Development of reactor model for glucose isomerization catalyzed by whole-cell immobilized glucose isomerase

Based on the kinetic constants determined and the mathematical model of the reactor system developed, the performance of axial flow packed bed continuous enzyme reactor system was studied experimentally and also simulated with the aid of a computer for ultimate objective of optimization of the glucose isomerase reactor system.A reactor model was established analogous to heterogeneous catalytic reactor model taking into account the effect of fluid mass transfer and reversible kinetics. The investigated catalyst system consists of immobilized Streptomyces bambergiensis cells containing the enzyme glucose isomerase, which catalyzes the isomerization of glucose to fructose.List of Symbols A ₀, A ₁, A ₂ parameters in axial dispersion reactor model - c _go, c_g, c_gemol m^–3 glucose concentration at time t=0, at any time and at equilibrium conditions - c _gsmol m^–3 glucose concentration at particle surface - C dimensionless glucose concentration - d _pm particle diameter - d _rm diameter of reactor tube - Da Damkohler number - D _eff m² s^–1 effective glucose diffusion coefficient in Ca-alginate gel beads - k _fm s^–1 film transfer coefficient - K _e equilibrium constant - K _mg, K_mfmol m^–3 Michaelis-Menten constant for glucose and fructose, respectively - K _mmol m^–3 modified Michaelis-Menten constant - K dimensionless parameter - K ^* dimensionless parameter - L m length of reactor tube - Pe Peclet number - Pe _p particle Peclet number - Q m³ s^–1 volumetric flow rate - (-r _g) mol m^–3 s^–1 reaction rate - Re _p Reynolds particle number - Sc Schmidt number - Sh Sherwood number - t s time - v ₀ m s^–1 linear superficial fluid velocity - V _mg, V_mfmol g^–1 s^–1 maximal reaction rate for glucose and fructose, respectively - V _mmol m^–3 s^–1 modified maximal reaction rate for glucose - V _mg ^x mol m^–2 s^–1 maximal reaction rate for glucose - X _g, X_ge glucose conversion and glucose conversion at equilibrium conditions - X normalized conversion - Y dimensionless glucose concentration - void fraction of fixed bed - effectiveness factor of biocatalyst - Pa s kinematic viscosity of substrate - ₁ s first absolute weighted moment - ₂ s² second central weighted moment - _gkg m^–3 substrate density - _pkg m^–3 particle density - ² dimensionless variance of RTD curve - s residence time     

Redirection of biochemical pathways for the enhancement of H2 production by Enterobacter cloacae

Improvement in H₂ production was achieved through redirection of metabolic pathways by blocking formation of alcohol and some organic acids in Enterobacter cloacae IIT-BT 08. The wild type strain was more susceptible to allyl alcohol (7 mM) and to the combined effect of NaBr and NaBrO₃ (40 mM each at pH 5.5) than were double mutants, with defects in both alcohol and organic acid formation pathways, which had higher H₂ yields (3.4 mol mol^–1 glucose) than the wild type strain (2.1 mol mol^–1 glucose).     

The effect of<Emphasis Type="Italic"> pfl</Emphasis> gene knockout on the metabolism for optically pure <Emphasis Type="SmallCaps">d</Emphasis>-lactate production by<Emphasis Type="Italic"> Escherichia coli</Emphasis>

