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A Strancar

Publications and source records attributed to A Strancar.

16 recordsLinked to original sources
PubMed2006

Fast and efficient separation of immunoglobulin M from immunoglobulin G using short monolithic columns.

Certain diagnostic, analytical and preparative applications require the separation of immunoglobulin G (IgG) from immunoglobulin M (IgM). In the present work, different ion-exchange methacrylate monoliths were tested for the separation of IgG and IgM. The strong anion-exchange column had the highest dynamic binding capacity reaching more than 20mg of IgM/ml of support. Additionally, separation of IgM from human serum albumin, a common contaminant in immunoglobulin purification, was achieved on the weak ethylenediamino anion-exchange column, which set the basis for the IgM purification method developed on convective interaction media (CIM) supports. Experiments also confirmed flow independent characteristics of the short monolithic columns.

Chromatography, High Pressure Liquid↗
PubMed2005

Characterisation of metal-chelate methacrylate monoliths.

Monoliths are attractive stationary phases for purification of large biomolecules like proteins because of their flow-unaffected properties. Isolation of histidine containing proteins to high purity can be efficiently performed using metal-chelate interactions within a single chromatographic step. In this work, we investigated properties of commercial metal-chelate methacrylate monoliths-Convective Interaction Media (CIM). Analytical CIM disk monolithic columns and CIM 8 ml monolithic columns were used for purification of tumor necrosis factor-alpha (TNF-alpha) analog LK-801 and green fluorescence protein with 6 histidine tag (GFP-6His). In both cases, purity over 90% was achieved. Dynamic binding capacity at 10% of breakthrough was around 17-18 mg/ml for LK-801 and around 30 mg/ml for GFP-6His. Adsorption isotherm revealed that the maximal capacity is achieved at protein concentration above 60 microg/ml. Dynamic binding capacity and resolution were found to be flow unaffected.

Adsorption↗
PubMed2004

Large-scale methacrylate monolithic columns: design and properties.

Monoliths represent a special class of chromatographic supports. In contrast to other stationary phases, they consist of a single piece of highly porous material through which a sample is mainly transported by convection. As a consequence, monoliths enable fast separations and exhibit flow-unaffected properties, which make them attractive for purification of macromolecules like proteins or DNA. In this work, methacrylate-based monolithic columns with the bed volume up to 8000 ml are characterized. They perform high-resolution separations of several hundreds of grams of proteins per hour by utilizing liter per minute flow rates. They are incompressible under these operating conditions and resistant to strong alkaline conditions.

Animals↗
PubMed2003

Transfer of gradient chromatographic methods for protein separation to Convective Interaction Media monolithic columns.

Convective Interaction Media (CIM) columns are monolithic columns optimized for the separation of macromolecules. Some of them operate in the axial mode while others operate in the radial mode depending on the column size. In this work we tested the approach suggested by Yamamoto [Biotechnol. Bioeng., 48 (1995) 444] for transfer of gradient methods between columns of different size. A simplified equation for transfer was derived together with a criterion for its application. Separation was evaluated for a standard protein mixture and peroxidase enzymes present in fermentation broth. Salt and pH gradients were applied. Similar resolutions were obtained for each sample on all columns which demonstrates that the proposed approach can be successfully used for method scale-up on this type of column.

Chromatography, Ion Exchange↗
PubMed2003

Application of semi-industrial monolithic columns for downstream processing of clotting factor IX.

It has been shown in a previous study that monolithic columns can be used for downstream processing of different concentrates of clotting factor IX [K. Branović et al., J. Chromatogr. A 903 (2000) 21]. This paper demonstrates that such supports are useful tools also at an early stage of the purification process of factor IX from human plasma. Starting with the eluate after solid-phase extraction with DEAE-Sephadex, the use of monolithic columns has allowed much better purification than that achieved with conventional anion-exchange supports. The period of time required for separation is also much reduced. In up-scaling experiments, separations are carried out with 8, 80 and 500 ml columns. A volume of 1830 ml of DEAE-Sephadex eluate, containing a total of 27.6 g of protein and 48500 IU of factor IX is applied to the 500 ml monolithic column. This corresponds to a separation on a pilot scale. The results of this separation after up-scaling are comparable to those obtained with the 8 ml column on a laboratory scale.

