts. This culture system permits these cells to retain their state of malignant progression in vitro and should be a useful model for studying the origin of heterogeneity within tumors and its role in tumor behavior. This work was supported by a grant from the National Cancer Institute of Canada. J. T. E. is a Research Scholar of the National Cancer Institute of Canada.     

Synthesis of -Dopa by Escherichia intermedia cells immobilized in a carrageenan gel

Escherichia intermedia cells were immobilized by entrapment in a carrageenan gel and used for -DOPA synthesis from catechol, pyruvate, and ammonia. A preparation containing 75 mg of cell per gram of gel retained 60–65% of its original activity. The effect of substrate concentrations on the initial rate of -DOPA synthesis was very similar for free and immobilized cells, and substrate inhibition was observed for the three substrates. In batch reactors, up to 7.8 g l⁻¹ of -DOPA was obtained in 20 h (productivity 0.39 g l⁻¹ h⁻¹). Cells immobilized in a carrageenan gel showed higher -DOPA synthesis, in both initial rates conditions and batch reactors, than cells immobilized in a polyacrylamide gel.     

Polyphenoloxidases immobilized in organic gels: Properties and applications in the detoxification of aromatic compounds

Gelatine gels originate from water in oil microemulsions in which the ternary system consists of isooctane/ sulfosuccinic acid bis [2-ethyl hexyl] ester/water; the solubilization of gelatin in the water pool of these microemulsions transforms them into viscous gels in which it is possible to cosolubilize various reactive molecules. These gels were used to immobilize two phenoloxidases, a laccase from Trametes versicolor and a tyrosinase from mushroom. The best balance between gel retention and catalytic activity was reached at a gelatine concentration of 2.5% (w/v) in the case of tyrosinase, while laccase immobilization was independent of gelatine concentration. Both enzymes kept the same optimum pH as the corresponding soluble controls, while a partial loss of activity was observed when they were immobilized. Immobilized enzymes showed an increased stability when incubated for several days at 4 degrees C with a very low release from the gels in the incubation solutions. The immobilization of tyrosinase and of laccase enhanced stability to thermal inactivation. Furthermore, gel-entrapped tyrosinase was almost completely preserved from proteolysis: more than 80% of the activity was maintained, while only 25% of the soluble control activity was detected after the same proteolytic treatments. A column packed with gel-immobilized tyrosinase was used to demonstrate that enzymes immobilized with this technique may be reused several times in the same reaction without loosing their efficiency. Finally, gel-entrapped tyrosinase and laccase were capable of removing naturally occurring and xeno-biotic aromatic compounds from aqueous suspensions with different degrees of efficiency. (c) 1995 John Wiley & Sons, Inc.     

Growth performances ofLactobacillus hilgardii immobilized in dextran gel and in continuous fermentation

A variant ofLactobacillus hilgardii was immobilized by its own production of dextran gel, forming grains. The best rate of weight increase of the gel in continuous fermentation was 16.3±3.3%/h, at pH 4.8±0.1 and with a dilution rate of 0.22 to 0.26/h. Observation by scanning electron microscopy located most of the bacteria as microcolonies on the surface. A similar arrangement appeared in calcium alginate beads. The best population density (10¹⁰ cells/g) was obtained in grains at pH 5.8, after 30h. At a similar pH value, 4.8, the growth rate was higher in alginate beads than in dextran gel but the final population density was approximately the same. Acidification rate increased faster with mixed gel at pH 5.2 than with dextran at pH 5.8.     

A simple correlation for predicting effective diffusivities in immobilized cell systems

A simple correlation method has been developed to predict effective diffusivities of small molecules in heterogeneous materials such as immobilized cell systems. This correlation uses a single diffusivity measurement at one cell volume fraction to predict diffusivities for any other volume fraction of cell. The method has been applied to 20 sets of published diffusivity measurements in immobilized cell systems and accurately predicts affective diffusivities of molecules for the full range of cell fractions. It may also be used to predict effective diffusivities in heterogeneous materials in which the diffusivity of a molecule in each phase and the volume fraction of each phase are known. (c) 1996 John Wiley & Sons, Inc.     

