Development of medium components for the production of glucosyl-transferring enzyme by Aureobasidium

Aureobasidium sp. ATCC 20524 produced a glucosyl-transferring enzyme which produced panose (O--D-glucopyranosyl-(1»6)-O--D-glucopyranosyl-(1»4)-d-glucose) from maltose. Optimum production for the enzyme was with maltose at 2% (w/v) and yeast extract at 1.5% (w/v). Enzymatic activity reached 0.7×10³ U/g dry cells after 48 h.     

Na-dependent <Emphasis Type="SmallCaps">D</Emphasis>-Glucose Transport by Intestinal Brush Border Membrane Vesicles from Gilthead Sea Bream (<Emphasis Type="Italic">Sparus aurata</Emphasis>)

Brush border membrane vesicles (BBMV) enriched in sucrase, maltase and alkaline phosphatase, and impoverished in Na⁺-K⁺-ATPase, were isolated from proximal and distal intestine of the gilthead sea bream (Sparus aurata) by a MgCl₂ precipitation method. Vesicles were suitable for the study of the characteristics of D-glucose apical transport. Only one D-glucose carrier was found in vesicles from each intestinal segment. In both cases, the D-glucose transport system was sodium-dependent, phlorizin-sensitive, significantly inhibited by D-glucose, D-galactose, α-methyl-D-glucose, 3-O-methyl-D-glucose and 2-deoxy-D-glucose, and showed stereospecificity. Apparent affinity constants of D-glucose transport (K_t) were 0.24 ± 0.03 mM in proximal and 0.18 ± 0.03 mM in distal intestine. Maximal rate of influx (Jmax) was 47.3 ± 2.2 pmols. mg⁻¹ protein for proximal and 27.3 ± 3.6 pmols. mg⁻¹ protein for distal intestine. Specific phlorizin binding and relative abundance of an anti-SGLT1 reactive protein were significantly higher in proximal than in distal BBMV. These results suggest the presence of the same D-glucose transporter along the intestine, with a higher density in the proximal portion. This transporter is compatible with the sodium-dependent D-glucose carrier described for other fish and with the SGLT1 of higher vertebrates.This revised version was published online in June 2005 with a corrected cover date.     

Ethanol fermentation of mixed-sugars using a two-phase, fed-batch process: method to minimize D-glucose repression of Candida shehatae D-xylose fermentations

Candida shehatae cells pre-grown on D-xylose simultaneously consumed mixtures of D-xylose and D-glucose, under both non-growing (anoxic) and actively growing conditions (aerobic), to produce ethanol. The rate of D-glucose consumption was independent of the D-xylose concentration for cells induced on D-xylose. However, the D-xylose consumption rate was approximately three times lower than the D-glucose consumption rate at a 50% D-glucose: 50% D-xylose mixture. Repression was not observed (substrate utilization rates were approximately equal) when the percentage of D-glucose and D-xylose was changed to 22% and 78%, respectively. In fermentations with actively growing cells (50% glucose and D-xylose), ethanol yields from D-xylose increased, the % D-xylose utilized increased, and the xylitol yield was significantly reduced in the presence of D-glucose, compared to anoxic fermentations (Y_ETOH,xylose = 0.2–0.40 g g⁻¹, 75–100%, and Y_xylitol = 0–0.2 g g⁻¹ compared to Y_ETOH,xylose = 0.15 g g⁻¹, 56%, Y_xylitol = 0.51 g g⁻¹, respectively). To increase ethanol levels and reduce process time, fed-batch fermentations were performed in a single stage reactor employing two phases: (1) rapid aerobic growth on D-xylose (μ = 0.32 h⁻¹) to high cell densities; (2) D-glucose addition and anaerobic conditions to produce ethanol (Y_ETOH,xylose = 0.23 g g⁻¹). The process generated high cell densities, 2 × 10⁹ cells ml⁻¹, and produced 45–50 g L⁻¹ ethanol within 50 h from a mixture of D-glucose and D-xylose (compared to 30 g L⁻¹ in 80 h in the best batch process). The two-phase process minimized loss of cell viability, increased D-xylose utilization, reduced process time, and increased final ethanol levels compared to the batch process. Received 23 February 1998/ Accepted in revised form 15 July 1998     

