Radioactive penicillin G production by immobilized fungal vesicles

Summary Radioactive penicillin G production from l-[1-¹⁴C]-valine (1.75 GBq · mmol^-1) by native and by calcium alginate gel immobilized mycelium of Penicillium chrysogenum PQ-96 in a medium for antibiotic production as well as by vesicles isolated from the protoplasts of the same strain in a well-defined reaction mixture was investigated. Specific radioactivity of the penicillin G produced by the native vesicles was 1.45 GBq · mmol^-1 and that of the antibiotic synthesized by the calcium alginate gel immobilized vesicles was 1.48 GBq · mmol^-1. By comparison, the specific radioactivity of penicillin G produced by native mycelium was 0.42 GBq · mmol^-1 and of that synthesized by the immobilized mycelium was 0.96 GBq · mmol^-1. Production of radioactive penicillin G by native and immobilized vesicles in repeated use was also investigated. At the beginning of the production phase, the radioactive penicillin G synthesized by the immobilized vesicles was 25 nmol · mg protein^-1 · h^-1 and decreased after 8 days to a level of 11 nmol · mg protein^-1 · h^-1. The half-life of the immobilized vesicles was 7 days. The native vesicles showed a rapid decrease in radioactive antibiotic production. In comparison, the penicillin G production in a repeated use of immobilized vesicles decreased during 40 days from 140 nmol · mg protein^-1 · h^-1 to 60 nmol · mg protein^-1 · h^-1. The half-life of the immobilized vesicles was 35 days. The native vesicles showed after 4 days a lack of activity of penicillin G production. The stability of immobilized mycelium or vesicles in the process of radioactive penicillin G production is discussed.     

Continuous degradation of phenol(s) by Pseudomonas putida P8 entrapped in polyacrylamidehydrazide

Summary The continuous degradation of phenol by immobilized cells of Pseudomonas putida P8 under different conditions was investigated. The bacterial cells were entrapped in polyacrylamidehydrazide (PAAH) and cultivated in a columnar fluidized-bed bioreactor. Working with a dilution rate of 0.067 h^-1 the phenol content in the feed was varied to find the capacity of an one-stage system with complete phenol degradation.Under sterile conditions and with phenol as the sole carbon source a degradation rate of 7.2 g·l^-1·d^-1 was reached whereas in non-sterile waste water only 3.12 g·l^-1·d^-1 were degraded. In any case the immobilized cells showed a stable phenol degradation activity and even simultaneously fed cresols or 4-chlorophenol were utilized completely.     

Continuous production of gibberellic acid in a fixed-bed reactor by immobilized mycelia of Gibberella fujikuroi in calcium alginate beads

Summary The continuous production of gibberellic acid with immobilized mycelia of Gibberella fujikuroi was maintained over a hundred days in a tubular fixed-bed reactor. Free mycelium at the beginning of the storage phase was harvested from G. fujikuroi shake-flask culture and was immobilized by ionotropic gelation in calcium alginate beads.The continuous recycle production system consisted of a fixed-bed reactor, a container in which the culture medium was heated, stirred and aerated, and valves for sample withdrawal or reactant addition during the first 1320 h (55 days). A two-phase continuous extractor was then added for the last 960 hours (40 days). Free and immobilized mycelium shake-flask cultures with the same strain used in the continuous culture system were also realized to compare growth, maintenance and production parameters. The results show about the same gibberellic acid productivity in both free and immobilized mycelium shakeflask cultures: 0.384 and 0.408 mgGA₃·gBiomass^-1 ·day^-1, respectively, whereas in the continuous system the gibberellic acid production is about twice as large for a similar biomass: 0.768 mgGA₃·gBiomass^-1·day^-1. Several factors affecting the overall productivity of the immobilized systems were found to be: the quality and the quantity of mycelia in the biocatalyst beads and the immobilization conditions.     

