On-line monitoring of the methanol concentration in Pichia pastoris cultures producing an heterologous lipase by sequential injection analysis

An automated sequential injection analysis (SIA) system using stop-flow technique was developed to determine methanol concentration by means of the enzymatic reactions of alcohol oxidase and peroxidase. Its application as an on-line device for monitoring Pichia pastoris fermentations producing an heterologous protein was demonstrated. Linear response, observed up to 2 g l^–1, was reached by including a dilution chamber in the SIA manifold. The sampling frequency was 7 analyses per hour with a relative standard deviation lower than 4%.     

A system for the on-line determination of glucose concentration

An off-line glucose analyzer, Yellow Springs Instrument (YSI) model 27 was modified and coupled to various peripheral components to produce a fast, fully automated system for the online determination of glucose concentration. The amount of time required to accomplish each measurement was in the order of two minutes. To demonstrate the utility of this system, various tests were performed. First, a stream containing known amounts of glucose was monitored on-line and the system was calibrated. The calibration curve was shown to be described by Michaelis-Menten kinetics. Once the system was properly calibrated, it was used to monitor the glucose concentration in the effluent stream of two different enzyme reactor systems. The glucose concentrations were within experimental error of those obtained via standard off-line techniques.     

On-line immunoanalysis of monoclonal antibodies during a continuous culture of hybridoma cells

The monoclonal-antibody production of an immobilized hybridoma cell line cultivated in a fluidized-bed reactor was monitored on-line for nearly 900 h. The monoclonal antibody concentration was determined by an immuno affinity-chromatography method (ABICAP). Antibodies directed against the product, e.g. IgG, were immobilized on a micro-porous gel and packed in small columns. After all IgG present in the sample was bound to the immobilized antibodies, unbound proteins were removed by rinsing the column. Elution of the bound antibodies followed and the antibodies were determined by fluorescence. The analytical procedure was automated with a robotic device to enable on-line measurements. The correlation between the on-line determined data and antibody concentrations measured by HPLC was linear. A sampling system was constructed, which was based on a pneumatically actuated in-line membrane valve integrated into the circulation loop of the reactor. Separation of the cells from the sample stream was achieved by a depth filter made of glass-fibre, situated outside the reactor. Rapid obstruction of the filter by cells or cell debris and contamination of the sample system was avoided by intermittent rinsing of the sample system with a chemical solution. The intermittent rinsing of the filter, which had a surface of 4.8 cm², resulted in an operational capacity of up to 40 samples (1.0 l total sample volume). Both the sampling system and the analytical device functioned without failure during this long-term culture. The culture temperature was varied between 34 and 40 °C. Raising the temperature from 34 up to 37 °C resulted in a simultaneous increase of growth and specific antibody production rate. Specific metabolic rates of glucose, lactate, glutamine and ammonium stayed constant in this temperature range. A further enhancement of temperature up to 40 °C had a negative effect on the growth rate, whereas the specific monoclonal antibody production rate showed a small increase. The other specific metabolic rates also increased in the temperature range between 38 to 40 °C. This revised version was published online in July 2006 with corrections to the Cover Date.     

Purification and Characterization of Trehalose Phosphorylase from Micrococcus varians

Trehalose phosphorylase (EC 2.4.1.64), which catalyzes the reversible reaction of phosphorolysis and synthesis of trehalose, was purified to homogeneity from a cell-free extract of Micrococcus varians strain No. 39. The enzyme was shown to have a molecular weight of 570,000 to 580,000 by gel filtration, and to have a subunit of molecular weight of 105,000 by SDS–polyacrylamide gel electrophoresis. The stoichiometry of the reaction between trehalose, Pi, glucose, and β-glucose 1-phosphate was 1: 1: 1: 1 (molar ratio). The enzyme had high specificity for trehalose, glucose, and β-glucose 1-phosphate. The K_ms for trehalose, Pi, glucose, and β-glucose 1-phosphate were 10, 3.1, 23, and 38mM, respectively. The k_cats were 200s^?1 for trehalose phosphorolysis and 660s^?1 for trehalose synthesis. The enzyme was inhibited by validamycin A, validoxylamine A, 1-deoxynojirimycin, and Cu^{2 +} during trehalose phosphorolysis, and by Cu^{2 +}, Zn^{2 +}, and Ni^{2 +} during trehalose synthesis. Inhibition competitive against trehalose was noted with validamycin A, validoxylamide A, and 1-deoxynojirimycin. Initial velocity, product inhibition, and dead-end inhibition studies suggested that both trehalose phosphorolysis and trehalose synthesis proceeded through an ordered Bi Bi mechanism.     

