Amperometric determination of total assimilable sugars in fermentation broths with use of immobilized whole cells

A microbial sensor consisting of immobilized living whole cells of Brevibacterium lactofermentum and an oxygen electrode was prepared for continuous determination of total assimilable sugars (glucose, fructose and sucrose) in a fermentation broth for glutamic acid production. Total assimilable sugars were evaluated from oxygen consumption by the immobilized microorganisms. When a sample solution containing glucose was applied to the sensor system, increased consumption of oxygen by the microorganisms caused a decrease in the dissolved oxygen around the Teflon membrane of the oxygen electrode and the current of the electrode decreased markedly with time until steady state was reached. The response time was ≈ 10 min by the steady state method and 1 min by the pulse method. A linear relationship was found between the decrease in current and the concentration of glucose (<1 mM), fructose (<1 mM) and sucrose (<0.8 mM). The ratio of the sensitivity of the microbial sensor to glucose, fructose and sucrose was 1.00:0.80:0.92. The decrease in current was reproducible to within 2% of the relative standard deviation when a sample solution containing glucose (0.8 mM) was employed for experiments. The selectivity of the microbial sensor for assimilable sugars was satisfactory for use in the fermentation process. The additivity of the response of the microbial sensor for glucose, fructose and sucrose was examined. The difference between the observed and calculated values was within 8%. The microbial sensor was applied to a fermentation broth for glutamic acid production. Total assimilable sugars can be determined by the microbial sensor which can be used for more than 10 days and 960 assays.     

Microbial corrosion monitoring by an amperometric microbial biosensor developed using whole cell of Pseudomonas sp.

A microbial biosensor was developed for monitoring microbiologically influenced corrosion (MIC) of metallic materials in industrial systems. The Pseudomonas sp. isolated from corroded metal surface was immobilized on acetylcellulose membrane and its respiratory activity was estimated by measuring oxygen consumption. The microbial biosensor was used for the measurement of sulfuric acid in a batch culture medium contaminated by microorganisms. A linear relationship between the microbial sensor response and the concentration of sulfuric acid was observed. The response time of biosensor was 5 min and was dependent on the immobilized cell loading of Pseudomonas sp., pH, temperature and corrosive environments. The microbial biosensor response was stable, reproducible and specific for sensing of sulfur oxidizing bacterial activity.     

Microbial corrosion monitoring by an amperometric microbial biosensor developed using whole cell of Pseudomonas sp.

A microbial biosensor was developed for monitoring microbiologically influenced corrosion (MIC) of metallic materials in industrial systems. The Pseudomonas sp. isolated from corroded metal surface was immobilized on acetylcellulose membrane and its respiratory activity was estimated by measuring oxygen consumption. The microbial biosensor was used for the measurement of sulfuric acid in a batch culture medium contaminated by microorganisms. A linear relationship between the microbial sensor response and the concentration of sulfuric acid was observed. The response time of biosensor was 5 min and was dependent on the immobilized cell loading of Pseudomonas sp., pH, temperature and corrosive environments. The microbial biosensor response was stable, reproducible and specific for sensing of sulfur oxidizing bacterial activity.     

Online measurement of dissolved carbon monoxide concentrations reveals critical operating conditions in gas fermentation experiments

Syngas fermentation is one possible contributor to the reduction of greenhouse gas emissions. The conversion of industrial waste gas streams containing CO or H₂, which are usually combusted, directly reduces the emission of CO₂ into the atmosphere. Additionally, other carbon‐containing waste streams can be gasified, making them accessible for microbial conversion into platform chemicals. However, there is still a lack of detailed process understanding, as online monitoring of dissolved gas concentrations is currently not possible. Several studies have demonstrated growth inhibition of Clostridium ljungdahlii at high CO concentrations in the headspace. However, growth is not inhibited by the CO concentration in the headspace, but by the dissolved carbon monoxide tension (DCOT). The DCOT depends on the CO concentration in the headspace, CO transfer rate, and biomass concentration. Hence, the measurement of the DCOT is a superior method to investigate the toxic effects of CO on microbial fermentation. Since CO is a component of syngas, a detailed understanding is crucial. In this study, a newly developed measurement setup is presented that allows sterile online measurement of the DCOT. In an abiotic experiment, the functionality of the measurement principle was demonstrated for various CO concentrations in the gas supply (0%–40%) and various agitation rates (300–1100 min^?1). In continuous stirred tank reactor fermentation experiments, the measurement showed reliable results. The production of ethanol and 2,3‐butanediol increased with increasing DCOT. Moreover, a critical DCOT was identified, leading to the inhibition of the culture. Thus, the reported online measurement method is beneficial for process understanding. In future processes, it can be used for closed‐loop fermentation control.     

