Efficient production of 2,3-butanediol in Saccharomyces cerevisiae by eliminating ethanol and glycerol production and redox rebalancing

2,3-Butanediol is a promising valuable chemical that can be used in various areas as a liquid fuel and a platform chemical. Here, 2,3-butanediol production in Saccharomyces cerevisiae was improved stepwise by eliminating byproduct formation and redox rebalancing. By introducing heterologous 2,3-butanediol biosynthetic pathway and deleting competing pathways producing ethanol and glycerol, metabolic flux was successfully redirected to 2,3-butanediol. In addition, the resulting redox cofactor imbalance was restored by overexpressing water-forming NADH oxidase (NoxE) from Lactococcus lactis. In a flask fed-batch fermentation with optimized conditions, the engineered adh1Δadh2Δadh3Δadh4Δadh5Δgpd1Δgpd2Δ strain overexpressing Bacillus subtilis α-acetolactate synthase (AlsS) and α-acetolactate decarboxylase (AlsD), S. cerevisiae 2,3-butanediol dehydrogenase (Bdh1), and L. lactis NoxE from a single multigene-expression vector produced 72.9 g/L 2,3-butanediol with the highest yield (0.41 g/g glucose) and productivity (1.43 g/(L·h)) ever reported in S. cerevisiae.     

Surface-<Emphasis Type="Italic">engineered Saccharomyces cerevisiae</Emphasis> displaying α-acetolactate decarboxylase from <Emphasis Type="Italic">Acetobacter aceti</Emphasis> ssp <Emphasis Type="Italic">xylinum</Emphasis>

Objectives

To convert α-acetolactate into acetoin by an α-acetolactate decarboxylase (ALDC) to prevent its conversion into diacetyl that gives beer an unfavourable buttery flavour.

Results

We constructed a whole Saccharomyces cerevisiae cell catalyst with a truncated active ALDC from Acetobacter aceti ssp xylinum attached to the cell wall using the C-terminal anchoring domain of α-agglutinin. ALDC variants in which 43 and 69 N-terminal residues were absent performed equally well and had significantly decreased amounts of diacetyl during fermentation. With these cells, the highest concentrations of diacetyl observed during fermentation were 30 % less than those in wort fermented with control yeasts displaying only the anchoring domain and, unlike the control, virtually no diacetyl was present in wort after 7 days of fermentation.

Conclusions

Since modification of yeasts with ALDC variants did not affect their fermentation performance, the display of α-acetolactate decarboxylase activity is an effective approach to decrease the formation of diacetyl during beer fermentation.

     

Improvement of acetoin reductase activity enhances bacitracin production by Bacillus licheniformis

Bacitracin fermentation by Bacillus licheniformis in this work showed three characteristics: (1) the extracellular propionate, butyrate, acetoin and 2,3-butanediol accumulates under conditions of low dissolved oxygen (zero after 4 h cultivation), reaching a total content of approximately 11.1 g/L; (2) cell growth occurs quickly subsequent to cell autolysis and the second growth; and (3) there is a low content of 2,3-butanediol, a reduced product of acetoin catalyzed by acetoin reductase, in the culture process. In this study, addition of MnCl₂ (0.3 mg/L) to the production medium increased the acetoin reductase activity, redirected the NADH oxidation partly from the propionate- and butyrate-production pathways to the 2,3-butanediol synthesis pathway, reduced the intracellular NADH/NAD⁺ ratio, and facilitated cell growth, ultimately achieving a 11.6% increase in bacitracin production (1076 U/mL) versus the control. The results provide useful information regarding large-scale bacitracin production by B. licheniformis.     

