Protein liquid chromatographic analysis in biotechnology

Eliminating disulfide exchange during glutamyl endopeptidase digestion of native protein

Numerous advantages of using immobilized enzymes over free-solution protein digests have been cited in the literature. This investigation examines both the rate of hydrolysis and the extent of disulfide bond exchange in disulfide bridged dipeptide fragments formed during proteolysis of native protein. Glutamyl endopeptidase as both an immobilized enzyme and in free solution was used in these studies. It was found that extensive hydrolysis of insulin was achieved in 2 min with immobilized enzyme cartridges operated in the stopped-flow mode orders. This is orders of magnitude faster than was seen in free solution. Other advantages ranging from ease of use and reduction in sample size to the potential for automation were also noted with the immobilized enzyme cartridge. Normal free-solution proteolysis generally requires 12-24 h, based on the lower enzyme-to-substrate ratio in solution. A disturbing feature noted in these lengthy free-solution reactions was the tendency to form disulfide bridged peptide artifacts. This could lead to the erroneous conclusion that disulfide bonding in a sample was not that of the native protein. It is concluded that the advantage of immobilized enzymes over free-solution reactions will be most important in the pharmaceutical industry where proteolytic fragment "fingerprinting" of recombinant proteins is being used to confirm structure.

Rapid verification of disulfide linkages in recombinant human growth hormone by tandem column tryptic mapping

An automated tryptic mapping method was developed for characterization of disulfide linkages in recombinant human growth hormone (rhGH). The hormone was trypsin digested and the peptide fragments concentrated by eluting rhGH through an immobilized trypsin column and transferring the peptides directly to a reversed-phase liquid chromatography (RP-LC) column where they were collected. Reaction time was controlled by the flow-rate. Following tryptic digestion of a sample, the immobilized enzyme column was uncoupled from the flow train by a switching valve and the RP-LC column eluted with a solvent gradient ranging from 0.1% trifluoroacetic acid (TFA) with 1% acetonitrile (ACN) to ACN with 0.1% TFA and 5% water. This two-step mapping process was achieved within 2 h on both native and reduced rhGH samples. The chromatographic elution position and mass spectra matrix-assisted laser desorption ionization time-of-flight mass spectrometry of native rhGH and sulfur-containing peptides were determined with standards. Standards of the individual sulfhydryl (-SH) containing peptides and all possible disulfide linked peptides that could result from coupling the -SH peptides in disulfide linkages were obtained by synthesis and chromatographic purification. This approach allowed the chromatographic elution position of all possible mismatched disulfide containing peptides to be established and samples of rhGH to be examined for improper folding.

The stability of insulin in crystalline and amorphous solids: observation of greater stability for the amorphous form

PURPOSE

Generalizations based upon behavior of small molecules have established that a crystalline solid is generally much more stable toward chemical degradation than is the amorphous solid. This study examines the validity of this generalization for proteins using biosynthetic human insulin as the model protein.

METHODS

Amorphous insulin was prepared by freeze drying the supernate from a suspension of zinc insulin crystals adjusted to pH 7.1. Storage stability at 25 degrees C and 40 degrees C were compared for the freeze dried material, the dried suspended crystals, and the starting batch of crystals. Samples were equilibrated at selected relative humidities between zero and 75% to obtain samples at various water contents. Assays for dimer formation were performed by size exclusion HPLC and assays for deamidated product were carried out by reverse phase HPLC. Degradation was found to be linear in square root of time, and the slopes from % degradation vs. square root of time were used to define the rate constants for degradation. Differential scanning calorimetry (DSC) and Fourier-transform infrared spectroscopy (FTIR) were used to characterize the state of the protein in the solids.

RESULTS

As expected based upon previous results, the primary degradation pathways involve deamidation at the AsnA21 site and co-valent dimer formation, presumably involving the A-21 site. Contrary to expectations, amorphous insulin is far more stable than crystalline insulin under all conditions investigated. While increasing water content increases the rate of degradation of crystalline insulin, rate constants for degradation in the amorphous solid are essentially independent of water content up to the maximum water content studied (approximately 15%).

CONCLUSIONS

Based upon the FTIR and DSC data, both crystalline and amorphous insulin retain some higher order structure when dried, but the secondary structure is significantly perturbed from that characteristic of the native solution state. However, neither DSC nor FTIR data provide a clear interpretation of the difference in stability between the amorphous and crystalline solids. The mechanism responsible for the superior stability of amorphous insulin remains obscure.

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.