muramidase and potassium-phosphate

The partition efficiency of the double-spaced coil for eccentric and toroidal coils on countercurrent chromatographic separation of proteins was evaluated using the small-scale cross-axis coil planet centrifuge (CPC) equipped with circular and elliptic cylindrical columns. Standard cytochrome c, myoglobin and lysozyme samples were used for separation with the 12.5% (w/w) polyethylene glycol 1000 and 12.5% (w/w) dibasic potassium phosphate system. In the circular column, the double-spaced eccentric coil yielded better peak resolution than the double-spaced toroidal coil, and the double-spaced eccentric coil yielded better peak resolution than the single-spaced eccentric coil. In the elliptic column, the double-spaced eccentric coil also produced better peak resolution than the double-spaced toroidal coil, but the single-spaced eccentric coil yielded better peak resolution than the double-spaced eccentric coil. The overall results indicated that the double-spaced eccentric coil for the circular column and the single-spaced eccentric coil for the elliptic column yielded better protein separation using the small-scale cross-axis CPC with aqueous two-phase solvent systems.

Topics: Centrifugation; Countercurrent Distribution; Cytochromes c; Muramidase; Myoglobin; Phosphates; Planets; Polyethylene Glycols; Potassium Compounds

Protein separation was performed using the high-speed countercurrent chromatograph (HSCCC) at both synchronous and nonsynchronous type-J planetary motions. The partition efficiency was evaluated with two different column configurations, eccentric coil and toroidal coil, on the separation of a set of stable protein samples including cytochrome C, myoglobin and lysozyme with a polymer phase system composed of 12.5% (w/w) polyethylene glycol 1000 and 12.5% (w/w) dibasic potassium phosphate. Better peak resolution was obtained by the eccentric coil than by the toroidal coil using either lower or upper phase as the mobile phase. The peak resolution was further improved using the eccentric coil by the nonsynchronous type-J planetary motion with the combination of 1066 rpm of column rotation and 1000 rpm of revolution.

Topics: Animals; Centrifugation; Countercurrent Distribution; Cytochromes c; Equipment Design; Humans; Motion; Muramidase; Myoglobin; Phosphates; Polyethylene Glycols; Polymers; Potassium Compounds; Proteins

Manufacturing high-value added biotech biopharmaceutical products (e.g. therapeutic proteins) requires quick-to-develop, GMP-compliant, easy-to-scale and cost effective preparatory chromatography technologies. In this work, we describe the construction and testing of a set of 5-mm inner diameter stainless steel toroidal columns for use on commercially available preparatory scale synchronous J-type counter-current chromatography (CCC) machinery. We used a 20.2m long column with an aqueous two-phase system containing 14% (w/w) PEG1000 and 14% (w/w) potassium phosphate at pH 7, and tested a sample loading of 5% column volume and a mobile phase flow rate of 20ml/min. We then satisfactorily demonstrated the potential for a weekly protein separation and preparation throughput of ca. 11g based on a normal weekly routine for separating a pair of model proteins by making five stacked injections on a single portion of stationary phase with no stripping. Compared to our previous 1.6mm bore PTFE toroidal column, the present columns enlarged the nominal column processing throughput by nearly 10. For an ideal model protein injection modality, we observed a scaling up factor of at least 21. The 2 scales of protein separation and purification steps were realized on the same commercial CCC device.

Topics: Countercurrent Distribution; Indicators and Reagents; Models, Theoretical; Muramidase; Myoglobin; Phosphates; Polyethylene Glycols; Potassium Compounds; Proteins; Stainless Steel

A new spiral column assembly for analytical separation by counter-current chromatography is described. The column is made from a plastic spiral tube support which has 12 interwoven spiral grooves. The PTFE tubing of 1.6mm ID was first flattened by extruding through a narrow slit and inserted into the grooves to make 5 spiral layers with about 60ml capacity. The performance of the spiral column assembly was tested with separation of three stable protein samples including cytochrome C, myoglobin and lysozyme in a polymer phase system composed of polyethylene glycol 1000 and dibasic potassium phosphate each at 12.5% (w/w) in water. At 2ml/min, three protein samples were well resolved in 1h. The separation time may be further shortened by application of higher revolution speed and flow rate by improving the strength of the spiral tube support in the future.

Topics: Countercurrent Distribution; Cytochromes c; Muramidase; Myoglobin; Phosphates; Polyethylene Glycols; Potassium Compounds

A new spiral tube assembly was designed to improve the column capacity and partition efficiency for protein separation. This spiral tube assembly has greater column capacity than the original tubing because of an increase in radial grooves from 4 to 12 to accommodate more spiral layers and 12 narrow spots instead of 4 in each circular loop to interrupt the laminar flow that causes sample band broadening. Standard PTFE tubing (1.6mm ID) and the modified flat-twisted tubing were used as the separation column. The performances of both assemblies were compared for separating three stable test proteins including cytochrome c, myoglobin, and lysozyme using a two phase aqueous-aqueous solvent system composed of polyethylene glycol 1000 (12.5% w/w) and dibasic potassium phosphate (12.5% w/w). All samples were run at 1, 2, 3, and 5mL/min at both 800rpm and 1000rpm. The separation of these three protein samples produced high stationary phase retentions at 1, 2, and 3mL/min, yet separated efficiently at 5mL/min in 40min. After comparing the separation efficiency in terms of the peak resolutions, theoretical plate numbers, and separation times, it was determined that the flat-twisted tubing was more effective in separating these protein samples. In order to validate the efficacy of this novel assembly, a mixture of five protein samples (cytochrome c, myoglobin, ovalbumin, lysozyme, and hemoglobin) were separated, under the optimal conditions established with these three protein samples, at 1mL/min with a revolution speed of 1000rpm. There were high stationary phase retentions of around 60%, with effective separations, demonstrating the efficiency of the flat-twisted spiral tube assembly. The separation time of 6h was a limitation but can potentially be shortened by improving the strength of the column that will permit an increase in revolution speed and flow rate. This novel spiral separation column will allow rapid and efficient separation of mixtures with high yield of the constituent components.