Selection of an endogenous 2,3-butanediol pathway in Escherichia coli by fermentative redox balance

Fermentative redox balance has long been utilized as a metabolic evolution platform to improve efficiency of NADH-dependent pathways. However, such system relies on the complete recycling of NADH and may become limited when the target pathway results in excess NADH stoichiometrically. In this study, endogenous capability of Escherichia coli for 2,3-butanediol (2,3-BD) synthesis was explored using the anaerobic selection platform based on redox balance. To address the issue of NADH excess associated with the 2,3-BD pathway, we devised a substrate-decoupled system where a pathway intermediate is externally supplied in addition to the carbon source to decouple NADH recycling ratio from the intrinsic pathway stoichiometry. In this case, feeding of the 2,3-BD precursor acetoin effectively restored anaerobic growth of the mixed-acid fermentation mutant that remained otherwise inhibited even in the presence of a functional 2,3-BD pathway. Using established 2,3-BD dehydrogenases as model enzyme, we verified that the redox-based selection system is responsive to NADPH-dependent reactions but with lower sensitivity. Based on this substrate-decoupled selection scheme, we successfully identified the glycerol/1,2-propanediol dehydrogenase (Ec-GldA) as the major enzyme responsible for the acetoin reducing activity (k_cat/K_m≈0.4 mM⁻¹ s⁻¹) observed in E. coli. Significant shift of 2,3-BD configuration upon withdrawal of the heterologous acetolactate decarboxylase revealed that the endogenous synthesis of acetoin occurs via diacetyl. Among the predicted diacetyl reductase in E. coli, Ec-UcpA displayed the most significant activity towards diacetyl reduction into acetoin (V_max≈6 U/mg). The final strain demonstrated a meso-2,3-BD production titer of 3 g/L without introduction of foreign genes. The substrate-decoupled selection system allows redox balance regardless of the pathway stoichiometry thus enables segmented optimization of different reductive pathways through enzyme bioprospecting and metabolic evolution.     

The rebalanced pathway significantly enhances acetoin production by disruption of acetoin reductase gene and moderate-expression of a new water-forming NADH oxidase in Bacillus subtilis

Bacillus subtilis produces acetoin as a major extracellular product. However, the by-products of 2,3-butanediol, lactic acid and ethanol were accompanied in the NADH-dependent pathways. In this work, metabolic engineering strategies were proposed to redistribute the carbon flux to acetoin by manipulation the NADH levels. We first knocked out the acetoin reductase gene bdhA to block the main flux from acetoin to 2,3-butanediol. Then, among four putative candidates, we successfully screened an active water-forming NADH oxidase, YODC. Moderate-expression of YODC in the bdhA disrupted B. subtilis weakened the NADH-linked pathways to by-product pools of acetoin. Through these strategies, acetoin production was improved to 56.7 g/l with an increase of 35.3%, while the production of 2,3-butanediol, lactic acid and ethanol were decreased by 92.3%, 70.1% and 75.0%, respectively, simultaneously the fermentation duration was decreased 1.7-fold. Acetoin productivity by B. subtilis was improved to 0.639 g/(l h).     

Harnessing the respiration machinery for high-yield production of chemicals in metabolically engineered Lactococcus lactis

When modifying the metabolism of living organisms with the aim of achieving biosynthesis of useful compounds, it is essential to ensure that it is possible to achieve overall redox balance. We propose a generalized strategy for this, based on fine-tuning of respiration. The strategy was applied on metabolically engineered Lactococcus lactis strains to optimize the production of acetoin and (R,R)-2,3-butanediol (R-BDO). In the absence of an external electron acceptor, a surplus of two NADH per acetoin molecule is produced. We found that a fully activated respiration was able to efficiently regenerate NAD⁺, and a high titer of 371 mM (32 g/L) of acetoin was obtained with a yield of 82% of the theoretical maximum. Subsequently, we extended the metabolic pathway from acetoin to R-BDO by introducing the butanediol dehydrogenase gene from Bacillus subtilis. Since one mole of NADH is consumed when acetoin is converted into R-BDO per mole, only the excess of NADH needs to be oxidized via respiration. Either by fine-tuning the respiration capacity or by using a dual-phase fermentation approach involving a switch from fully respiratory to non-respiratory conditions, we obtained 361 mM (32 g/L) R-BDO with a yield of 81% or 365 mM (33 g/L) with a yield of 82%, respectively. These results demonstrate the great potential in using finely-tuned respiration machineries for bio-production.     