R-mandelic acid production with immobilized recombinant Escherichia coli cells in a recirculating packed bed reactor

A recirculating packed bed reactor (RPBR) was used for efficient production of R-mandelic acid (R-MA) by kinetic resolution of racemic R,S-mandelonitrile (R,S-MN) using the recombinant E. coli cells crosslinked with diatomite (DA)/glutaraldehyde (GA)/polyethyleneimine (PEI). The performance and productivity of RPBR were evaluated by several parameters, including cell load, substrate feeding rate, height diameter (H/D) ratio, reactor structures, and operation stability. The kinetic resolution process showed higher initial reaction rate (1.52?mM/min) and yield (100%) by recycling 100?mL of substrate solution (70?mM) through RPBR packed with 6.0?g immobilized cells at a substrate-feeding rate of 19?mL/min while the H/D ratio was 2.8. The immobilized cells were successfully applied into kinetic resolution of R,S-MN in the RPBR for 50 batches with an average productivity of 4.12?g/L/h for R-MA with >99% of enantiomeric excess.     

Ultrastructural features of bovine mammary epithelial cells grown on collagen gels

Bovine mammary epithelial cells cultured on floating gels of rat tail collagen showed two principal cell types, columnar and squamous, with ultrastructural features resembling secretory and myoepithelial cells respectively. Cultures of freshly prepared cells released alpha-lactalbumin into the culture medium and in some cases contained fat droplets, although these did not appear to be released. No ultrastructural evidence of casein synthesis was observed. A notable feature was the failure to secrete a continuous basement membrane. Intermediate filaments were present in abundance in squamous epithelial cells.     

Diffusion and reaction within porous packing media: a phenomenological model

A phenomenological model has been developed to describe biomass distribution and substrate depletion in porous diatomaceous earth (DE) pellets colonized by Pseudomonas aeruginosa. The essential features of the model are diffusion, attachment and detachment to/from pore walls of the biomass, diffusion of substrate within the pellet, and external mass transfer of both substrate and biomass in the bulk fluid of a packed bed containing the pellets. A bench-scale reactor filled with DE pellets was inoculated with P. aeruginosa and operated in plug flow without recycle using a feed containing glucose as the limiting nutrient. Steady-state effluent glucose concentrations were measured at various residence times, and biomass distribution within the pellet was measured at the lowest residence time. In the model, microorganism/substrate kinetics and mass transfer characteristics were predicted from the literature. Only the attachment and detachment parameters were treated as unknowns, and were determined by fitting biomass distribution data within the pellets to the mathematical model. The rate-limiting step in substrate conversion was determined to be internal mass transfer resistance; external mass transfer resistance and microbial kinetic limitations were found to be nearly negligible. Only the outer 5% of the pellets contributed to substrate conversion. (c) 1993 Wiley & Sons, Inc.     

Characterization of nitrifying bacteria immobilized in calcium alginate

Activated sludge has been fed with a medium containing ammonium ions as the sole nitrogen source. Biomass collected from this continuous culture was immobilized in calcium alginate. The influence of pH, temperature, and the size and cell load of the biocatalyst beads on the nitrifying activity was determined, as well as the storage and operational stability of the system. The results are compared with those obtained with Nitrosomonas europaea. It has been concluded that the mixed culture is more difficult to work with than the pure strain and that the reproducibility of the results is lower. The trends found, however, were largely similar, except for the operational stability which was poorer in the case of the immobilized mixed culture.     

