Elimination of glycerol and replacement with alternative products in ethanol fermentation by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Glycerol is a major by-product of ethanol fermentation by Saccharomyces cerevisiae and typically 2–3% of the sugar fermented is converted to glycerol. Replacing the NAD⁺-regenerating glycerol pathway in S. cerevisiae with alternative NADH reoxidation pathways may be useful to produce metabolites of biotechnological relevance. Under fermentative conditions yeast reoxidizes excess NADH through glycerol production which involves NADH-dependent glycerol-3-phosphate dehydrogenases (Gpd1p and Gpd2p). Deletion of these two genes limits fermentative activity under anaerobic conditions due to accumulation of NADH. We investigated the possibility of converting this excess NADH to NAD⁺ by transforming a double mutant (gpd1∆gpd2∆) with alternative oxidoreductase genes that might restore the redox balance and produce either sorbitol or propane-1,2-diol. All of the modifications improved fermentative ability and/or growth of the double mutant strain in a self-generated anaerobic high sugar medium. However, these strain properties were not restored to the level of the parental wild-type strain. The results indicate an apparent partial NAD⁺ regeneration ability and formation of significant amounts of the commodity chemicals like sorbitol or propane-1,2-diol. The ethanol yields were maintained between 46 and 48% of the sugar mixture. Other factors apart from the maintenance of the redox balance appeared to influence the growth and production of the alternative products by the genetically manipulated strains.     

产甘油假丝酵母与酿酒酵母胞浆3-磷酸甘油脱氢酶基因的功能比较

胞浆3-磷酸甘油脱氢酶(GPD)是酿酒酵母细胞甘油合成过程中的关键限速酶．尽管高产甘油菌株产甘油假丝酵母基因组中编码该酶的基因CgGPD已经被克隆出来,但是具体的功能,特别是与酿酒酵母GPD1和GPD2基因的功能比较值得进一步研究．以酿酒酵母渗透压敏感型的gpd1/gpd2和gpd1突变株为宿主,分别导入CgGPD、GPD1和GPD2基因,比较分析了CgGPD、GPD1和GPD2基因在高渗透压胁迫条件下和厌氧环境中的表达调控,及其对细胞甘油合成能力的影响．研究发现,GPD1基因受到渗透压诱导表达,GPD2基因在细胞厌氧条件下起着氧化还原平衡调节作用,而CgGPD基因不仅能够在渗透压胁迫条件下通过过量快速合成甘油调节渗透压平衡,而且能够在厌氧培养环境中互补GPD2基因的缺失,使gpd1/gpd2缺失突变株能够正常生长,同时提高了突变株的甘油合成能力．结果表明,CgGPD基因在gpd1/gpd2缺失突变株中既具有GPD1基因的功能,又能发挥GPD2基因的功能．     

Improved ethanol production by glycerol-3-phosphate dehydrogenase mutants of Saccharomyces cerevisiae

The anaerobic performance of gpd1Δ and gpd2Δ mutants of Saccharomyces cerevisiae was characterized and compared to that of a wild-type strain under well-controlled conditions by using a high-performance bioreactor. There was a 40% reduction in glycerol level in the gpd2Δ mutant compared to the wild-type. Also the gpd1Δ mutant showed a slight decrease in glycerol formation but to a much lesser degree. As a consequence, ethanol formation in the gpd2Δ mutant was elevated by 13%. In terms of growth, the gpd1Δ mutant and the wild-type were indistinguishable. The gpd2Δ mutant, on the other hand, displayed an extended lag phase as well as a reduced growth rate under the exponential phase. Even though glycerol-3-phosphate dehydrogenase 2 (GPD2) is the important enzyme under anaerobic conditions it can, at least in part, be substituted by GPD1. This was indicated by the higher expression level of GPD1 in the gpd2Δ mutant compared to the wild type. These results also show that the cells are able to cope and maintain redox balance under anaerobic conditions even if glycerol formation is substantially reduced, as observed in the gpd2Δ mutant. One obvious way of solving the redox problem would be to make a biomass containing less protein, since most of the excess NADH originates from amino acid biosynthesis. However, the gpd2Δ mutant did not show any decrease in the protein content of the biomass. Received: 16 February 1998 / Received revision: 16 March 1998 / Accepted: 1 June 1998     

