Continuous production of high-purity fructooligosaccharides and ethanol by immobilized Aspergillus japonicus and Pichia heimii

High-purity fructooligosaccharides (FOS) were produced from sucrose by an innovative process incorporating immobilized Aspergillus japonicus and Pichia heimii cells. Intracellular FTase of A. japonicus converted sucrose into FOS and glucose, and P. heimii fermented glucose mainly into ethanol. The continuous production of FOS was carried out using a tanks-in-series bioreactor consisting of three stirred tanks. When a solution composed of 1 g L^?1 yeast extract and 300 g L^?1 sucrose was fed continuously to the bioreactor at a dilution rate of 0.1 h^?1, FOS at a purity of up to 98.2 % could be achieved and the value-added byproduct ethanol at 79.6 g L^?1 was also obtained. One gram of sucrose yielded 0.62 g FOS and 0.27 g ethanol. This immobilized dual-cell system was effective for continuous production of high-purity FOS and ethanol for as long as 10 days.     

Nitrogen removal through different pathways in an aged refuse bioreactor treating mature landfill leachate

In this study, an aged refuse bioreactor was constructed to remove nitrogen in a mature landfill leachate. The nitrogen removal efficiency and the microbial community composition in the bioreactor were investigated. The results showed that the aged refuse bioreactor removed more than 90 % of total nitrogen in the leachate under the nitrogen loading rate (NLR) of 0.74 g/kg (vs) day, and the total nitrogen removal rate decreased to 62.2 % when NLR increased up to 2.03 g/kg (vs) day. Quantitative polymerase chain reaction results showed that the average cell number of ammonia-oxidizing bacteria in the bioreactor was 1.58?×?10⁸ cells/g, which accounted for 0.41 % of total bacteria. The number of anammox bacteria in the reactor was 1.09?×?10⁸ cells/g, which accounted for 0.27 % of total bacteria. Isotopic ¹⁵N tracing experiments showed that nearly 10 % of nitrogen was removed by anammox. High-throughout 454 pyrosequencing revealed that the predominant bacteria in the bioreactor were Proteobacteria, Chloroflexi, Actinobacteria, Bacteroidetes, and Gemmatimonadetes, including various nitrifiers and denitrifiers with diverse heterotrophic and autotrophic metabolic pathways, supporting that nitrogen was removed through different pathways in this aged refuse bioreactor.     

A two-dimensional mass transfer model for an annular bioreactor using immobilized photosynthetic bacteria for hydrogen production

A two-dimensional model for substrate transfer and biodegradation in a novel, annular fiber-illuminating bioreactor (AFIBR) is proposed in which photosynthetic bacteria are immobilized on the surface of a side-glowing optical fiber to form a stable biofilm. When excited by light, the desired intensity and uniform light distribution can be obtained within the biofilm zone in bioreactor and then realize continuous hydrogen production. Substrate transfer and biodegradation within the biofilm zone, as well as substrate diffusion and convection within bulk fluid regions are considered simultaneously in this model. The validity of the model is verified experimentally. Based on the model analysis, influences of flow rate and light intensity on the substrate consumption rate and substrate degradation efficiency were investigated. The simulation results show that the optimum operational conditions for the substrate degradation within the AFIBR are: flow rate 100 ml h^?1 and light intensity 14.6 μmol photons m^?2 s^?1.     

NaCS‐PDMDAAC immobilized cultivation of recombinant Dictyostelium discoideum for soluble human Fas ligand production

Dictyostelium discoideum is a promising eukaryotic host for the expression of heterologous proteins requiring post‐translational modifications. However, the dilute nature of D. discoideum cell culture limits applications for high value proteins production. D. discoideum cells, entrapped in sodium cellulose sulfate/poly‐dimethyl‐diallyl‐ammonium chloride (NaCS‐PDMDAAC) capsules were used for biosynthesis of the heterologous protein, soluble human Fas ligand (hFasL). Semi‐continuous cultivations with capsules recycling were carried out in shake flasks. Also, a scaled‐up cultivation of immobilized D. discoideum for hFasL production in a customized vitreous airlift bioreactor was conducted. The results show that NaCS‐PDMDAAC capsules have desirable biophysical properties including biocompatibility with the D. discoideum cells and good mechanical stability throughout the duration of cultivation. A maximum cell density of 2.02 × 10⁷ cells mL^?1 (equivalent to a maximum cell density of 2.22 × 10⁸ cells mL^?1 in capsules) and a hFasL concentration of 130.40 μg L^?1 (equivalent to a hFasL concentration of 1434.40 μg L^?1 in capsules) were obtained in shake flask cultivation with capsules recycling. Also, a maximum cell density of 1.72 × 10⁷cells mL^?1 (equivalent to a maximum cell density of 1.89 × 10⁸ cells mL^?1 in capsules) and a hFasL concentration of 106.10 μg L^?1 (equivalent to a hFasL concentration of 1167.10 μg L^?1 in capsules) were obtained after ～170 h cultivation in the airlift bioreactor (with a working volume of 200 mL in a 315 mL bioreactor). As the article presents a premier work in the application of NaCS‐PDMDAAC immobilized D. discoideum cells for the production of hFasL, more work is required to further optimize the system to generate higher cell densities and hFasL titers for large‐scale applications. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:424–430, 2015     

