Doubling the catabolic reducing power (NADH) output of Escherichia coli fermentation for production of reduced products

Expression of acetaldehyde dehydrogenase (aldB) improved ethanol production from xylose by the ethanologenic Escherichia coli RM10

An endogenous homoethanol pathway (glucose/1.2 xylose => 2 pyruvate => 2 ethanol) was previously engineered in Escherichia coli SZ410 via eliminating acid-producing pathways and anaerobic expression of the pyruvate dehydrogenase complex (aceEF-lpd operon). This ethanologenic derivative was subsequently engineered through adaptive evolution and partial deletion of the RNase G, resulting in an improved strain of E. coli RM10 for ethanol production using C6 and C5 sugars. Nevertheless, compared to the ethanol tolerance and/or ethanol titer achieved by industrial yeast, further incremental improvement of RM10 was needed for ethanol production using cellulosic biomass derived C6 and C5 sugars. In this study, the role of aldB gene (encoding for acetaldehyde dehydrogenase, AldB, which oxidizes acetaldehyde to acetic acid) was evaluated for ethanol/acetaldehyde tolerance and xylose fermentation by RM10. Deletion of aldB gene decreased ethanol tolerance, fermentative cell growth and ethanol production from xylose; while overexpression of aldB gene improved fermentative cell growth, and increased ethanol production from xylose. The improvement is likely attributed to preventing acetaldehyde accumulation (a toxic intermediate of homoethanol pathway) via AldB catalyzed oxidation.

Engineering a synthetic anaerobic respiration for reduction of xylose to xylitol using NADH output of glucose catabolism by Escherichia coli AI21

Background

Anaerobic rather than aerobic fermentation is preferred for conversion of biomass derived sugars to high value redox-neutral and reduced commodities. This will likely result in a higher yield of substrate to product conversion and decrease production cost since substrate often accounts for a significant portion of the overall cost. To this goal, metabolic pathway engineering has been used to optimize substrate carbon flow to target products. This approach works well for the production of redox neutral products such as lactic acid from redox neutral sugars using the reducing power NADH (nicotinamide adenine dinucleotide, reduced) generated from glycolysis (2 NADH per glucose equivalent). Nevertheless, greater than two NADH per glucose catabolized is needed for the production of reduced products (such as xylitol) from redox neutral sugars by anaerobic fermentation.

Results

The Escherichia coli strain AI05 (ΔfrdBC ΔldhA ΔackA Δ(focA-pflB) ΔadhE ΔptsG ΔpdhR::pflBp₆-(aceEF-lpd)), previously engineered for reduction of xylose to xylitol using reducing power (NADH equivalent) of glucose catabolism, was further engineered by 1) deleting xylAB operon (encoding for xylose isomerase and xylulokinase) to prevent xylose from entering the pentose phosphate pathway; 2) anaerobically expressing the sdhCDAB-sucABCD operon (encoding for succinate dehydrogenase, α-ketoglutarate dehydrogenase and succinyl-CoA synthetase) to enable an anaerobically functional tricarboxcylic acid cycle with a theoretical 10 NAD(P)H equivalent per glucose catabolized. These reducing equivalents can be oxidized by synthetic respiration via xylose reduction, producing xylitol. The resulting strain, AI21 (pAI02), achieved a 96 % xylose to xylitol conversion, with a yield of 6 xylitol per glucose catabolized (molar yield of xylitol per glucose consumed (Y_RPG) = 6). This represents a 33 % improvement in xylose to xylitol conversion, and a 63 % increase in xylitol yield per glucose catabolized over that achieved by AI05 (pAI02).

Conclusions

Increasing reducing power (NADH equivalent) output per glucose catabolized was achieved by anaerobic expression of both the pdh operon (pyruvate dehydrogenase) and the sdhCDAB-sucABCD operon, resulting in a strain capable of generating 10 NADH equivalent per glucose under anaerobic condition. The new E. coli strain AI21 (pAI02) achieved an actual 96 % conversion of xylose to xylitol (via synthetic respiration), and 6 xylitol (from xylose) per glucose catabolized (Y_RPG = 6, the highest known value). This strategy can be used to engineer microbial strains for the production of other reduced products from redox neutral sugars using glucose as a source of reducing power.