Over-expressing <Emphasis Type="Italic">GLT1</Emphasis> in a <Emphasis Type="Italic">gpd2</Emphasis>Δ mutant of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> to improve ethanol production

We constructed two recombinant strains of Saccharomyces cerevisiae in which the GPD2 gene was deleted using a one-step gene replacement method to minimize formation of glycerol and improve ethanol production. In addition, we also over-expressed the GLT1 gene by a two-step gene replacement method to overcome the redox-imbalancing problem in the genetically modified strains. The result of anaerobic batch fermentations showed that the rate of growth and glucose consumption of the KAM-5 (MATα ura3 gpd2Δ::RPT) strain were slower than the original strain, and the KAM-13 (MATα ura3 gpd2Δ::RPT P _PGK -GLT1) strain, however, was indistinguishable compared to the original strain using the same criteria, as analyzed. On the other hand, when compared to the original strain, there were 32 and 38% reduction in glycerol formation for KAM-5 and KAM-13, respectively. Ethanol production increased by 8.6% for KAM-5 and 13.4% for KAM-13. Dramatic reduction in acetate and pyruvic acid was also observed in both mutants compared to the original strains. Although gene GPD2 is responsible for the glycerol synthesis, the mutant KAM-13, in which glycerol formation was substantially reduced, was able to cope and maintain osmoregulation and redox balance and have increased ethanol production under anaerobic fermentations. The result verified the proposed concept of increasing ethanol production in S. cerevisiae by genetic engineering of glycerol synthesis and over-expressing the GLT1 gene along with reconstituted nicotinamide adenine dinucleotide metabolism.     

Expression of protein engineered NADP<Superscript>+</Superscript>-dependent xylitol dehydrogenase increases ethanol production from xylose in recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

A recombinant Saccharomyces cerevisiae strain transformed with xylose reductase (XR) and xylitol dehydrogenase (XDH) genes from Pichia stipitis has the ability to convert xylose to ethanol together with the unfavorable excretion of xylitol, which may be due to cofactor imbalance between NADPH-preferring XR and NAD⁺-dependent XDH. To reduce xylitol formation, we have already generated several XDH mutants with a reversal of coenzyme specificity toward NADP⁺. In this study, we constructed a set of recombinant S. cerevisiae strains with xylose-fermenting ability, including protein-engineered NADP⁺-dependent XDH-expressing strains. The most positive effect on xylose-to-ethanol fermentation was found by using a strain named MA-N5, constructed by chromosomal integration of the gene for NADP⁺-dependent XDH along with XR and endogenous xylulokinase genes. The MA-N5 strain had an increase in ethanol production and decrease in xylitol excretion compared with the reference strain expressing wild-type XDH when fermenting not only xylose but also mixed sugars containing glucose and xylose. Furthermore, the MA-N5 strain produced ethanol with a high yield of 0.49 g of ethanol/g of total consumed sugars in the nonsulfuric acid hydrolysate of wood chips. The results demonstrate that glucose and xylose present in the lignocellulosic hydrolysate can be efficiently fermented by this redox-engineered strain.     

Elimination of Glycerol Production in Anaerobic Cultures of a Saccharomyces cerevisiae Strain Engineered To Use Acetic Acid as an Electron Acceptor

