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Applied and Environmental Microbiology, September 2002, p. 4274-4282, Vol. 68, No. 9
0099-2240/02/$04.00+0 DOI: 10.1128/AEM.68.9.4274-4282.2002
Copyright © 2002, American Society for Microbiology. All Rights Reserved.
Section of Molecular Microbiology, BioCentrum-DTU, Technical University of Denmark, DK-2800 Kgs. Lyngby,1 Department of Genomics and Strain Development,2 CH Bio Ingredients, Chr. Hansen A/S, DK-2970 Hørsholm, Denmark3
Received 28 March 2002/ Accepted 24 June 2002
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In spite of the importance of glycolysis for fermentation purposes, it is still not known what controls the glycolytic flux in microbial bioreactors. It has been suggested that the enzyme glyceraldehyde-3-phosphate dehydrogenase (GAPDH) has a high level of control (estimated to be 90% of the control) over the glycolytic flux in nonproliferating cells of Lactococcus lactis (33). However, it has recently been shown that GAPDH has no control over the glycolytic flux in steadily growing L. lactis cells (Solem, Koebmann, and Jensen, unpublished data). The control over the glycolytic flux exerted by lactate dehydrogenase was also reported to be close to zero (2).
According to metabolic control theory (16, 25), flux control can reside in any of the steps in a system; i.e., it can reside in the numerous processes that consume the ATP generated in glycolysis (8, 17). Indeed, we have recently shown that at least 75% of the control over glycolysis in aerobic Escherichia coli cultures occurs in the ATP-consuming reactions (26). This result was obtained by overexpression of genes encoding part of the F1 unit of the (F1F0) H+-ATPase, which resulted in uncoupling of glycolysis from biomass production and a 70% increase in the glycolytic flux.
In this paper we show that expression of genes encoding F1-ATPase can also induce uncoupling of glycolysis from biomass production in L. lactis. Interestingly, the glycolytic flux was not increased in cells steadily growing on glucose, and we concluded that control of the glycolytic flux under these conditions resides in glycolysis itself or perhaps in sugar transport.
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TABLE 1. Bacterial strains and plasmids
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Antibiotics were used at the following concentrations: ampicillin, 100 µg/ml (for selection of a pMOSBlue derivative in E. coli); and erythromycin, 5 µg/ml (for selection of pAK80 derivatives in L. lactis) and 200 µg/ml (for selection of pAK80 derivatives in E. coli).
Growth experiments with L. lactis were carried out at 30°C by using batch cultures in flasks containing 100 ml of SA medium (21) supplemented with 1.0 g of glucose per liter and 5 µg of erythromycin per ml. The strains were inoculated by using growing overnight cultures at low densities 6 to 10 h before optical densities were first measured in order to obtain exponentially growing cells. A strain containing promoter cloning vector pAK80 was used as a reference. Slowly rotating magnets were used to keep the cultures homogeneous. Regular measurements of optical density at 450 nm (OD450) were obtained, and samples were withdrawn and used for determination of ATP and ADP concentrations and for high-performance liquid chromatography (HPLC) to measure glucose and by-product contents. The cell density was correlated with the cell mass of L. lactis as follows: 0.19 g (dry weight)/liter of SA medium was equivalent to an OD450 of 1 (31). The biomass yield was determined from the cell density divided by the glucose concentration by using a molar weight of glucose of 198 g/mol. The glycolytic flux was routinely calculated from the specific growth rate and the biomass yield (specific growth rate/biomass yield), assuming steady-state conditions, and was validated by HPLC measurements. The fluxes measured by HPLC matched the fluxes deduced from specific growth rate/biomass yield with an error of less than 3%.
Growth of resuspended cells.
L. lactis was grown in 100 ml of SA medium supplemented with 2 g of glucose per liter to an OD450 of 0.9. The cultures were put on ice. After cooling, the cells were centrifuged (7,000 x g for 10 min) and washed once with SA medium supplemented with 2 g of glucose per liter but without amino acids or vitamins. The cells were resuspended in the latter medium to an OD450 of 0.9. Samples were withdrawn for measuring the ATP and ADP concentrations, and samples were also used for HPLC to measure glucose and product concentrations at 10, 30, 70, 150, and 310 min after resuspension.