Degradation of cationic surfactants using Pseudomonas putida A ATCC 12633 immobilized in calcium alginate beads

In this study, the degradation of tetradecyltrimethylammonium bromide (TTAB) by freely suspended and alginate-entrapped cells from the bacteria Pseudomonas putida (P. putida) A ATCC 12633 was investigated in batch cultures. The optimal conditions to prepare beads for achieving a higher TTAB degradation rate were investigated by changing the concentration of sodium alginate, pH, temperature, agitation rate and initial concentration of TTAB. The results show that the optimal embedding conditions of calcium alginate beads are 4 % w/v of sodium alginate content and 2 × 10⁸ cfu ml^?1 of P. putida A ATCC 12633 cells that had been previously grown in rich medium. The optimal degradation process was carried out in pH 7.4 buffered medium at 30 °C on a rotary shaker at 100 rpm. After 48 h of incubation, the free cells degraded 26 mg l^?1 of TTAB from an initial concentration of 50 mg l^?1 TTAB. When the initial TTAB concentration was increased to 100 mg l^?1, the free cells lost their degrading activity and were no longer viable. In contrast, when the cells were immobilized on alginate, they degraded 75 % of the TTAB after 24 h of incubation from an initial concentration of 330 mg l^?1 of TTAB. The immobilized cells can be stored at 4 °C for 25 days without loss of viability and can be reused without losing degrading capacity for three cycles.     

Laboratory-scale biofiltration of acrylonitrile by <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> DAP 96622 in a trickling bed bioreactor

Acrylonitrile (ACN), a volatile component of the waste generated during the production of acrylamide, also is often associated with aromatic contaminants such as toluene and styrene. Biofiltration, considered an effective technique for the treatment of volatile hydrocarbons, has not been used to treat volatile nitriles. An experimental laboratory-scale trickling bed bioreactor using cells of Rhodococcus rhodochrous DAP 96622 supported on granular activated carbon (GAC) was developed and evaluated to assess the ability of biofiltration to treat ACN. In addition to following the course of treatability of ACN, kinetics of ACN biodegradation during both recycle batch and open modes of operation by immobilized and free cells were evaluated. For fed-batch mode bioreactor with immobilized cells, almost complete ACN removal (>95%) was achieved at a flow rate of 0.1 μl/min ACN and 0.8 μl/min toluene (TOL) (for comparative purposes this is equivalent to 6.9 mg l^?1 h^?1 ACN and 83.52 mg l^?1 h^?1 TOL). In a single-pass mode bioreactor with immobilized cells, at ACN inlet loads of 100–200 mg l^?1 h^?1 and TOL inlet load of ~400 mg l^?1 h^?1, with empty bed retention time (EBRT) of 8 min, ACN removal efficiency was ~90%. The three-dimensional structure and characteristics of the biofilm were investigated using confocal scanning laser microscopy (CSLM). CLSM images revealed a robust and heterogeneous biofilm, with microcolonies interspersed with voids and channels. Analysis of the precise measurement of biofilm characteristics using COMSTAT^® agreed with the assumption that both biomass and biofilm thickness increased along the carbon column depth.     

