Glucose 6-Phosphate Accumulation in Mycobacteria: IMPLICATIONS FOR A NOVEL F420-DEPENDENT ANTI-OXIDANT DEFENSE SYSTEM*

Glucose 6-phosphate (G6P) is a metabolic intermediate with many possible cellular fates. In mycobacteria, G6P is a substrate for an enzyme, F₄₂₀-dependent glucose-6-phosphate dehydrogenase (Fgd), found in few bacterial genera. Intracellular G6P levels in six Mycobacterium sp. were remarkably higher (∼17–130-fold) than Escherichia coli and Bacillus megaterium. The high G6P level in Mycobacterium smegmatis may result from 10–25-fold higher activity of the gluconeogenic enzyme fructose-1,6-bisphosphatase when grown on glucose, glycerol, or acetate compared with B. megaterium and E. coli. In M. smegmatis this coincided with up-regulation of the first gluconeogenic enzyme, phosphoenolpyruvate carboxykinase, when acetate was the carbon source, suggesting a cellular program for maintaining high G6P levels. G6P was depleted in cells under oxidative stress induced by redox cycling agents plumbagin and menadione, whereas an fgd mutant of M. smegmatis used G6P less well under such conditions. The fgd mutant was more sensitive to these agents and, in contrast to wild type, was defective in its ability to reduce extracellular plumbagin and menadione. These data suggest that intracellular G6P in mycobacteria serves as a source of reducing power and, with the mycobacteria-specific Fgd-F₄₂₀ system, plays a protective role against oxidative stress.     

Acetate accumulation through alternative metabolic pathways in ackA?pta?poxB? triple mutant in E. coli B (BL21)

Individual deletions of acs and aceA genes in E. coli B (BL21) showed little difference in the metabolite accumulation patterns but deletion of the ackA gene alone or together with pta showed acetic acid gradually accumulated to 3.1 and 1.7 g/l, respectively, with a minimal extended lag in bacterial growth and a higher pyruvate formation. Single poxB deletion in E. coli B (BL21) or additional poxB deletion in the ackA-pta mutants did not change the acetate accumulation pattern. When the acetate production genes (ackA-pta-poxB) were deleted in E. coli B (BL21) acetate still accumulated. This may be an indication that perhaps acetate is not only a by-product of carbon metabolism; it is possible that acetate plays also a role in other cellular metabolite pathways. It is likely that there are alternative acetate production pathways.     

Modeling of the pyruvate production with<Emphasis Type="Italic"> Escherichia coli</Emphasis> in a fed-batch bioreactor

A family of 10 competing, unstructured models has been developed to model cell growth, substrate consumption, and product formation of the pyruvate producing strain Escherichia coli YYC202 ldhA::Kan strain used in fed-batch processes. The strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate (using glucose as the carbon source) resulting in an acetate auxotrophy during growth in glucose minimal medium. Parameter estimation was carried out using data from fed-batch fermentation performed at constant glucose feed rates of q_VG=10 mL h^–1. Acetate was fed according to the previously developed feeding strategy. While the model identification was realized by least-square fit, the model discrimination was based on the model selection criterion (MSC). The validation of model parameters was performed applying data from two different fed-batch experiments with glucose feed rate q_VG=20 and 30 mL h^–1, respectively. Consequently, the most suitable model was identified that reflected the pyruvate and biomass curves adequately by considering a pyruvate inhibited growth (Jerusalimsky approach) and pyruvate inhibited product formation (described by modified Luedeking–Piret/Levenspiel term).List of symbols c_A acetate concentration (g L^–1) - c_A,0 acetate concentration in the feed (g L^–1) - c_G glucose concentration (g L^–1) - c_G,0 glucose concentration in the feed (g L^–1) - c_P pyruvate concentration (g L^–1) - c_P,max critical pyruvate concentration above which reaction cannot proceed (g L^–1) - c_X biomass concentration (g L^–1) - K_I inhibition constant for pyruvate production (g L^–1) - K_I^A inhibition constant for biomass growth on acetate (g L^–1) - K_P saturation constant for pyruvate production (g L^–1) - K_P inhibition constant of Jerusalimsky (g L^–1) - K_S^A Monod growth constant for acetate (g L^–1) - K_S^G Monod growth constant for glucose (g L^–1) - m_A maintenance coefficient for growth on acetate (g g^–1 h^–1) - m_G maintenance coefficient for growth on glucose (g g^–1 h^–1) - n constant of extended Monod kinetics (Levenspiel) (–) - q_V volumetric flow rate (L h^–1) - q_VA volumetric flow rate of acetate (L h^–1) - q_VG volumetric flow rate of glucose (L h^–1) - r_A specific rate of acetate consumption (g g^–1 h^–1) - r_G specific rate of glucose consumption (g g^–1 h^–1) - r_P specific rate of pyruvate production (g g^–1 h^–1) - r_P,max maximum specific rate of pyruvate production (g g^–1 h^–1) - t time (h) - V reaction (broth) volume (L) - Y_P/G yield coefficient pyruvate from glucose (g g^–1) - Y_X/A yield coefficient biomass from acetate (g g^–1) - Y_X/A,max maximum yield coefficient biomass from acetate (g g^–1) - Y_X/G yield coefficient biomass from glucose (g g^–1) - Y_X/G,max maximum yield coefficient biomass from glucose (g g^–1) - growth associated product formation coefficient (g g^–1) - non-growth associated product formation coefficient (g g^–1 h^–1) - specific growth rate (h^–1) - _max maximum specific growth rate (h^–1)     