Chromatography, Liquid↗
PubMed2002

Very fast analysis of impurities in immunoglobulin concentrates using conjoint liquid chromatography on short monolithic disks.

Transferrin and albumin are often present in immunoglobulin G (IgG) concentrates and are considered as impurities. Therefore, it is important to determine their concentration in order to obtain a well-characterized biological product. Here, we describe their determination based on conjoint liquid chromatography (CLC). The established method combines two different chromatographic modes in one step: affinity and ion-exchange chromatography (IEC) combined in one column. Therefore, two CIM Protein G and one CIM quaternary amine (QA) monolithic disks were placed in series in one housing forming a CLC monolithic column. Binding conditions were optimized in a way that immunoglobulins were captured on the CIM Protein G disks, while transferrin and albumin were bound on the CIM QA disks. Subsequently, transferrin and albumin were eluted separately by a stepwise gradient with sodium chloride, whereas immunoglobulins were released from the Protein G ligands by applying low pH. A complete separation of all three proteins was achieved in less than 5 min. The method permits the quantification of albumin and transferrin in IgG concentrates and has been successfully validated.

Amines↗
PubMed2000

Construction of large-volume monolithic columns.

Monolithic supports have become the subject of extensive study in the past years. Despite their advantageous features and many successful chromatographic applications in the analytical scale, only a very few examples of larger volume monoliths were described. In the case of GMA-EDMA monoliths, this can be attributed to the fact that due to the exothermic polymerization a pronounced temperature increase inside the monolith significantly affects the structure. The temperature increase depends on the thickness of the monolith, and consequently, there is an upper limit that allows the preparation of a unit with a uniform structure. In the present work, we have analyzed a heat release during the polymerization and have derived a mathematical model for the prediction of the maximal thickness of the monolithic annulus having a uniform structure. On the basis of the calculations, two annuluses of different diameters were polymerized and merged into a single monolithic unit with a volume of 80 mL. In addition, a special housing was designed to provide a uniform flow distribution in the radial direction over the entire monolith bed. It was shown that such a monolithic column exhibits flow-independent separation efficiency and dynamic binding capacity up to flow rates higher than 100 mL/min. The separation and loading times are in the range of a few minutes. The pressure drop on the column is linearly dependent on the flow rate and does not exceed 2.5 MPa at a flow rate of 250 ml/min.

Journal Article↗
PubMed2000

Application of monoliths for downstream processing of clotting factor IX.

In this paper, the application of monolithic columns for downstream processing of different clotting factor IX concentrates is shown. Determination of basic chromatographic conditions as well as investigations on the regeneration of disk- and tube-shaped monolithic columns using human serum albumin as a model protein, were performed. Separation of factor IX and vitronectin, a possible impurity in commercial factor IX concentrates was accomplished using disk-shaped monolithic columns. These same applications were also carried out with identical results on up-scaled tube-shaped monolithic columns. Since these media allow very fast separations, this method can be successfully applied not only to an in-process control of the purification of factor IX but also to other biopolymers from human plasma. Besides, the same application on the up-scaled tube-shaped monolithic column was successfully carried out.

Biopolymers↗
PubMed2000

Application of Convective Interaction Media (CIM) disk monolithic columns for fast separation and monitoring of organic acids.

The separation of organic acids on the anion-exchange monolithic support, commercially available as Convective Interaction Media (CIM), is presented in this study. It is demonstrated that citric, isocitric, pyruvic, fumaric, malic, and alpha-ketoglutaric acid can be successfully separated using a CIM monolithic column of suitable user-adjustable length. The effect of the mobile phase composition on the separation is investigated. CIM monolithic columns of adjustable length from 3 to 18 mm are compared regarding the resolution and the back pressure. It is shown that the CIM monolithic column of 12 mm in length enables a good separation of all six organic acids within 3 min and exhibits a linear dependence of back pressure versus flow rate. The resolution and the dynamic binding capacity are found to be flow-unaffected. A filtrated sample of bioprocess supernatant is analyzed without previous pretreatment, which indicates the possibility of online monitoring of small molecules during the bioprocess using CIM monolithic columns.

