Batch- and Continuous-Culture Transients for Two Substrate Systems

Batch growth of Escherichia coli in the presence of equal initial concentrations of glucose and a secondary substrate (xylose) is characterized by sequential utilization of the substrates, whereas continuous-culture systems with equal concentrations of the two substrates in the feed are characterized by complete utilization of both substrates at both high and low dilution rates. Such systems at steady state at a low dilution rate, when suddenly shifted to a higher dilution rate, experience a transient drop in population density accompanied by accumulation of the secondary substrate but virtually no accumulation of glucose. Systems at steady state with 200 mg of glucose per liter were found to undergo a transient population decrease and eventual recovery when switched to feed containing 200 mg of a secondary substrate per liter.     

Carbohydrate utilization patterns and substrate preferences in Bacteroides thetaiotaomicron

Specific growth rates of Bacteroides thetaiotaomicron NCTC 10582 with either glucose, arabinose, mannose, galactose or xylose as sole carbon sources were 0.42/h, 0.10/h, 0.38/h, 0.38/h and 0.16/h respectively, suggesting that hexose metabolism was energetically more efficient than pentose fermentation in this bacterium. Batch culture experiments to determine whether carbohydrate utilization was controlled by substrate-induced regulatory mechanisms demonstrated that mannose inhibited uptake of glucose, galactose and arabinose, but had less effect on xylose. Arabinose and xylose were preferentially utilized at high dilution rates (D > 0.26/h) in carbon-limited continuous cultures grown on mixtures of arabinose, xylose, galactose and glucose. When mannose was also present, xylose was co-assimilated at all dilution rates. Under nitrogen-limited conditions, however, mannose repressed uptake of all sugars, showing that its effect on xylose utilization was strongly concentration dependent. Studies with individual D-ZU-14C]-labelled substrates showed that transport systems for glucose, galactose, xylose and mannose were inducible. Measurements to determine incorporation of these sugars into trichloroacetic acid-precipitable material indicated that glucose and mannose were the principal precursor monosaccharides. Xylose was only incorporated into intracellular macromolecules when it served as growth substrate. Phosphoenolpyruvate:phosphotransferase systems were not detected in preliminary experiments to elucidate the mechanisms of sugar uptake, and studies with inhibitors of carbohydrate transport showed no consistent pattern of inhibition with glucose, galactose, xylose and mannose. These results indicate the existence of a variety of different systems involved in sugar transport in B. thetaiotaomicron.     

Evidence for catabolite inhibition in regulation of pentose utilization and transport in the ruminal bacterium Selenomonas ruminantium.

Pentose sugars can be an important energy source for ruminal bacteria, but there has been relatively little study regarding the regulation of pentose utilization and transport by these organisms. Selenomonas ruminantium, a prevalent ruminal bacterium, actively metabolizes xylose and arabinose. When strain D was incubated with a combination of glucose and xylose or arabinose, the hexose was preferentially utilized over pentoses, and similar preferences were observed for sucrose and maltose. However, there was simultaneous utilization of cellobiose and pentoses. Continuous-culture studies indicated that at a low dilution rate (0.10 h-1) the organism was able to co-utilize glucose and xylose. This co-utilization was associated with growth rate-dependent decreases in glucose phosphotransferase activity, and it appeared that inhibition of pentose utilization was due to catabolite inhibition by the glucose phosphotransferase transport system. Xylose transport activity in strain D required induction, while arabinose permease synthesis did not require inducer but was subject to repression by glucose. Since an electrical potential or a chemical gradient of protons drove xylose and arabinose uptake, pentose-proton symport systems apparently contributed to transport.     

Cultivation of hybridoma cells in continuous cultures: kinetics of growth and product formation

Mouse hybridoma cells were grown in suspension in continuous stirred bioreactors. Cell growth, substrate utilization, and monoclonal antibody (MAb) production were studied using serum-free medium. Steady-state data were obtained at different dilution rates, between 0.012 and 0.039 h(-1) Viability was profoundly affected by dilution rate, particularly near the lower end of the dilution-rate range investigated. MAb concentration and productivity went through a maximum with respect to dilution rate. Lactate yield on glucose declined with in creasing dilution rate. Experiments were carried out to study the effects of medium glucose concentration on cell growth, product formation, and lactate yield on glucose. Reduction of glucose concentration in the feed medium did not considerably affect cell density and MAb concentration in the culture, but lactate levels dropped sharply; lactate yield on glucose declined substantially, indicating alterations in cell metabolic path ways for energy metabolism. Optimization strategy for continuous cell culture is discussed.     

