Robust counterselection and advanced λRed recombineering enable markerless chromosomal integration of large heterologous constructs.

Despite advances in bacterial genome engineering, delivery of large synthetic constructs remains challenging in practice. In this study, we propose a straightforward and robust approach for the markerless integration of DNA fragments encoding whole metabolic pathways into the genome. This approach relies on the replacement of a counterselection marker with cargo DNA cassettes via λRed recombineering. We employed a counterselection strategy involving a genetic circuit based on the CI repressor of λ phage. Our design ensures elimination of most spontaneous mutants, and thus provides a counterselection stringency close to the maximum possible. We improved the efficiency of integrating long PCR-generated cassettes by exploiting the Ocr antirestriction function of T7 phage, which completely prevents degradation of unmethylated DNA by restriction endonucleases in wild-type bacteria. The employment of highly restrictive counterselection and ocr-assisted λRed recombineering allowed markerless integration of operon-sized cassettes into arbitrary genomic loci of four enterobacterial species with an efficiency of 50-100%. In the case of Escherichia coli, our strategy ensures simple combination of markerless mutations in a single strain via P1 transduction. Overall, the proposed approach can serve as a general tool for synthetic biology and metabolic engineering in a range of bacterial hosts.

Engineering Yarrowia lipolytica for the selective and high-level production of isocitric acid through manipulation of mitochondrial dicarboxylate-tricarboxylate carriers.

During cultivation under nitrogen starvation, Yarrowia lipolytica produces a mixture of citric acid and isocitric acid whose ratio is mainly determined by the carbon source used. We report that mitochondrial succinate-fumarate carrier YlSfc1 controls isocitric acid efflux from mitochondria. YlSfc1 purified and reconstituted into liposomes transports succinate, fumarate, oxaloacetate, isocitrate and α-ketoglutarate. YlSFC1 overexpression determined the inversion of isocitric acid/citric acid ratio towards isocitric acid, resulting in 33.4 ± 1.9 g/L and 43.3 ± 2.8 g/L of ICA production in test-tube cultivation with glucose and glycerol, respectively. These titers represent a 4.0 and 6.3-fold increase compared to the wild type. YlSFC1 gene expression was repressed in the wild type strain grown in glucose-based medium compared to olive oil medium explaining the reason for the preferred citric acid production during Y. lipolytica growth on carbohydrates. Coexpression of YlSFC1 and adenosine monophosphate deaminase YlAMPD genes together with inactivation of citrate mitochondrial carrier YlYHM2 gene enhanced isocitric acid accumulation up to 41.4 ± 4.1 g/L with an isocitric acid/citric acid ratio of 14.3 in a small-scale cultivation with glucose as a carbon source. During large-scale cultivation with glucose pulse-feeding, the engineered strain produced 136.7 ± 2.5 g/L of ICA with a process selectivity of 88.1%, the highest reported titer and selectivity to date. These results represent the first reported isocitric acid secretion by Y. lipolytica as a main organic acid during cultivation on carbohydrate. Moreover, we demonstrate for the first time that the replacement of one mitochondrial transport system for another can be an efficient tool for switching product accumulation.

The mitochondrial citrate carrier in Yarrowia lipolytica: Its identification, characterization and functional significance for the production of citric acid.

