Physiological aspects of continuous lactic acid fermentations at high dilution rates

The effects of the substrate conditions on the volumetric productivity of Lactobacillus helveticus at different cell densities up to 60 g l⁻¹ in a continuous stirred-tank reactor with microfiltration to retain the biomass were investigated. At low dilution rates, D, the steady-state volumetric productivity, r _p, gradually increased to a maximum at D = 1.2–1.5 h⁻¹, because of reduced product inhibition. At higher D values, r _p unexpectedly decreased, although the substrate conditions further improved. The maxima of r _p at different cell densities coincided with a critical specific substrate utilization rate beyond which the cell metabolism seems to be controlled through a catabolic modulator factor, and r _p decreases. Received: 8 September 1997 / Received last revision: 31 December 1997 / Accepted: 2 January 1998     

Continuous production of ethanol using yeast cells immobilized in preformed cellulose beads

 Saccharomyces cerevisiae cells were immobilized on preformed cellulose beads by adsorption. The fermentation capacity of the immobilized yeast cells was found to be practically independent of the hydrogen ion concentration between pH 3.1 and 6.25. The fermentation capacity was maximal at 30 °C. The immobilized yeast cells were used for continuous production of ethanol in a fluidized-bead reactor. The average values characteristic for the process were an ethanol concentration of 41.9±0.1 g l^-1, a fermentation efficiency of 82.9±2.1% and a volumetric productivity of 3.94±0.52 g l^-1 h^-1. Received: 9 October 1995/Accepted: 22 April 1996     

Caroteno-protein and exopolysaccharide production by co-cultures of Rhodotorula glutinis and Lactobacillus helveticus

The lactose-negative yeast Rhodotorula glutinis 22P and the homofermentative lactic acid bacterium Lactobacillus helveticus 12A were cultured together in a cheese whey ultrafiltrate containing 42 g L⁻¹ lactose. The chemical composition of the caroteno-protein has been determined. The carotenoid and protein contents are 248  μ g g⁻¹ dry cells and 48.2% dry weight. Carotenoids produced by Rhodotorula glutinis 22P have been identified as β-carotene 15%, torulene 10%, and torularhodin 69%. After separating the cell mass from the microbial association, the exopolysaccharides synthesized by Rhodotorula glutinis 22P were isolated from the supernatant medium in a yield of 9.2 g L⁻¹. The monosaccharide composition of the synthesized biopolymer was predominantly D-mannose (57.5%). Received 08 July 1996/ Accepted in revised form 11 December 1996     

Genetic variation for in vitro sesame pollen germination and tube growth

  In vitro pollen germination and tube length studies are valuable in elucidating mechanisms (germination capacity and rate, tube growth rate) possibly associated with genetic differences in male transmission. On each of two collection dates, the percentage germination and tube length of the binucleate pollen grains from five diverse sesame (Sesamum indicum L.) genotypes were determined at eight times (30, 60, 90, 120, 150, 180, 240, 300 min) after inoculation on a semisolid medium containing 10% (100 g l^-1) sucrose (C₁₂H₂₂O₁₁), 0.4% (4 g l^-1) purified agar (Fisher Lot 914409), 0.1% (1 g l^-1) calcium nitrate [Ca(NO₃)₂ ⋅ 4H₂O] and 0.01% (100 mg l^-1) boric acid (H₃BO₃). Before heating, the pH of the medium was adjusted to 7.0 with a 0.1 N potassium hydroxide (KOH) solution. Over the five genotypes, 5% germination was found 30 min after inoculation and a maximum of 37% germination 120 min after inoculation with no significant changes thereafter. As indicated by the highly significant genotype×time after inoculation interaction, the genotypes differed in the time at which germination was initiated and maximum germination attained. Over all five genotypes, the tube length was 91 μm 30 min after inoculation, reaching a maximum of 1000 μm 300 min after inoculation. As shown by the highly significant genotype×time after inoculation interaction, the genotypes differed in the time at which tube length was observed and the maximum tube length was attained. Little or no relationship between percent germination and tube length was observed among the genotypes. For both percent germination and tube length, the statistical significance of collection date and its interactions with genotype and time after inoculation indicated that environment in the form of collection date was also an influencing factor. These results indicated that genetic differences among genotypes were present for in vitro germination capacity, germination rate and tube growth rate and that these factors singly or in combination could alter male transmission of genetic elements. Received: 5 February 1997 / Accepted: 23 June 1997     

The production of xylitol from d-xylose by fermentation with Hansenula polymorpha

