Removal of hydrogen sulfide by Chlorobium thiosulfatophilum in immobilized-cell and sulfur-settling free-cell recycle reactors.

Bioconversion of hydrogen sulfide to elementary sulfur by the photosynthetic bacterium Chlorobium thiosulfatophilum was studied in immobilized-cell and sulfur-settling free-cell recycle reactors. The cells immobilized in strontium alginate beads excreted elementary sulfur and accumulated it as crystal in the bead matrices, which made it possible that the reactor broth remained clear and the light penetrated the reactor deeper than with the free cells. In comparison with the free cells, the immobilized cells required 30% less light energy at a H2S removal rate of 2 mM/(L.h) and showed an activity of 2.4 times that of the free cells. However, in 40 h after the reaction the deterioration of the H2S removal efficiency became significant due to the accumulation of sulfur in the beads. The scanning electron micrograph (SEM) and energy-dispersive X-ray spectrometer (EDS) studies showed that the sulfur in the beads existed within a layer of 0.4 mm from the bead surface. In the sulfur-settling free-cell recycle reactor, about 80% of the sulfur excreted by the free cells could be removed in a settler. The 4-L fed batch reactor with the settler improved the light transmission to result in a H2S removal rate of 3 mumol/(mg of protein.h), 50% higher than that without it. The settling recycle reactor was much better in the removal of H2S than the immobilized-cell reactor because the former was a continuous system with the constant removal of sulfur particles by settling and of spent medium by supplying fresh medium at the same rate as the filtering rate of the reactor broth, while the latter was essentially a batch system where toxic metabolites and produced sulfur could not be removed.     

Bioconversion of gitoxigenin by immobilized plant cells in a column bioreactor

Summary Daucus carota cells immobilized in a Ca-alginate performed the bioconversion of gitoxigenin to 5-hydroxygitoxigenin in a column bioreactor. The smooth spherical shape of the alginate beads was preserved for more than three weeks. The bioreactor was functional for more than thirty days as detected by the bioconversion activity. The rate of bioconversion was influenced by means of aeration.Issued as National Research Council of Canada Publication Number 19556     

Bioconversion of lipophilic compounds by immobilized microbial cells in organic solvents

Microbial cells were gel-entrapped with photo-crosslinkable resin prepolymers or urethane prepolymers, respectively. The resulting gels have different tailor-made hydrophobic or hydrophilic character. They were used for successful bioconversion of hydrophobic steroids and terpenoids in watersaturated mixtures of organic solvents. The experiments show the influence of the hydrophobicity of the gels and the polarity of the solvent mixtures, respectively. Use of hydrophobic gels and less polar solvents is preferable for bioconversion of hydrophobic compounds. The selective formation of a desired product among diverse products from a single substrate by appropriate use of hydrophobic or hydrophilic gels is possible. In each case, tests should be made to select the appropriate gel and solvent mixture. Bioconversions tested are: dehydroepiandrosterone to 4-androstene-3,17-dione; cholesterol to cholestenone; β-sitosterol to β-sitostenone; stigmasterol to stigmastenone; pregnenolone to progesterone; testosterone to Δ¹-dehydrotestosterone or 4-androstene-3,17-dione, respectively; all with immobilized cells of Nocardia rhodocrous; and stereoselective hydrolysis of dl-menthyl-succinate to yield l-menthol with immobilized cells of Rhodotorula minuta var. texensis.     

Removal of dimethyl sulfide,methyl mercaptan,and hydrogen sulfide by immobilized Thiobacillus thioparus TK-m

Cells of Thiobacillus thioparus TK-m were immobilized on cylindrical porous polypropylene pellets (5 mmφ × 5 mm) which were packed in an acrylic cylinder of 50 mm inner diameter up to the height of 800 mm. When a sulfur-containing malodorous gas was charged to this packed tower at the superficial velocity of 0.1 m/s, maximum loading capacity (mmol/l·d) for a malodorous gas to attain the removal rate of 95% or more was: 3.65 for dimethyl sulfide, 8.74 for methyl mercaptan, and 17.36 for hydrogen sulfide. At this time, the inlet concentration (μl/l) of the malodorous compound was: 7.44 for dimethyl sulfide, 17.8 for methyl mercaptan, and 35.4 for hydrogen sulfide. For every compound, higher loading resulted in greater removal quantities. The removal rate of dimethyl sulfide was not overly affected by the presence of a large amount of easily decomposable hydrogen sulfide.     

Kinetics of hydrogen sulfide oxidation by immobilized autotrophic and heterotrophic bacteria in bioreactors

Summary The kinetics of H₂S oxidation in bioreactors with separately packed autotrophic Thiobacillus thioparus CH11 and heterotrophic Pseudomonas putida CH11 were evaluated. The reaction rates were determined to be first-order below 20 ppm, zero-order above 60 ppm, and fractional-order in the intermediate concentration ranges for the Thiobacillus thioparus CH11 bioreactor, and first-order below 35 ppm, zero-order above 80 ppm, and fractional-order in the intermediate concentration ranges for the Pseudomonas putida CH11 bioreactor. The saturation constants for H₂S by Thiobacillus thioparus CH11 and Pseudomonas putida CH11 were calculated to be 30.3 ppm and 44.2 ppm, respectively.     

