Metabolic Engineering of Acinetobacter baylyi ADP1 for Improved Growth on Gluconate and Glucose

A high growth rate in bacterial cultures is usually achieved by optimizing growth conditions, but metabolism of the bacterium limits the maximal growth rate attainable on the carbon source used. This limitation can be circumvented by engineering the metabolism of the bacterium. Acinetobacter baylyi has become a model organism for studies of bacterial metabolism and metabolic engineering due to its wide substrate spectrum and easy-to-engineer genome. It produces naturally storage lipids, such as wax esters, and has a unique gluconate catabolism as it lacks a gene for pyruvate kinase. We engineered the central metabolism of A. baylyi ADP1 more favorable for gluconate catabolism by expressing the pyruvate kinase gene (pykF) of Escherichia coli. This modification increased growth rate when cultivated on gluconate or glucose as a sole carbon source in a batch cultivation. The engineered cells reached stationary phase on these carbon sources approximately twice as fast as control cells carrying an empty plasmid and produced similar amount of biomass. Furthermore, when grown on either gluconate or glucose, pykF expression did not lead to significant accumulation of overflow metabolites and consumption of the substrate remained unaltered. Increased growth rate on glucose was not accompanied with decreased wax ester production, and the pykF-expressing cells accumulated significantly more of these storage lipids with respect to cultivation time.     

Glucokinase contributes to glucose phosphorylation in d-lactic acid production by Sporolactobacillus inulinus Y2-8

Sporolactobacillus inulinus, a homofermentative lactic acid bacterium, is a species capable of efficient industrial d-lactic acid production from glucose. Glucose phosphorylation is the key step of glucose metabolism, and fine-tuned expression of which can improve d-lactic acid production. During growth on high-concentration glucose, a fast induction of high glucokinase (GLK) activity was observed, and paralleled the patterns of glucose consumption and d-lactic acid accumulation, while phosphoenolpyruvate phosphotransferase system (PTS) activity was completely repressed. The transmembrane proton gradient of 1.3–1.5 units was expected to generate a large proton motive force to the uptake of glucose. This suggests that the GLK pathway is the major route for glucose utilization, with the uptake of glucose through PTS-independent transport systems and phosphorylation of glucose by GLK in S. inulinus d-lactic acid production. The gene encoding GLK was cloned from S. inulinus and expressed in Escherichia coli. The amino acid sequence revealed significant similarity to GLK sequences from Bacillaceae. The recombinant GLK was purified and shown to be a homodimer with a subunit molecular mass of 34.5?kDa. Strikingly, it demonstrated an unusual broad substrate specificity, catalyzing phosphorylation of 2-deoxyglucose, mannitol, maltose, galactose and glucosamine, in addition to glucose. This report documented the key step concerning glucose phosphorylation of S. inulinus, which will help to understand the regulation of glucose metabolism and d-lactic acid production.     

Effects of membrane-bound glucose dehydrogenase overproduction on the respiratory chain of Gluconobacter oxydans

The acetic acid bacterium Gluconobacter oxydans incompletely oxidizes carbon sources as a natural part of its metabolism, and this feature has been exploited for many biotechnological applications. The most important enzymes used to harness the biocatalytic oxidative capacity of G. oxydans are the pyrroloquinoline quinone (PQQ)-dependent dehydrogenases. The membrane-bound PQQ-dependent glucose dehydrogenase (mGDH), encoded by gox0265, was used as model protein for homologous membrane protein production using the previously described Gluconobacter expression vector pBBR1p452. The mgdh gene had ninefold higher expression in the overproduction strain compared to the parental strain. Furthermore, membranes from the overexpression strain had a five- and threefold increase of mGDH activity and oxygen consumption rates, respectively. Oxygen consumption rate of the membrane fraction could not be increased by the addition of a substrate combination of glucose and ethanol in the overproduction strain, indicating that the terminal quinol oxidases of the respiratory chain were rate limiting. In contrast, addition of glucose and ethanol to membranes of the control strain increased oxygen consumption rates approaching the observed rates with G. oxydans overproducing mGDH. The higher glucose oxidation rates of the mGDH overproduction strain corresponded to a 70 % increase of the gluconate production rate compared to the control strain. The high rate of glucose oxidation may be useful in the industrial production of gluconates and ketogluconates, or as whole-cell biosensors. Furthermore, mGDH was purified to homogeneity by one-step strep-tactin affinity chromatography and characterized. To our knowledge, this is the first report of a membrane integral quinoprotein being purified by affinity chromatography and serves as a proof-of-principle for using G. oxydans as a host for membrane protein expression and purification.     

