Production of thermostable and neutral glucoamylase using immobilized <Emphasis Type="Italic">Thermomucor indicae-seudaticae</Emphasis>

Thermomucor indicae-seudaticae was immobilized in alginate, κ-carrageenan, agarose, agar, polyacrylamide and loofah (Luffa cylindrica) sponge (as such or coated with alginate/starch/Emerson YpSs agar), and used for the production of glucoamylase in submerged fermentation. The mycelium developed from alginate-immobilized sporangiospores secreted higher glucoamylase titres (22.7 U ml⁻¹) than those immobilized in other gel matrices and the freely growing mycelial pellets (18.5 U ml⁻¹). Loofah network provided a good support for mycelial growth, but the enzyme production was lower than that attained with alginate beads. Glucoamylase production increased with inoculum density and the optimum levels were achieved when 40 calcium alginate beads (∼5 × 10⁶ immobilized spores) were used to inoculate 50 ml production medium. The alginate bead inoculum displayed high storage stability at 4°C and produced comparable enzyme titres up to 120 days. The glucoamylase production by hyphae emerged from the immobilized sporangiospores was almost stable over eight batches of repeated fermentation. Scanning electron micrographs of alginate beads, after batch fermentation, revealed extensive mycelial growth inside and around the beads.     

Optimization of lactic acid production by immobilized <Emphasis Type="Italic">Lactococcus lactis</Emphasis> IO-1

Production of lactic acid from glucose by immobilized cells of Lactococcus lactis IO-1 was investigated using cells that had been immobilized by either entrapment in beads of alginate or encapsulation in microcapsules of alginate membrane. The fermentation process was optimized in shake flasks using the Taguchi method and then further assessed in a production bioreactor. The bioreactor consisted of a packed bed of immobilized cells and its operation involved recycling of the broth through the bed. Both batch and continuous modes of operation of the reactor were investigated. Microencapsulation proved to be the better method of immobilization. For microencapsulated cells at immobilized cell concentration of 5.3 g l⁻¹, the optimal production medium had the following initial concentrations of nutrients (g l⁻¹): glucose 45, yeast extract 10, beef extract 10, peptone 7.5 and calcium chloride 10 at an initial pH of 6.85. Under these conditions, at 37 °C, the volumetric productivity of lactic acid in shake flasks was 1.8 g l⁻¹ h⁻¹. Use of a packed bed of encapsulated cells with recycle of the broth through the bed, increased the volumetric productivity to 4.5 g l⁻¹ h⁻¹. The packed bed could be used in repeated batch runs to produce lactic acid.     

An enzymatic method for removal of phenol from industrial effluent

Phenols in an aqueous solution were removed after treatment with peroxidase in the presence of hydrogen peroxide. Phenols occur in wastewater of a number of industries, such as high temperature coal conversion, petroleum refining, resin and plastic, wood and dye industries, etc. It can be toxic when present at elevated levels and is known to be carcinogeneous. Thus, removal of such compound from these industrial effluents is of great importance. An enzymatic method for removal of phenols from industrial wastewater, using turnip peroxidase, has been developed. Phenol-containing industrial wastewater was treated with immobilized turnip peroxidase in the presence of hydrogen peroxide. In the reaction, a number of phenols are oxidized to form the corresponding free radicals in the presence of hydrogen peroxide as an oxidant. Free radicals polymerize to form substances that are less soluble in water than the original substances. The precipitates were removed by conventional methods and residual phenol was estimated. The present report describes the immobilization of turnip peroxidase on silica via covalent coupling, and its utility in phenol removal. A comparative study was also carried out with other immobilization techniques, viz., calcium alginate entrapment, polyacrylamide gel entrapment, etc. Peroxidase, covalently bound to silica, showed 95% removal of phenol, whereas naphthol was removed up to 99%.     

Production of xylanase by immobilized Trichoderma reesei SAF3 in Ca-alginate beads

In the present study, the optimum conditions for the production of xylanase by immobilized spores of Trichoderma reesei SAF3 in calcium alginate beads were determined. The operational stability of the beads during xylanase production under semi-continuous fermentation was also studied. The influence of alginate concentration (1, 2, 3, and 4%) and initial cell loading (100, 200, 300, 400, and 500 beads per flask) on xylanase production was considered. The production of xylanase was found to increase significantly with increasing concentration of alginate and reached a maximum yield of 3.12 ± 0.18 U ml⁻¹ at 2% (w/v). The immobilized cells produced xylanase consistently up to 10 cycles and reached a maximum level at the forth cycle (3.36 ± 0.2 U ml⁻¹).     