Atmospheric methane removal by methane-oxidizing bacteria immobilized on porous building materials

Biological treatment using methane-oxidizing bacteria (MOB) immobilized on six porous carrier materials have been used to mitigate methane emission. Experiments were performed with different MOB inoculated in building materials at high (~20 % (v/v)) and low (~100 ppmv) methane mixing ratios. Methylocystis parvus in autoclaved aerated concrete (AAC) exhibited the highest methane removal rate at high (28.5?±?3.8 μg CH₄ g^?1 building material h^?1) and low (1.7?±?0.4 μg CH₄ g^?1 building material h^?1) methane mixing ratio. Due to the higher volume of pores with diameter >5 μm compared to other materials tested, AAC was able to adsorb more bacteria which might explain for the higher methane removal observed. The total methane and carbon dioxide-carbon in the headspace was decreased for 65.2?±?10.9 % when M. parvus in Ytong was incubated for 100 h. This study showed that immobilized MOB on building materials could be used to remove methane from the air and also act as carbon sink.     

Continuous production of human erythropoietin by immobilized recombinant L-929 cells

Recombinant L-929 cells transfected with the human erythropoietin (EPO) gene were immobilized in a macroporous cellulosic support and its derivatives in which charged groups or cell attachment factors were introduced. The immobilized cells were cultured in serum-containing and serum-free media. Comparable production of EPO was observed even in the serum-free medium when a support modified by polyethyleneimine was used for immobilization. The cells immobilized on the supports were cultured in fluidized-bed and inner-loop type air-lift bioreactors for continuous production of EPO. A high cell density of more than 2 × 10⁷ cells/cm³-support and high EPO productivity were achieved and maintained for 50 d through the use of the inner-loop type air-lift bioreactor. The productivity was 13.4-fold higher than that of conventional static cultures in petri-dishes.     

Microorganisms immobilized by membrane inclusion: kinetic measurements in a fixed bed bioreactor and oxygen consumption calculations

Cells living in the pores of macroporous carriers can be immobilized by coating the carriers with a porous membrane. To evaluate the performance of cells immobilized with such a technique, a fixed bed bioreactor was used to study the oxidation of D-sorbitol to L-sorbose by Acetobacter suboxydans. Comparisons were made of immobilized cells to cells living in the pores of a non-coated carrier and to cells living in the absence of a carrier (“submerged cells”). Productivity was similar in all three cultures (4.6–6.3?g sorbose?l^?1?h^?1). Biomass concentration at the outlet was highest for submerged cells (1.3?·?10⁹?cells?ml^?1) but was equal for coated and non-coated carriers (0.4?·?10⁹?cells?ml^?1). Examination of the coated carriers under the electron microscope revealed that only a thin layer near the surface was actually colonized by bacteria. Interestingly, when normalized on the basis of volume, sorbitol oxidation in the colonized layer appeared to be about 100-fold faster than in the bulk medium. A model was derived for oxygen relations inside the coated carriers. This model implicates that the inner parts of the carrier are not colonized by bacteria due to oxygen limitation. The findings indicate that coated carriers have potential to catalyze biotransformations at very high rates, and identify oxygen supply and confinement of cells to the carriers as issues that need further attention. The mathematical model for oxygen concentration profiles inside the coated carriers will be useful for designing improved carriers.     

Absorption characteristics and kinetics of CO2 capture into N-methyldiethanolamine aqueous solution catalyzed by the immobilized carbonic anhydrase

Abstract

Carbonic anhydrase (CA) is the most effective CO₂ hydratase catalyst, but the poor storage stability and repeatability of CA limit its development. Therefore, CA was immobilized on the epoxy magnetic composite microspheres to enhance the CO₂ absorption into N-methyldiethanolamine (MDEA) aqueous solution in this work. In the presence of immobilized CA, the CO₂ absorption rate of MDEA solution (10?wt%) (0.63?mmol·min^?1) was greatly improved by almost 40%, and their reaction equilibrium time was shortened from 150?min to 90?min compared with that into MDEA solution. The results indicated that the absorption of CO₂ into MDEA solution had been significantly enhanced by using CA. After the 7th reuse recycle, the activity of the immobilized CA was still closed to its initial value at 313.15?K. Moreover, enzyme catalytic kinetics of immobilized CA was investigated using the p-nitrophenyl acetate (p-NPA) as substrate. The values of Michaelis–Menten constant (K_m) and the maximum velocity (V_max) of the immobilized CA were calculated to be 27.61?mmol/L and 20.14?×?10^?3?mmol·min^?1·mL^?1, respectively. Besides, the kinetics of CO₂ reaction into MDEA with or without CA were also compared. The results showed that CO₂ absorption into CA/MDEA aqueous solution obeyed the pseudo first order regime and the second order kinetics rate constant (k₂) was calculated to be 929?m³·kmol^?1·s^?1, which was twice higher than that of MDEA aqueous solution without immobilized CA (k₂=414 m³·kmol^?1·s^?1) at 313.15?K.     