Kinetic modeling of <Emphasis Type="Italic">Moorella thermoacetica</Emphasis> growth on single and dual-substrate systems

Acetic acid is an important chemical raw material that can be produced directly from sugars in lignocellulosic biomass. Development of kinetic models that capture the bioconversion dynamics of multiple sugar systems will be critical to optimization and process control in future lignocellulosic biorefinery processes. In this work, a kinetic model was developed for the single- and dual-substrate conversion of xylose and glucose to acetic acid using the acetogen Moorella thermoacetica. Batch fermentations were performed experimentally at 20 g L^?1 total sugar concentration using synthetic glucose, xylose, and a mixture of glucose and xylose at a 1:1 ratio. The product yield, calculated as total product formed divided by total sugars consumed, was 79.2, 69.9, and 69.7 % for conversion of glucose, xylose, and a mixture of glucose and xylose (1:1 ratio), respectively. During dual-substrate fermentation, M. thermoacetica demonstrated diauxic growth where xylose (the preferred substrate) was almost entirely consumed before consumption of glucose began. Kinetic parameters were similar for the single-substrate fermentations, and a strong linear correlation was determined between the maximum specific growth rate μ _max and substrate inhibition constant, K _s . Parameters estimated for the dual-substrate system demonstrated changes in the specific growth rate of both xylose and glucose consumption. In particular, the maximum growth rate related to glucose tripled compared to the single-substrate system. Kinetic growth is affected when multiple substrates are present in a fermentation system, and models should be developed to reflect these features.     

Cell growth and extracellular enzyme synthesis in fermentations

The synthesis of extracellular enzymes by microorganisms frequently occurs under genetic control. A simple two-parameter model is developed describing the degree of repression or induction in fermentation media. The case of substrate utilization by an extracellular enzyme was analyzed for a vegetable oil-lipase-yeast system. It is shown that fatty acids released by the lipase may accumulate in the early stage of growth and exert an influence on the limiting after which relatively little repression or induction takes place. Expressions are also derived for growth and extracellular enzyme synthesis in single-and multistage continuous cultures. When the cells grow on a directly available soluble substrate, the specific enzyme synthesis is maximal at low dilution rates in the case of repression and at high dilution rates in the case of induction. If the substrate is not directly available, a single continuous stirred tank reactor stage may not be sufficient for efficient substrate utilization; for fermentation processes where an insoluble has to be broken down before the cells can assimilate it, a plug flow type fermentor rather than a mixed chemostat may prove more satisfactory.     

Growth of the thermophilic bacterium Clostridium thermocellum in continuous culture

Clostridium thermocellum is an anaerobic thermophilic bacterium that produces enthanol from cellulosic substrates. When the organism was grown in continuous culture at dilution rates ranging from 0.04 to 0.25 h^-1, growth yields on cellobiose were higher than on glucose, and even higher yields were observed on cellotetraose. However, differences in bacterial yield were much greater at slow growth rates, and it appeared that glucose-grown cells had a fourfold higher (0.41 g substrate/g protein/h) maintenance energy requirement than cellobiose-grown cultures. Cellobiose and glucose were co-utilized in dual substrate continuous culture, and this was in contrast to batch culture experiments which indicated that the organism preferred the disaccharide. These experiments demonstrate that carbohydrate utilization patterns in continuous culture are different from those in batch culture and that submaximal growth rates affect substrate preference and bioenergetic parameters. The mechanisms regulating carbohydrate use may be different in batch versus continuous culture.Published with the approval of the Director of the Kentucky Agricultural Experiment Station as journal article no. 95-07-064.     