We have analysed the influence of the initial pH of the medium and the quantity of aeration provided during the batch fermentation of solutions of d-xylose by the yeast Hansenula polymorpha (34438 ATCC). The initial pH was altered between 3.5 and 6.5 whilst aeration varied between 0.0 and 0.3 vvm. The temperature was kept at 30 °C during all the experiments. Hansenula polymorpha is known to produce high quantities of xylitol and low quantities of ethanol. The most favourable conditions for the growth of xylitol turned out to be: an initial pH of between 4.5 and 5.5 and the aeration provided by the stirring vortex alone. Thus, at an initial pH of 5.5, the maximum specific production rate (μ_m) was 0.41 h⁻¹, the overall biomass yield (Y _x/s ^G) was 0.12 g g⁻¹, the specific d-xylose-consumption rate (q _s ) was 0.075 g g⁻¹ h⁻¹ (for t = 75 h), the specific xylitol-production rate (q _Xy ) was 0.31 g g⁻¹ h⁻¹ (for t = 30 h) and the overall yields of ethanol (Y _E/s ^G) and xylitol (Y _Xy/s ^G) were 0.017 and 0.61 g g⁻¹ respectively. Both q _s and q _Xy decreased during the course of the experiments once the exponential growth phase had finished. Received: 26 March 1998 / Received revision: 30 June 1998 / Accepted: 2 July 1998     

Ethanol production using nuclear petite yeast mutants

Two respiratory-deficient nuclear petites, FY23Δpet191 and FY23Δcox5a, of the yeast Saccharomyces cerevisiae were generated using polymerase-chain-reaction-mediated gene disruption, and their respective ethanol tolerance and productivity assessed and compared to those of the parental grande, FY23WT, and a mitochondrial petite, FY23ρ⁰. Batch culture studies demonstrated that the parental strain was the most tolerant to exogenously added ethanol with an inhibition constant. K _i, of 2.3% (w/v) and a specific rate of ethanol production, q _p, of 0.90 g ethanol g dry cells⁻¹ h⁻¹. FY23ρ⁰ was the most sensitive to ethanol, exhibiting a K _i of 1.71% (w/v) and q _p of 0.87 g ethanol g dry cells⁻¹ h⁻¹. Analyses of the ethanol tolerance of the nuclear petites demonstrate that functional mitochondria are essential for maintaining tolerance to the toxin with the 100% respiratory-deficient nuclear petite, FY23Δpet191, having a K _i of 2.14% (w/v) and the 85% respiratory-deficient FY23Δcox5a, having a K _i of 1.94% (w/v). The retention of ethanol tolerance in the nuclear petites as compared to that of FY23ρ⁰ is mirrored by the ethanol productivities of these nuclear mutants, being respectively 43% and 30% higher than that of the respiratory-sufficient parent strain. This demonstrates that, because of their respiratory deficiency, the nuclear petites are not subject to the Pasteur effect and so exhibit higher rates of fermentation. Received: 22 September 1997 / Accepted: 7 December 1997     

Shake-flask culture of Laccaria laccata,an ectomycorrhizal basidiomycete

 Large-scale exploitation of the potential benefits of ectomycorrhizal fungi in improving plantation yields means that fermentation techniques for these fungi will be required. Starting with a base performance on a rich, complex medium, the effect of variations in some physicochemical culture parameters on biomass yield was studied. It was possible to reduce the amount of phosphate salts (to 1/9th) and other ingredients (to 1/3rd) in the medium. A shaking speed of either 100 rpm or 200 rpm in an orbital incubator was satisfactory and biomass yield responded to an increase in carbon substrate (glucose, from 10 g l^-1 and 20 g l^-1) though Y _x/s declined. An increase in inoculum size shortened culture time but decreased biomass yield. The upper limit of the incubation temperature was between 25°C and 30°C. Biomass yields were about 12 g l^-1 dry weight (Y _x/s=0.63) when 20 g l^-1 glucose was supplied, and about 7 g l^-1 (Y _x/s=0.74) when 10 g l^-1 glucose was supplied. Received: 9 October 1995/Accepted: 4 December 1995     

Pentachlorophenol biodegradation kinetics of an oligotrophic fluidized-bed enrichment culture