Production of influenza H1N1 vaccine from MDCK cells using a novel disposable packed-bed bioreactor

A process for human influenza H1N1 virus vaccine production from Madin–Darby canine kidney (MDCK) cells using a novel packed-bed bioreactor is described in this report. The mini-bioreactor was used to study the relationship between cell density and glucose consumption rate and to optimize the infection parameters of the influenza H1N1 virus (A/New Caledonia/20/99). The MDCK cell culture and virus infection were then monitored in a disposable perfusion bioreactor (AmProtein Current Perfusion Bioreactor) with proportional–integral–derivative control of pH, dissolved O₂ (DO), agitation, and temperature. During 6 days of culture, the total cell number increased from 2.0?×?10⁹ to 3.2?×?10¹⁰ cells. The maximum virus titers of 768 hemagglutinin units/100 μL and 7.8?×?10⁷ 50 % tissue culture infectious doses/mL were obtained 3 days after infection. These results demonstrate that using a disposable perfusion bioreactor for large-scale cultivation of MDCK cells, which allows for the control of DO, pH, and other conditions, is a convenient and stable platform for industrial-scale production of influenza vaccines.     

Kinetics of enzymatic transesterification and thermal deactivation using immobilized Burkholderia lipase as catalyst

The most effective way of enzymatic synthesis of biodiesel is through lipase-catalyzed transesterification, while its performance and economic feasibility should still be improved. In this study, lipase produced by an isolated Burkholderia sp. was immobilized on microsize Celite materials functionally modified with long alkyl groups. The specific activity of the immobilized lipase was 1,154 U/g. The methanolysis of olive oil catalyzed by the immobilized lipase obeyed Ping Pong Bi Bi model with an estimated V _max, K _m,TG, K _m,M and K _i,M value of 0.61 mol/(L min), 7.93 mol/L, 1.01 mol/L, and 0.24 mol/L, respectively. The activation energy of the enzymatic reaction is estimated as 15.51 kJ/mol. The immobilized lipase exhibits high thermal stability with thermal deactivation energy of 83 kJ/mol and a long half-life. The enthalpy, Gibb’s free energy, and entropy of the immobilized lipase were in the range of 80.02–80.35 kJ/mol, 88.35–90.13 kJ/mol, and ?28.22 to ?25.11 J/(mol K), respectively.     

Selective fengycin production in a modified rotating discs bioreactor

Production of lipopeptides fengycin and surfactin in rotating discs bioreactor was studied. The effects of rotation velocity and the addition of agitators between the discs on volumetric oxygen transfer coefficient k _L a were firstly studied in model media. Then the production of lipopeptides was also studied at different agitation conditions in the modified bioreactor (with agitators). The effect of agitation on dissolved oxygen, on submerged and immobilized biomass, on lipopeptide concentrations and yields and on the selectivity of the bioreaction was elucidated and discussed. The proposed modified rotating discs bioreactor allowed to obtain high fengycin concentrations (up to 787 mg L^?1), but also better selectivity of the bioreaction towards fengycin (up to 88 %) and better yields of fengycin per glucose (up to 62.9 mg g^?1), lipopeptides per glucose (up to 71.5 mg g^?1), fengycin per biomass (up to 309 mg g^?1) and lipopeptides per biomass (up to 396 mg g^?1) than those reported in the literature. Highest fengycin production and selectivity were obtained at agitation velocity of 30 min^?1. The proposed non-foaming fermentation process could contribute to the scale-up of lipopeptide fermentors and promote the industrial production of fengycin. The proposed bioreactor and bioprocess could be very useful also for the production of other molecules using bioprocesses requiring bubbleless oxygen supply.     

Low‐temperature (9°C) AMD treatment in a sulfidogenic bioreactor dominated by a mesophilic Desulfomicrobium species

The possibilities for the treatment of low‐temperature mine waste waters have not been widely studied. The amenability of low‐temperature sulfate reduction for mine waste water treatment at 9°C was studied in a bench‐scale fluidized‐bed bioreactor (FBR). Formate was used as the electron and carbon source. The first influent for the FBR was acidic, synthetic waste water containing iron, nutrients, and sulfate, followed by diluted barren bioleaching solution (DBBS). The average sulfate reduction rates were 8 mmol L^?1 day^?1 and 6 mmol L^?1 day^?1 with synthetic waste water and DBBS, respectively. The corresponding specific activities were 2.4 and 1.6 mmol SO g VSS^?1 day^?1, respectively. The composition of the microbial community and the active species of the FBR was analyzed by extracting the DNA and RNA, followed by PCR‐DGGE with the universal bacterial 16S rRNA gene primers and dsrB‐primers specific for sulfate‐reducing bacteria. The FBR microbial community was simple and stable and the dominant and active species belonged to the genus Desulfomicrobium. In summary, long‐term operation of a low‐temperature bioreactor resulted in enrichment of formate‐utilizing, psychrotolerant mesophilic sulfate reducing bacteria. Biotechnol. Bioeng. 2009; 104: 740–751 © 2009 Wiley Periodicals, Inc.     