Degradation of malic acid in wine by immobilized Issatchenkia orientalis cells with oriental oak charcoal and alginate

Aims: To test degradation of malic acid content in wine by immobilized Issatchenkia orientalis KMBL 5774 cells recently isolated from Korean wine pomace as a malic acid‐degrading yeast. Methods and Results: I. orientalis KMBL 5774 cells were immobilized using a mixture of oriental oak (Quercus variabilis) charcoal with sodium alginate. When the immobilized yeast cells were observed on a scanning electron microscope, cells were efficiently immobilized on the surface area of the charcoal. A Korean wine containing a high level of malic acid was treated with the immobilized yeast cells. The HPLC analysis of the malic acid content in the treated wine showed the malic acid content was reduced to 0·75 mg ml^?1 after treatment from the original content of 8·96 mg ml^?1, representing 91·6% of the malic acid was degraded during the treatment. Conclusions: The immobilization of the malic acid‐degrading yeasts with oriental oak charcoal and sodium alginate is useful for degradation of malic acid in wines containing a high level of malic acid with no significant increase in other acids. Significance and Impact of the study: Malic acid is sometimes detrimental to the quality of wines when present at high concentrations in some varieties. The immobilized I. orientalis KMBL5774 cells appear to be a promising candidate in view of developing biotechnological methods for reduction of malic acid contents in wine.     

Synthesis of l-dopa by escherichia intermedia cells immobilized in a polyacrylamide gel

Summary Escherichia intermedia cells were immobilized by entrapment in a polyacrylamide gel and used for l-dopa synthesis from pyrocatechol, pyruvate and ammonia. An immobilized cell preparation containing 75 mg cells/g gel retained 45%–50% of the activity of free cells. The effect of temperature, pH and substrate concentration of the initial rate of l-dopa synthesis was very similar for free and immobilized cells. Substrate inhibition was observed for pyrocatechol, pyruvate and ammonia. In a batch reactor, 5.4 g·l^-1 l-dopa was obtained, with 100% conversion yield of pyrocatechol and l-dopa productivity of 0.18 g·l^-1·h^-1. The use of a pyrocatechol-borate complex decreased by-product formation and catalyst inactivation.     

Direct alcoholic fermentation of starchy biomass using amylolytic yeast strains in batch and immobilized cell systems

Summary Direct alcoholic fermentation of dextrin or soluble starch with selected amylolytic yeasts was studied in both batch and immobilized cell systems. In batch fermentations, Saccharomyces diastaticus was capable of fermenting high dextrin concentrations much more efficiently than Schwanniomyces castellii. From 200 g·l^–1 of dextrin S. diastaticus produced 77 g·l^–1 of ethanol (75% conversion efficiency). The conversion efficiency decreased to 59% but a higher final ethanol concentration of 120 g·l^–1 was obtained with a medium containing 400 g·l^–1 of dextrin. With a mixed culture of S. diastaticus and Schw. castellii 136 g·l^–1 of ethanol was produced from 400 g·l^–1 of dextrin (67% conversion efficiency). S. diastaticus cells attached well to polyurethane foam cubes and a S. diastaticus immobilized cell reactor produced 69 g·l^–1 of ethanol from 200 g·l^–1 of dextrin, corresponding to an ethanol productivity of 7.6g·l^–1·h^–1. The effluent from a two-stage immobilized cell reactor with S. diastaticus and Endomycopsis fibuligera contained 70 g·l^–1 and 80 g·l^–1 of ethanol using initial dextrin concentrations of 200 and 250 g·l^–1 respectively. The corresponding values for ethanol productivity were 12.7 and 9.6 g·l^–1·h^–1. The productivity of the immobilized cell systems was higher than for the batch systems, but much lower than for glucose fermentation.     

Intraparticle mass-transfer resistance and apparent time stability of immobilized yeast alcohol dehydrogenase

