At-line quantification of bioactive antibody in bioreactor by surface plasmon resonance using epitope detection

We report an innovative at-line method to monitor concentration of bioactive antibody (i.e., antibody with conserved antigen-binding activity) secreted during bioreactor culture by the use of surface plasmon resonance (SPR)-based biosensor technology. In a first series of experiments, conditions for SPR-based measurements were validated off-line by monitoring bioactive antibody concentration in conditioned medium from 500-ml baffled flask hybridoma cell cultures. A fully automated experimental setup in which the SPR-based biosensor was harnessed to a bioreactor was then used at-line to monitor the concentration of bioactive antibody produced in a 3.5-L bioreactor. Quantitative SPR measurements performed both at-line and off-line were in excellent agreement with quantitative Western blotting followed by densitometry analyses. Thus, our experimental study confirms that SPR biosensors can be applied to at-line quantification of correctly folded proteins that are secreted by cells cultured in a bioreactor. Our experimental approach represents a novel and robust analytical strategy to be applied to the control and optimization of the production of bioactive secreted proteins.     

Long-term continuous monitoring of dissolved oxygen in cell culture medium for perfused bioreactors using optical oxygen sensors

For long-term growth of mammalian cells in perfused bioreactors, it is essential to monitor the concentration of dissolved oxygen (DO) present in the culture medium to ascertain the health of the cells. An optical oxygen sensor based on dynamic fluorescent quenching was developed for long-term continuous measurement of DO for NASA-designed rotating perfused bioreactors. Tris(4,7-diphenyl-1,10-phenanthroline) ruthenium(II) chloride is employed as the fluorescent dye indicator. A pulsed, blue LED was chosen as the excitation light source. The sensor can be sterilized using an autoclave. The sensors were tested in a perfused rotating bioreactor supporting a BHK-21 (baby hamster kidney) cell culture over one 28-day, one 43-day, and one 180-day cell runs. The sensors were initially calibrated in sterile phosphate-buffered saline (PBS) against a blood-gas analyzer (BGA), and then used continuously during the entire cell culture without recalibration. In the 180-day cell run, two oxygen sensors were employed; one interfaced at the outlet of the bioreactor and the other at the inlet of the bioreactor. The DO concentrations determined by both sensors were compared with those sampled and measured regularly with the BGA reference. The sensor outputs were found to correlate well with the BGA data throughout the experiment using a single calibration, where the DO of the culture medium varied between 25 and 60 mm Hg at the bioreactor outlet and 80-116 mm Hg at the bioreactor inlet. During all 180 days of culture, the precision and the bias were +/-5.1 mm Hg and -3.8 mm Hg at the bioreactor outlet, and +/- 19 mm Hg and -18 mm Hg at inlet. The sensor dynamic range is between 0 and 200 mm Hg and the response time is less than 1 minute. The resolution of the sensor is 0.1 mm Hg at 50 mm Hg, and 0.25 mm Hg at 130 mm Hg.     

Two-phase bioreactor system for cell-laden hydrogel assembly

Bottom-up approach is a potentially useful tool for hydrogel assembly of cell-laden individual building blocks. In this article, we assembled individual building blocks of photocrosslinkable microgels in a rapid and controlled manner. Individual building blocks of poly(ethylene glycol) (PEG) microgels with square and hexagonal shapes were fabricated by using a photolithography technique. Individual building blocks of PEG microgels were assembled on a hydrophobic mineral oil phase in a bioreactor with a magnetic stirrer. The hydrophobic mineral oil minimized the surface free energy to assemble hydrophilic PEG microgels on a two-phase oil-aqueous solution interface. We used the hydrophobic effect as a driving force for the hydrogel assembly. Various types of the hydrogel assembly were generated by controlling the stirring rate. As stirring speed increased, the percentage of linear, branched, and closely packed hydrogel assembly was increased. However, the percentage of random assembly was reduced by increasing stirring rate. The stirring time also played an important role in controlling the types of hydrogel assembly. The percentage of linear, branched, and closely packed hydrogel assembly was improved by increasing stirring time. Therefore, we performed directed cell-laden hydrogel assembly using a two-phase bioreactor system and optimized the stirring rate and time to regulate the desired types of hydrogel assembly. Furthermore, we analyzed cell viability of hydrogel linear assembly with square shapes, showing highly viable even after secondary photocrosslinking reaction. This bioreactor system-based hydrogel assembly could be a potentially powerful approach for creating tissue microarchitectures in a three-dimensional manner.     

