Separation of viable and nonviable animal cell using dielectrophoretic filter

Selective separation of cells using dielectrophoresis (DEP) has recently been studied and methods have been proposed. However, these methods are not applicable to large‐scale separation because they cannot be performed efficiently. In DEP separation, the DEP force is effective only when it is applied close to the electrodes. Utilizing a DEP filter is a solution for large‐scale separation. In this article, the separation efficiency for viable and nonviable cells in a DEP filter was examined. The effects of an applied AC electric field frequency and the gradient of the squared electric field intensity on a DEP velocity for the viable and nonviable animal cells (3‐2H3 cell) were discussed. The frequency response of the DEP velocity differed between the viable and the nonviable cells. We deducted an empirical equation that can be used as guiding principle for the DEP separation. The results indicate that the viable and the nonviable cells were separated using the DEP filter, and the best operating conditions such as the applied voltage and the flow rate were discussed. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Development of dielectrophoresis separator with an insulating porous membrane using DC‐Offset AC Electric Fields

Our previous studies revealed that the dielectrophoresis method is effective for separating cells having different dielectric properties. The purpose of this study was to evaluate the separation characteristics of two kinds of cells by direct current (DC) voltage offset/alternating current (AC) voltage using an insulating porous membrane dielectrophoretic separator. The separation device gives dielectrophoretic (DEP) force and electrophoretic (EP) force to dispersed particles by applying the DC‐offset AC voltage. This device separates cells of different DEP properties by adopting a structure in which only the parallel plate electrodes and the insulating porous membrane are disposed in the flow path through which the cell‐suspension flows. The difference in the retention ratios of electrically homogeneous 4.5 μm or 20.0 μm diameter standard particles was a maximum of 82 points. Furthermore, the influences of the AC voltage or offset voltage on the retention ratios of mouse hybridoma 3‐2H3 cells and horse red blood cells (HRBC) were investigated. The difference in the retention ratio of the two kinds of cells was a maximum of 56 points. The separation efficiency of this device is expected to be improved by changing the device shape, number of pores, and pore placement. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1292–1300, 2016     

A novel dielectrophoresis-based device for the selective retention of viable cells in cell culture media

Cost-effective production of biopharmaceuticals on a large scale can be carried out by perfusion cultures of mammalian cells. One problem with this mode of operation for submerged free-cell cultures is the requirement for an efficient cell separation device located in the effluent stream. The present work investigates the potential for the development of a novel dielectrophoresis-based cell separator, capable of providing selective retention of viable cells in cell culture media, which are highly conductive. Predictions of the dielectrophoretic (DEP) response in culture media were first obtained through a series of DEP-levitation experiments. Subsequently, a prototype microelectrode "filter" was microfabricated and tested with C174 myeloma cell suspensions of density 1 x 10(6) cells/mL. The optimum frequency range for selective retention of viable cells was found in the range 5-15 MHz. A maximum separation efficiency of 98% was achieved at 10 MHz, with an applied peak-to-peak voltage of 30 V (maximum field strength of 10(5) V/m) and a flow rate of 30 mL/h which corresponds to a superficial velocity of 5.23 cm/h through the DEP-filter channels. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 239-250, 1997.     

Effects of Dielectrophoresis on Growth, Viability and Immuno-reactivity of Listeria monocytogenes

Dielectrophoresis (DEP) has been regarded as a useful tool for manipulating biological cells prior to the detection of cells. Since DEP uses high AC electrical fields, it is important to examine whether these electrical fields in any way damage cells or affect their characteristics in subsequent analytical procedures. In this study, we investigated the effects of DEP manipulation on the characteristics of Listeria monocytogenes cells, including the immuno-reactivity to several Listeria-specific antibodies, the cell growth profile in liquid medium, and the cell viability on selective agar plates. It was found that a 1-h DEP treatment increased the cell immuno-reactivity to the commercial Listeria species-specific polyclonal antibodies (from KPL) by ~31.8% and to the C11E9 monoclonal antibodies by ~82.9%, whereas no significant changes were observed with either anti-InlB or anti-ActA antibodies. A 1-h DEP treatment did not cause any change in the growth profile of Listeria in the low conductive growth medium (LCGM); however, prolonged treatments (4 h or greater) caused significant delays in cell growth. The results of plating methods showed that a 4-h DEP treatment (5 MHz, 20 Vpp) reduced the viable cell numbers by 56.8–89.7 %. These results indicated that DEP manipulation may or may not affect the final detection signal in immuno-based detection depending on the type of antigen-antibody reaction involved. However, prolonged DEP treatment for manipulating bacterial cells could produce negative effects on the cell detection by growth-based methods. Careful selection of DEP operation conditions could avoid or minimize negative effects on subsequent cell detection performance.     

