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.     

Phenanthrene biodegradation by immobilized microbial consortium in polyvinyl alcohol cryogel beads

Removal of polycyclic aromatic hydrocarbons (PAHs), a group of widespread toxic compounds, has been one of the environmental issues in wastewater treatment systems for many years. In this study, biodegradation of phenanthrene (PHE), as a model contaminant, by a microbial consortium entrapped in polyvinyl alcohol (PVA) cryogel prepared by freeze-thaw method was investigated. The effect of inoculum size (300–900 mg of cell dry weight per liter) and initial PHE concentration (100–2000 ppm) as well as bead cell density (5 and 10 mg ml⁻¹) on PHE biodegradation by freely suspended cell (FC) and immobilized cell (IC) systems in aqueous phase was examined. Results showed that although both IC and FC systems were capable of complete removal of 100 and 250 ppm of initial PHE (as sole carbon and energy sources), incomplete PHE removals were observed at higher initial PHE concentrations up to 2000 ppm after 7 days. IC system resulted in the maximum PHE removal of 400 ppm at initial PHE concentration of 750 ppm and inoculum size of 600 mg l⁻¹, while under these conditions FC system removed 310 ppm of PHE. Moreover, bead cell density was shown to affect the performance of IC system, with the lower density of 5 mg ml⁻¹ leading to a higher PHE removal due to the enhanced transport phenomena in the culture. Additionally, a correlation was proposed to predict PHE biodegradation at a range of initial PHE concentrations.     

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.     

Diffusion in gels containing immobilized cells: a critical review

Eleven experimental investigation of diffusion in gels containing immobilized cells are reviewed. The experimental data, which quantitatively express the diffusion coefficient as a function of the cell concentration, are compared with a number of well-known equations developed for mass transfer in heterogeneous media. Based on this comparison, a procedure for the theoretical prediction of effective diffusion coefficients in cell-containing gels is recommended.     

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.     

Ethanol production from whey permeate by immobilized yeast cells

The ability of two yeast strains to utilize the lactose in whey permeate has been studied. Kluyveromyces marxianus NCYC 179 completely utilized the lactose (9.8%), whereas Saccharomyces cerevisiae NCYC 240 displayed an inability to metabolize whey lactose for ethanol production. Of the two gel matrices tested for immobilizing K. marxianus NCYC 179 cells, sodium alginate at 2% (w/v) concentration proved to be the optimum gel for entrapping the yeast cells effectively. The data on optimization of physiological conditions of fermentation (temperature, pH, ethanol concentration and substrate concentration) showed similar effects on immobilized and free cell suspensions of K. marxianus NCYC 179, in batch fermentation. A maximum yield of 42.6 g ethanol l^?1 (82% of theoretical) was obtained from 98 g lactose l^?1 when fermentation was carried at pH 5.5 and 30°C using 120 g dry weight l^?1 cell load of yeast cells. These results suggest that whey lactose can be metabolized effectively for ethanol production using immobilized K. marxianus NCYC 179 cells.     

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.     

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.     

Protease production by free and immobilized cells of the cold-adapted yeast Cryptococcus victoriae CA-8

The present study was performed to produce the protease using free and immobilized cells of locally isolated cold-adapted psychrotolerant yeast Cryptococcus victoriae CA-8. Cell immobilization was performed using sodium alginate as entrapping agent. The best conditions for enzyme production by both free and immobilized cells of the yeast were temperature of 15°C and initial pH of 8.0. The optimal incubation times were 72 and 96 h for immobilized and free cells, respectively. Immobilized cells were reused in 3 successive reaction cycles without any loss in the maximum protease activity. Little decreases in the protease activity were observed in 4 and 5 cycles. Under the optimized conditions, the maximum enzyme activities were determined as 12.1 and 13.5 U/mL for free and immobilized cells, respectively. This is a first attempt on cold-active alkaline protease production by free and/or immobilized cells of yeasts. Besides, the protease activity of the yeast C. victoriae CA-8 was investigated for the first time in the present study.     

