Synthesis of D-Alanine Oligopeptides Catalyzed by D-Aminopeptidase in Non-Aqueous Media

Synthesis of D-alanine oligopeptides from D-alanine methylester hydrochloride has been demonstrated by use of immobilized D-aminopeptidase from Ochrobactrum anthropi (Achromobacter sp.) in non-aqueous media. D-Alanine dimer and trimer were obtained in 56% and 6% yield, respectively, when 250 mM of the substrate was incubated for 3 hours with urethane-prepolymer immobilized D-aminopeptidase (1.5 U/ml) and 3 equivalents of triethylamine in water-saturated toluene. The k_cat of this reaction was calculated to be 19,500 (min^-1), which is several ten thousand times greater than that of the known enzymatic syntheses of amino acid oligomers.     

Kinetic and thermodynamic properties of purified alkaline protease from Bacillus pumilus Y7 and non‐covalent immobilization to poly(vinylimidazole)/clay hydrogel

The characterization of the hydrogel was performed using Fourier‐transform infrared spectroscopy, X‐ray diffraction, and scanning electron microscopy. Purified Bacillus pumilus Y7‐derived alkaline protease was immobilized in Poly (vinylimidazole)/clay (PVI/SEP) hydrogel with 95% yield of immobilization. Immobilization decreased the pH optimum from 9 to 6 for free and immobilized enzyme, respectively. Temperature optimum 3°C decreased for immobilized enzyme. The K_m, V_m, and k_cat of immobilized enzyme were 4.4, 1.7, and 7.5‐fold increased over its free counterpart. Immobilized protease retained about 65% residual activity for 16^th reuse. The immobilized protease endured its 35% residual activity in the material after six cycle's batch applications. The results of thermodynamic analysis for casein hydrolysis showed that the ΔG^≠ (activation free energy) and ΔG^≠_E‐T (activation free energy of transition state formation) obtained for the immobilized enzyme decreased in comparison to those obtained for the free enzyme. On the other hand, the value of ΔG^≠_ES (free energy of substrate binding) was observed to have increased. These results indicate an increase in the spontaneity of the biochemical reaction post immobilization. Enthalpy value of immobilized enzyme that was 2.2‐fold increased over the free enzyme indicated lower energy for the formation of the transition state, and increased ΔS^≠ value implied that the immobilized form of the enzyme was more ordered than its free form.     

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.     

Biosorption of Malathion by immobilized cells of Bacillus sp. S14

Abstract

Biosorption is potentially an attractive technology for the treatment of wastewater by removing pesticide molecules from dilute solutions. This study investigated the feasibility of an isolated Bacillus sp. S₁₄ immobilized in calcium alginate that was used as a biosorbent for Malathion removal from aqueous solutions in batch mode. The highest value of Malathion uptake by isolated Bacillus sp. S14 (1.33g L^?1, dry basis) immobilized in 3% calcium alginate was 64.4% at 25°C and pH7.0 when the initial Malathion concentration was 50 mg L^?1. Equilibrium was attained at 8h. The sorption data conformed well to the Fruendlich isotherm model.     

Comparison of Immobilized and Free Amyloglucosidase Process in Glucose SyrupsProduction from White Sorghum Starch

Optimum conditions for glucose syrups production from white sorghum were studied through sequential liquefaction and saccharification processes. In the liquefaction process, a maximum dextrose equivalent (DE) of 10.98 % was achieved using 30 % (w/v) of starch and Termamyl ɑ-amylase from Bacillus licheniformis. Saccharification was performed by free and immobilized amyloglucosidase from Rhizopus mold at 1 % (w/v). DE values of 88.32 % and 79.95 % were obtained from 30 % (w/v) of starch with, respectively, free and immobilized enzyme. The immobilized Amyloglucosidase in calcium alginate beads showed reusable capacity for up to 6 cycles with 46 % of the original activity retained. The kinetic behaviour of immobilized and free enzyme gives K_m value of 22.13 and 16.55 mg mL⁻¹ and V_max of 0.69 and 1.61 mg mL⁻¹ min⁻¹, respectively. The hydrolysis yield using immobilized amyloglucosidase were lower than that of the free one. However, it is relevant to reuse enzyme without losing activity in order to trim down the overall costs of enzymatic bioprocesses as starch transformation into required products in industrial manufacturing. Hydrolysis of sorghum starch using immobilized amyloglucosidase represents a promising alternative towards the development of the glucose syrups production process and its utilization in various industries.     

