Some factors influencing the proportion of periplasmic hepatitisB virus pre-S2 antigen in the recombinant yeastHansenula polymorpha

Summary A central composite design (CCD) was used to evaluate, for the purpose of future process optimization, the influence of pH, yeast extract and ammonium chloride concentrations on the proportion of periplasmic hepatitisB pre-S2 antigen in the recombinant yeastHansenula polymorpha. Each factor was tested at five levels, and a second order polynomial model for the proportion of periplasmic antigen was fitted to the treatment combinations. pH showed the greatest effect: the proportion of periplasmic antigen was greatly increased at the higher pH levels. At the higher pH levels used, the proportion of periplasmic antigen was enhanced by a high concentration of ammonium chloride. Additional experiments have confirmed both the validity of the selected model and the optimal conditions found. A significant correlation was found between the proportion of periplasmic antigen and the total yield of antigen. These results indicated that is should be possible to modulate the distribution of the pre-S2 antigen between the periplasm and the cytoplasm of the yeast.     

Influence of pH,nitrogen and phosphorus sources on the production of hepatitis B virus pre-S2 antigen by Hansenula polymorpha

Experimental design techniques were used to study the influence of the composition of the culture medium on the production of hepatitis B virus pre-S2 antigen by the methylotrophic yeast Hansenula polymorpha. pH, phosphoric acid, ammonium chloride and yeast extract concentrations were selected as experimental factors and their influence was investigated using Central Composite design techniques. The results indicated that antigen yield was maximized at high pH and in a culture medium containing both ammonium chloride and yeast extract. Phosphoric acid was found to have a detrimental effect on antigen production. This study allowed a 50% increase in antigen production in a medium in which the yeast extract cocentration was decreased to 32 g/1. These optimal conditions have been confirmed with an octagonal design experiment. Moreover, it was shown that the antigen produced was very stable up to at least 8 days after induction and that the yeast extract concentration could be lowered to 22 g/1 without apprciable effect on antigen yield. The increase in antigen production was not due to an increase in cell biomass, since no correlation could be found between these two parameters. The newly defined culture medium should allow a greatly increased antigen production at the fermentor level, at a lower cost and with minimal operational problems.Correspondence to: D. Groleau     

Mitochondrial activity of 2,6-diaminopurine in Saccharomyces cerevisiae.

Summary 2,6-diaminpurine (DAP) selectively inhibited mitochondrial protein synthesis in yeast cells with concomitant failure of cells to grow in non-fermentable (yeast extract, glycerol) medium. The selectivity was pronounced in all strains tested (15) nearly all of which were able to grow in yeast extract, glucose medium containing 5 mg/ml DAP (maximum solubility) whereas growth was arrested in all strains at 250–500 g/ml DAP in the glycerol medium. The inhibition was reversed by further addition of adenine to the culture medium. RNA synthesis in rat liver mitochondria was depressed by DAP suggesting that the analogue affected RNA polymerase activity.There was no evidence of nuclear mutagenicity by DAP but resistance to the antibiotics chloramphenicol and oligomycin was induced by the drug. Genetic evidence, although limited, indicated that the resistance mutations were cytoplasmic. The mitochondrial petite mutation was also induced by DAP but only at comparatively high concentrations. The mutagenic effects were seen only in the glycerol medium.     

Targeting sequences of the two major peroxisomal proteins in the methylotrophic yeast Hansenula polymorpha.

