Optimization of conditions for transformation of maleic acid by immobilized cells of Alcaligenes xylosoxidans subspecies xylosoxidans 260

Immobilized cells of Alcaligenes xylosoxidans subsp. xylosoxidans 260 used 98% of maleic acid (initial concentration of 5.0 g/l medium) in periodic conditions for 48 h. Free cells transformed only 26% of substrate in 96 h. Immobilized cells of a selected S-variant of A. xylosoxidans used maleate (30.0 g/l) entirely in 96 h during periodic cultivation and only 15.0 g/l of maleate in continuous cultivation at a flow rate of 0.03 h-1.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from a mixture of xylose and glucose by co-cultivation of lactic acid bacteria

The production of optically pure lactic acid in a high yield from xylose or a mixture of xylose and glucose, which is a model hydrolysate of lignocellulose, is described. In a single cultivation, Enterococcus casseliflavus produced 38 g/l of lactic acid with an optical purity of 96% enantiomeric excess (ee) and 6.4 g/l of acetic acid from 50 g/l of xylose when MRS medium was used. When a mixture of 50 g/l of xylose and 100 g/l of glucose was used as the carbon source in a cultivation of E. casseliflavus alone, glucose was converted to lactic acid in the early phase of the cultivation but xylose was hardly consumed. In a co-cultivation where E. casseliflavus and Lactobacillus casei specific for glucose were simultaneously inoculated, little or no lactic acid was produced after the glucose was almost consumed. A co-cultivation with two-stage inoculation (in which E. casseliflavus was added at a cultivation time of 40 h after L. casei cells were inoculated) resulted in complete consumption of 50 g/l of xylose and 100 g/l of glucose. In the co-cultivation, 95 g/l of lactic acid with a high optical purity of 96% ee was obtained at 192 h. Such a co-cultivation using two microorganisms specific for each sugar is considered to be one promising cultivation technique for the efficient production of lactic acid from a sugar mixture derived from lignocellulose.     

Maleic Acid Utilization by Mixed Cultures of Microorganisms

In a mixed batch culture, Alcaligenes xylosoxidans subsp. xylosoxidans 260 transformed maleic acid into malic acid. Bacillus subtilis 271 used malic acid as a substrate, thus stimulating further transformation of maleic acid. Both bacterial cultures dissociated with the formation of R, S, and M forms. At a concentration of 5.0 g/l, maleic acid was utilized maximally by RS and SS forms of the association A. xylosoxidans and B. subtilis. At concentrations 15.0 and 25.0 g/l, maleic acid was utilized maximally by SS and MS forms of the mixed culture, respectively. Association of bacteria A. xylosoxidans and B. subtilis was not stable under flow conditions of water.     

Response of Intact Cyanobacterial Cells and their Photosynthetic Apparatus to Cd2+ Ion Treatment

Intact cells of Synechococcus elongatus were treated with different concentrations (0.1 and 1.0 mM = Cd_0.1, Cd_1.0) of CdCl₂ for 24 h. Cd_0.1 treatment stimulated growth of the cell culture and chlorophyll (Chl) a concentration in the culture. Cd_1.0 inhibited both the above mentioned parameters. The oxygen evolving activity of intact cells (H₂O BQ) as well as of isolated thylakoid membranes, TM (H₂O DCPIP; H₂O PBQ + FeCy) decreased after 24 h of Cd_1.0 cultivation to 7 %. Photosystem 1 (PS1) activity was less sensitive to the effect of Cd²⁺ than PS2 activity. CdCl₂ concentration in cultivation media after 24 h of cultivation proved that the cyanobacterium cells take up these ions to a large extent from the cultivation medium. After 24 h of the Cd_1.0 treatment only 12 % of the amount of Cd²⁺ originally added to the cultivation medium was found. The ratio of external-antenna pigments, phycocyanin, and allophycocyanin to Chl increased approximately twofold with growing Cd²⁺ concentration in the cultivation medium. This ratio was found in both TM and dodecylmaltoside extracts.     

Alcoholic fermentation by agar-immobilized yeast cells

Immobilized yeast cells in agar gel beads were used in a packed bed reactor for the production of ethanol from cane molasses at 30°C, pH 4.5. The maximum productivity, 79.5g ethanol/l.h was obtained with 195g/l reducing sugar as feed. Substrate (64.2%) was utilized at a dilution of 1.33h^-1. The immobilized cell reactor was operated continuously at a constant dilution rate of 0.67h^-1 for 100 days. The maximum specific ethanol productivity and specific sugar uptake rate were 0.610g ethanol/g cell.h and 1.275g sugar/g cell.h, respectively.     