A fluidized-bed reactor (FBR) was used to enrich an aerobic chlorophenol-degrading microbial culture. Long-term continuous-flow operation with low effluent concentrations selected oligotrophic microorganisms producing good-quality effluent for pentachlorophenol(PCP)-contaminated water. PCP biodegradation kinetics was studied using this FBR enrichment culture. The results from FBR batch experiments were modeled using a modified Haldane equation, which resulted in the following kinetic constants: q _max = 0.41 mg PCP mg protein⁻¹ day⁻¹, K _S = 16 μg l⁻¹, K _i = 5.3 mg l⁻¹, and n = 3.5. These results show that the culture has a high affinity for PCP but is also inhibited by relatively low PCP concentrations (above 1.1 mg PCP l⁻¹). This enrichment culture was maintained over 1 year of continuous-flow operation with PCP as the sole source of carbon and energy. During continuous-flow operation, effluent concentrations below 2 μg l⁻¹ were achieved at 268 min hydraulic retention time (t _HR) and 2.5 mg PCP l⁻¹ feed concentration. An increase in loading rate by decreasing t _HR did not significantly deteriorate the effluent quality until a t _HR decrease from 30 min to 21 min resulted in process failure. Recovery from process failure was slow. Decreasing the feed PCP concentration and increasing t _HR resulted in an improved process recovery. Received: 10 October 1996 / Received revision: 21 January 1997 / Accepted: 24 January 1997     

The effect of inoculation and the type of carrier material used on the biofiltration of methyl sulphides

 Low elimination capacities (less than 10 g m^-3 day^-1) were observed for the odorant dimethyl sulphide (Me₂S) when either wood bark or compost was used as the carrier material in a laboratory-scale biofilter. Enrichment experiments were set up by incubation of garden soil samples during 4 weeks with 100 ppm (v/v) headspace concentrations of both Me₂S and dimethyl disulphide (Me₂S₂). After transfer to a mineral medium, Me₂S- and Me₂S₂-degrading enrichment cultures were obtained for all five soil samples tested, both compounds being converted stoichiometrically to sulphuric acid. Upon inoculation of the laboratory-scale biofilter with one of these enrichment cultures (±120 g cell dry weight m^-3 reactor), the elimination capacity for Me₂S increased in a 3-week period to 35 g m^-3 day^-1 and 680 g m^-3 day^-1 when wood bark and compost were used as the respective carrier materials. Both inoculated biofilters were able to degrade Me₂S₂, however the elimination capacities obtained for Me₂S₂ were lower (e.g. 24 g m^-3 day^-1 for the wood bark filter) compared to those for Me₂S. For both inoculated biofilters, a gradual decrease of the elimination capacity for the methyl sulphides was observed as a result of acidification of the carrier material, suggesting that pH regulation is necessary if long-term biofiltration experiments are to be performed. Received: 6 June 1995/Received revision: 10 August 1995/Accepted: 22 August 1995     

Lactose and galactose uptake by genetically engineered Pediococcus species

The ability to utilize lactose is requisite for lactic acid bacteria used as starters in the dairy industry. Modern genetic recombination techniques have facilitated the introduction of the lactose-positive phenotype into bacteria such as Pediococcus species, which traditionally have not been used as dairy starters. This study investigated lactose and galactose uptake along with phospho-β-galactosidase activity in pediococci that had been transformed with a Latococcus lactis lactose plasmid. Lactose-positive transformants, Pediococcus acidilactici SAL and Pediococcus pentosaceus SPL-2, demonstrated an ability to accumulate [¹⁴C]lactose at a rate greater than the Lactococcus lactis control. Phospho-β-galactosidase activity was also higher in transformants versus Lactococcus lactis. Studies of [³H]galactose uptake suggested that a wild-type galactose transport system and the introduced lactose phosphotransferase system both functioned in galactose uptake by Pediococcus spp. transformants. Significantly lower levels of free galactose were detected in milk fermented with Lactobacillus helveticus LH100 and SAL or SPL-2 than in milk fermented with a LH100 plus Streptococcus thermophilus TA061 control starter blend. Received: 16 September 1997 /  Received revision: 11 November 1997 / Accepted: 21 November 1997     

Transition rate kinetics from ethanol oxidation to glucose utilisation within a structured model of baker’s yeast

 The transition rate kinetics from ethanol oxidation to glucose utilisation, within a structured model of baker’s yeast, described previously, were experimentally identified. The shift in metabolism has been assessed through glucose pulses during batch growth on ethanol. The influence of glucose concentration (between 0.25 g l^-1 and 0.90 g l^-1) and initial biomass concentration (between 0.61 g l^-1 and 1.44 g l^-1) on the transition rate was determined. The transition rate can not be described by a first-order saturation-type kinetics with respect to glucose only. A corrective term, which takes into account biomass concentration should be included. Received: 28 April 1995/Received revision: 6 July 1995/Accepted: 22 August 1995     