Properties of 2,3-Butanediol Dehydrogenases from Lactococcus lactis subsp. lactis in Relation to Citrate Fermentation

Two 2,3-butanediol dehydrogenases (enzymes 1 and 2; molecular weight of each, 170,000) have been partially purified from Lactococcus lactis subsp. lactis (Streptococcus diacetylactis) D10 and shown to have reductase activity with either diacetyl or acetoin as the substrate. However, the reductase activity with 10 mM diacetyl was far greater for both enzymes (7.0- and 4.7-fold for enzymes 1 and 2, respectively) than with 10 mM acetoin as the substrate. In contrast, when acetoin and diacetyl were present together, acetoin was the preferred substrate for both enzymes, with enzyme 1 showing the more marked preference for acetoin. meso-2,3-Butanediol was the only isomeric product, with enzyme 1 independent of the substrate combinations. For enzyme 2, both the meso and optical isomers of 2,3-butanediol were formed with acetoin as the substrate, but only the optical isomers were produced with diacetyl as the substrate. With batch cultures of strain D10 at or near the point of citrate exhaustion, the main isomers of 2,3-butanediol present were the optical forms. If the pH was sufficiently high (>pH 5), acetoin reduction occurred over time and was followed by diacetyl reduction, and meso-2,3-butanediol became the predominant isomer. Interconversion of the optical isomers into the meso isomer did occur. The properties of 2,3-butanediol dehydrogenases are consistent with diacetyl and acetoin removal and the appearance of the isomers of 2,3-butanediol.     

Establishment of a novel gene expression method,BICES (biomass-inducible chromosome-based expression system), and its application to the production of 2,3-butanediol and acetoin

In this study, we describe a novel method for producing valuable chemicals from glucose and xylose in Escherichia coli. The notable features in our method are avoidance of plasmids and expensive inducers for foreign gene expression to reduce production costs; foreign genes are knocked into the chromosome, and their expression is induced with xylose that is present in most biomass feedstock. As loci for the gene knock-in, lacZYA and some pseudogenes are chosen to minimize unexpected effects of the knock-in on cell physiology. The promoter of xylF is inducible with xylose and is combined with the T7 RNA polymerase–T7 promoter system to ensure strong gene expression. This expression system was named BICES (biomass-inducible chromosome-based expression system). As examples of BICES application, 2,3-butanediol and acetoin were successfully produced from glucose and xylose, and the maximal concentrations reached 54 g L⁻¹ [99.6% in (R,S)-form] and 31 g L⁻¹, respectively. 2,3-Butanediol and acetoin are industrially important chemicals that are, at present, produced primarily through petrochemical processes. To demonstrate usability of BICES in practical situations, we produced these chemicals from a saccharified cedar solution. From these results, we can conclude that BICES is suitable for practical production of valuable chemicals from biomass.     

High-yield production of (R)-acetoin in Saccharomyces cerevisiae by deleting genes for NAD(P)H-dependent ketone reductases producing meso-2,3-butanediol and 2,3-dimethylglycerate

Acetoin is widely used in food and cosmetics industries as a taste and fragrance enhancer. To produce (R)-acetoin in Saccharomyces cerevisiae, acetoin biosynthetic genes encoding α-acetolactate synthase (AlsS) and α-acetolactate decarboxylase (AlsD) from Bacillus subtilis and water-forming NADH oxidase (NoxE) from Lactococcus lactis were integrated into delta-sequences in JHY605 strain, where the production of ethanol, glycerol, and (R,R)-2,3-butanediol (BDO) was largely eliminated. We further improved acetoin production by increasing acetoin tolerance by adaptive laboratory evolution, and eliminating other byproducts including meso-2,3-BDO and 2,3-dimethylglycerate, a newly identified byproduct. Ara1, Ypr1, and Ymr226c (named Ora1) were identified as (S)-alcohol-forming reductases, which can reduce (R)-acetoin to meso-2,3-BDO in vitro. However, only Ara1 and Ypr1 contributed to meso-2,3-BDO production in vivo. We elucidate that Ora1, having a substrate preference for (S)-acetoin, reduces (S)-α-acetolactate to 2,3-dimethylglycerate, thus competing with AlsD-mediated (R)-acetoin production. By deleting ARA1, YPR1, and ORA1, 101.3 g/L of (R)-acetoin was produced with a high yield (96% of the maximum theoretical yield) and high stereospecificity (98.2%).     