A completely noninvasive method of dissolved oxygen monitoring in disposable small‐scale cell culture vessels based on diffusion through permeable vessel walls

Disposable cell culture vessels are extensively used at small scales for process optimization and validation, but they lack monitoring capabilities. Optical sensors that can be easily adapted for use in small‐scale vessels are commercially available for pH, dissolved oxygen (DO), and dissolved carbon dioxide (DCO₂). However, their use has been limited due to the contamination and compatibility issues. We have developed a novel solution to these problems for DO monitoring. Oxygen diffusion through permeable vessel wall can be exploited for noninvasive monitoring. An optical oxygen sensor can be placed outside the oxygen permeable vessel wall thereby allowing oxygen diffusing through the vessel wall to be detected by the sensor. This way the sensor stays separate from the cell culture and there are no concerns about contaminants or leachants. Here we implement this method for two cell culture devices: polystyrene‐made T‐75 tissue culture flask and fluorinated ethylene propylene (FEP)‐made Vuelife^® cell culture bag. Additionally, mammalian and microbial cell cultures were performed in Vuelife^® cell culture bags, proving that a sensor placed outside can be used to track changes in cell cultures. This approach toward noninvasive monitoring will help in integrating cell culture vessels with sensors in a seamless manner. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:172–177, 2014     

A novel microbial sensor using luminous bacteria.

A novel microbial sensor system that uses luminous bacteria was developed for the determination of both glucose and toxic compounds. The sensor system consisted of a membrane with luminous bacteria immobilized upon it and a photomultiplier. Measurements were based on the in vivo intensity of the light emitted by the bacteria, as this is affected by their environment. A linear relationship was observed between increased luminescence and concentrations of glucose between 0.05 mM and 0.55 mM. The relative standard deviation was 10% for 0.55 mM glucose (n = 10). Toxic compounds such as benzalkonium chloride, sodium dodecyl sulphate and chromium(VI) were also detected by measuring the decrease in luminescence in their presence.     

An immersible manometric sensor for measurement of humidity and enzyme mediated changes in dissolved gas

An immersible manometric sensor was made by covering the gaseous cavity of a pressure transducer with a 1 microm controlled pore membrane. Transfer of gas across the membrane allowed the pressure transducer to record changes in humidity or dissolved gas when immersed in solution. By immersing the sensor in distilled water, atmospheric humidity could be estimated by the deficit of atmospheric vapor pressure from saturation. In another application of the sensor, CO(2) was monitored continuously. This was not possible in previous closed-reactor type manometric sensors, and may allow the new technology to be used in applications requiring continuous monitoring of a process or stream. By coupling the sensor with enzymes liberating or consuming dissolved gas, different chemicals could be estimated. Urea was estimated by first hydrolyzing it with urease and then measuring the resulting CO(2) gas in solution. Glucose was measured through its enzymatic oxidation by glucose oxidase. The sensitivity to urea over the range 0-2.5 mM was about 1.02 kPa/mM, and the standard error was 0.086 mM. Due to the lower solubility of oxygen, the sensitivity to glucose in a range from 0 to 10 microM was over 100 kPa/mM, with a standard error of only 0.76 microM. This sensitivity was not possible in closed-reactor type manometric sensors due to constraints of dimensioning the head space gas volume for reproducibility and effective mass transfer. The 90% rise times for the sensor ranged from about 1-60 min for the different applications. The dynamic characteristics of the device may be improved by using a membrane with greater porosity, higher rigidity and lower thickness, and by reducing the dimensions of the cavity volume in the sensor through integrated microfabrication of the membrane onto the transducer.     

Closure effects on oxygen transfer and aerobic growth in shake flasks

Oxygen mass transfer in shake flasks is an important aspect limiting the culture of aerobic microorganisms. In this work, mass transfer of oxygen through a closure and headspace of shake flasks is investigated. New equations for prediction of kGa in shake flasks with closures are introduced. Using Pseudomonas putida, microbial growth on glucose (fast metabolism) and phenol (slow metabolism) in shake flasks with closures were studied, considering both substrate and oxygen restrictions. A combined model for oxygen mass transfer and microbial growth is shown to accurately predict experimental oxygen concentrations and oxygen yield factors during growth experiments more accurately than previous models.     