Denitrifying and methanogenic bacteria in the biofilm of a fixed-film reactor operated with methanol/nitrate demonstrated by immunofluorescence and microscopy

 A denitrifying bacterial biofilm population established on a polypropylene substratum of a fixed-film reactor was characterized by microscopy, scanning electron microscopy and immunofluorescence after 120 days of operation. The reactor, operated at pH 7.0, 22°C, and −180 mV with synthetic wastewater containing methanol/nitrate, achieved a denitrification rate of 0.24 mol NO^- ₃ l^-1 day^-1 with a removal efficiency for nitrate of 95%–99% at an organic loading rate of 0.325 mol methanol l^-1 day^-1. The gas produced contained 2%–3% (v/v) methane and 3%–4% (v/v) carbon dioxide in addition to nitrogen. The biofilm contained mainly cells of Methanobrevibacter arboriphilus antigenically related to strain DC, short, flagellated, gram-negatively staining rods of Pseudomonas sp. antigenically related to Pseudomonas stutzeri strain AN11, non-identified pink-pigmented rods and small lemon-shaped cells with mono- and bipolar appendages resembling prosthecate Hyphomicrobium sp. The biofilm analysis provided evidence for a syntrophy between the denitrifying, methylotrophic, bacterial consortium and hydrogenotrophic methanogens, which were identified by antigenic fingerprinting with 17 antibody probes. Received: 11 July 1994/Received revision: 23 September 1994/Accepted: 28 September 1994     

Pullulan production from deproteinized whey by Aureobasidium pullulans

Aureobasidium pullulans P56 was investigated using an adaptation technique and a mixed culture system. The adaptation of A. pullulans and the mixed cultures of A. pullulans and/or Lactobacillus brevisX20, Debaryomyces hansenii 194 and Aspergillus niger did not increase the production of polysaccharide. Enzymic hydrolysis of lactose in deproteinized whey gave a higher polysaccharide concentration and polysaccharide yield than acidic hydrolysed lactose. Maximum polysaccharide concentration (11.0 ± 0.5 g L⁻¹), biomass dry weight (10.5 ± 0.4 g L⁻¹), polysaccharide yield (47.2 ± 1.8%) and sugar utilization (93.2 ± 2.8%) were achieved using enzyme-hydrolysed whey (pH 6.5) containing 25 g L⁻¹ lactose and supplemented with K₂HPO₄ 0.5%, L-glutamic acid 1%, olive oil 2.5%, and Tween 80 0.5%. In this case the pullulan content of the crude polysaccharide was 40%. Received 16 December 1997/ Accepted in revised form 12 March 1999     

Picophytoplankton biomass, community structure and productivity in the Great Astrolabe Lagoon, Fiji

 Phytoplankton biomass, community structure and productivity of the Great Astrolabe lagoon and surrounding ocean were studied using measurements of chlorophyll concentration and carbon uptake. The contribution of picophytoplankton to biomass, productivity and community structure was estimated by size fractionation, ¹⁴C-incubation and flow cytometry analysis. Picoplankton red fluorescence was demonstrated to be a proxy for chlorophyll <3 μm. Consequently, the percentage contribution to chl a<3 μm from each picoplankton group could be calculated using regression estimated values of ψ _i (fg chl a per unit of red fluorescence). In the lagoon, average chlorophyll concentration was 0.8 mg m^-3 with 45% of phytoplankton <3 μm. Primary production reached 1.3 g C m^-2 day^-1 with 53% due to phytoplankton <3 μm. Synechococcus was the most abundant group at all stations, followed by Prochlorococcus and picoeukaryotes. At all stations, Prochlorococcus represented less than 4% of the chl a <3 μm, Synechococcus between 85 and 95%, and Picoeukaryotes between 5 and 10%. In the upper 40 m of surrounding oceanic waters, phytoplankton biomass was dominated by the >3 μm size fraction. In deeper water, the <1 μm size fraction dominated. Prochlorococcus was the most abundant picoplankton group and their contributions to the chlorophyll a<3 μm were close to that of the picoeukaryotes (50% each). Accepted: 27 May 1999     

Cell-free extract(s) of Pseudomonas putida catalyzes the conversion of cyanides,cyanates, thiocyanates,formamide, and cyanide-containing mine waters into ammonia

