Role of betaine:CoA ligase (CaiC) in the activation of betaines and the transfer of coenzyme A in Escherichia coli

Aims:  Characterization of the role of CaiC in the biotransformation of trimethylammonium compounds into l (−)-carnitine in Escherichia coli .
Methods and Results:  The caiC gene was cloned and overexpressed in E. coli and its effect on the production of l (−)-carnitine was analysed. Betaine:CoA ligase and CoA transferase activities were analysed in cell free extracts and products were studied by electrospray mass spectrometry (ESI-MS). Substrate specificity of the caiC gene product was high, reflecting the high specialization of the carnitine pathway. Although CoA-transferase activity was also detected in vitro , the main in vivo role of CaiC was found to be the synthesis of betainyl-CoAs. Overexpression of CaiC allowed the biotransformation of crotonobetaine to l (−)-carnitine to be enhanced nearly 20-fold, the yield reaching up to 30% (with growing cells). Higher yields were obtained using resting cells (up to 60%), even when d (+)-carnitine was used as substrate.
Conclusions:  The expression of CaiC is a control step in the biotransformation of trimethylammonium compounds in E. coli .
Significance and Impact of the Study:  A bacterial betaine:CoA ligase has been characterized for the first time, underlining its important role for the production of l -carnitine with Escherichia coli .     

Role of energetic coenzyme pools in the production of L-carnitine by Escherichia coli

The aim of this work was to understand the steps controlling the biotransformation of trimethylammonium compounds into L(-)-carnitine by Escherichia coli. The high-cell density reactor steady-state levels of carbon source (glycerol), biotransformation substrate (crotonobetaine), acetate (anaerobiosis product) and fumarate (as an electron acceptor) were pulsed by increasing them fivefold. Following the pulse, the evolution of the enzyme activities involved in the biotransformation process of crotonobetaine into L(-)-carnitine (crotonobetaine hydration), in the synthesis of acetyl-CoA (ACS: acetyl-CoA synthetase and PTA: ATP: acetate phosphotransferase) and in the distribution of metabolites for the tricarboxylic acid (ICDH: isocitrate dehydrogenase) and glyoxylate (ICL: isocitrate lyase) cycles was monitored. In addition, the levels of carnitine, the cell ATP content and the NADH/NAD(+) ratio were measured in order to assess the importance and participation of these energetic coenzymes in the catabolic system. The results provided an experimental demonstration of the important role of the glyoxylate shunt during biotransformation and the need for high levels of ATP to maintain metabolite transport and biotransformation. Moreover, the results obtained for the NADH/NAD(+) pool indicated that it is correlated with the biotransformation process at the NAD(+) regeneration and ATP production level in anaerobiosis. More importantly, a linear correlation between the NADH/NAD(+) ratio and the levels of the ICDH and ICL (carbon and electron flows) and the PTA and ACS (acetate and ATP production and acetyl-CoA synthesis) activity levels was assessed. The main metabolic pathway operating during cell metabolic perturbation with a pulse of glycerol and acetate in the high-cell density membrane reactor was that related to ICDH and ICL, both regulating the carbon metabolism, together with PTA and ACS enzymes (regulating ATP production).     

Link between primary and secondary metabolism in the biotransformation of trimethylammonium compounds by escherichia coli

The aim of this work was to understand the steps controlling the process of biotransformation of trimethylamonium compounds into L(-)-carnitine by Escherichia coli and the link between the central carbon or primary and the secondary metabolism expressed. Thus, the enzyme activities involved in the biotransformation process of crotonobetaine into L(-)-carnitine (crotonobetaine hydration reaction and crotonobetaine reduction reaction), in the synthesis of acetyl-CoA (pyruvate dehydrogenase, acetyl-CoA synthetase, and ATP:acetate phosphotransferase) and in the distribution of metabolites for the tricarboxylic acid (isocitrate dehydrogenase) and glyoxylate (isocitrate lyase) cycles, were followed in batch with both growing and resting cells and during continuous cell growth in stirred-tank and high-cell-density membrane reactors. In addition, the levels of carnitine, crotonobetaine, gamma-butyrobetaine, ATP, NADH/NAD(+), and acetyl-CoA/CoA ratios were measured to determine how metabolic fluxes were distributed in the catabolic system. The results provide the first experimental evidence demonstrating the important role of the glyoxylate shunt during biotransformation of resting cells and the need for high levels of ATP to maintain metabolite transport and biotransformation (2.1 to 16.0 mmol L cellular/mmol ATP L reactor h). Moreover, the results obtained for the pool of acetyl-CoA/CoA indicate that it also correlated with the biotransformation process. The main metabolic pathway operating during cell growth in the high cell-density membrane reactor was that related to isocitrate dehydrogenase (during start-up) and isocitrate lyase (during steady-state operation), together with phosphotransacetylase and acetyl-CoA synthetase. More importantly, the link between central carbon and L(-)-carnitine metabolism at the level of the ATP pool was also confirmed.     

