Cloning of Azorhizobium caulinodans nicotinate catabolism genes and characterization of their importance in N2 fixation.

Twenty Azorhizobium caulinodans vector insertion (Vi) mutants unable to catabolize nicotinate (Nic- phenotype) were identified and directly cloned as pVi plasmids. These pVi plasmids were used as DNA hybridization probes to isolate homologous wild-type sequences. From subsequent physical mapping experiments, the nic::Vi mutants defined four distinct loci. Two, possibly three, of these loci are physically linked. A. caulinodans nic loci II and III encode the structural genes for nicotinate catabolism; nic loci I and IV encode nicotinate-driven respiratory chain components. Recombinant lambda bacteriophages corresponding to three of these loci were subcloned in pRK293; resulting plasmids were used for complementation tests with resolved nic::IS50 derivatives of the nic::Vi mutants. When wild-type A. caulinodans was cultured in defined liquid medium under 3% O2, nicotinate catabolism stimulated N2 fixation 10-fold. In these exponentially growing cultures, the entire (300 microM) nicotinate supplement was exhausted within 10 h. While nic::Vi mutants retained the ability to fix some N2, they did so at rates only 10% of that of the wild type: nitrogenase activity by nic::Vi mutants was not stimulated by 300 microM added nicotinate. Higher-level (5 mM) nicotinate supplementation inhibited N2 fixation. Because 5 mM nicotinate repressed nitrogenase induction in all nic::Vi mutants as well, this repression was independent of nicotinate catabolism. During catabolism, nicotinate is first oxidized to 6-OH-nicotinate by a membrane-bound nicotinate hydroxylase which drives a respiratory chain to O2. In A. caulinodans wild-type cultures, added 300 microM 6-OH-nicotinate stimulated N2 fixation twofold better than did added 300 microM nicotinate. Likewise, nic::Vi mutant 61302, defective in nicotinate hydroxylase, fixed N2 at wild-type levels when supplemented with 300 microM 6-OH-nicotinate. Therefore, nicotinate catabolism stimulates N2 fixation not by nicotinate hydroxylase-driven respiration but rather by some subsequent aspect(s) of nicotinate catabolism.     

Identification of cyclic intermediates in Azorhizobium caulinodans nicotinate catabolism.

In wild-type Azorhizobium caulinodans ORS571, nicotinate served both as anabolic substrate for NAD+ production and as catabolic substrate for use as the N source. Catabolic enzyme activities were greatest from cultures grown with nicotinate as the N source and least when cultures were grown with ammonium as the N source. Vector insertion mutants unable to catabolize nicotinate (nic::Vi mutants) still required micromolar quantities of this compound for growth. Therefore, A. caulinodans wild type is NAD+ auxotrophic. As the first two intermediates in A. caulinodans nicotinate catabolism, two cyclic compounds, 6-hydroxynicotinate and 1,4,5,6-tetrahydro-6-oxonicotinate, were identified. These compounds were purified from the growth medium of strain 61009 (a nic::Vi mutant) by high-performance liquid chromatography; their identities were subsequently confirmed by UV absorbance, nuclear magnetic resonance, and mass spectra. The conversion of 1 mol of nicotinate to 6-hydroxynicotinate consumed 0.5 mol of O2. From 18O isotopic incorporation experiments, water was the hydroxyl-equivalent source. A nicotinate hydroxylase activity proved to be cell wall-membrane associated; this activity served as direct electron donor (not indirect via NADP+) to O2 via membrane electron transport. These catabolic reactions have not previously been witnessed together in the same organism. A. caulinodans nicotinate catabolism seems coupled to N2 fixation, although the explicit mechanism of this coupling remains to be determined.     