Patterning cells on optically transparent indium tin oxide electrodes

The ability to exercise precise spatial and temporal control over cell-surface interactions is an important prerequisite to the assembly of multi-cellular constructs serving as in vitro mimics of native tissues. In this study, photolithography and wet etching techniques were used to fabricate individually addressable indium tin oxide (ITO) electrodes on glass substrates. The glass substrates containing ITO microelectrodes were modified with poly(ethylene glycol) (PEG) silane to make them protein and cell resistive. Presence of insulating PEG molecules on the electrode surface was verified by cyclic voltammetry employing potassium ferricyanide as a redox reporter molecule. Importantly, the application of reductive potential caused desorption of the PEG layer, resulting in regeneration of the conductive electrode surface and appearance of typical ferricyanide redox peaks. Application of reductive potential also corresponded to switching of ITO electrode properties from cell non-adhesive to cell-adhesive. Electrochemical stripping of PEG-silane layer from ITO microelectrodes allowed for cell adhesion to take place in a spatially defined fashion, with cellular patterns corresponding closely to electrode patterns. Micropatterning of several cell types was demonstrated on these substrates. In the future, the control of the biointerfacial properties afforded by this method will allow to engineer cellular microenvironments through the assembly of three or more cell types into a precise geometric configuration on an optically transparent substrate.     

Multispectral imaging of ion transport in neutral carrier-based cation-selective membranes.

BACKGROUND: High-resolution spectroscopic imaging of the cross section of ion-selective membranes during real-time electrochemical measurements is termed spectroelectrochemical microscopy (SpECM). SpECM is aimed for optimizing the experimental conditions in mass transport controlled ion-selective electrode (ISE) membranes for improved detection limit. METHODS: The SpECM measurements are performed in a thin layer electrochemical cell. The key element of the cell is a membrane strip spacer ring assembly which forms a two compartment electrochemical cell. The cell is placed onto the stage of a microscope and the membrane strip is positioned in the center of the field of view. A slice of the image is focused onto the entrance slit of the imaging spectrometer. RESULTS: SpECM has been used for the determination of the diffusion coefficients of different membrane ingredients and for the quantitative assessment of the charged site concentrations in ISE membranes and membrane plasticizers. In addition, changes in the concentration profiles of the ionophore (free and complexed) and charged mobile sites inside the ISE membranes are documented upon the application of large external voltages. CONCLUSIONS: This account demonstrates the power and advantages of SpECM, a multispectral imaging method for investigations of mass transport processes in ISE membranes during electrochemical measurements.     

Activity coefficients of NaCl in trehalose-water and maltose-water mixtures at 298.15 K

The ionic mean activity coefficients of NaCl in trehalose-water and maltose-water mixtures have been experimentally determined at 298.15 K from emf measurements by electrochemical cell containing ion selective electrodes (ISE): Na-ISE/NaCl (m), sugar (Y%), H(2)O (100-Y%)/Cl-ISE. The electrolyte molality (m) ranged between 0.01 and 3 mol kg(-1), approximately, and the weight percent (Y%) of sugar in the mixture of solvents between 0, 10, 20, 30 and 40%. The system is considered as an electrolyte in a mixture of solvents and the data have been analysed by using the Debye-Hückel and Pitzer equations. The results obtained with both equations are in quite agreement with each other. The variation of the fit parameter from both equations were studied relative to the change in the dielectric properties of the mixture of solvents. Standard free energy of transference were comparatively discussed in terms of ion-solvent, ion-ion interactions and the hydration of both the electrolyte and the sugar.     