The stability and, consequently, the lifetime of immobilized enzymes (IME) are important factors in practical applications of IME, especially so far as design and operation of the enzyme reactors are concerned. In this paper a model is presented which describes the effect of intraparticle diffusion on time stability behaviour of IME, and which has been verified experimentally by the two-substrate enzymic reaction. As a model reaction the ethanol oxidation catalysed by immobilized yeast alcohol dehydrogenase was chosen. The reaction was performed in the batch-recycle reactor at 303 K and pH-value 8.9, under the conditions of high ethanol concentration and low coenzyme (NAD⁺) concentration, so that NAD⁺ was the limiting substrate. The values of the apparent and intrinsic deactivation constant as well as the apparent relative lifetime of the enzyme were calculated.The results show that the diffusional resistance influences the time stability of the IME catalyst and that IME appears to be more stabilized under the larger diffusion resistance.List of Symbols C _A, C_B, C_E mol · m^–3 concentration of coenzyme NAD⁺, ethanol and enzyme, respectively - C _p mol · m³ concentration of reaction product NADH - d _p mm particle diameter - D _eff m² · s^–1 effective volume diffusivity of NAD⁺ within porous matrix - k _d s^–1 intrinsic deactivation constant - K _A, K_A, K_B mol · m^–3 kinetic constant defined by Eq. (1) - K _A ^x mol · m^–3 kinetic constant defined by Eq. (5) - r _A mol · m^–3 · s^–1 intrinsic reaction rate - R m particle radius - R _v mol · m^–3 · s^–1 observed reaction rate per unit volume of immobilized enzyme - t _E s enzyme deactivation time - t _r s reaction time - V mol · m^–3 · s^–1 maximum reaction rate in Eq. (1) - V ^x mol · m^–3 · s^–1 parameter defined by Eq. (4) - V _f m³ total volume of fluid in reactor - w _s kg mass of immobilized enzyme bed - factor defined by Eqs. (19) and (20) - kg · m^–3 density of immobilized enzyme bed - unstableness factor - effectiveness factor - Thiele modulus - relative half-lifetime of immobilized enzyme Index o values obtained with fresh immobilized enzyme     

Degradation of caffeine by immobilized cells of Pseudomonas putida strain C 3024

Summary A caffeine-resistant strain of Pseudomonas putida was isolated from soil and was grown with caffeine as the sole source of carbon, energy and nitrogen. Cells were immobilized in agar gel particles which were continuously supplied with a caffeine solution (0.52 g · l^–1, D=1.0 h^–1) in a homogeneously mixed aerated reaction vessel. In the presence of the ATPase inhibitor arsenate the caffeine was removed by the immobilized cells at an average rate of 0.25 mg caffeine · h^–1 · (mg cell carbon)^–1 during 6 days. Thereafter a rapid decline of activity was observed. From a similar system without arsenate supplied with a growth medium containing a limiting amount of caffeine (0.13 g · l^–1) the caffeine was almost completely oxidized by the immobilized cells. The concentration of the remaining caffeine was 1.4 mg · l^–1, which is much lower than the substrate constant for caffeine (9.7 mg · l^–1) observed with freshly harvested suspended resting cells.     

Continuous production of itaconic acid by Aspergillus terreus immobilized in a porous disk bioreactor

Summary Aspergillus terreus NRRL 1960 was grown on porous disks rotating intermittently in and out of the liquid phase. This immobilized fungal cell bioreactor was used to produce itaconic acid from glucose in a continuous operation. The effect of temperature, pH, disk rotation speed, and feed rate on the itaconic acid concentration and volumetric productivity were studied. The highest itaconic acid concentration and volumetric productivity obtained were 18.2 g/l and 0.73 g/l·h, respectively, under the following conditions: temperature at 36°C, pH 3.0, disk rotation speed at 8 rpm, and feed rate at 60 ml/h. These results are better than those by conventional fermentation or by other immobilized method.Nomenclature F feed rate (l/h) - K _1s saturation constant for immobilized cells (g/l) - K _2s saturation constant for suspended cells (g/l) - M ₁ increased mass of immobilized cells (g) - M ₂ total mass of immobilized cells (g) - P concentration of itaconic acid (g/l) - S substrate concentration in and out of the reactor (g/l) - S ₀ substrate concentration in the feed (g/l) - V liquid volume of the reactor (1) - X concentration of the suspended cells (g/l) - Y ₁ apparent yield of the immobilized cells (g cells/g substrate) - Y ₂ apparent yield of the suspended cells (g cell/g substrate) - Y ₃ apparent yield of itaconic acid (g itaconic acid/g substrate) - m ₁ maintenance and by-products coefficient of the immobilized cells (g substrate/g cell·h) - m ₂ maintenance and by-products coefficient of the suspended cells (g substrate/g cell·h) - µ_1max maximum specific growth rate of the immobilized cells (h^-1) - µ_2max maximum specific growth rate of the suspended cells (h^-1)     

Metabolic activity of yeast immobilized as supported monolayer

Summary Immobilization of Saccharomyces cerevisiae as a monocellular layer adhering to a glass support has been achieved by adsorbing Al or Fe(III) ions on the cells or by coating the support with Al(OH)₃ or Fe₂O₃ particles. The initial rate of glucose to ethanol conversion was measured in pure glucose solutions for free cells in suspension, either untreated or submitted to the chemical treatments used for immobilization, and for immobilized cells, using a small reactor (50–70 ml) in closed circuit. The conversion rate of immobilized cells is in the range of 3.5 to 5×10^-14 mol/cell·h while that of untreated suspended cells is in the range of 5 to 7×10^-14 mol/cell·h.     