Transient kinetics of yeast growth in batch and continous culture with an inhibitory carbon and energy source

Growth and acetate metabolism by Candida utilis (ATCC 9226) is reported for both acetate- and zinc-limited cultures in defined media. Acetate concentrations were varied from suboptimal to inhibitory levels in both types of media in differential shake flask culture and in batch and continuous cultures in stirred fermentors. Transient responses of steady-state cultures to small or large additions of concentrated sodium acetate, or to shifts in dilution rate or inlet acetate concentration are compared with one another and with simple mathematical models of growth and acetate metabolism. Exponential growth was observed during unrestricted growth (differential shake flask and batch cultures) with both types of media. Addition of acetate during unrestricted growth always caused lags and for larger pulses, lower specific growth rates were observed after exponential growth resumed. Inhibition by high acetate concentrations was much greater in acetate–limited than in zinc–limited cultures. During restricted growth (steady-state, continuous cultures), high acetate concentrations again consistently caused growth lags but stimulated, inhibited, or temporarily stopped acetage uptake. Qualitative agreement between the predictions of a simple mathematical model of acetate inhibition fitted to differential shake flask data and the observed transient data was surprisingly good.     

Physiological analysis of Methylobacterium extorquens AM1 grown in continuous and batch cultures

Chemostat cultures of Methylobacterium extorquens AM1 grown on methanol or succinate at a range of dilution rates were compared to batch cultures in terms of enzyme levels, poly-β-hydroxybutyrate content, and intracellular concentrations of adenine and pyridine nucleotides. In both chemostat and batch cultures, enzymes specific to C₁ metabolism were up-regulated during growth on methanol and down-regulated during growth on succinate, polyhydroxybutyrate levels were higher on succinate, intracellular ATP levels and the energy charge were higher during growth on methanol, while the pools of reducing equivalents were higher during growth on succinate. For most of the tested parameters, little alteration occurred in response to growth rate. Overall, we conclude that the chemostat cultivation conditions developed in this study roughly mimic the growth in batch cultures, but provide a better control over the culturing conditions and a better data reproducibility, which are important for integrative functional studies. This study provides baseline data for future work using chemostat cultures, defining key similarities and differences in the physiology compared to existing batch culture data.     

Nitrogen fixation in molybdenum-deficient continuous culture by a strain of Azotobacter vinelandii carrying a deletion of the structural genes for nitrogenase (nifHDK).

Steady-state chemostat cultures of Azotobacter vinelandii strain CA11, carrying a deletion of genes encoding the structural polypeptides of nitrogenase nifHDK, were established in a simple defined medium chemically purified to minimize contamination by Mo. The medium contained no utilizable N source. Growth was dependent on N2 (1.1 X 10(8) viable cells X ml-1 at D = 0.176 h-1), and was inhibited by Mo (20 nM). DNA hybridization showed the deletion to be stable during prolonged (55 days) growth in the chemostat (132 doublings). Since batch cultures, using unsupplemented 'spent' chemostat medium, showed good growth (1.9 X 10(8) cells X ml-1), no requirement for subnanomolar concentrations of Mo was found. The biomass yield, as the dilution rate (D) was varied, showed that the N content of the culture, protein and dry wt. increased as D was decreased, indicating that neither N2 nor O2 were limiting growth. The limiting nutrient was not identified. Substantial amounts of H2 were evolved by the chemostat cultures, probably as the result of inhibition of O2-dependent hydrogenase activity by nitrilotriacetic acid present in the medium. Over a range of D values approx. 50% of the electron flux through the alternative system was allocated to H+ reduction. C2H2 was a poor substrate, being reduced at 0.14-0.1 times the rate of N2 fixation, calculated from the N content of the cells. SO4(2-)-limited steady-state continuous cultures of strain UW136 (wild-type for nifHDK) had a 2-fold greater biomass in the presence of MoO4(2-) (1 microM). The significance of this finding for 'Mo-limited' continuous cultures [Eady & Robson (1984) Biochem. J. 224, 853-862] is discussed.     

Degradation of 2,4-dichlorophenoxyacetic acid by Pseudomonas cepacia DBO1(pRO101) in a dual-substrate chemostat.

