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.     

Penicillin G production by immobilized fungal vesicles

Summary The activity of penicillin G production was compared in a well defined medium by native vesicles as well as by calcium alginate gel immobilized vesicles isolated from the protoplasts of Penicillium chrysogenum PQ-96. The activity yield of the immobilized vesicles was 44% in comparison with native vesicles. After 60 h of storage at 4° C the native vesicles showed a rapid decrease in penicillin G production. The storage stability of these vesicles was improved after entrapment inside the calcium alginate gel. After 240 h of storage 1 mg of immobilized vesicular protein catalyzed the production of about 140 nmoles of penicillin G in 1 h.     

Biphasic nitrogenase activity in Azospirillum brasilense in long lasting batch cultures

Long lasting batch cultures of Azospirillum brasilense SP 7 ATCC 29145 grown in liquid malate medium for 8–14 days without any fixed nitrogen source exhibited a biphasic nitrogenase activity, when incubated under gas atmospheres of 99.0% N₂ and 1.0% O₂ or 99.5% N₂ and 0.5% O₂ respectively. Maximum specific nitrogenase activity was 1100 nmol C₂H₄·mg protein^-1·h^-1. Poly-3-hydroxybutanoic acid (PHBA) synthesis and growth of the cells also showed two phases. Maxima and minima of glutamine synthetase activity developed synchronously with nitrogenase activity, whereas those of glutamate dehydrogenase and alanine aminotransferase were reverse. During a 192 h period of growth protein increased 3–4-fold and PHBA 25 fold. At maximum accumulation of the polymer the PHBA-nitrogen ratio was 6:1 or 8:1. Azospirillum brasilense was also able to fix nitrogen on agar surfaces exposed to air, but nitrogen fixation was monophasic under these conditions during a 14 d period. Specific nitrogenase activity was dependent on the type and concentration of the source of fixed nitrogen (leucine, ammonia) in solidified media. With 1 mM leucine maximum specific nitrogenase activity was 110 nmol C₂H₄·mg protein^-1·h^-1.Non-Standard Abbreviations PHBA poly-3-hydroxybutanoic acid - TAPS tris(hydroxymethyl)methylaminopropane sulfonic acid - TES N-tris(hydroxymethyl)methyl-2-aminoethane sulfonic acid - TRICINE N-tris(hydroxymethyl)methylglycine - TRIS tris(hydroxymethyl)aminomethane     

Dissimilatory nitrate reduction by a strain ofClostridium butyricum isolated from estuarine sediments

Nitrate dissimilation in chemostat grown cultures ofClostridium butyricum SS6 has been investigated. Sucrose limited cultures grown on nitrate produced nitrite as the principal end-product of nitrate reduction whilst under nitrate-limiting conditions ammonia accumulated in the spent media. Nitrate reduction was accompanied by the synthesis of a soluble nitrate reductase (123 nmol·NADH oxidised · min^-1 · mg protein^-1) and in addition, under N-limiting conditions, a soluble nitrite reductase (56 nmol NADH oxidised min^-1 · mg protein^-1). Corresponding ammonia grown cultures synthesised neither enzyme. Concurrent with the dissimilation of nitrate to nitrite and ammonia cell population densities increased by 18% (C-limitation) and 32% (N-limitation). Spent media analyses of the fermentation products from ammonia and nitrate grown cells showed the accumulation of acetate in nitrate dissimilating cultures. Molar ratios of acetate/butyrate increased by a factor of 5 (C-limitation) to 12 (N-limitation) upon adding nitrate to the growth medium. In C-limited cultures, grown on nitrate, hydrogenase activity was 340 nmol · min^-1 · mg protein^-1 and under N-limitation this increased to 906 nmol · min^-1 · mg protein^-1. Since N-limited cultures are electron acceptor limited, the increase in hydrogenase activity enables excess electrons to be spilled by this route.     