Enhanced separation of filamentous fungi by ultrasonic field: possible usage in repeated batch processes

Usage of ultrasonic field-based filters in retention of filamentous fungal cells was assessed using Rhizopus arrhizus NRRL 1526 as a model organism. Effects of operating conditions, such as power input, harvest pump flow rate, run time and stop time, on the system's separation efficiency (SE) were evaluated by modulating the variables according to a Central Composite Design (CCD). The standard pump with which the ultrasonic filter was equipped was shown to be unsuitable and was, therefore, substituted for with a prime rate reverse pump that made possible separation and recycle of the mycelial biomass. The operating conditions were optimised (run time, 300 s; stop time, 3 s; power input, 6 W; harvest pump flow rate, 4 l per day) and a repeated batch process (three batches for a total of 192 h) was performed during which the SE was maintained always higher than 88%.     

Isolation of insulin-like growth Factors I and II from human plasma

Insulin-like growth factors I and II have been isolated from Cohn fraction IV-1 of human plasma using gel permeation chromatography, ion exchange chromatography, reversed phase chromatography, isoelectric focusing (IEF) and high performance liquid chromatography(HPLC). IGF I of specific activity 89 U/g, as measured by the isolated rat adipocyte assay, and IGF II, of specific activity 78 U/g, were obtained in yields of 16 micrograms and 34 micrograms respectively per 100g of Cohn fraction. Although this process yields IGF I which is contaminated with IGF II (due to the relatively large amount of the latter present in the original plasma), the IGF II preparations appear to be relatively free from IGF I. This separation was mainly achieved with IEF since the two factors elute close together on HPLC. Nevertheless, HPLC is important for their subsequent purification. The process is thus especially suitable for the preparation of IGF II and appears to give better yields than those obtained by earlier methods which used acid-ethanol extraction, gel permeation chromatography and polyacrylamide gel electrophoresis.     

Separation of polystyrene microbeads using dielectrophoretic/gravitational field-flow-fractionation.

The characterization of a dielectrophoretic/gravitational field-flow-fractionation (DEP/G-FFF) system using model polystyrene (PS) microbeads is presented. Separations of PS beads of different surface functionalization (COOH and none) and different sizes (6, 10, and 15 microm in diameter) are demonstrated. To investigate the factors influencing separation performance, particle elution times were determined as a function of particle suspension conductivity, fluid flow rate, and applied field frequency and voltage. Experimental data were analyzed using a previously reported theoretical model and good agreement between theory and experiment was found. It was shown that separation of PS beads was based on the differences in their effective dielectric properties. Particles possessing different dielectric properties were positioned at different heights in a fluid-flow profile in a thin chamber by the balance of DEP and gravitational forces, transported at different velocities under the influence of the fluid flow, and thereby separated. To explore hydrodynamic (HD) lift effects, velocities of PS beads were determined as a function of fluid flow rate in the separation chamber when no DEP field was applied. In this case, particle equilibrium height positions were governed solely by the balance of HD lift and gravitational forces. It was concluded that under the experimental conditions reported here, the DEP force was the dominant factor in controlling particle equilibrium height and that HD lift force played little role in DEP/G-FFF operation. Finally, the influence of various experimental parameters on separation performance was discussed for the optimization of DEP/G-FFF.     

Purification of a monocyte chemotactic factor secreted by nonhuman primate vascular cells in culture

A protein chemotactic for peripheral blood monocytes (SMC-CF) of potential importance in their recruitment to the arterial intima in atherogenesis was purified from serum-free medium conditioned by cultured baboon aortic medial smooth muscle cells. The purification of SMC-CF was monitored by a filter assay using human peripheral blood mononuclear cells and was achieved by batch separation on a cation-exchange gel followed by gel permeation chromatography, ion-exchange high-performance liquid chromatography (HPLC), and reversed-phase HPLC. The overall recovery was approximately 10% of the initial activity and yielded 0.5-1 microgram of SMC-CF/L of conditioned medium. On analytical sodium dodecyl sulfate-polyacrylamide gel electrophoresis, SMC-CF migrated as a monomeric protein with an apparent molecular weight of 14,500. A dose-dependent relationship was observed between SMC-CF concentration and monocyte chemotactic activity, with maximal and half-maximal biologic activity being observed at approximately 5 and 0.1 nM, respectively. Cultured baboon aortic smooth muscle cells also express the genes for both the A and B polypeptide chains of platelet-derived growth factor, which has been reported to be chemotactic for blood monocytes and neutrophils [Deuel, T. F., Senior, R. M., Huang, J. S., & Griffin, G. L. (1982) J. Clin. Invest. 69, 1046-1049]. Amino acid composition analyses indicate that SMC-CF is not derived either from polypeptide chain of this growth factor or from certain potentially chemotactic connective tissue proteins.     