To determine the effect of a secondary carbon source on biodegradation of a chloroaromatic compound, Pseudomonas cepacia DBO1(pRO101) was grown in continuous cultures on basal salts media containing various mixtures of 2,4-dichlorophenoxyacetic acid (2,4-D) and succinate. Both succinate and 2,4-D were metabolized over the entire range of dilution rates and compositions analyzed (0.05 to 0.6 h-1). 2,4-Dichlorophenol (DCP), the only intermediate detected, accumulated to significant amounts (10 to 21 mg/liter) in the chemostat only when the dilution rate was 0.4 h-1 or greater. At these concentrations, DCP reduced the apparent growth rate of P. cepacia DBO1(pRO101) in batch cultures by 15 to 35% over the apparent growth rate on succinate alone. Succinate fed to the chemostat increased the cell density as well as the percentage of 2,4-D that was consumed at each dilution rate. When the amount of succinate in the feed exceeded the amount of 2,4-D, the specific rates of 2,4-D degradation in the chemostat or by washed cells were significantly lower than the specific rates for cells grown on 2,4-D alone, suggesting repression by succinate. However, when the amount of 2,4-D in the feed exceeded the amount of succinate, the specific rates of 2,4-D degradation remained at values equivalent to or higher than the specific rate for cells grown on 2,4-D alone. DCP accumulated significantly in the washed-cell assay, suggesting that the level of DCP hydroxylase is rate limiting.(ABSTRACT TRUNCATED AT 250 WORDS)     

Growth and enzymological characteristics of a pink-pigmented facultative methylotrophMethylobacterium sp. MB1

Growth characteristics of batch and continuous cultures of the pink facultative methylotrophMethylobacterium sp. MB1 were determined. The response of a chemostat culture to a pulse increase of methanol concentration was studied. Malate, succinate and oxaloacetate additions to the methanol-supplemented medium decreased batch culture growth inhibition by methanol. The carotenoid content in cells grown in a chemostat decreased with increasing growth rate. The key enzyme activities of C₁-metabolism were measured in a chemostat culture at different dilution rates.     

Cyclic-2,3-diphosphoglycerate levels in Methanobacterium thermoautotrophicum reflect inorganic phosphate availability

Methanobacterium thermoautotrophicum was grown in phosphate-limited chemostat cultures at a dilution rate corresponding to a doubling time of 13.2 h. The cyclic-2,3-diphospho-D-glycerate content of these cells was 8 to 10-fold lower than that of cells grown in batch cultures having a doubling time of 11.5 h. This metabolite accounted for 5% of cell dry weight during batch growth on 2 mM phosphate. In the chemostat the steady-state concentration of phosphate was 4 microM, showing that this methanogen is adapted to highly efficient growth at low phosphate concentrations. Since growth rates were similar in both cultures, the growth rate clearly does not depend on intracellular levels of cyclic-2,3-diphosphoglycerate.     

Influence of Carbon Source on Nitrate Removal by Nitrate-Tolerant Klebsiella oxytoca CECT 4460 in Batch and Chemostat Cultures