High concentration cultivation of Bifidobacterium longum in fermenter with cross-flow filtration

Summary High concentration cultivation of Bifidobacterium longum in a fermenter with cross-flow filtration using a ceramic filter is described. Continuous cross-flow filtration allowed complete recycling of the cells to the fermenter and also continuous separation of inhibitory metabolites. The final cell concentration attained in the cultivation was 54.4 g dry wt./l; this was seven times as high as that without cross-flow filtration. The time course of the cultivation with cross-flow filtration was predicted, based on the assumption that the specific growth rate can be expressed only as a function of concentrations of metabolites (acetate and lactate) in a culture broth.Nomenclature D dilution rate (h^-1) - m maintenance coefficient (h^-1) - OD ₅₇₀ optimal density at 570 nm - P _A acetate concentration (g/l) - P _A0 initial acetate concentration (g/l) - P _L lactate concentration (g/l) - P _L0 initial lactate concentration (g/l) - S lactose (substrate) concentration (g/l) - S ₀ initial lactose (substrate) concentration (g/l) - t cultivation time (h) - Y _x/s growth yield (g/g) - X dry cell concentration (g/l) - X ₀ initial dry cell concentration (g/l) - constant - constant     

High-performance fermentation with lactic acid bacteria entrapped in pectate gel. Immobilizates with enhanced lactate formation activity

High-loaded pectate gels containing more than 10¹⁴ cells/l of gel (viability > 60%) were obtained. Immobbilizates of Lactobacillus sp. IMET 11466 showed a maximum mean gel activity of 120 g of lactate/l of gel * h. With the strain Streptococcus thermophilus ? 129 a value of 139 g of lactate/l of gel * h was attained. Using these immobilizates the conversion of 100 g of glucose/l with a yield of 90–95% can be realized in only 6–8 h. On the basis of a detailed analysis of the time course of the lactate-forming activity of the immobilizates during batch fermentations evidence is given of an analogy in the lactate-inhibitory behaviour of immobilized and free cells.     

Enhanced conversion of sucrose to isomaltulose by a mutant of Erwinia rhapontici

Mutagenesis of Erwinia rhapontici was performed to enhance the production of isomaltulose from sucrose. A mutant strain, BN 68089, was obtained through a screening process involving automated and miniaturized cultivation in Bioscreen C. This high-throughput, miniaturized screening system was optimized to identify the mutant strain, which had a conversion yield (90%) and productivity (194 g l^–1 h^–1). The BN 68089 mutant cells were immobilized in sodium alginate and when operated in a packed bed reactor gave a yield of 89% and a productivity of 144 g l^–1 h^–1 of at 30 °C, the optimal temperature. Immobilized BN 68089 cells exhibited 8% and 15% higher yield and productivity, respectively, than those of the wild-type strain.     

Biotransformation of tolbutamide to 4′-hydroxytolbutamide by the fungus Cunninghamella blakesleeana

The hypoglycemic drug tolbutamide is commonly used as a probe drug to evaluate CYP2C9 enzyme activity in terms of production of 4′-hydroxytolbutamide. In the present study, an initial screening of seven filamentous fungi was carried out to identify which was most competent to transform tolbutamide into 4′-hydroxytolbutamide. From this screening, the fungus Cunninghamella blakesleeana AS 3.910 was selected as a suitable bioconverter. At a concentration of 1.2 mg ml⁻¹, the growing fungus transformed 95.0% of tolbutamide into 4′-hydroxytolbutamide in 96 h. With resting culture, the yield could reach 91.7% and exceeded 91.0% even when the tolbutamide concentration was increased to 4.0 mg ml⁻¹. On scale-up to 3 l buffer containing 12.0 g tolbutamide, 90% of tolbutamide was transformed into 4′-hydroxytolbutamide in 96 h. Work-up of the broth by column chromatography and recrystallization yielded 6.5 g (53.9% recovered) of 4′-hydroxytolbutamide with a purity of more than 99%. These results suggest C. blakesleeana AS 3.910 is a useful biosynthetic tool in the preparation of 4′-hydroxytolbutamide.     