An online, non-invasive fluorescence probe for immobilized cell culture process development

An online, analytical technology was developed that utilized fluorescence to detect cells during an immobilized cell culture process. Chinese hamster ovary (CHO) cells that produced monoclonal antibodies (mAb) were transfected to express green fluorescent protein (GFP), and stable, fluorescence-positive cells were obtained by fluorescence-activated cell sorting (FACS). The immobilized cell culture process was then used to test the effects of sodium butyrate on cells. In this study, cells were cultured in porous, fibrous matrices that were placed in spinner flasks. A lab-scale, perfusion bioreactor with computer-controlled, online fluorescence sensors that continuously detected GFP fluorescence and quantified cell growth was utilized. In addition, the level of GFP fluorescence was used to predict mAb production in the culture without sampling for cell counting and protein analysis. Thus, non-invasive, fluorescence detection of cells provided a rapid, reliable and robust approach for developing an immobilized cell culture process.     

Pulse mode shear horizontal-surface acoustic wave (SH-SAW) system for liquid based sensing applications

In this work, we describe a novel pulse mode shear horizontal-surface acoustic wave (SH-SAW) polymer coated biosensor that monitors rapid changes in both amplitude and phase. The SH-SAW sensors were fabricated on 36 degrees rotated Y-cut X propagating lithium tantalate (36 YX.LT). The sensitivity of the device to both mass loading and visco-elastic effects may be increased by using a thin guiding layer of cross-linked polymer. Two acoustic modes are excited by the electrodes in this crystalline direction. Metallisation of the propagation path of the 36 YX.LT devices allows the two modes to be discriminated. Successive polymer coatings resulted in the observation of resonant conditions in both modes as the layer thickness was increased. Using the 36 YX.LT devices, we have investigated the application of a novel pulse mode system by sensing a sequence of deposition and removal of a biological layer consisting of vesicles of the phospholipid POPC. A continuous wave system was used to verify the accuracy of the pulse mode system by sensing a series of poly(ethylene glycol) (PEG) solutions. The data clearly demonstrates the ability of the 36 YX.LT pulse mode system to provide rapid measurements of both amplitude and phase for biosensing applications.     

Membrane-aerated microbioreactor for high-throughput bioprocessing

A microbioreactor with a volume of microliters is fabricated out of poly(dimethylsiloxane) (PDMS) and glass. Aeration of microbial cultures is through a gas-permeable PDMS membrane. Sensors are integrated for on-line measurement of optical density (OD), dissolved oxygen (DO), and pH. All three parameter measurements are based on optical methods. Optical density is monitored via transmittance measurements through the well of the microbioreactor while dissolved oxygen and pH are measured using fluorescence lifetime-based sensors incorporated into the body of the microbioreactor. Bacterial fermentations carried out in the microbioreactor under well-defined conditions are compared to results obtained in a 500-mL bench-scale bioreactor. It is shown that the behavior of the bacteria in the microbioreactor is similar to that in the larger bioreactor. This similarity includes growth kinetics, dissolved oxygen profile within the vessel over time, pH profile over time, final number of cells, and cell morphology. Results from off-line analysis of the medium to examine organic acid production and substrate utilization are presented. By changing the gaseous environmental conditions, it is demonstrated that oxygen levels within the microbioreactor can be manipulated. Furthermore, it is demonstrated that the sensitivity and reproducibility of the microbioreactor system are such that statistically significant differences in the time evolution of the OD, DO, and pH can be used to distinguish between different physiological states. Finally, modeling of the transient oxygen transfer within the microbioreactor based on observed and predicted growth kinetics is used to quantitatively characterize oxygen depletion in the system.     

Characterization of oxygen transfer in a membrane-aerated hollow-fibre bioreactor using modified microcoaxial needle electrodes

In this work the volumetric O₂ transfer coefficient (OTC) through a membrane of a miniaturized hollow-fibre bioreactor was measured by the use of modified O₂ microaxial needle electrodes. Before measurment, available electrodes were modified by inserting and gluering them in thin galss capillaries to avoid damage. No differences in the behaviour of the electrodes occurred in comparison to the non-modified electrodes. These modified electrodes allowed O₂ partial pressure measurement in the 0.8-mm-high extracapillary space (ECS) of the bioreactor with high sensitivity and reliability. O₂ measurements were carried out the two ports of the ECS at different insertion depths. The results of the measurements showed a homogenous O₂ supply during variation of the radial co-coordinate of the electrode. In addition to these results, an increase in the local supply in the direction of medium flow was observed . The calculated mean OTC (47–63 h^–1) gave extremely improved O₂ transfer due to membrane aeration compared to conventional hallow-fibre systems and other bioreactors used in animal-cell culture technology. The improved OTC and the small ECS volume (4.3 ml) makes this culture system suitable for the cultivation of primary cells with tissue-like densities.     