Absence of diauxie during simultaneous utilization of glucose and Xylose by Sulfolobus acidocaldarius

Sulfolobus acidocaldarius utilizes glucose and xylose as sole carbon sources, but its ability to metabolize these sugars simultaneously is not known. We report the absence of diauxie during growth of S. acidocaldarius on glucose and xylose as co-carbon sources. The presence of glucose did not repress xylose utilization. The organism utilized a mixture of 1 g/liter of each sugar simultaneously with a specific growth rate of 0.079 h(-1) and showed no preference for the order in which it utilized each sugar. The organism grew faster on 2 g/liter xylose (0.074 h(-1)) as the sole carbon source than on an equal amount of glucose (0.022 h(-1)). When grown on a mixture of the two carbon sources, the growth rate of the organism increased from 0.052 h(-1) to 0.085 h(-1) as the ratio of xylose to glucose increased from 0.25 to 4. S. acidocaldarius appeared to utilize a mixture of glucose and xylose at a rate roughly proportional to their concentrations in the medium, resulting in complete utilization of both sugars at about the same time. Gene expression in cells grown on xylose alone was very similar to that in cells grown on a mixture of xylose and glucose and substantially different from that in cells grown on glucose alone. The mechanism by which the organism utilized a mixture of sugars has yet to be elucidated.     

Complete genome sequence,metabolic model construction and phenotypic characterization of Geobacillus LC300, an extremely thermophilic,fast growing,xylose-utilizing bacterium

We have isolated a new extremely thermophilic fast-growing Geobacillus strain that can efficiently utilize xylose, glucose, mannose and galactose for cell growth. When grown aerobically at 72 °C, Geobacillus LC300 has a growth rate of 2.15 h⁻¹ on glucose and 1.52 h⁻¹ on xylose (doubling time less than 30 min). The corresponding specific glucose and xylose utilization rates are 5.55 g/g/h and 5.24 g/g/h, respectively. As such, Geobacillus LC300 grows 3-times faster than E. coli on glucose and xylose, and has a specific xylose utilization rate that is 3-times higher than the best metabolically engineered organism to date. To gain more insight into the metabolism of Geobacillus LC300 its genome was sequenced using PacBio׳s RS II single-molecule real-time (SMRT) sequencing platform and annotated using the RAST server. Based on the genome annotation and the measured biomass composition a core metabolic network model was constructed. To further demonstrate the biotechnological potential of this organism, Geobacillus LC300 was grown to high cell-densities in a fed-batch culture, where cells maintained a high xylose utilization rate under low dissolved oxygen concentrations. All of these characteristics make Geobacillus LC300 an attractive host for future metabolic engineering and biotechnology applications.     

Plasmid stability and alpha-amylase production in batch and continuous cultures of Bacillus subtilis TN106[pAT5

Cell growth and enzyme (alpha-amylase) production characteristics of Bacillus subtilis TN106 containing the recombinant plasmid pAT5 are investigated in batch and continuous cultures using a defined medium with glucose as the limiting nutrient. The batch culture studies demonstrate that the recombinant plasmid, reported earlier(1) to be stably maintained in the host, suffers from segregational and structural instabilities. The structural instability of this strain occurred during culture storage and can be eliminated in bioreactor experiments by using a modified inoculum preparation procedure. Such elimination allows an unbiased investigation of segregational instability via continuous culture studies. Such studies conducted with this fast growing microorganism, in the absence of antibiotic selection pressure, indicate a very efficient glucose utilization (very low residual glucose concentrations) over a wide range of dilution rates (0.16 h(-1) - 0.94 h(-1)). The nearly time-invariant and low residual glucose concentrations at each such dilution rate enable convenient estimation of growth parameters of the host and recombinant cells and frequency of segregational instability from transients in the resulting mixed cultures. The specific alpha-amylase activity exhibits an inverse relationship to the specific growth rate of recombinant cells. The growth of recombinant cells is not affected by the presence of antibiotic (kanamycin). The growth advantage of host cells over recombinant cells diminishes with increasing dilution rate.     