Biodegradation of 4-chlorophenol by entrappedAlcaligenes sp. A 7-2

Summary The degradation of 4-chlorophenol by free and by Ca-alginate-immobilized cells ofAlcaligenes sp. A 7-2 has been studied. Increasing concentrations of 4-chlorophenol (0.4–0.55 mM) were better tolerated and more quickly degraded by the immobilized organisms than by free cells. The capability for haloarene-degradation is inducible. In semicontinuous fermentation at pH 7 a minimal degradation time of 5 h for degrading 0.2 mM 4-chlorophenol was reached. Fermentation temperature was shown to be important for inducing the degradation capability, but to be less important for the degradation rate by induced organisms. High-frequency feeding of small amounts of 4-chlorophenol (0.05 mM) was more favourable than low-frequency feeding of larger amounts (0.15 mM).Continuous fermentation with unbuffered medium allowed a degradation rate of about 2 mmol·l^-1·d^-1; with buffered medium a higher degradation rate of nearly 4 mmol·l^-1·d^-1 was reached, but the Ca-alginate beads dissolved.     

Dynamics of production oftrans-zeatin andtrans-zeatin riboside by immobilized cytokinin-autonomous and cytokinin-dependent tobacco cells

Two strains of cultured tobacco cells (Nicotiana tabacum L. cv. Wisconsin 38) differing in their requirement for exogenous cytokinins (cytokinin-dependent and cytokinin-autonomous) were immobilized on polyphenylenoxide (Sorfix) activated with glutaraldehyde. Columns packed with immobilized cells were continually eluted with diluted Murashige and Skoog's medium lacking or supplemented with synthetic cytokinin (6-benzylaminopurine; BA). Purified samples of column eluates were fractionated by HPLC, andtrans-zeatin (t-Z) andtrans-zeatin riboside (t-ZR) content was estimated by enzyme immunoassay. Both cytokinin-autonomous and cytokinin-dependent tobacco cells produced and excretedt-Z and its riboside, and there were significant quantitative differences between the strains. The steady-state excretion rate oft-Z was 19.8 ng · g^–1 dw · h^–1 and 4 ng · g^–1 dw · h^–1, respectively, and that oft-ZR 4 ng · g^–1 dw · h^–1 and 1 ng · g^–1 dw · h^–1, respectively. Exposure of cytokinin-dependent cells to BA after 72 h of starving for this synthetic cytokinin caused temporary increase in excretion of both zeatin and its riboside. After the application of 5 M BA for 24 h, the excretion rate oft-ZR reached 5 ng · g^–1 dw · h^–1 (5-fold increase), and that oft-Z achieved 12 ng · g^–1 dw · h^–1 (3-fold increase). The elevation oft-Z excretion was delayed about 13 h compared witht-ZR excretion, which started increasing almost immediately after BA application. A pulse of BA in lower concentration (1.5 M for 30 h) provoked lower response.     

Evaluation of alginate-immobilized Lactobacillus casei for lactate production

Summary Lactate production by immobilized Lactobacillus casei has been studied. The cells were immobilized in alginate and the effect of variations in different parameters on product formation and productivity was investigated. The performance of the reaction was evaluated in stirred batch as well as in packed-bed conditions. pH control was a problem in the packed-bed reactor. In stirred batch experiments, nearly total glucose utilization was observed with a lactate yield of 90–99% and a total productivity of 1.6 g·l^–1·h^–1. Under standard conditions only a low percentage (3–4%) of the total lactate formed was the abetd-isomer. When immobilized cells were reused, increased formation of abetd-lactate took place, especially when the cell conditions were sub-optimal. After revitalization by exposure to growth nutrients the balance was restored.On leave from Microbiology Institute, Zhejiang Academy of Agricultural Sciences, Hangzhou-310021, China Offprint requests to: Bo Mattiasson     