An automated flow injection analysis system for on-line monitoring of glucose and L-lactate during lactic acid fermentation in a recycle bioreactor

The study concerns on-line sequential analysis of glucose and L-lactate during lactic acid fermentation using a flow injection analysis (FIA) system. Enzyme electrodes containing immobilized glucose oxidase and L-lactate oxidase were used with an amperometric detection system. A 12-bit data acquisition card with 16 analog input channels and 8 digital output channels was used. The software for data acquisition was developed using Visual C++, and was devised for sampling every hour for sequential analyses of lactate and glucose. The detection range was found to be 2–100 g l^–1 for glucose and 1–60 g l^–1 for L-lactate using the biosensors. This FIA system was used for monitoring glucose utilization and L-lactate production by immobilized cells of Lactobacillus casei subsp. rhamnosus during a lactic acid fermentation process in a recycle batch reactor. After 13 h of fermentation, complete sugar utilization and maximal L-lactate production was observed. A good agreement was observed between analysis data obtained using the biosensors and data from standard analyses of reducing sugar and L-lactate. The biosensors exhibited excellent stability during continuous operation for at least 45 days.     

Immobilized antibody-based flow type enzyme immunosensor for determination of human serum albumin

A flow-type enzyme immunosensor was prepared for the electrochemical determination of human serum albumin (HSA). The immunosensor was constructed from the immobilized antibody (anti-HSA IgG) reactor and an oxygen electrode. The immunochemical reaction of catalase-labelled antibody with HSA was completed with 30 min. After the immunochemical reaction, hydrogen peroxide solution was injected into the system and a peak current was obtained within 2 min. A linear relationship was observed between the current increase and the logarithm of HSA concentration in the range 10⁻⁸-10⁻⁶ g ml⁻¹. The minimum measurable concentration was 10⁻⁸ g ml⁻¹. The current increase was reproducible with 10% of the relative errors when a sample solution containing 10⁻⁷ g ml⁻¹ of HSA was used. The minimum measurable concentration increased to 10⁻⁹ g ml⁻¹ when hydrogen peroxide was recycled for 5 min in the reactor system. The immobilized antibody reactor could be reused. HSA in human serum was determined by the system proposed.     

On-line biomass monitoring in bench-scale stirred bioreactors using parts of a liquid chromatography system

A cell density monitor, comprising parts of a liquid chromatography system, was adapted for on-line real-time measurement of bacterial cell density up to 75 g l^–1. The device dilutes the sample containing cells and measures the absorbancy at 280 nm. This detector gives an excellent correlation with off-line measurements, good reproducibility, a low limit of detection (3.5 mg l^–1), and becomes a low cost alternative for fermentation monitoring in small stirred bioreactors.     

Production of acetone and butanol by Clostridium acetobutylicum in continuous culture with cell recycle

Summary To increase the solvent productivity of the acetone-butanol fermentation, a continuous culture of Clostridium acetobytylicum with cell recycling was used. At a dry cell mass concentration of 8 g l^-1 and a dilution rate of D=0.64 h^-1, a solvent productivity of 5.4 g l^-1 h^-1 was attained. To prevent degeneration of the culture, which occurs with high concentrations of solvents (acetone, butanol and ethanol), different reactor cascades were used. A two-stage cascade with cell recycling and turbidostatic cell concentration control turned out to be the best solution, the first stage of which was kept at relatively low cell and product concentrations. A solvent productivity of 3 and 2.3 g l^-1 h^-1, respectively, was achieved at solvent concentrations of 12 and 15 g l^-1.Symbols D Dilution rate (h^-1) - r _p solvent productivity (g l^-1 h^-1) - s residual glucose concentration (g l^-1) - V _R reactor volume (l) - V _O overall volume (l) - x (dry) cell mass concentration (g l^-1) - Y _P/S solvent yield (g g^-1)     