Mass transfer effects on the reaction rate for heterogeneously distributed immobilized yeast cells

Here we examine the efficiency of different immobilized cell gradients applied to immobilized Saccharomyces cerevisiae fermenting glucose to ethanol. We developed a simulation model to fully study the competing effects of mass transfer hindrance and kinetics. It is based on a diffusion-reaction model and can be used to analyze the different cell concentration profiles inside an immobilized gel bead, in terms of effectiveness factors, productivity, and mass flux. The internal diffusion coefficient, which varies with the local cell concentration, as well as the external mass transfer, is taken into account when describing the efficiency. Although the diffusion hindrance is greater at higher cell concentrations, high cell concentration is still advantageous in the present case because the increase in reaction rate outweighs the diffusion hindrance. Thus, high cell concentrations contribute to increased productivity. The influence of the cell concentration gradient on the efficiency of the beads is negligible. Within the range of cell profiles studied it has been established that the location of the cells within the bead is of lesser importance. However, a steep cell gradient increases the importance of the external mass transfer.     

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.     

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.     

Characterization of microbial traits associated with glyphosate biodegradation in industrial activated sludge

Summary The microorganisms from two industrial (I1, I2) activated sludges that treat glyphosate (N-phosphonomethyl glycine) wastes and one domestic (D1) sludge were enumerated by microscopic examination and by the use of eight selective media. I1 and I2 had higher total counts but fewer pseudomonads and no yeasts. The enumerations correlated directly with traditional biological performance measurements. A total of 393 microbial strains were isolated from the sludges to correlate the occurrence and relationship of glyphosate-degrading activity (GDA) to 155 biochemical and morphological characteristics. Each activated sludge contained unique bacterial populations with the microbes treating industrial wastes, capable of utilizing a wide range of carbohydrates. Numerical taxonomy (arithmetic average linkage) using simple matching and Jaccard coefficients confirmed that there were five (D1), three (I1), and 12 (I2) clusters. GDA was found in only a small portion of the industrial clusters and did not correlate with any other characteristic tested, even though the GDA strains had a large phenotypic diversity. This suggests that GDA is not a universal trait and its expression requires enrichment through specific selective pressures.     

Comparative evaluation of pectolytic and proteolytic enzyme production by free and immobilized cells of some strains of the phytopathogenic Erwinia chrysanthemi

Whole cells of the phytopathogenic Erwinia chrysanthemi strains were immobilized in k-carrageenan and grown in high-calcium Xanthomonas campestris medium containing sodium polypectate as carbon source. All the strains used survived immobilization into k-carrageenan beads. Immobilized E. chrysanthemi strains displayed higher pectolytic and proteolytic enzyme activities than free cells in liquid suspension. Carrageenan immobilization techniques could provide a system to mimic the conditions of E. chrysanthemi cells in the infected plant tissue. This could prompt a thorough study of the factors governing the biosynthesis of virulence factors by this bacterium. Journal of Industrial Microbiology & Biotechnology (2001) 27, 215–219. Received 04 April 2001/ Accepted in revised form 12 June 2001     

Surfactant aided biodegradation of pyrene using immobilized cells of Mycobacterium frederiksbergense

Low aqueous phase solubility is the major limiting factor in successful biodegradation of pyrene and other polycyclic aromatic hydrocarbons (PAH), which can, however, be overcome by using a suitable surfactant. Biodegradation of pyrene by immobilized cells of Mycobacterium frederiksbergense in presence of non-ionic surfactant Tween 80 was evaluated. For cell immobilization, beads were prepared using calcium alginate as the immobilizing material based on immobilized cell viability and mechanical stability of the beads. Complete degradation of pyrene was achieved employing the immobilized cells in batch shake flask experiments for all four different initial concentrations of the PAH at 100 mg l⁻¹, 200 mg l⁻¹, 400 mg l⁻¹ and 1000 mg l⁻¹. The experimental results of biodegradation of pyrene at very high initial concentration of 1000 mg l⁻¹ using the cell immobilized beads was further investigated in a 3 l fermentor operated at controlled conditions of 150 rpm, 28 °C, pH 7 and 1.5 l min⁻¹ aeration. The results confirmed complete degradation of the PAH with a very higher degradation rate of 250 mg l⁻¹ d⁻¹, which is so far the highest value reported for pyrene biodegradation.     