Summary Dihydroxyacetone synthase (DAS) and methanol oxidase (MOX) are the major enzyme constituents of the peroxisomal matrix in the methylotrophic yeast Hansenula polymorpha when grown on methanol as a sole carbon source. In order to characterize their topogenic signals the localization of truncated polypeptides and hybrid proteins was analysed in transformed yeast cells by subcellular fractionation and electron microscopy. The C-terminal part of DAS, when fused to the bacterial -lactamase or mouse dihydrofolate reductase, directed these hybrid polypeptides to the peroxisome compartment. The targeting signal was further delimited to the extreme C-terminus, comprising the sequence N-K-L-COOH, similar to the recently identified and widely distributed peroxisomal targeting signal (PTS) S-K-L-COOH in firefly luciferase. By an identical approach, the extreme C-terminus of MOX, comprising the tripeptide A-R-F-COOH, was shown to be the PTS of this protein. Furthermore, on fusion of a C-terminal sequence from firefly luciferase including the PTS, -lactamase was also imported into the peroxisomes of H. polymorpha. We conclude that, besides the conserved PTS (or described variants), other amino acid sequences with this function have evolved in nature.     

Process development in Hansenula polymorpha and Arxula adeninivorans, a re-assessment

A range of industrial H. polymorpha-based processes exist, most of them for the production of pharmaceuticals. The established industrial processes lean on the use of promoters derived from MOX and FMD, genes of the methanol metabolism pathway. In Hansenula polymorpha these promoters are de-repressed upon depletion of a range of carbon sources like glucose and glycerol instead of being induced by methanol as reported for other methylotrophs. Due to these characteristics screening and fermentation modes have been defined for strains harbouring such expression control elements that lean on a limited supplementation of glycerol or glucose to a culture medium. For fermentation of H. polymorpha a synthetic minimal medium (SYN6) has been developed. No industrial processes have been developed so far based on Arxula adeninivorans and only a limited range of strong promoter elements exists, suitable for heterologous gene expression. SYN6 originally designed for H. polymorpha provided a suitable basis for the initial definition of fermentation conditions for this dimorphic yeast. Characteristics like osmo- and thermotolerance can be addressed for the definition of culture conditions.     

Cytochemical studies on the localization of methanol oxidase and other oxidases in peroxisomes of methanol-grown Hansenula polymorpha

The localization of methanol oxidase activity in cells of methanol-limited chemostat cultures of the yeast Hansenula polymorpha has been studied with different cytochemical staining techniques. The methods were based on enzymatic or chemical trapping of the hydrogen peroxide produced by the enzyme during aerobic incubations of whole cells in methanol-containing media. The results showed that methanol-dependent hydrogen peroxide production in either fixed or unfixed cells exclusively occurred in peroxisomes, which characteristically develop during growth of this yeast on methanol. Apart from methanol oxidase and catalase, the typical peroxisomal enzymes d-aminoacid oxidase and l--hydroxyacid oxidase were also found to be located in the peroxisomes. Urate oxidase was not detected in these organelles. Phase-contrast microscopy of living cells revealed the occurrence of peroxisomes which were cubic of form. This unusual shape was also observed in thin sections examined by electron microscopy. The contents of the peroxisomes showed, after various fixation procedures, a completely crystalline or striated substructure. It is suggested that this substructure might represent the in vivo organization structure of the peroxisomal enzymes.     

Fermentation conditions for efficient production of thermophilic protease in Escherichia coli harboring a plasmid

Escherichia coli TG1, transformed with an expression plasmid pAQN carrying the aqualysin I (AQI) gene derived from Thermus aquaticus YT-1 under the control of the tac promoter, was cultivated under various conditions in order to find fermentation conditions for the efficient production of the thermophilic protease, AQI. The amount of AQI produced was closely related to the growth phase at the time of isopropyl--d-thiogalactopyranoside (IPTG) induction, and the highest production was obtained when it was added during the exponential growth phase. The addition of yeast extract had a greater effect on AQI production than did Polypeptone or casamino acids, and AQI productivity increased from 1.1 × 10³ kU/g to 2.7 × 10³ kU/g cells when 2 g/l yeast extract was supplied. Furthermore, the specific growth rate improved from 0.35 h^–1 to 0.89 h^–1 when 5 g/l yeast extract was supplied. The culture temperature also affected AQI gene expression. When the temperature was shifted from 37°C to 34°C at the time of IPTG induction, 19 kU/ml enzymatically active AQI was obtained, corresponding to a 28% increase over the amount produced in a batch culture without a shift. This is about a 44-fold higher yield than was obtained from the original strain, T. aquaticus YT-1.     