Methyl mercury uptake by free and immobilized cyanobacterium

Methyl mercury uptake in free cells and different immobilizates of the cyanobacteriumNostoc calcicola has been examined. The general growth of the immobilized cyanobacterial cells could be negatively correlated with methyl mercury uptake. Alginate spheres proved most efficient in terms of uptake rate (0.48 nmol mg protein^–1 min^–1, 10 min) and total bioaccumulation (10.71 nmol mg protein^–1, 1 h) with a bioconcentration factor of 3.3×10³. Alginate biofilms showed a faster methyl mercury accumulation rate (0.83 nmol mg protein^–1 min^–1, 10 min) with a saturation of 10.28 nmol mg protein^–1 reached within only 30 min (bioconcentration factor, 3.1×10³). Foam preparations with a slow initial uptake approximated biofilms but were characterized by a lower bioconcentration factor (2.8×10³). Free cells, in comparison, maintained the initial slow rate of uptake (0.62 nmol mg protein^–1 min^–1, 10 min), saturating at 30 min (8.81 nmol mg protein^–1), and the resultant lowest bioconcentration factor (2.7×10³). Cell ageing (30 days) brought a drastic reduction (3-fold) in organomercury uptake by free cells while alginate spheres maintained the same potential. Foam preparations of the same age showed a significant improvement in methyl mercury uptake followed by only a marginal decline in alginate biofilms. Data are discussed in the light of the physiological efficiency and longevity of immobilized cells.     

Glutathione reductase activity in heterocysts and vegetative cells of the cyanobacterium Nostoc muscorum

Glutathione reductase activity was detected and characterized in heterocysts and vegetative cells of the cyanobacterium Nostoc muscorum. The activity of the enzyme varied between 50 and 150 nmol reduced glutathione· min^-1·mg protein^-1, and the apparent K_m for NADPH was 0.125 and 0.200 mM for heterocysts and vegetative cells, respectively. The enzyme was found to be sensitive to Zn⁺² ions, however, preincubation with oxidized glutathione rendered its resistance to Zn⁺² inhibition. Nostoc muscorum filaments were found to contain 0.6–0.7mM glutathione, and it is suggested that glutathione reductase can regenerate reduced glutathione in both cell types. The combined activity of glutathione reductase and isocitrate dehydrogenase in heterocysts was as high as 18 nmol reduced glutathione·min^-1·mg protein^-1. A relatively high superoxide dismutase activity was found in the two cell types; 34.2 and 64.3 enzyme units·min^-1·mg protein^-1 in heterocysts and vegetative cells, respectively.We suggest that glutathione reductase plays a role in the protection mechanism which removes oxygen radicals in the N₂-fixing cyanobacterium Nostoc muscorum.Abbreviations DTNB 5-5-dithiobis-(2-nitrobenzoic acid) - EDTA ethylenediaminetetra-acetic acid - GR glutathione reductase (EC1.6.4.2) - GSH reduced glutathione - GSSG oxidized glutathione - OPT O-phtaldialdehyde - SOD superoxide dismutase (EC 1.15.1.1)     

Morphology,physiology and infectivity of twoFrankia isolates An 1 and An 2 from root nodules ofAlnus nitida

Summary Two different strains, An 1 and An 2, were obtained from root nodules ofAlnus nitida Endl., collected from one locality in the area of its natural habitat near Bahrin, District Swat, Pakistan. The light and electron microscopy of the isolates revealed the occurrence of septate and branched hyphae bearing sporangia and vesicles. The strains differed in their growth requirements, nitrogen-fixing ability and production of extracellular pigments, thus indicating the existence of more than oneFrankia strain in the same locality. In the absence of combined nitrogen in the medium strain An 1 formed vesicles and fixed N₂ (up to 200 nmol C₂H₄. mg protein^–1.h^–1), while strain An 2 under the experimental conditions formed only few vesicles and fixed N₂ at a very low rate (ca 10 nmol C₂H₄. mg protein^–1 .h^–1). The nitrogenase activity of strain An 1 was strongly affected by the O₂ concentration.Frankia An 1 and An 2 were infective and effective onA. nitida andA. glutinosa but not onDatisca cannabina andElaeagnus umbellata. Both An 1 and An 2 strains were more infective and effective onA. glutinosa thanFrankia strains AvcIl and CpI1.     