DNA techniques and DNA isolation.
Extraction of chromosomal DNA from L. lactis was carried out as previously described (24), with the following modifications: a final concentration of 15.5 mg of lysozyme per ml for 30 min was used for lysis, and the sample was incubated with sodium dodecyl sulfate for 10 min at 37°C and then for 10 min at 65°C. PCR amplification with Pfu DNA polymerase (Stratagene, La Jolla, Calif.) was performed as recommended by the manufacturer. Plasmid DNA from E. coli for analytic purposes was isolated by using an alkaline lysis method, and plasmid DNA from E. coli for preparative purposes was isolated by using Qiagen columns (Qiagen, Hilden, Germany). Plasmid DNA from L. lactis was isolated as described by Birnboim and Doly (5), with the following modification: a final concentration of 15.5 mg of lysozyme per ml for 20 min at 37°C was used for lysis of the cell wall. Digestion with restriction enzymes (Gibco BRL, Pharmacia, New England Biolabs) and treatment with T4 DNA ligase (Gibco BRL) and calf intestine alkaline phosphatase (Pharmacia) were carried out by using standard recombinant DNA techniques as described by Sambrook et al. (36) and as recommended by the manufacturers. DNA fragments were purified from agarose gels by using GFX columns (Pharmacia) or a High Pure PCR product purification kit (Boehringer Mannheim). Linearized cloning vectors were treated with calf intestine alkaline phosphatase to avoid religation of the vector.
Transformation.
E. coli strains were made competent by using a CaCl2 treatment (36). After transformation, the cells were regenerated in LB medium (36) and subsequently transferred to LB agar plates supplemented with the appropriate antibiotic. Cells of L. lactis were made competent by growing them in M17 medium supplemented with 5 g of glucose per liter and 10 g of glycine per liter and resuspending them in a solution containing 100 g of glycerol per liter and 0.5 M sucrose as described by Holo and Nes (18). Plasmid DNA was used to transform the cells by electroporation (18), and the cells were allowed to regenerate in Schmidt-Ruppin medium (30) for 2 h and then plated on Schmidt-Ruppin agar plates supplemented with the appropriate antibiotics. Histochemical screening for lacLM was carried out with 5-bromo-4-chloro-3-indolyl-ß-D-galactoside (X-Gal) (Sigma) at a final concentration of 100 µg/ml.
PCR amplification and cloning of atpAGD from L. lactis MG1363.
A 4.0-kb DNA fragment encoding atpAGD (positions 3205 to 7240) from the atp operon of L. lactis MG1363 (sequence positions 3205 to 7240 of the atp operon deposited in the National Center for Biotechnology Information data bank under accession no. AF059739) was amplified by PCR with primer 5704F (5'-CGGGATCCAGCTAAATAGCCTTGAACTAG-3') and primer 6243R (5'-CTGGATCCTTTCATAAGAAATCGAATTAATAACCC-3') purchased from Hobolth DNA Synthese, Hillerød, Denmark (Fig. 1A). The resulting PCR product was digested with SpeI, positioned immediately upstream of the ribosome binding site of atpA, and cloned in plasmid cloning vector pMOSBlue (Pharmacia) digested with SpeI and HincII (2.7 kb), resulting in pMOS::atpAGD.