Catabolite repression of tryptophanase in Escherichia coli

Catabolite repression of tryptophanase was studied in detail under various conditions in several strains of Escherichia coli and was compared with catabolite repression of beta-glactosidase. Induction of tryptophanase and beta-galactosidase in cultures grown with various carbon sources including succinate, glycerol, pyruvate, glucose, gluconate, and arabinose is affected differently by the various carbon sources. The extent of induction does not seem to be related to the growth rate of the culture permitted by the carbon source during the course of the experiment. In cultures grown with glycerol as carbon source, preinduced for beta-galactosidase or tryptophanase and made permeable by ethylenediaminetetraacetic acid (EDTA) treatment, catabolite repression of tryptophanase was not affected markedly by the addition of cAMP (3',5'-cyclic adenosine monophosphate). Catabolite repression by glucose was only partially relieved by the addition of cAMP. In contrast, under the same conditions, cAMP completely relieved catabolite repression of beta-galactosidase by either pyruvate or glucose. Under conditions of limited oxygen, induction of tryptophanase is sensitive to catabolite repression; under the same conditions, beta-galactosidase induction is not sensitive to catabolite repression. Induction of tryptophanase in cells grown with succinate as carbon source is sensitive to catabolite repression by glycerol and pyruvate as well as by glucose. Studies with a glycerol kinaseless mutant indicate that glycerol must be metabolized before it can cause catabolite repression. The EDTA treatment used to make the cells permeable to cAMP was found to affect subsequent growth and induction of either beta-galactosidase or tryptophanase much more adversely in E. coli strain BB than in E. coli strain K-12. Inducation of tryptophanase was reduced by the EDTA treatment significantly more than induction of beta-galactosidase in both strains. Addition of 2.5 x 10(-3)m cAMP appeared partially to reverse the inhibitory effect of the EDTA treatment on enzyme induction but did not restore normal growth.     

A metabolic model of cellular energetics and carbon flux during aerobic Escherichia coli fermentation

An integrated metabolic model for the production of acetate by Escherichia coli growing on glucose under aerobic conditions was presented previously (Ko et al., 1993). The resulting model equations can be used to explain phenomena often observed with industrial fermentations, i.e., increased acetate production which follows from high glucose uptake rate, a low dissolved oxygen concentration, a high specific growth rate, or a combination of these conditions. However, several questions still need to be addressed. First, cell composition is growth rate and media dependent. Second, the macromolecular composition varied between E. coli strains. And finally, a model that represents the carbon fluxes between the Embden-Meyerhof-Parnas (EMP) and the hexose monophosphate (HMP) pathways when cells are subject to internal and/or external stresses is still not well defined. In the present work, we have made an effort to account for these effects, and the resulting model equations show good agreement for wild-type and recombinant E. coli experimental data for the acetate concentration, the onset of acetate secretion, and cell yield based on glucose. These results are useful for optimizing aerobic E. coli fermentation processes. More specifically, we have determined the EMP pathway carbon flux profiles required by the integrated metabolic model for an accurate fit of the acetic acid profile data from a wild-type E. coli strain ML308. These EMP carbon flux profiles were correlated with a dimensionless measurement of biomass and then used to predict the acetic acid profiles for E. coli strain F-122 expressing human immunodeficiency virus-(HIV(528)) beta-galactosidase fusion protein. The effect of different macromolecular compositions and growth rates between these two E. coli strains required a constant scaling factor for improved quantitative predictions.     

Effect of oxygen limitation and medium composition on Escherichia coli fermentation in shake-flask cultures

Shake-flask cultures are widely used for screening of high producing strains. To select suitable strains for production scale, cultivation parameters should be applied that provide optimal growth conditions. A novel method of measuring respiratory activity in shake-flask cultures was employed to analyze Escherichia coli fermentation under laboratory conditions. Our results suggest that the length of fermentation, choice of medium, and aeration do not normally satisfy the requirements for unlimited growth in shake flasks. Using glycerol rather than glucose as a carbon source greatly reduced the accumulation of overflow and fermentative metabolites when oxygen supply was unlimited. A rich buffered medium, Terrific Broth (TB), yielded 5 times more biomass compared to LB medium but also caused oxygen limitation in standard shake-flask cultures at shaking frequencies below 400 rpm. These results were used to optimize the production of benzoylformate decarboxylase from Pseudomonas putida in E. coli SG13009, resulting in a 10-fold increase in volumetric enzyme production. This example demonstrates how variation of medium composition and oxygen supply can be evaluated by the measurement of the respiratory activity. This can help to efficiently optimize screening conditions for E. coli.     