Extracellular protein release and its response to pH level in Saccharomyces cerevisiae

Saccharomyces cerevisiae grown in batch culture at pH 5.5 releases 0.1 to 0.2 pg protein per cell to the external medium over a period of four to five days, final concentration 20–40 g/ml. Cells grown at pH 3.0 release 10-fold this quantity (1–2 pg/cell, final concentration 100–200 g/ml). A kinetic model based on published behavior of periplasmic protein gave a good fit to the observed kinetics of exoprotein yield. The electrophoretic pattern of exoprotein differed from that of cell lysate protein, and exoprotein synthesis was apparently limited to early stages of the life cycle. These results are consistent with the identification of exoprotein as periplasmic protein released to the external medium through the cell wall. Analysis of the observed kinetics of exoprotein yield, utilizing the kinetic model suggests that the greater exoprotein production of cells grown at pH 3.0 was due entirely to greater synthesis of periplasmic proteins while the fraction of periplasmic protein released per unit time was greater for cells grown at pH 5.5. The latter conclusion is supported by thicker cell walls of cells grown at pH 3.0 as observed by electron microscopy. At an applied level the apparent limitation of exoprotein synthesis to the first few hours of cell life, the slow leakage of exoprotein through the cell wall, and the dilute nature of a yeast suspension do not favor the utilization of yeast cells for direct conversion of substrate into protein released to the external medium.     

High-cell-density production of poly-β-hydroxybutyrate (PHB) from methanol by Methylobacterium extorquens: production of high-molecular-mass PHB

Methylobacterium extorquens ATCC 55366 was successfully cultivated at very high cell densities in a fed-batch fermentation system using methanol as a sole carbon and energy source and a completely minimal culture medium for the production of poly--hydroxybutyrate (PHB). Cell biomass levels were between 100 g/l and 115 g/l (dry weight) and cells contained between 40% and 46% PHB on a dry-weight basis. PHB with higher molecular mass values than previously reported for methylotrophic bacteria was obtained under certain conditions. Shake-flask and fermentor experiments showed the importance of adjusting the mineral composition of the medium for improved biomass production and higher growth rates. High-cell-density cultures were obtained without the need for oxygen-enriched air; once the oxygen transfer capacity of the fermentor was reached, methanol was thereafter added in proportion to the amount of available dissolved oxygen, thus preventing oxygen limitation. Controlling the methanol concentration at a very low level (less than 0.01 g/l), during the PHB production phase, led not only to prevention of oxygen limitation but also to the production of very high-molecular-mass PHB, in the 900–1800 kDa range. Biomass yields relative to the total methanol consumed were in the range 0.29–0.33 g/g, whereas PHB yields were in the range 0.09–0.12 g/g. During the active period of PHB synthesis, PHB yields relative to the total methanol consumed were between 0.2 g/g and 0.22 g/g. M. extorquens ATCC 55366 appears to be a promising organism for industrial PHB production.     

Product inhibition during the feeding phasein fed-batch ethanol fermentation of sugar-cane blackstrap molasses

Summary The following equations represent the influence of the ethanol concentration (E) on the specific growth rate of the yeast cells () and on the specific production rate of ethanol () during the reactor filling phase in fed-batch fermentation of sugar-cane blackstrap molasses: = ₀ - k · E and v = v ₀ · K/(K +E) Nomenclature E ethanol concentration in the aqueous phase of the fermenting medium (g.L^–1) - E_m value of E when = 0 or = 0 (g.L^–1) - F medium feeding rate (L.h^–1) - k empirical constant (L.g^–1.h^–1) - K empirical constant (g.L^–1) - M_as mass of TRS added to the, reactor (g) - M_cs mass of consumed TRS (g) - M_e mass of ethanol in the aqueous phase of the fermenting medium (g) - M_s mass of TRS in the aqueous phase of the fermenting medium (g) - M_x mass of yeast cells (dry matter) in the fermenting medium (g) - r correlation coefficient - S TRS concentration in the aqueous phase of the fermenting medium (g.L^–1) - S_m TRS concentration of the feeding medium (g.L^–1) - t time (h) - T temperature (° C) - TRS total reducing sugars calculated as glucose - V volume of the fermenting medium (L) - V₀ volume of the inoculum (L) - X yeast cells concentration (dry matter) in the fermenting medium (g.L^–1) - filling-up time (h) - specific growth rate of the yeast cells (h^–1) - ₀ value of when E=0 - specific production rate of ethanol (h^–1) - ₀ value of when E=0 - density of the yeast cells (g.L^–1) - dry matter content of the yeast cells     