Diacetyl production and growth of Lactobacillus rhamnosus on multiple substrates

Lactobacillus rhamnosus is a heterolactic acid bacterium, which can be used to produce flavour compounds like diacetyl and acetoin. Various startegies have been applied to improve the growth rate and diacetyl yield. The use of multiple substrates affected growth as well as the yield of diacetyl. Growth on a medium containing glucose demonstrated a diauxic growth profile, with the second phase of growth being on the product, lactic acid. L. rhamnosus also grew on a medium containing citrate. Growth on medium containing glucose+citrate demonstrated simultaneous utilization of carbon sources. L. rhamnosus did not grow in a medium containing acetate and also did not co-metabolize it with glucose. Maximum specific growth rate ( _max) was found to increase in the case of simultaneous utilization of glucose+citrate (0.38 h^–1) as compared to glucose as the sole carbon source (0.28 h^–1). The yields of diacetyl were also found to increase for glucose + pyruvate and glucose + citrate (0.10 and 0.05 g g^–1 of glucose, respectively) as compared to glucose alone (0.01 g g^–1 of glucose). The productivity of diacetyl on medium containing glucose and citrate was double that of a medium containing only citrate, although the yields were comparable.     

Production of acetate by mutant strains of Clostridium thermoaceticum

Summary Mutant strains were derived from Clostridium thermoaceticum ATCC 39 289 by treatment with chemical mutagenic agents and selective enrichment procedures. Some mutant strains exhibited growth when cultured in media containing 20 mabetm (1.75 g l^–1) pyruvate of high-magnesium lime (dolime) above pH 6.0. One strain (G-20) grew and produced acetate when 80 mabetm (7 gl^–1) pyruvate or 50 mabetm (2.3 g l^–1) formate at pH 5.6 was the sole energy source. In a fed-batch process controlled at pH 6.2, this mutant produced 52.5 g l^–1 acetate (equivalent to 72.5 g l^–1 Na acetate) and 67 g l^–1 calcium-magnesium acetate (CMA) in 140 h when dolime was the neutralizing agent, with 93% substrate utilization. This mutant strain holds promise for CMA production due to its better tolerance of dolime and its ability to synthesize high levels of acetic acid. Offprint requests to: S. R. Parekh     

Preparation and testing of Sardinella protein hydrolysates as nitrogen source for extracellular lipase production by Rhizopus oryzae

Various fish protein hydrolysates (FPH) from sardinella (Sardinella aurita) were used as nitrogen sources for the production of extracellular lipase by the filamentous fungus Rhizopus oryzae. The best results were obtained with defatted meat–fish protein hydrolysates (DMFPH), indicating the presence in the lipid fraction of some constituents which may repress lipase synthesis. Furthermore, it was found that the extensive hydrolysis of fish proteins resulted in a higher lipase production. The use of 40 g DMFPH l^–1 for the growth of Rhizopus oryzae in medium R1 resulted in a lipase production of 394 U ml^–1, higher than the yield obtained with standard soy peptone as nitrogen source (373 U ml^–1). The most appropriate medium for the growth and the production of lipase is composed only of 24 g DMFPH l^–1 and 10 g glucose l^–1, indicating that the strain can obtain its nitrogen and salts requirements directly from fish substrate.     