Immobilization of soybean seed coat peroxidase on polyaniline: Synthesis optimization and catalytic properties

Soybean seed coat peroxidase (SBP) was immobilized on various polyaniline-based polymers (PANI), activated with glutaraldehyde. The most reduced polymer (PANIG₂) showed the highest immobilization capacity (8.2 mg SBP?g^?1 PANIG₂). The optimum pH for immobilization was 6.0 and the maximum retention was achieved after a 6-h reaction period. The efficiency of enzyme activity retention was 82%. When stored at 4°C, the immobilized enzyme retained 80% of its activity for 15 weeks as evidenced by tests performed at 2-week intervals. The immobilized SBP showed the same pH-activity profile as that of the free SBP for pyrogallol oxidation but the optimum temperature (55°C) was 10°C below that of the free enzyme. Kinetic analysis show that the K_m was conserved while the specific V_max dropped from 14.6 to 11.4 µmol min^?1 µg^?1, in agreement with the immobilization efficiency. Substrate specificity was practically the same for both enzymes. Immobilized SBP showed a greatly improved tolerance to different organic solvents; while free SBP lost around 90% of its activity at a 50% organic solvent concentration, immobilized SBP underwent only 30% inactivation at a concentration of 70% acetonitrile. Taking into account that immobilized HRP loses more than 40% of its activity at a 20% organic solvent concentration, immobilized SBP performed much better than its widely used counterpart HRP.     

Immobilization of Serratia marcescens lipase onto amino-functionalized magnetic nanoparticles for repeated use in enzymatic synthesis of Diltiazem intermediate

Magnetic Fe₃O₄ nanoparticles were prepared by chemical coprecipitation method and subsequently coated with 3-aminopropyltriethoxysilane (APTES) via silanization reaction. The synthesized materials were characterized by transmission electron microscopy (TEM) and Fourier transform infrared spectroscopy (FTIR). With glutaraldehyde as the coupling agent, the lipase from Serratia marcescens ECU1010 (SmL) was successfully immobilized onto the amino-functionalized magnetic nanoparticles. The results showed that the immobilized protein load could reach as high as 35.2 mg protein g⁻¹ support and the activity recovery was up to 62.0%. The immobilized lipase demonstrated a high enantioselectivity toward (+)-MPGM (with an E-value of 122) and it also displayed the improved thermal stability as compared to the free lipase. When the immobilized lipase was employed to enantioselectively hydrolyze (±)-trans-3-(4-methoxyphenyl)glycidic acid methyl ester [(±)-MPGM] in water/toluene biphasic reaction system for 11 consecutive cycles (totally 105 h), still 59.6% of its initial activity was retained, indicating a high stability in practical operation.     

Application of a quinohaemoprotein alcohol dehydrogenase in bio-electrocatalysis: Immobilization of the enzyme and mediated electron transfer between the enzyme and an electrode

Summary Quinohaemoprotein alcohol dehydrogenase from Comamonas testosteroni was immobilized on polypyrrole-coated track-etch and microporous membranes. On the track-etch membrane, 3.4 to 4.8 × 10^–3 Units of enzyme/cm² was immobilized whilst on the microporous membrane 0.05 U/cm² was immobilized. The track-etch membrane was then used in electrochemical studies using ferricyanide as a redox mediator giving a maximum catalytic current of 0.022 mA/cm² membrane with 1-pentanol as the substrate. The kinetic parameters (K_m and V_max) of the immobilized enzyme are of the same order of magnitude as those of the free enzyme.     