Influence of Zn2+ and Fe3+ on polysaccharide production and mycelium/yeast dimorphism of Aureobasidium pullulans in batch cultivations

Cultivation of Aureobasidium pullulans in medium with a low concentration of yeast extract (0.4 g/l) led to a decrease in the growth rate early in the fermentation as compared to cultivations in medium with high concentration of yeast extract. When this medium was supplemented with zinc and iron the cultivation closely resembled that obtained in medium with high concentration of yeast extract (4.0 g/l). The culture retained a high growth rate throughout the fermentation and the initiation of the mycelial to yeast (M-Y) transition and the exopolysaccharide production was delayed. In a defined medium or in defined medium without iron only a little exopolysaccharide was produced and the yeast fraction of the total biomass at the onset of the stationary phase was 22%–25%. However, cultivation in the defined medium without zinc resulted in a high production of exopolysaccharide and an increased intensity of the M-Y transition, which led to a yeast fraction of 41%.     

Cloning of the GSH1 and GSH2 Genes Complementing the Defective Biosynthesis of Glutathione in the Methylotrophic Yeast Hansenula polymorpha

The cloning of 7.2- and 9.6-kbp fragments of the methylotrophic yeast Hansenula polymorpha DNA restored the wild-type phenotype Gsh⁺ in the glutathione-dependent gsh1 and gsh2 mutants of this yeast defective in glutathione (GSH) synthesis because of a failure of the -glutamylcysteine synthetase reaction. The 9.6-kbp DNA fragment was found to contain a 4.3-kbp subfragment, which complemented the Gsh^– phenotype of the gsh2 mutant. The Gsh⁺ transformants of the gsh1 and gsh2 mutants, which bear plasmids pG1 and pG24, having the 7.2- and 4.3-kbp DNA fragments, respectively, had a completely restored wild-type phenotype with the ability to synthesize GSH and to grow in GSH-deficient synthetic media on various carbon sources, including methanol, and with acquired tolerance to cadmium ions. In addition, the 4.3-kbp DNA fragment borne by plasmid pG24 eliminated pleiotropic changes in the gsh2 mutants associated with methylotrophic growth in a semisynthetic (GSH-supplemented) medium (poor growth and alterations in the activity of the GSH-catabolizing enzyme -glutamyltransferase and the methanol-oxidizing enzyme alcohol oxidase).     

Glycerol metabolism in the methylotrophic yeast Hansenula polymorpha: phosphorylation as the initial step