Modelling the growth kinetics of <Emphasis Type="Italic">Kocuria marina</Emphasis> DAGII as a function of single and binary substrate during batch production of β-Cryptoxanthin

In the present investigation, growth kinetics of Kocuria marina DAGII during batch production of β-Cryptoxanthin (β-CRX) was studied by considering the effect of glucose and maltose as a single and binary substrate. The importance of mixed substrate over single substrate has been emphasised in the present study. Different mathematical models namely, the Logistic model for cell growth, the Logistic mass balance equation for substrate consumption and the Luedeking–Piret model for β-CRX production were successfully implemented. Model-based analyses for the single substrate experiments suggested that the concentrations of glucose and maltose higher than 7.5 and 10.0 g/L, respectively, inhibited the growth and β-CRX production by K. marina DAGII. The Han and Levenspiel model and the Luong product inhibition model accurately described the cell growth in glucose and maltose substrate systems with a R ² value of 0.9989 and 0.9998, respectively. The effect of glucose and maltose as binary substrate was further investigated. The binary substrate kinetics was well described using the sum-kinetics with interaction parameters model. The results of production kinetics revealed that the presence of binary substrate in the cultivation medium increased the biomass and β-CRX yield significantly. This study is a first time detailed investigation on kinetic behaviours of K. marina DAGII during β-CRX production. The parameters obtained in the study might be helpful for developing strategies for commercial production of β-CRX by K. marina DAGII.     

Improved n-butanol production by a non-acetone producing Clostridium pasteurianum DSMZ 525 in mixed substrate fermentation

The kinetics of growth, acid and solvent production in batch culture of Clostridium pasteurianum DSMZ 525 were examined in mixed or mono-substrate fermentations. In pH-uncontrolled batch cultures, the addition of butyric acid or glucose significantly enhanced n-butanol production and the ratio of butanol/1,3-propanediol. In pH-controlled batch culture at pH?=?6, butyric acid addition had a negative effect on growth and did not lead to a higher n-butanol productivity. On the other hand, mixed substrate fermentation using glucose and glycerol enhanced the growth and acid production significantly. Glucose limitation in the mixed substrate fermentation led to the reduction or inhibition of the glycerol consumption by the growing bacteria. Therefore, for the optimal growth and n-butanol production by C. pasteurianum, a limitation of either substrate should be avoided. Under optimized batch conditions, n-butanol concentration and maximum productivity achieved were 21 g/L, and 0.96 g/L?×?h, respectively. In comparison, mixed substrate fermentation using biomass hydrolysate and glycerol gave a n-butanol concentration of 17 g/L with a maximum productivity of 1.1 g/L?×?h. In terms of productivity and final n-butanol concentration, the results demonstrated that C. pasteurianum DSMZ 525 is well suitable for n-butanol production from mixed substrates of biomass hydrolysate and glycerol and represents an alternative promising production strain.     