Degradation of ethylbenzene by free and immobilized <Emphasis Type="Italic">Pseudomonas</Emphasis><Emphasis Type="Italic">fluorescens-</Emphasis>CS2

Pseudomonas fluorescens-CS2 metabolized ethylbenzene as the sole source of carbon and energy. The involvement of catechol as the hydroxylated intermediate during the biodegradation of ethylbenzene was established by TLC, HPLC and enzyme analysis. The specific activity of Catechol 2,3-dioxygenase in the cell free extracts of P. fluorescens-CS2 was determined to be 0.428 μmoles min⁻¹ mg⁻¹ protein. An aqueous-organic, Two-Phase Batch Culture System (TPBCS) was developed to overcome inhibition due to higher substrate concentrations. In TPBCS, P. fluorescens-CS2 demonstrated ethylbenzene utilization up to 50 mM without substrate inhibition on inclusion of n-decanol as the second phase. The rate of ethylbenzene metabolism in TPBCS was found enhance by fivefold in comparison with single phase system. Alternatively the alginate, agar and polyacrylamide matrix immobilized P. fluorescens-CS2 cells efficiently degraded ethylebenzene with enhanced efficiency compared to free cell cultures in single and two-phase systems. The cells entrapped in ployacrylamide and alginate were found to be stable and degradation efficient for a period of 42 days where as agar-entrapped P. fluorescens was stable and efficient a period of 36 days. This demonstrates that alginate and polyacrylamide matrices are more promising as compared to agar for cell immobilization.     

Micropropagation of <Emphasis Type="Italic">Penthorum chinense</Emphasis> through axillary bud

This study reports a protocol for successful micropropagation of Penthorum chinense using nodal explants on Murashige and Skoog (MS) medium supplemented with 6-benzyladenine (BA) or kinetin (Kn). The presence of BA promoted a higher rate of shoot multiplication than Kn. Maximum multiple shoot formation was observed in 59.2% of nodal explants cultured on MS medium supplemented with 2.0 mg l⁻¹ BA after 6 wk. After subculture for 4 wk, the maximum number of shoots (6.4) was obtained on a medium with 2.0 mg l⁻¹ BA, but shoots were too short and not suitable for micropropagation. The taller shoots that regenerated in the presence of lower BA concentration (1.0 mg l⁻¹) were selected for root induction study. Most shoots (98.8%) rooted in the presence of 0.5 mg l⁻¹ indole-3-acetic acid after 3 wk, with each shoot forming an average of 10.0 roots. Plantlets were transferred to soil and successfully acclimatized.     

Enzymatic detection of heavy metal ions in aqueous solution from vegetable wastes by immobilizing pumpkin (<Emphasis Type="Italic">Cucumis melo</Emphasis>) urease in calcium alginate beads

Enzyme urease is extracted from the discarded seeds of pumpkin. Urease was purified to apparent homogeneity (5.2 fold) by heat treatment at 48 ± 1°C and gel filtration through Sephadex G-200. Effect of model metal ions on the activity of the homogeneous enzyme preparation (sp. activity 353 U/mg protein, A₂₈₀/A₂₆₀ = 1.12) of soluble as well as immobilized enzyme was investigated. The soluble and immobilized urease has been used for the quantitative estimation of general water pollution with heavy metal ions like Hg²⁺, Cu²⁺, Cd²⁺, and Co²⁺. The measurements of the urease residual activity have been carried out in tris-acetate buffer after pre-incubation of model metal salt. The inhibition was found to be biphasic with an initial rapid loss of activity and remainder in slow phase of 10∼15 min. The immobilization was done in 3.5% alginate beads leading to 86% of entrapment. There was no leaching of the enzyme over a period of 15 days at 4°C. The beads were fairly stable up to 50°C and exhibited activity even at −10°C. The inhibition by these ions was non-competitive and irreversible, hence could not be restored by dialysis. Based on the values of inhibition constant Ki the heavy-metal ions were found to inhibit urease in the following order Hg²⁺ > Cu²⁺ > Cd²⁺ > Co²⁺.     