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FIG. 1. Cloning of PCR fragment of atpAGD from L. lactis MG1363. (A) PCR amplification of the atpAGD genes from L. lactis MG1363. A 4.0-kb PCR fragment encoding the , , and ß subunits was amplified with primers 5704F and 6243R (sequence positions 3205 to 7240 of the atp operon deposited in the National Center for Biotechnology Information data bank under accession no. AF059739) and cloned in pMOSBlue. (B) Plasmids used for introduction of F1-ATPase in L. lactis. A 4.1-kb fragment encoding atpAGD was cloned downstream of constitutive promoters in a transcriptional fusion with the reporter gene lacLM coding for ß-galactosidase. The open reading frames are indicated by boxes, and the designations of the genes and their products are shown above the boxes. The arrows indicate the promoters and show the direction of transcription. The plasmid designation is shown to the left of the linear plasmid. The plasmid is not drawn to scale. In this study a library of new synthetic constitutive promoters was employed. CPC, individual constitutive promoters (23); ori, origin of replication; erm, erythromycin resistance; lacLM, ß-galactosidase.
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Measurement of ß-galactosidase activity.
Sampling was carried out by pipetting 1-ml portions of culture into ice-cooled Eppendorf tubes containing 12.5 µl of 0.1% sodium dodecyl sulfate and 25 µl of chloroform to permeabilize the cells. After vortexing for 10 s, the samples were placed on ice until the enzyme activities were measured. The extracts were diluted with suitable volumes of Z-buffer (0.06 M Na2HPO4, 0.04 M NaH2PO4, 0.01 M KCl, 0.001 M MgSO4; pH 7.0) to obtain a total volume of 1 ml in each case. Each diluted sample was preheated at 30°C for 5 min, and the enzyme activity was determined by a standard procedure described by Miller (28) and modified by Israelsen and coworkers (20). ß-Galactosidase activities greater than 400 Miller units were subject to larger errors due to instability resulting from high levels of expression of the genes encoding F1-ATPase.
Measurement of the intracellular ATP and ADP concentrations.
Samples (0.5 ml) were quenched in 0.5 ml of 80°C buffer-saturated phenol (equilibrated with 10 mM Tris-1 mM EDTA, pH 8.0) containing 0.6 g of glass beads (diameter, 106 µm; Sigma) as previously described (26). Treatment and measurement of the intracellular concentrations of ATP and ADP were carried out as previously described (26). Determinations of ratios of ATP to ADP greater than 15 were more uncertain due to relatively low levels of ADP.
Measurement of G6P and FBP concentrations.
Extracts were prepared from batch cultures at OD450 of 0.6 to 1.8 by quenching in 80°C buffer-saturated phenol (equilibrated with 10 mM Tris-1 mM EDTA, pH 8.0) supplemented with 0.6 g of glass beads (diameter, 106 µm; Sigma) as previously described for measurement of ATP and ADP concentrations (26). After chloroform treatment, the concentrations of glucose 6-phosphate (G6P) and fructose 1,6-bisphosphate (FBP) were measured by recording the increase in NADH fluorescence as described previously (1, 44), with the following modification: the buffer contained 50 mM triethanolamine (pH 7.5) instead of imidazole hydrochloride. Glucose-6-phosphate dehydrogenase, aldolase, and glycerol-3-phosphate dehydrogenase were obtained from Boehringer GmbH, Mannheim, Germany. Intracellular concentrations of sugar phosphates (42) were calculated by assuming that 1 g (dry weight) corresponded to 1.67 ml of intracellular volume.
Quantification of glucose and end products by HPLC.
Glucose and product concentrations were determined by HPLC as previously described (1). The carbon balance was calculated by determining the recovery of substrates converted into products in terms of C-moles.
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,
, and ß has been found to be most active with respect to ATP hydrolysis in vitro (10), and in vivo experiments with E. coli have confirmed this observation (26). To study the effect of a gradual increase in uncoupled ATPase activity in L. lactis, the atpA, atpG, and atpD genes encoding the
,
, and ß subunits, respectively, were cloned into a library of synthetic constitutive promoters having different strengths (23). Clones were obtained in which the atpAGD genes were inserted into an operon structure together with the lacLM genes encoding a ß-galactosidase (Fig. 1B). The specific ß-galactosidase activities in these cells should therefore reflect the expression of the F1-encoding genes. We found a good correlation between the measured ß-galactosidase activities and the biomass yields; greater expression of the lacLM reporter gene resulted in a gradually decreasing growth yield. This indicates that there was increased uncoupling of glycolysis from biomass production as a result of increased ATPase activity (Fig. 2). At the highest ß-galactosidase activities the biomass yield was reduced to one-half of the wild-type biomass yield.