The nitrate-tolerant organism Klebsiella oxytoca CECT 4460 tolerates nitrate at concentrations up to 1 M and is used to treat wastewater with high nitrate loads in industrial wastewater treatment plants. We studied the influence of the C source (glycerol or sucrose or both) on the growth rate and the efficiency of nitrate removal under laboratory conditions. With sucrose as the sole C source the maximum specific growth rate was 0.3 h⁻¹, whereas with glycerol it was 0.45 h⁻¹. In batch cultures K. oxytoca cells grown on sucrose or glycerol were able to immediately use sucrose as a sole C source, suggesting that sucrose uptake and metabolism were constitutive. In contrast, glycerol uptake occurred preferentially in glycerol-grown cells. Independent of the preculture conditions, when sucrose and glycerol were added simultaneously to batch cultures, the sucrose was used first, and once the supply of sucrose was exhausted, the glycerol was consumed. Utilization of nitrate as an N source occurred without nitrite or ammonium accumulation when glycerol was used, but nitrite accumulated when sucrose was used. In chemostat cultures K. oxytoca CECT 4460 efficiently removed nitrate without accumulation of nitrate or ammonium when sucrose, glycerol, or mixtures of these two C sources were used. The growth yields and the efficiencies of C and N utilization were determined at different growth rates in chemostat cultures. Regardless of the C source, yield carbon (Y_C) ranged between 1.3 and 1.0 g (dry weight) per g of sucrose C or glycerol C consumed. Regardless of the specific growth rate and the C source, yield nitrogen (Y_N) ranged from 17.2 to 12.5 g (dry weight) per g of nitrate N consumed. In contrast to batch cultures, in continuous cultures glycerol and sucrose were utilized simultaneously, although the specific rate of sucrose consumption was higher than the specific rate of glycerol consumption. In continuous cultures double-nutrient-limited growth appeared with respect to the C/N ratio of the feed medium and the dilution rate, so that for a C/N ratio between 10 and 30 and a growth rate of 0.1 h⁻¹ the process led to simultaneous and efficient removal of the C and N sources used. At a growth rate of 0.2 h⁻¹ the zone of double limitation was between 8 and 11. This suggests that the regimen of double limitation is influenced by the C/N ratio and the growth rate. The results of these experiments were validated by pulse assays.     

Regulation of proteinase synthesis in Lactococcus lactis

The synthesis of extracellular serine proteinase of Lactococcus lactis was studied during the growth in a batch and a continuous culture on chemically defined media. In a batch culture the proteinase synthesis started during the exponential phase of growth and the highest proteinase concentrations were found at the end of the exponential and beginning of the stationary phase of growth. During the growth in a lactose-limited chemostat with amino acids as the sole source of nitrogen, the specific rate of proteinase synthesis was maximal at a μof 0.23 h^?1. At higher growth rates the proteinase productin declined. The proteinase synthesis was dependent on the amino acid sources in the medium. In batch cultures of L. lactis grown on a chemically defined medium with amino acids, the proteinase production was increased four-fold compared to media containing casein or a tryptic digest of casein as the sole source of nitrogen. The inhibition of the rate of proteinase synthesis by casein and peptides was also observed during the growth in a chemostat. The addition of the dipeptide leucylproline (final concentration of 100 μM) to a lactose-limited continuous culture during the steady state (D = 0.23 h^?1) resulted in a transient inhibition of the rate of proteinase synthesis. This suggested that exogenously supplied peptides control the regulation of proteinase synthesis of L. lactis.     

Accumulation of poly[(R)-3-hydroxyalkanoates] in Pseudomonas oleovorans during growth in batch and chemostat culture with different carbon sources

Pseudomonas oleovorans (ATCC 29347) was grown in batch and chemostat cultures with citrate, hexanoate, heptanoate, octanoate, and nonanoate as single carbon substrates. The growth medium for batch cultures was adjusted such that nitrogen (NH(4)(+)) limitation terminated the exponential-growth phase. During batch cultivation with octanoate or nonanoate the biomass continued to increase after depletion of ammonium due to the accumulation of medium-chain-length poly[(R)-3-hydroxyalkanoates] (mcl-PHAs). Additionally, a significant rate of mcl-PHA accumulation was also observed in the exponential-growth phase of batch cultures. It is well known that the accumulation of reserve materials is strongly dependent on the ratio of nutrients (here of carbon, C, and of nitrogen, N) and that in a batch culture the ratio of C:N is continuously changing. Therefore, we have also investigated the effect of defined ratios of C:N under constant cultivation conditions, namely at a fixed dilution rate (D) in a chemostat fed with different medium C:N ratios. These experiments were performed at a constant D of 0.2 h(-1). The concentration of the nitrogen source in the inflowing medium (N()) was kept constant, while its carbon concentration (C()) was increased stepwise, resulting in an increase of the medium carbon to nitrogen ratio (C()/N() ratio). The culture parameters and the cell composition of steady-state cultures were determined as a function of the C()/N() ratio in the feed medium. Mcl-PHA accumulation was detected during growth with the fatty acids, and three distinct regimes of growth limitation were discovered: In addition to carbon limitation at low, and nitrogen limitation at high C()/N() ratios, an intermediate growth regime of simultaneous limitation by carbon and nitrogen was detected where both substrates were used to completion. The width of this dual-nutrient-limited growth regime was dependent on the change in the yield factors for carbon and nitrogen (Y(X/C), Y(X/N)) measured during single-nutrient-limited growth.     