Purification, immobilization and characterization of linoleic acid isomerase on modified palygorskite

Linoleic acid isomerase from Lactobacillus delbrueckii subsp. bulgaricus 1.1480 was purified by DEAE ion-exchange chromatography and gel filtration chromatography. An overall 5.1% yield and purification of 93-fold were obtained. The molecular weight of the purified protein was ~41 kDa which was analyzed by SDS-PAGE. The purified enzyme was immobilized on palygorskite modified with 3-aminopropyltriethoxysilane. The immobilized enzyme showed an activity of 82 U/g. The optimal temperature and pH for the activity of the free enzyme were 30 °C and pH 6.5, respectively; whereas those for the immobilized enzyme were 35 °C and pH 7.0, respectively. The immobilized enzyme was more stable than the free enzyme at 30–60 °C, and the operational stability result showed that more than 85% of its initial activity was retained after incubation for 3 h. The K _m and V _max values of the immobilized enzyme were found to be 0.0619 mmol l⁻¹ and 0.147 mmol h⁻¹ mg⁻¹, respectively. The immobilized enzyme had high operational stability and retained high enzymatic activity after seven cycles of reuse at 37 °C.     

Production of high fructose syrup from <Emphasis Type="Italic">Asparagus</Emphasis> inulin using immobilized exoinulinase from <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> YS-1

Extracellular exoinulinase from Kluyveromyces marxianus YS-1, which hydrolyzes inulin into fructose, was immobilized on Duolite A568 after partial purification by ethanol precipitation and gel exclusion chromatography on Sephadex G-100. Optimum temperature of immobilized enzyme was 55 °C, which was 5 °C higher than the free enzyme and optimal pH was 5.5. Immobilized biocatalyst retained more than 90% of its original activity after incubation at 60 °C for 3 h, whereas in free form its activity was reduced to 10% under same conditions, showing a significant improvement in the thermal stability of the biocatalyst after immobilization. Apparent K _m values for inulin, raffinose and sucrose were found to be 3.75, 28.5 and 30.7 mM, respectively. Activation energy (E _a) of the immobilized biocatalyst was found to be 46.8 kJ/mol. Metal ions like Co²⁺ and Mn²⁺ enhanced the activity, whereas Hg²⁺ and Ag²⁺ were found to be potent inhibitors even at lower concentrations of 1 mM. Immobilized biocatalyst was effectively used in batch preparation of high fructose syrup from Asparagus racemosus raw inulin and pure inulin, which yielded 39.2 and 40.2 g/L of fructose in 4 h; it was 85.5 and 92.6% of total reducing sugars produced, respectively.     

Production of precursors for anti-Alzheimer drugs: Asymmetric bioreduction in a packed-bed bioreactor using immobilized D. carota cells

(S)-1-Phenylethanol derivatives, which are the precursors of many pharmacological products, have also been used as anti-Alzheimer drugs. Bioreduction experiments were performed in a batch and packed-bed bioreactor. Then, the kinetics constants were determined by examining the reaction kinetics in the batch system with free and immobilized carrot cells. Also, the effective diffusion coefficient (D_e) of acetophenone in calcium alginate-immobilized carrot cells was investigated. Kinetics constants for free cells, which are intrinsic values, are reaction rate V_max?=?0.052?mmol?L^?1?min^?1, and constants of the Michaelis–Menten K_M?=?2.31?mmol?L^?1. Kinetics constants for immobilized cells, which are considered apparent values, are V_{max, app}?=?0.0407?mmol?L^?1 min^?1, K_{M, app}?=?3.0472?mmol?L^?1 for 2?mm bead diameter, and V_{max, app}?=?0.0453?mmol?L^?1 min^?1, K_{M, app}?=?4.9383?mmol?L^?1 for 3?mm bead diameter. Average value of effective diffusion coefficient of acetophenone in immobilized beads was determined as 1.97?×?10^?6?cm²?s^?1. Using immobilized carrot cells in an up-flow packed-bed reactor, continuous production of (S)-1-phenylethanol through asymmetric bioreduction of acetophenone was performed. The effects of the residence time and concentrations of substrate were investigated at pH 7.6 and 33°C. Enantiomerically pure (S)-1-phenylethanol (ee?>?99%) was produced with 75% conversion at 4-hr residence time.     