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FIG. 2. Correlation between specific ß-galactosidase activities and biomass yield for the F1-ATPase library. The specific ß-galactosidase activities and biomass yields were measured for overnight cultures of L. lactis strains grown in SA medium supplemented with 1.5 g of glucose per liter and 5 µg of erythromycin per ml. (A) Primary data for L. lactis strains containing ATPase plasmids from the pCPCx::atpAGD plasmid library. The bars and lines indicate the specific ß-galactosidase activities and biomass yields, respectively. (B) Correlation between specific ß-galactosidase activity and biomass yield. The symbols represent clones with a range of expression of genes coding for F1-ATPase.
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FIG. 3. Effect of uncoupled F1-ATPase on the intracellular energy level: correlation of specific ß-galactosidase activity with the ATP, ADP, and ATP plus ADP pools and the [ATP]/[ADP] ratio. The experimental data for the ATP, ADP, and ATP plus ADP pools are fitted to linear curves indicated by dotted lines, and the [ATP]/[ADP] ratio is fitted to a curve indicated by a solid line. The error bars indicate the standard deviations of the measurements.
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TABLE 2. Growth and sugar consumption of derivatives of strain L. lactis MG1363 with uncoupled F1-ATPase activity ( , , and ß subunits)
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FIG. 4. Growth curves of derivatives of L. lactis MG1363 with uncoupled F1-ATPase. Cell density (OD450) is plotted as a function of time for the cultures. The cultures were grown in batches without aeration at 30°C in SA medium (21) supplemented with 1 g of glucose per liter and 5 µg of erythromycin per ml. The strains and their doubling times (td) (in minutes) are indicated on the right. The growth curves are offset for clarity. The standard deviations of the calculated doubling times were <3%.
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FIG. 5. Steady-state consumption of glucose in L. lactis strains with uncoupled F1-ATPase during batch fermentation. The consumption of glucose in a time course experiment as measured by HPLC is plotted as a function of cell density (OD450). The plasmids of the individual strains are indicated at the bottom. pAK80 is a vector without atp genes. The samples were taken from an independent experiment.
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FIG. 6. Lactate and formate production by strains with incorporated F1-ATPase in the batch experiment described in the legend to Fig. 4. Samples for HPLC measurements were taken when the cultures entered the stationary phase. The level of recovery of C-moles ranged between 85 and 95%.
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TABLE 3. Pools of G6P and FBPa
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FIG. 7. Effect of uncoupled F1-ATPase in nongrowing cells. The glycolytic fluxes in nongrowing cells are plotted as a function of the ß-galactosidase activities of strains measured with steadily growing cells. The glycolytic fluxes were estimated from measurements of glucose consumption by HPLC. The strains used were MG1363, BK1511, BK1503, BK1525, BK1517, and BK1536, which exhibit gradually increased expression of genes coding for F1-ATPase. The glycolytic flux in steadily growing L. lactis MG1363 in the experiment is indicated by a solid line.