Impedance analysis of adherent cells after in situ electroporation: non-invasive monitoring during intracellular manipulations

In this study adherent animal cells were grown to confluence on circular gold-film electrodes of 250 μm diameter that had been deposited on the surface of a regular culture dish. The impedance of the cell-covered electrode was measured at designated frequencies to monitor the behavior of the cells with time. This approach is referred to as electric cell-substrate impedance sensing or short ECIS in the literature. The gold-film electrodes were also used to deliver well-defined AC voltage pulses of several volts amplitude and several hundred milliseconds duration to the adherent cells in order to achieve reversible membrane electroporation (in situ electroporation=ISE). Electroporation-assisted introduction of membrane impermeable molecules into the cytoplasm was studied by using FITC-labeled dextran molecules of different molecular weights. Probes as big as 2MDa were successfully loaded into the cells residing on the electrode surface. Time-resolved impedance measurements before and immediately after the electroporation pulse revealed the kinetics of membrane resealing as well as subsequent changes in cell morphology. Cells recovered from the electroporation pulse within less than 90 min. When membrane-impermeable, bioactive compounds like N(3)(-) or bleomycin were introduced into the cells by in situ electroporation, concomitant ECIS readings sensitively reported on the associated response of the cells to these toxins as a function of time (ISE-ECIS).     

Label-free detection of cupric ions and histidine-tagged proteins using single poly(pyrrole)-NTA chelator conducting polymer nanotube chemiresistive sensor

Novel chemical and biological sensors based on a single poly(pyrrole)-NTA chelator nanotube for sensitive, selective, rapid and real-time detection of histidine-tagged protein and cupric ions are reported. NTA groups on the nanotube surface provided a simple mechanism for metal ion sensing via the high-affinity interaction between NTA and the subsequent detection of histidine-tagged protein through the coordination with metal chelated nanotube. Poly(pyrrole)-NTA chelator nanotubes of 190 nm outside diameter, 35 nm wall thickness and 30 microm long were synthesized by electrochemical polymerization of pyrrole-NTA inside a 200 nm diameter alumina template and assembled as a chemoresistive device by bottom-up contact geometry on a pair of parallel gold electrodes with a gap distance of 3 microm. The chemoresistive sensors based on single poly(pyrrole)-NTA chelator nanotube exhibited detection as low as one-hundredth attomolar (0.6 ppt) cupric ions and 1 ng/ml of penta-histidine tagged syntaxin protein.     

Effects of methocel A15LV, polyethylene glycol, and polyvinyl alcohol on CD13 and CD33 receptor surface content and metabolism of HL60 cells cultured in stirred tank bioreactors

Flow cytometry was used to examine the effect of hydrodynamic forces in a stirred tank bioreactor on the CD13 and CD33 receptor surface content of HL60 (human promyelocytic leukemia) cells. A step increase in agitation rate from 80 to 400 rpm reduced the HL60 cell apparent growth rate and increased the CD13 receptor surface content per cell, on average, by 95%. In contrast, this step increase in agitation rate to 400 rpm decreased the CD33 receptor surface content per cell, on average, by 10%. The protective effects of 0.1% Methocel A15LV, polyethylene glycol (PEG), and polyvinyl alcohol (PVA) on CD13 and CD33 receptor surface content were examined under agitation at 300 rpm in parallel 2 L bioreactor runs. The average CD33 receptor surface content was unaffected by the presence of Methocel A15LV or PEG, while PVA had a slight protective effect. In contrast, in terms of CD13 receptor content, HL60 cells agitated at 300 rpm with Methocel A15LV, PEG, or PVA behaved like cells agitated at 80 rpm with no media additives (McDowell and Papoutsakis, 1998). That is, Methocel A15LV, PEG, and PVA prevented the transduction of mechanical forces which affect CD13 cell content. HL60 cells cultured with 0.1% A15LV, PEG or PVA under conditions of mild agitation (60 rpm) in spinner flasks exhibited glucose consumption and lactate production rates that were approximately 20% lower than values of cultures containing no additive. Under conditions of agitation at 300 rpm in the 2 L bioreactor, the presence of A15LV, PEG, and PVA reduced the HL60 glucose consumption and lactate production rates by approximately 50%. Thus, media additives can dramatically reduce lactate accumulation in agitated bioreactors due to cell growth, in addition to providing protection from cellular injury.     