The effect of gene knockout on metabolism in the pflA^–, pflB^–, pflC^–, and pflD^– mutants of Escherichia coli was investigated. Batch cultivations of the pfl ^– mutants and their parent strain were conducted using glucose as a carbon source. It was found that pflA^– and pflB^– mutants, but not pflC^– and pflD^– mutants, produced large amounts of d-lactate from glucose under the microaerobic condition, and the maximum yield was 73%. In order to investigate the metabolic regulation mechanism, we measured enzyme activities for the following eight enzymes: glucose 6-phosphate dehydrogenase, 6-phosphogluconate dehydrogenase, glyceraldehyde 3-phosphate dehydrogenase (GAPDH), pyruvate kinase, lactate dehydrogenase (LDH), phosphoenolpyruvate carboxylase, acetate kinase, and alcohol dehydrogenase. Intracellular metabolite concentrations of glucose 6-phosphate, fructose 1,6-bisphosphate, phosphoenolpyruvate, pyruvate, acetyl coenzyme A as well as ATP, ADP, AMP, NADH, and NAD⁺ were also measured. It was shown that the GAPDH and LDH activities were considerably higher in pflA^– and pflB^– mutants, which implies coupling between NADH production and consumption between the two corresponding reactions. The urgent energy requirement was shown by the lower ATP/AMP level due to both oxygen limitation and pfl gene knockout, which promoted significant stepping-up of glycolysis when using glucose as a carbon source. It was shown that the demand for energy is more important than intracellular redox balance, thus excess NADH produced through GAPDH resulted in a significantly higher intracellular NADH/NAD⁺ ratio in pfl ^– mutants. Consequently, the homolactate production was achieved to meet the requirements of the redox balance and the energy production through glycolysis. The effect of using different carbon sources such as gluconate, pyruvate, fructose, and glycerol was investigated.     

MSX-resistant mutants of Anabaena 7120 with derepressed heterocyst development and nitrogen fixation

To investigate the role of ammonium-assimilating enzyme in heterocyst differentiation, pattern formation and nitrogen fixation, MSX-resistant and GS-impaired mutants of Anabaena 7120 were isolated using transposon (Tn5-1063) mutagenesis. Mutant Gs1 and Gs2 (impaired in GS activity) exhibited a similar rate of nitrogenase activity compared to that of the wild type under dinitrogen aerobic conditions in the presence and absence of MSX. Filaments of Gs1 and Gs2 produced heterocysts with an evenly spaced pattern in N₂-grown conditions, while addition of MSX altered the interheterocyst spacing pattern in wild type as well as in mutant strains. The wild type showed complete repression of heterocyst development and nitrogen fixation in the presence of NO₃ ^– or NH₄ ⁺, whereas the mutants Gs1 and Gs2 formed heterocysts and fixed nitrogen in the presence of NO₃ ^– and NH₄ ⁺. Addition of MSX caused complete inhibition of glutamine synthetase activity in wild type but Gs1 and Gs2 remained unaffected. These results suggest that glutamine but not ammonium is directly involved in regulation of heterocyst differentiation, interheterocyst spacing pattern and nitrogen fixation in Anabaena.     

Improvement of a mammalian cell culture process by adaptive,model-based dialysis fed-batch cultivation and suppression of apoptosis