Metal-dependent thermal stability of recombinant endo-mannanase (ManB-1601) belonging to family GH 26 from Bacillus sp. CFR1601

A GH 26 endo-mannanase from Bacillus sp. CFR1601 was purified to homogeneity (M_w ∼39 kDa, specific activity 10,461.5 ± 100 IU/mg). Endo-mannanase gene (manb-1601, 1083 bp, accession No. KM404299) was expressed in Escherichia coli BL21 (DE3) and showed typical fingerprints of α/β proteins in the far-UV CD. A high degree of conservation among amino acid residues involved in metal chelation (His-1, 23 and Glu-336) and internal repeats (122–152 and 181–212) was observed in endo-mannanases reported from various Bacillus sp. Thermal inactivation kinetics suggested that metal ions are quintessential for stabilization of ManB-1601 structure as holoenzyme (E_a 87.4 kcal/mol, ΔH 86.7 kcal/mol, ΔS 186.6 cal/k/mol) displayed better values of thermodynamic parameters compared to metal-depleted ManB-1601 (E_a 47 kcal/mol, ΔH 45.7 kcal/mol, ΔS 64.7 cal/k/mol). EDTA treatment of ManB-1601 not only lead to transitions in both secondary and tertiary structure but also promulgated the population of conformational state that unfolds at lower temperature. ManB-1601 followed a three-state process for thermal inactivation wherein loss of tertiary structure preceded the concurrent loss of secondary structure and activity.     

Improved 2,3-butanediol production from corncob acid hydrolysate by fed-batch fermentation using Klebsiella oxytoca

Corncob acid hydrolysate, detoxed by sequently boiling, overliming and activated charcoal adsorption, was used for 2,3-butanediol production by Klebsiella oxytoca ACCC 10370. The effects of acetate in hydrolysate and pH on 2,3-butanediol production were investigated. It was found that acetic acid in hydrolysate inhibited the growth of K. oxytoca while benefited the 2,3-butanediol yield. With the increase in acetic acid concentration in medium from 0 to 4 g/l, the lag phase was prolonged and the specific growth rate decreased. The acetic acid inhibition on cell growth can be alleviated by adjusting pH to 6.3 prior to fermentation and a substrate fed-batch strategy with a low initial acetic acid concentration. Under the optimum condition, a maximal 2,3-butanediol concentration of 35.7 g/l was obtained after 60 h of fed-batch fermentation, giving a yield of 0.5 g/g reducing sugar and a productivity of 0.59 g/h l.     

Reducing diacetyl production of wine by overexpressing <Emphasis Type="Italic">BDH1</Emphasis> and <Emphasis Type="Italic">BDH2</Emphasis> in <Emphasis Type="Italic">Saccharomyces uvarum</Emphasis>

As a byproduct of yeast valine metabolism during fermentation, diacetyl can produce a buttery aroma in wine. However, high diacetyl concentrations generate an aromatic off-flavor and poor quality in wine. 2,3-Butanediol dehydrogenase encoded by BDH1 can catalyze the two reactions of acetoin from diacetyl and 2,3-butanediol from acetoin. BDH2 is a gene adjacent to BDH1, and these genes are regulated reciprocally. In this study, BDH1 and BDH2 were overexpressed in Saccharomyces uvarum to reduce the diacetyl production of wine either individually or in combination. Compared with those in the host strain WY1, the diacetyl concentrations in the recombinant strains WY1-1 with overexpressed BDH1, WY1-2 with overexpressed BDH2 alone, and WY1-12 with co-overexpressed BDH1 and BDH2 were decreased by 39.87, 33.42, and 46.71%, respectively. BDH2 was only responsible for converting diacetyl into acetoin, but not for the metabolic pathway of acetoin to 2,3-butanediol in S. uvarum. This study provided valuable insights into diacetyl reduction in wine.     