Mitochondrial citrate carrier plays a central role in exporting acetyl-CoA in the form of citrate from mitochondria to cytosol thereby connecting carbohydrate catabolism and lipogenesis. In this study, Yarrowia lipolytica mitochondrial citrate carrier was functionally defined and characterized. Firstly, deletion of Y. lipolytica YlCTP1 and YlYHM2 genes coding putative tricarboxylate mitochondrial carriers were performed. ΔYlctp1 strain did not differ significantly from wild type strain in terms of growth rate, organic acids and lipid production. In contrast, ΔYlyhm2 strain did not grow in liquid citrate-containing minimal medium. Moreover, in glucose-containing lipogenic medium YlYHM2 null mutant strain did not produce citric acid; the production of isocitric acid and lipids were decreased. Reintroduction of YlYHM2 gene as well as heterologous expression of Aspergillus niger gene AnYHM2 into ΔYlyhm2 strain restored the growth in minimal citrate medium and even enhanced citric acid production by 45% in both variants compared with wild type strain during test tube cultivation. Mitochondrial extracts isolated from YlYHM2 null mutant and wild type strain were incorporated into liposomes; citrate/citrate and α-ketoglutarate/α-ketoglutarate homoexchange activities were reduced by 87% and 40% in ΔYlyhm2 strain, respectively, compared with the wild type, whereas citratein/α-ketoglutarateout and α-ketoglutaratein/citrateout heteroexchanges were decreased by 87% and 95%, respectively. YlYhm2p was expressed in Escherichia coli, purified and reconstituted into liposomes. Besides high efficiency to citrate and α-ketoglutarate transport, YlYhm2p also transported oxaloacetate, succinate, fumarate, and to a much lesser extent, aconitate, malate, isocitrate, oxoadipate, and glutamate. The activity of reconstituted YlYhm2p was inhibited strongly by SH-blocking reagents, pyridoxal-5'-phosphate, and partly by N-ethylmaleimide. Co-expression of YlYHM2 and adenosine monophosphate deaminase YlAMPD genes resulted in the production of 49.7 g/L of citric acid during test tube cultivation, whereas wild type strain accumulated 30.1 g/L of citric acid. Large-scale cultivation in bioreactor of the engineered strain resulted in 97.1 g/L of citric acid production with a process selectivity of 94.2% and an overall citric acid yield of 0.5 g/g. The maximal specific rate of citric acid synthesis was 0.93 g/L/h. Therefore, the physiological role of YlYhm2p in glucose-containing medium is to catalyze both import of citrate into mitochondria for catabolic reactions and export of citrate as a source of acetyl-CoA from mitochondria. Possible shuttles for citrate exporting are discussed. Moreover, for the first time evidence has been given for the improvement of TCA cycle intermediate production by manipulation of a gene coding a mitochondrial carrier.

A metabolic engineering strategy for producing free fatty acids by the Yarrowia lipolytica yeast based on impairment of glycerol metabolism.

In recent years, bio-based production of free fatty acids from renewable resources has attracted attention for their potential as precursors for the production of biofuels and biochemicals. In this study, the oleaginous yeast Yarrowia lipolytica was engineered to produce free fatty acids by eliminating glycerol metabolism. Free fatty acid production was monitored under lipogenic conditions with glycerol as a limiting factor. Firstly, the strain W29 (Δgpd1), which is deficient in glycerol synthesis, was obtained. However, W29 (Δgpd1) showed decreased biomass accumulation and glucose consumption in lipogenic medium containing a limiting supply of glycerol. Analysis of substrate utilization from a mixture of glucose and glycerol by the parental strain W29 revealed that glycerol was metabolized first and glucose utilization was suppressed. Thus, the Δgpd1Δgut2 double mutant, which is deficient also in glycerol catabolism, was constructed. In this genetic background, growth was repressed by glycerol. Oleate toxicity was observed in the Δgpd1Δgut2Δpex10 triple mutant strain which is deficient additionally in peroxisome biogenesis. Consequently, two consecutive rounds of selection of spontaneous mutants were performed. A mutant released from growth repression by glycerol was able to produce 136.8 mg L-1 of free fatty acids in a test tube, whereas the wild type accumulated only 30.2 mg L-1 . Next, an isolated oleate-resistant strain produced 382.8 mg L-1 of free fatty acids. Finely, acyl-CoA carboxylase gene (ACC1) over-expression resulted to production of 1436.7 mg L-1 of free fatty acids. The addition of dodecane promoted free fatty acid secretion and enhanced the level of free fatty acids up to 2033.8 mg L-1 during test tube cultivation.

Metabolic evolution and (13) C flux analysis of a succinate dehydrogenase deficient strain of Yarrowia lipolytica.