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TABLE 4. Intracellular [ATP]/[ADP] ratios in resuspended cells
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Gp is the cellular energy state and e1 and e2 represent the anabolic and catabolic modules, respectively. The flux control of this simple metabolic scheme can be expressed in terms of the elasticities (the metabolic control analysis term for sensitivities) (J. A. Burns, A. Cornish-Bowden, A. K. Groen, R. Heinrich, H. Kacser, J. W. Porteous, S. M. Rapoport, T. A. Rapoport, J. W. Stucki, J. M. Tager, R. J. A. Wanders, and H. V. Westerhoff, Letter, Trends Biochem. Sci. 10:16, 1985) of the two blocks:
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) can be calculated if we know how elastic the catabolic reactions (
) and the anabolic reactions (
) are towards changes in the cellular energy state. A high elasticity coefficient means that a block is very sensitive, while a value close to zero means that a block is completely insensitive. The absence of control of the glycolytic flux by ATP-consuming reactions can then be explained either by a low elasticity of catabolism (
) towards the cellular energy state or by a relatively higher elasticity of anabolism (
) towards the cellular energy state. The relationship among the growth rate, the glycolytic flux, and the cellular energy state ([ATP]/[ADP]) is plotted in Fig. 8. The glycolytic flux does not change much over a twofold change in the [ATP]/[ADP] ratio, while the growth rate changes even when a small change in the [ATP]/[ADP] ratio is induced. Figure 8B shows a log-log plot of the glycolytic flux and the growth rate as a function of the intracellular [ATP]/[ADP] ratio in strains with modulated expression of genes encoding F1-ATPase. Different curves (logarithmic, linear, exponential, power) were fitted to the data points with low to moderate changes in the [ATP]/[ADP] ratio. We then determined the elasticities of the catabolic and anabolic blocks towards the [ATP]/[ADP] ratio (Fig. 8C), which are simply the slopes of the two curves in Fig. 8B. The elasticity of the catabolic block was estimated to be close to zero (-0.02), which confirms that glycolysis is very insensitive to changes in the energy level. The elasticity of the anabolic block (growth rate) ranged between 0.22 and 0.26 in the absence of ATPase, depending on the applied curve fit, and increased at the highest level of ATPase.
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FIG. 8. Dependence of glycolytic flux and growth rate on the [ATP]/[ADP] ratio and calculation of elasticity and flux control coefficients. Cultures of L. lactis MG1363 derivatives were grown as described in the legend to Fig. 4. (A) Relative glycolytic fluxes and growth rates plotted as a function of the [ATP]/[ADP] ratio for derivatives of L. lactis MG1363 in which genes encoding F1-ATPase are expressed from synthetic promoters with different strengths. (B) Logarithmic (scaled) relative glycolytic fluxes (Jg) and growth rates (µ) plotted as functions of logarithmic [ATP]/[ADP] ratios for derivatives of L. lactis MG1363 in which the atpAGD genes are expressed at five different strengths. The experimental data points indicated by shaded symbols are fitted to curves shown by solid lines. The equations are indicated above and below the plots. (C) Elasticities of the glycolytic flux (glyc. flux) and the growth rate towards the intracellular [ATP]/[ADP] ratio. The elasticities are the slopes of the scaled fluxes towards the [ATP]/[ADP] ratios shown in panel B, calculated from the fitted equations. (D) Flux control by the demand for ATP on the glycolytic flux as a function of the [ATP]/[ADP] ratio, calculated by using the equation in the text.
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0.09). According to metabolic control analysis, the flux control values should add up to 1, which means that the catabolic module (i.e., glycolysis itself and/or the sugar uptake system) might have a flux control value close to 1. |
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,
, and ß subunits reconstituted from isolated individual subunits of E. coli (9, 10, 11), Bacillus strain PS3 (46), and Salmonella enterica serovar Typhimurium (19) were found to have high ATPase activities. The reduction in the intracellular energy level with an increased level of uncoupled F1-ATPase did not result in a shift of metabolism from homolactic fermentation to a mixed-acid pattern that would otherwise have provided the cell with extra ATP (14, 43). This is in agreement with the results of previous chemostat experiments, which showed that cells remained homolactic at a dilution rate of 0.5 h-1 (27, 43).
Glycolytic flux in growing L. lactis is close to the maximal capacity.
The glycolytic flux was virtually unaffected by the expression of genes encoding F1-ATPase in growing cells. This means that the flux control by the ATP-demanding processes was close to zero, indicating that glycolysis in L. lactis is close to the maximal capacity under these conditions. The lack of control by demand for ATP on the glycolytic flux is in sharp contrast to previous results obtained with E. coli, in which the glycolytic flux was observed to increase gradually in response to increased expression of genes encoding F1-ATPase (26). The difference may reflect differences in energy generation. The homofermentative metabolism of L. lactis yields only 2 mol of ATP per mol of glucose, whereas aerobic organisms that possess oxidative phosphorylation can obtain 8 to 10 mol of ATP per mol of hexose (22). L. lactis therefore requires a considerably higher flux through glycolysis for energy production (
24 mmol of glucose/h/g [dry weight] at 30°C in defined medium) than E. coli requires (
7 mmol of glucose/h/g [dry weight] at 30°C in minimal medium) (26) in order to obtain sufficient energy for rapid growth.