Kinetic and nuclear magnetic resonance studies of xylose metabolism by recombinant Zymomonas mobilis ZM4(pZB5)

The specific rates of growth, substrate utilization, and ethanol production as well as yields of biomass and ethanol production on xylose for the recombinant Zymomonas mobilis ZM4(pZB5) were shown to be much less than those on glucose or glucose-xylose mixtures. Typical fermentations with ZM4(pZB5) growing on glucose-xylose mixtures followed two-phase growth kinetics with the initial uptakes of glucose and xylose being followed by slower growth and metabolic uncoupling on xylose after glucose depletion. The reductions in rates and yields from xylose metabolism were considered in the present investigation and may be due to a number of factors, including the following: (i) the increased metabolic burden from maintenance of plasmid-related functions, (ii) the production of by-products identified as xylitol, acetate, lactate, acetoin, and dihydroxyacetone by (13)C-nuclear magnetic resonance (NMR) spectroscopy and high-performance liquid chromatography, (iii) growth inhibition due to xylitol by the putative inhibitory compound xylitol phosphate, and (iv) the less energized state of ZM4(pZB5). In vivo (31)P-NMR studies have established that the levels of NTP and UDP sugars on xylose were less than those on glucose, and this energy limitation is likely to restrict the growth of the recombinant strain on xylose media.     

The regulatory effects of growth rate and cyclic AMP levels on carbon catabolism and respiration in Escherichia coli K-12.

Cyclic AMP levels in glucose and succinate-limited and ammonia-limited glucose-containing continuous cultures of Escherichia coli were measured at different bacterial growth rates. Intracellular cyclic AMP concentrations were fairly constant (about 5 micrometer) at all dilution rates used when glucose was limiting. In ammonia-limited glucose cultures the cyclic AMP content was much lower (about 0.3 micrometer). In succinate-limited cultures cyclic AMP levels fell from 2.7 to 0.8 micrometer as dilution rate increased from 0.05 to 0.4 h-1. The effects of cyclic AMP on respiratory and carbon catabolic enzyme levels were studied. There was no indication of a direct cyclic AMP involvement in the regulation of these cellular functions. It seems more likely that the variations in enzyme levels observed resulted from variation of the specific growth rate of cultures.     

Mixed Continuous Cultures of Polyvinyl Alcohol-Utilizing Symbionts Pseudomonas putida VM15A and Pseudomonas sp. Strain VM15C

Stable mixed continuous cultures of Pseudomonas sp. strain VM15C and Pseudomonas putida VM15A, the former of which produced a polyvinyl alcohol (PVA)-degrading enzyme and the latter of which produced an essential growth factor for PVA utilization by strain VM15C, were established with PVA as the sole source of carbon and energy with chemostat cultivation. A high extent of PVA degradation was achieved at dilution rates of less than 0.030/h. The predominant strain in the cultures was the primary metabolizer of PVA, strain VM15C. The growth supporter, strain VM15A, existed as a minor population, although its population was maintained at an almost constant level throughout a dilution region in which the VM15C population decreased markedly as the dilution rate was raised. A crude growth factor which was prepared from a culture supernatant of strain VM15A and increased the specific growth rate of strain VM15C with PVA in an axenic batch culture was also effective for enhancing the VM15C population and PVA degradation in the mixed continuous culture at a high dilution rate (0.064/h). This indicated that the growth-limiting substrate for strain VM15C in the mixed continuous culture is the growth factor produced by strain VM15A.     

The acetone butanol fermentation on glucose and xylose. II. Regulation and kinetics in fed-batch cultures

The kinetics in fed-batch cultures of acetone butanol fermentation by Clostridium acetobutylicum is compared on glucose, xylose, and mixtures of both sugars. The final conversion yield of sugars into solvents always increases with the sugar feeding rate. At low feeding rates, the sugar concentration in the medium becomes limiting, which results in a slower cellular growth, a slower metabolic transition from an acid to a solvent fermentation and, thus, a higher accumulation of acids. It is only at sufficiently high feeding rates that fed-batch fermentations yield kinetic results comparable to those of batch fermentations. With mixtures of glucose and xylose, because of a maintained low glucose level, both sugars are taken up at the same rate during a first fermentation period. An earlier accumulation of xylose when the fermentation becomes inhibited suggest that xylose utilization is inhibited when the catabolic flux of glucose alone can satisfy the metabolic activity of the cell. Kinetic results with batch and fed-batch fermentations indicate several important features of the regulation of C. acetobutylicum metabolism: an early inhibition by the produced acids; an initiation of solvent formation between 4 and 6 g/L acetic and butyric acid depending on the metabolic activity of the cell; a metabolic transition from acids to solvents production at a rate closely related to the rate of sugar uptake; during solvent production, a reassimilation of acids above a minimal rate of sugar consumption of 0.2 h(-1); a final inhibition of the fermentation at a total butanol and acids concentration of ca. 20 g/L.     