Genetics and Physiology of Acetate Metabolism by the Pta-Ack Pathway of Streptococcus mutans

In the dental caries pathogen Streptococcus mutans, phosphotransacetylase (Pta) catalyzes the conversion of acetyl coenzyme A (acetyl-CoA) to acetyl phosphate (AcP), which can be converted to acetate by acetate kinase (Ack), with the concomitant generation of ATP. A ΔackA mutant displayed enhanced accumulation of AcP under aerobic conditions, whereas little or no AcP was observed in the Δpta or Δpta ΔackA mutant. The Δpta and Δpta ΔackA mutants also had diminished ATP pools compared to the size of the ATP pool for the parental or ΔackA strain. Surprisingly, when exposed to oxidative stress, the Δpta ΔackA strain appeared to regain the capacity to produce AcP, with a concurrent increase in the size of the ATP pool compared to that for the parental strain. The ΔackA and Δpta ΔackA mutants exhibited enhanced (p)ppGpp accumulation, whereas the strain lacking Pta produced less (p)ppGpp than the wild-type strain. The ΔackA and Δpta ΔackA mutants displayed global changes in gene expression, as assessed by microarrays. All strains lacking Pta, which had defects in AcP production under aerobic conditions, were impaired in their abilities to form biofilms when glucose was the growth carbohydrate. Collectively, these data demonstrate the complex regulation of the Pta-Ack pathway and critical roles for these enzymes in processes that appear to be essential for the persistence and pathogenesis of S. mutans.     

Kinetic analysis of ethanol production by an acetate-resistant strain of recombinant Zymomonas mobilis

Zymomonas mobilis ZM4/Ac^R (pZB5), a mutant recombinant strain with increased acetate resistance, has been isolated following electroporation of Z. mobilis ZM4/Ac^R. This mutant strain showed enhanced kinetic characteristics in the presence of 12 g sodium acetate l^–1 at pH 5 in batch culture on 40 g glucose, 40 g xylose l^–1 medium when compared to ZM4 (pZB5). In continuous culture, there was evidence of increased maintenance energy requirements/uncoupling of metabolism for ZM4/Ac^R (pZB5) in the presence of sodium acetate; a result confirmed by analysis of the effect of acetate on other strains of Z. mobilis. Nomenclature m Cell maintenance energy coefficient (g g^–1 h^–1)Maximum overall specific growth rate (1 h^–1)Maximum specific ethanol production rate (g g^–1 h^–1)Maximum specific total sugar utilization rate (g g^–1 h^–1)Biomass yield per mole of ATP (g mole^–1 Ethanol yield on total sugars (g g^–1)Biomass yield on total sugars (g g^–1)True biomass yield on total sugars (g g^–1)     

Conversion of an obligate autotrophic bacteria to heterotrophic growth: expression of a heterogeneous phosphofructokinase gene in the chemolithotroph Acidithiobacillus thiooxidans

A plasmid pSDK-1 containing the Escherichia coli phosphofructokinase-1 gene (pfkA) was constructed, and transferred into Acidithiobacillus thiooxidans Tt-7 by conjugation. The pfkA gene from E. coli could be expressed in this obligately autotrophic bacterium but the enzyme activity (18 U g^–1) was lower than that in E. coli (K12: 86 U g^–1; DF1010 carrying plasmid pSDK-1: 97 U g^–1). In the presence of glucose, the Tt-7 transconjugant consumed glucose leading to a better growth yield.     

Production of a fusion protein of sweet potato sporamin from recombinant E. coli XL1 Blue by fed-batch fermentations

Glucose-stat and pH-stat control strategies were employed in order to culture a recombinant E. coli XL1 Blue to produce a fusion protein of sweet potato sporamin (SPA) and glutathione S-transferase (GST) from the recombinant E. coli XL1 Blue. Cell densities up to 25 g l^–1 and 28.9 mg fusion protein (GST-SPA) g^–1 cell dry weight (CDW) was achieved from a fed-batch fermentation controlled by glucose-stat strategy. A pH-stat control fermentation using glycerol as a carbon source gave E. coli up to 27 g l^–1 and 31.5 mg GST-SPA g^–1 CDW. Additionally, a pH-stat control strategy using glucose as a carbon source gave E. coli up to 15 g l^–1 and about 22.7 mg g^–1 CDW of GST-SPA.     