Both conventional and genetic engineering techniques can significantly improve the performance of animal cell cultures for the large-scale production of pharmaceutical products. In this paper, the effect of such techniques on cell yield and antibody production of two NS0 cell lines is presented. On the one hand, the effect of fed-batch cultivation using dialysis is compared to cultivation without dialysis. Maximum cell density could be increased by a factor of ~5–7 by dialysis fed-batch cultivation. On the other hand, suppression of apoptosis in the NS0 cell line 6A1 bcl-2 resulted in a prolonged growth phase and a higher viability and maximum cell density in fed-batch cultivation in contrast to the control cell line 6A1 (100)3. These factors resulted in more product formation (by a factor ~2). Finally, the adaptive model-based OLFO controller, developed as a general tool for cell culture fed-batch processes, was able to control the fed-batch and dialysis fed-batch cultivations of both cell lines.Abbreviations A membrane area (dm²) - c _Glc,F glucose concentration in nutrient feed (mmol L^–1) - c _Glc,FD glucose concentration in dialysis feed (mmol L^–1) - c _Glc,i glucose concentration in inner reactor chamber (mmol L^–1) - c _Glc,o glucose concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _Lac,FD lactate concentration in dialysis feed (mmol L^–1) - c _Lac,i lactate concentration in inner reactor chamber (mmol L^–1) - c _Lac,o lactate concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _LS,FD limiting substrate concentration in dialysis feed (mmol L^–1) - c _LS,i limiting substrate concentration in inner reactor chamber (mmol L^–1) - c _LS,o limiting substrate concentration in outer reactor chamber (dialysis chamber) (mmol L^–1) - c _Mab monoclonal antibody concentration (mg L^–1) - F _D feed rate of dialysis feed (L h^–1) - F _Glc feed rate of nutrient concentrate feed (L h^–1) - K _d maximum death constant (h^–1) - k _d,LS death rate constant for limiting substrate (mmol L^–1) - k _Glc monod kinetic constant for glucose uptake (mmol L^–1) - k _Lac monod kinetic constant for lactate uptake (mmol L^–1) - k _LS monod kinetic constant for limiting substrate uptake (mmol L^–1) - K _Lys cell lysis constant (h^–1) - K _S,Glc monod kinetic constant for glucose (mmol L^–1) - K _S,LS monod kinetic constant for limiting substrate (mmol L^–1) - µ cell-specific growth rate (h^–1) - µ _d cell-specific death rate (h^–1) - µ _d,min minimum cell-specific death rate (h^–1) - µ _max maximum cell-specific growth rate (h^–1) - P _Glc membrane permeation coefficient for glucose (dm h^–1) - P _Lac membrane permeation coefficient for lactate (dm h^–1) - P _LS membrane permeation coefficient for limiting substrate (dm h^–1) - q _Glc cell-specific glucose uptake rate (mmol cell^–1 h^–1) - q _Glc,max maximum cell-specific glucose uptake rate (mmol cell^–1 h^–1) - q _Lac cell-specific lactate uptake/production rate (mmol cell^–1 h^–1) - q _Lac,max maximum cell-specific lactate uptake rate (mmol cell^–1 h^–1) - q _LS cell-specific limiting substrate uptake rate (mmol cell^–1 h^–1) - q _LS,max maximum cell-specific limiting substrate uptake rate (mmol cell ^–1 h^–1) - q _Mab cell-specific antibody production rate (mg cell^–1 h^–1) - q _MAb,max maximum cell-specific antibody production rate (mg cell^–1 h^–1) - t time (h) - V _i volume of inner reactor chamber (culture chamber) (L) - V _o volume of outer reactor chamber (dialysis chamber) (L) - X _t total cell concentration (cells L^–1) - X viable cell concentration (cells L^–1) - Y _Lac/Glc kinetic production constant (stoichiometric ratio of lactate production and glucose uptake) (–)     

Clostridium acetobutylicum mutants isolated for resistance to the pyruvate halogen analogs

Pyruvate halogen analogs, 3-fluoropyruvate and 3-bromopyruvate, are toxic towardClostridium acetobutylicum. After mutagenesis with nitrosoguanidine, mutants resistant to these compounds were selected. In a normal batch culture regulated at pH 4.8, mutants quickly initiated the acid-solvent transition, accumulating more acetoin and lactate than the wild type strain. The maximum rate of specific glucose uptake was higher in the mutants than in the wild type: 1.76 h^–1 and 0.9 h^–1 respectively. When the pH was uncontrolled, mutants converted glucose into solvents, essentially butanol, while the wild-type strain ceased its fermentation at the acidogenic stage. Enzymatic investigations revealed that acetate kinase, butyrate kinase, and acetoacetate decarboxylase activities decreased sooner in the mutants than in the parent strain.     

Amiloride sensitivity of proton-conductive pathways in gastric and intestinal apical membrane vesicles

