Requirement of heme for growth of Bacteroides fragilis.

Heme or protoporphyrin IX was required for growth of Bacteroides fragilis in a defined medium. The amount of heme necessary for half-maximal growth was 2 to 10 ng/ml (3.8 to 15 pmol/ml) among the Bacteroides species and strains tested. The growth rate, metabolic products from glucose fermentation, and cell yields were affected by the concentration of heme in the medium and by the length of time the culture was incubated. When heme was growth limiting (4 ng/ml), growth rates decreased by 50%, cultures started producing lactic and fumaric acids, and the cell yields declined. The cell yield for B. fragilis (ATCC 25285) at 24 h in medium containing 6.5 microgram of heme per ml was 69 g (dry weight) of cells per mol of glucose compared to 16 g (dry weight) of cells per mol of glucose with 4 ng of heme per ml. B. fragilis was unable to grow in defined medium when a porphyrin precursor, delta-aminolevulenic acid or porphobilinogen, was added in place of heme.     

Pathway of Succinate and Propionate Formation in Bacteroides fragilis

Cell suspensions of Bacteroides fragilis were allowed to ferment glucose and lactate labeled with (14)C in different positions. The fermentation products, propionate and acetate, were isolated, and the distribution of radioactivity was determined. An analysis of key enzymes of possible pathways was also made. The results of the labeling experiments showed that: (i) B. fragilis ferments glucose via the Embden-Meyerhof pathway; and (ii) there was a randomization of carbons 1, 2, and 6 of glucose during conversion to propionate, which is in accordance with propionate formation via fumarate and succinate. The enzymes 6-phosphofrucktokinase (pyrophosphate-dependent), fructose-1,6-diphosphate aldolase, phosphoenolpyruvate carboxykinase, malate dehydrogenase, fumarate reductase, and methylmalonyl-coenzyme A mutase could be demonstrated in cell extracts. Their presence supported the labeling results and suggested that propionate is formed from succinate via succinyl-, methylmalonyl-, and propionyl-coenzyme A. From the results it also is clear that CO(2) is necessary for growth because it is needed for the formation of C4 acids. There was also a randomization of carbons 1, 2, and 6 of glucose during conversion to acetate, which indicated that pyruvate kinase played a minor role in pyruvate formation from phosphoenolpyruvate. Phosphoenolpyruvate carboxykinase, oxaloacetate decarboxylase, and malic enzyme (nicotinamide adenine dinucleotide phosphate-dependent) were present in cell extracts of B. fragilis, and the results of the labeling experiments agreed with pyruvate synthesis via oxaloacetate and malate if these acids are in equilibrium with fumarate. The conversion of [2-(14)C]- and [3-(14)C]lactate to acetate was not associated with a randomization of radioactivity.     

Evidence for cytochrome involvement in fumarate reduction and adenosine 5'-triphosphate synthesis by Bacteroides fragilis grown in the presence of hemin.

Growth of Bacteroides fragilis subsp. fragilis on glucose was very much stimulated by the addition of hemin (2 mg/liter) to the medium. The generation time decreased from 8 to 2 h, and the molar growth yield increased from YM = 17.9 to YM = 47 g (dry weight) of cells per mol of glucose. In the absence of hemin, glucose was fermented to fumarate, lactate, and acetate. The cells did not contain detectable amounts of cytochromes or fumarate reductase. In the presence of hemin, the major products of fermentation were succinate, propionate, and acetate. A b-type cytochrome, possibly a c-type cytochrome, and a very active fumarate reductase were present in the cells. It is concluded from these results that hemin is required by B. fragilis to synthesize a functional fumarate reductase and that the hemin-dependent, enormous increase of the growth yield may be due to adenosine 5'-triphosphate production during reduction of fumarate to succinate.     

Inhibition of Clostridium perfringens sporulation by Bacteroides fragilis and short-chain fatty acids

The effect a common fecal organism, Bacteroides fragilis, has on the sporulation of Clostridium perfringens, an organism linked to some cases of antibiotic associated diarrhea, was examined. Established B. fragilis cultures significantly decreased the number of heat resistant spores formed by C. perfringens ATCC 12915 and increased the number of vegetative cells. To determine if short-chain fatty acids (SCFA), fermentation products of B. fragilis, inhibited sporulation, the SCFA were added to sporulation broth. Sporulation decreased in the presence of acetate, isobutyrate, isovalerate, and succinate. Vegetative cell number for C. perfringens decreased in the cultures with isobutyrate. Propionate did not affect sporulation or vegetative cell number. The data support the hypothesis that the decrease in short-chain fatty acid concentration following antibiotic therapy predisposes patients to diarrheas caused by C. perfringens.     