Structural and related functional changes in sarcoplasmic reticulum induced by long-chain fatty acids

The effect of palmitic and oleic acids on Ca²⁺-ATPase activity in coupled preparations of sarcoplasmic reticulum isolated from rabbit hind leg muscle have been compared with their effects on vesicles uncoupled with Ca²⁺ ionophore, A23187. Palmitate at 2 µM · mg protein^–1 has no significant effect on enzyme activity and does not uncouple catalytic activity from calcium accumulation within the vesicles. Oleic acid at 1 µM · mg protein^–1 uncouples the vesicles, whereas 2 µM · mg protein^–1 completely inhibits Ca²⁺-ATPase activity. Fluorescence anisotropy of diphenylhexatriene is not significantly altered by palmitate, but a large transient increase in motion of the probe is observed with addition of oleic acid. The effects of oleic acid on enzyme activity are not mediated via an effect on the bulk properties of the hydrophobic domain of the membrane lipids.     

Degradation of caffeine by immobilized cells of Pseudomonas putida strain C 3024

Summary A caffeine-resistant strain of Pseudomonas putida was isolated from soil and was grown with caffeine as the sole source of carbon, energy and nitrogen. Cells were immobilized in agar gel particles which were continuously supplied with a caffeine solution (0.52 g · l^–1, D=1.0 h^–1) in a homogeneously mixed aerated reaction vessel. In the presence of the ATPase inhibitor arsenate the caffeine was removed by the immobilized cells at an average rate of 0.25 mg caffeine · h^–1 · (mg cell carbon)^–1 during 6 days. Thereafter a rapid decline of activity was observed. From a similar system without arsenate supplied with a growth medium containing a limiting amount of caffeine (0.13 g · l^–1) the caffeine was almost completely oxidized by the immobilized cells. The concentration of the remaining caffeine was 1.4 mg · l^–1, which is much lower than the substrate constant for caffeine (9.7 mg · l^–1) observed with freshly harvested suspended resting cells.     

Continuous production of fructooligosaccharides from sucrose by immobilized fructosyltransferase

The productivity of the continuous production of fructooligosaccharides from sucrose was investigated by fructosyltransferase immobilized onto a high-porous ion exchange resin was optimal with 600 g sucrose/l at a flow rate of 2.7 h^–1 expressed as a superficial space velocity. When the column was operated at 50 °C, about 8% loss of the initial activity of immobilized enzyme was observed after 30 days continuous operation, achieving high productivity of 1174 g/l · h.     

Chloride transport in apical membrane vesicles from bovine tracheal epithelium: Characterization using a fluorescent indicator

