recent-advances-in-methods-for-analyzing-lipids-and-fatty-acids

Recent Advances in Methods for Analyzing Lipids and Fatty Acids

ARTICLES DISCUSSED:
Parrish, C. C., Wells, J. S. Determination of total lipid and lipid classes in marine samples. Journal of Visualized Experiments. ...

Jiangnan University

The two homologous genes GPD1 and GPD2, encoding two isoenzymes of NAD(+)-dependent glycerol-3-phosphate dehydrogenase in industrial yeast Saccharomyces cerevisiae CICIMY0086, had been deleted. The obtained two kinds of mutants gpd1Delta and gpd2Delta were studied under alcoholic fermentation conditions. gpd1Delta mutants exhibited a 4.29% (relative to the amount of substrate consumed) decrease in glycerol production and 6.83% (relative to the amount of substrate consumed) increased ethanol yield while gpd2Delta mutants exhibited a 7.95% (relative to the amount of substrate consumed) decrease in glycerol production and 7.41% (relative to the amount of substrate consumed) increased ethanol yield compared with the parental strain. The growth rate of the two mutants were slightly lower than that of the wild type under the exponential phase whereas ANG1 (gpd1Delta) and the decrease in glycerol production was not accompanied by any decline in the protein content of the strain ANG1 (gpd1Delta) but a slight decrease in the strain ANG2 (gpd2Delta). Meanwhile, dramatic decrease of acetate acid formation was observed in strain ANG1 (gpd1Delta) and ANG2 (gpd2Delta) compared to the parental strain. Therefore, it is possible to improve the ethanol yield by interruption of glycerol pathway in industrial alcoholic yeast.

Interruption of glycerol pathway in industrial alcoholic yeasts to improve the ethanol production.

The yeasts used in fuel ethanol manufacture are unable to metabolize soluble proteins. The PEP4 gene, encoding a vacuolar aspartyl protease in Saccharomyces cerevisiae, was either secretively or cell-surface anchored expressed in industrial ethanol-producing S. cerevisiae. The obtained recombinant strains APA (expressing the protease secretively) and APB (expressing the protease on the cell wall) were studied under ethanol fermentation conditions in feed barley cultures. The effects of expression of the protease on product formation, growth and cell protein content were measured. The biomass yield of the wild-type was clearly lower than that of the recombinant strains (0.578 ± 0.12 g biomass/g glucose for APA and 0.582 ± 0.08 g biomass/g glucose for APB). In addition, nearly 98-99% of the theoretical maximum level of ethanol yield was achieved (relative to the amount of substrate consumed) for the recombinant strains, while limiting the nitrogen source resulted in dissatisfactory fermentation for the wild-type and more than 30 g/l residual sugar was detected at the end of fermentation. In addition, higher growth rate, viability and lower yields of byproducts such as glycerol and pyruvic acid for recombinant strains were observed. Expressing acid protease can be expected to lead to a significant increase in ethanol productivity.

Improving the performance of industrial ethanol-producing yeast by expressing the aspartyl protease on the cell surface.

The GPD2 gene, encoding NAD(+)-dependent glycerol-3-phosphate dehydrogenase in an industrial ethanol-producing strain of Saccharomyces cerevisiae, was deleted. And then, either the non-phosphorylating NADP(+)-dependent glyceraldehyde-3-phosphate dehydrogenase (GAPN) from Bacillus cereus, or the NADP(+)-dependent glyceraldehyde-3-phosphate dehydrogenase (GAPDH) from Kluyveromyces lactis, was expressed in the obtained mutant AG2 deletion of GPD2, respectively. The resultant recombinant strain AG2A (gpd2Δ P (PGK)-gapN) exhibited a 48.70 ± 0.34% (relative to the amount of substrate consumed) decrease in glycerol production and a 7.60 ± 0.12% (relative to the amount of substrate consumed) increase in ethanol yield, while recombinant AG2B (gpd2Δ P (PGK)-GAPDH) exhibited a 52.90 ± 0.45% (relative to the amount of substrate consumed) decrease in glycerol production and a 7.34 ± 0.15% (relative to the amount of substrate consumed) increase in ethanol yield compared with the wild-type strain. More importantly, the maximum specific growth rates (μ (max)) of the recombinant AG2A and AG2B were higher than that of the mutant gpd2Δ and were indistinguishable compared with the wild-type strain in anaerobic batch fermentations. The results indicated that the redox imbalance of the mutant could be partially solved by expressing the heterologous genes.

Improving ethanol productivity by modification of glycolytic redox factor generation in glycerol-3-phosphate dehydrogenase mutants of an industrial ethanol yeast.