Differential expression of Na<Superscript>+</Superscript>/<Emphasis Type="SmallCaps">d</Emphasis>-glucose cotransport in isolated cells of<Emphasis Type="Italic"> Marsupenaeus japonicus</Emphasis> hepatopancreas

d-Glucose absorptive processes at the gastrointestinal tract of decapod crustaceans are largely under-investigated. We have studied Na⁺-dependent d-glucose transport (Na⁺/d-glucose cotransport) in the hepatopancreas of the Kuruma prawn, Marsupenaeus japonicus, using both brush-border membrane vesicles and purified R and B hepatopancreatic cell suspensions. As assessed by brush-border membrane vesicle studies, Na⁺/d-glucose cotransport was inhibited by phloridzin and responsive to the (inside negative) membrane potential. Furthermore, it was strongly activated by protons (although only in the presence of an inside-negative membrane potential), which correlates with the fact that the lumen of crustacean hepatopancreatic tubules is acidic. When assayed in purified R and B cell suspensions, Na⁺/d-glucose cotransport activity was restricted to B cells only. Mab 13, a monoclonal antibody recognizing an 80- to 85-KDa protein at the brush-border membrane location, inhibited Na⁺/D-glucose cotransport in brush-border membrane vesicles as well as in enriched B cell suspensions. Primers designed after comparison of highly homologous regions of various mammalian sodium-glucose transporter) nucleotide sequences failed to produce RT-PCR amplification products from Kuruma prawn hepatopancreatic RNA. The molecular nature of this Na⁺/d-glucose cotransport system is still to be established.Communicated by: G. Heldmaier     

Production of d-arabitol by a newly isolated Kodamaea ohmeri

A new yeast, isolated from natural osmophilic sources, produces d-arabitol as the main metabolic product from glucose. According to 18S rRNA analysis, the NH-9 strain belongs to the genus Kodamaea. The optimal culture conditions for inducing production of d-arabitol were 37 °C, neutral pH, 220 rpm shaking, and 5% inoculum. The yeast produced 81.2 ± 0.67 g L⁻¹ d-arabitol from 200 g L⁻¹ d-glucose in 72 h with a yield of 0.406 g g⁻¹ glucose and volumetric productivity Q_\textP Q_{\text{P}} of 1.128 g L⁻¹ h⁻¹. Semi-continuous repeated-batch fermentation was performed in shaker-flasks to enhance the process of d-arabitol production by Kodamaea ohmeri NH-9 from d-glucose. Under repeated-batch culture conditions, the highest volumetric productivity was 1.380 g L⁻¹ h⁻¹.     

Evaluation of 2-[N-(7-nitrobenz-2-oxa-1,3-diazol-4-yl)amino]-2-deoxy-d-glucose, a new fluorescent derivative of glucose, for viability assessment of yeast Candida albicans

A new fluorescent derivative of d-glucose, 2-[N-(7-nitrobenz-2-oxa-1,3-diazol-4-yl)amino]-2-deoxy-d-glucose (2-NBDG), which had been previously developed for the analysis of glucose uptake activity by living cells, was investigated to evaluate its applicability for assaying the viability of yeast Candida albicans. Lineweaver-Burk plots showed the uptake of 2-NBDG to be competitively inhibited by d-glucose and not by l-glucose, which suggested the involvement of the glucose transporting system of C. albicans in the uptake of 2-NBDG. A good correlation was obtained between the yeast viability, determined by the plate-count method, and the 2-NBDG uptake activity of yeast cells (correlation constant: r=0.97). This is expected to lead to the development of a new fluorescent probe for the determination of yeast cell viability.     

Role of sugars in phosphate transport in baker's yeast

Sugar substrates which depress the intracellular level of inorganic phosphate in baker's yeast (d-glucose,d-fructose,d-mannose, sucrose, as well as maltose andd-galactose after appropriate induction) also make transmembrane flux of phosphate anions possible. Acetate and ethanol, although readily oxidized, as well as nonmetabolized sugars, do not produce the effect. Phosphate uptake in whole cells (but not in protoplasts) is accelerated by preincubation with substrate either aerobically or anaerobically but the actual presence of substrate in the incubation medium is required for transport to take place. Starved cells take up phosphate from the medium with aK _m of 3mm, the half-activation concentration by glucose being 18mm, the amount taken up being constant under given conditions (40 μmol/g dry wt. here). Phosphate-rich cells lose phosphate to the medium in the presence of a suitable substrate. The uptake process is characterized by an activation energy of 13400 cal/mol at 10⁻⁶ m phosphate and of 9400 cal/mol at 10⁻³ m phosphate. The process shows two optima at pH 5.0 and 7.0. A short-lived intermediate of fermentative sugar metabolism is postulated as essential for the translocation of phosphate across the yeast membrane.     