 Our isolate, Pseudomonas putida, is known to be capable of utilizing cyanides as the sole source of carbon (C) and nitrogen (N) both in the form of free cells and cells immobilized in calcium alginate. In the present study, the cell-free extract(s) were prepared from the cells of P. putida grown in the presence of sodium cyanide. The ability of enzyme(s) to convert cyanides, cyanates, thiocyanates, formamide and cyanide-containing mine waters into ammonia (NH₃) was studied at pH 7.5 and pH 9.5. The kinetic analysis of cyanide and formamide conversion into NH₃ at pH 7.5 and pH 9.5 by the cell-free extract(s) of P. putida was also studied. The K _m and V _max values for cyanide/formamide were found to be 4.3/8 mM and 142/227 μmol NH₃ released mg protein^-1 min^-1 respectively at pH 7.5 and 5/16.67 mM and 181/434 μmol NH₃ released mg protein^-1 h^-1 respectively at pH 9.5. The study thus concludes that the cell-free extract(s) of P. putida is able to metabolize not only cyanides, cyanates, thiocyanates, and formamide but also cyanide-containing mine waters to NH₃. Received: 10 April 1995/Received revision: 24 July 1995/Accepted: 22 August 1995     

Continuous production of l(+)-lactic acid by Lactobacillus casei in two-stage systems

A two-stage two-stream chemostat system and a two-stage two-stream immobilized upflow packed-bed reactor system were used for the study of lactic acid production by Lactobacillus casei subsp casei. A mixing ratio of D ₁₂/D ₂= 0.5 (D = dilution rate) resulted in optimum production, making it possible to generate continuously a broth with high lactic acid concentration (48 g l⁻¹) and with a lowered overall content of initial yeast extract (5  g l⁻¹), half the concentration supplied in the one-step process. In the two-stage chemostat system, with the first stage at pH 5.5 and 37 °C and a second stage at pH 6.0, a temperature change from 40 °C to 45 °C in the second stage resulted in a 100% substrate consumption at an overall dilution rate of 0.05 h⁻¹. To increase the cell mass in the system, an adhesive strain of L. casei was used to inoculate two packed-bed reactors, which operated with two mixed feedstock streams at the optimal conditions found above. Lactic acid fermentation started after a lag period of cell growth over foam glass particles. No significant amount of free cells, compared with those adhering to the glass foam, was observed during continuous lactic acid production. The extreme values, 57.5 g l⁻¹ for lactic acid concentration and 9.72 g l⁻¹ h⁻¹ for the volumetric productivity, in upflow packed-bed reactors were higher than those obtained for free cells (48 g l⁻¹  and 2.42 g l⁻¹ h⁻¹) respectively and the highest overall l(+)-lactic acid purity (96.8%) was obtained in the two-chemostat system as compared with the immobilized-cell reactors (93%). Received: 4 December 1997 / Received revision: 23 February 1998 / Accepted: 14 March 1998     

Effect of temperature and various nitrogen sources on L(+)-lactic acid production by Lactobacillus casei

 Two homofermentative strains, Lactobacillus casei NRRL B-441 and Lactobacillus casei subsp. rhamnosus NRRL B-445 were selected for further study from 17 lactic acid bacterial strains screened for lactic acid production. The effect of temperature on lactic acid production with the selected strains was investigated by adapting both strains to four different temperatures. The production of L(+)-lactic acid by both strains was most efficient at 37°C, although with L. casei the highest lactic acid concentration was obtained at 41°C. The maximal volumetric productivity with L. casei was 4.1 g l^-1 h^-1 and with L. casei subsp. rhamnosus 3.5 g l^-1 h^-1. The composition of the medium was studied in order to replace the costly yeast extract with less expensive sources of nitrogen and amino acids. From 11 different nitrogen sources investigated at 37°C, barley malt sprouts (88 g l^-1 lactic acid in 66 h) and grass extract (74 g l^-1 lactic acid in 73 h) were the best economic alternatives. The effect of different combinations of yeast extract, peptone and malt sprouts was further studied by using statistical experimental design, and an empirical second-order polynomial model was constructed on the basis of the results. With the right combination most of the yeast extract could be substituted by barley malt sprouts for efficient lactic acid production. A method for extraction of nutrients and growth factors from malt sprouts is also described. Received: 25 September 1995/Accepted: 24 October 1995     