Effect of salicylic acid potentiates cadmium-induced oxidative damage in <Emphasis Type="Italic">Oryza sativa</Emphasis> L. leaves

In the present investigation, we studied the possible potentiating effect of salicylic acid (SA) under Cd toxicity in Oryza sativa L. leaves. Cd treatments for 24 h reduced the shoot length, dry biomass and total chlorophyll content followed by high Cd accumulation in shoots. About 16 h presoaking with SA resulted in partial protection against Cd, as observed by minor changes in length, biomass and total chlorophyll. SA priming resulted in low Cd accumulation. Enhanced thiobarbituric acid reactive substances (TBARS), hydrogen peroxide (H₂O₂) and superoxide anion (O₂ ⁻) content were seen when Cd was applied alone, while under SA priming the extent of TBARS, H₂O₂ and O₂ ⁻ were significantly low, suggesting SA-regulated protection against oxidative stress. The antioxidant enzymes like Catalase (CAT), guaiacol peroxidase (GPx), glutathione reductase (GR) and superoxide dismutase (SOD) showed varied activities under Cd alone. CAT activity increased after Cd treatment, followed by a decline in GPX and GR activity. SOD also declined at the highest concentrations with an initial increase. Under SA-priming conditions, the efficiency of the antioxidant enzymes was significantly elevated. GPx and SOD activity showed significant increase in activity. The ascorbate activity increased after Cd treatment, followed by a decline in glutathione under SA-free condition. SA priming showed gradual increase in these non-enzymic antioxidants. Our results indicate that Cd-induced oxidative stress can be regulated by SA.     

Immobilization of watermelon (<Emphasis Type="Italic">Citrullus vulgaris</Emphasis>) urease in agarose gel for urea estimation

Urease from dehusked seeds of watermelon was immobilized in 1.5% agarose gel with 53.9% entrapment. There was negligible leaching (<10% at 4°C) and the same gel membrane could repeatedly be used for seven days. The immobilization exhibited no apparent change in the optimum pH but there was a significant decrease in the optimum temperature (50°C as compared to 65°C for soluble urease). The immobilized urease revealed an apparentK _m of 9.3±0.3 mM; 1.2 times lower than the soluble enzyme (11.4±0.2 mM). Unlike soluble enzyme which was inhibited at 200 mM urea, the immobilized urease was inhibited at 600 mM of urea and above, and about 47% activity was retained at 2 M urea. The time-dependent thermal inactivation kinetics at 48 and 52°C was found to be biphasic, in which half of the initial activity was destroyed more rapidly than the remaining half. These gel membranes were also used for estimating the urea content of the blood samples from the University hospital. The results obtained matched well with those obtained by the usual method employed in the clinical pathology laboratory. The significance of these observations is discussed.     

Lactic acid production from hemicellulosic hydrolyzate by cells of <Emphasis Type="Italic">Lactobacillus bifermentans</Emphasis> immobilized in Ca-alginate using response surface methodology

Consumption of hexoses/pentoses and production of lactic acid by Lactobacillus bifermentans were investigated in optimized culture medium and hemicellulosic hydrolyzates. The hydrolyzate used had the following composition (expressed in gL⁻¹): xylose 50 ± 5 gL⁻¹; glucose 18 ± 3 gL⁻¹; arabinose 29 ± 5 gL⁻¹. The immobilization experiments were conducted with microbial cells entrapped in calcium alginate beads. The results indicate that maximum concentrations of lactic acid were produced after 54 h of fermentation. All glucose and arabinose in wheat bran hydrolyzate were consumed during fermentation. Only xylose was not completely consumed. The substrate consumption rate was 3.2 gh⁻¹, 1.9 gh⁻¹, 1.6 gh⁻¹ respectively for glucose, arabinose, and xylose. The optimized culture condition gave a lactic acid concentration and metabolic yield of 62.77 gL⁻¹ and 0.83 gg⁻¹. These parameters improved to 41.3 gL⁻¹ and 0.47 gg⁻¹ respectively, when cell free was used.     