To test this hypothesis, experiments were performed with nongrowing cells. In nongrowing cells the glycolytic flux of the wild type was approximately threefold lower than that in growing cells, since no ATP was being used for biomass production. The glycolytic flux increased gradually with increased expression of F1 genes until the level found in exponentially grown cultures was approached. Thus, it appears that when there is excess glycolytic capacity, the flux through glycolysis can indeed be increased by increasing the ATP turnover in the cells until the full capacity is being employed. The finding that there was control by ATP demand under conditions under which anabolism was limited is in agreement with a mechanistic model for glycolysis in L. lactis that describes the sugar metabolism in nongrowing cells (29).
A decrease in the intracellular energy state of the cell may affect the kinetics of enzymatic steps involved in metabolism. Such a kinetic effect has, for instance, been demonstrated for PFK by simulations with erythrocytes (34). The reaction catalyzed by PFK is an ATP-requiring step, after which further metabolism yields surplus ATP, also referred to as a turbo design (41). Lowering the [ATP]/[ADP] ratio may therefore ultimately reduce the activity of PFK. The excess capacity of PFK in L. lactis was recently found to be small, and a slight reduction in PFK activity results in an increased pool of upstream metabolites (1). Indeed, in growing cells the level of the upstream metabolite G6P increased twofold in the presence of F1-ATPase compared to the level in the reference strain, while the concentration of FBP was found to be slightly decreased. The increased concentration of G6P and the decreased concentration of FBP observed here fit well with the potential risk of a turbo design, as suggested by Teusink and coworkers (41), resulting in decreased glycolytic flux at low [ATP]/[ADP] ratios.
According to metabolic control theory flux control is usually distributed over several steps. Our results indicate that control resides either in glycolysis itself or perhaps in glucose uptake. Interestingly, the glycolytic enzymes in yeast and also sugar transport in E. coli have been found to exert no significant control over the glycolytic flux (35, 37). It has been suggested that in L. lactis GAPDH has a high level of flux control in nongrowing cells (33). However, it was recently found that GAPDH has no control over the glycolytic flux in growing cells of L. lactis (Solem et al., unpublished). Lactate dehydrogenase had no control over the glycolytic flux either (2). A recent study of sugar catabolism in L. lactis IL-1403 also suggested a catabolic flux limitation (12), and due to concomitant high in vivo glycolytic enzyme capacities it was suggested that the control was probably at the level of sugar transport (12).
Based on the existing data we suggest that simultaneous modulation of several metabolic steps might be necessary to increase the glycolytic flux. Thus, by increasing the glycolytic capacity in L. lactis, the control of glycolysis is likely to shift to ATP demand, which can then be increased by introduction of uncoupled F1-ATPase, as shown previously for E. coli (26) and here for nongrowing L. lactis. This would be in agreement with a recent study of glycolysis in Trypanosoma brucei, in which experiments and computer simulations indicated that control of the glycolytic flux is shared by several steps in the pathway (3).
It may also be important to achieve appropriate levels of each of the individual enzymes involved in order to maintain proper metabolite concentrations (1, 13). At first, the task of simultaneous and accurate modulation of many genes in a cell may seem impracticable. However, the so-called SPL technology developed recently in our laboratory (23, 38) involving synthetic promoter libraries has greatly facilitated such an undertaking.
We thank Regina Shürmann for excellent technical assistance.
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, ß and subunit
tagged with six histidine residues at the C-terminus. FEBS Lett. 427:64-68.[CrossRef][Medline]
-aminoisobutyric acid transport system in Streptococcus lactis. J. Bacteriol. 127:719-730.
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