Catalytic properties of the immobilized Talaromyces thermophilus β-xylosidase and its use for xylose and xylooligosaccharides production

The present study explores the efficiency of Talaromyces thermophilus β-xylosidase, in the production of xylose and xylooligosaccharides. The β-xylosidase was immobilized by different methods namely ionic binding, entrapment and covalent coupling and using various carriers. Chitosan, pre-treated with glutaraldehyde, was selected as the best support material for β-xylosidase immobilization; it gave the highest immobilization and activity yields (94%, 87%, respectively) of initial activity, and also provided the highest stability, retaining 94% of its initial activity even after being recycled 25 times. Shifts in the optimal temperature and pH were observed for the immobilized β-xylosidase when compared to the free enzyme. The maximal activity obtained for the immobilized enzyme was achieved at pH 8.0 and 53 °C, whereas that for the free enzyme was obtained at pH 7.0 and 50 °C. The immobilized enzyme was more thermostable than the free β-xylosidase. We observed an increase of the K_m values of the free enzyme from 2.37 to 3.42 mM at the immobilized state. Native and immobilized β-xylosidase were found to be stimulated by Ca²⁺, Mn²⁺ and Co²⁺ and to be inhibited by Zn²⁺, Cu²⁺, Hg²⁺, Fe²⁺, EDTA and SDS. Immobilized enzyme was found to catalyze the reverse hydrolysis reaction, forming xylooligosaccharides in the presence of a high concentration of xylose. In order to examine the synergistic action of xylanase and β-xylosidase of T. thermophilus, these two enzymes were co-immobilized on chitosan. A continuous hydrolysis of 3% Oat spelt xylan at 50 °C was performed and better hydrolysis yields and higher amount of xylose was obtained.     

IMMOBILIZATION OF CARBONIC ANHYDRASE ENZYME PURIFIED FROM Bacillus subtilis VSG-4 AND ITS APPLICATION AS CO2 SEQUESTERER

The purification, immobilization, and characterization of carbonic anhydrase (CA) secreted by Bacillus subtilis VSG-4 isolated from tropical soil have been investigated in this work. Carbonic anhydrase was purified using ammonium sulfate precipitation, Sephadex-G-75 column chromatography, and DEAE-cellulose chromatography, achieving a 24.6-fold purification. The apparent molecular mass of purified CA obtained by SDS-PAGE was found to be 37 kD. The purified CA was entrapped within a chitosan–alginate polyelectrolyte complex (C-A PEC) hydrogel for potential use as an immobilized enzyme. The optimum pH and temperature for both free and immobilized enzymes were 8.2 and 37°C, respectively. The immobilized enzyme had a much higher storage stability than the free enzyme. Certain metal ions, namely, Co²⁺, Cu²⁺, and Fe³⁺, increased the enzyme activity, whereas CA activity was inhibited by Pb²⁺, Hg²⁺, ethylenediamine tetraacetic acid (EDTA), 5,5′-dithiobis-(2-nitrobenzoic acid (DTNB), and acetazolamide. Free and immobilized CAs were tested further for the targeted application of the carbonation reaction to convert CO₂ to CaCO₃. The maximum CO₂ sequestration potential was achieved with immobilized CA (480 mg CaCO₃/mg protein). These properties suggest that immobilized VSG-4 carbonic anhydrase has the potential to be used for biomimetic CO₂ sequestration.     