Bio-based succinic acid production can redirect industrial chemistry processes from using limited hydrocarbons to renewable carbohydrates. A fermentation process that does not require pH-titrating agents will be advantageous to the industry. Previously, a Yarrowia lipolytica strain that was defective for succinate dehydrogenase was constructed and was found to accumulate up to 17.5 g L(-1) of succinic acid when grown on glycerol without buffering. Here, a derivative mutant was isolated that produced 40.5 g L(-1) of succinic acid in 36 h with a yield of 0.32 g g(-1) glycerol. A combination approach of induced mutagenesis and metabolic evolution allowed isolation of another derivative that could utilize glucose efficiently and accumulated 50.2 g L(-1) succinic acid in 54 h with a yield of 0.43 g g(-1) . The parent strain of these isolated mutants was used for [1,6-(13) C2 ]glucose assimilation analysis. At least 35% glucose was estimated to be utilized through the pentose phosphate pathway, while ≥84% succinic acid was formed through the oxidative branch of the tricarboxylic acid cycle. Biotechnol. Bioeng. 2016;113: 2425-2432. © 2016 Wiley Periodicals, Inc.

Boosting Geranyl Diphosphate Synthesis for Linalool Production in Engineered Yarrowia lipolytica.

Linalool is a pleasant-smelling monoterpenoid widely found in the essential oils of most flowers. Due to its biologically active properties, linalool has considerable commercial potential, especially in the food and perfume industries. In this study, the oleaginous yeast Yarrowia lipolytica was successfully engineered to produce linalool de novo. The (S)-linalool synthase (LIS) gene from Actinidia argute was overexpressed to convert geranyl diphosphate (GPP) into linalool. Flux was diverted from farnesyl diphosphate (FPP) synthesis to GPP by introducing a mutated copy of the native ERG20F88W-N119W gene, and CrGPPS gene from Catharanthus roseus on its own and as part of a fusion with LIS. Disruption of native diacylglycerol kinase enzyme, DGK1, by oligo-mediated CRISPR-Cas9 inactivation further increased linalool production. The resulting strain accumulated 109.6 mg/L of linalool during cultivation in shake flasks with sucrose as a carbon source. CrGPPS expression in Yarrowia lipolytica increased linalool accumulation more efficiently than the ERG20F88W-N119W expression, suggesting that the increase in linalool production was predominantly influenced by the level of GPP precursor supply.

A DNA assembly toolkit to unlock the CRISPR/Cas9 potential for metabolic engineering.

CRISPR/Cas9-based technologies are revolutionising the way we engineer microbial cells. One of the key advantages of CRISPR in strain design is that it enables chromosomal integration of marker-free DNA, eliminating laborious and often inefficient marker recovery procedures. Despite the benefits, assembling CRISPR/Cas9 editing systems is still not a straightforward process, which may prevent its use and applications. In this work, we have identified some of the main limitations of current Cas9 toolkits and designed improvements with the goal of making CRISPR technologies easier to access and implement. These include 1) A system to quickly switch between marker-free and marker-based integration constructs using both a Cre-expressing and standard Escherichia coli strains, 2) the ability to redirect multigene integration cassettes into alternative genomic loci via Golden Gate-based exchange of homology arms, 3) a rapid, simple in-vivo method to assembly guide RNA sequences via recombineering between Cas9-helper plasmids and single oligonucleotides. We combine these methodologies with well-established technologies into a comprehensive toolkit for efficient metabolic engineering using CRISPR/Cas9. As a proof of concept, we developed the YaliCraft toolkit for Yarrowia lipolytica, which is composed of a basic set of 147 plasmids and 7 modules with different purposes. We used the toolkit to generate and characterize a library of 137 promoters and to build a de novo strain synthetizing 373.8 mg/L homogentisic acid.

A study on L-threonine and L-serine uptake in Escherichia coli K-12.

