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.
Transposons are mobile genetic elements that are part of the genomic DNA of numerous organisms and belong to two classes. Unlike class I transposons, class II DNA transposons do not use the stage of RNA synthesis in their transition; they perform it by the cut-and-paste mechanism or with a replicative transposition. The integration of a DNA transposon in a new site results in the duplication of a target sequence on either side of a transposon, and its excision is, as a rule, associated with insertions and deletions. The piggyBac transposon isolated from the Trichoplusia ni moth differs from other mobile elements of its class. Due to its unique ability to leave no traces after excision from an insertion site and to perform successful transposition and transference of large DNA fragments, piggyBac is a convenient tool for the development of gene engineering approaches. The TTAA sequence serves as a target site for transposon integration: insertion in the AT-rich DNA regions is more frequent. The ability of piggyBac to be transferred to a new area independently of the cell apparatus and to restore a DNA site without error after excision lies in the mechanism of its transposition, which is discussed in detail in the present review. Along with other transposons and viruses, the piggyBac transposon is widely used in the transgenesis of various organisms; it also finds application in insertion mutagenesis and gene therapy.
ABSTRACTBio‐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 [1,6‐13C2]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.
The yeast Yarrowia lipolytica is capable of high-intensity synthesis (overproduction) of citric (CA) and isocitric (ICA) acids under nitrogen limitation. The ratio of the synthesized acids depends on the producing strains used and the expression level of the aconitate hydratase gene (ACO1). Recombinant variants with overexpression of the multicopy ACO1 gene have been obtained based on the natural ICA-producing strain Y. lipolytica 672. A recombinant strain Y. lipolytica 20, which has an isocitrate-citrate ratio shifted towards ICA (2.3: 1) as compared to the parental strain (1.1: 1), has been selected. Culturing of the 20 variant in a 10 L reactor has resulted in the production of 72.6 g/L of ICA and 29.0 g/L of CA with a ratio of 2.5: 1. This makes it possible to regard Y. lipolytica 20 as a promising producer for the development of an industrial process for isocitrate production.
We studied the biosynthesis of isocitric acid from rapeseed (canola) oil by the yeast Yarrowia lipolytica and its regulation. We determined a fundamental possibility for directed biosynthesis of isocitric acid by Y. lipolytica yeast, with only minimal amounts of citric acid byproduct, when grown on a medium containing canola oil. Wild type strains of Y. lipolytica were mutagenized by UV irradiation and treatment with N-methyl-N′-nitro-N-nitrosoguanidine (NG). Subsequent selection on media with acetate and isocitrate resulted in isolation of a mutant Y. lipolytica UV/NG that synthesized isocitrate and citrate at a ratio of 2.7 : 1. In the parent strain, this ratio is 1 : 1. Inhibition of isocitrate lyase, a key enzyme in the metabolism of isocitric acid, by the addition of itaconic acid resulted in increased synthesis of isocitrate, with a ratio of isocitrate to citrate reaching 6 : 1. The cultivation of the Y. lipolytica UV/NG mutant in a pilot industrial fermenter in the presence of itaconic acid resulted in the production of 88.7 g/L of isocitric acid with a yield of 90%.
We studied the biosynthesis of isocitric acid from rapeseed (canola) oil by the yeast Yarrowia lipolytica and its regulation. We determined a fundamental possibility for directed biosynthesis of isocitric acid by Y lipolytica yeast, with only minimal amounts of citric acid byproduct, when grown on a medium containing canola oil. Wild type strains of Y lipolytica were mutagenized by UV irradiation and treatment with N-methyl-N'-nitro-N-nitrosoguanidine (NG). Subsequent selection on media with acetate and isocitrate resulted in isolation of a UV/NG Y lipolytica UV/NG mutant that synthesized isocitrate and citrate at a ratio of 2.7:1. In the parent strain, this ratio is 1:1. Inhibition of isocitrate lyase, a key enzyme in the metabolism of isocitric acid, by the addition of itaconic acid resulted in increased synthesis of isocitrate with a ratio of isocitrate to citrate reaching 6:1. Culturing of the Y lipolytica UV/NG mutant in a pilot industrial fermenter in the presence of itaconic acid resulted in the production of 88.7 g/L of isocitric acid with a yield of 90%.