Features of rumen and sewage sludge strains of Eubacterium limosum, a methanol- and H2-CO2-utilizing species

Eubacterium limosum was isolated as the most numerous methanol-utilizing bacterium in the rumen fluid of sheep fed a diet in which molasses was a major component (mean most probable number of 6.3 X 10(8) viable cells per ml). It was also isolated from sewage sludge at 9.5 X 10(4) cells per ml. It was not detected in the rumen fluid of a steer on a normal hay-grain diet, although Methanosarcina, as expected, was found at 9.5 X 10(5) cells per ml. The doubling time of E. limosum in basal medium (5% rumen fluid) with methanol as the energy source (37 degree C) was 7 h. Acetate, cysteine, carbon dioxide, and the vitamins biotin, calcium-D-pantothenate, and lipoic acid were required for growth on a chemically defined methanol medium. Acetate, butyrate, and caproate were produced from methanol. Ammonia or each of several amino acids served as the main nitrogen source. Other energy sources included adonitol, arabitol, erythritol, fructose, glucose, isoleucine, lactate, mannitol, ribose, valine, and H2-CO2. The doubling time for growth on H2-CO2 (5% rumen fluid, 37 degree C) was 14 h as compared with 5.2 h for isoleucine and 3.5 h for glucose. The vitamin requirements for growth on H2-CO2 were the same as those for methanol; however, acetate was not required for growth on H2-CO2, although it was necessary for growth on valine, isoleucine, and lactate and was stimulatory to growth on glucose. Acetate and butyrate were formed during growth on H2-CO2, whereas branched-chain fatty acids and ammonia were fermentation products from the amino acids. Heat tolerance was detected, but spores were not observed. The type strain of E. limosum (ATCC 8486) and strain L34, which was isolated from the rumen of a young calf, grew on methanol, H2-CO2, valine, and isoleucine and showed the same requirements for acetate as the freshly isolated strains.     

Features of rumen and sewage sludge strains of Eubacterium limosum, a methanol- and H2-CO2-utilizing species.

Eubacterium limosum was isolated as the most numerous methanol-utilizing bacterium in the rumen fluid of sheep fed a diet in which molasses was a major component (mean most probable number of 6.3 X 10(8) viable cells per ml). It was also isolated from sewage sludge at 9.5 X 10(4) cells per ml. It was not detected in the rumen fluid of a steer on a normal hay-grain diet, although Methanosarcina, as expected, was found at 9.5 X 10(5) cells per ml. The doubling time of E. limosum in basal medium (5% rumen fluid) with methanol as the energy source (37 degree C) was 7 h. Acetate, cysteine, carbon dioxide, and the vitamins biotin, calcium-D-pantothenate, and lipoic acid were required for growth on a chemically defined methanol medium. Acetate, butyrate, and caproate were produced from methanol. Ammonia or each of several amino acids served as the main nitrogen source. Other energy sources included adonitol, arabitol, erythritol, fructose, glucose, isoleucine, lactate, mannitol, ribose, valine, and H2-CO2. The doubling time for growth on H2-CO2 (5% rumen fluid, 37 degree C) was 14 h as compared with 5.2 h for isoleucine and 3.5 h for glucose. The vitamin requirements for growth on H2-CO2 were the same as those for methanol; however, acetate was not required for growth on H2-CO2, although it was necessary for growth on valine, isoleucine, and lactate and was stimulatory to growth on glucose. Acetate and butyrate were formed during growth on H2-CO2, whereas branched-chain fatty acids and ammonia were fermentation products from the amino acids. Heat tolerance was detected, but spores were not observed. The type strain of E. limosum (ATCC 8486) and strain L34, which was isolated from the rumen of a young calf, grew on methanol, H2-CO2, valine, and isoleucine and showed the same requirements for acetate as the freshly isolated strains.     