Bioconversion of nitriles by Candida guilliermondii CCT 7207 cells immobilized in barium alginate

Nitrile degradation by Candida guilliermondii CCT 7207 using free and immobilized cell systems was compared. Different specific growth rates were observed for immobilized (mumax=0.021 h(-1)) and the free cells (mumax=0.029 h(-1)). The maximum specific rate of acetic acid formation was 0.387 h(-1) and 0.266 h(-1) for free and immobilized cells, respectively. Cell adhesion to the support materials was confirmed by scanning electron microscopy. When immobilized, the yeast was able to use high nitrile and amide concentrations (aliphatic and aromatic) as nitrogen sources. The results suggest that C. guilliermondii CCT 7207 presents a physiological pattern potentially useful for the bioremediation of polluted environments or for the bioproduction of amides and organic acid of high commercial value.     

Phytate dephosphorylation by free and immobilized cells ofSaccharomyces cerevisiae

Summary Saccharomyces cerevisiae in the form of baker's yeast, cells cultivated on a yeast extract-peptone-glucose medium, as well as cells immobilized in 18% (w/v) polyacrylamide gel showed the ability to hydrolyze 1.727 mM sodium phytate solution at 45°C, pH 4.6, in a stirred tank reactor. Seventy percent yield of dephosphorylation was observed after 2 h using a baker's yeast concentration of 5.8 g dry matter per 100 ml. Hydrolytic activity at 1.8–2.0 M Pi min^–1 was observed between 1st and 3rd h of the reaction in cells cultured 24 or 48 h. No inhibition by the substrate was found at sodium phytate concentrations of 0.587–1.727 mM. After 1.5 h of hydrolysis a single, well distinguished peak ofmyo-inositol-triphosphate was the main product found. By means of immobilization the stability of the biocatalyst was enhanced 3.3-fold and reached its half-life at 64 ninety-minute runs.     

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.     

ByDioscorea deltoidea free and immobilized plant cells

Summary 2-(4-methoxybenzyl)-1-cyclohexanone (1) was converted to its glucoside (4,5) via corresponding alcohols (3,4) usingDioscorea deltoidea Wall. free and immobilized plant cells.     

Glycosylation of ergot alkaloids by free and immobilized cells of Claviceps purpurea

Summary A new strain, Claviceps purpurea 88-EP-47, with high invertase activity was selected. Free and Calginate immobilized cultures of this strain were used for fructosylation of ergot alkaloids. By bioconversion from their aglycones, elymoclavine-O--d-fructofuranosyl(21)-O--d-fructofuranoside, and elymoclavine-O--d-fructoside, the respective fructosides of chanoclavine, lysergol and dihydro-lysergol monofructosides were obtained. These substances are formed by -d-fructofuranosidase present in Claviceps cells. The bioconversion activity of the enzyme system (fructose transfer) is strongly dependent on pH, substrate (sucrose) concentration and the developmental profile of invertase activity. The pH optimum for elymoclavine fructosylation is 6.5, for chanoclavine 5.7, and the optimal sucrose concentration is 75 g/l. Fifteen-day-old production cultures had the best glycosylation activities. Fructosylation of alkaloids can be stimulated in production cultures of C. purpurea or C. fusiformis forming elymoclavine or chanoclavine by a pH shift to 6.5 at the end of the production phase. Glycosylating Claviceps strains producing elymoclavine eliminate the free alkaloid into glycosides. The feedback inhibition of alkaloid synthesis by elymoclavine is then strongly reduced, helping to further improve elymoclavine yields. Elymoclavine can be liberated simply by invertase activity of baker's yeast.Offprint requests to: V. Ken     

Transformation of microcrystalline hydrocortisone by free and immobilized cells of Arthrobacter simplex

Summary The transformation of microcrystalline hydrocortisone by free and immobilized cells of Arthrobacter simplex resulted in formation of prednisolone. The effect of medium composition, non-ionogenic surfactants and exogeneous electron acceptors on the ¹-dexydrogenase activity of free and immobilized cells is described. Offprint requests to: R. Vlahov     

Enzymatic synthesis of 3,4-dihydroxyphenyl-L-alanine by free and immobilized Citrobacter freundii cells

The Citrobacter freundii 62 cells immobilized in PAAG and possessing the tyrosine-phenol-lyase (TPL) activity catalyse the synthesis of 3,4-dihydroxyphenyl-L-alanine (DOPA) from pyrocatechol and ammonium pyruvate. The synthesis of DOPA was studied using both free and immobilized bacterial cells. When the concentration of pyrocatechol is over 0.1 M the TPL activity of the cells is inhibited. The concentration of pyrocatechol can be increased up to 0.3 M by using an equimolar mixture of pyrocatechol and boric acid. The addition of ascorbic acid as an antioxidant results in a lower TPL activity of both free and immobilized bacterial cells.     