Membrane enzyme reactor with simultaneous separation using electrophoresis

A membrane enzyme reactor with simultaneous separation was investigated. Enzymes, urease and aspartase, were immobilized by a porous polytetrafluoroethylene membrane. Electrical field was applied in the medium while the reaction was carried out. Products with electrical charge could be separated through the membrane from the reaction medium as they were formed. Reaction behavior was analyzed by a simple model considering both pore-migration and reaction in the skelton of the membrane. According to the analysis the inherent reaction rate of the immobilized enzymes decreases significantly. This is probably caused by the structural variation of enzymes. For the case of urease, the change of pH inside the membrane may also cause the decrease of the reaction rate. The model analysis showed that the enzyme content in the membrane and the residence time of the substrate in the membrane governed overall extent of reaction.List of Symbols e g (dm³)^–1 enzyme concentration in the membrane - L cm membrane thickness - K _m mM Michaelis constant - Rate mmol · min^–1 · g^–1 rate of product formation per unit weight of enzyme - S mM substrate concentration - S _in mM inlet substrate concentration - S _out mM outlet substrate concentration - u cm · min^–1 migration rate - V V voltage between the electrodes - V _m mmol · min^–1 · g^–1 maximum reaction rate - X conversion - z cm distance from the surface inside the membrane - void fraction of the porous membrane - tortuosity of the membrane - min space time     

Ammonium photoproduction by free and immobilized cells of Chlamydomonas reinhardtii

Summary Free-living or immobilized Chlamydomonas reinhardtii cells photoproduce ammonium from nitrite in a medium containing 1 mM of l-methionine-d,l-sulphoximine (MSX). Ammonium is accumulated in the medium to 8 mM final concentration, which inhibits nitrite uptake by the MSX-treated cells and consequently the excretion of ammonium is blocked. However, if ammonium was removed from the medium and nitrite and MSX periodically restored, the photoproduction process could be maintained over 96 h, with a final ammonium concentration of about 18 mM for free-living cells and 28 mM for immobilized ones. The MSX-treated cells showed a photoproduction productivity of 1300 mol NH ₄ ⁺ · mg chlorophyll (Chl)^-1, with an average production rate of 14 mol NH ₄ ⁺ · mg Chl^-1 per hour, for calcium alginate-entrapped cells, while the corresponding data for free-living ones was 650 mol NH ₄ ⁺ · mg Chl^-1 and 6.7 mol NH ₄ ⁺ · mg Chl^-1 per hour, respectively. Immobilized cells showed a significant increase in the nitrite uptake rate, probably due to a change in membrane permeability as a consequence of cell-matrix interactions.     

Carbon dioxide and biearbonate in cell division

Summary The effects of carbon dioxide and of bicarbonate on cell division were studied on synchronized cells of the high-temperature green alga, Chlorella 7-11-05. After 7 hours of growth in nutrient medium in light, cells were centrifuged and resuspended in distilled water or in bicarbonate and placed in darkness. Atmospheric air, or a mixture of carbon dioxide and air, was bubbled through algal suspensions during the dark period. In distilled water cells readily divided in atmospheric air but not in 1% (2.6·10^-4 M) or in higher concentrations of carbon dioxide. The suspension of cells in bicarbonate counteracted the inhibitory action of carbon dioxide. A minimum molar concentration of bicarbonate necessary to counteract the inhibitory effect of carbon dioxide was found to be equal to the molar concentration of carbon dioxide in the suspending fluid. The highest concentration of carbon dioxide, the adverse effect of which could not be balanced by any concentration of bicarbonate, was found to be in the vicinity of 1.3·10^-2 M (50% CO₂ in air). Possible effects on cell division of the change in Ph and the implicated role of carbon dioxide in normal and neoplastic growth were discussed.     

Production of l-glutamate by immobilized protoplasts

Summary Protoplasts of Brevibacterium flavum cultured in a medium containing 50 g·l^-1 of biotin were prepared with lysozyme and immobilized in matrices of agar-acetylcellulose filters. The immobilized protoplasts were applied to l-glutamate production from glucose and urea in a batch system. The productivity of l-glutamate by the immobilized protoplasts was 2.5 times higher than that by immobilized whole cells under optimal conditions. Maximal productivity initially reached 1.5 mg·ml^-1. The immobilized protoplasts of B. flavum could be used six times for l-glutamate production with retention of about 70% of the initial productivity.     