Growth dynamics of a methylotroph (Methylomonas L3) in continuous cultures. I. Fast transients induced by methanol pulses and methanol accumulation

The dynamic behavior of the Ribulose Monophosphate-type Methylomonas L3 in continuous cultures was studied, using methanol pulses to induce fast transients in steady-state cultures of single (methanol) and mixed (methanol plus formaldehyde) substrates. In several experiments, the methanol-uptake rate (MUR) profiles displayed negative MUR values for a time period following the methanol pulse, and significant amounts of methanol disappeared immediately following the pulse. These phenomena suggested the accumulation of methanol in the cells upon pulsing, apparently due to an active transport system. Accordingly, and in order to estimate the potential of the transport system for methanol accumulation, accumulation profiles were calculated for several pulse experiments. The calculations are based on a methanol balance and experimentally determined values of the cell volume and the true transient biomass yields. It is calculated that methanol accumulates up to 200-fold to very high intracellular concentrations. The accumulation is calculated to be much higher in single- (methanol) substrate cultures of low dilution rate than in cultures of high dilution rate or of mixed substrates. The specific growth rate immediately following the methanol pulse decreased in single-substrate cultures and increased in mixed-substrate ones. The biomass yield decreased after the methanol addition in all experiments; however, the drop was less severe in the mixed-substrate experiments. It is also suggested that formaldehyde as a methanol cosubstrate may be an effective means of providing more stable biomass yields and growth rates in reactors with imperfect mixing, and of protecting the reactor against accidentally induced methanol accumulation.     

酿酒酵母木糖发酵酒精途径工程的研究进展

途径工程(Pathway engineering),被称为第三代基因工程,改变代谢流向,开辟新的代谢途径是途径工程的主要目的。利用途径工程理念,对酿酒酵母（Saccharomyces cerevisiae）代谢途径进行理性设计,以拓展这一传统酒精生产菌的底物范围,使其充分利用可再生纤维质水解物中的各种糖分,是酿酒酵母酒精途径工程的研究热点之一。这里介绍了近年来酿酒酵母以木糖为底物的酒精途径工程的研究进展。     

Kinetic and Nuclear Magnetic Resonance Studies of Xylose Metabolism by Recombinant Zymomonas mobilis ZM4(pZB5)

The specific rates of growth, substrate utilization, and ethanol production as well as yields of biomass and ethanol production on xylose for the recombinant Zymomonas mobilis ZM4(pZB5) were shown to be much less than those on glucose or glucose-xylose mixtures. Typical fermentations with ZM4(pZB5) growing on glucose-xylose mixtures followed two-phase growth kinetics with the initial uptakes of glucose and xylose being followed by slower growth and metabolic uncoupling on xylose after glucose depletion. The reductions in rates and yields from xylose metabolism were considered in the present investigation and may be due to a number of factors, including the following: (i) the increased metabolic burden from maintenance of plasmid-related functions, (ii) the production of by-products identified as xylitol, acetate, lactate, acetoin, and dihydroxyacetone by ¹³C-nuclear magnetic resonance (NMR) spectroscopy and high-performance liquid chromatography, (iii) growth inhibition due to xylitol by the putative inhibitory compound xylitol phosphate, and (iv) the less energized state of ZM4(pZB5). In vivo ³¹P-NMR studies have established that the levels of NTP and UDP sugars on xylose were less than those on glucose, and this energy limitation is likely to restrict the growth of the recombinant strain on xylose media.