Catalytic properties of the immobilized Aspergillus tamarii xylanase

Xylanase from Aspergillus tamarii was covalently immobilized on Duolite A147 pretreated with the bifunctional agent glutaraldehyde. The bound enzyme retained 54.2% of the original specific activity exhibited by the free enzyme (120 U/mg protein). Compared to the free enzyme, the immobilized enzyme exhibited lower optimum pH, higher optimum reaction temperature, lower energy of activation, higher K_m (Michaelis constant), lower V_max (maximal reaction rate). The half-life for the free enzyme was 186.0, 93.0, and 50.0 min for 40, 50, and 60°C, respectively, whereas the immobilized form at the same temperatures had half-life of 320, 136, and 65 min. The deactivation rate constant at 60°C for the immobilized enzyme is about 6.0 × 10⁻³, which is lower than that of the free enzyme (7.77 × 10⁻³ min). The energy of thermal deactivation was 15.22 and 20.72 kcal/mol, respectively for the free and immobilized enzyme, confirming stabilization by immobilization. An external mass transfer resistance was identified with the immobilization carrier (Duolite A147). The effect of some metal ions on the activity of the free and immobilized xylanase has been investigated. The immobilized enzyme retained about 73.0% of the initial catalytic activity even after being used 8 cycles.     

Microbial community analysis of simultaneous ammonium removal and Fe3+ reduction at different influent ammonium concentrations

This study investigates the impacts of influent ammonium concentrations on the microbial community in immobilized heterotrophic ammonium removal system. Klebsiella sp. FC61, the immobilized species, has the ability to perform simultaneous ammonium removal and Fe³⁺ reduction. It was found that average ammonium removal rate decreased from 0.308 to 0.157 mg/L/h, as the influent NH₄ ⁺-N was reduced from 20 to 10 mg/L. Meanwhile, at a total Fe³⁺ concentration of 20 mg/L, the average Fe³⁺ reduction removal efficiency and rate decreased from 44.61% and 0.18 mg/L/h, to 27.10% and 0.11 mg/L/h, respectively. High-throughput sequencing was used to observe microbial communities in bioreactor Samples B1, B2, and B3, after exposure to different influent NH₄ ⁺-N conditions. Results show that higher influent NH₄ ⁺-N concentrations increased microbial richness and diversity and that Klebsiella sp. FC61 play a functional role in the simultaneous removal of NH₄ ⁺-N and Fe³⁺ reduction in bioreactor systems.

     

Production of gluconic acid by immobilized in pumice stones mycelium of Aspergillus niger using unconventional oxygenation of culture

Gluconic acid was produced in repeated batch processes with Aspergillus niger AM-11, immobilized in pumice stone particles using an unconventional oxygenation of culture media based on the addition of H₂O₂, decomposed by catalase to O₂ and water. The highest gluconic acid productivity of 8.2 g l^–1 h^–1 was reached with 30 g immobilized mycelium per 150 ml, 10% (w/v) glucose, at 24 °C and pH 6.5, with O₂ at 100% saturation. The immobilized mycelium was successfully reused up to 8 times in 1-h batches with only a slight loss (11%) of gluconic acid productivity.     

Response surface design for the optimization of enzymatic detection of mercury in aqueous solution using immobilized urease from vegetable waste