In anaerobic cultures of wild-type Saccharomyces cerevisiae, glycerol production is essential to reoxidize NADH produced in biosynthetic processes. Consequently, glycerol is a major by-product during anaerobic production of ethanol by S. cerevisiae, the single largest fermentation process in industrial biotechnology. The present study investigates the possibility of completely eliminating glycerol production by engineering S. cerevisiae such that it can reoxidize NADH by the reduction of acetic acid to ethanol via NADH-dependent reactions. Acetic acid is available at significant amounts in lignocellulosic hydrolysates of agricultural residues. Consistent with earlier studies, deletion of the two genes encoding NAD-dependent glycerol-3-phosphate dehydrogenase (GPD1 and GPD2) led to elimination of glycerol production and an inability to grow anaerobically. However, when the E. coli mhpF gene, encoding the acetylating NAD-dependent acetaldehyde dehydrogenase (EC 1.2.1.10; acetaldehyde + NAD⁺ + coenzyme A ↔ acetyl coenzyme A + NADH + H⁺), was expressed in the gpd1Δ gpd2Δ strain, anaerobic growth was restored by supplementation with 2.0 g liter⁻¹ acetic acid. The stoichiometry of acetate consumption and growth was consistent with the complete replacement of glycerol formation by acetate reduction to ethanol as the mechanism for NADH reoxidation. This study provides a proof of principle for the potential of this metabolic engineering strategy to improve ethanol yields, eliminate glycerol production, and partially convert acetate, which is a well-known inhibitor of yeast performance in lignocellulosic hydrolysates, to ethanol. Further research should address the kinetic aspects of acetate reduction and the effect of the elimination of glycerol production on cellular robustness (e.g., osmotolerance).Bioethanol production by Saccharomyces cerevisiae is currently, by volume, the single largest fermentation process in industrial biotechnology. A global research effort is under way to expand the substrate range of S. cerevisiae to include lignocellulosic hydrolysates of nonfood feedstocks (e.g., energy crops and agricultural residues) and to increase productivity, robustness, and product yield (for reviews see references 20 and 35). A major challenge relating to the stoichiometry of yeast-based ethanol production is that substantial amounts of glycerol are invariably formed as a by-product (24). It has been estimated that, in typical industrial ethanol processes, up to 4% of the sugar feedstock is converted into glycerol (24). Although glycerol also serves as a compatible solute at high extracellular osmolarity (10), glycerol production under anaerobic conditions is primarily linked to redox metabolism (34).During anaerobic growth of S. cerevisiae, sugar dissimilation occurs via alcoholic fermentation. In this process, the NADH formed in the glycolytic glyceraldehyde-3-phosphate dehydrogenase reaction is reoxidized by converting acetaldehyde, formed by decarboxylation of pyruvate to ethanol via NAD⁺-dependent alcohol dehydrogenase. The fixed stoichiometry of this redox-neutral dissimilatory pathway causes problems when a net reduction of NAD⁺ to NADH occurs elsewhere in the metabolism. Such a net production of NADH occurs in assimilation when yeast biomass is synthesized from glucose and ammonia (34). Under anaerobic conditions, NADH reoxidation in S. cerevisiae is strictly dependent on reduction of sugar to glycerol (34). Glycerol formation is initiated by reduction of the glycolytic intermediate dihydroxyacetone phosphate to glycerol-3-phosphate, a reaction catalyzed by NAD⁺-dependent glycerol-3-phosphate dehydrogenase. Subsequently, the glycerol-3-phosphate formed in this reaction is hydrolyzed by glycerol-3-phosphatase to yield glycerol and inorganic phosphate.The importance of glycerol production for fermentative growth of yeasts was already observed in the 1960s during studies of non-Saccharomyces yeasts that exhibit a so-called “Custers effect.” In such yeast species, which are naturally unable to produce glycerol, fermentative growth on glucose is possible only in the presence of an external electron acceptor that can be reduced via an NADH-dependent reaction (e.g., the reduction of acetoin to butanediol via NAD⁺-dependent butanediol dehydrogenase) (29). It was later shown that gpd1Δ gpd2Δ strains of S. cerevisiae, which are also unable to produce glycerol, are similarly unable to grow under anaerobic conditions unless provided with acetoin as an external electron acceptor (8).In view of its large economic significance, several metabolic engineering strategies have been explored to reduce or eliminate glycerol production in anaerobic cultures of S. cerevisiae. Nissen et al. (25) changed the cofactor specificity of glutamate dehydrogenase, the major ammonia-fixing enzyme of S. cerevisiae, thereby increasing NADH consumption in biosynthesis. This approach significantly reduced glycerol production in anaerobic cultures grown with ammonia as the nitrogen source. Attempts to further reduce glycerol production by expression of a heterologous transhydrogenase, with the aim to convert NADH and NADP⁺ into NAD⁺ and NADPH, were unsuccessful (24) because intracellular concentrations of these pyridine nucleotide cofactor couples favor the reverse reaction (23).The goal of the present study was to investigate whether the engineering of a linear pathway for the NADH-dependent reduction of acetic acid to ethanol can replace glycerol formation as a redox sink in anaerobic, glucose-grown cultures of S. cerevisiae and thus provide a stoichiometric basis for elimination of glycerol production during industrial ethanol production. Significant amounts of acetic acid are released upon hydrolysis of lignocellulosic biomass, and, in fact, acetic acid is studied as an inhibitor of yeast metabolism in lignocellulosic hydrolysates (5, 7, 26). The S. cerevisiae genome already contains genes encoding acetyl coenzyme A (acetyl-CoA) synthetase (32) and NAD⁺-dependent alcohol dehydrogenases (ADH1-5 [12]). To complete the linear pathway for acetic acid reduction, we expressed an NAD⁺-dependent, acetylating acetaldehyde dehydrogenase (EC 1.2.1.10) from Escherichia coli into a gpd1Δ gpd2Δ strain of S. cerevisiae. This enzyme, encoded by the E. coli mhpF gene (15), catalyzes the reaction acetaldehyde + NAD⁺ + coenzyme A ↔ acetyl coenzyme A + NADH + H⁺. Growth and product formation of the engineered strain were then compared in the presence and absence of acetic acid and compared to those of a congenic reference strain.     