In hansenula polymorpha glycerol is metabolized via glycerol kinase and NAD(P)-independent glycerol-3-phosphate (G3P) dehydrogenase, enzymes which hitherto were reported to be absent in this methylotrophic yeast. Activity of glycerol kinase was readily detectable when cell-free extracts were incubated at pH 7–8 with glycerol/ATP/Mg²⁺ and a discontinuous assay for G3P formation was used. This glycerol kinase activity could be separated from dihydroxyacetone (DHA) kinase activity by ion exchange chromatography. Glycerol kinase showed relatively low affinities for glycerol (apparent K _m=1.0 mM) and ATP (apparent K _m=0.5 mM) and was not active with other substrates tested. No inhibition by fructose-1,6-bisphosphate (FBP) was observed. Both NAD-dependent and NAD(P)-independent G3P dehydrogenases were present. The latter enzyme could be assayed with PMS/MTT and cosedimented with the mitochondrial fraction. Glucose partly repressed synthesis of glycerol kinase and NAD(P)-independent G3P dehydrogenase, but compared to several other non-repressing carbon sources no clear induction of these enzymes by glycerol was apparent. Amongst glycerolnegative mutants of H. polymorpha strain 17B (a DHA kinase-negative mutant), strains blocked in either glycerol kinase or membrane-bound G3P dehydrogenase were identified. Crosses between representatives of the latter mutants and wild type resulted in the isolation of, amongst others, segregants which had regained DHA kinase but were still blocked in the membrane-bound G3P dehydrogenase. These strains, employing the oxidative pathway, were only able to grow very slowly in glycerol mineral medium.Abbreviations DHA dihydroxyacetone - G3P glycerol-3-phosphate - EMS ethyl methanesulphonate - MTT 3-(4,5-dimethyl-thiazolyl-2)-2,5-diphenyl tetrazolium bromide - PMS phenazine methosulphate - FBP fructose-1,6-bisphosphate     

Optimization of Conditions for Storage and Cultivation of the Fungus Claviceps sp., a Producer of the Ergot Alkaloid Agroclavine

Conditions of agroclavine biosynthesis by the mutant Claviceps sp. strain c106 were studied. The content of agroclavine was maximum (1.5–2 g/l) on days 15–16 of cultivation in the complex medium T25, containing sucrose, citric acid, and yeast extract. Agroclavine was the major component of the alkaloid fraction (90–95%). Storage of the culture at –70°C in T25 supplemented by 7% glycerol provided a stable level of alkaloid formation.     

Extension of Yeast Chronological Lifespan by Methylamine

Background

Chronological aging of yeast cells is commonly used as a model for aging of human post-mitotic cells. The yeast Saccharomyces cerevisiae grown on glucose in the presence of ammonium sulphate is mainly used in yeast aging research. We have analyzed chronological aging of the yeast Hansenula polymorpha grown at conditions that require primary peroxisome metabolism for growth.

Methodology/Principal Findings

The chronological lifespan of H. polymorpha is strongly enhanced when cells are grown on methanol or ethanol, metabolized by peroxisome enzymes, relative to growth on glucose that does not require peroxisomes. The short lifespan of H. polymorpha on glucose is mainly due to medium acidification, whereas most likely ROS do not play an important role. Growth of cells on methanol/methylamine instead of methanol/ammonium sulphate resulted in further lifespan enhancement. This was unrelated to medium acidification. We show that oxidation of methylamine by peroxisomal amine oxidase at carbon starvation conditions is responsible for lifespan extension. The methylamine oxidation product formaldehyde is further oxidized resulting in NADH generation, which contributes to increased ATP generation and reduction of ROS levels in the stationary phase.

Conclusion/Significance

We conclude that primary peroxisome metabolism enhanced chronological lifespan of H. polymorpha. Moreover, the possibility to generate NADH at carbon starvation conditions by an organic nitrogen source supports further extension of the lifespan of the cell. Consequently, the interpretation of CLS analyses in yeast should include possible effects on the energy status of the cell.     

Determination of Growth and Glycerol Production Kinetics of a Wine Yeast Strain Saccharomyces cerevisiae Kalecik 1 in Different Substrate Media

Summary Glycerol has been known as an important by-product of wine fermentations improving the sensory quality of wine. This study was carried out with an endogenic wine yeast strain Saccharomyces cerevisiae Kalecik 1. The kinetics of growth and glycerol biosynthesis were analysed at various initial concentrations of glucose, fructose, and sucrose in a batch system. Depending on the determined values of Monod constants, glucose (K_s = 28.09 g/l) was found as the most suitable substrate for the yeast growth. Initial glucose, fructose and sucrose concentrations necessary for maximum specific yeast growth rate were determined as 175 g, 100 l, and 200 g/l, respectively. The yeast produced glycerol at very high concentrations in fructose medium. Fructose was determined as the most suitable substrate for glycerol production while the strain showed low tendency to use it for growth. S. cerevisiae Kalecik 1 could not produce glycerol below 200 g/l initial sucrose concentration. When natural white grape juice was used as fermentation medium, maximum glycerol concentration and dry weight of the yeast were determined as 9.3 g/l and 11.8 g/l, respectively.     