Vertical Rotating Immobilized Cell Reactor of the bacteriumZymomonas mobilis for stable long-term continuous ethanol production

Summary Vertical Rotating Immobilized Cell Reactor was designed and built for glucose conversion into ethanol. Immobilized biomass units withZ. mobilis cells attached into polyurethane foam discs were fixed along a rotating shaft inside the bioreactor. The effect of rotation speed on the concentration of immobilized biomass was studied. Stability of the bioreactor over long-term operation was dependent on the concentration of the immobilized biomass. With fermentation carried out at 6 rpm a constant active immobilized cell concentration of only 34.5 g/l was maintained and used to convert up to 140 g glucose/l into more than 70 g ethanol/l with a volumetric ethanol productivity of 63 g/l/h.     

Ammonium lactate from deproteinized alfalfa juice byStreptococcus faecium

Summary Deproteinized alfalfa juice is a by-product of the mechanical fractionation of alfalfa to obtain protein. In this work the juice was used as the substrate for the production of ammonium lactate (l-lactic acid) by a strain ofStreptococcus faecium. Batch fermentation with a constant pH of 5.8 gave 27.2 g/l of lactic acid (90% conversion and 1.1 g/l/h productivity) and 6×10¹² cells/l after 24 h. Semicontinuous fermentation allowed the conversion of 3-times the volume of deproteinized juice after 44 h, finally giving 29.7 g/l of ammonium lactate (99% conversion and 2.5 g/l/h productivity) and 4–6×10¹² cells/l.     

Selective production of glutamate by an immobilized marine blue-green alga,Synechococcus sp.

Summary Among 200 strains of marine bluegreen algae isolated from the coastal areas of Japan, the marine blue-green alga Synechococcus sp. NKBG 040607 excreted glutamate at the highest rate, 82.6% of total amino acids production being glutamate. Synechococcus sp. NKBG 40607 was immobilized in calcium alginate gel. Glutamate production by immobilized cells was double that of native cells. Maximal glutamate production (25 g/cm³ gel per day) of the immobilized cells was observed under a light intensity of 144 Einstein/m² per second at a cell concentration of 7.5 mg dry cells/cm³ gel. Immobilized cells of Synechococcus sp. can use nitrate as a nitrogen source. Immobilized marine Synechococcus sp. produced 0265 mg/cm³ gel of glutamate for 7 days in the presence of chloramphenicol.     

Oxidative biotransformation of thioanisole by <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> IEGM 66 cells

Comparative study of sulfoxidation activity of free and immobilized Rhodococcus rhodochrous IEGM 66 cells was performed. Free Rhodococcus cells (in the presence of 0.1 vol % n-hexadecane) displayed maximal oxidative activity towards thioanisole (0.5 g/l), a prochiral organic sulfide, added after 48-h cultivation of bacterial cells. Higher sulfide concentrations inhibited sulfoxidation activity of Rhodococcus. Use of immobilized cells allowed the 2-day preparatory stage to be omitted and a complete thioanisole bioconversion to be achieved in 24 h in the case that biocatalyst and 0.5 g/l thioanisole were added simultaneously. The biocatalyst immobilized on gel provides for complete thioanisole transformation into (S)-thioanisole sulfoxide (optical purity of 82.1%) at high (1.0–1.5 g/l) concentrations of sulfide substrate.     

The effect of pH,temperature and sucrose concentration on high productivity continuous ethanol fermentation using Zymomonas mobilis

Summary A flocculent strain of Zymomonas mobilis was used for ethanol production from sucrose. Using a fermentor with cell recycle (internal and external settler) high sugar conversion and ethanol productivity were obtained. At a dilution rate of 0.5 h^-1 (giving 96% sugar conversion) the ethanol productivity, yield and concentrations respectively were 20 g/l/h, 0.45 g/g and 40 g/l using a medium containing 100 g/l sucrose. At a sucrose concentration of 150 g/l, the ethanol concentration reached 60 g/l. The ethanol yield was 80% theoretical due to levan and fructo-oligomer formation. No sorbitol was detected. This fermentation was conducted at a range of conditions from 30 to 36°C and from pH 4.0 to 5.5.     

Production of L-DOPA from pyrocatechol and DL-serine by bioconversion using immobilized Erwinia herbicola cells

Summary Immobilized cells of Erwinia herbicola were used for L-DOPA production from pyrocatechol and DL-serine. Optimal conditions have been defined and utilized in batch and continuous reactors. A maximal volumetric productivity of 0.46 g/l.h in L-DOPA was obtained with a conversion yield of 18% (L-DOPA concentration 2.3 g/l).     