Trehalose absorption related with trehalase in developing ovaries of the silkworm,Bombyx mori

Summary The mechanism of trehalose absorption was examined in developing ovaries of the silkworm,Bombyx mori. Trehalose and glucose absorption followed saturation kinetics giving an apparentK _m value of 8.4 mM and a V_max of 12.5 moles/30 min per g ovaries for trehalose absorption, and an apparentK _m value of 26.4 mM and a V_max of 36.6 moles/30 min per g ovaries for glucose uptake. Trehalose absorption was clearly inhibited by addition of NaCN or NaN₃ to the incubation medium.Cellobiose, maltose, sucrose and turanose were taken up by ovaries at much lower rates than trehalose. Among the disaccharidases which hydrolyse these sugars, trehalase activity was highest. The correlation between trehalase activity and trehalose absorption rate was also demonstrated by a reduction of trehalase activity accompanied by reduced absorption rates after extirpation of the suboesophageal ganglion (SG). During trehalose absorption, glucose was released into the incubation medium, but after SG removal, no liberation of glucose was observed. Furthermore, no accumulation of¹⁴C-trehalose, added to the medium, was observed in the cells and almost all radioactivity was recovered as glucose and glycogen in the ovaries.These results suggest that in developing silkworm ovaries, trehalose is absorbed by a specific carriermediated and energy-dependent system, in which the hydrolysis by trehalase is an obligatory step.     

Trehalose phosphorylase from Pichia fermentans and its role in the metabolism of trehalose

During a screening for novel microbial trehalose phosphorylase three Pichia strains were identified as producers of this particular enzyme that have not yet been described. To our knowledge, this is the first time that this enzyme activity has been shown in yeasts. Pichia fermentans formed trehalose phosphorylase when cultivated on a growth medium containing easily metabolizable sugers such as glucose. Addition of NaCl (0.4 M) to the medium increased the synthesis of the enzyme significantly. Production of trehalose phosphorylase was found to be growth-associated with a maximum of activity formed at the transition of the exponential to the stationary phase of growth. Trehalose phosphorylase catalyzes the phosphorolytic cleavage of trehalose, yielding glucose 1-phosphate (glucose-1-P) and glucose as products. In vitro the enzyme readily catalyzes the reverse reaction, the synthesis of trehalose from glucose and glucose-1-P. For this reaction, the enzyme of P. fermentans was found to utilize -glucose-1-P preferentially. A partially purified enzyme preparation showed a pH optimum of 6.3 for the synthesis of trehalose. The enzyme was found to be rather unstable; it was easily inactivated by dilution unless Ca²⁺ or Mn²⁺ were added. This instability is presumably caused by dissociation of the enzyme. In contrast to other yeasts, P. fermentans rapidly degraded intracellularly accumulated trehalose when the carbon source in the medium was depleted. Trehalose phosphorylase seems to be a key enzyme in the degradative pathway of trehalose in P. fermentans. Additional enzymes in this catabolic pathway of trehalose include phosphoglucomutase, glucose-6-phosphate dehydrogenase, and gluconolactonase.This contribution is part of the Ph.D. thesis of Ingrid Schick     