In the current study, we report the identification and characterization of the yifK gene product as a novel amino acid carrier in E. coli K-12 cells. Both phenotypic and biochemical analyses showed that YifK acts as a permease specific to L-threonine and, to a lesser extent, L-serine. An assay of the effect of uncouplers and composition of the reaction medium on the transport activity indicates that YifK utilizes a proton motive force to energize substrate uptake. To identify the remaining threonine carriers, we screened a genomic library prepared from the yifK-mutant strain and found that brnQ acts as a multicopy suppressor of the threonine transport defect caused by yifK disruption. Our results indicate that BrnQ is directly involved in threonine uptake as a low-affinity but high-flux transporter, which forms the main entry point when the threonine concentration in the external environment reaches a toxic level. By abolishing YifK and BrnQ activity, we unmasked and quantified the threonine transport activity of the LIV-I branched chain amino acid transport system and demonstrated that LIV-I contributes significantly to total threonine uptake. However, this contribution is likely smaller than that of YifK. We also observed the serine transport activity of LIV-I, which was much lower compared with that of the dedicated SdaC carrier, indicating that LIV-I plays a minor role in the serine uptake. Overall, these findings allow us to propose a comprehensive model of the threonine/serine uptake subsystem in E. coli cells.

Production of recombinant Rhizopus oryzae lipase by the yeast Yarrowia lipolytica results in increased enzymatic thermostability.

The gene encoding Rhizopus oryzae lipase (ROL) was expressed in the non-conventional yeast Yarrowia lipolytica under the control of the strong inducible XPR2 gene promoter. The effects of three different preprosequence variants were examined: a preprosequence of the Y. lipolytica alkaline extracellular protease (AEP) encoded by XPR2, the native preprosequence of ROL, and a hybrid variant of the presequence of AEP and the prosequence of ROL. Lipase production was highest (7.6 U/mL) with the hybrid prepropeptide. The recombinant protein was purified by ion-exchange chromatography. The ROL included 28 amino acids of the C-terminal region of the prosequence, indicating that proteolytic cleavage occurred below the KR site through the activity of the Kex2-like endoprotease. The optimum temperature for recombinant lipase activity was between 30 and 40 °C, and the optimum pH was 7.5. The enzyme was shown not to be glycosylated. Furthermore, recombinant ROL exhibited greater thermostability than previously reported, with the enzyme retaining 64% of its hydrolytic activity after 30 min of incubation at 55 °C.

Efficient cell surface display of Lip2 lipase using C-domains of glycosylphosphatidylinositol-anchored cell wall proteins of Yarrowia lipolytica.

The cell surface display of enzymes is of great interest because of its simplified purification stage and the possibility for recycling in industrial processes. In this study, we have focused on the cell wall immobilization of Yarrowia lipolytica Lip2 protein--an enzyme that has a wide technological application. By genome analysis of Y. lipolytica in addition to already characterized Ylcwp1, we identified five putative open reading frames encoding glycosylphosphatidylinositol-anchored proteins. Lip2 translation fusion with the carboxyl termini of these proteins revealed that all proteins were capable of immobilizing lipase in active form on the cell surface. The highest level of cell-bound lipase activity was achieved using C-domains encoded by YlCWP1, YlCWP3 (YALI0D27214g) and YlCWP6 (YALI0F18282g) comprising 16,173 ± 1,800, 18,785 ± 1,130 and 17,700 ± 2,101 U/g dry cells, respectively. To the best of our knowledge, these results significantly exceed the highest cell-bound lipase activity previously reported for engineered Saccharomyces cerevisiae and Pichia pastoris strains. Furthermore, the lyophilized biomass retained the activity and was robust to collecting/resuspending procedures. Nevertheless, in most cases, a substantial amount of lipase activity was also found in the growth medium. Further work will be necessary to better understand the nature of this phenomenon.

Production of succinic acid at low pH by a recombinant strain of the aerobic yeast Yarrowia lipolytica.