Topics: Countercurrent Distribution; Cytochromes c; Hemoglobins; Indicators and Reagents; Muramidase; Myoglobin; Ovalbumin; Phosphates; Polyethylene Glycols; Potassium Compounds; Proteins; Solvents; Water

The partitioning of model proteins (bovine serum albumin, ovalbumin, trypsin and lysozyme) was assayed in aqueous two-phase systems formed by a salt (potassium phosphate, sodium sulfate and ammonium sulfate) and a mixture of two polyethyleneglycols of different molecular mass. The ratio between the PEG masses in the mixtures was changed in order to obtain different polymer average molecular mass. The effect of polymer molecular mass and polydispersivity on the protein partition coefficient was studied. The relationship between the logarithm of the protein partition coefficient and the average molecular mass of the phase-forming polymer was found to depend on the polyethyleneglycol molecular mass, the salt type in the bottom phase and the molecular weight of the partitioned protein. The polymer polydispersivity proved to be a very useful tool to increase the separation between two proteins having similar isoelectrical point.

Topics: Algorithms; Ammonium Sulfate; Animals; Cattle; Chemical Fractionation; Chemical Phenomena; Chemistry, Physical; Molecular Weight; Muramidase; Ovalbumin; Phosphates; Polyethylene Glycols; Potassium Compounds; Proteins; Reproducibility of Results; Serum Albumin, Bovine; Sulfates; Trypsin

The effect of protein aggregates on the aggregation of D-glyceraldehyde-3-phosphate dehydrogenase (GAPDH) during unfolding and refolding has been studied. The aggregation of GAPDH follows a sigmoid course. The presence of protein aggregates increases the aggregation rate during unfolding and refolding of GAPDH but does not change the extent of aggregation and the final renaturation yield. It is suggested that protein aggregates function as seeds for aggregation via hydrophobic interaction with only GAPDH folding intermediates destined to aggregate and do not affect the distribution between pathways leading to correct folding and aggregation. Moreover, two different proteins do not interfere with each other during their simultaneous refolding together in a buffer. These findings provide insight into a mechanism by which cells prevent protein folding against the interference from aggregation of other proteins.

Topics: Animals; Cattle; Glutathione Disulfide; Glyceraldehyde-3-Phosphate Dehydrogenases; Guanidine; Hydrophobic and Hydrophilic Interactions; Muramidase; Muscles; Parasympathomimetics; Phosphates; Potassium Compounds; Protein Denaturation; Protein Disulfide-Isomerases; Protein Folding; Proteins; Rabbits; Serum Albumin, Bovine; Time Factors

The electrophoretic mobility of proteins was successfully determined by means of capillary electrophoresis (CE) with various background electrolytes (BGEs). The objective was focused on the variation in BGE physico-chemical composition and the consequential impact on the observed protein charge. Experimental and calculated mobilities, according to Henry's equation, versus ionic strength have been compared. For positively-charged lysozyme, a good agreement between observed and calculated mobilities was observed using triethanolamine chloride at pH 7.0 as the BGE. Mobility close to zero was shown using borate (pH 8.0) and phosphate (pH 7.0) at a low ionic strength of about 20 mmol l(-1), and as a consequence, specific adsorption of oxyanions was evidenced. Lysozyme retention in the case of reversed-phase high-performance liquid chromatography (RP-HPLC) was decreased by the presence of phosphate ions. CE and HPLC are complementary tools for characterizing the behaviour of lysozyme. On the other hand, the mobility of the negatively-charged alpha-lactalbumin remained constant as regards phosphate at pH 7.0 in the 20-200 mmol l(-1) range, contrary to the decrease that had been expected with the increasing ionic strength. beta-Lactoglobulin exhibited increasingly lower mobilities than those expected of boric acid/borate at pH 7.0 and 8.0 (I=20 mmol l(-1)).

Topics: Boric Acids; Chemical Phenomena; Chemistry, Physical; Electrochemistry; Electrolytes; Electrophoresis, Capillary; Hydrogen-Ion Concentration; Lactalbumin; Lactoglobulins; Muramidase; Osmolar Concentration; Phosphates; Potassium Compounds; Proteins

Proteins present in chicken egg white are separated by counter-current chromatography (CCC) in one step using a cross-axis coil planet centrifuge (X-axis CPC). The separation was performed with an aqueous polymer two-phase system composed of 16% (w/w) poly(ethylene glycol) 1000 and 12.5% (w/w) dibasic potassium phosphate by eluting the lower phase at a flow-rate of 1.0 ml/min. From about 20 g of the crude egg white solution, lysozyme, ovalbumin, and ovotransferrin were resolved within 5.5 h. Each component was identified by 12% SDS gel electrophoresis with Coomassie brilliant blue staining.

Topics: Animals; Buffers; Centrifugation; Chickens; Chromatography; Conalbumin; Egg White; Electrophoresis, Polyacrylamide Gel; Muramidase; Ovalbumin; Phosphates; Polyethylene Glycols; Potassium Compounds