Construction and characterization of pta gene-deleted mutant of Clostridium tyrobutyricum for enhanced butyric acid fermentation

Clostridium tyrobutyricum ATCC 25755 is an acidogenic bacterium, producing butyrate and acetate as its main fermentation products. In order to decrease acetate and increase butyrate production, integrational mutagenesis was used to disrupt the gene associated with the acetate formation pathway in C. tyrobutyricum. A nonreplicative integrational plasmid containing the phosphotransacetylase gene (pta) fragment cloned from C. tyrobutyricum by using degenerate primers and an erythromycin resistance cassette were constructed and introduced into C. tyrobutyricum by electroporation. Integration of the plasmid into the homologous region on the chromosome inactivated the target pta gene and produced the pta-deleted mutant (PTA-Em), which was confirmed by Southern hybridization. SDS-PAGE and two-dimensional protein electrophoresis results indicated that protein expression was changed in the mutant. Enzyme activity assays using the cell lysate showed that the activities of PTA and acetate kinase (AK) in the mutant were reduced by more than 60% for PTA and 80% for AK. The mutant grew more slowly in batch fermentation with glucose as the substrate but produced 15% more butyrate and 14% less acetate as compared to the wild-type strain. Its butyrate productivity was approximately 2-fold higher than the wild-type strain. Moreover, the mutant showed much higher tolerance to butyrate inhibition, and the final butyrate concentration was improved by 68%. However, inactivation of pta gene did not completely eliminate acetate production in the fermentation, suggesting the existence of other enzymes (or pathways) also leading to acetate formation. This is the first-reported genetic engineering study demonstrating the feasibility of using a gene-inactivation technique to manipulate the acetic acid formation pathway in C. tyrobutyricum in order to improve butyric acid production from glucose.     

Kinetics of product formation in batch and continuous culture of Clostridium barkeri

Summary The main fermentation end products in batch culture (unlimited glucose supply) of Clostridium barkeri were butyrate and lactate. The specific rate of butyrate production was linearly proportional to the growth rate while the specific rate of lactate production increased at low growth rates. In a glucose limited chemostat culture butyrate production was partly growth associated while acetate and lactate production was growth associated. Lactate was, however, only produced at high dilution rates. By varying the glucose concentration in the inflowing medium it was shown that lactate production was stimulated by a high feeding rate of the carbon source. These results are discussed in view of the fructose-1,6-diphosphate dependent lactate dehydrogenase activity in many other organisms.     

Quantitative analysis of growth and volatile fatty acid production by the anaerobic ruminal bacterium Megasphaera elsdenii T81

Megasphaera elsdenii T81 grew on either dl-lactate or d-glucose at similar rates (0.85 h^?1) but displayed major differences in the fermentation of these substrates. Lactate was fermented at up to 210-mM concentration to yield acetic, propionic, butyric, and valeric acids. The bacterium was able to grow at much higher concentrations of d-glucose (500 mM), but never removed more than 80 mM of glucose from the medium, and nearly 60 % the glucose removed was sequestered as intracellular glycogen, with low yields of even-carbon acids (acetate, butyrate, caproate). In the presence of both substrates, glucose was not used until lactate was nearly exhausted, even by cells pregrown on glucose. Glucose-grown cultures maintained only low extracellular concentrations of acetate, and addition of exogenous acetate increased yields of butyrate, but not caproate. By contrast, exogenous acetate had little effect on lactate fermentation. At pH 6.6, growth rate was halved by exogenous addition of 60 mM propionate, 69 mM butyrate, 44 mM valerate, or 33 mM caproate; at pH 5.9, these values were reduced to 49, 49, 18, and 22 mM, respectively. The results are consistent with this species’ role as an effective ruminal lactate consumer and suggest that this organism may be useful for industrial production of volatile fatty acids from lactate if product tolerance could be improved. The poor fermentation of glucose and sensitivity to caproate suggests that this strain is not practical for industrial caproate production.     

Influence of Metronidazole, CO, CO(2), and Methanogens on the Fermentative Metabolism of the Anaerobic Fungus Neocallimastix sp. Strain L2