Biological evaluation of a series of 2-acetamido-2-deoxy-D-glucose analogs towards cellular glycosaminoglycan and protein synthesis in vitro

Using primary hepatocytes in culture, various 2-acetamido-2-deoxy-D-glucose (GlcNAc) analogs were examined for their effects on the incorporation of D-[³H]glucosamine, [³⁵S]sulfate, and L-[¹⁴C]leucine into cellular glycoconjugates. A series of acetylated GlcNAc analogs, namely methyl 2-acetamido-3,4,6-tri-O-acetyl-2-deoxy-α-(3) and β-D-glucopyranoside (4) and 2-acetamido-1,3,4,6-tetra-O-acetyl-2-deoxy-D-glucopyranose (5), exhibited a concentration-dependent reduction of D-[³H]glucosamine, but not of [³⁵S]sulfate incorporation into isolated glycosaminoglycans (GAGs), without affecting L-[¹⁴C]leucine incorporation into total protein synthesis. These results suggest that analogs 3–5 exhibit an inhibitory effect on D-[³H]glucosamine incorporation into isolated GAGs by diluting the specific activity of cellular D-[³H]glucosamine and by competing for the same metabolic pathways. In the case of the corresponding series of 4-deoxy-GlcNAc analogs, namely methyl 2-acetamido-3,6-di-O-acetyl-2,4-dideoxy-α-(6) and β-D-xylo-hexopyranoside (7) and 2-acetamido-1,3,6-tri-O-acetyl-2,4-dideoxy-D-xylo-hexopyranose (8), compound 8 at 1.0 mM exhibited the greatest reduction of D-[³H]glucosamine and [³⁵S]sulfate incorporation into isolated GAGs, namely to ∼7% of controls, and a moderate inhibition of total protein synthesis, namely to 60% of controls. Exogenous uridine was able to restore the inhibition of total protein synthesis by compound 8 at 1.0 mM. Isolated GAGs from cultures treated with compound 8 were shown to be smaller in size (∼40 kDa) than for control cultures (∼77 kDa). These results suggest that the inhibitory effects of compound 8 on cellular GAG synthesis may be mediated by the incorporation of a 4-deoxy moiety into GAGs resulting in premature chain termination and/or by its serving as an enzymatic inhibitor of the normal sugar metabolites. The inhibition of total protein synthesis from cultures treated with compound 8 suggests a uridine trapping mechanism which would result in the depletion of UTP pools and cause the inhibition of total protein synthesis. A 1-deoxy-GlcNAc analog, namely 2-acetamido-3,4,6-tri-O-acetyl-1,5-anhydro-2-deoxy-D-glucitol (9), also exhibited a reduction in both D -[³H]glucosamine and [³⁵S]sulfate incorporation into isolated GAGs by 19 and 57%, of the control cells, respectively, at 1.0 mM without affecting total protein synthesis. The inability of compound 9 to form a UDP-sugar and, hence, be incorporated into GAGs presents another metabolic route for the inhibition of cellular GAG synthesis. Potential metabolic routes for each analog's effects are presented.     

A membrane-bound enzyme complex synthesising glucan and glucomannan in pine tissues

Particulate membrane preparations isolated from cambial cells and differentiating and differentiated xylem cells of pine (Pinus sylvestris L.) trees synthesised [¹⁴C]glucans using either guanosine 5-diphosphate (GDP)-D-[U-¹⁴C]glucose or uridine 5-diphosphate (UDP)-D-[U-¹⁴C]glucose as glycosyl donors. Although these glucans had -(13) and -(14) linkages in an approximate ratio 1:1, the distribution of the linkages in the glucan synthesised from GDP-D-glucose was different from that synthesised from UDP-D-glucose. The synthesis of the mixed -(13) and -(14) glucan from GDP-D-[U-¹⁴C]glucose was changed to that of -(14) glucomannan in the presence of increasing concentrations of GDP-D-mannose. The glucan formed from UDP-D-[U-¹⁴C]glucose was not affected by any concentration of GDP-D-mannose. The membrane preparations epimerized GDP-D-glucose to GDP-D-mannose; however, the low amount of GDP-D-mannose formed was not incorporated into the polymer becaus the affinity of the synthase for GDP-D-glucose was much greater than that for GDP-D-mannose. The glucan formed from GDP-D-glucose and the glucomannan formed from GDP-D-glucose together with GDP-D-mannose were characterized. The apparent K _m and V _max of the glucan synthase for GDP-D-glucose were 6.38 M and 5.08 M·min^-1, respectively. No lipid intermediates were detected during the synthesis of either glucan or glucomannan. The results indicated that an enzyme complex for the formation of the glucomannan was bound to the membrane.Abbreviations GDP guanosine 5-diphosphate - GLC gasliquid chromatography - UDP trridine 5-diphosphate     

<Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> NAD-dependent, <Emphasis Type="SmallCaps">D</Emphasis>-fructose reducing,polyol dehydrogenases activity: screening,medium optimisation and application for enzymatic polyol production

Gluconobacter oxydans LMG 1489 was selected as the best strain for NAD(P)-dependent polyol dehydrogenase production. The highest enzyme activities were obtained when this strain was cultivated on a medium consisting of 30 g glycerol l^–1, 7.2 g peptone l–1 and 1.8 g yeast extract l^–1. Two D-fructose reducing, NAD-dependent intracellular enzymes were present in the G. oxydans cell-free extract: sorbitol dehydrogenase, and mannitol dehydrogenase. Substrate reduction occurred optimally at a low pH (pH 6), while the optimum for substrate oxidation was situated at alkaline pHs (pH 9.5–10.5). The mannitol dehydrogenase was more thermostable than the sorbitol dehydrogenase. The cell-free extract could be used to produce D-mannitol and D-sorbitol enzymatically from D-fructose. Efficient coenzyme regeneration was accomplished by formate dehydrogenase-mediated oxidation of formate into CO₂.     

Expression of glf Z.m. increases D-mannitol formation in whole cell biotransformation with resting cells of Corynebacterium glutamicum

A recombinant oxidation/reduction cycle for the conversion of D-fructose to D-mannitol was established in resting cells of Corynebacterium glutamicum. Whole cells were used as biocatalysts, supplied with 250 mM sodium formate and 500 mM D-fructose at pH 6.5. The mannitol dehydrogenase gene (mdh) from Leuconostoc pseudomesenteroides was overexpressed in strain C. glutamicum ATCC 13032. To ensure sufficient cofactor [nicotinamide adenine dinucleotide (reduced form, NADH)] supply, the fdh gene encoding formate dehydrogenase from Mycobacterium vaccae N10 was coexpressed. The recombinant C. glutamicum cells produced D-mannitol at a constant production rate of 0.22 g (g cdw)⁻¹ h⁻¹. Expression of the glucose/fructose facilitator gene glf from Zymomonas mobilis in C. glutamicum led to a 5.5-fold increased productivity of 1.25 g (g cdw)⁻¹ h⁻¹, yielding 87 g l⁻¹ D-mannitol from 93.7 g l⁻¹ D-fructose. Determination of intracellular NAD(H) concentration during biotransformation showed a constant NAD(H) pool size and a NADH/NAD⁺ ratio of approximately 1. In repetitive fed-batch biotransformation, 285 g l⁻¹ D-mannitol over a time period of 96 h with an average productivity of 1.0 g (g cdw)⁻¹ h⁻¹ was formed. These results show that C. glutamicum is a favorable biocatalyst for long-term biotransformation with resting cells. Dedicated to Prof. Hermann Sahm on the occasion of his 65th birthday.     

Different affinities of the α- and β-anomers ofD-glucose,D-mannose andD-xylose for the glucose uptake system of baker’s yeast

A recording technique for measuring the sugar uptake by cell suspensions using a polarimeter is described. The method makes it possible to calculate the uptake rates of the α-and β-anomers. The constitutive monosaccharide transport system ofSaccharomyces cerevisiae andSaccharomyces fragilis exhibits a higher affinity for the α-anomers ofd-glucose,d-manose andd-xylose than for the corresponding β-anomers, this resulting in a preferential uptake of the α-anomers from a mixture. The α-anomer ofd-xylose is preferred both during influx and efflux. The membrane transport ofd-xylose inSaccharomyces cerevisiae is not associated with a change of the anomer configuration. The facilitated diffusion system appears to possess a regulatory role for the utilization ofd-glucose andd-mannose in both yeast species investigated.     