Anaerobic and aerobic energy metabolism in the larvae (tetrathyridia) of Mesocestoides corti

The tetrathyridia of Mesocestoides corti produce lactate, succinate, acetate, and CO₂ as major carbon-containing end products during in vitro incubation with glucose as the substrate. Differences in the rate of glucose consumption and lactate production under anaerobic or aerobic conditions were observed, but their significance could not be determined. However, succinate production was greatly decreased in the presence of oxygen.The relative activities and intracellular distribution of various enzymes involved in energy-supplying metabolism of the larvae appear to conform to the pathways observed in other parasitic helminths known to produce lactate, succinate, and volatile fatty acids as metabolic end products. Some common features found in this respect are the relatively low pyruvate kinase activity, the presence of a highly active cytoplasmic phosphoenolpyruvate carboxylase and the capability of mitochondrial membrane bound fumarate reductase to reduce fumarate by means of NADH. Although a stimulatory effect of fructose-1,6-diphosphate on the reaction velocity of pyruvate kinase occurred, the absolute activity of this enzyme is very low.Nearly all the enzymes required for Krebs cycle activity are available in the tetrathyridia. Under the assay conditions employed by us, only NAD-dependent isocitrate dehydrogenase could not be demonstrated. The small amounts of ¹⁴CO₂ liberated from 6-¹⁴C-glucose suggest that the cycle in its classical form probably only functions at a very low rate. The incorporation of ¹⁴C from labeled glucose into glycogen indicates the presence of enzymes capable of glycogenesis. The incorporation rate was found to be higher in the presence of oxygen than under anaerobic conditions. On account of the very low NAD-linked glycerol-3-phosphate dehydrogenase activity the glycerolphosphate cycle may be of minor importance for the tetrathyridia.As a result of these studies a scheme for the main carbohydrate dissimilating pathways in the tetrathyridia is proposed and the significance of oxygen with respect to energy-supplying metabolism is discussed.     

The role of Hox hydrogenase in the H2 metabolism of Thiocapsa roseopersicina

The purple sulfur phototrophic bacterium Thiocapsa roseopersicina BBS synthesizes at least three NiFe hydrogenases (Hox, Hup, Hyn). We characterized the physiological H₂ consumption/evolution reactions in mutants having deletions of the structural genes of two hydrogenases in various combinations. This made possible the separation of the functionally distinct roles of the three hydrogenases. Data showed that Hox hydrogenase (unlike the Hup and Hyn hydrogenases) catalyzed the dark fermentative H₂ evolution and the light-dependent H₂ production in the presence of thiosulfate. Both Hox⁺ and Hup⁺ mutants demonstrated light-dependent H₂ uptake stimulated by CO₂ but only the Hup⁺ mutant was able to mediate O₂-dependent H₂ consumption in the dark. The ability of the Hox⁺ mutant to evolve or consume hydrogen was found to depend on a number of interplaying factors including both growth and reaction conditions (availability of glucose, sulfur compounds, CO₂, H₂, light). The study of the redox properties of Hox hydrogenase supported the reversibility of its action. Based on the results a scheme is suggested to describe the role of Hox hydrogenase in light-dependent and dark hydrogen metabolism in T. roseopersicina BBS.     

Microcalorimetric Measurements of Glucose Metabolism by Marine Bacterium Vibrio alginolyticus

Microcalorimetric measurements of heat production from glucose by Vibrio alginolyticus were made to assess the viability of calorimetry as a technique for studying the metabolism of marine bacteria at organic nutrient concentrations found in marine waters. The results show that the metabolism of glucose by this bacterium can be measured by calorimetry at submicromolar concentrations. A linear correlation between glucose concentration and total heat production was observed over a concentration range of 8 mM to 0.35 μM. It is suggested that these data indicate a constant efficiency of metabolism for this bacterium over the wide range of glucose concentrations studied.     

Effect of Organic Complex Compounds on Bacillus thermoamylovorans Growth and Glucose Fermentation

The effect of the concentration of a mixture (1/1 [wt/wt]) of yeast extract and bioTrypcase (YE+bT) on the growth and physiology of a new species, Bacillus thermoamylovorans, a moderately thermophilic, non-spore-forming, lactic acid-producing bacterium isolated from palm wine, was studied. At an initial glucose concentration of 100 mM, B. thermoamylovorans growth was limited when the concentration of YE+bT was lower than 5.0 g liter⁻¹; under these conditions, cellular yield reached a maximum value of 0.4 g of cells per g of YE+bT. Growth limitation due to deficiency in growth factors led to a significant shift in glucose metabolism towards lactate production. Lactate constituted 27.5 and 76% of the end products of glucose fermentation in media containing YE+bT at 20.0 and 1.0 g liter⁻¹, respectively. This result markedly differed from published data for lactic bacteria, which indicated that fermentative metabolism remained homolactic regardless of the concentration of YE. Our results showed that the ratio between cellular synthesis and energy production increased with the concentration of YE+bT in the culture medium. They indicate that the industrial production of lactic acid through glucose fermentation by B. thermoamylovorans can be optimized by using a medium where glucose is present in excess and the organic additives are limiting.     

