Effect of iron and EDTA on ethyl acetate accumulation in Candida utilis

Summary Production of economically-recoverable products from dilute sugar or ethanol is of practical importance. Conversion of glucose to ethyl acetate by Candida utilis was inhibited by FeCl₃ supplementation as low as 10 uM. EDTA added at the onset of growth on glucose relieved such an inhibition and also caused faster and greater amounts of accumulation of the ester. Addition of EDTA during conversion of ethanol to ethyl acetate showed little effect. EDTA may affect cell permeability and/or oxidative metabolism. For continual ethyl acetate production iron limitation must be maintained during as well as before ethanol utilization.EDTA = Ethylenediaminetetraacetic acid.     

Production of acetaldehyde from ethanol byCandida utilis

Summary Ethanol-adaptedCandida utilis efficiently converted ethanol to acetaldehyde, a chemical feedstock of recognized importance. Acetaldehyde which has a low boiling point (21°C) readily evaporates and is easily recovered, thus this bioconversion could provide an energy saving process for efficient recovery of a useful product from low concentrations of ethanol.     

Production of Candida utilis protein from peat extracts

Sphagnum peat extracts or hydrolysates have been obtained and used as a culture medium for the production of Candida utilis biomass as single cell proteins. Acid hydrolysis of ground peat (4–60 mesh) in an autoclave operated under a set of conditions for acid strength (0.3-1.5 (v/v) H₂SO₄), holding time (1–4 hr), temperature (100–165°C), and weight ratio of dry peat to solution (3.3–16.7 g dry peat/100 g solution) yielded carbohydrate-rich extracts of different concentrations (1–34g/liter). The best yield (mg total carbohydrate/g dry peat) was obtained for a holding time of I hr and a temperature of 152°C. Low peat concentratio (4.1 g dry peat/100 g solution)resulted in high yield(280mg total carbohydrate/gdry peat) with a corresponding low carbohydrate content in hydrolysate (13 g/liter), while a lower yield with a higher carbohydrate content (34 g/liter)in hydrolysate were found when increasing peat concentration (16.7 g dry peat/100 g solution). Shake-fladk experiments using peat hydrolysates as the culture medium together with NH₄OH (～4.8 g/liter) and K₂HPO₄(5 g/liter) as nitrogen and phosphate supplement, respectively, gave a maximum biomass concentration of 7.5 g/liter after 60 hr at 30°C and 200rpm. Batch cultivation in a fermentor under controlled conditions for aeration (4.2 liter/min), agitation (500rpm), temperature (30°C), and pH (5.0) produced a maximum biomass of 10 g/liter after 20 hr with a specific growth rate of 0.13 hr^?1. For the continuous cultivation, a maximal biomass productivity of 1.24 g/gliter-he was obtained at a dilution rate of 0.125 hr ^?1. Monod's equation's equation has been used for the estimation of the coefficients μ_Max, K_s, and Y. It was found that the yield coefficient Y is not constant during the progress of batch cultivation.     

Production of ethanol from dilute glucose solutions A technical-economic evaluation of various refining alternatives

In order for ethanol to be competitive with gasoline, the production cost of ethanol must be lower than it is today. One economically crucial step in the production of ethanol from lignocellulosics is refining, since hydrolysis yields dilute glucose solutions which, after fermentation, result in a dilute ethanol solution, 2–3 wt-% ethanol. A technical-economic investigation of various energy-saving alternatives to conventional distillation has been performed. The energy-saving techniques investigated were: multi-column distillation, distillation with mechanical vapour recompression, distillation with an absorption heat transformer, phase separation with potassium carbonate and extraction of ethanol from the fermentation broth with Aldol 85. The most economical refining step for the production of ethanol from a dilute glucose solution, around 5 wt-%, was found to be multicolumn distillation.The authors wish to thank the Swedish Ethanol Development Foundation (SSEU) and The Swedish National Board for Industrial and Technical Development (NUTEK) for their financial support. The authors would also like to thank Professor Åke Jernqvist at The Department of Chemical Engineering 1, Lund University for his help with the calculations of the heat transformer cycle.     

Growth of Candida utilis on ethanol and isopropanol

Candida utilis grew on ehtanol and an ethanol-isopropanol-water (22:2:1 vols) mixture but not on isopropanol alone. Acetone accumulated in all cultures containing isopropranol but its presence in the alcohol mixture did not lower growth rate or yield significantly when compared with growth experiments on ethanol alone. Growth rate and yield declined at ethanol concentrations greater than 1% (v/v) and 0.3% (v/v) respectively. In a 0.3% (v/v) alcohol mixture, acetate was found only during the exponential growth phase. In a 3% (v/v) mixture, acetate and ethyl acetate accumulated during growth whereas acetaldehyde was present only during the exponential growth phase.     