Increasing reducing power output (NADH) of glucose catabolism for reduction of xylose to xylitol by genetically engineered Escherichia coli AI05

Anaerobic homofermentative production of reduced products requires additional reducing power (NADH and/or NADPH) output from glucose catabolism. Previously, with an anaerobically expressed pyruvate dehydrogenase operon (aceEF-lpd), we doubled the reducing power output to four NADH per glucose (or 1.2 xylose) catabolized anaerobically, which satisfied the NADH requirement to establish a non-transgenic homoethanol pathway (1 glucose or 1.2 xylose --> 2 acetyl-CoA + 4 NADH --> 2 ethanol) in the engineered strain, Escherichia coli SZ420 (∆frdBC ∆ldhA ∆ackA ∆focA-pflB ∆pdhR::pflBp6-pflBrbs-aceEF-lpd). In this study, E. coli SZ420 was further engineered for reduction of xylose to xylitol by (1) deleting the alcohol dehydrogenase gene (adhE) to divert NADH from the ethanol pathway; (2) deleting the glucose-specific PTS permease gene (ptsG) to eliminate catabolite repression and allow simultaneous uptake of glucose and xylose; (3) cloning the aldose reductase gene (xylI) of Candida boidinii to reduce xylose to xylitol. The resulting strain, E. coli AI05 (pAGI02), could in theory simultaneously uptake glucose and xylose, and utilize glucose as a source of reducing power for the reduction of xylose to xylitol, with an expected yield of four xylitol for each glucose consumed (YRPG = 4) under anaerobic conditions. In resting cell fermentation tests using glucose and xylose mixtures, E. coli AI05 (pAGI02) achieved an actual YRPG value of ~3.6, with xylitol as the major fermentation product and acetate as the by-product.

Escherichia coli redox mutants as microbial cell factories for the synthesis of reduced biochemicals

Bioprocesses conducted under conditions with restricted O₂ supply are increasingly exploited for the synthesis of reduced biochemicals using different biocatalysts. The model facultative aerobe Escherichia coli, the microbial cell factory par excellence, has elaborate sensing and signal transduction mechanisms that respond to the availability of electron acceptors and alternative carbon sources in the surrounding environment. In particular, the ArcBA and CreBC two-component signal transduction systems are largely responsible for the metabolic regulation of redox control in response to O₂ availability and carbon source utilization, respectively. Significant advances in the understanding of the biochemical, genetic, and physiological duties of these regulatory systems have been achieved in recent years. This situation allowed to rationally-design novel engineering approaches that ensure optimal carbon and energy flows within central metabolism, as well as to manipulate redox homeostasis, in order to optimize the production of industrially-relevant metabolites. In particular, metabolic flux analysis provided new clues to understand the metabolic regulation mediated by the ArcBA and CreBC systems. Genetic manipulation of these regulators proved useful for designing microbial cells factories tailored for the synthesis of reduced biochemicals with added value, such as poly(3-hydroxybutyrate), under conditions with restricted O₂ supply. This network-wide strategy is in contrast with traditional metabolic engineering approaches, that entail direct modification of the pathway(s) at stake, and opens new avenues for the targeted modulation of central catabolic pathways at the transcriptional level.