Biodegradation of 4-chlorophenol by adsorptive immobilized Alcaligenes sp. A 7-2 in soil

Summary Alcaligenes sp. A 7-2 immobilized on granular clay has been applied in a percolator to degrade 4-chlorophenol in sandy soil. Good adsorption rates on granular clay were achieved using cell suspensions with high titres and media at pH 8.0. The influence of various parameters such as aeration rate, pH, temperature, concentration of 4-chlorophenol and size of inoculum on the degradation rate were investigated. During fedbatch fermentations under optimal culture conditions, concentrations of 4-chlorophenol up to 160 mg·1^–1 could be degraded. Semicontinuous culture experiments demonstrated that the degradation potential in soil could be well established and enhanced by the addition of immobilized bacteria. Continuous fermentation was performed with varying 4-chlorophenol concentrations in the feed and different input levels. The maximum degradation rate was 1.64 g·1^–1·day^–1. Offprint requests to: H.-J. Rehm     

Immobilization of lactase for the continuous hydrolysis of whey permaete

The production of lactose-based sweeteners is considered very promising. Fungal lactase has been immobilized on crosslinked chitin to develop a process for the continuous hydrolysis of demineralized whey permaete. The optimization of lactase immobilization on chitin and chitosan was performed, activities of 4 · 10⁵ and 2.2 · 10⁵ u/kg at yields of 33 and 23% were obtained for both supports, respectively. The chitin based catalyst was selected for further studies and a procedure was developed for in-situ enzyme immobilization. The kinetic behaviour of the catalyst was determined to propose a kinetic model for the initial rate of lactose hydrolysis. Pseudo steady-state and long term operation of packed bed reactors with chitin-immobilized lactase ranging from small laboratory to pre-pilot unit was carried out. The results are discussed and compared with commercial immobilized lactases. Preliminary economic evaluation for the production of ultrafiltered whey protein and hydrolyzed lactose syrup, within a dairy industry in Chile, was satisfactory in terms of profitability, both for the chitin immobilized lactase developed and for a commercial immobilized lactase.List of Symbols a moles/m³ glucose concentration in Eq. (1) - C _i US$ total annual cost (without considering plant depreciation) - D US$ annual depreciation - F m³/h flowrate - h m³/h volumetric mass transfer coefficient - i moles/m³ galactose concentration in Eqs. (1) and (2) - K _A moles/m³ dissociation constant for glucose in Eq. (1) - K _A moles/m³ dissociation constant for glucose in Eq. (1) - K _I moles/m³ inhibition constant for galactose in Eqs. (1) and (2) - K _m moles/m³ Michaelis constant for substrate in Eqs. (1) and (2) - k _D h^–1 first-order thermal deactivation constant - P kg dry weight of catalyst - PV US$ net present value - R % discounted cash-flow rate of return - s moles/m³ substrate concentration - s₀ moles/m³ feed substrate concentration - S _n US$ annual sales income - TC US$ total capital income - t _1/2 h catalyst half-life - v moles/h · kg initial rate of reaction - V _MAX moles/h · kg maximum reaction rate in Eqs. (1) and (2) - V _MAX moles/h · kg maximum reaction rate in Eq. (1) - ¯V _max moles/h initial rate of reaction - V _R m³ reaction volume free of catalyst particles - X substrate degree of conversion = s₀–s/s₀ - Damkoehler number = ¯V _MAX /h k _m - moles/(m³ · h) reactor productivity in Eq. (3)     

The use of polyurethane foam for microbial retention in methanogenic fermentation of propionate

Summary The use of polyurethane foam (PUF) as a microbial support carrier was evaluated with a mesophilic propionate-acclimatized sludge. The acclimatized sludge could be immobilized rapidly and stably in PUF of smaller pore size under shaking conditions. The sludge retained in PUF could maintain a high propionate metabolic activity for a long period. High conversion rates of propionate to methane of 23–65 g chemical oxygen demand (COD)·1^–1 · day^–1 could be achieved in reactors packed with PUF-retained sludge. A dense sludge of 0.08–0.25 g mixed-liquor volatile suspended solids (MLVSS)·cm^–3 was retained in PUF. Microscopic analysis suggested that filamentous microorganisms, e.g., Methanothrix spp. could play an important role in the efficient retention of acclimatized sludge in PUF. Offprint requests to: Shiro Nagai