Fractionation of chicken egg glycoproteins and their purification using preparative HPLC

A new method of fractionation of hen egg glycoproteins has been developed. The procedure involves high-speed mass ion-exchange chromatography on ZetaPrep cartridges, differential precipitation, and ultrafiltration on "Minitan" tangential-flow system. Six fractions were obtained from egg white (ovomucin, avidin, riboflavin-binding glycoprotein RF-GPw, ovoinhibitor, ovalbumin-ovotransferrin, and ovomucoid fractions), and two fractions from egg yolk (riboflavin-binding glycoprotein RF-GPy and phosvitin fractions). Using ion-exchange HPLC on columns (150 X 21.5 mm) Protein PAK DEAE-5PW and SP-5PW, six homogenous glycoproteins (avidin, RF-GPw, ovalbumin, ovotransferrin, ovomucoid, and RF-GPy) were isolated in preparative quantities (0.1-1 g). Ion-exchange HPLC also resolves some glycoproteins' isoforms with different pI values.     

Extraction and analysis of microcystins RR and LR in cyanobacteria using a cyano cartridge

A new method for the extraction of microcystins RR and LR in cyanobacteria was developed using a cyano cartridge. Lyophilized cells (100 mg) were extracted with 5% (v/v) acetic acid. The extract was centrifuged and then the supernatant was applied to a CN cartridge. The cartridge that contained microcystins was rinsed with 5 ml of water and 5 ml of 0.5 M acetic acid, followed by 5 ml of 5% acetonitrile in water. Microcystins were finally eluted from the CN cartridge with 70% acetonitrile in water and were determined by HPLC. Better recoveries and chromatograms were observed than with ODS cartridges.     

Molecularly imprinted cryogel cartridges for the selective recognition of tyrosine

Molecularly imprinted polymers are used for creating a specific cavity and selective recognition sites for the structure of a target molecule in a polymeric structure. In this study, specific molecularly imprinted cryogel cartridges were synthesized using two distinct functional monomers to compare imprinting efficiency for the selective recognition of Tyrosine (Tyr). Tyr-imprinted cryogel cartridge (MIP1) was prepared using metal-chelate coordination for the imprinting process by free-radical bulk polymerization under frozen conditions, and Tyr-imprinted cryogel cartridge (MIP2) was prepared in the same way using hydrophobic effects for imprinting. After the characterization of the cryogel cartridges was carried out, the optimum adsorption conditions of both were determined according to the different parameters such as flow rate (0.5–2.5 ml/min), pH of the medium (4.0–8.0), initial Tyr concentration (0.1–3.0 mg/ml), and temperature (4–45°C). Selectivity experiments of Tyr-imprinted and non-imprinted cryogel cartridges were carried out by using phenylalanine, tryptophan, and cysteine. Besides, the eluted Tyr from MIP1 and MIP2 cryogel cartridge were applied to FPLC system. Also, the reusability experiments of Tyr-imprinted cryogel cartridges was observed no significant decrease in the adsorption capacity.     

Pilot-scale process for magnetic bead purification of antibodies directly from non-clarified CHO cell culture

High capacity magnetic protein A agarose beads, LOABeads PrtA, were used in the development of a new process for affinity purification of monoclonal antibodies (mAbs) from non-clarified CHO cell broth using a pilot-scale magnetic separator. The LOABeads had a maximum binding capacity of 65 mg/mL and an adsorption capacity of 25–42 mg IgG/mL bead in suspension for an IgG concentration of 1 to 8 g/L. Pilot-scale separation was initially tested in a mAb capture step from 26 L clarified harvest. Small-scale experiments showed that similar mAb adsorptions were obtained in cell broth containing 40 × 10⁶ cells/mL as in clarified supernatant. Two pilot-scale purification runs were then performed on non-clarified cell broth from fed-batch runs of 16 L, where a rapid mAb adsorption ≥96.6% was observed after 1 h. This process using 1 L of magnetic beads had an overall mAb yield of 86% and 16 times concentration factor. After this single protein A capture step, the mAb purity was similar to the one obtained by column chromatography, while the host cell protein content was very low, <10 ppm. Our results showed that this magnetic bead mAb purification process, using a dedicated pilot-scale separation device, was a highly efficient single step, which directly connected the culture to the downstream process without cell clarification. Purification of mAb directly from non-clarified cell broth without cell separation can provide significant savings in terms of resources, operation time, and equipment, compared to legacy procedure of cell separation followed by column chromatography step. © 2019 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2775, 2019.     