Engineering a homobutanol fermentation pathway in Escherichia coli EG03

A homobutanol fermentation pathway was engineered in a derivative of Escherichia coli B (glucose [glycolysis] => 2 pyruvate + 2 NADH; pyruvate [pyruvate dehydrogenase] => acetyl-CoA + NADH; 2 acetyl-CoA [butanol pathway enzymes] + 4 NADH => butanol; summary stoichiometry: glucose => butanol). Initially, the native fermentation pathways were eliminated from E. coli B by deleting the genes encoding for lactate dehydrogenase (ldhA), acetate kinase (ackA), fumarate reductase (frdABCD), pyruvate formate lyase (pflB), and alcohol dehydrogenase (adhE), and the pyruvate dehydrogenase complex (aceEF-lpd) was anaerobically expressed through promoter replacement. The resulting strain, E. coli EG03 (ΔfrdABCD ΔldhA ΔackA ΔpflB Δ adhE ΔpdhR ::pflBp6-aceEF-lpd ΔmgsA), could generate 4 NADH for every glucose oxidized to two acetyl-CoA through glycolysis and the pyruvate dehydrogenase complex. However, EG03 lost its ability for anaerobic growth due to the lack of NADH oxidation pathways. When the butanol pathway genes that encode for acetyl-CoA acetyltransferase (thiL), 3-hydroxybutyryl-CoA dehydrogenase (hbd), crotonase (crt), butyryl-CoA dehydrogenase (bcd, etfA, etfB), and butyraldehyde dehydrogenase (adheII) were cloned from Clostridium acetobutylicum ATCC 824, and expressed in E. coli EG03, a balanced NADH oxidation pathway was established for homobutanol fermentation (glucose => 4 NADH + 2 acetyl-CoA => butanol). This strain was able to convert glucose to butanol (1,254 mg l(-1)) under anaerobic condition.

Partial deletion of rng (RNase G)-enhanced homoethanol fermentation of xylose by the non-transgenic Escherichia coli RM10

Previously, a native homoethanol pathway was engineered in Escherichia coli B by deletions of competing pathway genes and anaerobic expression of pyruvate dehydrogenase (PDH encoded by aceEF-lpd). The resulting ethanol pathway involves glycolysis, PDH, and alcohol dehydrogenase (AdhE). The E. coli B-derived ethanologenic strain SZ420 was then further improved for ethanol tolerance (up to 40 g l(-1) ethanol) through adaptive evolution. However, the resulting ethanol tolerant mutant, SZ470, was still unable to complete fermentation of 75 g l(-1) xylose, even though the theoretical maximum ethanol titer would have been less than 40 g l(-1) should the fermentation have reached completion. In this study, the cra (encoding for a catabolite repressor activator) and the HSR2 region of rng (encoding for RNase G) were deleted from SZ470 in order to improve xylose fermentation. Deletion of the HSR2 domain resulted in significantly increased mRNA levels (47-fold to 409-fold) of multiple glycolytic genes (pgi, tpiA, gapA, eno), as well as the engineered ethanol pathway genes (aceEF-lpd, adhE) and the transcriptional regulator Fnr (fnr). The higher adhE mRNA level resulted in increased AdhE activity (>twofold). Although not measured, the increase of other mRNAs might also enhance expressions of their encoding proteins. The increased enzymes would then enable the resulting strain, RM10, to achieve increased cell growth and complete fermentation of 75 g l(-1) xylose with an 84% improved ethanol titer (35 g l(-1)), compared to that (19 g l(-1)) obtained by the parent, SZ470. However, deletion of cra resulted in a negative impact on cell growth and xylose fermentation, suggesting that Cra is important for long-term fermentative cell growth.

Adaptive evolution of nontransgenic Escherichia coli KC01 for improved ethanol tolerance and homoethanol fermentation from xylose

Due to its excellent capability to ferment five-carbon sugars, Escherichia coli has been considered one of the platform organisms to be engineered for production of cellulosic ethanol. Nevertheless, genetically engineered ethanologenic E. coli lacks the essential trait of alcohol tolerance. Development of ethanol tolerance is required for cost-effective ethanol fermentation. In this study, we improved alcohol tolerance of a nontransgenic E. coli KC01 (ldhA pflB ackA frdBC pdhR::pflBp6-aceEF-lpd) through adaptive evolution. During ~350 generations of adaptive evolution, a gradually increased concentration of ethanol was used as a selection pressure to enrich ethanol-tolerant mutants. The evolved mutant, E. coli SZ470, was able to grow anaerobically at 40 g l(-1) ethanol, a twofold improvement over parent KC01. When compared with KC01 for small-scale (500 ml) xylose (50 g l(-1)) fermentation, SZ470 achieved 67% higher cell mass, 48% faster volumetric ethanol productivity, and 50% shorter time to complete fermentation with ethanol titer of 23.5 g l(-1) and yield of 94%. These results demonstrate that an industry-oriented nontransgenic E. coli strain could be developed through incremental improvements of desired traits by a combination of molecular biology and traditional microbiology techniques.