Summary Passive proton permeability of gastrointestinal apical membrane vesicles was determined. The nature of the pathways for proton permeation was investigated using amiloride. The rate of proton permeation (k _H ⁺ was determined by addition of vesicles (pH _i = 6.5) to a pH 8.0 solution containing acridine orange. The rate of recovery of acridine orange fluorescence after quenching by the acidic vesicles ranged from 4 × 10^–3 (gastric parietal cell stimulation-associated vesicles; SAV) and 5 × 10^–3 (duodenal brush-border membrane vesicles; dBBMV) to 11 × 10+^–3 sec^–1 (ileal BBMV; iBBMV). Amiloride, 0.03 and 0.1 mm, significantly reduced the rate of proton permeation in dBBMV and iBBMV, but not gastric SAV. The decreases in k _H ⁺ were proportionately greater in iBBMV as compared with dBBMV. The presence of Na⁺/H⁺ exchange was demonstrated in both dBBMV and iBBMV by proton-driven (pH _i < pH _o ) ²²Na⁺ uptake. Evidence was also sought for the conductive nature of pathways for proton permeation. Intravesicular acidification, again determined by quenching of acridine orange fluorescence, was observed during imposition of K⁺-diffusion potential ([K⁺] _i [K⁺ _o ). In dBBMV and iBBMV, intravesicular acidification was enhanced in the presence of the K⁺-ionophore valinomycin, indicating that the native K⁺ permeability is rate limiting. In the presence of valinomycin, the K⁺-diffusion potential drove BBMV intravesicular acidification to levels close to the electrochemical potential. In gastric SAV, acidification was not limited by the K⁺ permeability. Valinomycin was without effect, but the K⁺/H⁺ ionophore nigericin enhanced acidification in gastric SAV, illustrating the low proton permeability of these membranes. Amiloride, 0.03–1 mm, resulted in concentration-dependent reductions of K⁺-diffusion potential-driven acidification in dBBMV and iBBMV but not in gastric SAV. These data demonstrate that proton permeation in the three membrane types is rheogenic. The sensitivity of the proton-conductive pathways in intestinal BBMV to high concentrations of amiloride correlated with the presence of the Na⁺/H⁺ antiport and indicates that this transmembrane protein may represent a pathway for proton permeation.We thank Ruth Briggs for assistance with the Na/H exchange experiments. This work was supported by a grant from the Medical Research Council (G8418056CA).     

Modeling of the pyruvate production with<Emphasis Type="Italic"> Escherichia coli</Emphasis> in a fed-batch bioreactor

A family of 10 competing, unstructured models has been developed to model cell growth, substrate consumption, and product formation of the pyruvate producing strain Escherichia coli YYC202 ldhA::Kan strain used in fed-batch processes. The strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate (using glucose as the carbon source) resulting in an acetate auxotrophy during growth in glucose minimal medium. Parameter estimation was carried out using data from fed-batch fermentation performed at constant glucose feed rates of q_VG=10 mL h^–1. Acetate was fed according to the previously developed feeding strategy. While the model identification was realized by least-square fit, the model discrimination was based on the model selection criterion (MSC). The validation of model parameters was performed applying data from two different fed-batch experiments with glucose feed rate q_VG=20 and 30 mL h^–1, respectively. Consequently, the most suitable model was identified that reflected the pyruvate and biomass curves adequately by considering a pyruvate inhibited growth (Jerusalimsky approach) and pyruvate inhibited product formation (described by modified Luedeking–Piret/Levenspiel term).List of symbols c_A acetate concentration (g L^–1) - c_A,0 acetate concentration in the feed (g L^–1) - c_G glucose concentration (g L^–1) - c_G,0 glucose concentration in the feed (g L^–1) - c_P pyruvate concentration (g L^–1) - c_P,max critical pyruvate concentration above which reaction cannot proceed (g L^–1) - c_X biomass concentration (g L^–1) - K_I inhibition constant for pyruvate production (g L^–1) - K_I^A inhibition constant for biomass growth on acetate (g L^–1) - K_P saturation constant for pyruvate production (g L^–1) - K_P inhibition constant of Jerusalimsky (g L^–1) - K_S^A Monod growth constant for acetate (g L^–1) - K_S^G Monod growth constant for glucose (g L^–1) - m_A maintenance coefficient for growth on acetate (g g^–1 h^–1) - m_G maintenance coefficient for growth on glucose (g g^–1 h^–1) - n constant of extended Monod kinetics (Levenspiel) (–) - q_V volumetric flow rate (L h^–1) - q_VA volumetric flow rate of acetate (L h^–1) - q_VG volumetric flow rate of glucose (L h^–1) - r_A specific rate of acetate consumption (g g^–1 h^–1) - r_G specific rate of glucose consumption (g g^–1 h^–1) - r_P specific rate of pyruvate production (g g^–1 h^–1) - r_P,max maximum specific rate of pyruvate production (g g^–1 h^–1) - t time (h) - V reaction (broth) volume (L) - Y_P/G yield coefficient pyruvate from glucose (g g^–1) - Y_X/A yield coefficient biomass from acetate (g g^–1) - Y_X/A,max maximum yield coefficient biomass from acetate (g g^–1) - Y_X/G yield coefficient biomass from glucose (g g^–1) - Y_X/G,max maximum yield coefficient biomass from glucose (g g^–1) - growth associated product formation coefficient (g g^–1) - non-growth associated product formation coefficient (g g^–1 h^–1) - specific growth rate (h^–1) - _max maximum specific growth rate (h^–1)     