Sensor and biosensor based on Prussian Blue modified gold and platinum screen printed electrodes

Gold (Au) and platinum (Pt) screen-printed electrodes were modified with Prussian Blue (PB) for the development of amperometric sensors selective for hydrogen peroxide detection. The sensors exhibited sensitivities towards H(2)O(2) equal to 2 A M(-1) cm(-2) for Au and 1 A M(-1) cm(-2) for Pt electrodes. The sensors were also employed as the basis for construction of glucose biosensors through further modification with crystallised glucose oxidase immobilised in a Nafion membrane. In order to improve the operational stability of the modified electrodes a buffer solution containing tetrabutylammonium toluene-4-sulfonate was used. The long-term performance of the sensors and biosensors were evaluated by continuous monitoring of hydrogen peroxide and glucose solutions (50 microM and 1 mM, respectively) in the flow-injection mode for 10 h.     

Monitoring Cl<Superscript>−</Superscript> Movement in Single Cells Exposed to Hypotonic Solution

Self-referencing ion - selective electrodes (ISEs), made with Chloride Ionophore I-Cocktail A (Fluka), were positioned 1–3 μm from human embryonic kidney cells (tsA201a) and used to record chloride flux during a sustained hyposmotic challenge. The ISE response was close to Nernstian when comparing potentials (V_N) measured in 100 and 10 mM NaCl (ΔV_N = 57 ± 2 mV), but was slightly greater than ideal when comparing 1 and 10 mm NaCl (ΔV_N = 70 ± 3 mV). The response was also linear in the presence of 1 mm glutamate, gluconate, or acetate, 10 μm tamoxifen, or 0.1, 1, or 10 mm HEPES at pH 7.0. The ISE was ∼3 orders of magnitude more selective for Cl⁻ over glutamate or gluconate but less than 2 orders of magnitude move selective for Cl⁻ over bicarbonate, acetate, citrate or thiosulfate. As a result this ISE is best described as an anion sensor. The ISE was ‘poisoned’ by 50 μm 5−nitro-2-(3phenylpropyl-amino)-benzoic acid (NPPB), but not by tamoxifen. An outward anion efflux was recorded from cells challenged with hypotonic (250 ± 5 mOsm) solution. The increase in efflux peaked 7–8 min before decreasing, consistent with regulatory volume decreases observed in separate experiments using a similar osmotic protocol. This anion efflux was blocked by 10 μm tamoxifen. These results establish the feasibility of using the modulation of electrochemical, anion-selective, electrodes to monitor anions and, in this case, chloride movement during volume regulatory events. The approach provides a real-time measure of anion movement during regulated volume decrease at the single-cell level.     

Supermacroporous polymer‐based cryogel bioreactor for monoclonal antibody production in continuous culture using hybridoma cells