Biodegradation of N-methylated carbamates by free and immobilized cells of newly isolated strain Enterobacter cloacae strain TA7

A bacterial strain (TA7) capable of consuming three N-methylated carbamates as sole nitrogen and carbon source was isolated and identified as “Enterobacter cloacae” on the basis of 16S rRNA, from carbamate contaminated agricultural soil by enrichment culture technique. The agar entrapment was used to immobilize the bacterial cells. Both the free as well as the immobilized cells were used to study the degradation of three carbamets viz. aldicarb, carbofuran, and carbaryl. The immobilized cells degraded all the three carbamates much faster than their free cell counterparts. The biodegradation kinetics of aldicarb, carbaryl, and carbofuran was studied using 50 ppm as initial concentration in the presence of free cells. The average values of K_s for aldicarb, carbofuran, and carbaryl were 22.6, 17.87, and 8.9 mg/L, respectively, whereas the values for µ_max were calculated as 1.35, 1.3, and 1.2 mg/l/h^?1. The results indicated that the bacterium has high affinity towards all the three carbamates. However, relatively higher affinity is for carbaryl, in comparison with carbofuran and aldicarb. Results indicate the potential of E. Cloacae TA7 to remediate N-methylated carbamates polluted water and soil.     

Biotransformation of furfural and 5-hydroxymethyl furfural by enteric bacteria

Summary A survey was conducted with seventeen enteric bacterial strains (including the generaKlebsiella, Enterobacter, Escherichia, Citrobacter, Edwardsiella andProteus) to examine their ability to transform furfural and 5-hydroxymethyl furfural (5-MHF). The enteric bacteria were able to convert furfural to furfuryl alcohol under both aerobic and anaerobic conditions in a relatively short incubation time of 8 h. 5-HMF was transformed by all the enteric bacteria studied to an unidentified compound postulated to be 5-hydroxymethyl furfuryl alcohol, which had an absorbance maximum of 222 nm. These bacteria did not transform furfuryl alcohol or 2-furoic acid. The enteric bacteria did not use furfural, 5-HMF, furfuryl alcohol or 2-furoic acid as sole source of carbon and energy. Biotransformation of furfural and 5-HMF was accomplished by co-metabolism in the presence of glucose and peptone as main substrates. The rate of transformation was similar under both aerobic and anaerobic conditions. These transformations are likely to be of value in the detoxification of furfurals, and in their ultimate conversion to methane and CO₂ by anaerobic digestion.     

New enzymatic immobilized biocatalysts for detoxification of organophosphorus compounds

New immobilized biocatalysts based on phosphotriesterase and porous fabric materials impregnated with chemically cross-linked chitosan and sulphate chitosan gels were investigated. Analysis of the rheological characteristics of enzyme-containing gels confirmed their high plasticity and mechanical strength, while scanning electron microscopy verified their macroporous structure. The fabric matrix could absorb and retain a large amount of liquid thereby increasing its own weight 3.5-4.5 fold. The catalytic characteristics of the immobilized biocatalyst hydrolyzing Paraoxon, Coumaphos, Chlorpyrifos and Diisopropyl fluorophosphate were investigated. The catalytic efficacy of the soluble enzyme was 3.0-5.5-times higher compared to the immobilized form mainly due to the lower K_m values. With constant 55-60% humidity the biocatalyst retained 77% and 67-70% activity after 50-day storage at 4°C and 23°C, respectively. Benzalkonium chloride appeared to be an appropriate preservative for long-term storage of immobilized biocatalyst in a wet state.     

Kinetics of biodegradation of p-xylene and naphthalene and oxygen transfer in a novel airlift immobilized bioreactor

The scope of this study included the biodegradation performance and the rate of oxygen transfer in a pilot-scale immobilized soil bioreactor system (ISBR) of 10-L working volume. The ISBR was inoculated with an acclimatized population of contaminant degrading microorganisms. Immobilization of microorganisms on a non-woven polyester textile developed the active biofilm, thereby obtaining biodegradation rates of 81 mg/L x h and 40 mg/L x h for p-xylene and naphthalene, respectively. Monod kinetic model was found to be suitable to correlate the experimental data obtained during the course of batch and continuous operations. Oxygen uptake and transfer rates were determined during the batch biodegradation process. The dynamic gassing-out method was used to determine the oxygen uptake rate (OUR) and volumetric oxygen mass transfer, K(L) a. The maximum volumetric OUR of 255 mg O(2)/L x h occurred approximately at 720-722 h after inoculation, when the dry weight of biomass concentration was 0.67 g/L.     

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.