Regulation of glycerol metabolism in <Emphasis Type="Italic">Enterobacter aerogenes</Emphasis> NBRC12010 under electrochemical conditions

Enterobacter aerogenes NBRC12010 was able to ferment glycerol to ethanol and hydrogen gas. Fermentation of glycerol ceased in the stationary phase of growth, and it was activated by electrochemical reactions using thionine as an electron transfer mediator from bacterial cells to an electrode. Using resting cells of E. aerogenes NBRC12010 in only citrate buffer solution, the cells did not consume glycerol at all, but they could metabolize glucose. These results suggest that the regulation of glycerol metabolism occurred at enzymatic steps before glycolysis. In E. aerogenes NBRC12010, glycerol was metabolized via glycerol dehydrogenase (GDH) and then dehydroxyacetone kinase. The GDH-catalyzed reaction mainly depended on the ratio of NAD⁺/NADH. At a NAD⁺/NADH ratio of nearly 1 or less, it was substantially suppressed and glycerol metabolism stopped. When the ratio was higher than 1, GDH was activated and glycerol was metabolized. Thus, the reaction of glycerol metabolism depended on the balance of cellular NAD⁺/NADH. Exogenous NADH was oxidized to NAD⁺ by electrochemical reactions with thionine. We proposed the activation mechanism of glycerol metabolism under electrochemical conditions.     

Stimulation of reductive glycerol metabolism by overexpression of an aldehyde dehydrogenase in a recombinant <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> strain defective in the oxidative pathway

Previously, we constructed a glycerol oxidative pathway-deficient mutant strain of Klebsiella pneumoniae by inactivation of glycerol dehydrogenase (dhaD) to eliminate by-product synthesis during production of 1,3-propanediol (1,3-PD) from glycerol. Although by-product formation was successfully blocked in the resultant strain, the yield of 1,3-PD was not enhanced, probably because dhaD disruption resulted in insufficient regeneration of the cofactor NADH essential for the activity of 1,3-PD oxidoreductase (DhaT). To improve cofactor regeneration, in the present study we overexpressed an NAD⁺-dependent aldehyde dehydrogenase in the recombinant strain. To this end, an aldehyde dehydrogenase AldHk homologous to E. coli AldH but with NAD⁺-dependent propionaldehyde dehydrogenase activity was identified in K. pneumoniae. Functional analysis revealed that the substrate specificity of AldHk embraced various aldehydes including propionaldehyde, and that NAD⁺ was preferred over NADP⁺ as a cofactor. Overexpression of AldHk in the glycerol oxidative pathway-deficient mutant AK/pVOTHk resulted in a 3.6-fold increase (0.57 g l⁻¹ to 2.07 g l⁻¹) in the production of 3-hydroxypropionic acid (3-HP), and a 1.1-fold enhancement (8.43 g l⁻¹ to 9.65 g l⁻¹) of 1,3-PD synthesis, when glycerol was provided as the carbon source, compared to the levels synthesized by the control strain (AK/pVOT). Batch fermentation using AK/pVOTHk showed a significant increase (to 70%, w/w) in conversion of glycerol to the reductive metabolites, 1,3-PD and 3-HP, with no production of by-products except acetate.     