Bioconversion of phospholipids by immobilized phospholipase A2

Phospholipase A₂ selectively hydrolyses the ester linkage at the sn-2 position of phospholipids forming lysocompounds. This bioconversion has importance in biotechnology since lysophospholipids are strong bioemulsifiers. The aim of the present work was to study the kinetic behaviour and properties of immobilized phospholipase A₂ from bee venom adsorbed into an ion exchange support. The enzyme had high affinity for CM-Sephadex^® support and the non-covalent interaction was optimum at pH 8. The activity of immobilized phospholipase A₂ was comparatively evaluated with the soluble enzyme using a phospholipid/Triton X-100 mixed micelle as assay system. The immobilized enzyme showed high retention activity and excellent stability under storage. The activity of the immobilized system remained almost constant after several cycles of hydrolysis. Immobilized phospholipase A₂ was less sensitive to pH changes compared to soluble form. The kinetic parameters obtained (V_max 883.4 μmol mg⁻¹ min⁻¹ and a K_m 12.9 mM for soluble form and V_max = 306 μmol mg⁻¹ min⁻¹ and a K_m = 3.9 for immobilized phospholipase A₂) were in agreement with the immobilization effect. The results obtained with CM-Sephadex^®-phospholipase A₂ system give a good framework for the development of a continuous phospholipid bioconversion process.     

Halotolerance studies onChlamydomonas reinhardtii: glycerol excretion by free and immobilized cells

The freshwater green algaChlamydomonas reinhardtii can tolerate a maximum saline concentration of 200 mM NaCl. In response to this osmotic shock, the cells accumulated during the first 24 h 15% of the total glycerol synthesized as osmoregulatory metabolite, to provide the corresponding osmotic balance. After this period all glycerol synthesized was excreted to the medium, 4 g L^-1 at 120 h in optimal conditions, before cell degradation occurred. This excretion was about 2-fold higher in Ca-alginate entrapped cells in the presence of 250 mM NaCl. It was concluded that immobilized cells may be of biotechnological interest for continuous glycerol photoproduction in air-lift bioreactors.     

Bioconversion of linoleic acid into conjugated linoleic acid by immobilized Lactobacillus reuteri

Lactobacillus reuteri was immobilized on silica gel to evaluate the bioconversion of linoleic acid (LA) into conjugated linoleic acid (CLA), consisting of cis-9,trans-11 and trans-10,cis-12 isomers. The amount of cell to carrier, the reaction time, and the substrate concentration, pH, and temperature for CLA production were optimized at 10 mg of cells/(g of carrier), 1 h, 500 mg/L LA, 10.5, and 55 degrees C, respectively. In the presence of 1.0 mM Cu(2+), CLA production increased by 110%. Under the optimal conditions, the immobilized cells produced 175 mg/L CLA from 500 mg/L LA for 1 h with a productivity of 175 mg/(L.h) and accumulated 5.5 times more CLA than that obtained from bioconversion by free washed cells. The CLA-producing ability of reused cells was investigated over five reuse reactions and was maximal at pH 7.5, 25 degrees C, and 1.0 mM Cu(2+). The total amount of CLA by the combined five reuse reactions was 344 mg of CLA/L reaction volume. This was 8.6 times higher than the amount obtained from reuse reactions by free washed cells.     

Oxidation of hydrogen sulfide by Thiobacilli

It has been previously demonstrated that the chemoautotroph and facultative anaerobe, Thiobacillus denitrificans, may be cultured aerobically or anaerobically in batch and continuous reactors on H(2)S(g) under sulfide-limiting conditions. A process has been proposed for the removal of H(2)S from gases based on oxidation of H(2)S by T. denitrificans. Described here is a study of H(2)S oxidation by other Thiobacilli, the purpose of which has been to determine whether other Thiobacilli offer any advantages over T. denitrificans in the aerobic oxidation of H(2)S. Although four other species of Thiobacillus were found to grow on H(2)S as an energy source, none offer a clear advantage over T. denitrificans.     

Palatinose production by free and Ca-alginate gel immobilized cells of Erwinia sp.

Palatinose is a non-cariogenic disaccharide obtained from the enzymatic conversion of sucrose, used in food industries as a sugar substitute. Free and Ca-alginate immobilized cells of Erwinia sp. D12 were used to produce palatinose from sucrose. Palatinose production was studied in a repeated-batch process using different immobilized biocatalysts: whole cells, disrupted cells and glucosyltransferase. Successive batches were treated with the immobilized biocatalyst, but a decrease in palatinose production was observed. A continuous process using a packed-bed reactor was investigated, and found to produce 55–66% of palatinose during 17 days using immobilized cells treated with glutaraldehyde and a substrate flow speed of 0.56 ml min⁻¹. However, immobilized cells in a packed-bed reactor failed to maintain the palatinose production for a prolonged period. The free cells showed a high conversion rate using batch fermentation, obtaining a palatinose yield of 77%. The cells remained viable for 16 cycles with high palatinose yields (65–77%). Free Erwinia sp. D12 cells supported high production levels in repeated-batch operations, and the results showed the potential for repeated reuse.