Metabolic engineering of Bacillus subtilis for the co-production of uridine and acetoin

In this study, a uridine and acetoin co-production pathway was designed and engineered in Bacillus subtilis for the first time. A positive correlation between acetoin and uridine production was observed and investigated. By disrupting acetoin reductase/2,3-butanediol dehydrogenasegenebdhA, the acetoin and uridine yield was increased while 2,3-butanediol formation was markedly reduced. Subsequent overexpression of the alsSD operon further improved acetoin yield and abolished acetate formation. After optimization of fermentation medium, key supplementation strategies of yeast extract and soybean meal hydrolysate were identified and applied to improve the co-production of uridine and acetoin. With a consumption of 290.33 g/L glycerol, the recombinant strain can accumulate 40.62 g/L uridine and 60.48 g/L acetoin during 48 h of fed-batch fermentation. The results indicate that simultaneous production of uridine and acetoin is an efficient strategy for balancing the carbon metabolism in engineered Bacillus subtilis. More importantly, co-production of value-added products is a possible way to improve the economics of uridine fermentation.

     

Parameter’s optimization and kinetics study of α-amylase enzyme of Bacillus sp. MB6 isolated from vegetable waste

α-Amylase, a very critical enzyme for hydrolysis of starch into simple sugar and it has various applications in industrial settings. This study reports the identification of Bacillus sp. MB6 which produces increased amount of enzyme from less required resources. To optimize the yield of enzyme, we used various combinations of parameters. The most optimized conditions for production of amylase enzyme from the bacterium Bacillus sp. MB6 are pH of 6, temperature of 37 °C, and incubation period of 48 h. Condition of enzymatic activity were also examined and the results show that pH of 6, a temperature of 55 °C, and a reaction time of 30 min are the best available conditions for its activity. Purification of enzyme by 1.63 fold enhanced the specific activity of enzyme based upon its activity analysis as compared with unpurified enzyme. Enzyme kinetics studies show the Michaelis constant (Km) to be 5.45 mg/ml and maximum velocity of the reaction (Vmax) to be 24.15 mg/ml/min. In conclusion, we report enzyme production and purification methodology that exhibit better yield of alpha-amylase for commercial applications.     

Production of 1,3-propanediol, 2,3-butanediol and ethanol by a newly isolated Klebsiella oxytoca strain growing on biodiesel-derived glycerol based media

The production of 1,3-propanediol, 2,3-butanediol and ethanol was studied, during cultivations of strain Klebsiella oxytoca FMCC-197 on biodiesel-derived glycerol based media. Different kinds of glycerol feedstocks and experimental conditions had an important impact upon the distribution of metabolic products; production of 1,3-propanediol was positively influenced by stable pH conditions and by the absence of N₂ gas infusions throughout the fermentation. Thus, during batch bioreactor fermentations conducted at increasing glycerol concentrations, 1,3-propanediol at 41.3 g/L and yield ～47% (w/w) was achieved at initial glycerol concentration ～120 g/L. At even higher initial glycerol media (150 and 170 g/L), growth was not ceased, but 1,3-propanediol production declined. During fed-batch fermentation under optimal experimental conditions, 126 g/L of glycerol were converted into 50.1 g/L of 1,3-propanediol. In this experiment, also 25.2 g/L of ethanol (conversion yield ～20%, w/w) were formed. A batch-bioreactor culture was performed under non-sterilized conditions and the 1,3-propanediol production was almost equivalent to the sterilized process. Concerning 2,3-butanediol formation, the most detrimental parameter was the absence of N₂ sparging and as a result, no 2,3-butanediol was produced. The presence of glucose as co-substrate seriously enhanced 2,3-butanediol production; when commercial glucose was employed as sole substrate, 32.1 g/L of 2,3-butanediol were formed.     