Thymidine production by overexpressing NAD<Superscript>+</Superscript> kinase in an <Emphasis Type="Italic">Escherichia coli</Emphasis> recombinant strain

Intracellular NADPH/NADP⁺ ratio in cells grown on various production media with different carbon and nitrogen sources had a positive correlation with the thymidine production. To improve thymidine production in a previously engineered E. coli strain, NAD⁺ kinase was overexpressed in it resulting in the NADPH/NADP⁺ ratio shifting from 0.184 to 0.267. The [NADH + NADP⁺]/[NAD⁺ + NADPH] ratio was, however, not significantly altered. In jar fermentation, 740 mg thymidine l⁻¹ was produced in parental strain, while 940 mg l⁻¹ of thymidine was produced in NAD⁺ kinase-expressing strain.     

Engineering of a matched pair of xylose reductase and xylitol dehydrogenase for xylose fermentation by Saccharomyces cerevisiae

Metabolic engineering of Saccharomyces cerevisiae for xylose fermentation has often relied on insertion of a heterologous pathway consisting of nicotinamide adenine dinucleotide (phosphate) NAD(P)H-dependent xylose reductase (XR) and NAD⁺-dependent xylitol dehydrogenase (XDH). Low ethanol yield, formation of xylitol and other fermentation by-products are seen for many of the S. cerevisiae strains constructed in this way. This has been ascribed to incomplete coenzyme recycling in the steps catalyzed by XR and XDH. Despite various protein-engineering efforts to alter the coenzyme specificity of XR and XDH individually, a pair of enzymes displaying matched utilization of NAD(H) and NADP(H) was not previously reported. We have introduced multiple site-directed mutations in the coenzyme-binding pocket of Galactocandida mastotermitis XDH to enable activity with NADP⁺, which is lacking in the wild-type enzyme. We describe four enzyme variants showing activity for xylitol oxidation by NADP⁺ and NAD⁺. One of the XDH variants utilized NADP⁺ about 4 times more efficiently than NAD⁺. This is close to the preference for NADPH compared with NADH in mutants of Candida tenuis XR. Compared to an S. cerevisiae-reference strain expressing the genes for the wild-type enzymes, the strains comprising the gene encoding the mutated XDH in combination a matched XR mutant gene showed up to 50% decreased glycerol yield without increase in ethanol during xylose fermentation.     

Expression of NAD<Superscript>+</Superscript>-dependent formate dehydrogenase in <Emphasis Type="Italic">Enterobacter aerogenes</Emphasis> and its involvement in anaerobic metabolism and H<Subscript>2</Subscript> production

An expression system for NAD⁺-dependent formate dehydrogenase gene (fdh1), from Candida boidinii, was constructed and cloned into Enterobacter aerogenes IAM1183. With the fdh1 expression, the total H₂ yield was attributed to a decrease in activity of the lactate pathway and an increase of the formate pathway flux due to the NADH regeneration. Analysis of the redox state balance and ethanol-to-acetate ratio in the fdhl-expressed strain showed that increased reducing power arose from the reconstruction of NADH regeneration pathway from formate thereby contributing to the improved H₂ production.     