Summary Cl transport in apical membrane vesicles derived from bovine tracheal epithelial cells was studied using the Cl-sensitive fluorescent indicator 6-methoxy-N-(3-sulfopropyl) quinolinium. With an inwardly directed 50 mM Cl gradient at 23°C, the initial rate of Cl entry (J _Cl) was increased significantly from 0.32±0.12 nmol · sec^–1 · mg protein^–1 (mean±sem) to 0.50±0.07 nmol · sec^–1 · mg protein^–1 when membrane potential was changed from 0 to +60 mV with K/valinomycin. At 37°C, with membrane potential clamped at 0 mV, there was a 34±7% (n=5) decrease inJ _Cl from a control value of 0.37±0.03 nmol · sec^–1 · mg protein^–1 upon addition of 0.2mm diphenylamine-2-carboxylate. The following did not alterJ _Cl significantly (J _Cl values gives as percent change from control): 50mm cis Na (–1±5%), 0.1mm furosemide (–3±4%), 0.1mm furosemide in the presence of 50mm cis Na (–5±2%), 0.1mm H₂DIDS (–18±9%), a 1.5 pH unit inwardly directed H gradient (–7±7%), and 0.1mm H₂DIDS in the presence of a 1.5 unit pH gradient (4±18%). With inward 50mm anion gradients, the initial rates of Br and I entry (J _Br andJ ₁, respectively) were not significantly different fromJ _Cl.J _Cl was a saturable function of Cl concentration with apparentK _d of 24mm and apparentV _max of 0.54 nmol · sec^–1 · mg protein^–1. Measurement of the temperature dependence ofJ _Cl yielded an activation energy of 5.0 kcal/mol (16–37°C). These results demonstrate that Cl transport in tracheal apical membrane vesicles is voltage-dependent and inhibited by diphenylamine-2-carboxylate. There is no significant contribution from the Na/K/2Cl, Na/Cl, or Cl/OH(H) transporters. The conductive pathway does not discriminate between Cl, Br, and I and is saturable. The low activation energy supports a pore-type mechanism for the conductance.     

Production of mead by immobilized cells of Hansenula anomala

Summary Mead was produced by immobilized cells of Hansenula anomala in calcium alginate gels. The immobilized cell beads of 3 mm diameter packed in column reactors of dimensions 2.2x60, 4x40 and 8x80 cm, produced mead containing maximum concentrations of ethanol and ethyl acetate of 70 g/l and 730 mg/l, respectively at a dilution rate of 0.1 h^–1. The maximum alcohol productivity achieved was 23.1 g/l·h at a dilution rate of 0.33 h^–1. With intermittent regenerations of the cells the reactor operated continuously for 110 days. This process enables the quick production of matured mead by a single culture and the elimination of the traditionally used long aging periods.     

Pyridine nucleotide-dependent ferricyanide reduction associated with isolated plasma membranes of maize (Zea mays L.) roots

Summary Plasma membranes (PM) from maize roots (Zea mays L.) were isolated by aqueous two-phase partitioning. The isolated membrane fraction showed a 4.6-fold enrichment in specific activity of the PM marker enzyme vanadate-sensitive, Mg²⁺-ATPase over a microsomal pellet collected at 50,000 × g. Activities of marker enzymes for mitochondria, endoplasmic reticulum, tonoplast, and Golgi apparatus were low or not detectable in the PM fraction. Quantitative morphometric analysis using the PM-specific silicotungstic acid stain showed the fraction to be > 92% PM vesicles. Using detergent stimulation of ATPase activity as a measure of structurally linked latency, greater than 90% of the PM vesicles were oriented with the cytoplasmic surface inside.An electron transport activity was investigated in the PM fraction. The rate of NADH oxidation in the absence of an artificial electron acceptor was < 167pkat·mg protein^–1; however, NADH catalysed the reduction of a variety of artificial electron acceptors including ferricyanide (2.6 nkat·mg protein^–1), cytochromec (0.8 nkat·mg protein^–1), a tetrazolium derivative (0.6 nkat·mg protein^–1) and dichlorophenol indophenol (0.4 nkat·mg protein^–1). While the NADH-dependent ferricyanide and dichlorophenol indophenol reductases were stimulated 6-fold by 0.025% (v/v) Triton X-100, the cytochromec and INT reductases were not greatly stimulated. Washing membranes with high salt significantly decreased the NADH-dependent, and eliminated the NADPH-dependent, ferricyanide reductase activity measured in the absence of detergent. These results suggest that NADH was oxidized on the extracytoplasmic surface of the membrane; however, a significant portion of this activity was extrinsic and may have originated from cytoplasmic contamination during isolation. The greater portion of the PM-associated NAD(P)H oxidation and/or ferricyanide reduction was catalyzed on sites not exposed to the outer surface of the membrane.Abbreviations BTP 1,3-bis[tris(hydroxymethyl)-methylamino]-propane - CHAPS 3-[(3-cholamidopropyl)dimethylammonio]-1-propane sulfonate dihydrate - cytc cytochromec - DCIP 2,6-dichlorophenol indolphenol - INT 2-(4-iodophenyl)-3-(4-nitrophenyl)-5-phenyltetrazolium chloride - kat mole·s^–1 - Mes 2-(N-morpholino)ethanesulfonic acid - MF microsomal fraction - PM plasma membrane - STA silicotungstic acid - Tris 2-amino-2-(hydroxymethyl)-1,3-propanediol The mention of vendor or product does not imply that they are endorsed or recommended by U.S. Department of Agriculture over vendors of similar products not mentioned.     