Mammalian cell retention in a spinfilter perfusion bioreactor

A spinning cylindrical filter is often used to retain mammalian cells in a continuous perfusion bioreactor. This device, known as a spinfilter, has typically been with pore size smaller than the cell particles (single cells or aggregates) in order to achieve cell separation. For single cells in suspension, such an operation cannot be sustained over a long period of time because of clogging of the filter surface. Recently, screens with openings larger than the average cell size have been used to reduce the incidence of clogging. In this article, we have investigated how the screen size affects cell retention. We also showed why it is necessary to optimize the rotational speed of the spinfilter in order to achieve cell retention and reduce screen clogging. Effects of bulk mixing and perfusion rate on screen fouling cell retention, and cell washout were also investigated. (c) 1992 John Wiley & Sons, Inc.     

Analysis of nucleotide sugars from cell lysates by ion-pair solid-phase extraction and reversed-phase high-performance liquid chromatography

Analysis of nucleotide sugar metabolism is essential in studying glycosylation in cells. Here we describe practical methods for both extraction of nucleotide sugars from cell lysates and for their analytical separation. Solid-phase extraction cartridges containing graphitized carbon can be used for the purification of nucleotide sugars by using triethylammonium acetate buffer as a ion-pairing reagent for decreasing retention. After that they are separated by high-performance liquid chromatography using a C18 reversed-phase column and the same ion-pairing reagent for increasing retention. These new sample preparation and analysis methods enable good separation of structurally similar sugar nucleotides, compatibility with rapid evaporative concentration, and possibility to automation. Monitoring the production of GDP-deoxyhexoses in genetically engineered yeast and native bacterial cells are described here as specific applications.     

Alternating flow filtration as an alternative to internal spin filter based perfusion process: Impact on productivity and product quality

This article reports the results obtained from comparison of internal spin filter (ISF) and alternating flow filtration (ATF) as cell retention systems, regarding cell growth, volumetric perfusion rate, cell specific perfusion rate and cell productivity in the fermentation process. As expected we were able to reach higher cell densities and to achieve longer runs since ATF systems are known to be less affected by fouling. Volumetric production of the reactor using the ATF system was 50‐70% higher than the production achieved using the ISF due to higher cell density and a two‐fold increase in the perfusion rate. On the other hand, downstream processing performances were evaluated regarding chromatographic steps yields and productivity and quality attributes of the purified materials. Similar results were obtained for all evaluated systems. The fact that we were able to achieve a 2 working volumes (WV)/day perfusion rate using an ATF system as cell retention device allowed us to virtually double the WV of a 25 L reactor. These results constitute valuable data for the optimization of recombinant protein production in perfusion processes since a two‐fold increase in the average production of a manufacturing facility could be easily achieved as long as downstream scale up is possible. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1010–1014, 2017     

Size-dependent, chromatographic separation of double-stranded DNA which is not based on gel permeation mode

A new procedure for size-dependent fractionation of DNA was investigated. DNA fragments ranging from 10 to 40 kbp were separated by using columns for high-performance gel permeation chromatography. However, the order of elution was opposite to that which would be expected for gel permeation chromatography, i.e., smaller fragments were eluted faster than larger fragments, though separation based on normal gel permeation chromatography was observed when smaller DNA fragments (less than 5 kbp) were applied. The size range of DNA which can be resolved by this new procedure was found to depend on both particle size and flow rate; the use of a column packed with smaller particles or the application of a faster flow rate enabled us to resolve smaller DNA fragments, but the pore size or chemical nature of the column packing had scarcely any effect on the resolution. This mode of separation was attained by using both silica and polymer packings. The results suggest that the separation is based on a hydrodynamic phenomenon.     