Evolutionary engineering of a glycerol‐3‐phosphate dehydrogenase‐negative,acetate‐reducing Saccharomyces cerevisiae strain enables anaerobic growth at high glucose concentrations

Glycerol production by Saccharomyces cerevisiae, which is required for redox-cofactor balancing in anaerobic cultures, causes yield reduction in industrial bioethanol production. Recently, glycerol formation in anaerobic S. cerevisiae cultures was eliminated by expressing Escherichia coli (acetylating) acetaldehyde dehydrogenase (encoded by mhpF) and simultaneously deleting the GPD1 and GPD2 genes encoding glycerol-3-phosphate dehydrogenase, thus coupling NADH reoxidation to reduction of acetate to ethanol. Gpd^– strains are, however, sensitive to high sugar concentrations, which complicates industrial implementation of this metabolic engineering concept. In this study, laboratory evolution was used to improve osmotolerance of a Gpd^– mhpF-expressing S. cerevisiae strain. Serial batch cultivation at increasing osmotic pressure enabled isolation of an evolved strain that grew anaerobically at 1 M glucose, at a specific growth rate of 0.12 h⁻¹. The evolved strain produced glycerol at low concentrations (0.64 ± 0.33 g l⁻¹). However, these glycerol concentrations were below 10% of those observed with a Gpd⁺ reference strain. Consequently, the ethanol yield on sugar increased from 79% of the theoretical maximum in the reference strain to 92% for the evolved strains. Genetic analysis indicated that osmotolerance under aerobic conditions required a single dominant chromosomal mutation, and one further mutation in the plasmid-borne mhpF gene for anaerobic growth.     

Interruption of glycerol pathway in industrial alcoholic yeasts to improve the ethanol production

The two homologous genes GPD1 and GPD2, encoding two isoenzymes of NAD⁺-dependent glycerol-3-phosphate dehydrogenase in industrial yeast Saccharomyces cerevisiae CICIMY0086, had been deleted. The obtained two kinds of mutants gpd1Δ and gpd2Δ were studied under alcoholic fermentation conditions. gpd1Δ mutants exhibited a 4.29% (relative to the amount of substrate consumed) decrease in glycerol production and 6.83% (relative to the amount of substrate consumed) increased ethanol yield while gpd2Δ mutants exhibited a 7.95% (relative to the amount of substrate consumed) decrease in glycerol production and 7.41% (relative to the amount of substrate consumed) increased ethanol yield compared with the parental strain. The growth rate of the two mutants were slightly lower than that of the wild type under the exponential phase whereas ANG1 (gpd1Δ) and the decrease in glycerol production was not accompanied by any decline in the protein content of the strain ANG1 (gpd1Δ) but a slight decrease in the strain ANG2 (gpd2Δ). Meanwhile, dramatic decrease of acetate acid formation was observed in strain ANG1 (gpd1Δ) and ANG2 (gpd2Δ) compared to the parental strain. Therefore, it is possible to improve the ethanol yield by interruption of glycerol pathway in industrial alcoholic yeast.     

A genetic overhaul of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> 424A(LNH-ST) to improve xylose fermentation

Robust microorganisms are necessary for economical bioethanol production. However, such organisms must be able to effectively ferment both hexose and pentose sugars present in lignocellulosic hydrolysate to ethanol. Wild type Saccharomyces cerevisiae can rapidly ferment hexose, but cannot ferment pentose sugars. Considerable efforts were made to genetically engineer S. cerevisiae to ferment xylose. Our genetically engineered S cerevisiae yeast, 424A(LNH-ST), expresses NADPH/NADH xylose reductase (XR) that prefer NADPH and NAD⁺-dependent xylitol dehydrogenase (XD) from Pichia stipitis, and overexpresses endogenous xylulokinase (XK). This strain is able to ferment glucose and xylose, as well as other hexose sugars, to ethanol. However, the preference for different cofactors by XR and XD might lead to redox imbalance, xylitol excretion, and thus might reduce ethanol yield and productivity. In the present study, genes responsible for the conversion of xylose to xylulose with different cofactor specificity (1) XR from N. crassa (NADPH-dependent) and C. parapsilosis (NADH-dependent), and (2) mutant XD from P. stipitis (containing three mutations D207A/I208R/F209S) were overexpressed in wild type yeast. To increase the NADPH pool, the fungal GAPDH enzyme from Kluyveromyces lactis was overexpressed in the 424A(LNH-ST) strain. Four pentose phosphate pathway (PPP) genes, TKL1, TAL1, RKI1 and RPE1 from S. cerevisiae, were also overexpressed in 424A(LNH-ST). Overexpression of GAPDH lowered xylitol production by more than 40%. However, other strains carrying different combinations of XR and XD, as well as new strains containing the overexpressed PPP genes, did not yield any significant improvement in xylose fermentation.     