Production and characterization of anti-nisin Z monoclonal antibodies: suitability for distinguishing active from inactive forms through a competitive enzyme immunoassay

As a pre-requisite to monoclonal antibody development, an efficient purification strategy was devised that yielded 72 mg of nisin Z from 14.5 1 of Lactococcus lactis subsp. lactis biovar. diacetylactis UL 719 (L. diacetylactis UL719) culture in supplemented whey permeate. Specific monoclonal antibodies (mAbs) were produced in mice against the purified nisin Z using keyhole limpet hemocyanin as a carrier protein. These antibodies did not recognize nisin A, suggesting that the asparagine residue at position 27 is involved in antibody recognition to nisin Z. However, the high reactivity of mAbs against biologically inactive nisin Z degradation products, produced during storage of freeze-dried pure nisin Z at -70 degrees C, indicated that the dehydroalanine residue at position 5 (Dha5), required for biological activity, is not necessary in nisin Z recognition by the mAb. A competitive enzyme immunoassay (cEIA) using the specific anti-nisin Z mAb was developed and used for rapid and sensitive detection and quantification of nisin Z in fresh culture supernatant, milk and whey. Detection limits of 78 ng/ml in phosphate-buffered saline, 87 ng/ml in culture supernatant, 106 ng/ml in milk and 90.5 ng/ml in whey were obtained for this assay. The cEIA using specific mAbs can be used to quantify nisin Z in food products.     

Concurrent separation of catecholamines, dihydroxyphenylglycol, vasoactive intestinal peptide, and neuropeptide Y in superfusate and tissue extract

A method is described for separation and quantification of 3,4-dihydroxyphenylglycol (DO-PEG), norepinephrine (NE), dopamine (DA), vasoactive intestinal peptide (VIP), and neuropeptide Y (NPY) from single samples of tissue homogenate and from superfusate from in vitro dog blood vessel preparations using cartridges containing 0.4 g of octadecylsilane (Sep-Pak C-18). Samples were passed through the cartridge at pH 7.4. A step-gradient system was used to first selectively desorb the catechols (DOPEG, NE, DA) with a moderately polar eluent; subsequently VIP and NPY were eluted with 2.5 ml of a mixture of 1% trifluoroacetic acid, 80% acetonitrile. Five Sep-Pak catechol eluents were tested. Catechols were quantified by HPLC with electrochemical detection and peptides by radioimmunoassay. An HPLC solvent system is described which is particularly useful for chromatography of the more hydrophilic catechols DOPEG, 3,4-dihydroxymandelic acid, and 3,4-dihydroxyphenylalanine concurrently with catecholamines. For superfusion studies, sample cleanup time was reduced to about 4 min per sample by attachment of the cartridges directly to the bottom of the superfusion chamber. Superfusate was subsequently pulled through the cartridges immediately after they were passed over the tissue. Batches of 12 high-speed tissue supernates were processed through the method in about 30 min. The method was used to analyze DOPEG, NE, DA, VIP, and NPY in various rat and dog tissues. The values obtained were similar to values obtained previously by other methods. Because the catechols and peptides are separated from a single sample, the method has several advantages over those described previously; e.g., it is rapid, simple, and more sensitive.     