Biosensor for the monitoring of hydrogen peroxide using poly(vinyl alcohol) membrane system

Summary A biosensor system for continuous on-line monitoring of hydrogen peroxide concentration was developed employing catalase and a poly(vinyl alcohol)/poly(tetra fluoro ethylene) bilayer membrane system, Catalase was entrapped between poly(vinyl alcohol) membrane layer and poly(tetra fluoro ethylene) membrane layer outside of the galvanic type DO probe. Since poly(vinyl alcohol) membrane has non-porous, hydrophilic characteristics, the difference in hydrogen peroxide concentration between inside and outside of the membrane was therefore approximately 100 times. The developed hydrogen peroxide sensor has a wide linear range of hydrogen peroxide sensing more than 140 mM and favourable dynamic response characteristics. The sensor showed also good operational stability, rapid response time, and long life time.     

In vitro testing of a simply constructed, highly stable glucose sensor suitable for implantation in diabetic patients

We have constructed and tested in vitro a potentially implantable, needle-type amperometric enzyme electrode which is suitable for continuous monitoring of glucose concentrations in diabetic patients. The major requirements of stability during operation and ease of manufacture have been met with a sensor design which involves a simple dip-coating procedure for applying to a platinum base electrode an inner membrane of glucose oxidase immobilised in polyhydroxyethyl methacrylate (pHEMA), and an outer membrane composed of a pHEMA/polyurethane mixture. Sensors were operated at 700 mV for detection of hydrogen peroxide. Calibration curves for the sensor were linear to at least 20 mM glucose and were unaffected by a reduction in PO2 from 20 to 5 kPa. During continuous operation in 5 mM buffered glucose solutions in vitro, sensors suffered no significant loss of response over periods of up to 60 h. Such electrodes are, therefore, useful for development as in vivo glucose sensors.     

Measurement and control of dissolved carbon dioxide in mammalian cell culture processes using an in situ fiber optic chemical sensor

At high viable cell concentrations in large-scale mammalian cell culture processes, the accumulation of dissolved carbon dioxide (dCO(2), typically quantified as an equilibrium gas-phase concentration) becomes problematic as a result of low CO(2) removal rates at reduced surface-to-volume ratios. High dCO(2) concentrations have previously been shown to inhibit cell growth and product formation in mammalian cells and to alter the glycosylation pattern of recombinant proteins. Therefore, reliable monitoring and control of dCO(2) are important for successful large-scale operation. Off-line measurements by instruments such as blood gas analyzers (BGA) are constrained by the low frequency of data collection and cannot be used for on-line control. In a preliminary evaluation of the YSI 8500 in situ sensor, a response time (t(90%)) of 6 min, sensitivity of 0.5% CO(2) (3.6 mmHg), and linearity of measurement (R(2) = 0.9997) between the equivalent gas-phase partial pressure of 0-180 mmHg (0% and 25% CO(2)) were established. Measurements were found to be unaffected by culture pH and typical mammalian cell culture concentrations of glucose, glutamine, glutamate, lactate, and ammonium. The sensor withstood repeated sterilization and cleaning cycles. The reliability of this sensor was demonstrated in microcarrier-based Chinese hamster ovary (CHO) cell perfusion cultures at reactor scales of 30, 40, 340, and 2000 L and was successfully implemented in a dCO(2) control strategy using N(2) sparging.     

Continuous glucose monitoring and control in a rotating wall perfused bioreactor

A glucose control system consisting of a single in-line glucose sensor, concentrated glucose solution, and computer hardware and software were developed. The system was applied to continuously control glucose concentrations of a perfusion medium in a rotating wall perfused vessel (RWPV) bioreactor culturing BHK-21 cells. The custom-made glucose sensor was based on a hydrogen peroxide electrode. The sensor continuously and accurately measured the glucose concentration of GTSF-2 medium in the RWPV bioreactor during cell culture. Three sets of two-point calibrations were applied to the glucose sensor during the 55-day cell culture. The system first controlled the glucose concentration in perfusing medium between 4.2 and 5.6 mM for 36 days and then at different glucose levels for 19 days. A stock solution with a high glucose concentration (266 mM) was used as the glucose injection solution. The standard error of prediction (SEP) for glucose measurement by the sensor, compared to measurement by the Beckman glucose analyzer, was +/-0.4 mM for 55 days.     