AC electrokinetic characterisation and separation of cells with high and low embryogenic potential in suspension cultures of carrot (Daucus carota)

Suspension cultures of Daucus carota L. were established, and cells with embryogenic potential were separated from those without by density gradient centrifugation in Ficoll at different stages in the growth curve. In order to obtain information about the electrical properties of individual cells, electrorotation spectra of single plant cells from different fractions were measured before and after induction of embryogenesis. The data were analysed using models based on Maxwell–Wagner's theories of interfacial polarisation. It was found that the denser cells had a higher embryogenic potential, a darker appearance and a higher internal conductivity (>1 S m^–1) than the less dense cells, which had less or no embryogenic potential and a lower internal conductivity (<1 S m^–1). Modelling the dielectrophoretic (DEP) response on the basis of the electrorotation data suggested that separation of cells with high embryogenic potential may be achievable in the frequency range 1–10 MHz. Actual dielectrophoretic separation of cells with high embryogenic potential from suspensions in which embryogenesis had not yet been induced was achieved using steric as well as hyperlayer dielectrophoretic Field-Flow Fractionation (DEP-FFF).     

Improved Ocular Delivery of Nepafenac by Cyclodextrin Complexation

Nepafenac is a nonsteroidal anti-inflammatory drug (NSAID), currently only available as 0.1% ophthalmic suspension (Nevanac®). This study utilized hydroxypropyl-β-cyclodextrin (HPBCD) to increase the water solubility and trans-corneal permeation of nepafenac. The nepafenac-HPBCD complexation in the liquid and solid states were confirmed by phase solubility, differential scanning calorimetry (DSC), X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), and nuclear magnetic resonance spectroscopy (NMR) analyses. Nepafenac 0.1% ophthalmic solution was formulated using HPBCD (same pH and osmolality as that of Nevanac®) and pig eye trans-corneal permeation was studied versus Nevanac®. Furthermore, nepafenac content in cornea, sclera, iris, lens, aqueous humor, choroid, ciliary body, retina, and vitreous humor was studied in a continuous isolated pig eye perfusion model in comparison to the suspension and Nevanac®. Permeation studies using porcine corneas revealed that the solution formulation had a permeation rate 18 times higher than Nevanac®. Furthermore, the solution had 11 times higher corneal retention than Nevanac®. Drug distribution studies using porcine eyes revealed that the solution formulation enables detectable levels in various ocular tissues while the drug was undetectable by Nevanac®. The ocular solution formulation had a significantly higher drug concentration in the cornea compared to the suspension or Nevanac®.     

Kinetics of inactivation of phytase (phy A) during modification of histidine residue by IAA and DEP

Chemical probing of histidine residues using specific modifiers, iodoacetic acid (IAA) and diethylpyrocarbonate (DEP) resulted in the inactivation of phytase (phy A). The kinetic theory of the substrate reaction during the modification of enzyme activity was applied to a study of the kinetics of the course of inactivation of phytase by IAA and DEP. The results suggested that histidine residues are involved in the active site of the enzyme. They also indicated that inactivation of the enzyme by IAA was via a complexing type inhibition, while the inhibition by DEP reaction involved a conformational change step before inactivation. The dissociation constant of the enzyme-inhibitor complex of IAA, the constant of the conformational change of DEP and the microscopic rate constants of two inhibitors were obtained.     

A direct competitive enzyme-linked immunosorbent assay by antibody coated for diethyl phthalate analysis

A direct competitive enzyme-linked immunosorbent assay (ELISA) has been developed for detection of diethyl phthalate (DEP). Protein-hapten conjugate was synthesized to produce polyclonal antibodies against DEP. Experimental parameters were optimized, including immunoreaction conditions, the dilution ratio of horseradish peroxidase (HRP)-antigen conjugate, time of the antibody coated, effect of pH, and ionic strength. The limit of detection was 0.096 ng/ml, and the linear range was 0.1-3500 ng/ml with a regression coefficient (R²) of 0.9957. Recoveries were between 96.4 and 106.2%. The cross-reactivities of the anti-DEP antibody to six structurally related phthalate esters were less than 9%. The method was successfully applied to the determination of DEP in tap water, river water (Yangtze River), and leachate from plastic drinking bottles. This immunoassay was highly specific, sensitive, rapid, simple, and suitable for DEP monitoring. The results obtained were compared with those obtained using the high-performance liquid chromatography method.     