Catalytic removal of sulfide by an immobilized sulfide-oxidase bioreactor

A bioreactor packed with chitosan immobilized sulfide-oxidase from Streptomyces species LD048 was developed to treat a liquid stream of sulfide. The inoculation system was composed of glass with a 0.7 L working volume and enzyme activity of 2 mmol S g^?1 carrier. The sulfide removal efficiency was almost 100% when the volumetric loading was increased up to 3.9 mmol S L^?1 h^?1 at a space velocity of 18 h^?1. The maximal elimination capacity was 22.1 mmol S L^?1 h^?1 with a space velocity of 72 h^?1. When the aeration was increased from 0.05 to 0.1 L min^?1, the average removal efficiency improved from 81% to 94%. A removal efficiency of 90% was obtained after 15 days of operation with a load rate of 8.9 mmol S L^?1 h^?1 and a space velocity of 14.28 h^?1. An operational equation based on the ideal plug flow bioreactor and the Michaelis–Menten model predicted the performance of this bioreactor.     

Adaptation of hybridoma cells to higher ammonia concentration

Using two mouse-mouse hybridoma cell lines, the response to ammonia step and serial changes was investigated in batch and continuous cultures with serum-free medium. The inhibitory effect of ammonia on cell growth depended on the cultivation mode, and differed markedly between cell lines. The cell line, 4C10B6 producing IgG monoclonal antibody against Pseudomonas, showed a high adaptation ability to ammonia. The 4C10B6 cells could grow under ammonia concentration as high as 21 mmol/l NH₄Cl with a viability of 80% in the continuous culture with serial increase in ammonia concentration. Whereas, in the batch culture with ammonia step change the cell growth completely ceased at 12 mmol/l NH₄Cl. The other cell line, TO-405 producing IgG monoclonal antibody against hepatitis B surface antigen, could not adapt to ammonia, and the cell growth did not occur at 9 mmol/l NH₄Cl even under the ammonia serial change.List of symbols D_Feed d^-1 Dilution rate of fresh feed medium (=F_o/V) - D_Out d^-1 Dilution rate of cell suspension (=F₁/V) - F₁ ml·d^-1 Volumetric discharge rate of cell suspension - F₀ ml·d^-1 Volumetric flow rate of fresh feed medium - k_D h^-1 Specific death rate - P mmol·l^-1 Product concentration - S mmol·l^-1 Substrate concentration in culture broth - S₀ mmol·l^-1 Substrate concentration in feed medium - t d Cultivation time - V ml Working volume of reactor - X₀ cells·ml^-1 Total cell density - X_V cells·ml^-1 Viable cell density - Y_P/S mmol·mmol^-1 Yield of product from substrate - Y_X/S cells·mmol^-1 Yield of cells from substrate - mmol·cell^-1·h^-1 Specific production rate - h^-1 Specific growth rate - mmol·cell^-1·h^-1 Specific consumption rate of substrate     

Continuous degradation of phenol(s) by Pseudomonas putida P8 entrapped in polyacrylamidehydrazide