Ethanol production from xylose by Thermoanaerobacter ethanolicus in batch and continuous culture

The fermentation of xylose by Thermoanaerobacter ethanolicus ATCC 31938 was studied in pH-controlled batch and continuous cultures. In batch culture, a dependency of growth rate, product yield, and product distribution upon xylose concentration was observed. With 27 mM xylose media, an ethanol yield of 1.3 mol ethanol/mol xylose (78% of maximum theoretical yield) was typically obtained. With the same media, xylose-limited growth in continuous culture could be achieved with a volumetric productivity of 0.50 g ethanol/liter h and a yield of 0.42 g ethanol/g xylose (1.37 mol ethanol/mol xylose). With extended operation of the chemostat, variation in xylose uptake and a decline in ethanol yield was seen. Instability with respect to fermentation performance was attributed to a selection for mutant populations with different metabolic characteristics. Ethanol production in these T. ethanolicus systems was compared with xylose-to-ethanol conversions of other organisms. Relative to the other systems, T. ethanolicus offers the advantages of a high ethanol yield at low xylose concentrations in batch culture and of a rapid growth rate. Its disadvantages include a lower ethanol yield at higher xylose concentrations in batch culture and an instability of fermentation characteristics in continuous culture.     

Characteristics of N2 fixation in Mo-limited batch and continuous cultures of Azotobacter vinelandii.

Steady-state chemostat cultures of Azotobacter vinelandii were established in a simple defined medium that had been chemically purified to minimize Mo and that contained no utilizable combined N source. Growth was dependent on N2 fixation, the limiting nutrient being the Mo contaminating the system. The Mo content of the organisms was at least 100-fold lower than that of Mo-sufficient cultures, and they lacked the characteristic g = 3.7 e.p.r. feature of the MoFe-protein of nitrogenase. A characteristic of nitrogenase activity in vivo in Mo-limited populations was a disproportionately low activity for acetylene reduction, which was 0.3 to 0.1 of that expected from the rate of N2 reduction. Acetylene was also a poor substrate in comparison with protons as a substrate for nitrogenase, and did not markedly inhibit H2 evolution, in contrast with Mo-sufficient populations. In batch cultures in similar medium or 'spent' chemostat medium inoculated with Mo-limited organisms, the addition of Mo elicited a biphasic increased growth response at concentrations as low as 2.5 nM, provided that sufficient Fe was supplied. In this system V did not substitute for Mo, and Mo-deficient cultures ceased growth at a 25-fold lower population density compared with cultures supplemented with Mo. Nitrogenase component proteins could not be unequivocally detected by visual inspection of fractionated crude extracts of Mo-limited organisms. 35SO42-pulse-labelling studies also showed that the rate of synthesis of the MoFe-protein component of nitrogenase was too low to be quantified. However, the Fe-protein of nitrogenase was apparently synthesized at high rates. The discussion includes an evaluation of the possibility that A. vinelandii possesses an Mo-independent N2-fixation system.     