Long-term production of soluble human Fas ligand through immobilization of <Emphasis Type="Italic">Dictyostelium discoideum</Emphasis> in a fibrous bed bioreactor

The production of recombinant glycoproteins in Dictyostelium discoideum by conventional cell culture methods was limited by low cell density as well as low growth rate. In this work, cotton towel with a good adsorption capability for D. discoideum cells was used as the immobilization matrix in an external fibrous bed bioreactor (FBB) system. With batch cultures in the FBB, the concentration of immobilized cells in the cotton fiber carrier increased to 1.37 × 10⁸ cells per milliliter after 110-h cultivation, which was about tenfold higher than the maximal cell density in the conventional free-cell culture. Correspondingly, a high concentration of soluble human Fas ligand (hFasL; 173.7 μg l⁻¹) was achieved with a high productivity (23 μg l⁻¹ h⁻¹). The FBB system also maintained a high density of viable cells for hFasL production during repeated-batch cultures, achieving a productivity of 9∼10 μg l⁻¹ h⁻¹ in all three batches studied during 15 days. The repeated-batch culture using immobilized cells of D. discoideum in the FBB system thus provides a good method for long-term and high-level production of hFasL.     

Biological denitrification by <Emphasis Type="Italic">Pseudomonas stutzeri</Emphasis> immobilized on microbial cellulose

This study demonstrated the feasibility of a biological denitrification process using immobilized Pseudomonas stutzeri. The microbial cellulose (MC) from Acetobacter xylinum was used as the support material for immobilization of the bacterium. Nitrate removal took place mainly in the anoxic system. The effects of various operating conditions such as the initial nitrate concentration, pH, and carbon source on biological denitrification were demonstrated experimentally. The system demonstrated a high capacity for reducing nitrate concentrations under optimum conditions. The denitrification rate increased up to a maximal value of 1.6 kg NO₃-N m⁻³ day⁻¹ with increasing nitrate loading rate. Because of its porosity and purity, MC may be considered as appropriate supports for adsorbed immobilized cells. The simplicity of immobilization and high efficiency in operation are the main advantages of such systems. To date, the immobilization of microorganisms onto MC has not been carried out. The results of this research shows that a pilot bioreactor containing P. stutzeri immobilized on MC exhibited efficient denitrification with a relatively low retention time.     

Immobilization of cyclodextrin glucanotransferase on amberlite IRA-900 for biosynthesis of transglycosylated xylitol

Cyclodextrin glucanotransferase (CGTase) fromThermoanaerobacter sp. was adsorbed on the ion exchange resin Amberlite IRA-900. The optimum conditions for the immobilization of the CGTase were pH 6.0 and 600 U CGTase/g resin, and the maximum yield of immobilization was around 63% on the basis of the amount ratio of the adsorbed enzyme to the initial amount in the solution. Immobilization of CGTase shifted the optimum temperature for the enzyme to produce transglycosylated xylitol from 70°C to 90°C and improved the thermal stability of immobilized CGTase, especially after the addition of soluble starch and calcium ions. Transglycosylated xylitol was continuously produced using immobilized CGTase in the column type packed bed reactor, and the operating conditions for maximum yield were 10% (w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10% (w/v) xylitol as the glycosyl acceptor, 20 mL/h of medium flow rate, and 60°C. The maximum yield of transglycosylated xylitol and productivity were 25% and 7.82 g·L⁻¹·h⁻¹, respectively. The half-life of the immobilized CGTase in a column type packed bed reactor was longer than 30 days.     

Involvement of oxidative stress and role of antioxidative defense system in growing rice seedlings exposed to toxic concentrations of aluminum

When seedlings of rice (Oryza sativa L.) cultivar Pant-12 were raised in sand cultures containing 80 and 160 μM Al³⁺ in the medium for 5–20 days, a regular increase in Al³⁺ uptake with a concomitant decrease in the length of roots as well as shoots was observed. Al³⁺ treatment of 160 μM resulted in increased generation of superoxide anion (O₂ ⁻) and hydrogen peroxide (H₂O₂), elevated amount of malondialdehyde, soluble protein and oxidized glutathione and decline in the concentrations of thiols (-SH) and ascorbic acid. Among antioxidative enzymes, activities of superoxide dismutase (SOD EC 1.15.1.1), guaiacol peroxidase (Guaiacol POX EC 1.11.1.7), ascorbate peroxidase (APX EC 1.11.1.11), monodehydroascorbate reductase (MDHAR EC 1.6.5.4), dehydroascorbate reductase (EC 1.8.5.1) and glutathione reductase (EC 1.6.4.2) increased significantly, whereas the activities of catalase (EC EC 1.11.1.6) and chloroplastic APX declined in 160 μM Al³⁺ stressed seedlings as compared to control seedlings. The results suggest that Al³⁺ toxicity is associated with induction of oxidative stress in rice plants and among antioxidative enzymes SOD, Guaiacol POX and cytosolic APX appear to serve as important components of an antioxidative defense mechanism under Al³⁺ toxicity. PAGE analysis confirmed the increased activity as well as appearance of new isoenzymes of APX in Al³⁺ stressed seedlings. Immunoblot analysis revealed that changes in the activities of APX are due to changes in the amounts of enzyme protein. Similar findings were obtained when the experiments were repeated using another popular rice cv. Malviya-36.     