The effects of external electric field: creating non-zero first hyperpolarizability for centrosymmetric benzene and strongly enhancing first hyperpolarizability for non-centrosymmetric edge-modified graphene ribbon H2N-(3,3)ZGNR-NO2

How to generate a non-zero first hyperpolarizability for a centrosymmetric molecule is a challenging question. In this paper, an external (pump) electric field is used to make a centrosymmetric benzene molecule generate a non-zero value of the electric field induced first hyperpolarizability (β ^F ). This comes from the centrosymmetry breaking of electron cloud. Two interesting rules are exhibited. (1) β ^F is anisotropic for different directional fields (F _i, i?=?X, Y, Z). (2) The field dependence of β ^F is a non-monotonic function, and an optimum external electric field causes the maximum value of β ^F . The largest first hyperpolarizability β ^F reaches the considerable level of 3.9?×?10⁵ a.u. under F _Y?=?330?×?10^?4 a.u. for benzene. The external electric field effects on non-centrosymmetric edge-modified graphene ribbon H₂N-(3,3)ZGNR-NO₂ was also studied in this work. The first hyperpolarizability reaches as much as 2.1?×?10⁷ a.u. under F _X?=?600?×?10^?4 a.u. for H₂N-(3,3)ZGNR-NO₂. We show that the external electric field can not only create a non-zero first hyperpolarizability for centrosymmetric molecule, but also remarkably enhance the first hyperpolarizability for a non-centrosymmetric molecule.     

Production of cyclodextrin glycosyltransferase by immobilized <Emphasis Type="Italic">Bacillus</Emphasis> sp. on chitosan matrix

The whole-cell immobilization on chitosan matrix was evaluated. Bacillus sp., as producer of CGTase, was grown in solid-state and batch cultivation using three types of starches (cassava, potato and cornstarch). Biomass growth and substrate consumption were assessed by flow cytometry and modified phenol–sulfuric acid assays, respectively. Qualitative analysis of CGTase production was determined by colorless area formation on solid culture containing phenolphthalein. Scanning electron microscopy (SEM) analysis demonstrated that bacterial cells were immobilized on chitosan matrix efficiently. Free cells reached very high numbers during batch culture while immobilized cells maintained initial inoculum concentration. The maximum enzyme activity achieved by free cells was 58.15 U ml^?1 (36 h), 47.50 U ml^?1 (36 h) and 68.36 U ml^?1 (36 h) on cassava, potato and cornstarch, respectively. CGTase activities for immobilized cells were 82.15 U ml^?1 (18 h) on cassava, 79.17 U ml^?1 (12 h) on potato and 55.37 U ml^?1 (in 6 h and max 77.75 U ml^?1 in 36 h) on cornstarch. Application of immobilization technique increased CGTase activity significantly. The immobilized cells produced CGTase with higher activity in a shorter fermentation time comparing to free cells.     

Engineering analysis of continuous production of L-aspartic acid by immobilized Escherichia coli cells in fixed beds

The reaction mechanism and decay behavior of aspartase activity for immobilized Escherichia coli cells were investigated by using a sectional packed column. Reaction within the immobilized cell column proceeded at zero-order on substrate solutions ranging in concentration from 0.1 to 1.0M, and the initial reaction rate was found to be 1.556 × 10^?2 mol/min/liter of immobilized cells. The effect of temperature on the reaction rate constant was investigated. The Arrhenius plot was straight line at temperatures below 43°C, and the activation energy for immobilized cells was calculated to be 12.36 kcal/mol. Asparatase activity in the immobilized cell column decayed exponentially and uniformly in all sections of a column. Its half-life was approximately 120 days. The rate of formation of L-aspartic acid was shown to be independent of column dimensions.     