Biotechnological production of weak organic acids such as succinic acid is most economically advantageous when carried out at low pH. Among naturally occurring microorganisms, several bacterial strains are known to produce considerable amounts of succinic acid under anaerobic conditions but they are inefficient in performing the low-pH fermentation due to their physiological properties. We have proposed therefore a new strategy for construction of an aerobic eukaryotic producer on the basis of the yeast Yarrowia lipolytica with a deletion in the gene coding one of succinate dehydrogenase subunits. Firstly, an original in vitro mutagenesis-based approach was proposed to construct strains with Ts mutations in the Y. lipolytica SDH1 gene. These mutants were used to optimize the composition of the media for selection of transformants with the deletion in the Y. lipolytica SDH2 gene. Surprisingly, the defects of each succinate dehydrogenase subunit prevented the growth on glucose but the mutant strains grew on glycerol and produced succinate in the presence of the buffering agent CaCO(3). Subsequent selection of the strain with deleted SDH2 gene for increased viability allowed us to obtain a strain capable of accumulating succinate at the level of more than 45 g L(-1) in shaking flasks with buffering and more than 17 g L(-1) without buffering. The possible effect of the mutations on the utilization of different substrates and perspectives of constructing an industrial producer is discussed.

Excision of selectable markers from the Escherichia coli genome without counterselection using an optimized λRed recombineering procedure.

The introduction of chromosomal mutations into the E. coli genome using λRed-mediated recombineering includes two consecutive steps-the insertion of an antibiotic resistance gene and the subsequent excision of the marker. The second step usually requires a counterselection method, because the efficiency of recombination is not high enough to find recombinants among non-recombinant cells. Most counterselection methods require the introduction of additional mutations into the genome or the use of expensive chemicals. In this paper, we describe the development of a reliable procedure for the removal of an antibiotic resistance marker from the E. coli genome without the need for counterselection. For this purpose, we used dsDNA cassettes consisting of two regions homologous to the sequences that flank the marker on the chromosome. We optimized the length of the homologous regions, the electroporation conditions, and the duration of recovery for the electroporated cells in order to maximize the recombination efficiency. Using the optimal parameters identified, we obtained a rate of 4-6% recombinants among the transformed cells. This high efficiency allowed us to find marker-less, antibiotic-sensitive recombinants by replica plating without the need for selection.

Development of new versatile plasmid-based systems for λRed-mediated Escherichia coli genome engineering.

Plasmid-based systems are the most appropriate for multistep lambda Red (λRed)-mediated recombineering, such as the assembly of strains for biotechnological applications. Currently, the widely used λRed-expressing plasmids use a temperature-sensitive origin of replication or temperature shift control of λRed expression. In this work, we have constructed a new, conditionally replicating vector that can be efficiently eliminated from the host strain through passaging in medium containing isopropyl-ß-d-thiogalactopyranoside. Using the new vector, we have developed two improved helper plasmids (viz., pDL17 and pDL14) for dsDNA and oligonucleotide-mediated recombineering, respectively. The plasmid pDL14 contains a dominant negative mutSK622A allele that suppresses methyl-directed mismatch repair (MMR). The coexpression of λRed and mutSK622A provides efficient oligonucleotide-mediated recombineering in the presence of active host MMR. The expression of λRed was placed under the control of the tightly regulated PrhaB promoter. Because of their low expression level under uninduced conditions, both plasmids could be maintained without elimination for multiple recombineering steps. The temperature-independent replication of the plasmids and control of λRed expression by l-rhamnose allow for all procedures to be performed at 37 °C. Thus, the new plasmids are robust, convenient, and versatile tools for Escherichia coli genome editing.

Co-expression of glucose-6-phosphate dehydrogenase and acyl-CoA binding protein enhances lipid accumulation in the yeast Yarrowia lipolytica.