Immobilization of <Emphasis Type="Italic">Streptomyces</Emphasis> phospholipase D on a Dowex macroporous resin

The immobilization of phospholipase D produced by Streptomyces sp. YU100 was evaluated to see it would be practical for industrial applications. To accomplish this, the purified enzyme, which contained 53 unit/mg of protein, was subjected to immobilization on various matrices. When immobilization supports including calcium alginate gel, polyacrylamide gel, and macroporous resin were evaluated, the highest enzyme retention ratio (> 42%) was observed on a Dowex MSA-2 macro-porous resin. This may have occurred as a result of the ability of the hydrophobic domain of phospholipase D to interact with the polystyrene backbone of the resin, as well as the ability of the dimethylethanolamine group of the MSA-2 resin to retain the enzyme by forming hydrogen bonds with the acidic residues of the enzyme. Upon the operation of a reactor packed with enzyme that had been immobilized on a Dowex MSA-2 resin, greater than 80% of the initial enzyme activity was retained for 16 days. During the reaction, phosphatidylcholine became bound to the immobilized resin and interfered with the enzyme reaction, therefore, the resin was washed with ethyl ether every 2 h. A process for recovering excessive l-serine from phospholipids using the Dowex MR-3 resin was designed, and the separated l -serine was employed again after replacing the amount that was used.     

Biodegradation of phenol by immobilized Aspergillus awamori NRRL 3112 on modified polyacrylonitrile membrane

Covalent immobilization of Aspergillus awamori NRRL 3112 was conducted onto modified polyacrylonitrile membrane with glutaraldehyde as a coupling agent. The polymer carrier was preliminarily modified in an aqueous solution of NaOH and 1,2-diaminoethane. The content of amino groups was determined to be 0.58 mgeq g⁻¹. Two ways of immobilization were used—in the presence of 0.2 g l⁻¹ phenol and without phenol. The capability of two immobilized system to degrade phenol (concentration—0.5 g l⁻¹) as a sole carbon and energy source was investigated in batch experiments. Seven cycles of phenol biodegradation were conducted. Better results were obtained with the immobilized system prepared in the presence of phenol, regarding degradation time and phenol biodegradation rate. Scanning electron micrographs of the polyacrylonitrile membrane/immobilized Aspergillus awamori NRRL at the beginning of repeated batch cultivation and after the 7th cycle were compared. After the 7th cycle of cultivation the observations showed large groups of cells. The results from the batch experiments with immobilized system were compared to the results produced by the free strain. Phenol biodegradation experiments were carried out also in a bioreactor with spirally wound membrane with bound Aspergillus awamori NRRL 3112 in a regime of recirculation. 10 cycles of 0.5 g l⁻¹ phenol biodegradation were run consecutively to determine the degradation time and rate for each cycle. The design of the bioreactor appeared to be quite effective, providing large membrane surface to bind the strain.     

Immobilization of soybean (Glycine max) urease on alginate and chitosan beads showing improved stability: Analytical applications