The distribution of carbonic anhydrase type I and II isozymes in lamprey and trout: possible co-evolution with erythrocyte chloride/bicarbonate exchange

The subcellular distribution and kinetic properties of carbonic anhydrase were examined in red blood cells and gills of the lamprey, Petromyzon marinus, a primitive agnathan, and rainbow trout, Oncorhynchus mykiss, a modern teleost, in relation to the evolution of rapid Cl^–/HCO ₃ ^– exchange in the membrane of red blood cells. In the lamprey, which either lacks or has minimal red cell Cl^–/HCO ₃ ^– exchange, there has been no compensatory incorporation of carbonic anhydrase into the membrane fraction of either the red cell or the gill. Carbonic anhydrase activity in red cells is exclusively cytoplasmic, and the single isozyme displays kinetic properties typical of the type I, slow turnover, isozyme. In the red blood cells of the trout, however, which possess high amounts of the band-3 Cl^–/HCO ₃ ^– exchange protein, the single carbonic anhydrase isozyme appears to be kinetically similar to the type II, fast turnover, isozyme. It thus appears that the type I isozyme present in the red blood cells of primitive aquatic vertebrates was replaced in modern teleosts by the kinetically more efficient type II isozyme only after the incorporation and expression of a significant amount of the band-3 exchange protein in the membrane of the red cell.Abbreviations BCIP 5-bromo-4-chloro-3-indolyl phosphate - CA carbonic anhydrase - DTT dithiothreitol - EDTA ethylenediaminetetra-acetate - E ₀ total concentration of free enzyme - i fractional inhibition of enzyme activity - IU international units - K ₁ inhibition constant - K _M Michaelis constant - NBT nitro blue tetrazolium - NCP nitrocellulose paper - RBC red blood cell - SDS-PAGE sodium dodecyl sulphate polyacrylamide gel electrophoresis - V _max maximal velocity of reaction     

Alteration of coenzyme specificity in halophilic NAD(P) glucose dehydrogenase by site-directed mutagenesis

Structural analysis of glucose dehydrogenase from Haloferax mediterranei revealed that the adenosine 2′-phosphate of NADP⁺ was stabilized by the side chains of Arg207 and Arg208. To investigate the structural determinants for coenzyme specificity, several mutants involving residues Gly206, Arg207 and Arg208 were engineered and kinetically characterized. The single mutants G206D and R207I were less efficient with NADP⁺ than the wild type, and the double and triple mutants G206D/R207I and G206D/R207I/R208N showed no activity with NADP⁺.In the single mutant G206D, the relation k_cat/K_NAD⁺ was 1.6 times higher than in the wild type, resulting in an enzyme that preferred NAD⁺ over NADP⁺. The single mutation was sufficient to modify coenzyme specificity, whereas other dehydrogenases usually required more than one or two mutations to change coenzyme specificity. However, the highest reaction rates were reached with the double mutant G206D/R207I and with coenzyme NAD⁺, where the k_cat was 1.6 times higher than the k_cat of the wild-type enzyme with NADP⁺. However, catalytic efficiency with NAD⁺ was lower, as the K_m value for coenzyme was 77 times higher than the wild type with NADP⁺.     