Ethanol tolerance of Pichia stipitis and Candida shehatae strains in fed-batch cultures at controlled low dissolved oxygen levels

Summary Fed-batch cultivations of Pichia stipitis and strains of Candida shehatae with d-xylose or d-glucose were conducted at controlled low dissolved oxygen tension (DOT) levels. There were some marked differences between the strains. In general growth was inhibited at lower ethanol concentrations than fermentation, and ethanol levels of up to 47 g·l^-1 were produced at 30°C. Ethanol production was mainly growth associated. The yeast strains formed small amounts of monocarboxylic acids and higher alcohols, which apparently did not enhance the ethanol toxicity. The maximum ethanol concentration obtained on d-xylose could not be increased by using a high cell density culture, nor by using d-glucose as substrate. The latter observation suggested that the low ethanol tolerance of these xylose-fermenting yeast strains was not a consequence of the metabolic pathway used during pentose fermentation. In contrast with the C. shehatae strains, it was apparent with P. stipitis CSIR-Y633 that when the ethanol concentration reached about 28 g·l^-1, ethanol assimilation exceeded ethanol production, despite cultivation at a low DOT of 0.2% of air saturation. Discontinuing the aeration enabled ethanol accumulation to proceed, but with concomitant xylitol production and cessation of growth.     

The pathway ofD-cycloserine biosynthesis inStreptomyces garyphalus

Incubation experiments using washed cells and toluene treated cells ofStreptomyces garyphalus showed that O-acetyl-L-serine and hydroxyurea are intermediates in the biosynthesis ofD-cycloserine. The formation of [¹⁴C]O-ureidoserine from O-acetyl-L-serine and hydroxyurea was demonstrated by incubating an enzyme solution with¹⁴C-labelled substrates. Desalted cell-free extract catalyzed the conversion of O-ureido-D-serine toD-cycloserine in a reaction requiring ATP and Mg²⁺. The results suggested the following pathway forD-cycloserine biosynthesis.     

An investigation of d-{1-13C} xylose metabolism in Pichia stipitis under aerobic and anaerobic conditions

Summary The uptake of d-{1-¹³C} xylose, the accumulation of intermediates and the distribution of the label in ethanol in Pichia stipitis under aerobic and anaerobic conditions were investigated by nuclear magnetic resonance spectroscopy. The rate-limiting step of d-xylose metabolism under aerobic conditions appeared to be uptake, whereas under anaerobic conditions it was the conversion of xylitol to xylulose. The yeast showed no preference to either the alpha-or beta-forms of d-xylose. Under anaerobic conditions only {2-¹³C{ ethanol was detected and this suggests that NADH but not NADPH was used as cofactor in the conversion of xylose to xylitol. d-Xylose is most likely metabolised by the pentose phosphate pathway in this yeast.     

Optimization of exopolysaccharide production by Tremella mesenterica NRRL Y-6158 through implementation of fed-batch fermentation

In liquid culture conditions, the yeast-like fungus Tremella mesenterica occurs in the yeast state and synthesizes an exopolysaccharide (EPS) capsule, which is eventually released into the culture fluid. It is composed of an α-1,3-D-mannan backbone, to which β-1,2 side chains are attached, consisting of D-xylose and D-glucuronic acid. Potato dextrose broth (PDB) seemed to be an excellent medium for both growth of the yeast cells and synthesis of the EPS. This medium is composed solely of an extract of potatoes to which glucose was added. Yet an important disadvantage of this production medium is the presence of starch in the potato extract, since Tremella cells are not capable of metabolizing this component; furthermore, it coprecipitates upon isolation of the polymer [3]. In this respect, it was essential to remove the starch in order to achieve high polysaccharide production and recovery. A good method was the removal of starch through ultrafiltration of the PDB medium before inoculation of the strain. This resulted in an excellent starch-free medium in which other components essential for polysaccharide production were still present [3]. Through implementation of single and cyclic fed-batch fermentations with glucose feed, 1.6- and 2.2-fold increases in EPS yield were obtained, respectively. Lowering the carbon source level by using a cyclic fed-batch technique might decrease the osmotic effect of glucose or any catabolite regulation possibly exerted by this sugar on enzymes involved in EPS synthesis. Journal of Industrial Microbiology & Biotechnology (2002) 29, 181–184 doi:10.1038/sj.jim.7000276 Received 18 March 2002/ Accepted in revised form 20 May 2002     