The effects of metronidazole, CO, methanogens, and CO(2) on the fermentation of glucose by the anaerobic fungus Neocallimastix sp. strain L2 were investigated. Both metronidazole and CO caused a shift in the fermentation products from predominantly H(2), acetate, and formate to lactate as the major product and caused a lower glucose consumption rate and cell protein yield. An increased lactate dehydrogenase activity and a decreased hydrogenase activity were observed in cells grown under both culture conditions. In metronidazole-grown cells, the amount of hydrogenase protein was decreased compared with the amount in cells grown in the absence of metronidazole. When Neocallimastix sp. strain L2 was cocultured with the methanogenic bacterium Methanobrevibacter smithii, the fermentation pattern changed in the opposite direction: H(2) and acetate production increased at the expense of the electron sink products lactate, succinate, and ethanol. A concomitant decrease in the enzyme activities leading to these electron sink products was observed, as well as an increase in the glucose consumption rate and cell protein yield, compared with those of pure cultures of the fungus. Low levels of CO(2) in the gas phase resulted in increased H(2) and lactate formation and decreased production of formate, acetate, succinate, and ethanol, a decreased glucose consumption rate and cell protein yield, and a decrease in most of the hydrogenosomal enzyme activities. None of the tested culture conditions resulted in changed quantities of hydrogenosomal proteins. The results indicate that manipulation of the pattern of fermentation in Neocallimastix sp. strain L2 results in changes in enzyme activities but not in the proliferation or disappearance of hydrogenosomes.     

Effect of carbon sources differing in oxidation state and transport route on succinate production in metabolically engineered Escherichia coli

In mixed-acid fermentation, succinate synthesis requires one mole of phosphoenolpyruvate (PEP), one mole of CO₂, and two moles of NADH for every mole of succinate to be formed. Different carbon sources with different properties were used to address these requirements. Sorbitol generates one more mole of NADH than glucose. Fermentation of sorbitol was shown in this study (and by others) to produce significantly more succinate than fermentation of glucose, due to increased NADH availability. Xylose fermentation conserves the intracellular PEP pool, since its transport does not require the phosphotransferase system normally used for glucose transport. The extra PEP can then be assimilated in the succinate pathway to improve production. In this study, fermentation of xylose did yield higher succinate production than glucose fermentation. Subsequent inactivation of the acetate and lactate pathways was performed to study metabolite redistribution and the effect on succinate production. With the acetate pathway inactivated, significant carbon flux shifted toward lactate rather than succinate. When both acetate and lactate pathways were inactivated, succinate yield ultimately increased with a concomitant increase in ethanol yield.     

Environmental and physiological factors affecting the succinate product ratio during carbohydrate fermentation by Actinobacillus sp. 130Z

Actinobacillus sp. 130Z fermented glucose to the major products succinate, acetate, and formate. Ethanol was formed as a minor fermentation product. Under CO₂-limiting conditions, less succinate and more ethanol were formed. The fermentation product ratio remained constant at pH values from 6.0 to 7.4. More succinate was produced when hydrogen was present in the gas phase. Actinobacillus sp. 130Z grew at the expense of fumarate and l-malate reduction, with hydrogen as an electron donor. Other substrates such as more-reduced carbohydrates (e.g., d-sorbitol) resulted in higher succinate and/or ethanol production. Actinobacillus sp. 130Z contained the key enzymes involved in the Embden-Meyerhof-Parnas and the pentose-phosphate pathways and contained high levels of phosphoenolpyruvate (PEP) carboxykinase, malate dehydrogenase, fumarase, fumarate reductase, pyruvate kinase, pyruvate formate-lyase, phosphotransacetylase, acetate kinase, malic enzyme, and oxaloacetate decarboxylase. The levels of PEP carboxykinase, malate dehydrogenase, and fumarase were significantly higher in Actinobacillus sp. 130Z than in Escherichia coli K-12 and accounted for the differences in succinate production. Key enzymes in end product formation in Actinobacillus sp. 130Z were regulated by the energy substrates. Received: 2 September 1996 / Accepted: 10 January 1997     

Lactate Metabolism by Veillonella parvula

A strain of Veillonella parvula M4, which grows readily in lactate broth without a requirement for carbon dioxide, has been isolated from the oral cavity. Anaerobic, washed cells of this organism fermented sodium lactate to the following products (moles/100 moles of lactate): propionate, 66; acetate, 40; carbon dioxide, 40; and hydrogen, 14. Cells grew readily in tryptone-yeast extract broth with pyruvate, oxaloacetate, malate, and fumarate, but poorly with succinate. The fermentation of pyruvate, oxaloacetate, or lactate plus oxaloacetate by washed cells resulted in the formation of propionate and acetate in ratios significantly lower than those observed with lactate as the sole carbon source. This was primarily due to increased acetate production. Cell-free extracts were unable to degrade lactate but metabolized lactate in the presence of oxaloacetate, indicating the presence of malic-lactic transhydrogenase in this organism. Lactic dehydrogenase activity was not observed. Evidence is presented for oxaloacetate decarboxylase and malic dehydrogenase activities in extracts.     