Mutational Analyses of Glucose Dehydrogenase and Glucose-6-Phosphate Dehydrogenase Genes in Pseudomonas fluorescens Reveal Their Effects on Growth and Alginate Production

The biosynthesis of alginate has been studied extensively due to the importance of this polymer in medicine and industry. Alginate is synthesized from fructose-6-phosphate and thus competes with the central carbon metabolism for this metabolite. The alginate-producing bacterium Pseudomonas fluorescens relies on the Entner-Doudoroff and pentose phosphate pathways for glucose metabolism, and these pathways are also important for the metabolism of fructose and glycerol. In the present study, the impact of key carbohydrate metabolism enzymes on growth and alginate synthesis was investigated in P. fluorescens. Mutants defective in glucose-6-phosphate dehydrogenase isoenzymes (Zwf-1 and Zwf-2) or glucose dehydrogenase (Gcd) were evaluated using media containing glucose, fructose, or glycerol. Zwf-1 was shown to be the most important glucose-6-phosphate dehydrogenase for catabolism. Both Zwf enzymes preferred NADP as a coenzyme, although NAD was also accepted. Only Zwf-2 was active in the presence of 3 mM ATP, and then only with NADP as a coenzyme, indicating an anabolic role for this isoenzyme. Disruption of zwf-1 resulted in increased alginate production when glycerol was used as the carbon source, possibly due to decreased flux through the Entner-Doudoroff pathway rendering more fructose-6-phosphate available for alginate biosynthesis. In alginate-producing cells grown on glucose, disruption of gcd increased both cell numbers and alginate production levels, while this mutation had no positive effect on growth in a non-alginate-producing strain. A possible explanation is that alginate synthesis might function as a sink for surplus hexose phosphates that could otherwise be detrimental to the cell.     

Metabolic changes in a pyruvate kinase gene deletion mutant of Corynebacterium glutamicum ATCC 13032

To investigate primary effects of a pyruvate kinase (PYK) defect on glucose metabolism in Corynebacterium glutamicum, a pyk-deleted mutant was derived from wild-type C. glutamicum ATCC13032 using the double-crossover chromosome replacement technique. The mutant was then evaluated under glutamic acid-producing conditions induced by biotin limitation. The mutant showed an increased specific rate of glucose consumption, decreased growth, higher glutamic acid production, and aspartic acid formation during the glutamic acid production phase. A significant increase in phosphoenolpyruvate (PEP) carboxylase activity and a significant decrease in PEP carboxykinase activity occurred in the mutant, which suggested an enhanced overall flux of the anaplerotic pathway from PEP to oxaloacetic acid in the mutant. The enhanced anaplerotic flux may explain both the increased rate of glucose consumption and the higher productivity of glutamic acid in the mutant. Since the pyk-complemented strain had similar metabolic profiles to the wild-type strain, the observed changes represented intrinsic effects of pyk deletion on the physiology of C. glutamicum.     