Soluble and alginate immobilized urease was utilized for detection and quantitation of mercury in aqueous samples. Urease from the seeds of pumpkin, being a vegetable waste, was extracted and purified to apparent homogeneity (sp. activity 353 U/mg protein; A₂₈₀/A₂₆₀ = 1.12) by heat treatment at 48 ± 0.1 °C and gel filtration through Sephadex G-200. Homogeneous enzyme preparation was immobilized in 3.5% alginate leading to 86% immobilization, no leaching of enzyme was found over a period of 15 days at 4 °C. Urease catalyzed urea hydrolysis by soluble and immobilized enzyme revealed a clear dependence on the concentration of Hg²⁺. Inhibition caused by Hg²⁺ was non-competitive (K_i = 1.2 × 10⁻¹ μM for soluble and 1.46 × 10⁻¹ μM for alginate immobilized urease.). Time-dependent inhibition both in presence and in absence of Hg²⁺ ion revealed a biphasic inhibition in activity. For optimization of this process response surface methodology (RSM) was utilized where two-level-two-full factorial (2²) central composite design (CCD) has been employed. The regression equation and analysis of variance (ANOVA) were obtained using MINITAB^® 15 software. Predicted values thus obtained were closed to experimental value indicating suitability of the model. 3D response surface plot, iso-response contour plot and process optimization curve were helpful to predict the results by performing only limited set of experiments.     

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.     

Immobilization of glycerol dehydrogenase on magnetic silica nanoparticles for conversion of glycerol to value-added 1,3-dihydroxyacetone

Abstract

Glycerol dehydrogenase (GlyDH) which oxidizes glycerol to the value-added chemical, 1,3-dihydroxyacetone, is of interest due to the oversupply of glycerol as a by-product of the biodiesel industry. To exploit the enzymatic oxidation of glycerol industrially, silica coated magnetic Fe₃O₄ nanoparticles were prepared and then activated with an amino-silane reagent for covalent immobilization of GlyDH via a glutaraldehyde linkage. At the optimal glutaraldehyde concentration of 0.05% (v/v), an enzyme loading of up to 57.5 mg/g-nanoparticles was achieved with 81.1% of the original activity retained. Reaction kinetic analysis indicated that the immobilized GlyDH had almost the same Michaelis-Menten constants for both NAD⁺ and glycerol as the free GlyDH did. However, after immobilization the turnover number k_cat of the GlyDH decreased from 164 s^?1 to 113 s^?1, and the reaction was 1.3-fold less sensitive to inhibition by DHA, which could compensate the decrease in k_cat. The immobilized GlyDH was also less sensitive to changes in pH and temperature, and showed a 5.3-fold improvement in thermal stability at 50^°C. Furthermore, excellent reusability was observed such that 10 cycles of re-use only led to 9% loss of enzyme activity.     

ROLE OF GLUTAMATE DEHYDROGENASE AND GLUTAMINE SYNTHETASE IN CHLORELLA VULGARIS DURING ASSIMILATION OF AMMONIUM WHEN JOINTLY IMMOBILIZED WITH THE MICROALGAE‐GROWTH‐PROMOTING BACTERIUM AZOSPIRILLUM BRASILENSE1

Enzymatic activities of glutamate dehydrogenase (GDH) and glutamine synthetase (GS) participating in the nitrogen metabolism and related ammonium absorption were assayed after the microalga Chlorella vulgaris Beij. was jointly immobilized with the microalgae‐growth‐promoting bacterium Azospirillum brasilense. At initial concentrations of 3, 6, and 10 mg · L^?1 NH₄⁺, joint immobilization enhances growth of C. vulgaris but does not affect ammonium absorption capacity of the microalga. However, at 8 mg · L^?1 NH₄⁺, joint immobilization enhanced ammonium absorption by the microalga without affecting the growth of the microalgal population. Correlations between absorption of ammonium per cell and per culture showed direct (negative and positive) linear correlations between these parameters and microalga populations at 3, 6, and 10 mg · L^?1 NH₄⁺, but not at 8 mg · L^?1 NH₄⁺, where the highest absorption of ammonium occurred. In all cultures, immobilized and jointly immobilized, having the four initial ammonium concentrations, enzymatic activities of Chlorella are affected by A. brasilense. Regardless of the initial concentration of ammonium, GS activity in C. vulgaris was always higher when jointly immobilized and determined on a per‐cell basis. When jointly immobilized, only at an initial concentration of 8 mg · L^?1 NH₄⁺ was GDH activity per cell higher.