Clostridium thermobutyricum: growth studies and stimulation of butyrate formation by acetate supplementation

Clostridium thermobutyricum produces butyrate as the main fermentation product from glucose, and from yeast extract, which is required for substantial growth. After sequential transfer in the presence of increasing butyrate concentrations, strain JW 171 K grew in the presence of up to 350 mM butyrate either at pH 5.5 or at pH 8.0 and at 40 degrees C as well as at 60 degrees C. This result indicated that butyrate-dependent growth inhibition was independent from the concentration of undissociated butyric acid. Increased butyrate concentration decreased the level of tolerated glucose from above 15% to below 10%. At 0.05 and 2.0% (wt/vol) yeast extract, the Y(Glucose) was 30 and 55 g dry weight cells per mole glucose, respectively. Y(ATP) values between 18 and 21 g weight cells per mole ATP, obtained after growth in the presence of 2% yeast extract, indicate that the butyrate fermentation under thermophilic growth conditions is as energy efficient as it is under mesophilic conditions. Externally added acetate stimulated the production of butyrate. Supplemented 14C-acetate was converted to butyrate, resulting in the formation of 44% labeled butyrate (i.e. formed from 14C-acetate) and 56% unlabeled butyrate (formed from glucose and yeast extract). Continuous removal of H2 in batch cultures led to a shift in the fermentation products from more butyrate to the more oxidized and more energy yielding acetate.     

Nutrition of Acetobacter rancens S3 and F11 Isolated from Tanks for Vinegar Production

The strains S3 and F11 which were isolated respectively from static and submerged tanks for vinegar production were identified as Acetobacter rancens. Neither strain grew in an ammonium defined medium containing ethanol, glucose, glycerol or organic acids as the sole carbon source. When casamino acids were added, they grew luxuriantly with lactate, ethanol or glycerol as the carbon source and less well with acetate or glucose. They grew, forming much acetic acid, in defined ethanol medium when alanine was supplied in place of casamino acids, but strain S3 showed a longer lag time than strain Fl1. This lag time could be shortened by addition of aspartate and glutamate. These amino acids could be replaced by succinate, fumarate, malate, lactate, pyruvate or propionate but not by glucose. Both strains required lactate or pyruvate in defined glucose medium but many other organic acids, which were effective in defined ethanol medium, were ineffective or slightly effective in glucose medium.     

产丁二酸工程菌的构建及其厌氧发酵

为了考察过量表达苹果酸酶对于E.coli NZN111(ldhA::Kan pfl::Cam)厌氧发酵产丁二酸的影响, 将连接有苹果酸酶基因sfcA的表达载体pTrc99a-sfcA转化进NZN111中, 构建了重组NZN111(pTrc99a-sfcA)。0.5 mmol/L IPTG诱导8 h后, 测定的苹果酸酶比酶活为30.67 u/mg, 比受体菌提高了140倍。采用两阶段发酵模式, 结果表明: 过量表达的苹果酸酶在NZN111体内催化了从丙酮酸到苹果酸的逆向反应, 丁二酸是发酵过程中积累的主要有机酸, 且当加入0.7 mmol/L IPTG诱导, 初始葡萄糖糖浓度为18.5 g/L时, 选择对数生长期后期的菌种以10%的接种量转入厌氧发酵, 发酵结束时发酵液中丁二酸的浓度为12.84 g/L, 对葡萄糖的收率为69.43%, 乙酸为0.58 g/L, 二者浓度比为22:1, 没有检测到甲酸和乳酸。构建的菌种具有高产丁二酸和副产物极少的优点, 在同类菌种中处于先进水平。     

RNA synthesis during morphogenesis of the fungusMucor racemosus

Bacteroides succinogenes produces acetate and succinate as major products of carbohydrate fermentation. An investigation of the enzymes involved indicated that pyruvate is oxidized by a flavin-dependent pyruvate cleavage enzyme to acetyl-CoA and CO₂. Active CO₂ exchange is associated with the pyruvate oxidation system. Reduction of flavin nucleotides is CoASH-dependent and does not require ferredoxin. Acetyl-CoA is further metabolized via acetyl phosphate to acetate and ATP. Reduced flavin nucleotide is used to reduce fumarate to succinate by a particulate flavin-specific fumarate reductase reaction which may involve cytochrome b. Phosphoenolpyruvate (PEP) is carboxylated to oxalacetate by a GDP-specific PEP carboxykinase. Oxalacetate, in turn, is converted to malate by a pyridine nucleotide-dependent malate dehydrogenase. The organism has a NAD-dependent glyceraldehyde-3-phosphate dehydrogenase. The data suggest that reduced pyridine nucleotides generated during glycolysis are oxidized in malate formation and that the electrons generated during pyruvate oxidation are used to reduce fumarate to succinate.     