Journal Article↗
PubMed1998

Use of compact, porous units with immobilized ligands with high molecular masses in affinity chromatography and enzymatic conversion of substrates with high and low molecular masses.

Different ligands with high molecular masses are immobilized on compact, porous separation units and used for affinity chromatography. In subsequent experiments different enzymes are immobilized and used for converting substrates with low and high molecular masses. Disk or tube with immobilized concanavalin A (ConA) are used as model systems for lectin affinity chromatography. The enzyme glucose oxidase is used as a standard protein to test the ConA units. Subsequently glycoproteins from plasma membranes of rat liver are separated, using units with immobilized ConA. The enzyme dipeptidyl peptidase i.v., which is used as a model protein in the experiments, is enriched about 40-fold in a single step, with a yield of over 90%. The results are only slightly better than those obtained with ConA when it is immobilized on bulk supports. The important improvement lies in the reduction of separation time to only 1 h. Experiments concerning the isolation of monoclonal antibodies against clotting factor VIII (FVIII) are carried out on disks, combining anion-exchange chromatography and protein A affinity chromatography as a model for multidimensional chromatography. Both IgG (bound to the protein A disk) and accompanying proteins (bound to the anion-exchange disk) from mouse ascites fluid are retarded and eluted separately. With the immobilized enzymes invertase and glucose oxidase (GOX) the corresponding substrates with low molecular masses, saccharose and glucose, are converted. It is shown that the amount of immobilized enzyme and the concentration of the substrate are responsible for the extent of the conversion, whereas the flow-rates used in the experiments have no effect at all. The influence of immobilization chemistry was investigated with GOX. Indirect immobilization with ConA as spacer proved to be the best alternative. With trypsin, immobilized on a disk, substrates with high molecular masses are digested in flow-through. For optimal digestion the proteins have to be denatured in the buffer for sodium dodecyl sulfate-polyacrlyamide gel electrophoresis prior to application. In contrast to the conversion of substrates with low molecular masses, flow-rates play an important part in conversion of substrates with high molecular masses. With lower flow-rates a higher degree of digestion is achieved.

Animals↗
PubMed1997

Issues in the development of medical products based on human plasma.

Product development and process validation are shown in the case of several products obtained from human plasma. These are virus-inactivated plasma, intravenous immunoglobulins and the clotting factors VIII and IX. Different analytical methods are presented, which are used for product control and in-process control. For the production of virus-inactivated human plasma a down-scale protocol is presented, allowing a simulation of the production on a laboratory scale. Virus validation has shown that the reduction of transfusion-relevant viruses in the process was higher than six log steps. Determination of leachables from the RP-column, which was used in this production, proved that they appear in the final product in quantities below the detection limits only. It was also shown that the chemicals used for virus inactivation could be quantitatively removed from the product. For the isolation of other products, here intravenous gamma globulins and the clotting factors VIII and IX, similar validation steps had to be taken. In the case of clotting factor VIII the following data were determined, the reduction of viruses, the amount of leachables from the column, the residues of chemicals from the solvent/detergent treatment for virus inactivation. Virus reduction was successfully performed as well as the removal of chemicals used for virus inactivation. The amount of leachables from the columns used for chromatographic purification was found to be far below the permissible levels.

Biological Products↗
PubMed1997

Application of compact porous tubes for preparative isolation of clotting factor VIII from human plasma.