Effect of glucose concentration on the rate of fructose consumption in native strains isolated from the fermentation of Agave duranguensis

Studies on hexose consumption by Saccharomyces cerevisiae show that glucose is consumed faster than fructose when both are present (9:1 fructose to glucose) in the medium during the fermentation of Agave. The objective of this work was to select strains of S. cerevisiae that consume fructose equal to or faster than glucose at high fructose concentrations by analyzing the influence of different glucose concentrations on the fructose consumption rate. The optimal growth conditions were determined by a kinetics assay using high performance liquid chromatography (HPLC) using 50?g of glucose and 50?g of fructose per liter of synthetic medium containing peptone and yeast extract. Using the same substrate concentrations, strain ITD-00185 was shown to have a higher reaction rate for fructose over glucose. At 75?g of fructose and 25?g of glucose per liter, strain ITD-00185 had a productivity of 1.02 gL^?1?h^?1 after 40?h and a fructose rate constant of 0.071?h^?1. It was observed that glucose concentration positively influences fructose consumption when present in a 3:1 ratio of fructose to glucose. Therefore, adapted strains at high fructose concentrations could be used as an alternative to traditional fermentation processes.     

Environmental and Nutritional Factors That Affect Growth and Metabolism of the Pneumococcal Serotype 2 Strain D39 and Its Nonencapsulated Derivative Strain R6

Links between carbohydrate metabolism and virulence in Streptococcus pneumoniae have been recurrently established. To investigate these links further we developed a chemically defined medium (CDM) and standardized growth conditions that allowed for high growth yields of the related pneumococcal strains D39 and R6. The utilization of the defined medium enabled the evaluation of different environmental and nutritional factors on growth and fermentation patterns under controlled conditions of pH, temperature and gas atmosphere. The same growth conditions impacted differently on the nonencapsulated R6, and its encapsulated progenitor D39. A semi-aerobic atmosphere and a raised concentration of uracil, a fundamental component of the D39 capsule, improved considerably D39 growth rate and biomass. In contrast, in strain R6, the growth rate was enhanced by strictly anaerobic conditions and uracil had no effect on biomass. In the presence of oxygen, the difference in the growth rates was mainly attributed to a lower activity of pyruvate oxidase in strain D39. Our data indicate an intricate connection between capsule production in strain D39 and uracil availability. In this study, we have also successfully applied the in vivo NMR technique to study sugar metabolism in S. pneumoniae R6. Glucose consumption, end-products formation and evolution of intracellular metabolite pools were monitored online by ¹³C-NMR. Additionally, the pools of NTP and inorganic phosphate were followed by ³¹P-NMR after a pulse of glucose. These results represent the first metabolic profiling data obtained non-invasively for S. pneumoniae, and pave the way to a better understanding of regulation of central metabolism.     

A Study on the Fundamental Mechanism and the Evolutionary Driving Forces behind Aerobic Fermentation in Yeast

Baker’s yeast Saccharomyces cerevisiae rapidly converts sugars to ethanol and carbon dioxide at both anaerobic and aerobic conditions. The later phenomenon is called Crabtree effect and has been described in two forms, long-term and short-term effect. We have previously studied under fully controlled aerobic conditions forty yeast species for their central carbon metabolism and the presence of long-term Crabtree effect. We have also studied ten steady-state yeast cultures, pulsed them with glucose, and followed the central carbon metabolism and the appearance of ethanol at dynamic conditions. In this paper we analyzed those wet laboratory data to elucidate possible mechanisms that determine the fate of glucose in different yeast species that cover approximately 250 million years of evolutionary history. We determine overflow metabolism to be the fundamental mechanism behind both long- and short-term Crabtree effect, which originated approximately 125–150 million years ago in the Saccharomyces lineage. The “invention” of overflow metabolism was the first step in the evolution of aerobic fermentation in yeast. It provides a general strategy to increase energy production rates, which we show is positively correlated to growth. The “invention” of overflow has also simultaneously enabled rapid glucose consumption in yeast, which is a trait that could have been selected for, to “starve” competitors in nature. We also show that glucose repression of respiration is confined mainly among S. cerevisiae and closely related species that diverged after the whole genome duplication event, less than 100 million years ago. Thus, glucose repression of respiration was apparently “invented” as a second step to further increase overflow and ethanol production, to inhibit growth of other microbes. The driving force behind the initial evolutionary steps was most likely competition with other microbes to faster consume and convert sugar into biomass, in niches that were semi-anaerobic.     