Metabolism of cyclic adenosine 3'',5''-monophosphate and induction of tryptophanase in Escherichia coli.

The relationship between cyclic adenosine 3',5'-monophosphate (cyclic AMP) metabolism and the induction of tryptophanase and beta-galactosidase was studied in several strains of Escherichia coli grown with succinate, acetate, glycerol, or glucose as the carbon source. No consistent relationship between the intracellular concentration of cyclic AMP in the several strains cultured and the various carbon sources was discerned. In E. coli K-12-1 the induction of tryptophanase was found to vary in the order: succinate greater than acetate greater than glycerol greater than glucose, and that of beta-galactosidase was found in the order: glycerol greater than acetate greater than succinate greater than glucose. Rate of accumulation of cyclic AMP in the culture filtrate was in the order: succinate greater than acetate greater than glycerol greater than glucose. The addition of glycerol to E. coli K-12-1 grown in acetate caused inhibition of tryptophanase and slight inhibition of accumulation of extracellular cyclic AMP. These same conditions caused beta-galactosidase induction to be stimulated. The addition of exogenous cyclic AMP to cultures grown with four different carbon sources had an effect characteristic for each of the two enzymes studied as well as each individual carbon source. The results suggest that there are control elements distinct from cyclic AMP and its receptor protein which respond to the catabolic situation of the cell.     

Elucidation of enzyme control mechanisms using macroscopic measurements in a mixed substrate fermentation system

The objective of this work was to relate macroscopically measurable on-line fermentation parameters such as dissolved oxygen, off-gas oxygen and carbon dioxide, and cell mass, to the controlled production of key intracellular enzymes under carbon limited conditions. Both batch and perturbed batch aerobic fermentations were performed using two different strains of Escherichia coli, with glucose and lactose as the sole carbon sources. The two strains differed from each other only in the lac operon region of their genome. The parent strain, E. coli 3000, was inducible for the enzyme beta-galactosidase. The other strain, E. coli 3300, was a constitutive mutant in the production of beta-galactosidase. In all experiments, off-line assays of sugars and beta-galactosidase activity were performed. It was observed that there is a clear relationship between the macroscopic on-line measurements, dissolved oxygen tension, carbon dioxide evolution rate and oxygen uptake rate, and the microscopic control phenomena of catabolite repression, catabolite inhibition, and inducer repression.     

On the control mechanism of bacterial growth by cyclic adenosine 3',5'-monophosphate

Inhibition of E. coli growth by cyclic adenosine monophosphate is observed in wild type strains cultured in glucose as carbon source, but not in a cyclic AMP receptor protein deficient mutant. A deletion mutant of the adenylate cyclase gene requires cyclic adenosine monophosphate for optimal growth. Using glucose as carbon source, 2 mM cyclic AMP promotes maximal rates of cell multiplication in this mutant; however higher concentrations of the nucleotide inhibit growth. Cell multiplication of wild type strains grown in glycerol is not affected by cyclic adenosine monophosphate. Nevertheless, in this carbon source the growth rate of the adenylate cyclase mutant is strongly inhibited by concentrations of this nucleotide beyond 0.1 mM. This suggests that growth inhibition by exogenous cyclic adenosine monophosphate is highly dependent on the intracellular levels of the nucleotide.     

Characterization of an oxygen-dependent inducible promoter,the Escherichia coli nar promoter,in gram-negative host strains