Microbial fuel cell-based biosensor for fast analysis of biodegradable organic matter

The current study was made to develop a biosensor based on a single-chamber microbial fuel cell in which anaerobes were retained in the anode compartment separated from the cathode compartment by a proton exchange membrane. In the sensor a replaceable anaerobic consortium was used for analyzing biodegradable organic matter. The anaerobes acted as biocatalysts in oxidizing organic matter and transferring electrons to the anode. The biocatalysts were renewed for each sample analysis by replacing the old anaerobic consortium with an equal amount of fresh one. A glucose standard solution was used as the target substrate. To obtain the maximum sensor output, the MFC-based sensor system was optimized using an 800 Ω resistor as the load to the external electric circuit and 25 mM phosphate buffer with 50 mM NaCl as catholyte in the aerobic compartment. The temperature of anaerobic compartment was maintained at optimal 37 °C. The cell potential across the electrodes increased with increasing loading of glucose. The sensor response was linear against concentration of glucose up to 25 g l⁻¹. The detection limit was found as 0.025 g l⁻¹. The microbial fuel cell with replaceable anaerobic consortium could be used as a biosensor for on-line monitoring of organic matter.     

Characterisation of operation conditions and online monitoring of physiological culture parameters in shaken 24-well microtiter plates

A new online monitoring technique to measure the physiological parameters, dissolved oxygen (DO) and pH of microbial cultures in continuously shaken 24-well microtiter plates (MTP) is introduced. The new technology is based on immobilised fluorophores at the bottom of standard 24-well MTPs. The sensor MTP is installed in a sensor dish reader, which can be fixed on an orbital shaker. This approach allows real online measurements of physiological parameters during continuous shaking of cultures without interrupting mixing and mass transfer like currently available technologies do. The oxygen transfer conditions at one constant shaking frequency (250 1/min) and diameter (25 mm) was examined with the chemical sulphite oxidation method. Varied filling volumes (600–1,200 μL) of Escherichia coli cultures demonstrated the importance of sufficient oxygen transfer to the culture. Cultures with higher filling volumes were subjected to an oxygen limitation, which influenced the cell metabolism and prolongated the cultivation time. The effects could be clearly monitored by online DO and pH measurements. A further study of different media in an E. coli fermentation elucidated the different growth behaviour in response to the medium composition. The MTP fermentations correlated very well with parallel fermentations in shake flasks. The new technique gives valuable new insights into biological processes at a very small scale, thus enabling parallel experimentation and shorter development times in bioprocessing.     

Continuous measurement of dissolved H2 in an anaerobic reactor using a new hydrogen/air fuel cell detector

A miniature fuel cell, using a hydrophobic Teflon(R) membrane, designed to continuously measure dissolved H(2) in nonbiological media, was tested for use in anaerobic digestion conditions. In water, this detector responds quickly and efficiently to variation of hydrogen concentration in the range from 80 to 770 nM The media used, and the metabolites or products found in anaerobic digestion media, i. e. inorganic carbon and phosphate buffers, formate, acetate, and dissolved methane, did not interfere with the signal of the detector cell. Dissolved hydrogen sulfide did not poison the cell but was detected. In spite of the detector's high sensitivity to hydrogen (about 21,000 times higher for hydrogen than for hydrogen sulfide), interferences can occur in media containing high sulfide levels.In a methanogenic reactor, the detector cell response to dissolved hydrogen was fast and reliable with time. The observed values ranged values ranged from 2 to 3.5muM. Dissolved hydrogen concentrations were 40 to 70 times higher than values calculated from measured hydrogen partial pressures and Henry's coefficient, suggesting a limitation of the process in the hydrogen transfer from the liquid to the gaseous phase.     

The use of co-immobilization of Trichosporon cutaneum and Bacillus licheniformis for a BOD sensor

The microorganisms Trichosporon cutaneum and Bacillus licheniformis were used to develop a microbial biochemical oxygen demand (BOD) sensor. It was found that T. cutaneum gave a greater response to glucose, whereas B. licheniformis gave a better response to glutamic acid. Hence, co-immobilized T. cutaneum and B. licheniformis were used to construct a glucose and glutamic acid sensor with improved sensitivity and dynamic range. A membrane loading of T. cutaneum at 1.1x10(8 )cells ml(-1) cm(-2) and B. licheniformis at 2.2x10(8) cells ml(-1) cm(-2) gave the optimum result: a linear range up to 40 mg BOD l(-1) with a sensitivity of 5.84 nA mg(-1) BOD l. The optimized BOD sensor showed operation stability for 58 intermittent batch measurements, with a standard deviation of 0.0362 and a variance of 0.131 nA. The response time of the co-immobilized microbial BOD sensor was within 5-10 min by steady-state measurement and the detection limit was 0.5 mg BOD l(-1). The BOD sensor was insensitive to pH in the range of pH 6.8-7.2.     