Production of ethanol by the yeastCandida utilis under autoanaerobic conditions

Candida utilis CCY 29-38-65 converts glucose to ethanol under autoanaerobic conditions. On aeration switch-on the produced ethanol is utilized as carbon source and the specific rate of biomass production increases.     

Production of single cell protein from rice polishings using Candida utilis

Microbial protein was produced from defatted rice polishings using Candida utilis in shake-flasks and a 14-l fermentor to optimize fermentation conditions before producing biomass in a 50-l fermentor. The organism supported maximum values of 0.224 h⁻¹, 0.94, 1.35, 1.75, 2.12 g l⁻¹ h⁻¹, 0.62 g cells g⁻¹ substrate utilized and 0.38 g g⁻¹ for specific growth rate, true protein productivity, crude protein productivity, cell mass productivity, substrate consumption rate, cell yield, crude protein yield, respectively in 50-l fermentor studies using optimized cultural conditions. Maximum values compared favourably or were superior to published data in literature. The biomass protein in the 50-l fermentor contained 22.3, 27.8, 19.2, 9.5, 38.12, 8.5 and 0.27% true protein, crude protein, crude fibre, ash, carbon, cellulose and RNA content, respectively. The dried biomass showed a gross metabolizable energy value of 2678 kcal kg⁻¹ and contained all essential and non-essential amino acids. Yeast biomass as animal feed may replace expensive feed ingredients currently being used in poultry feed and may improve the economics of feed produced in countries like Pakistan. This revised version was published online in August 2006 with corrections to the Cover Date.     

Proton extrusion and attendant transport phenomena in Candida utilis induced by ethanol

Summary Ion fluxes after ethanol addition to Candida utilis depend crucially on aeration (air versus oxygen). In O₂-aerated non-growing cells ethanol causes an H ⁺ / K ⁺ exchange and an extrusion of acetate and lactate accompanied mostly by K ⁺, and their subsequent reimportation together with H ⁺. Cells from continuous culture display generally stronger acidification and more marked K ⁺ movements than non-growing ones. Offprint requests to: A. Prell     

Maximization of Candida utilis cytochromes by pulse additions of ethanol to continuous cultures

Candida utilis was grown with glucose as growth-limiting carbon source in batch culture, steady-state continuous culture, and non-steady-state continuous culture. High cytochrome concentrations were routinely recorded in cells harvested in the latter stages of batch culture. They were occasionally recorded in cells from imprecisely controlled steady-state cultures, but precise control of the steady-state dissolved oxygen tension stabilized the cytochromes at relatively low levels. Controlled non-steady-state continuous cultures, imposed by pulse additions of ethanol, routinely produced cells with high cytochrome concentrations. A mechanism is proposed whereby maintenance of cytochrome derepression in continuous culture is dependent upon indefinitely prolonging an “overshoot” response in gene expression.     

Pentose Metabolism by Candida utilis

Xylose isomerase, an enzyme isomerizing xylose to xylulose, was produced adaptively when Candida utilis, a fodder yeast, was grown in a medium containing xylose. This experiment was carried out in order to isolate and purify the enzyme, and to clarify properties of the enzyme. As a result, it was revealed that the enzyme could be solubilized by plasmolysis, and was purified by dialysis, salting out with ammonium sulfate, precipitating with acetone, and adsorbing to calcium phosphate gel. The enzyme requires some divalent metal ions for its action and among them manganese ion is the most effective. The enzyme is inhibited particularly by ethylenediamine-tetraacetic acid and has somewhat thermotolerant character.     

Extraction of uricase from Candida utilis

Summary Six methods of uricase extraction from Candida utilis were tested and compared. X-press disintegration and sonic oscillation gave the best results.     

Effect of external pH on the respiration activity of Candida utilis induced by ethanol

Summary The kinetics of ethanol oxidation by non-growing cells of Candida utilis in different media at various external pH values was determined experimentally. The statistical discrimination between two rival mathematical models has shown that the mechanism of non-specific substrate inhibition of respiration kinetics fits better the experimental data. It has been found that the maximum respiration activity is controlled by the buffering properties of organic polycarbonic acids in the medium. The pH values at which the maximum respiration rate was observed were close to the pK values of the organic acids in the buffer solution, independently of whether the acids were metabolized or not. Offprint requests to: Jan Paca     

Protoplast production from Candida utilis]

The protoplasts of Candida utilis 295 t were produced with the aid of the lytic enzyme from Helix pomatia. If the cell wall of C. utilis 295 t is not treated with SH-compounds (the best effect was found with L-cysteine), it is resistant to the action of the enzyme. The yield of the protoplasts was 100 per cent after 15 minutes of the incubation with the lytic enzyme if the cells were preliminarily treated with L-cysteine. Optimal conditions for the production of the protoplasts are described.     