The Escherichia coli nar promoter is maximally induced under anaerobic conditions in the presence of nitrate ion or under anaerobic only conditions, depending on the genotype of the E. coli nar promoter. Previously, we found that the E. coli nar promoter has some desirable characteristics as an inducible promoter in the E. coli host strains. In this study, the E. coli nar promoter with lacZ gene at the downstream was cloned onto a broad-host-range Gram-negative vector, pBBR122. It was then induced in some other Gram-negative host strains, such as Agrobacterium, Pseudomonas, and Rhizobium, to determine whether the E. coli nar promoter could be used as an inducible promoter in these strains. From shake-flask experiments it was found that the wild-type E. coli nar promoter cloned onto pBBR122, pNW61, was suppressed under aerobic conditions in an Agrobacterium host strain, was partially induced under microaerobic only conditions, and was maximally induced under microaerobic conditions in the presence of nitrate ion. Whereas the mutant-type E. coli nar promoter cloned onto pBBR122, pNW618, was suppressed under aerobic conditions and was maximally induced under microaerobic conditions, regardless of the presence of nitrate ion. This kind of induction pattern observed for the E. coli nar promoters in the Agrobacterium host strain was similar to that observed for the E. coli nar promoters in the E. coli host strain. On the other hand, it was found that both of the E. coli nar promoters, pNW61 and pNW618, in a Pseudomonas host strain were partially induced under aerobic conditions and were maximally induced under microaerobic conditions, regardless of the presence of nitrate. Finally, it was found that both of the E. coli nar promoters in a Rhizobium host strain were minimally induced, regardless of the presence of oxygen or nitrate ion. Similar induction patterns for the three strains were also observed from fermentor experiments in which the dissolved oxygen (DO) level was tightly controlled. From an evolutionary point of view, the results from the three Gram-negative host strains indicate that the E. coli nar promoter system, including the promoter and regulatory proteins, was best conserved in the Agrobacterium host strain and the least conserved in the Rhizobium host strain. From an industrial point of view, the results indicate that the E. coli nar promoter system can be used as an oxygen-dependent inducible promoter in both Agrobacterium and Pseudomonas host strains.     

Design of metabolic engineering strategies for maximizing L-(-)-carnitine production by Escherichia coli. Integration of the metabolic and bioreactor levels

In this work metabolic engineering strategies for maximizing L-(-)-carnitine production by Escherichia coli based on the Biochemical System Theory and the Indirect Optimization Method are presented. The model integrates the metabolic and the bioreactor levels using power-law formalism. Based on the S-system model, the Indirect Optimization Method was applied, leading to profiles of parameter values that are compatible with both the physiology of the cells and the bioreactor system operating conditions. This guarantees their viability and fitness and yields higher rates of L-(-)-carnitine production. Experimental results using a high cell density reactor were compared with optimized predictions from the Indirect Optimization Method. When two parameters (the dilution rate and the initial crotonobetaine concentration) were directly changed in the real experimental system to the prescribed optimum values, the system showed better performance in L-(-)-carnitine production (74% increase in production rate), in close agreement with the model's predictions. The model shows control points at macroscopic (reactor operation) and microscopic (molecular) levels where conversion and productivity can be increased. In accordance with the optimized solution, the next logical step to improve the L-(-)-carnitine production rate will involve metabolic engineering of the E. coli strain by overexpressing the carnitine transferase, CaiB, activity and the protein carrier, CaiT, responsible for substrate and product transport in and out of the cell. By this means it is predicted production may be enhanced by up to three times the original value.     

Characterization of the acetate-producing pathways in Escherichia coli

Although the bacterium E. coli is chosen as the host in many bioprocesses, the accumulation of a common byproduct, acetate, is often problematic. Acetate, when present at high levels, will inhibit both cell growth and recombinant protein productivity. In addition, products derived from the central aerobic metabolic pathway often compete with the acetate-producing pathways poxB and ackA-pta for glucose as the substrate. As such, a significant portion of the glucose may be excreted as acetate, wasting substrate that otherwise could have been used for the desired product. We have created mutant E. coli strains with a deletion of either the poxB or the ackA-pta pathway. These two strains, along with the wild-type strain, have been studied in batch reactors over a 12 h time period, at pH 7.0 and 6.0. The wild-type strain has also been studied using glucose as the carbon source. Data were collected to correlate cellular growth, extracellular metabolite production, enzyme activity, and gene expression. Results show that the ackA-pta pathway dominates in exponential phase, and the poxB pathway dominates in stationary phase. The ackA-pta pathway is repressed in acidic environments, whereas the poxB pathway is activated.     

Molybdenum cofactor negative mutants of Escherichia coli use citrate anaerobically

Anaerobically, Escherichia coli cannot grow using either glycerol or citrate as sole carbon and energy source. However, it has been reported that a mixture of glycerol and citrate will support growth. We have found that wild-type strains of E. coli K-12 do not grow on glycerol plus citrate anaerobically. However, growth eventually occurs due to the frequent appearance of mutants. We found that such Cit+ mutants were defective in anaerobic respiration with nitrate or trimethylamine-N-oxide and were chlorate resistant (i.e. molybdenum cofactor deficient). Conversely, well characterized mutants in any of chlA, B, D, E, G and N were also able to use citrate anaerobically. No anaerobic growth differences between wild type and chl mutants were observed either with fermentable sugars or with glycerol plus fumarate or glycerol plus tartrate. Citrate lyase was induced anaerobically by citrate and repressed by glucose in both wild type strains and chl mutants. Furthermore, levels of citrate lyase, fumarate reductase, malate dehydrogenase, fumarase and alcohol dehydrogenase were similar in both types of strains under anaerobic conditions. It is conceivable that a functioning molybdenum cofactor prevents use of citrate by keeping citrate lyase in the inactive form.     