Isolation of the Melanization and Reddish Coloration Hormone (MRCH) of the Armyworm,Leucania separata,from the Silkworm,Bombyx mori

Two types of glycerol dehydrogenase (GDH) were found on DEAE-cellulose column chromatography of cell-free extracts of methylotrophic yeasts. One type, designated as GDH I, showed only the reductive activity which was detected in the reaction system containing dihydroxyacetone and NADH, at pH 6.0. The other type, designated as GDH II, showed the oxidative activity which was detected in the system containing glycerol and NAD ⁺, at pH 9.0, together with the reductive activity.

Candida boidinii No. 2201, which possesses the phosphorylative pathway for glycerol dissimilation, had only GDH I when grown on glycerol or methanol as the carbon source. Hansenula ofunaensis, which has the oxidative pathway, had both GDH I and GDH II when grown on glycerol, but only GDH I when grown on methanol. Hansenula polymorpha Dl-1, which has both pathways, had both GDH I and GDH II when grown on glycerol or methanol.     

Simultaneous utilization of heterotrophic substrates by Hansenula polymorpha MH30 results in enhanced growth rates

Summary The maximum specific growth rate (_max) of Hansenula polymorpha MH30 on xylose as the sole source of carbon and energy is 0.175 h^–1, on methanol 0.21 h^–1, on glycerol 0.27 h^–1 and on glucose 0.61 h^–1. On mixtures of xylose plus methanol, xylose plus glycerol, xylose plus glucose and glycerol plus glucose H. polymorpha MH30 grows faster: 0.36 h^–1, 0.37 h^–1, 0.47 h^–1 and 0.52 h^–1, respectively. Attempts have been made to explain these somewhat surprising results, especially the fact that the growth rates on xylose plus methanol and xylose plus glycerol exceed the specific growth rates of these on even the faster partner in the mixture. Offprint requests to: W. Babel     

Nutrient effects on cellulase production by the new species, Clostridium thermocopriae

Summary The effects of urea, yeast extract and cellulose concentrations on extracellular cellulase production and cellulose hydrolysis by Clostridium thermocopriae JT3-3 were analysed by the orthogonal method. Using a new modified medium, in which urea and K₂HPO₄ concentrations were increased and the yeast extract concentration was decreased, cellulose hydrolysis and endocellulase production increased at least 1.6 times, but -glucosidase and -xylosidase production decreased slightly.     

Expression and characterization of a thermostable serine protease (TfpA) from Thermomonospora fusca YX in Pichia pastoris

A serine protease produced by Thermomonospora fusca YX (TfpA) is heat-stable (up to 85°C) and has a broad pH activity range and strong resistance to detergents. The objective of this study was to determine if the methylotropic yeast Pichia pastoris could express TfpA extracellularly. A 1.0-kb DNA fragment (tfpA) encoding the pro-peptide and mature protein of TfpA was cloned into expression vectors pPICZA (inducible) and pGAPZA (constitutive) and introduced into P. pastoris by electroporation. Expression of r-TfpA was greater in the inducible system than in the constitutive one, producing 135 U ml^–1 medium supernatant 6 days after methanol induction. The r-TfpA was not glycosylated (21.7 kDa), and had pH and temperature optima of 8.5 and 80°C, respectively, using azocasein as a substrate. In conclusion, P. pastoris can be used as a host to produce extracellular r-TfpA, and expression efficiency may be improved by optimizing fermentation conditions and modifying factors related to protein expression and stability.