Cryogel matrices composed of different polymeric blends were synthesized, yielding a unique combination of hydrophilicity and hydrophobicity with the presence or absence of charged surface. Four such cryogel matrices composed of polyacrylamide–chitosan (PAAC), poly(N‐isopropylacrylamide)–chitosan, polyacrylonitrile (PAN), and poly(N‐isopropylacrylamide) were tested for growth of different hybridoma cell lines and production of antibody in static culture. All the matrices were capable for the adherence of hybridoma cell lines 6A4D7, B7B10, and H9E10 to the polymeric surfaces as well as for the efficient monoclonal antibody (mAb) production. PAAC proved to be relatively better in terms of both mAb production and cell growth. Further, PAAC cryogel was designed into three different formats, monolith, disks, and beads, and used as packing material for packed‐bed bioreactor. Long‐term cultivation of 6A4D7 cell line on PAAC cryogel scaffold in all the three formats could be successfully done for a period of 6 weeks under static conditions. Continuous packed‐bed bioreactor was setup using 6A4D7 hybridoma cell line in the three reactor formats. The reactors ran continuously for a period of 60 days during which mAb production and metabolism of cells in the bioreactors were monitored periodically. The monolith bioreactor performed most efficiently over a period of 60 days and produced a total of 57.5 mg of antibody in the first 30 days (in 500 mL) with a highest concentration of 115 μg mL^?1, which is fourfold higher than t‐flask culture. The results demonstrate that appropriate chemistry and geometry of the bioreactor matrix for cell growth and immobilization can enhance the reactor productivity. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2011     

Yeast cell debris and protein partitioning in the poly(ethylene glycol)-poly(vinyl alcohol) biphasic system

Yeast cells, cell debris and protein partitioning have been investigated in the poly(ethylene glycol) (PEG) 8000/poly(vinyl alcohol) (PVA) 10,000 system. Cells and cell debris partition into the lower (PVA) phase over the pH range 4.8-7.5, and with up to 0.37 M KCl at pH 5.9. Protein partitioning is more pH-dependent in the PEG/PVA system than in the PEG/dextran system, and a significant fraction of the total protein is found at the interface at lower pH values. Significant, rapid purification of overproduced pyruvate kinase in a PEG/PVA system containing Blue Sepharose CL-6B particles is demonstrated.     

A multianalyte flow electrochemical cell: application to the simultaneous determination of carbohydrates based on bioelectrocatalytic detection

A multianalyte flow electrochemical cell (MAFEC) for bioanalysis is constructed, characterised and used for simultaneous carbohydrate analysis incorporating mediated amperometric enzyme electrodes. Although multidetection schemes can be addressed with microfabricated systems, it is demonstrated that a "meso" analytical device of low cost can give answers to traditional simultaneous multianalysis problems, being robust, and easy to construct and operate. The cell operates as a radial flow thin-layer device and can achieve mass transport controlled response for fast electrochemical reactions. When appropriate enzymatic electrodes are used the response becomes kinetically limited, but still shows a better than 5% R.S.D. for response to different sugars analysed. All the enzymatic sensors are mediated with different osmium compounds appropriate for each enzyme's mechanism (NAD or PQQ dehydrogenases) in some cases combining multienzyme sensors. All sensors were optimised so that different sugars do not produce interferences to other sensors. Matrix interferences were kept low by operating all sensors at or below 150 mV versus Ag/AgCl. The integrated system was used for the simultaneous detection of fructose, sucrose, glucose, galactose, and lactose, fully characterising the system for these analytes (sensitivity, dynamic range). Cross referenced calibration curves were used for signal treatment and interpretation and it was possible to analyse real juice and milk samples with results agreeing with the standard enzymatic methods for the same analyses with a sampling frequency of more than 100 h(-1).     

Analysis of CHO-K1 cell growth in a fixed bed bioreactor using magnetic resonance spectroscopy and imaging

Non-invasive magnetic resonance imaging and spectroscopy techniques have been used to monitor the growth and distribution of Chinese hamster ovary K1 cells growing in a fixed bed bioreactor composed of macroporous carriers. Diffusion-weighted 1H magnetic resonance spectroscopy was used to monitor the volume fraction of the bioreactor occupied by the cells and diffusion-weighted 1H magnetic resonance imaging was used to map cell distribution. The imaging measurements demonstrated that cell growth in the bioreactor was heterogeneous, with the highest cell densities being found at the surface of the carriers. The increase in the volume fraction occupied by the cells during cell growth showed a close correlation with bioreactor ATP content measured using 31P magnetic resonance spectroscopy. These magnetic resonance measurements, in conjunction with measurements of bioreactor glucose consumption, allowed estimation of the specific glucose consumption rate. This declined during the culture, in parallel with medium glucose concentration. This revised version was published online in July 2006 with corrections to the Cover Date.