Expanded bed adsorption at production scale: Scale-up verification, process example and sanitization of column and adsorbent

Expanded bed adsorption is a technique for recovery of biomolecules directly from unclarified feedstocks. The work described here demonstrates that expanded bed adsorption is a scaleable technique. The methods used to test scaleability were “determination of degree of bed expansion”, “determination of axial dispersion” and “determination of protein breakthrough capacity”. The performance of a production scale expanded bed column with 600?mm diameter was tested using these methods and the results were found to be consistent with the results obtained from lab scale and pilot scale expanded bed columns. The scaleability and function of the expanded bed technique was also tested by performing a “process example”: a purification mimicking a real process using a yeast culture spiked with bovine serum albumin as feedstock. The results show that the 600?mm diameter production scale column was as efficient as a 25?mm diameter lab scale column in recovering bovine serum albumin from the unclarified yeast culture. The production scale runs were fully automated using a software controlled system containing an adaptor position sensor and an adsorbent sensor. A cleaning study was performed which showed that after use of a proper cleaning protocol, no surviving microorganisms could be detected in the column or in the adsorbent.     

A rapid method for the extraction and analysis of abscisic Acid from plant tissue

A simple, economical, and rapid method for the purification of plant extracts prior to abscisic acid (ABA) analysis is described. The method makes use of silica Sep-pak prepacked cartridges. The ABA extracts are loaded on to the Sep-pak cartridges which are then washed with a series of solvents resulting in the removal of pigments and other unwanted compounds. The ABA is then eluted from the cartridge and the levels of this hormone are estimated by gas chromatography. The whole technique (from maceration of the tissue to measurement of ABA levels) takes only 2 to 3 hours per sample.     

Semi-automated solid-phase extraction procedure for the high-performance liquid chromatographic determination of alinastine in biological fluids

A solid-phase extraction (SPE) method for sample clean-up followed by a reversed-phase HPLC procedure for the assay of alinastina (pINN) in biological fluids is reported. The effects of the sample pH, composition of the washing and elution solvents and the nature of the SPE cartridge on recovery were evaluated. The selectivity of SPE was examined using spiked rat urine and plasma samples and the CH and PH cartridges gave rise to the cleanest extracts. The recoveries obtained in spiked rat urine and plasma samples were 91.2±2.7 and 99.9±2.8%, respectively. The proposed SPE method coupled off-line with a reserved-phase HPLC system with fluorimetric detection was applied to the quantitation of alinastine in real rat urine samples. The analytical method was also applied and validated for the determination of alinastine in dog plasma. The recovery from spiked dog plasma samples using the PH cartridge was around 65%. The within-day and between-day precisions were 7 and 12%, respectively. The detection and quantitation limits in dog plasma were 0.024 and 0.078 μg/ml, respectively.     

Scale-down prediction of industrial scale pleated membrane cartridge performance

Flat‐sheet membrane discs represent the current standard format used for experimental prediction of the scale‐up of normal flow filtration processes. Use of this format is problematic, however, since the scale‐down results typically show a 40–55% difference in performance compared to large‐scale cartridges depending upon the feedstock used. In this work, novel pleated scale‐down devices (A_m = 1.51–15.1 × 10⁻³ m²) have been designed and fabricated. It is shown that these can more accurately predict the performance of industrial scale single‐use pleated membrane cartridges (A_m = 1.06 m²) commonly used within biopharmaceutical manufacture. The single‐use scale‐down cartridges retain the same pleat characteristics of the larger cartridges, but require a reduced feed volume by virtue of a substantially diminished number of active membrane pleats. In this study, a 1,000‐fold reduction in feed volume requirement for the scale‐down cartridge with the smallest membrane area was achieved. The scale‐down cartridges were tested both with clean water and a pepsin protein solution, showing flux‐time relationships within 10% of the large‐scale cartridge in both cases. Protein transmission levels were also in close agreement between the different scale cartridges. The similarity in performance of the scale‐down and the large‐scale cartridges, coupled with the low feed requirement, make such devices an excellent method by which rapid scale‐up can be achieved during early stage process development for biopharmaceutical products. This new approach is a significant improvement over using flat‐sheet discs as the quantitative similarity in performance with the large‐scale leads to reliable scale‐up predictions while requiring especially small volumes of feed material. Biotechnol. Bioeng. 2011; 108:830–838. © 2010 Wiley Periodicals, Inc.     