Summary The continuous degradation of phenol by immobilized cells of Pseudomonas putida P8 under different conditions was investigated. The bacterial cells were entrapped in polyacrylamidehydrazide (PAAH) and cultivated in a columnar fluidized-bed bioreactor. Working with a dilution rate of 0.067 h^-1 the phenol content in the feed was varied to find the capacity of an one-stage system with complete phenol degradation.Under sterile conditions and with phenol as the sole carbon source a degradation rate of 7.2 g·l^-1·d^-1 was reached whereas in non-sterile waste water only 3.12 g·l^-1·d^-1 were degraded. In any case the immobilized cells showed a stable phenol degradation activity and even simultaneously fed cresols or 4-chlorophenol were utilized completely.     

Microcalorimetric investigations of the metabolism of yeasts. Growth in chemostat cultures on glucose

Summary As part of a project on the production of penicillin, the penicillin production of two strains of Penicillium chrysogenum which have a different penicillin productivity was investigated in bubble column bioreactors and for comparison in stirred fermenters. The main interest of this study were the complicated interrelations between the stirrer speed, the stirrer type, the shear stress, the morphology of the mycelium and broth viscosity as well as the effect of the oxygen transfer behavior on antibiotic productivity.Stirred tank reactors with different turbine stirrers as well as with a draught tube and propeller were employed.The main variable investigated was the stirrer speed. At low stirrer speeds, gas dispersion is inadequate and the insufficient oxygen transfer rate is a limiting factor. At higher stirrer speeds, the oxygen supply of pulpy mycelia is improved and more cell mass is formed. This result is the same for both strains in all three reactors.If the oxygen partial pressure is near the lower cirtical value, a high percentage of the carbon source is converted into penicillin but the penicillin productivity is low due to a low percentage of penicillin producing cells. At oxygen partial pressures just above 8% saturation, the absolute penicillin productivity is maximal. At higher stirrer speeds and dissolved oxygen concentrations the penicillin production phase is shorter, cell growth is higher and a higher percentage of the carbon source is converted into CO₂.In reactors with a draught tube and propeller, a lower productivity is attained than in those with turbine stirrers.The behavior of the two strains is fairly similar. The higher producing strain, however, has a more distinct separation between its periods of growth and production than does the low producing one. At high stirrer speeds the increase in the cell growth rate is less significant and the substrate yield coefficients are higher for the high producing strain than for the low producing one.Symbols C Dissolved oxygen concentration (mg l^–1) - C^* C at saturation (mg l^–1) - k_La Volumetric mass transfer coefficient (h^–1) - OTR Oxygen transfer rate (mg l^–1 h^–1) - OUR Oxygen uptake rate (mg l^–1 h^–1) - rpm Impeller speed (min^–1) - X (Dry) biomass concentration (g kg^–1) - V_g Volumetric gas flow rate (Nl min^–1) - CMC Carboxymethyl cellulose     

Batch and continuous ribonuclease production by immobilized Aspergillus clavatus cells in a bubble-collumn bioreactor

Summary Ribonuclease production using immobilized cells (IC) of Aspergillus clavatus has been studied under batch, repeated-batch and continuous fermentation conditions in a bubble-column bioreactor and compared with production by free cells, Immobilization was achieved by the method of cryostructurization in polyvinyl alcohol beads. The effect of various aeration rates in a column bioreactor has been investigated. Enzyme production by IC [42 000 units (U)·l^–1] during batch fermentations was comparable to that of a free-cell system. The specific productivity of IC was 8.5 times higher than that of free cells. In repeated batch fermentation at various aeration rates, successful reuse of IC was obtained, with comparable levels of enzyme production. Continuous ribonuclease production was achieved for 44 days at 1 vvm aeration and a dilution rate of 0.0 h^–1 with volumetric productivity (450 U·1^–1) and yield.     