Glucose uptake of Cytophaga johnsonae studied in batch and chemostat culture

The influence of different physiological states on the glucose uptake and mineralization by Cytophaga johnsonae, a freshwater isolate, was examined in batch and chemostat cultures. At different growth rates under glucose limitation in chemostat cultures, different uptake patterns for ¹⁴C labeled glucose were observed. In batch culture and at high growth rates the glucose uptake potential showed a higher maximum velocity and a much lower substrate affinity than at lower growth rates. These findings and the results of short-term labeling patterns could be explained by two different glucose uptake mechanisms which enable the strain to grow efficiently both at high and low substrate concentrations. Substrate specificity studies showed that a structural change of the C-2 atom of the glucose molecule was tolerated by both systems. The consequences of these results for the ecophysiological classification of the Cytophaga group and for the operation of continuous cultures are discussed.     

Production of teicoplanin by Actinoplanes teichomyceticus in continuous fermentation.

Production of the potent antibiotic teicoplanin by Actinoplanes teichomyceticus was studied in batch and in chemostat cultures. It is found that the producing strain deactivates to a non-producing strain named NP-12. This strain is used to find the growth kinetics of the A. teichomyceticus without interference from the product teicoplanin. In batch experiments with NP-12 grown on glucose at different initial concentrations and with different added amounts of teicoplanin, the strong inhibitory effect of teicoplanin was determined. These results obtained on NP-12 were validated in a series of chemostat experiments with the processing strain. All experiments in batch and in chemostat cultures were well represented by Monod kinetics with respect to the carbon and energy source (glucose) and with a substantial inhibitory effect of teicoplanin. Further experiments were made with the producing strain in a continuous reactor coupled to a microfilter that delivers a cell-free permeate. It was found that the derived kinetics almost exactly simulated the behavior of the cell recirculation reactor in addition to when the cell concentration in the reactor was more than four times higher than in the chemostat. For industrial production of teicoplanin, a continuous reactor with cell recirculation and working with a low effluent glucose concentration was by far the best mode of operation. Finally, the deactivation of the producing strain to NP-12 was modeled by a two-step deactivation mechanism. Deactivation was independent of dilution rate but dependent on the inoculum preparation and on the previous history of the inoculum.     

Role of the ptsN gene product in catabolite repression of the Pseudomonas putida TOL toluene degradation pathway in chemostat cultures

The Pseudomonas putida KT2440 TOL upper pathway is repressed under nonlimiting conditions in cells growing in chemostat with succinate as a carbon source. We show that the ptsN gene product IIA(Ntr) participates in this repression. Crc, involved in yeast extract-dependent repression in batch cultures, did not influence expression when cells were growing in a chemostat with succinate at maximum rate.     

The continuously fed batch reactor for measuring microbial growth rates

The contiuously fed batch reactor (CFBR) is proposed as an alternative technique to the traditional chemostat and batch cultures, for measuring microbial growth rates. After reviewing the pitfalls which plague the conventional growth measurement techniques, the methodology for operating the CFBR to generate specific growth-rate-versus-substrate-concentration data is detailed. This information is extracted from the transient state of the CFBR where both the biomass and substrate concentration show extrema in time. It is suggested that the CFBR can be used for measuring microbial growth rates at low rates at low substrate concentrations where the chemostat method normally encounters difficulties.     

Microaerophilic growth of Wolinella recta ATCC 33238

Abstract The influence of oxygen on growth and fumarate-dependent respiration of Wolinella recta ATCC 33238 was studied in continuous culture. Steady states were obtained with formate-limited cultures grown at a specific growth rate of 0.1 h⁻¹ with different levels of oxygenation. The extent of aeration was regulated by means of a redox control system permitting reproducible cultivation at oxygen levels below the detection limit of conventional lead-silver probes. The ratio of succinate produced to that of formate consumed (Suc/For) decreased from 0.99 in strictly anaerobic cultures to 0.06–0.10 in aerated cultures. The growth yield did not change significantly with increasing redox readings: 4.9–5.2 g cell carbon/mol formate. The ability to use O₂ as the sole electron acceptor was demonstrated in a chemostat culture with formate as electron donor and succinate as carbon source. Washed cells from all chemostat cultures comsumed O₂ with formate as electron donor at a high rate (2.1–3.7 μmol/min per mg protein) and possessed b - and c -type cytochromes and CO-binding pigments. These results clearly indicated the microaerophilic nature of W. recta .     