Production of poly(3-hydroxybutyrate) from whey by fed-batch culture of recombinant Escherichia coli in a pilot-scale fermenter

Production of poly(3-hydroxybutyrate) [P(3HB)] from wheyby fed-batch culture of recombinant Escherichia coli CGSC 4401 harboring a plasmid containing the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes was examined in a 30 l fermenter supplying air only. With lactose below 2 g l^–1, cells grew to 12 g dry cell l^–1 with 9% (w/w) P(3HB) content. Accumulation of P(3HB) could be triggered by increasing lactose to 20 g l^–1. By employing this strategy, 51 g dry cell l^–1 was obtained with a 70% (w/w) P(3HB) content after 26 h. The productivity was 1.35 g P(3HB) l^–1 h^–1. The same fermentation strategy was used in a 300 l fermenter, and 30 g dry cell l^–1 with 67% (w/w) P(3HB) content was obtained in 20 h.     

Improved synthesis of chiral alcohols with <Emphasis Type="Italic">Escherichia coli</Emphasis> cells co-expressing pyridine nucleotide transhydrogenase,NADP<Superscript>+</Superscript>-dependent alcohol dehydrogenase and NAD<Superscript>+</Superscript>-dependent formate dehydrogenase

Recombinant pyridine nucleotide transhydrogenase (PNT) from Escherichia coli has been used to regenerate NAD⁺ and NADPH. The pnta and pntb genes encoding for the - and -subunits were cloned and co-expressed with NADP⁺-dependent alcohol dehydrogenase (ADH) from Lactobacillus kefir and NAD⁺-dependent formate dehydrogenase (FDH) from Candida boidinii. Using this whole-cell biocatalyst, efficient conversion of prochiral ketones to chiral alcohols was achieved: 66% acetophenone was reduced to (R)-phenylethanol over 12h, whereas only 19% (R)-phenylethanol was formed under the same conditions with cells containing ADH and FDH genes but without PNT genes. Cells that were permeabilized with toluene showed ketone reduction only if both cofactors were present.     

Fed-batch two-phase production of alanine by a metabolically engineered Escherichia coli

dl-Alanine was produced from glucose in an Escherichia coli pfl pps poxB ldhA aceEF pTrc99A-alaD strain which lacked pyruvate-formate lyase, phosphoenolpyruvate (PEP) synthase, pyruvate oxidase, lactate dehydogenase, components of the pyruvate dehydogenase complex and over-produced alanine dehydrogenase (ALD). A two-phase process was developed with cell growth under aerobic conditions followed by alanine production under anaerobic conditions. Using the batch mode, cells grew to 5.3 g/l in 9 h with the accumulation of 6–10 g acetate/l, and under subsequent anaerobic conditions achieved 34 g alanine/l in 13 h with a yield of 0.86 g/g glucose. Using the fed-batch mode at μ = 0.15 h⁻¹, only about 1 g acetate/l formed in the 25 h required for the cells to reach 5.6 g/l, and 88 g alanine/l accumulated during the subsequent 23 h. This fed-batch process attained an alanine volumetric productivity of 4 g/lh during the production phase, and a yield that was essentially 1 g/g.     

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

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

Conversion of soybean sterols into 3,17-diketosteroids using actinobacteria <Emphasis Type="Italic">Mycobacterium neoaurum,Pimelobacter simplex</Emphasis>, and <Emphasis Type="Italic">Rhodococcus erythropolis</Emphasis>

Soybean sterols were converted into androst-4-ene-3,17-dione (AD) and 9α-hydroxyandrost-4-ene-3,17-dione (9-OH-AD) using three actinobacterium strains. The transformation of a microcrystallic substrate (particle size 5–15 μm) or the transformation in the presence of randomly methylated β-cyclodextrin (MCD) were carried out by Mycobacterium neoaurum with a phytosterol load of 30 g/l over 144 h with an AD content of 14.5 and 15.2 g/l, respectively. AD obtained in the presence of MCD was transformed into ADD (13.5 g/l) by Pimelobacter simplex cells over 3 h and into 9-OH-AD by Rhodococcus erythropolis cells after 22 h without the isolation of AD from the cultural liquid. The crude product ADD was obtained in 75% yield, based on phytosterol. It contained as by-products 1.25% of AD and 1.5% of 1,2-dehydrotestosterone. In a control experiment—the process of 1,2-dehydrogenation of 20 g/l AD in the water solution of MCD—no by-products were isolated. Thus, it is more expedient to introduce the 1,2-double bond into pure AD, whereas R. erythropolis strain with low destructive activity towards steroid nucleus can be used in the mixed culture with M. neoaurum. The crystal product contained, according to HPLC, 80% of 9-OH-AD, and 1.5% AD was obtained. The yield of 9-OH-AD (m.p. 218–220°C) based on transformed phytosterol was 56%.