Monitoring and control of enzymic sucrose hydrolysis using on-line biosensors

Summary Previously reported flow microcalorimeter devices for enzymic reaction heat measurement, enzyme thermistors, have here been extended with systems for on-line sample treatment. Glucose analysis was performed by intermittent flow injections of 50 l samples through such an enzyme thermistor device containing immobilized glucose oxidase and catalase. Sucroce analysis was performed by allowing diluted samples to continuously pass through an additional enzyme thermistor containing immobilized invertase. The reaction heats were recorded as temperature changes in the order of 10–50 m°C for concentrations of 0.05–0.30 M glucose or sucrose present in the original non-diluted samples.The performance of this system was investigated by its ability to follow concentration changes obtained from a gradient mixer. The system was applied to monitoring and controlling the hydrolysis of sucrose to glucose and fructose in a plug-flow reactor with immobilized invertase. The reactor was continuously fed by a flow of scurose of up to 0.3 M (100 g/l). Glucose and remaining sucrose were monitored in the effluent of the column. By using flow rate controlled feed pumps for sucrose and diluent the influent concentration of sucrose was varied while the overall flow rate remained constant.On-line control of the effluent concentration of lucose and sucrose was achieved by a proportional and integral regulator implemented on a microcomuter. Preset concentration of glucose in the effluent could be maintained over an extended period of time espite changes in the overall capacity of the invertase reactor. Long delay times in the sensor system and the enzyme column made it necessary to carefully tune the control parameters. Changes of set-point value and temperature disturbances were used to verify accuracy of controlling performance.     

Role of periplasmic trehalase in uptake of trehalose by the thermophilic bacterium Rhodothermus marinus

Trehalose uptake at 65°C in Rhodothermus marinus was characterized. The profile of trehalose uptake as a function of concentration showed two distinct types of saturation kinetics, and the analysis of the data was complicated by the activity of a periplasmic trehalase. The kinetic parameters of this enzyme determined in whole cells were as follows: K_m = 156 ± 11 μM and V_max = 21.2 ± 0.4 nmol/min/mg of total protein. Therefore, trehalose could be acted upon by this periplasmic activity, yielding glucose that subsequently entered the cell via the glucose uptake system, which was also characterized. To distinguish the several contributions in this intricate system, a mathematical model was developed that took into account the experimental kinetic parameters for trehalase, trehalose transport, glucose transport, competition data with trehalose, glucose, and palatinose, and measurements of glucose diffusion out of the periplasm. It was concluded that R. marinus has distinct transport systems for trehalose and glucose; moreover, the experimental data fit perfectly with a model considering a high-affinity, low-capacity transport system for trehalose (K_m = 0.11 ± 0.03 μM and V_max = 0.39 ± 0.02 nmol/min/mg of protein) and a glucose transporter with moderate affinity and capacity (K_m = 46 ± 3 μM and V_max = 48 ± 1 nmol/min/mg of protein). The contribution of the trehalose transporter is important only in trehalose-poor environments (trehalose concentrations up to 6 μM); at higher concentrations trehalose is assimilated primarily via trehalase and the glucose transport system. Trehalose uptake was constitutive, but the activity decreased 60% in response to osmotic stress. The nature of the trehalose transporter and the physiological relevance of these findings are discussed.     

On-line coupling of sequential injection with liquid chromatography for the automated derivatization and determination of gamma-aminobutyric acid in human biological fluids

The principle of sequential injection analysis (SIA) was exploited to develop a rapid fully automated and efficient pre-column derivatization procedure coupled on-line to liquid chromatography (HPLC). Using the SIA-HPLC derivatization protocol gamma-aminobutyric acid (GABA) was determined fluorimetrically in human biological fluids with o-phthaldialdehyde (OPA) as derivatization reagent and minimum sample pretreatment. A lab-built SIA system was used to handle samples, standard solutions and OPA reagent. Appropriate volumes of the reagents were introduced in the holding coil of the SIA system and were mixed on propulsion to the HPLC loop through a suitable reaction coil. The chemical (pH, c(OPA), c(mercaptoethanol)) and instrumental variables (volumes of sample and reagent, reaction time) of the reaction were studied and optimized in terms of maximum sensitivity. The chromatographic variables (gradient composition of the eluent and flow rate) were studied for optimum selectivity and peak characteristics. The developed experimental configuration facilitated fully-automated operation thus minimizing errors in handling. Additionally the method as a whole provided very satisfactory sensitivity, precision and accuracy. Direct determination of GABA in human urine and cerebrospinal fluid (CSF) at microg L(-1) (ppb) levels was accomplished, with minimum sample pretreatment.     