Some properties of carbohydrate and C4-dicarboxylic acid utilization negative mutants ofRhizobium leguminosarum biovarphaseoli strain P121

After NTG treatment of the very effective wild type strain P121 ofRhizobium leguminosarum biovarphaseoli, mutants defective in the utilization of sugars or organic acids were obtained. All the mutants nodulated the cultivar Goldie ofPhaseolus vulgaris. The arabinose, fructose, glucose and pyruvate utilization mutants formed nodules similar in shape and size to the nodules formed by the wild type strain. These mutants exhibited an acetylene reduction activity significantly lower than the activity observed with the wild type strain. All the C₄-dicarboxylic acid utilization mutatns, formed ineffective nodules that did not show a significant acetylene reduction activity. The C₄-dicarboxylic acids uptake system is apparently inducible in the free-living bacteria of strain P121. When P121 cells were grown on glucose in the presence of 2.5 mM malate, the rate of glucose-dependent O₂ consumption significantly decreased suggesting the presence of a catabolite repression-like phenomenon. Isolated bacteroids of strain P121, under the experimental conditions used, were able to oxidize succinate, fumarate or malate but did not oxidize pyruvate, glucose, fructose or sucrose.     

Inhibition of glucose phosphate isomerase by metabolic intermediates of fructose

1. Purified rabbit-muscle and -liver glucose phosphate isomerase, free of contaminating enzyme activities that could interfere with the assay procedures, were tested for inhibition by fructose, fructose 1-phosphate and fructose 1,6-diphosphate. 2. Fructose 1-phosphate and fructose 1,6-diphosphate are both competitive with fructose 6-phosphate in the enzymic reaction, the apparent K_i values being 1·37×10⁻³−1·67×10⁻³m for fructose 1-phosphate and 7·2×10⁻³−7·9×10⁻³m for fructose 1,6-diphosphate; fructose and inorganic phosphate were without effect. 3. The apparent K_m values for both liver and muscle enzymes at pH7·4 and 30° were 1·11×10⁻⁴−1·29×10⁻⁴m for fructose 6-phosphate, determined under the conditions in this paper. 4. In the reverse reaction, fructose, fructose 1-phosphate and fructose 1,6-diphosphate did not significantly inhibit the conversion of glucose 6-phosphate into fructose 6-phosphate. 5. The apparent K_m values for glucose 6-phosphate were in the range 5·6×10⁻⁴−8·5×10⁻⁴m. 6. The competitive inhibition of hepatic glucose phosphate isomerase by fructose 1-phosphate is discussed in relation to the mechanism of fructose-induced hypoglycaemia in hereditary fructose intolerance.     

H2-Recycling system in mungbean Rhizobium in relation to N2-fixation

Thirty isolates of mungbean Rhizobium were tested for the presence of H₂-recycling system. All the isolates were preliminary screened for detecting H₂-recycling system in free culture using triphenyltetrazolium chloride reduction as screening procedure. The isolates which reduced the dye rapidly at early stages of growth were found to recycle hydrogen both in vivo as well as in vitro. Nitrogen fixing efficiency of hydrogenase positive, hydrogenase negative isolates and Hup^– mutants was compared by green house experiments. There was 13–56% increase in dry matter and 21–46% increase in total nitrogen of the plants inoculated with H₂-recycling isolates over the plants inoculated with non-recycling isolates. There was reduction in dry matter and total nitrogen content of the plants inoculated with Hup^– mutants as compared to plants inoculated with wild type strain. The per cent decrease due to inoculation with Hup^– mutants over wild type strain was 19–22 and 20–26 of dry weight and total nitrogen in plants, respectively.Abbreviations TTC triphenyltetrazolium chloride     

Effects of fusicoccin and abscisic acid on glucose uptake into isolated beetroot protoplasts