Electrogenic cation transport across leech caecal epithelium

 Electrogenic cation transport across the caecal epithelium of the leech Hirudo medicinalis was investigated using modified Ussing chambers. Transepithelial resistance (R _T ) and potential difference (V _T ) were 61.0±3.5 Ω ⋅ cm² and −1.1±0.2 mV (n=149), respectively, indicating that leech caecal epithelium is a “leaky” epithelium. Under control conditions short circuit current (I _SC ) and transepithelial Na⁺ transport rate (I _Na ) averaged at 22.1±1.5 μA ⋅ cm^-2 and 49.7±2.6 μA ⋅ cm^-2, respectively. Mucosal application of amiloride (100 μmol ⋅ l^-1) or benzamil (50 μmol ⋅ l^-1) influenced neither I _SC nor I _Na . The transport system in the apical membrane showed no pronounced cation selectivity and a linear dependence on mucosal Na⁺ concentration. Removal of mucosal Ca²⁺ increased I _SC by about 50% due to an increase of transepithelial Na⁺ transport. Trivalent cations (La³⁺ and Tb³⁺, 1 mmol ⋅ l^-1 both) added to the mucosal Ringer solution reduced I _Na by more than 40%. Serosal ouabain (1 mmol ⋅ l^-1) almost halved I _SC and I _Na while 0.1% (=5.4 mmol ⋅ l^-1) DNP decreased I _Na to 11.8±5.1% of initial values. Serosal addition of cAMP increased both I _SC and I _Na whereas the neurotransmitters FMRFamide, acetylcholine, GABA, L-dopa, serotonin and dopamine failed to show any effects; octopamine, glycine and L-glutamate reduced I _Na markedly. On the basis of these results we conclude that in leech caecal epithelium apical uptake of monovalent cations is mediated by non-selective cation conductances which are sensitive to extracellular Ca²⁺ but insensitive to amiloride. Basolaterally Na⁺ is extruded via ouabain-sensitive and -insensitive ATPases. cAMP activates Na⁺ transport across leech caecal epithelium, although the physiological stimulus for cAMP-production remains unknown. Accepted: 20 May 1996     

Selection of an adhesive phenotype of Streptococcus salivarius subsp. thermophilus for use in fixed-bed reactors

 Streptococcus salivarius subsp. thermophilus was cultivated in a chemostat in order to obtain an adhesive phenotype of this strain. When the system was operated at low dilution rates (D<0.2 h^-1) for about 4 weeks, the strain formed a visible film on the surface of the culture vessel. The biofilm cells were not washed out even when dilution rates were increased (D=6.9 h^-1), and this resulted in a high biomass productivity (P=4.1 g l^-1h^-1). On the other hand, when the culture was grown at dilution rates faster than 0.2 h^-1, only the free suspended cells were present in the culture broth, and were washed out at velocities of about 1.0 h^-1. The biomass productivity was consequently lower (P=1.33 g l^-1h^-1) than in the previous case. The selected adhesive phenotype was grown on different glass beads and the possibility of lactate fermentation in a continuous and semicontinuous mode was demonstrated. Received: 16 August 1995/Received revision: 18 March 1996/Accepted: 25 March 1996     

The diversion of lactose carbon through the tagatose pathway reduces the intracellular fructose 1,6-bisphosphate and growth rate of Streptococcus bovis

Twenty strains of Streptococcus bovis grew more slowly on lactose (1.21 ± 0.12 h⁻¹) than on glucose (1.67 ± 0.12 h⁻¹), and repeated transfers or prolonged growth in continuous culture (more than 200 generations each) did not enhance the growth rate on lactose. Lactose transport activity was poorly correlated with growth rate, and slow growth could not be explained by the ATP production rate (catabolic rate). Batch cultures growing on lactose always had less␣intracellular fructose 1,6-bisphosphate (Fru1,6P ₂) than cells growing on glucose (6.6 mM compared to 16.7 mM), and this difference could be explained by the pathway of carbon metabolism. Glucose and the glucose moiety of lactose were metabolized by the Embden-Meyerhoff-Parnas (EMP) pathway, but the galactose moiety of lactose was catabolized by the tagatose pathway, a scheme that by-passed Fru1,6P ₂. A mutant capable of co-metabolizing lactose and glucose grew more rapidly when glucose was added, even though the total rate of hexose fermentation did not change. Wild-type S. bovis grew rapidly with galactose and melibiose, but these galactose-containing sugars were activated by galactokinase and catabolized via EMP. On the basis of these results, rapid glycolytic flux through the EMP pathway is needed for the rapid growth (more than 1.2 h⁻¹) of S.␣bovis. Received: 3 June 1997 / Received revision: 10 September 1997 / Accepted: 6 January 1998