The Saccharomyces cerevisiae phosphotyrosyl phosphatase activator proteins are required for a subset of the functions disrupted by protein phosphatase 2A mutations

In Saccharomyces cerevisiae, PTPA is encoded by two genes, YPA1 and YPA2. In order to examine the biological role of PTPA as potential regulator of protein phosphatase 2A (PP2A), we compared the phenotypes of the ypaDelta mutants with these of PP2A-deficient strains. While deletion of both YPA genes is lethal, deletion of YPA1 alone results in a phenotype resembling that of PP2A-deficient strains in specific aspects such as aberrant bud morphology, abnormal actin distribution, and similar growth defects under various growth conditions. These phenotypes were even more pronounced when YPA1 was deleted in a pph21Delta genetic background. Moreover, ypaDelta mutants are hypersensitive to nocodazole and show inappropriate mitotic spindle formation as previously described for mutants in the catalytic subunit of PP2A, suggesting that Ypa, like PP2A, has a function in mitotic spindle formation. These results are consistent with an in vivo role of Ypa as a regulator of PP2A. However, unlike a PP2A-deficient strain, ypaDelta mutants do not show a G2 arrest. Therefore, Ypa does not seem to play a role in the regulation of PP2A at this stage of the cell cycle. These results imply that Ypa regulates a specific subset of PP2A functions, possibly by controlling the subunit composition of PP2A.     

Involvement of distinct G-proteins, Gpa2 and Ras, in glucose- and intracellular acidification-induced cAMP signalling in the yeast Saccharomyces cerevisiae.

Adenylate cyclase activity in Saccharomyces cerevisiae is dependent on Ras proteins. Both addition of glucose to glucose-deprived (derepressed) cells and intracellular acidification trigger an increase in the cAMP level in vivo. We show that intracellular acidification, but not glucose, causes an increase in the GTP/GDP ratio on the Ras proteins independent of Cdc25 and Sdc25. Deletion of the GTPase-activating proteins Ira1 and Ira2, or expression of the RAS2(val19) allele, causes an enhanced GTP/GDP basal ratio and abolishes the intracellular acidification-induced increase. In the ira1Delta ira2Delta strain, intracellular acidification still triggers a cAMP increase. Glucose also did not cause an increase in the GTP/GDP ratio in a strain with reduced feedback inhibition of cAMP synthesis. Further investigation indicated that feedback inhibition by cAPK on cAMP synthesis acts independently of changes in the GTP/GDP ratio on Ras. Stimulation by glucose was dependent on the Galpha-protein Gpa2, whose deletion confers the typical phenotype associated with a reduced cAMP level: higher heat resistance, a higher level of trehalose and glycogen and elevated expression of STRE-controlled genes. However, the typical fluctuation in these characteristics during diauxic growth on glucose was still present. Overexpression of Ras2(val19) inhibited both the acidification- and glucose-induced cAMP increase even in a protein kinase A-attenuated strain. Our results suggest that intracellular acidification stimulates cAMP synthesis in vivo at least through activation of the Ras proteins, while glucose acts through the Gpa2 protein. Interaction of Ras2(val19) with adenylate cyclase apparently prevents its activation by both agonists.     

Isolation and characterization of novel bacterial strains exhibiting ligninolytic potential

Background

The number of biotransformations that use nicotinamide recycling systems is exponentially growing. For this reason one of the current challenges in biocatalysis is to develop and optimize more simple and efficient cofactor recycling systems. One promising approach to regenerate NAD⁺ pools is the use of NADH-oxidases that reduce oxygen to hydrogen peroxide while oxidizing NADH to NAD⁺. This class of enzymes may be applied to asymmetric reduction of prochiral substrates in order to obtain enantiopure compounds.

Results

The NADH-oxidase (NOX) presented here is a flavoenzyme which needs exogenous FAD or FMN to reach its maximum velocity. Interestingly, this enzyme is 6-fold hyperactivated by incubation at high temperatures (80°C) under limiting concentrations of flavin cofactor, a change that remains stable even at low temperatures (37°C). The hyperactivated form presented a high specific activity (37.5 U/mg) at low temperatures despite isolation from a thermophile source. Immobilization of NOX onto agarose activated with glyoxyl groups yielded the most stable enzyme preparation (6-fold more stable than the hyperactivated soluble enzyme). The immobilized derivative was able to be reactivated under physiological conditions after inactivation by high solvent concentrations. The inactivation/reactivation cycle could be repeated at least three times, recovering full NOX activity in all cases after the reactivation step. This immobilized catalyst is presented as a recycling partner for a thermophile alcohol dehydrogenase in order to perform the kinetic resolution secondary alcohols.

Conclusion

We have designed, developed and characterized a heterogeneous and robust biocatalyst which has been used as recycling partner in the kinetic resolution of rac-1-phenylethanol. The high stability along with its capability to be reactivated makes this biocatalyst highly re-useable for cofactor recycling in redox biotransformations.     