When consumer behavior dictates life cycle performance beyond the use phase: case study of inkjet cartridge end-of-life management

Purpose

Conventional wisdom suggests that product reuse can provide environmental savings. The purpose of this study is to first compare the environmental impacts of retail refilling and remanufactured inkjet cartridge alternatives to production of new inkjet cartridges, and then determine the extent to which consumer behavior can influence life cycle outcomes.

Methods

A life cycle inventory was developed for an inkjet cartridge with an integral print head using material composition data collected from cartridge disassembly and material processing, product manufacturing, and transportation inputs estimated from market data and the ecoinvent database in SimaPro 7.3. Although previous comparative life cycle assessment (LCA) studies for printer cartridges typically use “pages printed” or a variation thereof for the functional unit, “cartridge use cycles” is more suitable for examining reused inkjet cartridge alternatives that depend on the inkjet cartridge end-of-life (EOL) route chosen by the consumer. Since multiple reuse cycles achieved from refilling by a retailer was of specific interest, a functional unit defined in the form of “five use cycles” included the mode and manner in which consumers purchased inkjet cartridge use cycles.

Results and discussion

Cartridge refills present the lowest environmental impact, offering a 76 % savings in global warming potential (GWP) impact compared to production and purchase of a new inkjet cartridge alternative, followed by the remanufacturing case, which provided a 36 % savings in GWP impact compared to the new inkjet cartridge. However, results varied widely, even switching to favor new cartridge purchase, depending on how consumer transport was modeled, specifically the mode of travel, travel patterns (number of trips), and method of allocating impact to each trip.

Conclusions

Refilling an original equipment manufacturer (OEM) cartridge four consecutive times provides the best alternative for reducing environmental impact for those consumers that purchase inkjet cartridges one at a time. On the other hand, consumers that purchase multiple cartridges in a single trip to a retailer reduce environmental impact more by transport minimization than by refilling. Results reinforce the need for more comprehensive inclusion of consumer behavior when modeling life cycle environmental impact of product alternatives.     

Kinetic modeling as a tool to understand the influence of cell culture process parameters on the glycation of monoclonal antibody biotherapeutics

Glycation, the nonenzymatic reaction between the reducing sugar glucose and the primary amine residues on amino acid side chains, commonly occurs in the cell culture supernatant during production of therapeutic monoclonal antibodies (mAbs). While glycation has the potential to impact efficacy and pharmacokinetic properties for mAbs, the most common undesirable impact of glycation is on the distribution of charged species, often a release specification for commercial processes. Existing empirical approaches are usually insufficient to rationalize the effects of cell line and process changes on glycation. To address this gap, we developed a kinetic model for estimating mAb glycation levels during the cell culture process. The rate constant for glycation, including temperature and pH dependence, was estimated by fitting the kinetic model to time-course glycation data from bioreactors operated at different process settings that yielded a wide range of glycation values. The parameter values were further validated by independently estimating glycation rate constants using cell-free incubation studies at various temperatures. The model was applied to another mAb, by re-estimating the activation energy to account for effect of a glycation “hotspot”. The model was further utilized to study the role of temperature shift as an approach to reduce glycation levels in the manufacturing process for mAb2. While a downshift in temperature resulted in lowering of glycation levels for mAb2, the model helped elucidate that this effect was caused due to contribution from changes in glucose consumption, mAb secretion and temperature, instead of a direct impact of temperature alone on the kinetic rate of glycation.     

High voltage electron microscopy of the optic neuropile of the housefly,Musca domestica

Synaptic cartridges of the first optic neuropile (lamina ganglionaris) of the housefly were examined by high voltage electron microscopy (HVEM). Stereo pairs (from thick, i.e., 0.25 mum, sections viewed at 1,000 kV) provided a three dimensional representation of cartridge neurons and clearly revealed the lateral spread, bifurcation and some functional associations of Type I (L1, L2) monopolar interneurons. Slightly proximal to cartridge neck level, pairs of retinular (R) axons made contact with each other and it appeared that R processes projected through the cleft between the Type I interneurons. No junctional modifications were seen between contiguous R axon terminals. The speculation was made that functional contact might exist between neighboring R axons prior to their extensive synapses with principal first order interneurons. Such alleged coupling between R axons would account for several electrophysiological findings from other laboratories. Modifications in EM technique applicable for HVEM were detailed. The value of obtaining thick serial sections and the use of the HVEM in expediting three dimensional reconstructions of neuropile were demonstrated.     