Studies on neomycin production using immobilized cells of<Emphasis Type="Italic">S marinensis</Emphasis> NUV-5 in various reactor configurations: A technical note

Conclusion  Stirred tank, fluidized bed, and airlift reactors produced similar neomycin activity with immobilized cells. Packed bed reactor clearly under performed, probably because of insufficient aeration or mixing. Neomycin production using immobilized cells in fermentors requires good mixing and aeration.     

Oxygen supply to immobilized cells: 1. Oxygen production by immobilized Chlorella pyrenoidosa

Oxygen supply at high cell densities of aerobic organisms is a great problem in immobilized cell preparations. To investigate the possibility of in situ oxygen generation the alga Chlorella pyrenoidosa was immobilized on alginate beads. The conditions for optimal oxygen production were investigated and in long term experiments the preparations were successful for at least 30 days.     

Degradation kinetics of phenol by immobilized cells of Candida tropicalis in a fluidized bed reactor

Degradation kinetics of phenol by free and agar-entrapped cells of Candida tropicalis was studied in batch cultures. The initial phenol degradation rate achieved with free cells was higher than that obtained with immobilized cells, when phenol concentrations up to 1000 mg l^–1 were used. However, at higher phenol concentrations, the behaviour was quite different. The initial degradation rate of the immobilized yeast cells was about 10 times higher than that of the free cells, at a phenol concentration of 3500 mg l^–1. The semicontinuous and continuous degradation of phenol by immobilized yeast cells was also investigated in a multi-stage fluidized bed reactor. The highest phenol removal efficiencies and degradation rates as well as the lowest values of residual phenol and chemical oxygen demand were obtained in the semicontinuous culture when phenol concentrations up to 1560 mg l^–1 were used.     

Microbial transformation of validamycin A to valienamine by immobilized cells

Immobilized Pseudomonas sp. HZ519 cells have been used for transformation of validamycin A to valienamine and the degradation pathway of validamycin A by Pseudomonas sp. HZ519 has also been studied. Substrate inhibition in immobilized cell system was avoided. An average of 8.6 g L^-1 valienamine concentration was obtained when concentration of validamycin A was increased up to 120 g L^-1. Through a treatment of the immobilized cells with 0.3 mol L^-1 substrate, the activity of the immobilized cells was increased distinctly. Compared with free cells, the productivity of valienamine by CA-immobilized cells was improved about three times. The reusability of the immobilized cells was evaluated with repeated-batch degradation experiments. The Tiele modulus was obtained from the experimental effectiveness factor. The result showed that the degradation process in the immobilized system was governed by intraparticle diffusion and chemical reaction.     

Influence of selected physical parameters on the biodegradation of acrylamide by immobilized cells of Rhodococcus sp.

The influences of concentration of acrylamide, pH, temperature, duration of storage of encapsulated cells and presence of different metals and chelators on the ability of immobilized cells of a Rhodococcus sp. to degrade acrylamide were evaluated. Immobilized cells (3 g) rapidly degraded 64 and 128 mM acrylamide in 3 and 5 h, espectively, whereas free cells took more than 24 h to degrade 64 mM acrylamide. An acrylamide concentration of 128 mM inhibited the growth of the free cells. Immobilized bacteria were slow to degrade acrylamide at 10 °C. Less than 60% of acrylamide was degraded in 4 h. However, 100% of the compound was degraded in less than 3 h at 28 °C and 45 °C. The optimum pH for the degradation of acrylamide by encapsulated cells was pH 7.0. Less than 10% of acrylamide was degraded at pH 6.0, while ca. 60% of acrylamide was degraded at pH 8.0 and 8.5. Copper and nickel inhibited the degradation, suggesting the presence of sulfhydryl (-SH) groups in the active sites of the acrylamide degrading amidase. Iron enhanced the rates of degradation and chelators (EDTA and 1,10 phenanthroline) reduced the rates of degradation suggesting the involvement of iron in its active site(s) of the acrylamide-degrading-amidase. Immobilized cells could be stored up to 10 days without any detectable loss of acrylamide-degrading activity.