Regulation of NAD<Superscript>+</Superscript>-dependent isocitrate dehydrogenase in the citrate producing yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

The mechanism of the increased accumulation (overproduction) of citric acids in the yeast Yarrowia lipolytica while growing in the presence of glucose under nitrogen deficiency was investigated. The limitation of the yeast growth by the source of nitrogen decreases the total content of nucleotides and increases the ratios of ATP/AMP and NADH/NAD⁺. NAD⁺-Dependent isocitrate dehydrogenase, an enzyme of the tricarboxylic acid cycle playing a key role in the regulation of biosynthesis of citric and isocitric acids, was isolated from Y. lipolytica. The molecular weights of the native enzyme and its subunits were found to be 412 and 52 kD, respectively. It is concluded that the enzyme is a homooligomer consisting of eight subunits. Investigation of the effect of some intermediates of the tricarboxylic acid cycle on the activity of this enzyme suggests that the enhanced excretion of citric acids can be caused by the inhibition of NAD⁺-dependent isocitrate dehydrogenase due to the decrease in the content of AMP and increase in the NADH/NAD⁺ ratio in the cells of Y. lipolytica under depletion of nitrogen.Translated from Biokhimiya, Vol. 69, No. 12, 2004, pp. 1706–1714.Original Russian Text Copyright © 2004 by Morgunov, Solodovnikova, Sharyshev, Kamzolova, Finogenova.     

Enhanced aldehyde dehydrogenase activity by regenerating NAD+ in Klebsiella pneumoniae and implications for the glycerol dissimilation pathways

In Klebsiella pneumoniae, 3-hydroxypropaldehyde is converted to 3-hydroxypropionic acid (3-HP) by aldehyde dehydrogenase (ALDH) with NAD⁺ as a cofactor. Although ALDH overexpression stimulates the formation of 3-HP, it ceases to accumulate when NAD⁺ is exhausted. Here we show that NAD⁺ regeneration, together with ALDH overexpression, facilitates 3-HP production and benefits cell growth. Three distinct NAD⁺-regenerating enzymes: NADH oxidase and NADH dehydrogenase from K. pneumoniae, and glycerol-3-phosphate dehydrogenase (GPD1) from Saccharomyces cerevisiae, were individually expressed in K. pneumoniae. In vitro assay showed their higher activities than that of the control, indicating their capacities to regenerate NAD⁺. When they were respectively co-expressed with ALD4, an ALDH from S. cerevisiae, the activities of ALD4 were significantly elevated compared with that expressing ALD4 alone, suggesting that the regenerated NAD⁺ enhanced the activity of ALD4. More interestingly, the growth rates of all NAD⁺-regenerating strains were prolonged in comparison with the control, indicating that NAD⁺ regeneration stimulated cell proliferation. This study not only reveals the reliance of ALD4 activity on NAD⁺ availability but also provides a method for regulating the dha regulon.     

