In order to direct the persistent expression of recombinant human serum albumin (HSA) from the GAL10 promoter in the yeast Saccharomyces cerevisiae, we carried out periodic feeding of galactose during shake-flask cultures. Unexpectedly, the recombinant protein secreted was observed to undergo rapid degradation, which was apparently accelerated by carbon-source feeding. The extracellular degradation of HSA occurred even in the strain deficient in the major vacuolar proteases PrA and PrB, and in the strain lacking the acidic protease Yap3p (involved in the generation of HSA-truncated fragments). Interestingly, the degradation correlated closely with the acidification of extracellular pH and thus was significantly overcome either by buffering the culture medium above pH 5.0 or by adding amino acid-rich supplements to the culture medium, which could prevent the acidification of medium pH during cultivation. Addition of arginine or ammonium salt also substantially minimized the degradation of HSA, even without buffering. The extracellular degradation activity was not detected in the cell-free culture supernatant but was found to be associated with intact cells. The results of the present study strongly suggest that the HSA secreted in S. cerevisiae is highly susceptible to the pH-dependent proteolysis mediated by cell-bound protease(s) whose activity and expression are greatly affected by the composition of the medium.

The glyceraldehyde-3-phosphate dehydrogenase promoter, P(GAP), was employed to direct the constitutive expression of recombinant human serum albumin (HSA) in Hansenula polymorpha. A set of integration vectors containing the HSA cDNA under the control of P(GAP) was constructed and the elemental parameters affecting the expression of HSA from P(GAP) were analyzed. The presence of a 5'-untranslated region derived from the HSA cDNA and the integration of the expression vector into the GAP locus were shown to improve the expression of HSA under P(GAP). Glycerol supported a higher level of HSA expression from P(GAP) along with a higher cell density than either glucose or methanol. The growth at high glycerol concentrations up to 12% did not cause any significant repression of the cell growth. A high cell density culture, up to 83 g l(-1) dry cell weight with a HSA production of 550 mg l(-1), was obtained in less than 32 h of cultivation in a fed-batch fermentation employing intermittent feeding with 12% glycerol. The GAP promoter-based HSA expression system showed a higher specific production rate and required a much simpler fermentation process than the MOX promoter-based system, demonstrating that P(GAP) can be a practical alternative of the MOX promoter in the large-scale production of HSA from H. polymorpha.

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Production of D--hydroxyisobutyric acid (D-HIBA) from methacrylic acid (MA) was investigated using Candida rugosa IFO 0750 and its mutant. Cell growth decreased as the MA concentration increased and was inhibited at D-HIBA concentrations higher than 30 g/l. Optimal MA concentration for D-HIBA production was in the range of 10-20 g/l. It was also noted that cell growth and D-HIBA production were inhibited by higher concentrations of Na + , K + , and NH 4 + , which were required for pH control during cultivation. With a suitably designed feeding mode of MA, the parent strain produced 65 g/l of D-HIBA after 120 h of fed-batch cultivation, but molar conversion yield of D-HIBA was less than 40%. The mutant, unable to assimilate propionic acid, produced as high as 70 g/l of D-HIBA in the same culture period with a molar conversion yield of more than 70%.