In this paper we demonstrate that it is possibile to express the human gene for α
1-PI in the filamentous fungus
A. niger as a secreted glycosylated protein with stability that is significantly improved in comparison with non-glycosylated recombinant protein from
E. coli. The secreted r-α
1-PI was characterized in comparison with pd-α
1-PI and its enzymatically deglycosylated version (de-pd-α
1-PI) used as the "
in-house" standards, as well as with non-glycosylated r-α
1-PI produced in
E. coli [
27].
A. niger strains have been already used as hosts for the production of other serine proteinase inhibitors. Mikosch et al. reported on the secretion of active human mucus proteinase inhibitor (antileukoproteinase), which is a 11.7 kDa non-glycosylated single chain protein stabilized by eight disulfide bonds [
16]. Later, MacKenzie et al. reported on an aberrant processing of bovine pancreatic trypsin inhibitor (known as aprotinin, a small polypeptide of 58 amino acid residues) secreted by
A. niger [
20]. However, to the best of our knowledge, our work shows for the first time that human α
1-PI, a complex glycoprotein of medium size (394 amino acid residues, ~50.3 kDa) and of significant therapeutic value, can be successfully produced in this system.
The expression of α
1-PI in
A. niger was designed to obtain the recombinant inhibitor in the secreted glycosylated form with enhanced yield. This was successfully achieved by fusion of the α
1-PI coding sequence downstream of the glucoamylase truncated gene (glaA
G2), under transcriptional control of the constitutively expressed glyceraldehydes-3-phosphate dehydrogenase (gpdA) promoter, according to the earlier established strategy [
14-
16]. The efficiency of protein production was evaluated by the level of expression by direct determination of the secreted r-α
1-PI in the supernatant during growth.
To minimize possible interactions of native fungal proteases with the target recombinant inhibitor during growth, the following changes were implemented: (a) a protease-deficient mutant D15#26 was used for transformation (instead of AB4-1), and (b) the pH of the supernatants was maintained above 7.0. Screening for the target protein was routinely assayed by ELISA, in a protocol recently developed by us for this purpose [
21]. However, given the subtle nature of α
1-PI and the challenge of producing this medium size inhibitor in its biologically active form, standard SDS-PAGE/Western blot analysis was also conducted to visualize evidence for degradation peptides. As an analytical tool, ELISA was utilized to quantify r-α
1-PI's production under various growth conditions. Maximum yields of r-α
1-PI achieved in shake-flask cultures were at 12 mg/L, after 96 hours of batch culture growth, which is comparable with those reported for other mammalian proteins (10 mg/L) that were obtained in
Aspergillus strains [
16,
17,
28]. Although these yields of r-α
1-PI appear to be lower than the yields we achieved in
E. coli (20 mg/L and 38 mg/L in raw extracts before purification), the protein obtained from
A. niger is significantly more stable than the non-glycosylated α
1-PI versions from
E. coli, as evaluated by SE-HPLC.
Furthermore, inhibitory activity of r-α
1-PI from
A. niger is significantly higher than that of non-glycosylated r-α
1-PI version from
E. coli, which tends to aggregate more rapidly, thereby losing its inhibitory activity. This is consistent with the previously reported data on activity and stability of r-α
1-PI's that were produced in other host systems [
8], thus confirming that low stability results in lower potency.
As was reported earlier for bovine pancreatic trypsin inhibitor [
20], the possibility for aberrant processing of the fusion protein by KEX2-like endoprotease may result in a mixture of target proteins differing at the N-terminus. Although this possibility was not evaluated for r-α
1-PI obtained from shake-flask cultures, the secreted r-α
1-PI had high inhibitory activity (not less than 75%) in this system, suggesting that r-α
1-PI was mostly processed correctly. Although a higher yield was mentioned for r-α
1-PI produced in a fermentor [
8], it related to a total r-α
1-PI that contained certain amounts of latent (inactive) and digested α
1-PI species. The optimization for a semi-large scale production of r-α
1-PI in a fermentor with all parameters controlled is currently under development [
29].
As the secreted protein, r-α
1-PI is glycosylated, and the SDS-PAGE and Western blot demonstrate that the electrophoretic mobility of r-α
1-PI from
A. niger is comparable with that of pd-α
1-PI standard. Together with the activity results and SE-HPLC data, it suggests a correct cleavage by KEX2-like site and an appropriate folding of the secreted protein. MALDI-MS data provide additional proof that the average molecular mass of the recombinant protein (~50,100 Da) is close to that observed for pd-α
1-PI (50,300 Da), and therefore, the sizes of glycans in both are comparable. Although the results of testing with PNGase F suggest that glycosylation is predominantly of N-type, more detailed glycan characterization could be of interest in view of the comprehensive glyco-proteomic analysis recently performed by Kolarich et al. [
25,
26] for native human α
1-PI.