Determination of clenbuterol in beef liver and muscle tissue using immunoaffinity chromatographic cleanup and liquid chromatography with ultraviolet absorbance detection

Clenbuterol, a beta-agonist, was determined in samples of beef liver and muscle. The method employed an acidic aqueous extraction followed by protein precipitation. The supernatant liquid was passed through a weak cation-exchange cartridge and then through a commercially available immunoaffinity cartridge. Clenbuterol was eluted from the immunoaffinity cartridge with 80% ethanol in water. The eluate was concentrated and analysed directly by reversed-phase liquid chromatography using gradient elution and UV detection at 245 nm. Detection limits were estimated to be 0.3 ng g⁻¹ clenbuterol. A single immunoaffinity cartridge was used for ten sample extracts with no significant loss in capacity. No organic solvents other than ethanol and methanol were employed in the procedure. Recoveries of clenbuterol from samples of beef liver and muscle spiked at 2 and 5 ng g⁻¹ carried through the entire procedure were 63±11% (range, 53–74%) compared to pure standards. Absolute recoveries of pure standards (30 ng clenbuterol) carried through the same analytical steps were 70±5% (n = 6), the losses being primarily due to the ion-exchange step.     

Two step capture and purification of IgG2 using multicolumn countercurrent solvent gradient purification (MCSGP)

A two‐step chromatography process for monoclonal antibody (mAb) purification from clarified cell culture supernatant (cCCS) was developed using cation exchange Multicolumn Countercurrent Solvent Gradient Purification (MCSGP) as a capture step. After an initial characterization of the cell culture supernatant the capture step was designed from a batch gradient elution chromatogram. A variety of chromatographic materials was screened for polishing of the MCSGP‐captured material in batch mode. Using multi‐modal anion exchange in bind‐elute mode, mAb was produced consistently within the purity specification. The benchmark was a state‐of‐the‐art 3‐step chromatographic process based on protein A, anion and cation exchange stationary phases. The performance of the developed 2‐step process was compared to this process in terms of purity, yield, productivity and buffer consumption. Finally, the potential of the MCSGP process was investigated by comparing its performance to that of a classical batch process that used the same stationary phase. Biotechnol. Bioeng. 2010;107: 974–984. © 2010 Wiley Periodicals, Inc.     

Investigation of prostaglandins in the culture supernatant of mononuclear cells and its influence on platelet aggregation.

The prostaglandins can be synthesized by many cells types. Cells of the immune system also metabolise arachidonic acid to prostaglandins. However, the specific class of immunocompetent cells that synthesize prostaglandins as well as the spectrum of arachidonic acid metabolides produced by these cells is not firmly established. The aim of our study was to investigate the behaviour of prostaglandins in the culture supernatant of mononuclear cells and the influence of this supernatant on platelet aggregation. Blood cells were separated from peripheral blood according to a modification of the procedure of B?yum. The level of prostaglandins was determined by means of radioimmunoassay kits. The PGF2 alpha concentrations were significantly higher in the culture supernatant (F) in comparison with supernatant (K) and (O). The supernatant of lymphocytes culture does not influence platelet aggregation. The highest concentrations of PGE1 and PGF2 alpha were noted at the 12 and 24 hours of the monocyte cultivation, however the lowest at the 36 and 48 hours. The supernatant obtained from monocyte cultivation at the 36 hours exert an independent effect on platelets aggregation, whereas at 24 and 48 hours it plays a role in platelet aggregation. The presented results may indicate the influence of monocytes on AA metabolism and platelet function.     