An innovative online VFA monitoring system for the anerobic process, based on headspace gas chromatography

A new method for online measurement of volatile fatty acids (VFA) in anerobic digesters has been developed based on headspace gas chromatography (HSGC). The method applies ex situ VFA stripping with variable headspace volume and gas analysis by gas chromatography-flame ionization detection (GC-FID). In each extraction, digester sample was acidified with H(3)PO(4) and NaHSO(4), then heated to strip the VFA into the gas phase. The gas was sampled in a low friction glass syringe before injected into the GC for measurement. The system has been tested for online monitoring of a lab-scale CSTR reactor treating manure for more than 6 months and has shown good agreement with off-line analysis. The system is capable of measuring individual VFA components. This is of advantage since specific VFA components such as propionic and butyric acid can give extra information about the process status. Another important advantage of this sensor is that there is no filtration, which makes possible application in high solids environments. The system can thus be easily applied in a full-scale biogas reactor by connecting the system to the liquid circulation loop to obtain fresh sample from the reactor. Local calibration is needed but automatic calibration is also possible using standard addition method. Sampling duration is 25-40 min, depending on the washing duration, and sensor response is 10 min. This is appropriate for full-scale reactors, since dynamics within most biogas reactors are of the order of several hours.     

A simple and rapid method for monitoring dissolved oxygen in water with a submersible microbial fuel cell (SBMFC)

A submersible microbial fuel cell (SBMFC) was developed as a biosensor for in situ and real time monitoring of dissolved oxygen (DO) in environmental waters. Domestic wastewater was utilized as a sole fuel for powering the sensor. The sensor performance was firstly examined with tap water at varying DO levels. With an external resistance of 1000?, the current density produced by the sensor (5.6±0.5-462.2±0.5mA/m(2)) increased linearly with DO level up to 8.8±0.3mg/L (regression coefficient, R(2)=0.9912), while the maximum response time for each measurement was less than 4min. The current density showed different response to DO levels when different external resistances were applied, but a linear relationship was always observed. Investigation of the sensor performance at different substrate concentrations indicates that the organic matter contained in the domestic wastewater was sufficient to power the sensing activities. The sensor ability was further explored under different environmental conditions (e.g. pH, temperature, conductivity, and alternative electron acceptor), and the results indicated that a calibration would be required before field application. Lastly, the sensor was tested with different environmental waters and the results showed no significant difference (p>0.05) with that measured by DO meter. The simple, compact SBMFC sensor showed promising potential for direct, inexpensive and rapid DO monitoring in various environmental waters.     

Patterns of carbon flow from glucose to methane in a thermophilic anaerobic bioreactor

[U-¹⁴C]Glucose, added carrier-free to sludge from a thermophilic anaerobic bioreactor being fed a lignocellulose waste, was rapidly turned over with less than one-third of the original radiolabel remaining as glucose after 5 s of incubation. The primary labeled products found were [¹⁴C]acetate and ¹⁴CO₂, which were in a ratio near 2:1. Further incubation resulted in the disappearance of [¹⁴C]acetate and the appearance of an equivalent amount of label as ¹⁴CH₄ and ¹⁴CO₂. No significant production of [¹⁴C]propionate, butyrate, lactate, or ethanol was detected from [¹⁴C]glucose, even if these potential intermediates (unlabeled) were added to the sludge at a concentration of 1 mM to trap any label entering their pools. Addition of 0.8 atm (80 kPa) of H₂ to the headspace over sludge resulted in some accumulation of [¹⁴C]lactate and a corresponding decrease in [¹⁴C]acetate produced from [¹⁴C]glucose. Production of [¹⁴C]propionate, butyrate and ethanol were still not significant in the presence of H₂. Incubation of sludge for 1 h in the presence of hydrogen resulted in increases in the lactate and formate concentrations, but not those of propionate, butyrate, or ethanol. These results demonstrate that glucose was metabolized directly to acetate, CO₂, and H₂ by the microbial populations in the bioreactor with little carbon from glucose flowing through other intermediates, indicating a high degree of coupling between glucose fermentation and hydrogen uptake. The short-term response of these microbial populations to elevated H₂ partial pressures was to increase lactate production.