Linear correlation between online capacitance and offline biomass measurement up to high cell densities in Escherichia coli fermentations in a pilot-scale pressurized bioreactor

To yield high concentrations of protein expressed by genetically modified Escherichia coli, it is important that the bacterial strains are cultivated to high cell density in industrial bioprocesses. Since the expressed target protein is mostly accumulated inside the E. coli cells, the cellular product formation can be directly correlated to the bacterial biomass concentration. The typical way to determine this concentration is to sample offline. Such manual sampling, however, wastes time and is not efficient for acquiring direct feedback to control a fedbatch fermentation. An E. coli K12-derived strain was cultivated to high cell density in a pressurized stirred bioreactor on a pilot scale, by detecting biomass concentration online using a capacitance probe. This E. coli strain was grown in pure minimal medium using two carbon sources (glucose and glycerol). By applying exponential feeding profiles corresponding to a constant specific growth rate, the E. coli culture grew under carbon-limited conditions to minimize overflow metabolites. A high linearity was found between capacitance and biomass concentration, whereby up to 85 g/L dry cell weight was measured. To validate the viability of the culture, the oxygen transfer rate (OTR) was determined online, yielding maximum values of 0.69 mol/l/h and 0.98 mol/l/h by using glucose and glycerol as carbon sources, respectively. Consequently, online monitoring of biomass using a capacitance probe provides direct and fast information about the viable E. coli biomass generated under aerobic fermentation conditions at elevated headspace pressures.     

Aerobic fermentation of D-glucose by an evolved cytochrome oxidase-deficient Escherichia coli strain

Fermentation of glucose to D-lactic acid under aerobic growth conditions by an evolved Escherichia coli mutant deficient in three terminal oxidases is reported in this work. Cytochrome oxidases (cydAB, cyoABCD, and cbdAB) were removed from the E. coli K12 MG1655 genome, resulting in the ECOM3 (E. coli cytochrome oxidase mutant) strain. Removal of cytochrome oxidases reduced the oxygen uptake rate of the knockout strain by nearly 85%. Moreover, the knockout strain was initially incapable of growing on M9 minimal medium. After the ECOM3 strain was subjected to adaptive evolution on glucose M9 medium for 60 days, a growth rate equivalent to that of anaerobic wild-type E. coli was achieved. Our findings demonstrate that three independently adaptively evolved ECOM3 populations acquired different phenotypes: one produced lactate as a sole fermentation product, while the other two strains exhibited a mixed-acid fermentation under oxic growth conditions with lactate remaining as the major product. The homofermenting strain showed a D-lactate yield of 0.8 g/g from glucose. Gene expression and in silico model-based analyses were employed to identify perturbed pathways and explain phenotypic behavior. Significant upregulation of ygiN and sodAB explains the remaining oxygen uptake that was observed in evolved ECOM3 strains. E. coli strains produced in this study showed the ability to produce lactate as a fermentation product from glucose and to undergo mixed-acid fermentation during aerobic growth.     

Effect of glucose on the capacity of Escherichia coli to be infected by a virulent lamba bacteriophage

Howes, William V. (Massachusetts Institute of Technology, Cambridge). Effect of glucose on the capacity of Escherichia coli to be infected by a virulent lambda bacteriophage. J. Bacteriol. 90:1183-1193. 1965.-A substrate-dependent phenotypic resistance to phage lambda(vir) was observed among cells of Escherichia coli W3350 and C600 grown aerobically on glucose. Similar cells grown on glycerol were sensitive. When cells of W3350 grown on glycerol were transferred to glucose, the rate of appearance of the resistant fraction was proportional to the growth rate and became zero after 5.5 to 6.0 generations. Cells grown on glucose, upon transfer to glycerol, became sensitive within one generation. P(32) studies with W3350 indicated that the resistant cells did not adsorb phage. Furthermore, among the sensitive cells approximately the same number of particles adsorbed to each cell. Among five strains of E. coli K-12 investigated, three did not exhibit this aerobic phenotypic resistance. W3350 grown anaerobically on glucose was 100% resistant. Anaerobic growth had no further effect on C600. These inconsistent effects of anaerobiosis probably involved a mechanism different from that of aerobic growth.