Hexose-transport-deficient mutants of Chlorella vulgaris

Autotrophically grown cells of Chlorella vulgaris show a strong increase in the uptake rates for hexoses and for seven amino acids when incubated in the presence of hexoses. This increase is due to de-novo synthesis of three transport proteins: one forhexoses and two for amino acids. Mutants deficient in hexose transport were obtained after treatment of wild-type cells with acridine orange, followed by a selection procedure using the toxic hexose analogue, 2-deoxy-D-glucose. Moreover, the two amino-acid-transport systems could not be induced in these mutants by hexoses. The capacity to phosphorylate hexoses was identical in mutants and in the wild-type strain. The loss of transport activities can be correlated with the loss of certain radiolabeled protein bands on fluorograms of sodium dodecylsulfate-polyacrylamide gels. These proteins are assumed to be responsible for the different transport systems in the wild-type strain. With the help of additional mutants defective in one or two of the different aminoacid-transport systems, it has been attempted to assign the different transport activities to individual protein bands on the gel.Abbreviations AUP arginine-uptake-defective mutant - 2-DG 2-deoxy-D-glucose - 6-DG 6-deoxy-D-glucose - HUP hexose-uptake-defective mutant - PUP^- proline-uptake-defective mutant - SDS sodium dodecyl sulfate - WT wild type     

Carbon and nitrogen utilization and acid production by mycelia of the ectomycorrhizal fungusTricholoma bakamatsutake in vitro

Mycelial growth of an isolate ofT. bakamatsutake was tested in media with C/N ratio ranging from 0 to 50 and with 32 carbon and 12 nitrogen sources. The isolate grew best at the C/N ratio of 30. It utilized the monosaccharidesd-glucose,d-mannose, andd-fructose, the disaccharide trehalose, and polysaccharide pectin among the carbon sources; and yeast extract,l-glutamic acid, and ammonium compounds among the nitrogen sources. The growth of ten isolates and secretion of gluconic and oxalic acids were compared ind-glucose, trehalose, and pectin media. The utilization ofd-glucose, trehalose, and pectin differed among the ten isolates, but all the isolates secreted gluconic acid in thed-glucose media and oxalic acid in the pectin media.     

Presence of a sodium-dependentd-glucose transport system in the kidney of the atlantic hagfish (Myxine glutinosa)

Summary A membrane fraction, rich in brushborder membranes, was prepared from the archinephric duct of the atlantic hagfish (Myxine glutinosa) and the uptake ofd-glucose and other sugars into the membrane vesicles was investigated by a rapid filtration technique. Uptake ofd-glucose was found to be sodium-dependent, phloridzin-inhibitable and osmotically sensitive. A sodium gradient dependent overshoot was demonstrated at 25° C as well as at the more physiological temperature of 4°C. The sodium dependentd-glucose transport was inhibited by -methyl-d-glucoside, but not by 2-deoxy-d-glucose. Furthermore at the same concentration of sugars the initial uptake ofd-glucose was 7.2-fold higher thanl-glucose uptake.d-glucose transport across the membrane in the presence of a sodium gradient was stimulated when SCN^– replaced Cl^– and inhibited when gluconate replaced Cl^–.d-glucose uptake in the presence of a sodium- and potassium gradient was decreased by the addition of valinomycin. In addition, the presence of ad-glucose gradient enhanced sodium uptake into the vesicles as compared to a mannitolgradient. Phloridzin inhibited thed-glucose dependent sodium flux. Thus an electrogenic stereospecific sodium glucose co-transport system, with properties similar to that found in the kidney of higher vertebrates is present in this primitive vertebrate and might participate in secondary-active sugar reabsorption in the archinephric duct.     

Effect of culture conditions on astaxanthin production by a mutant of Phaffia rhodozyma in batch and chemostat culture

Temperature and pH had only a slight effect on the astaxanthin content of a Phaffia rhodozyma mutant, but influenced the maximum specific growth rate and cell yield profoundly. The optimum conditions for astaxanthin production were 22°C at pH 5.0 with a low concentration of carbon source. Astaxanthin production was growth-associated, and the volumetric astaxanthin concentration gradually decreased after depletion of the carbon source. The biomass concentration decreased rapidly during the stationary growth phase with a concomitant increase in the cellular content of astaxanthin. Sucrose hydrolysis exceeded the assimilation rates of D-glucose and D-fructose and these sugars accumulated during batch cultivation. D-Glucose initially delayed D-fructose uptake, but D-fructose utilization commenced before glucose depletion. In continuous culture, the highest astaxanthin content was obtained at the lowest dilution rate of 0.043 h^–1. The cell yield reached a maximum of 0.48 g cells·g^–1 glucose utilized between dilution rates of 0.05 h^–1 and 0.07 h^–1 and decreased markedly at higher dilution rates. Correspondence to: J. C. Du Preez