The designer leptin antagonist peptide Allo-aca compensates for short serum half-life with very tight binding to the receptor

The leptin receptor antagonist peptide Allo-aca exhibits picomolar activities in various cellular systems and sub-mg/kg subcutaneous efficacies in animal models making it a prime drug candidate and target validation tool. Here we identified the biochemical basis for its remarkable in vivo activity. Allo-aca decomposed within 30 min in pooled human serum and was undetectable beyond the same time period from mouse plasma during pharmacokinetic measurements. The C _max of 8.9 μg/mL at 5 min corresponds to approximately 22 % injected peptide present in the circulation. The half-life was extended to over 2 h in bovine vitreous fluid and 10 h in human tears suggesting potential efficacy in ophthalmic diseases. The peptide retained picomolar anti-proliferation activity against a chronic myeloid leukemia cell line; addition of a C-terminal biotin label increased the IC₅₀ value by approximately 200-fold. In surface plasmon resonance assays with the biotin-labeled peptide immobilized to a NeutrAvidin-coated chip, Allo-aca exhibited exceptionally tight binding to the binding domain of the human leptin receptor with k _a = 5 × 10⁵ M^?1 s^?1 and k _diss = 1.5 × 10^?4 s^?1 values. Peptides excel in terms of high activity and selectivity to their targets, and may activate or inactivate receptor functions considerably longer than molecular turnovers that take place in experimental animals.     

Performance of an external loop air-lift bioreactor for the production of monoclonal antibodies by immobilized hybridoma cells

Summary The performance of an external loop air-lift bioreactor was investigated by assessing the inter-relationships between various hydrodynamic properties and mass transfer. The feasibility of using this bioreactor for the production of monoclonal antibodies by mouse hybridoma cells immobilized in calcium alginate gel beads and alginate/poly-l-lysine microcapsules was also examined. When the superficial gas velocity, V _g , in the 300 ml reactor was varied from 2 to 36 cm/min, the average liquid velocity increased from 3 to 14 cm/sec, the gas hold-up rose from 0.2 to 3.0%, and the oxygen mass transfer coefficient, k _L a, increased from 2.5 to 18.1 h^-1. A minimum liquid velocity of 4 cm/s was required to maintain alginate gel beads (1000 m diameter, occupying 3% of reactor volume) in suspension. Batch culture of hybridoma cells immobilized in alginate beads followed logarithmic growth, reaching a concentration of 4×10⁷ cells/ml beads after 11 days. Significant antibody production did not occur until day 9 into the culture, reaching a value of 100 g/ml of medium at day 11. On the other hand, bioreactor studies with encapsulated hybridoma cells gave monoclonal antibody concentrations of up to 800 g/ml capsules (the antibody being retained within the semipermeable capsule) and maximum cell densities of 2×10⁸ cells/ml capsule at day 11. The volumetric productivities of the alginate gel immobilized cell system and the encapsulated cell system were 9 and 3 g antibody per ml of reactor volume per day, respectively. The main advantage of the bioreactor system is its simple design, since no mechanical input is required to vary the hydrodynamic properties.     

Immobilization of <Emphasis Type="BoldItalic">Irpex lacteus</Emphasis> to liquid-core alginate beads and their application to degradation of pollutants

White rot fungi (WRF) are applicable to biodegradation of recalcitrant pollutants. However, excessive biomass growth typical for WRF cultivation can hinder their large scale applications. Therefore, immobilization of Irpex lacteus to liquid-core alginate beads restricting excessive mycelium growth and simultaneously keeping high degradation rate of pollutants was tested. Effective diffusivities of dyes to the beads varied from (2.98 ± 0.69) × 10^?10 to (10.27 ± 2.60) × 10^?10 m²/s. Remazol Brilliant Blue R (RBBR), Reactive Orange 16 (RO16), and Naphthol Blue Black (NBB) were used as model dyes. The immobilized fungus decolorized model dyes when applied both in microwell plates and in fluidized bed reactors. Using the microwell plates, the apparent reaction rate constants ranged from (2.06 ± 0.11) × 10^?2 to (11.06 ± 0.27) × 10^?2 1/h, depending on the dye used and its initial concentration. High initial concentrations negatively affected the dye decolorization rate. No fungal growth outside the beads was observed in fluidized bed reactors and thus no operational problems linked to an excessive biomass growth occurred. When RBBR was decolorized in subsequent batches in the fluidized bed reactor, the apparent reaction rate constant increased from (11.63 ± 0.35) × 10^?2 to (29.26 ± 7.19) × 10^?2 1/h.