Изучен биосинтез изолимонной кислоты из рапсового масла дрожжами Yarrowia lipolytica и его регуляция. Установлена принципиальная возможность направленного биосинтеза дрожжами Y. lipolytica изолимонной кислоты с минимальным содержанием побочного продукта лимонной кислоты на среде, содержащей рапсовое масло. В результате УФ-облучения и обработки N-метил-N-нитро-N-нитрозогуанидином (НГ) природных штаммов Y. lipolytica и последующей селекции на средах с ацетатом и изоцитратом получен мутант Y. lipolytica УФ/НГ, который синтезировал изоцитрат и цитрат в соотношении 2.7 : 1, в отличие от исходного штамма, у которого это соотношение 1 : 1. Показано, что ингибирование изоцитрат-лиазы ключевого фермента метаболизма изолимонной кислоты, итаконовой кислотой приводило к увеличению синтеза изоцитрата до соотношения изоцитрат : цитрат 6 : 1. При выращивании мутанта Y. lipolytica УФ/НГ в полупромышленном ферментере в присутствии итаконовой кислоты синтезировалось 88.7 г/л изолимонной кислоты с выходом 90%.
The marine environment offers both economic and scientific potential which are relatively untapped from a biotechnological point of view. These environments whilst harsh are ironically fragile and dependent on a harmonious life form balance. Exploitation of natural resources by exhaustive wild harvesting has obvious negative environmental consequences. From a European industry perspective marine organisms are a largely underutilised resource. This is not due to lack of interest but due to a lack of choice the industry faces for cost competitive, sustainable and environmentally conscientious product alternatives. Knowledge of the biotechnological potential of marine organisms together with the development of sustainable systems for their cultivation, processing and utilisation are essential. In 2010, the European Commission recognised this need and funded a collaborative RTD/SME project under the Framework 7-Knowledge Based Bio-Economy (KBBE) Theme 2 Programme 'Sustainable culture of marine microorganisms, algae and/or invertebrates for high value added products'. The scope of that project entitled 'Sustainable Production of Biologically Active Molecules of Marine Based Origin' (BAMMBO) is outlined. Although the Union is a global leader in many technologies, it faces increasing competition from traditional rivals and emerging economies alike and must therefore improve its innovation performance. For this reason innovation is placed at the heart of a European Horizon 2020 Strategy wherein the challenge is to connect economic performance to eco performance. This article provides a synopsis of the research activities of the BAMMBO project as they fit within the wider scope of sustainable environmentally conscientious marine resource exploitation for high-value biomolecules.
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.
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.
The closest homologue of the Saccharomyces cerevisiae Flo1p cell wall protein was detected in Yarrowia lipolytica yeast (YALI0C09031p) by the method of genomic analysis, and capacity of its N- and C-domains to expose the Lip2 lipase on the cell surface was studied. The efficient fixation of the enzyme on the Y. lipolytica cell wall surface was demonstrated. The activity of the cell-bound lipase was 9170 and 3200 units per 1 g of dry solid matter when using N- and C-domains of the cell wall protein, respectively. At the same time, in the case of immobilization using the N-domain, approximately 30% of the total lipase activity was detected in the culture medium, whereas when using C-domain of the cell wall protein YALI0C09031p, practically all lipase was in the immobilized state. Obtained values of the level of the cell-bound lipase activity considerably exceed previously published data opening a prospect for new technological solutions which meet industrial needs.
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.
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 CaCO3. 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. Biotechnol. Bioeng. 2010;107:673–682. © 2010 Wiley Periodicals, Inc.