Continuous culture of Pseudomonas fluorescens with sodium maleate as a carbon source

Pseudomonas fluorescens (ATCC 11150) was grown in batch and continuous culture in minimal media with sodium maleate as growth-limiting sole organic carbon source. Growth was followed by turbidity and dry weight measurements. Gross composition of washed cells (relative amounts of protein, lipid, RNA, and DNA) and the distribution of amino acids in protein hydrolyses of the cells were determined for cells grown in continuous culture at various dilution rates. Extracellular concentrations of the original carbon source and a number of metabolites were monitored by a total carbon analysis, ion exchange chromatography, and ultraviolet-visible scans of cell-free supernatants and chromatographic fractions, thereof. Substrate inhibition by maleate was a major factor in the growth kinetics of both batch and continuous cultures. Excessive maleate concentration caused instability in continuous cultures. By appropriate operation, much higher specific growth rates (0.305/hr) could ultimately be achieved in continuous culture compared to batch culture (0.174/hr). Adaptation was responsible for only part of the differences between batch and continuous cultures; the differing distribution of metabolites were also major factors.     

Optimization and stability of glucoamylase production by recombinant strains of Aspergillus niger in chemostat culture

When grown on a medium containing 5 g maltodextrin L-1, Aspergillus niger transformant N402[pAB6-10]B1, which has an additional 20 copies of the glucoamylase (glaA) gene, produced 320 +/- 8 mg (mean +/- S.E.) glucoamylase (GAM) L-1 in batch culture and 373 +/- 9 mg GAM L-1 in maltodextrin-limited chemostat culture at a dilution rate of 0.13 h-1. These values correspond to specific production rates (qp) of 5.6 and 16.0 mg GAM [g biomass]-1 h-1, respectively. In maltodextrin-limited chemostat cultures grown at dilution rates from 0.06 to 0.14 h-1, GAM was produced by B1 in a growth-correlated manner, demonstrating that a continuous flow culture system operated at a high dilution rate is an efficient way of producing this enzyme. In chemostat cultures grown at high dilution rates, GAM production in chemostat cultures was repressed when the limiting nutrient was fructose or xylose, but derepressed when the limiting nutrient was glucose (qp, 12.0), potassium (6.2), ammonium (4.1), phosphate (2.0), magnesium (1.5) or sulphate (0.9). For chemostat cultures grown at a dilution rate of 0.13 h-1, the addition of 5 g mycopeptone L-1 to a glucose-mineral salts medium resulted in a 64% increase in GAM concentration (from 303 +/- 12 to 496 +/- 10 mg GAM L-1) and a 37% increase in specific production rate (from 12.0 +/- 0.4 to 16.4 +/- 1.6 mg GAM [g biomass]-1 h-1). However, although recombinant protein production was stable for at least 948 h (191 generations) when A. niger B1 was grown in chemostat culture on glucose-mineral salts medium, it was stable for less than 136 h (27 generations) on medium containing mycopeptone. The predominant morphological mutants occurring after prolonged chemostat culture were shown to have selective advantage in the chemostat over the parental strain. Compared to their parental strains, two morphological mutants had similar GAM production levels, while a third had a reduced production level. Growth tests and molecular analysis revealed that the number of glaA gene copies in this latter strain (B1-M) was reduced, which could explain its reduced GAM production. Shake-flask cultures carried out with the various morphological mutants revealed that in batch culture all three strains produced considerably less GAM than their parent strains and even less than N402. We show that physiological changes in these morphological mutants contribute to this decreased level of GAM production.