Efficient (R)-3-hydroxybutyrate production using acetyl CoA-regenerating pathway catalyzed by coenzyme A transferase

(R)-3-hydroxybutyrate [(R)-3HB] is a useful precursor in the synthesis of value-added chiral compounds such as antibiotics and vitamins. Typically, (R)-3HB has been microbially produced from sugars via modified (R)-3HB-polymer-synthesizing pathways in which acetyl CoA is converted into (R)-3-hydroxybutyryl-coenzyme A [(R)-3HB-CoA] by β-ketothiolase (PhaA) and acetoacetyl CoA reductase (PhaB). (R)-3HB-CoA is hydrolyzed into (R)-3HB by modifying enzymes or undergoes degradation of the polymerized product. In the present study, we constructed a new (R)-3HB-generating pathway from glucose by using propionyl CoA transferase (PCT). This pathway was designed to excrete (R)-3HB by means of a PCT-catalyzed reaction coupled with regeneration of acetyl CoA, the starting substance for synthesizing (R)-3HB-CoA. Considering the equilibrium reaction of PCT, the PCT-catalyzed (R)-3HB production would be expected to be facilitated by the addition of acetate since it acts as an acceptor of CoA. As expected, the engineered Escherichia coli harboring the phaAB and pct genes produced 1.0 g?L^?1 (R)-3HB from glucose, and with the addition of acetate into the medium, the concentration was increased up to 5.2 g?L^?1, with a productivity of 0.22 g?L^?1 h^?1. The effectiveness of the extracellularly added acetate was evaluated by monitoring the conversion of ¹³C carbonyl carbon-labeled acetate into (R)-3HB using gas chromatography/mass spectrometry. The enantiopurity of (R)-3HB was determined to be 99.2% using chiral liquid chromatography. These results demonstrate that the PCT pathway achieved a rapid co-conversion of glucose and acetate into (R)-3HB.     

Ethanol production by immobilized whole cells ofZymomonas mobilis in a continuous flow expanded bed bioreactor and a continuous flow stirred tank bioreactor

Continuous ethanol fermentation by immobilized whole cells ofZymomonas mobilis was investigated in an expanded bed bioreactor and in a continuous stirred tank reactor at glucose concentrations of 100, 150 and 200 g L^–1. The effect of different dilution rates on ethanol production by immobilized whole cells ofZymomonas mobilis was studied in both reactors. The maximum ethanol productivity attained was 21 g L^–1 h^–1 at a dilution rate of 0.36 h^–1 with 150 g glucose L^–1 in the continuous expanded bed bioreactor. The conversion of glucose to ethanol was independent of the glucose concentration in both reactors.     

Transport and metabolism of trehalose in Escherichia coli and Salmonella typhimurium

The metabolism of trehalose in wild type cells of Escherichia coli and Salmonella typhimurium has been investigated. Intact cells of Escherichia coli (grown on trehalose) accumulated [¹⁴C]-trehalose as [¹⁴C]-trehalose 6-phosphate. Toluene-treated cells catalyzed the synthesis of the [¹⁴C]-sugar phosphate from [¹⁴C]-trehalose and phosphoenolpyruvate; ATP did not serve as phosphoryl donor. Trehalose 6-phosphate could subsequently be hydrolyzed by trehalose 6-phosphate hydrolase, an enzyme which catalyzes the hydrolysis of the disaccharide phosphate into glucose and glucose 6-phosphate. Both Escherichia coli and Salmonella typhimurium induced this enzyme when they grew on trehalose.These findings suggest that trehalose is transported in these bacteria by an inducible phosphoenolpyruvate:trehalose phosphotransferase system.The presence of a constitutive trehalase was also detected.Abbreviations HEPES N-2-hydroxyethylpiperazine-N-2-ethanosulfonic acid - PEP phosphoenolpyruvate - PTS phosphoenolpyruvate: glycose phosphotransferase system - O.D. optical density     

Sorbitol and Gluconate Production in a Hollow Fibre Membrane Reactor by Immobilized Zymomonas Mobilis