ATP Production after ultraviolet irradiation inEscherichia coli

Doses of ultraviolet (UV) irradiation up to 40 Jm^–2 produce a continuous increase of both the level and the rate of ATP production in a RecA⁺ strain ofEscherichia coli growing in AB minimal medium with glucose as carbon source. At fluences higher than 40 Jm^–2, these two parameters increase at a constant rate independent of the dose. Furthermore, in the UV-irradiatedrecA13 mutant, the concentration of ATP is higher and its rate of production is faster than in the RecA⁺ strain. The same behavior as cited above was shown by both RecA⁺ and RecA^– cells when incubated in AB minimal medium without any carbon source both 60 min before and after UV irradiation.     

Fermentation characterization of an L-tryptophan producing Escherichia coli strain with inactivated phosphotransacetylase

Acetate is a primary inhibitory metabolite in Escherichia coli cultivation which is detrimental to bacterial growth and the formation of desired products. It can be derived from acetyl coenzyme A by the phosphotransacetylase (Pta)–acetate kinase (AckA) pathway. In this study, the fermentation characteristics of Pta mutant strain E. coli TRTHΔpta were compared with those of the control strain E. coli TRTH in a 30-L fermentor. The effects of glucose concentration and dissolved oxygen (DO) level were investigated, and the results suggest that DO and glucose concentration are vital influencing parameters for the production of L-tryptophan. Based on our experimental results, we then tested a DO-stat fed-batch fermentation strategy. When DO was controlled at about 20 % during L-tryptophan fermentation in the DO-stat fed-batch system, the pta mutant was able to maintain a higher growth rate at the exponential phase, and the final biomass and L-tryptophan production were increased to 55.3 g/L and 35.2 g/L, respectively. Concomitantly, as the concentration of acetate decreased to 0.7 g/L, the accumulation of pyruvate and lactate increased in the mutant strain as compared with the control strain. This characterization of the recombinant mutant strain provides useful information for the rational modification of metabolic fluxes to improve tryptophan production.     

Enzyme formation by a yeast cell wall lytic Arthrobacter species: chitinolytic activity

The kinetics of the release of chitinolytic activity (endochitinase EC 3.2.1.14, \-N-acetyglucosaminidase EC 3.2.1.30) by a yeast cell wall lytic Arthrobacter species was studied. The organism was cultivated on yeast cell wall, mycelium of Trichoderma reesei, colloidal chitin, N-acetylglucosamine, glucosamine and mixtures with acetate. With the exception of yeast cell wall, these substrates were used as the sole source of carbon and nitrogen. The growth on colloidal chitin (0.5%) proceeded at a maximum specific growth rate (_umax) of 0.23 h^–1 and yielded 2700 mU1^–1 chitinase. Yeast cell wall and mycelium of T. reesei supported more rapid growth (_max = 0.30 h^–1 and 0.25 h^–1 respectively) but yielded reduced chitinase activity (565 mUl^–1 and 700 mUl^–1). The growth rate on glucosamine (_max = 0.24 h^–1) was reduced when this was mixed with acetate (_max = 0.12 h^–1), whereas the enzyme yield was increased from 720 mUl^–1 to 960 mUl^–1. The same effect on growth rate was observed with glucose and equimolar mixtures of glucose and acetate, indicating a strong impact of the organic acid on carbohydrate transport or metabolism. The growth of adapted cells on N-acetylglucosamine was comparable to that observed on an equimolar mixture of glucosamine and acetate, indicating that N-acetylglucosamine is rapidly hydrolysed by adapted cells.     

Metabolism of d(+)-carnitine by Escherichia coli

Summary Escherichia coli 044 K74 grown under anaerobic conditions in the presence of l(–)-carnitine is able to convert d(+)-carnitine into the l(–)-enantiomer. This activity is repressed by electron acceptors such as oxygen and nitrate as well as by glucose. d(+)-Carnitine shows no effect on the induction or repression of the corresponding enzyme or enzyme system. Resting cells of E. coli 044 K74 were used for the formation of l(–)-carnitine from d(+)-carnitine. The maximum obtained yield was 50%. -Butyrobetaine was formed as a by-product. Offprint requests to: H. Jung     

Protease and lipase production by a strain ofSerratia marcescens (532 S)