Sensitivity improvement of circular dichroism detection in HPLC by using a low-pass electronic noise filter: Application to the enantiomeric determination purity of a basic drug

The quality control of chiral drugs requires the determination of their enantiomeric purity. Nowadays, circular dichroism (CD) spectroscopy is gaining increasing importance in pharmaceutical analysis because of the commercially available CD detector in liquid chromatography. The separation of the two enantiomers of a basic drug (efaroxan) was achieved by high performance liquid chromatography using an amylose-derivated column with both UV and CD detections. A baseline-resolved separation (resolution: 5) was obtained after optimization of the mobile phase composition with hexane-ethanol-diethylamine (90:10:0.05; v/v/v). The use of a commercial low-pass electronic noise filter of the CD signal has improved the signal-to-noise ratio by a factor twelve and allowed the quantitation of each enantiomer in the 1.25-300 microg ml(-1) concentration range. The CD linear calibration curve, expressed in terms of stereoisomer height ratio versus concentration ratio, was plotted over the 0.4-6% range. A correlation coefficient greater than 0.999 was obtained by least-squares regression and the limit of detection for the distomer/eutomer ratio was estimated at 0.14%. Although the method validation showed good repeatability on the retention times (RSD < 0.9%), on the peak height ratios (RSD < 8.7%) of each enantiomer only up to 99.2% enantiomeric purity was achieved.     

Enantioseparation of amfepramone (rac-diethylpropion): preparative separation of the enantiomers and enantioselective analysis

The enantiomers of the anorectic drug amfepramone [rac-diethylpropion, rac-2-(diethylamino)-1-phenyl-1-propanone; rac-DEP] were separated in the preparative scale by crystallization. With enantiopure di-O-benzoyltartaric acid as salt-forming chiral selector, diastereoisomeric salts of DEP enantiomers with a final purity of more than 97.5% were obtained. Analytical liquid chromatographic and electrophoretic methods for the control of the enantiomeric purity and the stoichiometry of the salts were developed. The enantioseparation of rac-DEP by capillary electrophoresis (CE) using hydroxypropyl-beta-cyclodextrin (HP-beta-CD) as chiral discriminator and phosphate buffer (pH 3.3) as run buffer led to good separations. HPLC methods were developed using polysaccharide chiral stationary phases (CSP). The separation of the two enantiomers and the two main degradation products (1-phenyl-1,2-propanedione and propiophenone), known from solid and liquid pharmaceutical preparations, was attained in one run on the silica-based CSP cellulose tris(3,5-dimethylphenylcarbamate) (Chiralcel OD). The conditions which might affect the enantioselectivity and the quality of the enantiomeric separation were investigated for Chiralcel OD and the related CSP amylose tris(3,5-dimethylphenylcarbamate) (Chiralpak AD). Both CSPs showed very similar chromatographic properties. The separation factors could be influenced significantly by varying the polar organic modifier added to the mobile phase.     

High-density perfusion culture of insect cells with a biosep ultrasonic filter

The baculovirus/insect cell expression system has provided a vital tool to produce a high level of active proteins for many applications. We have developed a very high-density insect cell perfusion process with an ultrasonic filter as a cell retention device. The separation efficiency of the filter was studied under various operating conditions. A cell density of over 30 million cells/mL was achieved in a controlled perfusion bioreactor and cell viability remained greater than 90%. Sf9 cells from a high-density culture and a spinner culture were infected with two recombinant baculoviruses expressing genes for the production of human chitinase and monocyte-colony inhibition factor. The protein yield on a cell basis from infecting high-density Sf9 cells was the same as or higher than that from the spinner Sf9 culture. Virus production from the high-density culture was similar to that from the spinner culture. The results show that the ultrasonic filter did not affect insect cells' ability to support protein expression and virus production following infection with baculovirus. The potential applications of the high-density perfusion culture for large-scale protein expression from Sf9 cells are also highlighted.     

UPLC/MS based method for quantitative determination of fatty acid composition in Gram-negative and Gram-positive bacteria

Quantitative fatty acid composition of microorganisms at various growth space points is required for understanding membrane associated processes of cells, but the majority of the relevant publications still restrict to the relative compositions. In the current study, a simple and reliable method for quantitative measurement of fatty acid content in bacterial biomass without prior derivatization using ultra performance liquid chromatography-electrospray ionization mass spectrometry was developed. The method was applied for investigating the influence of specific growth rate and pH on the fatty acid profiles of two biotechnologically important microorganisms — Gram-negative bacteria Escherichia coli and Gram-positive bacteria Lactococcus lactis grown in controlled physiological states. It was found that the membranes of slowly growing cells are more rigid and that the fatty acid fraction of the cells of L. lactis diminishes considerably with increasing growth rate.