Membranes as well as compact porous disks are successfully used for fast analytical separations of biopolymers. So far, technical difficulties have prevented the proper scaling-up of the processes and the use of membranes and compact disks for preparative separations in a large scale. In this paper, the use of a compact porous tube for fast preparative separations of proteins is shown as a possible solution to these problems. The units have yielded good results, in terms of performance and speed of separation. The application of compact porous tubes for the preparative isolation of clotting factor VIII from human plasma shows that this method can even be used for the separation of very sensitive biopolymers. As far as yield and purity of the isolated proteins are concerned, the method was comparable to preparative column chromatography. The period of time required for separation was five times shorter than with corresponding column chromatographic methods. Compact porous disks made of the same support material can also be used for in-process analysis in order to control the separation. The quick response, which is obtained from these units within 5 to 60 s, allows close monitoring of the purification process.

Chromatography, High Pressure Liquid↗
PubMed1994

Purification of factor VIII and von Willebrand factor from human plasma by anion-exchange chromatography.

Factor VIII (anti-hemophilia A factor) is isolated from human plasma. Purification is carried out by a combination of precipitation and chromatographic procedures. After precipitation, the first step in virus inactivation is achieved through the effect of a non-ionic detergent such as Tween 80, and a solvent, e.g. tri-n-butylphosphate (TnBP). By subsequent anion-exchange chromatography, a highly enriched product is isolated, consisting of a complex formed by factor VIII and von Willebrand factor (FVIII-vWF). This treatment also removes the virus-inactivating reagents to quantities in the low ppm range. The second step in virus inactivation is aimed specifically at the non-enveloped viruses and consists of pasteurization at temperatures higher than 60 degrees C for 10 h. Through the addition of stabilizers, between 80% and 90% of the initial activity of FVIII is preserved during the modified pasteurisation. Along with the possibly denatured proteins the stabilizers, such as sugars, amino acids and bivalent cations, are subsequently removed by ion-exchange chromatography. The two-fold virus inactivation, by solvent/detergent treatment and subsequent pasteurisation, allows the destruction of both lipid-enveloped and non-enveloped viruses. During the procedure FVIII is stabilized through the high content of vWF. The complex consisting of FVIII and vWF can be dissociated by adding calcium ions. Subsequently both glycoproteins from this complex are separated from one another by further anion-exchange chromatography.

Biocompatible Materials↗
PubMed1994

Application of high-performance membrane chromatography for separation of annexins from the plasma membranes of liver and isolation of monospecific polyclonal antibodies.

The separation of annexins, calcium-binding plasma membrane-associated proteins from rat liver and Morris hepatoma 7777 by high-performance membrane chromatography (HPMC) is described. The annexins with low molecular masses, CBP 33 and CBP 35, and the annexin with a high molecular mass, CBP 65/67, can be separated within 10 min from one another by anion-exchange HPMC under non-denaturing conditions. The separation devices used consist of compact, porous disks (QuickDisk) on the one hand and of bundled membranes made of cellulose fibers (MemSep) on the other. Both have been found to be equally well suited for this separation. The annexins obtained in this way are subsequently bound to epoxy-activated porons disks and used for the separation of monospecific polyclonal antibodies against the annexin CBP 65/67.

Animals↗
PubMed1994

Extraction of Triton X-100 and its determination in virus-inactivated human plasma by the solvent--detergent method.

For inactivation of lipid-enveloped viruses during the production of fresh frozen and lyophilized human plasma, the solvent-detergent method was applied. In this process, the solvent tri-n-butyl phosphate is removed by extraction with castor oil. The removal of the non-ionic detergent Triton X-100 is performed by solid-phase extraction using reversed-phase supports. For this purpose, different polymer- and silica-based supports were tested. The highest capacity for Triton X-100 was achieved with C18 silica gels. These supports can bind more than 0.1 ml of Triton X-100 per ml of support. None of the proteins, e.g., clotting factors, bind to the support and therefore they pass through the column and their biological activity is hardly affected. The determination of detergent during the production process was also studied. The application of special columns allowing direct sample injection was introduced. This is a simple method for the rapid in-process determination of Triton X-100 in human plasma by reversed-phase chromatography under isocratic conditions. Using the method developed here, less than 1.0 ppm of Triton X-100 can be detected in less than 12 min without any sample pretreatment.

Blood↗