Economic evaluation of preconcentration in production of ethanol from dilute sugar solutions

The economic feasibility of preconcentrating dilute sugar solutions prior to fermentation is investigated. Two methods, evaporation and reverse osmosis, are compared. A computer program to determine the optimal preconcentration conditions for glucose solutions of 1.5-16 wt% has been developed. It was used to compute the fractional cost for labor and maintenance, preconcentration, fermentation, and distillation. Preconcentration with evaporation resulted in a higher total cost, compared with no preconcentration, for all cases studied, although a six-effect unit was used. Reverse osmosis was found to be economically feasible for preconcentration to about 5-10 wt % depending on the concentration of the feed.     

Influence of acetate on the growth of Candida utilis in continuous culture

Candida utilis was grown on acetate in chemostat cultures that were, successively, carbon and ammonia-limited (30° C; pH 5.5). With carbon(acetate)-limited cultures, the specific rate of oxygen consumption (q _{O 2}) was not a linear function of the growth rate but was markedly stimulated at the higher dilution rates, thus effecting a marked decrease in the Y _O value. This increased respiration rate, and decreased yield value, correlated closely with a marked increase in the extracellular acetate concentration. Under ammonia-limiting conditions, very low Y _O values were found, generally comparable with those found with carbon-limited cultures growing at the higher dilution rates, but these varied markedly with the extracellular acetate concentration. Thus, when the unused acetate concentration was raised progressively from about 5 g/l to about 21 g/l, the Y _O value decreased non-linearly from 11.4 to 5.8. When the extracellular acetate concentration was further increased to 25 g/l, growth was inhibited and the culture washed out. This relationship between respiration rate and the extracellular concentration of unused acetate was also markedly influenced by the culture pH value. Thus, with a fixed extracellular acetate concentration (16±2g/l) and dilution rate (0.14 h^–1), lowering the culture pH value progressively from 6.9 to 5.1 effected a marked and progressive increase in the respiration rate. Further lowering of the culture pH to 4.8, however, caused a complete collapse of respiration. In contrast to this situation, progressively lowering the pH value of an acetatelimited culture from 6.9 to 4.5 affected only slightly the culture respiration rate, and growth was possible even at a pH value of 2.5. These results are discussed in the context of the possible mechanisms whereby acetate exerts its toxic effect on the growth of C. utilis.     

Production of chlamydospores by Candida albicans cultivated on dilute oxgall agar

Summary A simple easily prepared clear medium consisting of 2% oxgall in 1.8% agar is described. This has proved to be excellent for the rapid identification ofCandida albicans in swabs and cultures, provided that the inoculated area is covered by a coverslip and the incubation temperature period is maintained at 28°C for 24 to 48 hours. No special technical skill is required to prepare this medium. The results presented show thatC. albicans will always produce chlamydospores on this medium if the recommended procedure is followed.Head, Medical Mycology Section.Mycologist, Medical Mycology Section.     

Heterologous protein secretion by Candida utilis

The yeast Candida utilis (also referred to as Torula) is used as a whole-cell food additive and as a recombinant host for production of intracellular molecules. Here, we report recombinant C. utilis strains secreting significant amounts of Candida antarctica lipase B (CalB). Native and heterologous secretion signals led to secretion of CalB into the growth medium; CalB was enzymatically active and it carried a short N-glycosyl chain lacking extensive mannosylation. Furthermore, CalB fusions to the C. utilis Gas1 cell wall protein led to effective surface display of enzymatically active CalB and of β-galactosidase. Secretory production in C. utilis was achieved using a novel set of expression vectors containing sat1 conferring nourseothricin resistance, which could be transformed into C. utilis, Pichia jadinii, Candida albicans, and Saccharomyces cerevisiae; C. utilis promoters including the constitutive TDH3 and the highly xylose-inducible GXS1 promoters allowed efficient gene expression. These results establish C. utilis as a promising host for the secretory production of proteins.     

过氧化氢胁迫促进产朊假丝酵母合成谷胱甘肽

谷胱甘肽(GSH)在生物细胞抵御外界环境条件的刺激和胁迫时起到非常重要的作用。考察了不同时间不同浓度过氧化氢胁迫和过氧化氢连续胁迫对产朊假丝酵母合成GSH的影响, 发现低浓度过氧化氢的连续胁迫对GSH的合成有明显促进作用。进一步在发酵罐上应用了低浓度过氧化氢(36 mmol/L)持续胁迫策略, 最终GSH产量为922 mg/L, 胞内GSH含量为1.64%, 比对照分别提高了7%和35%。