Summary Production of both exolipase and exoprotease activities bySerratia marcescens 532 S isolated from an aerobic fixed-biomass reactor were strongly influenced by nutritional factors which acted as inducers or repressors. In batch culture, protease and lipase activities were produced after the exponential phase. NH₄Cl, amino acids and simple carbon sources caused repression of protease activity. At a concentration of 1.5 g L^–1, the individual addition of maltose, mannitol, acetate, fructose or glucose, repressed exoprotease production, with the greatest effect by glucose. An inverse relationship existed between exoprotease synthesis and increasing glucose concentrations. Lipids activated lipase production, the most significant increase occurred when Tween 80 was added in the medium. Thus, glucidolytic, proteolytic and lipolytic activities could be efficiently expressed in batch cultures only successively.At low dilution rate of chemostat cultures with a constant glucose input concentration of 2 g L^–1, glucidolytic, proteolytic and lipolytic activities were produced, but did not have the same regulation: atD values <0.08 h^–1, the level of protease activity dropped while that of lipase showed a corresponding increase. Above these values, increasingD led to a decrease of the two hydrolase activities, at the level of the specific activities as well as in the specific rate of biosynthesis of each enzyme. Similar results were obtained in chemostat culture with a constant specific growth rate of 0.04 h^–1 with increasing glucose input concentrations, i.e. protease and lipase activities decreased when the specific glucose uptake rates were enhanced.     

Citric acid production by 2-deoxyglucose-resistant mutant strains of Aspergillus niger

Summary Many mutant strains showing resistance to 2-deoxy-d-glucose (DG) on minimal medium containing glycerol as a carbon source were induced from Aspergillus niger WU-2223L, a citric acid-producing strain. The mutant strains were classifiable into two types according to their growth characteristics. On the agar plates containing glucose as a sole carbon source, mutant strains of the first type showed good growth irrespective of the presence or absence of DG. When cultivated in shake cultures, some strains of the first type, such as DGR1–2, showed faster glucose consumption and growth than strain WU-2223L. The period for citric acid production shortened from 9 days for strain WU-2223L to 6–7 days for these mutant strains. The levels and yields of citric acid production of the mutant strains were almost the same as those of strain WU-2223L. The mutant strains of the second type, however, showed very slow or no growth on both the agar plates containing glucose and fructose as sole carbon sources. In shake cultures, mutant strains such as DGR2-8 showed decreased glucose consumption rates, resulting in very low production of citric acid.     

Kinetic resolution of ketoprofen ester catalyzed by lipase from a mutant of CBS 5791

A biotransformation process was developed for the production of (S)-ketoprofen by enantioseletive hydrolysis of racemic ketoprofen ester using the mutant Trichosporon laibacchii strain CBS 5791. A satisfactory result was obtained, in which the E was 82.5, with an ee of 0.94 and a conversion of 0.47 under the optimum hydrolysis conditions [E is enantiomeric ratio, E=ln[1–X(1+ee)]/ln[1–X(1–ee)]; ee is enantiomeric excess, ee=(C_S–C_R)/(C_S+C_R): temperature of hydrolysis was 23°C]. The medium used in biotransformation was a mixture of growth broth and biotransformation broth at a ratio of 1:9, the concentration of Tween 80 was 15 g/l, the time of hydrolysis, 72 h. These results are promising for further scale-up. Tween 80 significantly improved lipase enantioselectivity and activity at the optimum concentration.     

Quantitative aspects of glucose metabolism by Escherichia coli B/r,grown in the presence of pyrroloquinoline quinone

Escherichia coli B/r was grown in chemostat cultures under various limitations with glucose as carbon source. Since E. coli only synthesized the glucose dehydrogenase (GDH) apo-enzyme and not the appropriate cofactor, pyrroloquinoline quinone (PQQ), no gluconate production could be observed. However, when cell-saturating amounts of PQQ (nmol to mol range) were pulsed into steady state glucose-excess cultures of E. coli, the organisms responded with an instantaneous formation of gluconate and an increased oxygen consumption rate. This showed that reconstitution of GDH in situ was possible.Hence, in order to examine the influence on glucose metabolism of an active GDH, E. coli was grown aerobically in chemostat cultures under various limitations in the presence of PQQ. It was found that the presence of PQQ indeed had a sizable effect: at pH 5.5 under phosphate- or sulphate- limited conditions more than 60% of the glucose consumed was converted to gluconate, which resulted in steady state gluconate concentrations up to 80 mmol/l. The specific rate of gluconate production (0.3–7.6 mmol·h^-1·(g dry wt cells)^-1) was dependent on the growth rate and the nature of the limitation. The production rate of other overflow metabolites such as acetate, pyruvate, and 2-oxoglutarate, was only slightly altered in the presence of PQQ. The fact that the cells were now able to use an active GDH apparently did not affect apo-enzyme synthesis.Abbreviations HEPES N-2-hydroxy-ethylpiperazine-N-2-ethane sulphonic acid - MES 2-morpholinoethane sulphonic acid - PQQ pyrroloquinoline quinone (systematic name: 2,7,9-tricarboxy-1H-pyrrolo-(2,3-f)-quinoline-4,5-dione) - WB Wurster's Blue (systematic name: 1,4-bis-(dimethylamino)-benzene perchlorate     