Differential protein synthesis in response to sulphate and phosphate deprivation: Identification of possible components of plasma-membrane transport systems in cultured tomato roots

Isolated roots of Lycopersicon esculentum Mill., cultured in axenic conditions were starved of sulphate or phosphate, and uptake capacities for the respective oxyanion-transport systems were observed for several days after sulphate or phosphate withdrawal. Sulphate-uptake capacity of the intact roots, measured in a 20-min period, increased from a control level of 100 nmol · g^–1 · h^–1 to 1100 nmol · g^–1 · h^–1 in 10 d, and phosphate-uptake capacity increased from 500 to 1400 nmol · g^–1 · h^–1 over 4 d. Newly synthesised polypeptides of these root cultures were pulse-labelled in vivo for 2 h, by adding [³H]leucine to the culture medium. The tissue was immediately homogenised and soluble and membrane fractions were prepared. A highly purified plasma-membrane fraction was separated from the crude microsomal membrane fraction using an aqueous two-phase partitioning technique. All fractions were analysed by sodium dodecyl sulphate-polyacrylamide gel electrophoresis and autoradiography. A 28-kilodalton (kDa) soluble polypeptide, and 36-, 43-, and 47-kDa plasma-membrane polypeptides were observed to have increased labelling after 4 d of sulphate deprivation. Longer periods resulted in additional polypeptides with increased [³H]leucine incorporation. The synthesis of a 25-kDa membrane polypeptide and a 65-kDa soluble polypeptide was increased after 4 d of phosphate deprivation. Two-dimensional electrophoresis afforded greater resolution of the plasmamembrane polypeptides, confirming increased synthesis of the 36-kDa polypeptide and the presence of the 28-kDa polypeptide in the plasma-membrane preparation from sulphate-starved roots. These polypeptides were also observed in protein-stained two-dimensional gels as low-abundant protein components of the plasmamembrane fraction. It is suggested that the 36-kDa polypeptide may be a component of the plasma-membrane sulphate-transport system and that the 25-kDa polypeptide may be a component of a phosphate-transport system.Abbreviations kDa kilodalton(s) - PAGE polyacrylamide gel electrophoresis - pI isoelectric point - SDS Sodium dodecyl sulphate This work was supported by the Agricultural and Food Research Council via grants-in-aid to Long Ashton Research Station. We are also grateful for discussions with our colleagues D.T. Clarkson (LARS) and J.-C. Davidian (ENSA/INRA, Montpellier).     

Production of sorbitol and gluconic acid by permeabilized cells of Zymomonas mobilis

Summary Zymomonas mobilis is able to convert glucose and fructose to gluconic acid and sorbitol. The enzyme, glucose-fructose oxidoreductase, catalysing the intermolecular oxidation-reduction of glucose and fructose to gluconolactone and sorbitol, was formed in high amounts [1.4 units (U)·mg^-1] when Z. mobilis was grown in chemostats with glucose as the only carbon source under non-carbon-limiting conditions. The activity of a gluconolactone-hydrolysing lactonase was constant at 0.2 U·mg^-1. Using glucose-grown cells for the conversion of equimolar fructose and glucose mixtures up to 60% (w/v), a maximum product concentration of only 240 g·1^-1 of sorbitol was found. The gluconic acid accumulated was further metabolized to ethanol. After permeabilizing the cells using cationic detergents, maximum sorbitol and gluconic acid concentrations of 295 g·1^-1 each were reached; no ethanol production occurred. In a continuous process with -carrageenan-immobilized and polyethylenimin-hardened, permeabilized cells no significant decrease in the conversion yield was observed after 75 days. The specific production rates for a high yield conversion ( > 98%) in a continuous two-stage process were 0.19 g·g^-1·h^-1 for sorbitol and 0.21 g·g^-1·h^-1 for gluconic acid, respectively. For the sugar conversion of cetyltrimethylammonium bromide-treated -carrageenan-immobilized cells a V _max of 1.7 g·g^-1·h^-1 for sorbitol production and a K _m of 77.2 g·1^-1 were determinedOffprint requests to: B. Rehr