Uptake of glucose, 3-O-methylglucose and sucrose into beetroot protoplasts is considerably stimulated by 10^–6M fusicoccin. This effect is decreased in the presence of 10mM Na⁺ or K⁺, 2 mM Mg²⁺ or Ca²⁺. Whereas fusicoccin causes no change in the pH-optimum of the sugar uptake (pH 5.0), the apparent K_m of this uptake which obeys a biphasic kinetics is decreased by the action of fusicoccin. In the protoplast suspension, fusicoccin induces an acidification which is suppressed by uncoupling agents. Correspondingly, uncouplers as well as vanadate and diethylstilbestrol markedly inhibit the effect of fusicoccin on sugar uptake. The present data support the view that glucose uptake into beetroot protoplasts depend on the proton-pumping activity of the plasmalemma-ATPase. cis–Abscisic acid diminishes significantly the fusicoccin-enhanced glucose uptake. By using a radioimmunoassay, the internal abscisic acid content of the protoplast was estimated to be in the range of 10^–6 M. Protoplasts isolated from bundle tissue contain twice as much abscisic acid as those derived from storage parenchyma. Because protoplasts from the bundle tissue were shown to take up sugars much faster than those from the storage cells, the observed effect of abscisic acid might reflect an involvement of this hormone in the regulation of carbohydrate partitioning in the beet.Abbreviations ABA cis–abscisic acid - bundle protoplast protoplasts isolated from the conducting tissue of beetroots - DES diethylstilbestrol - FC fusicoccin - 3-OMG 3-O-methylglucopyranose - PCMBS p–chloromercuribenzenesulfonic acid - storage protoplasts protoplasts isolated from storage parenchyma     

High-affinity transport and phosphorylation of 2-deoxy-D-glucose in synaptosomes

2-Deoxy-d -glucose (2 DG) entered synaptosomes (from rat brain) by a high-affinity, Na⁺-independent glucose transport system with a K_m, of 0.24 mM. 3-O-methyl-glucose, D-glucose, and phloretin were competitive inhibitors of 2-DG transport with K_i's of 7 mM, 64 μM, and 0·75 μM, respectively. Insulin was without effect. 2-DG uptake was also saturable at high substrate concentrations with an apparent low affinity K_m, of 75 mM, where the K_l, for glucose was 17.5 mM. We are not certain whether the rate-limiting step for the low-affinity uptake system is attributable to transport or phosphorylation. However, the high-affinity glucose transport system probably is a special property of neuronal cell membranes and could be useful in helping to distinguish separated neurons from glial cells.     

The production of ethanol plus fructose sweetener using fructose utilization negative mutants of Zymomonas mobilis

Summary Two mutants, unable to utilize fructose (Fru^–) as a sole source of carbon and energy, were isolated fromZymomonas mobilis following ethyl methane sulfonate (EMS) mutagenesis. The frequency of stable Fru^– mutants among survivors of mutagenesis was 1 in 10⁴. The two Fru^– mutants were able to cleave sucrose to glucose and fructose, and then ferment only the glucose to ethanol while accumulating fructose close to the theoretical value. Under controlled fermentation conditions, sucrose was converted to ethanol plus 80% or higher purity fructose syrup in a single-stage batch fermentation process, improving the Sucrotech Process significantly.     

