Recovery Of Protein Activity Research Articles

Convenient Partial Purification of Glucose Oxidase from <i>Aspergillus niger</i> A9 Fermentation Broth by Reversed Micelles

Aim of this work was to establish the optimum conditions for the extraction and recovery by cationic reversed micelles of glucose oxidase (GOX) from Aspergillus niger A9, The influence of pH, temperature, solvent/co-solvents ratio on the extraction was investigated by experiment, using the residual enzyme activity to evaluate the results. The best condition for GOX extraction were ensured using iso-octane as solvent and butanol and n-hexanol co-solvent at 76/18/6 volume ratio, pH 4.80, 200mM cetyl-trimethyl ammonium bromide (CTAB) as cationic surfactant, The enzyme activity of GOX is measured by DNS method (3,5-dinitro salicylic acid method). In the extraction process, ultrasonic oscillation was adopted to mix organic solvent and water, ultrasonic oscillation temperature is 45 °C. Protein activity recovery of GOX can reach 88.2% in extraction.

Improving the refolding of NTA protein by urea gradient and arginine gradient size-exclusion chromatography

Inclusion body refolding processes play a major role in the production of recombinant proteins. Improvement of the size-exclusion chromatography refolding process was achieved by combining a decreasing urea gradient with an increasing arginine gradient (two gradients) for the refolding of NTA protein (a new thrombolytic agent) in this paper. Different refolding methods and different operating conditions in two gradients gel filtration process were investigated with regard to increasing the NTA protein activity recovery and inhibition of aggregation. The refolding of denatured NTA protein showed this method could significantly increase the activity recovery of protein at high protein concentration. The activity recovery of 37% was obtained from the initial NTA protein concentration up to 20 mg/ml. The conclusions presented in this study could also be applied to the refolding of lysozyme.

Impact of critical process and formulation parameters affecting in‐process stability of lactate dehydrogenase during the secondary drying stage of lyophilization: A mini freeze dryer study

The stresses during the secondary-drying stage of lyophilization were investigated using a controlled humidity mini-freeze-dryer [Luthra S, Obert J-P, Kalonia DS, Pikal MJ. 2007. Investigation of drying stresses on proteins during lyophilization: Differentiation between primary and secondary-drying stresses on lactate dehydrogenase using a humidity controlled mini freeze-dryer. J Pharm Sci 96: 61-70.]. Lactate dehydrogenase (LDH), was formulated in: (1) Tween 80, (2) citrate buffer, and (3) both Tween 80 and citrate buffer. Protein activity recovery was measured as a function of relative humidity (RH), product temperature, and drying duration. Studies were also conducted with different concentrations of sucrose, sorbitol, and poly (vinyl pyrrolidone) (PVP). LDH stability was affected to a small extent by RH and significantly by drying temperature and duration. Complete stabilization of LDH was observed when lyophilized with sucrose and PVP but only a partial stabilization was observed with sorbitol. The mini-freeze-dryer enabled studying the process parameters independently, unlike a conventional study where these effects are generally convoluted. The results suggest that the stability of the protein is a function of the dynamics of the system during lyophilization. The origin of the stabilization effect of sucrose, which could, in principle, be attributed both to direct interaction with the protein or vitrification of the protein was elucidated using lyoprotectants that can either hydrogen bond well with the protein (sorbitol) or form a good glass (PVP). It appears both effects are required for complete stabilization of the protein.

Partially Crystalline Systems in Lyophilization: II. Withstanding Collapse at High Primary Drying Temperatures and Impact on Protein Activity Recovery

In an accompanying article we have described the construction of the water-rich sections of raffinose-glycine-water and trehalose-glycine-water state diagrams. In this study, we use the information obtained from the state diagrams to identify the minimum weight fraction of the crystalline component in glycine-carbohydrate systems necessary to withstand collapse at high primary drying temperatures. We also determine the impact of primary drying, substantially above T'g, on the recovery of lactate dehydrogenase (LDH) activity. Ambient and variable temperature X-ray powder diffractometry and differential scanning calorimetry were used to characterize the frozen and freeze-dried systems. Aqueous solutions with glycine to carbohydrate (raffinose pentahydrate or trehalose dihydrate) weight ratios ranging from 0.2 to 2.0 were freeze dried. The protein formulations contained 20 mM citrate buffer (pH 6.0) and LDH (20 microg/mL). A glycine to anhydrous raffinose weight ratio >or=1.18 and a glycine to anhydrous trehalose weight ratio >or=1.56 were necessary to withstand macroscopic collapse in the system, when the primary drying was carried out at a product temperature at least 10 degrees C above the T'g. The recovery of LDH activity was almost complete in the reconstituted lyophile whether the primary drying was carried out above T'g (-10 degrees C) or below T'g (-32 degrees C). Thus, by judiciously combining crystalline and amorphous components, it was possible to primary dry at temperatures substantially above the T'g.