The soybean (Glycine max) urease was immobilized on alginate and chitosan beads and various parameters were optimized and compared. The best immobilization obtained were 77% and 54% for chitosan and alginate, respectively. A 2% chitosan solution (w/v) was used to form beads in 1N KOH. The beads were activated with 1% glutaraldehyde and 0.5 mg protein was immobilized per ml of chitosan gel for optimum results. The activation and coupling time were 6 h and 12 h, respectively. Further, alginate and soluble urease were mixed to form beads and final concentrations of alginate and protein in beads were 3.5% (w/v) and 0.5 mg/5 ml gel. From steady-state kinetics, the optimum temperature for urease was 65 °C (soluble), 75 °C (chitosan) and 80 °C (alginate). The activation energies were found to be 3.68 kcal mol⁻¹, 5.02 kcal mol⁻¹, 6.45 kcal mol⁻¹ for the soluble, chitosan- and alginate-immobilized ureases, respectively. With time-dependent thermal inactivation studies, the immobilized urease showed improved stability at 75 °C and the t_1/2 of decay in urease activity was 12 min, 43 min and 58 min for soluble, alginate and chitosan, respectively. The optimum pH of urease was 7, 6.2 and 7.9 for soluble, alginate and chitosan, respectively. A significant change in K_m value was noticed for alginate-immobilized urease (5.88 mM), almost twice that of soluble urease (2.70 mM), while chitosan showed little change (3.92 mM). The values of V_max for alginate-, chitosan-immobilized ureases and soluble urease were 2.82 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein, 2.65 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein and 2.85 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein, respectively. By contrast, reusability studies showed that chitosan–urease beads can be used almost 14 times with only 20% loss in original activity while alginate–urease beads lost 45% of activity after same number of uses. Immobilized urease showed improved stability when stored at 4 °C and t_1/2 of urease was found to be 19 days, 80 days and 121 days, respectively for soluble, alginate and chitosan ureases. The immobilized urease was used to estimate the blood urea in clinical samples. The results obtained with the immobilized urease were quite similar to those obtained with the autoanalyzer^®. The immobilization studies have a potential role in haemodialysis machines.     

Lactic acid production from cellulosic waste by immobilized cells of Lactobacillus delbrueckii

Industrial waste corn cob residue (from xylose manufacturing) without pretreatment was hydrolyzed by cellulase and cellobiase. The cellulosic hydrolysate contained 52.4 g l⁻¹ of glucose and was used as carbon source for lactic acid fermentation by cells of Lactobacillus delbrueckii ZU-S2 immobilized in calcium alginate gel beads. The final concentration of lactic acid and the yield of lactic acid from glucose were 48.7 g l⁻¹ and 95.2%, respectively, which were comparative to the results of pure glucose fermentation. The immobilized cells were quite stable and reusable, and the average yield of lactic acid from glucose in the hydrolysate was 95.0% in 12 repeated batches of fermentation. The suitable dilution rate of continuous fermentation process was 0.13 h⁻¹, and the yield of lactic acid from glucose and the productivity were 92.4% and 5.746 g l⁻¹ h⁻¹, respectively. The production of lactic acid by simultaneous saccharification and fermentation (SSF) process was carried out in a coupling bioreactor, the final concentration of lactic acid was 55.6 g l⁻¹, the conversion efficiency of lactic acid from cellulose was 91.3% and the productivity was 0.927 g l⁻¹ h⁻¹. By using fed-batch technique in the SSF process, the final concentration of lactic acid and the productivity increased to 107.6 g l⁻¹ and 1.345 g l⁻¹ h⁻¹, respectively, while the dosage of cellulase per gram substrate decreased greatly. This research work should advance the bioconversion of renewable cellulosic resources and reduce environmental pollution.     

Production of molecular hydrogen with immobilized cells ofRhodospirillum rubrum

Summary Cells ofRhodospirillum rubrum have been immobilized in various gels and tested for photobiological hydrogen production. Agar proved to be the best immobilizing agent with respect to production rates as well as stability. Agar immobilized cells were also superior compared to liquid suspension cultures. Growth conditions of the cells prior to immobilization, e.g. cell age, light intensity or nutrient composition, were of primary importance for the activity in the later immobilized state. A reactor with agar immobilized cells has been operated successfully over 3000 h with a loss of the activity of about 60%. Mean rates for hydrogen production for immobilized cells in this work during the first 60 to 70 hours after immobilization were in the range of 18 to 34 μl H₂ mg⁻¹ d.w. h⁻¹ and thus by a factor of up to 2 higher than liquid cultures under the same conditions. Maximal rates of hydrogen production (57 μl H₂ ml⁻¹ immobilized cell suspension) were reached in agar gel beads with cells immobilized after 70 h growth in liquid culture in the light and a cell density of 1.0 mg ml⁻¹, 70 h after immobilization.