Optimization of culture on the overproduction of TRAIL in high-cell-density culture by recombinant Escherichia coli

Different nutrient-feeding cultures were carried out in producing recombinant protein of truncated tumor necrosis factor related apoptosis-inducing ligand (TRAIL) (114–281 amino acids of TRAIL) in Escherichia coli strain C600/pBV-TRAIL. The effects of preinduction specific growth rate, postinduction carbon source (glucose and glycerol), and feeding strategies were investigated. The higher preinduction specific growth rate (μ=0.22 h⁻¹) contributed to the increase in the TRAIL production, at which TRAIL was accumulated in bacterial cells as 7.2% of total cellular protein, corresponding to 1.99 g l⁻¹ in contrast with 5.1% (1.29 g l⁻¹) at preinduction specific growth rate (μ=0.1 h⁻¹) during high-cell-density culture. Glycerol was superior to glucose as the postinduction carbon source for TRAIL production. Under similar culture conditions, the final concentration of TRAIL was produced 1.59-fold more when glycerol was used as postinduction carbon source than when glucose was used. At the same time, the results showed that it is efficient to adopt the pH-stat feeding strategy at postinduction for the overproduction of TRAIL. The TRAIL production was increased up to 4.51 g l⁻¹, approximately 16.1% of total cellular protein. The mechanisms behind the preinduction specific growth rate effect on the expression level may be ascribed to the leakage secretion of acetate.     

The effect of<Emphasis Type="Italic"> pfl</Emphasis> gene knockout on the metabolism for optically pure <Emphasis Type="SmallCaps">d</Emphasis>-lactate production by<Emphasis Type="Italic"> Escherichia coli</Emphasis>

The effect of gene knockout on metabolism in the pflA^–, pflB^–, pflC^–, and pflD^– mutants of Escherichia coli was investigated. Batch cultivations of the pfl ^– mutants and their parent strain were conducted using glucose as a carbon source. It was found that pflA^– and pflB^– mutants, but not pflC^– and pflD^– mutants, produced large amounts of d-lactate from glucose under the microaerobic condition, and the maximum yield was 73%. In order to investigate the metabolic regulation mechanism, we measured enzyme activities for the following eight enzymes: glucose 6-phosphate dehydrogenase, 6-phosphogluconate dehydrogenase, glyceraldehyde 3-phosphate dehydrogenase (GAPDH), pyruvate kinase, lactate dehydrogenase (LDH), phosphoenolpyruvate carboxylase, acetate kinase, and alcohol dehydrogenase. Intracellular metabolite concentrations of glucose 6-phosphate, fructose 1,6-bisphosphate, phosphoenolpyruvate, pyruvate, acetyl coenzyme A as well as ATP, ADP, AMP, NADH, and NAD⁺ were also measured. It was shown that the GAPDH and LDH activities were considerably higher in pflA^– and pflB^– mutants, which implies coupling between NADH production and consumption between the two corresponding reactions. The urgent energy requirement was shown by the lower ATP/AMP level due to both oxygen limitation and pfl gene knockout, which promoted significant stepping-up of glycolysis when using glucose as a carbon source. It was shown that the demand for energy is more important than intracellular redox balance, thus excess NADH produced through GAPDH resulted in a significantly higher intracellular NADH/NAD⁺ ratio in pfl ^– mutants. Consequently, the homolactate production was achieved to meet the requirements of the redox balance and the energy production through glycolysis. The effect of using different carbon sources such as gluconate, pyruvate, fructose, and glycerol was investigated.