This study describes the results of a hollow fibre membrane reactor with immobilized treated cells of Zymomonas mobilis which produced sorbitol and gluconic acid continuously from fructose and glucose respectively. A productivity of 10–20 g sorbitol · L^-1 · h^-1 and 10–20 gluconate · L^-1 · h^-1 (based on total bioreactor volume) from a feed of 100 g · L^-1 each of glucose and fructose was possible at high dilution rates. Kinetic parameters describing the reaction rate of treated cells in batch reactors were used to analyse the performance of the hollow fibre membrane reactor employing significant convective mass transfer. No significant mass transfer limitation was apparent.     

Very high ethanol productivity in an innovative continuous two-stage bioreactor with cell recycle

The performance of an innovative two-stage continuous bioreactor with cell recycle—potentially capable of giving very high ethanol productivity—was investigated. The first stage was dedicated to cell growth, whereas the second stage was dedicated to ethanol production. A high cell density was obtained by an ultrafiltration module coupled to the outlet of the second reactor. A recycle loop from the second stage to the first one was tested to improve cell viability and activity. Cultivations of Saccharomyces cerevisiae in mineral medium on glucose were performed at 30°C and pH 4. At steady state, total biomass concentrations of 59 and 157 gDCW l⁻¹ and ethanol concentrations of 31 and 65 g l⁻¹ were obtained in the first and second stage, respectively. The residual glucose concentration was 73 g l⁻¹ in the first stage and close to zero in the second stage. The present study shows that a very high ethanol productivity (up to 41 g l⁻¹ h⁻¹) can indeed be obtained with complete conversion of the glucose and with a high ethanol titre (8.3°GL) in the two-stage system.     

Effect of glucose concentration on the rate of fructose consumption in native strains isolated from the fermentation of Agave duranguensis

Studies on hexose consumption by Saccharomyces cerevisiae show that glucose is consumed faster than fructose when both are present (9:1 fructose to glucose) in the medium during the fermentation of Agave. The objective of this work was to select strains of S. cerevisiae that consume fructose equal to or faster than glucose at high fructose concentrations by analyzing the influence of different glucose concentrations on the fructose consumption rate. The optimal growth conditions were determined by a kinetics assay using high performance liquid chromatography (HPLC) using 50?g of glucose and 50?g of fructose per liter of synthetic medium containing peptone and yeast extract. Using the same substrate concentrations, strain ITD-00185 was shown to have a higher reaction rate for fructose over glucose. At 75?g of fructose and 25?g of glucose per liter, strain ITD-00185 had a productivity of 1.02 gL^?1?h^?1 after 40?h and a fructose rate constant of 0.071?h^?1. It was observed that glucose concentration positively influences fructose consumption when present in a 3:1 ratio of fructose to glucose. Therefore, adapted strains at high fructose concentrations could be used as an alternative to traditional fermentation processes.     

C Nuclear Magnetic Resonance Study of Mannitol Cycle and Trehalose Synthesis during Glucose Utilization by the Ectomycorrhizal Ascomycete Cenococcum graniforme

¹³C nuclear magnetic resonance spectroscopy has been used to follow the utilization of glucose for the synthesis of carbohydrates in the ectomycorrhizal ascomycete Cenococcum graniforme. The fate of ¹³C label was analyzed in vivo and in mycelial extracts. The major carbohydrates produced from [1-¹³C]glucose and [6-¹³C]glucose were mannitol and trehalose. Mannitol was mainly synthesized via a direct route from glucose. Scrambling of the ¹³C label was observed to occur in trehalose during glycolysis. From the analysis of the scrambling patterns, it is concluded that the mannitol cycle was operative and that a large part of the carbon of glucose was used to form trehalose after cycling through the mannitol pool. The activities of NAD-mannitol-l-P dehydrogenase (EC 1.1.1.17) and NADP-mannitol dehydrogenase (EC 1.1.1.138), which participate in the mannitol cycle relative to the activity of glycolytic enzymes, provide evidence that the cycle is important for NADPH production.