Production of recombinant human relaxin 3 in AtT20 cells

Relaxin 3 has been reported recently as a member of the insulin/IGF/relaxin family. To clarify the function of relaxin 3, we prepared recombinant human relaxin 3 using a mouse adrenocorticotrophic hormone (ACTH)-secreting cell line, AtT20. To detect a mature form of recombinant human relaxin 3, a competitive enzyme immunoassay (EIA) was developed using a monoclonal antibody (mAb; HK4-144-10), which was raised for the N-terminal peptide of human relaxin 3 A-chain. We detected immunoreactive (ir-) relaxin 3 in the culture supernatant of AtT20 cells stably transfected with human relaxin 3 cDNA. After treatment with 5 microM forskolin for 3 days, the concentration of the ir-relaxin 3 in the culture supernatant reached 12 nM. Ir-relaxin 3 was purified from the culture supernatant by a combination of various chromatographies. By analyses of N-terminal amino acid sequence and electrospray ionization mass spectrometry (ESI-MS), we confirmed that the purified material was a mature form of human relaxin 3. The recombinant human relaxin 3 thereby obtained increased intracellular cAMP production in THP-1 cells. Our results demonstrate that the expression of relaxin 3 cDNA in AtT20 cells is a useful tool to produce a bioactive and mature form of relaxin 3.     

Comparison of sample preparation methods for the high-performance liquid chromatographic analysis of cell culture extracts for triphosphate ribonucleosides and deoxyribonucleosides

We compared four different procedures for the purification and concentration of nucleoside triphosphates in cell extracts prior to HPLC analysis. Two methods involved precipitation, with either acetonitrile or calcium fluoride. The acetonitrile procedure yielded reasonable recovery and sufficient purity for the subsequent HPLC analysis. The calcium fluoride coprecipitation procedure gave both good recovery and purity; but the recovery was shown to be dependent on the concentration of the nucleoside triphosphates. The other two methods involved small Sep-Pak cartridges. The silica cartridge procedure yielded unfavorable recoveries in periodate-treated cell extracts, apparently due to poor solubility of nucleoside triphosphates in the requisite solvents. The strong anion exchange cartridge procedure yielded both good recovery and purity. This procedure was found to be fast, efficient, and reliable for purifying and concentrating nucleotides in cell extracts.     

Regulation of synaptic frequency: comparison of the effects of hypoinnervation with those of hyperinnervation in the fly's compound eye

At the anterior rim of the first optic neuropile, or lamina, of the housefly's (Musca domestica) compound eye, the terminals of photoreceptors (R) innervate postsynaptic neurons in variable numbers to provide a continuous range of natural hypo- and hyperinnervations. Frequencies of photoreceptor synapses have been measured from quantitative electron microscopy on single sections of the lamina's unit synaptic modules, called cartridges. These are normally innervated by six photoreceptor terminals (6R cartridges). At the lamina's edge hypoinnervated cartridges (2R-5R) are found, whereas hyperinnervated cartridges (7R, 8R) are located at the equator between dorsal and ventral eye halves. In 2R cartridges each presynaptic terminal forms up to 1.5 times the normal, 6R cartridge number of synapses, thereby offsetting the reduced number of terminals and partially conserving the input upon the postsynaptic neurons. Thus the terminals have a reserve synaptogenic capacity never normally revealed. By comparison, terminals in 8R cartridges form about the same numbers of synapses as in "normal" eye regions, so that their postsynaptic neurons have a synaptic input increased by the extra number of terminals. The number of synapses formed between input terminals and target neurons is therefore not fixed but changes as a function of the total receptor terminal complement. The size of a photoreceptor terminal covaries to a certain extent with the number of its presynaptic sites; the spacing density of presynaptic sites over the terminals' surface in a 2R cartridge compared with an 8R cartridge increases far less (only 17%) than the increase in the number of sites (43%). The pair of postsynaptic cell interneurons in each 2R cartridge also shows a decrease in axonal diameter compared with those in 8R cartridges. Thus both the pre- and postsynaptic cells show size changes correlated with changes in their synaptic engagement.