The final acylation step in aromatic dithiolopyrrolone biosyntheses: Identification and characterization of the first bacterium N-benzoyltransferase from Saccharothrix algeriensis NRRL B-24137

The last step in the biosynthesis of dithiolopyrrolone antibiotics was thought to involve the transfer of acyl group from acyl-CoA to pyrrothine/holothin core. In Saccharothrix algeriensis NRRL B-24137, two acyltransferases, an acetyltransferase and a benzoyltransferase were proposed to catalyze this step. We have previously identified, in Sa. algeriensis genome, two open read frames, actA and actB patiently encoded these enzymes. This study focuses primarily on the characterization of the protein encoded by actA. After cloning and expressing of actA in Escherichia coli BL21, the recombinant protein encoded by actA was purified. Selectivity of ActA for pyrrothine/holothin as substrate and different acyl-CoA as co-substrate was evaluated using two acyls-groups, linear and aromatic. The enzyme was shown to prefer aromatic groups over linear groups as donor group; further neither product nor transfer was observed for linear groups. Therefore ActA has been determined to be a pyrrothine/holothin N-benzoyltransferase which can either pyrrothine (K_m of 72 μM) or holothin (K_m of 129.5 μM) as substrates and benzoyl-CoA (K_m of 348.65 and 395.28 μM) as co-substrates for pyrrothine and holothin, respectively. The optimum pH and temperature has been shown to be 8, 40 °C, respectively. ActA is the first enzyme characterized as N-benzoyltransferase in bacteria.     

Mathematical model for aerobic culture of a recombinant yeast

A mathematical model was formulated to simulate cell growth, plasmid loss and recombinant protein production during the aerobic culture of a recombinant yeast S. cerevisiae. Model development was based on three simplified metabolic events in the yeast: glucose fermentation, glucose oxidation and ethanol oxidation. Cell growth was expressed as a composite of these metabolic events. Their contributions to the total specific growth rate depended on the activities of the pacemaker enzyme pools of the individual pathways. The pacemaker enzyme pools were regulated by the specific glucose uptake rate. The effect of substrate concentrations on the specific growth rate was described by a modified Monod equation. It was assumed that recombinant protein formation is only associated with oxidative pathways. Plasmid loss kinetics was formulated based on segregational instability during cell division by assuming constant probability of plasmid loss. Experiments on batch fermentation of recombinant S. cerevisiae C468/pGAC9 (ATCC 20690), which expresses Aspergillus awamori glucoamylase gene and secretes glucoamylase into the extracellular medium, were carried out in an airlift bioreactor in order to evaluate the proposed model. The model successfully predicted the dynamics of cell growth, glucose consumption, ethanol metabolism, glucoamylase production and plasmid instability. Excellent agreement between model simulations and our experimental data was achieved. Using published experimental data, model agreement was also found for other recombinant yeast strains. In general, the proposed model appears to be useful for the design, scale-up, control and optimization of recombinant yeast bioprocesses.     

Modeling alcoholic fermentation of glucose/xylose mixtures by ethanologenic Escherichia coli as a function of pH

In order to understand the effect of pH on growth and ethanol production in ethanologenic Escherichia coli, we investigated the kinetic behavior of ethanologenic E. coli during alcoholic fermentation of glucose or xylose in a controlled pH environment and the fermentation of glucose, xylose, or their mixtures without pH control. Based on the Monod equation, an unstructured and unsegregated kinetic model was proposed as a function of the pH of the fermentation medium. The pH effects on cell growth, sugar consumption, and ethanol production were taken into account in the proposed model. Both cell growth and ethanol production were found to be significantly influenced by the pH of the fermentation medium. The optimal pH range for ethanol production by ethanologenic E. coli on either glucose or xylose was 6.0–6.5. The highest value of the maximum specific growth rate (μ _m) was obtained at pH 7.0. In the kinetic model of the fermentations of the sugar mixture, two inhibition terms related to glucose concentrations were included in both the cell growth and ethanol production equations because of the strong inhibitions of glucose and glucose metabolites on xylose metabolism. A good fit was found between model predictions and experimental data for both single-sugar and mixed-sugar fermentations without pH control within the experimental domain.