Enhanced production of 2,3-butanediol by engineered <Emphasis Type="Italic">Bacillus subtilis</Emphasis>

Production of 2,3-butanediol by Bacillus subtilis takes place in late-log or stationary phase, depending on the expression of bdhA gene encoding acetoin reductase, which converts acetoin to 2,3-butanediol. The present work focuses on the development of a strain of B. subtilis for enhanced production of 2,3-butanediol in early log phase of growth cycle. For this, the bdhA gene was expressed under the control of P _alsSD promoter of AlsSD operon for acetoin fermentation which served the substrate for 2,3-butanediol production. Addition of acetic acid in the medium induced the production of 2,3-butanediol by 2-fold. Two-step aerobic–anaerobic fermentation further enhanced 2,3-butanediol production by 4-fold in comparison to the control parental strain. Thus, addition of acetic acid and low dissolved oxygen in the medium are involved in activation of bdhA gene expression from P _alsSD promoter in early log phase. Under the conditions tested in this work, the maximum production of 2,3-butanediol, 2.1 g/l from 10 g/l glucose, was obtained at 24 h. Furthermore, under the optimized microaerophilic condition, the production of 2,3-butanediol improved up to 6.1 g/l and overall productivity increased by 6.7-fold to 0.4 g/l h in the engineered strain compared to that in the parental control.     

Purification and characterization of a novel α-amylase from a newly isolated Bacillus methylotrophicus strain P11-2

An aerobic bacterial strain P11-2 with high amylolytic activity was isolated from soil sample collected from wheat field of Jiyuan, China. The strain was identified as Bacillus methylotrophicus by morphological and physiological characteristics as well as by analysis of the gene encoding the 16S rRNA. The α-amylase was purified to homogeneity by a combination of 80% (NH₄)₂SO₄ precipitation, DEAE FF anion exchange, and superdex 75 10/300 GL gel filtration chromatography. The purified α-amylase exhibited specific activity of 330.7 U/mg protein that corresponds to 13.1 fold purification. The relative molecular mass of the α-amylase was 44.0 kDa by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE). The optimal pH and temperature for enzyme activity were 7.0 and 70 °C, respectively. The α-amylase activity was stimulated by Mg²⁺, Ba²⁺, Al³⁺ and dl-dithiothreitol (DTT), however, Ca²⁺ almost had no activation or inhibition on the α-amylase. After 4 h of reaction toward soluble starch, the end products were glucose, maltose and maltotriose. The 10 residues of the N-terminal sequence of the purified α-amylase were SVKNGQILHA, which showed no homology to other reported α-amylases from Bacillus strain.     

Biodegradability and mechanical properties of polycaprolactone composites encapsulating phosphate-solubilizing bacterium Bacillus sp. PG01

This study examined the feasibility of using polycaprolactone (PCL) and its composites (with starch and/or clay) in encapsulating cells of phosphate-solubilizing bacteria (PSB) for the development of biodegradable and “controlled-release” bacterial fertilizer. The PSB used in this work was an indigenous Bacillus sp. PG01 isolate. The results show that the PG01 strain was able to degrade all the cell-loaded capsules made of PCL and PCL composites, resulting in a continual cell release. Morphology observation indicates that severe disruption of the capsule structure occurred after incubation for 15–20 days. The biodegradability of the capsules decreased in the order of PCL/starch (20 wt%) > PCL/starch (20 wt%)/cay (7 wt%) > PCL alone > PCL/clay (7 wt%). Similar trends were also observed for the decrease in tensile strength and elongation at break, suggesting strong connections between biodegradability and the mechanical properties. Addition of starch appeared to enhance the biodegradability of the capsules, whereas the clay-blended composites were less biodegradable. The amount and rate of cell release from cell-encapsulated PCL-based capsules were positively dependent on the biodegradability and on the decrease in the mechanical strength. Nevertheless, the pattern of cell release was quite similar for all types of capsules. The outcome of this work seems to suggest that by proper manipulation of composite compositions, the controlled release of the bacterial fertilizer (i.e., Bacillus sp. PG01 cells) might be achievable.