Eliminating side products and increasing succinate yields in engineered strains of Escherichia coli C

Derivatives of Escherichia coli C were previously described for succinate production by combining the deletion of genes that disrupt fermentation pathways for alternative products (ldhA::FRT, adhE::FRT, ackA::FRT, focA-pflB::FRT, mgsA, poxB) with growth-based selection for increased ATP production. The resulting strain, KJ073, produced 1.2 mol of succinate per mol glucose in mineral salts medium with acetate, malate, and pyruvate as significant co-products. KJ073 has been further improved by removing residual recombinase sites (FRT sites) from the chromosomal regions of gene deletion to create a strain devoid of foreign DNA, strain KJ091(DeltaldhA DeltaadhE DeltaackA DeltafocA-pflB DeltamgsA DeltapoxB). KJ091 was further engineered for improvements in succinate production. Deletion of the threonine decarboxylase (tdcD; acetate kinase homologue) and 2-ketobutyrate formate-lyase (tdcE; pyruvate formate-lyase homologue) reduced the acetate level by 50% and increased succinate yield (1.3 mol mol(-1) glucose) by almost 10% as compared to KJ091 and KJ073. Deletion of two genes involved in oxaloacetate metabolism, aspartate aminotransferase (aspC) and the NAD(+)-linked malic enzyme (sfcA) (KJ122) significantly increased succinate yield (1.5 mol mol(-1) glucose), succinate titer (700 mM), and average volumetric productivity (0.9 g L(-1) h(-1)). Residual pyruvate and acetate were substantially reduced by further deletion of pta encoding phosphotransacetylase to produce KJ134 (DeltaldhA DeltaadhE DeltafocA-pflB DeltamgsA DeltapoxB DeltatdcDE DeltacitF DeltaaspC DeltasfcA Deltapta-ackA). Strains KJ122 and KJ134 produced near theoretical yields of succinate during simple, anaerobic, batch fermentations using mineral salts medium. Both may be useful as biocatalysts for the commercial production of succinate.     

Energy conservation by succinate decarboxylation in Veillonella parvula.

Veillonella parvula cannot grow with succinate as sole energy source. However, succinate decarboxylation simultaneous with malate or lactate fermentation increased growth yields by 2.4-3.5 g (mol succinate)-1. Malate was fermented stoichiometrically to acetate and propionate whereas lactate fermentation produced more acetate and considerable amounts of H2. Aspartate was utilized only in the presence of succinate as co-substrate. Methylmalonyl-CoA decarboxylase and ATP-dependent pyruvate carboxylase, but not methylmalonyl-CoA:pyruvate transcarboxylase, were detected in cell-free extracts of malate- or lactate-grown cells. The energetic aspects of these fermentation patterns are discussed.     

Glucose toxicity and inability of Bacteroides ruminicola to regulate glucose transport and utilization.

Ammonia-limited (3.5 mM ammonia) cultures of Bacteroides ruminicola B(1)4 had a high number of viable cells (greater than 10(9)/ml), but only when the concentration of glucose was not too high (10 mM or less). When the glucose concentration was increased from 10 to 50 mM, there was a marked decrease in viability (10(5)-fold or greater). Because there was little decline in pH and only a small increase in succinate and acetate as the glucose concentration was increased, it did not appear that end products were killing the cells. This conclusion was supported by the observation that reinoculated cultures grew in the spent medium which had been supplemented with ammonia. Unlabeled rhamnose did not inhibit [14C]-glucose uptake, and cultures which were selected with a low concentration of rhamnose tolerated high concentrations of glucose (50 mM). The glucose-resistant mutant transported glucose at a lower rate than the wild type, and the Vmax of glucose transport was fourfold lower. The wild type stored much more polysaccharide than the glucose-resistant mutant, but it is not clear if polysaccharide accumulation per se is responsible for the glucose toxicity. These results indicated that B. ruminicola B(1)4 is unable to regulate glucose transport and utilization when growth is limited by ammonia.