Raffinose Crystallization During Freeze-Drying and Its Impact on Recovery of Protein Activity

To study i) phase transitions in raffinose solution in the frozen state and during freeze-drying and ii) evaluate the impact of raffinose crystallization on the recovery of protein activity in reconstituted lyophiles. X-ray powder diffractometry (XRD) and differential scanning calorimetry (DSC) were used to study the frozen aqueous solutions of raffinose pentahydrate. Phase transitions during primary and secondary drying were monitored by simulating the entire freeze-drying process, in situ, in the sample chamber of the diffractometer. The activity of lactate dehydrogenase (LDH) in reconstituted lyophiles was determined spectrophotometrically. Raffinose formed a kinetically stable amorphous freeze-concentrated phase when aqueous solutions were frozen at different cooling rates. When these solutions were subjected to primary drying without annealing, raffinose remained amorphous. Raffinose crystallized as the pentahydrate when the solutions were annealed at a shelf temperature of -10 degrees C. Primary drying of these annealed systems resulted in the dehydration of raffinose pentahydrate to an amorphous phase. The phase separation of the protein from the amorphous raffinose in these two systems during freeze-drying resulted in a significant reduction in the recovery of LDH activity, even though the lyophile was amorphous. Annealing of frozen aqueous raffinose solutions can result in solute crystallization, possibly as the pentahydrate. The crystalline pentahydrate dehydrates during primary drying to yield an amorphous lyophile. Raffinose crystallization during freeze-drying is accompanied by a significant loss of protein activity.

Affinity precipitation and macroaffinity ligand facilitated three-phase partitioning for refolding and simultaneous purification of urea-denatured pectinase.

Protein refolding is an integral step in the recovery of protein activity from inclusion bodies. It is shown that affinity precipitation and macroaffinity ligand facilitated three-phase partitioning (MLFTPP) led to refolding of urea-denatured pectinase present in a commercial preparation, with simultaneous purification. Affinity precipitation consists of precipitation of the desired enzyme by complexing it with a suitable stimulus-sensitive macroaffinity ligand. This ligand in this case was alginate/esterified alginate. The complex of the polymer-pectinase could be precipitated by adding calcium ions. In MLFTPP (carried out by adding tertiary butanol and ammonium sulfate to the aqueous solution of crude enzyme and the polymer), the polymer or its complex with the enzyme form an interfacial precipitate between tert-butyl alcohol phase and aqueous phase. It is believed that in both processes, while molecular recognition of alginate/esterified alginate to pectinase facilitates their selective binding to the enzyme, the correct refolding is facilitated by preventing molecular aggregation of unfolded enzyme molecules. Three-phase partitioning with esterified alginate as the macroaffinity ligand gave 100% recovery with 4-fold purification. Affinity precipitation with 1% alginate gave 52% yield with 18-fold purification. On the other hand, use of 0.5% esterified alginate gave only 7-fold purification but with 75% recovery of activity.

Effect of process conditions on recovery of protein activity after freezing and freeze-drying

The objective of this research was to gain a better understanding of the degree to which recovery of activity of model proteins after freeze-drying can be maximized by manipulation of freeze-dry process conditions in the absence of protective solutes. Catalase, β-galactosidase and lactate dehydrogenase (LDH) were used as model proteins. All of the three proteins exhibited a concentration-dependent loss of activity after freezing, with significantly higher recovery at higher concentration. The freezing method and the type of buffer were also important, with sodium phosphate buffer and freezing by immersion of vials in liquid nitrogen associated with the lowest recovery of activity. Differential scanning calorimetry was predictive of the onset of collapse during freeze-drying only for β-galactosidase. For the other proteins, either no T g′ transition was observed, or the apparent glass transition did not correlate with the microscopically-observed collapse temperature. The time course of activity loss for β-galactosidase and LDH was compared during freeze-drying under conditions which produced collapse of the dried matrix and conditions which produced retention of microstructure in the dried solid. Recovery of activity decreased continuously during primary drying, with no sharp drop in recovery of activity associated with the onset of collapse. The most important drying process variable affecting recovery of activity was residual moisture level, with a dramatic drop in activity recovery associated with residual moisture levels less than about 10%.