Bioproduction of p-Hydroxystyrene from Glucose by the Solvent-Tolerant Bacterium Pseudomonas putida S12 in a Two-Phase Water-Decanol Fermentation

Two solvent-tolerant Pseudomonas putida S12 strains, originally designed for phenol and p-coumarate production, were engineered for efficient production of p-hydroxystyrene from glucose. This was established by introduction of the genes pal and pdc encoding l-phenylalanine/l-tyrosine ammonia lyase and p-coumaric acid decarboxylase, respectively. These enzymes allow the conversion of the central metabolite l-tyrosine into p-hydroxystyrene, via p-coumarate. Degradation of the p-coumarate intermediate was prevented by inactivating the fcs gene encoding feruloyl-coenzyme A synthetase. The best-performing strain was selected and cultivated in the fed-batch mode, resulting in the formation of 4.5 mM p-hydroxystyrene at a yield of 6.7% (C-mol of p-hydroxystyrene per C-mol of glucose) and a maximum volumetric productivity of 0.4 mM h⁻¹. At this concentration, growth and production were completely halted due to the toxicity of p-hydroxystyrene. Product toxicity was overcome by the application of a second phase of 1-decanol to extract p-hydroxystyrene during fed-batch cultivation. This resulted in a twofold increase of the maximum volumetric productivity (0.75 mM h⁻¹) and a final total p-hydroxystyrene concentration of 21 mM, which is a fourfold improvement compared to the single-phase fed-batch cultivation. The final concentration of p-hydroxystyrene in the water phase was 1.2 mM, while a concentration of 147 mM (17.6 g liter⁻¹) was obtained in the 1-decanol phase. Thus, a P. putida S12 strain producing the low-value compound phenol was successfully altered for the production of the toxic value-added compound p-hydroxystyrene.The demand for so called “green” production of chemicals is rapidly increasing due to the declining availability of fossil fuels and the urgency to reduce CO₂ emissions (10, 30). However, this bioproduction may be hindered by the toxicity of the product of interest, such as substituted aromatics, to the production host (1, 2, 12, 29). One way to cope with this product toxicity is to deploy solvent-tolerant microorganisms as biocatalysts (5, 28). Of special interest among these solvent-tolerant hosts are Pseudomonas putida strains that have been engineered to produce a variety of compounds such as p-hydroxybenzoate (25, 33), p-coumarate (19), and (S)-styrene oxide (22). In our laboratory, we study and employ the solvent-tolerant P. putida S12. This strain is well suited for the production of substituted aromatic chemicals (18, 19, 33, 38) thanks to its extreme solvent tolerance (5, 35) and metabolic versatility toward aromatics (14, 16, 34).An example of an industrially relevant but extremely toxic aromatic is p-hydroxystyrene (4-vinyl phenol) (23). This compound is widely used as a monomer for the production of various polymers that are applied in resins, inks, elastomers, and coatings. Ben-Bassat et al. (2, 3, 23) reported p-hydroxystyrene production from glucose in Escherichia coli. In this strain, phenylalanine/tyrosine ammonia lyase (PAL/TAL; encoded by pal) from Rhodotorula glutinis and p-coumaric acid decarboxylase (PDC; encoded by pdc) from Lactobacillus plantarum were introduced for the conversion of l-tyrosine into p-hydroxystyrene via p-coumarate. The maximum concentration of p-hydroxystyrene was limited to 3.3 mM due to the toxicity of the product to the E. coli host (3, 23). To alleviate product toxicity, a two-phase fermentation with 2-undecanone as the extractant was performed. This approach resulted in a modest 14.2 mM p-hydroxystyrene in the organic phase and 0.5 mM p-hydroxystyrene in the water phase (2). Toxicity-related adverse effects on p-hydroxystyrene production may also be avoided by dividing the whole process into three stages: production of l-tyrosine from glucose by E. coli, conversion of l-tyrosine into p-coumarate by immobilized PAL-overexpressing E. coli cells, and chemical decarboxylation of p-coumarate into p-hydroxystyrene (29).In this report, we address and strongly enhance the bio-based production of p-hydroxystyrene from glucose by employing the solvent-tolerant P. putida S12 as a host. Previously, two strains, P. putida S12 C3 (19) and P. putida S12 TPL3 (38), have been constructed for the production of the l-tyrosine-derived aromatics p-coumarate and phenol, respectively. These strains were highly optimized for aromatics production, resulting in a heavily increased metabolic flux toward l-tyrosine. Therefore, they are suitable platform strains for the production of other l-tyrosine-derived aromatics (33). The bifunctional enzyme PAL/TAL (EC 4.3.1.25) from Rhodosporidium toruloides and the enzyme PDC (EC 4.1.1.-) from L. plantarum were introduced into these strains to allow the conversion of l-tyrosine into p-hydroxystyrene (Fig. ​(Fig.1).1). These minor modifications resulted in an efficient biocatalyst for the production of the value-added compound p-hydroxystyrene from glucose.Open in a separate windowFIG. 1.Schematic overview of the biochemical pathway for p-hydroxystyrene production. TAL, tyrosine ammonia lyase; FCS, feruloyl-coenzyme A synthetase. The cross indicates the disruption of fcs, disabling p-coumarate degradation.