The oleaginous yeast Yarrowia lipolytica is a convenient model for investigating lipid biosynthesis and for engineering high lipid accumulated strains. In this organism, the pentose phosphate pathway is the major source of NADPH for lipid biosynthesis. Thus, we over-expressed gene encoding NADP+-dependent glucose-6-phosphate dehydrogenase (ZWF1) in a strain deficient in peroxisome biogenesis. However, this strategy suppressed growth during cultivation under lipogenic conditions and did not significantly increase lipid accumulation. Remarkably, co-expression of gene encoding acyl-CoA binding protein (ACBP), which functions as an intracellular acyl-CoA transporter and acyl-CoA-pool former, restored growth. Co-expression of ZWF1 and ACBP increased the lipid content to 30% of dry cell weight via de novo lipid synthesis. In comparison to wild type, the engineered strain accumulated 41% more lipids with a higher ratio of saturated to unsaturated fatty acids.

Repetitive genomic sequences as a substrate for homologous integration in the Rhizopus oryzae genome.

The vast number of repetitive genomic elements was identified in the genome of Rhizopus oryzae. Such genomic repeats can be used as homologous regions for integration of plasmids. Here, we evaluated the use of two different repeats: the short (575 bp) rptZ, widely distributed (about 34 copies per genome) and the long (2053 bp) rptH, less prevalent (about 15 copies). The plasmid carrying rptZ integrated, but did so through a 2256-bp region of homology to the pyrG locus, a unique genomic sequence. Thus, the length of rptZ was below the minimal requirements for homologous strand exchange in this fungus. In contrast, rptH was used efficiently for homologous integration. The plasmid bearing this repeat integrated in multicopy fashion, with up to 25 copies arranged in tandem. The latter vector, pPyrG-H, could be a valuable tool for integration at homologous sequences, for such purposes as high-level expression of proteins.

Cell surface display of Yarrowia lipolytica lipase Lip2p using the cell wall protein YlPir1p, its characterization, and application as a whole-cell biocatalyst.

The Yarrowia lipolytica lipase Lip2p was displayed on the yeast cell surface via N-terminal fusion variant using cell wall protein YlPir1p. The hydrolytic activity of the lipase displayed on Y. lipolytica cells reached 11,900 U/g of dry weight. However, leakage of enzyme from the cell wall was observed. The calculated number of recombinant enzyme displayed on the cell surface corresponds to approximately 6 × 10(5) molecules per cell, which is close to the theoretical maximum (2 × 10(6) molecules/cell). Furthermore, the leaking enzyme was presented as three N-glycosylated proteins, one of which corresponds to the whole hybrid protein. Thus, we attribute the enzyme leakage to the limited space available on the cell surface. Nevertheless, the surface-displayed lipase exhibited greater stability to short-term and long-term temperature treatment than the native enzyme. Cell-bound lipase retained 74 % of its original activity at 60 °C for 5 min of incubation, and 83 % of original activity after incubation at 50 °C during 5 h. Cell-bound lipase had also higher stability in organic solvents and detergents. The developed whole-cell biocatalyst was used for recycling biodiesel synthesis. Two repeated cycles of methanolysis yielded 84.1 and 71.0 % methyl esters after 33- and 45-h reactions, respectively.

Is it possible to produce succinic acid at a low pH?

Bio-based succinate is still a matter of special emphasis in biotechnology and adjacent research areas. The vast majority of natural and engineered producers are bacterial strains that accumulate succinate under anaerobic conditions. Recently, we succeeded in obtaining an aerobic yeast strain capable of producing succinic acid at low pH. Herein, we discuss some difficulties and advantages of microbial pathways producing "succinic acid" rather than "succinate." It was concluded that the peculiar properties of the constructed yeast strain could be clarified in view of a distorted energy balance. There is evidence that in an acidic environment, the majority of the cellular energy available as ATP will be spent for proton and anion efflux. The decreased ATP:ADP ratio could essentially reduce the growth rate or even completely inhibit growth. In the same way, the preference of this elaborated strain for certain carbon sources could be explained in terms of energy balance. Nevertheless, the opportunity to exclude alkali and mineral acid waste from microbial succinate production seems environmentally friendly and cost-effective.