Anaerobic glycerol production by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strains under hyperosmotic stress

Glycerol formation is vital for reoxidation of nicotinamide adenine dinucleotide (reduced form; NADH) under anaerobic conditions and for the hyperosmotic stress response in the yeast Saccharomyces cerevisiae. However, relatively few studies have been made on hyperosmotic stress under anaerobic conditions. To study the combined effect of salt stress and anaerobic conditions, industrial and laboratory strains of S. cerevisiae were grown anaerobically on glucose in batch-cultures containing 40 g/l NaCl. The time needed for complete glucose conversion increased considerably, and the specific growth rates decreased by 80–90% when the cells were subjected to the hyperosmotic conditions. This was accompanied by an increased yield of glycerol and other by-products and reduced biomass yield in all strains. The slowest fermenting strain doubled its glycerol yield (from 0.072 to 0.148 g/g glucose) and a nearly fivefold increase in acetate formation was seen. In more tolerant strains, a lower increase was seen in the glycerol and in the acetate, succinate and pyruvate yields. Additionally, the NADH-producing pathway from acetaldehyde to acetate was analysed by overexpressing the stress-induced gene ALD3. However, this had no or very marginal effect on the acetate and glycerol yields. In the control experiments, the production of NADH from known sources well matched the glycerol formation. This was not the case for the salt stress experiments in which the production of NADH from known sources was insufficient to explain the formed glycerol.     

Changes in the intracellular concentrations of the adenosine phosphates and nicotinamide adenine dinucleotides ofSaccharomyces cerevisiae during batch fermentation

Significant changes in the intracellular concentrations of adenosine phosphates and nicotinamide adenine dinucleotides were observed during fermentation of grape must by three different strains ofSaccharomyces cerevisiae: S. cerevisiae var.cerevisiae, a typical fermentative yeast strain and two flor-veil-forming strains,S. cerevisiae var.bayanus andS. cerevisiae var.capensis. The intracellular concentration of ATP was always higher inS. cerevisiae var.cerevisiae than in the flor-veil-forming strains. NAD⁺ and NADP⁺ concentrations decreased at faster rates in the flor-veil-forming yeasts than in the other yeast but NADH concentration was the same in all yeasts for the first 10 days of fermentation. NADPH concentration was always lower inS. cerevisiae var.cerevisiae than in the other yeasts and this yeast also showed higher rates of growth and fermentation during the early stages of the fermentation and the presence of non-viable cells at the end of fermentation. In contrast, the flor-veil-forming strains maintained growth and fermentation capabilities for a relatively long time and viable cells were present throughout the entire fermentation process (31 days).The authors are with the Department of Microbiology, Faculty of Sciences, University of Cordoba, Avda. San Alberto Magno s/n, 14004-Córdoba, Spain     

Growth rate of a non-fermentative <Emphasis Type="Italic">Escherichia coli</Emphasis> strain is influenced by NAD<Superscript>+</Superscript> regeneration

By complementing a non-fermentative Escherichia coli (ldhA ⁻ pflB ⁻) strain with the recombinant Zymomonas mobilis ethanol pathway (pdc, adhB), we evaluated the effect of different levels of enzymatic activity on growth rate demonstrating that there is a direct relationship between anaerobic growth rate and the total specific activity of pyruvate decarboxylase, which is the limiting enzyme of this specific fermentative NAD⁺ regenerating pathway. This relationship was proved to be useful to establish a selection strategy based on growth rate for the analysis of lctE libraries, which encode lactate dehydrogenase from Bacillus subtilis.     

A high effective NADH-ferricyanide dehydrogenase coupled with laccase for NAD<Superscript>+</Superscript> regeneration

Objectives

To find an efficient and cheap system for NAD⁺ regeneration

Results

A NADH-ferricyanide dehydrogenase was obtained from an isolate of Escherichia coli. Optimal activity of the NADH dehydrogenase was at 45 °C and pH 7.5, with a K _m value for NADH of 10 μM. By combining the NADH dehydrogenase, potassium ferricyanide and laccase, a bi-enzyme system for NAD⁺ regeneration was established. The system is attractive in that the O₂ consumed by laccase is from air and the sole byproduct of the reaction is water. During the reaction process, 10 mM NAD⁺ was transformed from NADH in less than 2 h under the condition of 0.5 U NADH dehydrogenase, 0.5 U laccase, 0.1 mM potassium ferricyanide at pH 5.6, 30 °C

Conclusion

The bi-enzyme system employed the NADH-ferricyanide dehydrogenase and laccase as catalysts, and potassium ferricyanide as redox mediator, is a promising alternative for NAD⁺ regeneration.