Electrogenic and diffusive components of the membrane ofHydrodictyon africanum

Summary In cells of the freshwater algaHydrodictyon africanum, in solutions where [K⁺]₀=0.1mm and pH₀>7.0, the membrane in the light is hyperpolarized. The membrane potential difference {ie179-1} has values from –180 to –275 mV, more negative than any ion diffusion potential difference, and is predominantly a function of pH₀, and independent of [K⁺]₀. The hyperpolarization of the membrane appears to arise from an electrogenic efflux of H⁺, estimated from voltage-clamp data to be about 8 nmol m^–2 sec^–1 when pH₀=8.5. In the light the membrane conductanceg _m is about 0.084 S m^–2. At light-off, {ie179-2} becomes less negative, with a halftime for change of 15 to 30 sec andg _m decreases by about 0.052 S m^–2. After dark periods of up to 300 sec, {ie179-3} is largely independent of pH₀ for values greater than 6.0 and usually behaves as a combined K⁺ and Na⁺ diffusion potential with permeability ratioP _Na/P _K=0.05 to 0.2. The membrane potassium conductanceg _K has either a low value of 2–6×10^–2 Sm^–2, or a high value of up to 18×10^–2 S m^–2 depending on [K⁺]₀, the transition from low to high values occurring when {ie179-4} moves over a threshold value that is more negative than {ie179-5}, the electrochemical equilibrium potential for K⁺. The time for half-change of the transition is about 30 sec. The results are consistent with a model of the membrane in which the pump electromotive force and conductance are in parallel with diffusive electromotive forces and conductances. When the pump is operating its properties determine membrane properties, and when it is inoperative, or running at a diminished rate, the membrane properties are determined more by the diffusive pathways. Changes in both pump rate andg _K can account for a variety of characteristic changes in membrane PD and conductance occurring in response to ligh-dark changes, changes in light intensity, pasage of externally applied electric current across the membrane and changes in ionic constituents of the external medium.     

Response surface optimization for the continuous glucose isomerization process

Production of fructose via a continuous glucose isomerization process was optimized using response surface methodology. Glucose isomerization was performed using immobilized glucose isomerase in a flow-through tubular reactor. Process factors eg pH (7.0–7.8), temperature (50–60°C), flow rate (5–17 ml min^–1) and glucose content (30–50% w/w) of the feedstock solution were simultaneously tested according to a central composite experimental design. Measured responses such as % isomerization, and fructose yield (gh^–1) has an excellent correlation with tested factors. The highest desirability,D, (geometric mean of % isomerization and fructose yield) was obtained when the feedstock (56–60°C) had 34–36% glucose, a pH of 7.4–7.8 and was pumped at 15 ml min^–1.     

The effect of the locus pstB on phosphate binding in the phosphate specific transport (PST) system of Escherichia coli

Summary The periplasmic phosphate binding protein is a product of the phoS gene and is an essential component of the phosphate specific transport (PST) system, which mediates Pi uptake in Escherichia coli. The binding of Pi to periplasmic protein(s) and the kinetic parameters of Pi uptake were studied in phoT and pstB mutants of E. coli. These mutants are impaired in Pi uptake but have a periplasmic Pi-binding protein whose Pi-binding acpacity was estimated by the retention kinetics. The Pi-binding activity in two pstB mutants was found to be weaker as compared to phoT9 and the wild type. The K _D values for Pi binding to periplasmic protein were determined by equilibrium dialysis. In the pstB mutants the K _D value was found to be 9–31 times higher than the values obtained for the wild type and the phoT mutant. The apparent K _m values for Pi uptake in one pstB mutant is 14.3 times higher than in the wild type. V _max of the mutant is 8.3 times lower that of the wild type. The data indicate that pstB, an essential gene of the PST transport system, is promoting the binding capacity of the Pi-binding protein.Abbreviations AP alkaline phosphatase - Pi inorganic orthophosphate - Km kanamycin     

Growth rate influences reductive biodegradation of the organophosphorus pesticide demeton by Corynebacterium glutamicum

The organophosphorous pesticide, demeton-S-methyl was transformed byCorynebacterium glutamicum in co-metabolism with more readilydegradable substrates. Glucose, acetate and fructose were tested as growth substrates, and the highest demeton-S-methyl biotransformation average rate (0.78 mg l^-1 h^-1) and maximum instantaneous rate (1.4 mg l^-1 h^-1) were achieved on fructose. This higher efficiency seems to be linked to the atypical behavior of C. glutamicum grown on fructose, characterized by a prolonged period of accelerating growth instead of a constant growth rate observed on glucose or acetate. More precisely, for growth rates in the 0.1–0.4 h^-1 range, a direct coupling between the specific demeton-S-methyl consumption rate and the growth rate was demonstrated on fructose during batch –, steady state continuous – or continuous cultures with a controlled transient growth rate (accelerostat technology). The demeton-S-methyl biotransformation was more favoured during an acceleration phase of the growth rate.