To synthesize glycerol, a major by-product during anaerobic production of ethanol, the yeast Saccharomyces cerevisiae would consume up to 4% of the sugar feedstock in typical industrial ethanol processes. The present study was dedicated to decreasing the glycerol production mostly in industrial ethanol producing yeast without affecting its desirable fermentation properties including high osmotic and ethanol tolerance, natural robustness in industrial processes. In the present study, the GPD1 gene, encoding NAD+-dependent glycerol-3-phosphate dehydrogenase in an industrial ethanol producing strain of S. cerevisiae, was deleted. Simultaneously, a non-phosphorylating NADP+-dependent glyceraldehyde-3-phosphate dehydrogenase (GAPN) from Bacillus cereus was expressed in the mutant deletion of GPD1. Although the resultant strain AG1A (gpd1△ P(PGK)-gapN) exhibited a 48.7±0.3% (relative to the amount of substrate consumed) lower glycerol yield and a 7.6±0.1% (relative to the amount of substrate consumed) higher ethanol yield compared to the wild-type strain, it was sensitive to osmotic stress and failed to ferment on 25% glucose. However, when trehalose synthesis genes TPS1 and TPS2 were over-expressed in the above recombinant strain AG1A, its high osmotic stress tolerance was not only restored but also improved. In addition, this new recombinant yeast strain displayed further reduced glycerol yield, indistinguishable maximum specific growth rate (μ(max)) and fermentation ability compared to the wild type in anaerobic batch fermentations. This study provides a promising strategy to improve ethanol yields by minimization of glycerol production.

Minimization of glycerol synthesis in industrial ethanol yeast without influencing its fermentation performance.

To increase ethanol yield and decrease glycerol production in Saccharomyces cerevisiae, the strategies of direct cofactor-regulation were explored. During anaerobic batch fermentations, the yeast expressing Bacillus cereus gapN gene, encoding non-phosphorylating NADP(+)-dependent glyceraldehyde-3-phosphate dehydrognease, produced 73.8 g ethanol l(-1), corresponding to 96% of theoretical maximum yield compared to 92% for the wild type. The yeast expressing Escherichia coli frdA gene encoding the NAD(+)-dependent fumarate reductase, exhibited a 22% (relative to the amount of substrate consumed) increase in glycerol yield in medium containing 2 g fumarate l(-1). The yeast expressing mhpF gene, encoding acetylating NAD(+)-dependent acetaldehyde dehydrogenase, produced 74.5 g ethanol l(-1), corresponding to 97.4% of theoretical maximum yield while glycerol decreased by 40% when acetic acid was added before inoculation. This strain represents a promising alternative for ethanol production with lignocellulosic hydrolysates where acetate is available at significant amounts.

Improving the ethanol yield by reducing glycerol formation using cofactor regulation in Saccharomyces cerevisiae.

The BGL1 gene, encoding β-glucosidase in Saccharomycopsis fibuligera, was intracellular, secreted or cell-wall associated expressed in an industrial strain of Saccharomyces cerevisiae. The obtained recombinant strains were studied under aerobic and anaerobic conditions. The results indicated that both the wild type and recombinant strain expressing intracellular β-glucosidase cannot grow in medium using cellobiose as sole carbon source. As for the recombinant EB1 expressing secreted enzyme and WB1 expressing cell-wall associated enzyme, the maximum specific growth rates (μ(max)) could reach 0.03 and 0.05 h(-1) under anaerobic conditions, respectively. Meanwhile, the surface-engineered S. cerevisiae utilized 5.2 g cellobioseL(-1) and produced 2.3 g ethanol L(-1) in 48 h, while S. cerevisiae secreting β-glucosidase into culture broth used 3.6 g cellobiose L(-1) and produced 1.5 g ethanolL(-1) over the same period, but no-full depletion of cellobiose were observed for both the used recombinant strains. The results suggest that S. cerevisiae used in industrial ethanol production is deficient in cellobiose transporter. However, when β-glucoside permease and β-glucosidase were co-expressed in this strain, it could uptake cellobiose and showed higher growth rate (0.11h(-1)) on cellobiose.

Development of an industrial ethanol-producing yeast strain for efficient utilization of cellobiose.

In order to further improve the utilization rate of raw materials and increase ethanol productivity, the gene Asp, encoding aspartic protease in Neurospora crassa was cloned and expressed in industrial ethanol-producing yeast. To promote secretion of the acid protease, the gene was fused to signal sequence of the yeast α-factor gene and constitutively expressed under transcriptional control of the Saccharomyces cerevisiae PGK1 promoter. The resultant recombinant enzyme was characterized with respect to pH and temperature optimum. Then, this acid protease was anchored to the yeast cell wall by fusing the mature protein to the α-agglutinin peptides. The resultant strain was evaluated in clarifying corn mash and very high gravity (VHG) raw starch fermentation. The present results demonstrated that expression of the acid protease increased both growth rate and viable yeast counts and the recombinant strain of S. cerevisiae exhibited a higher ethanol yield as compared to the parent strain.

Expression of aspartic protease from Neurospora crassa in industrial ethanol-producing yeast and its application in ethanol production.

Glycerol is a major by-product of industrial ethanol production and its formation consumes up to 4 % of the sugar substrate. This study modified the glycerol decomposition pathway of an industrial strain of Saccharomyces cerevisiae to optimize the consumption of substrate and yield of ethanol. This study is the first to couple glycerol degradation with ethanol formation, to the best of our knowledge. The recombinant strain overexpressing GCY1 and DAK1, encoding glycerol dehydrogenase and dihydroxyacetone kinase, respectively, in glycerol degradation pathway, exhibited a moderate increase in ethanol yield (2.9 %) and decrease in glycerol yield (24.9 %) compared to the wild type with the initial glucose concentration of 15 % under anaerobic conditions. However, when the mhpF gene, encoding acetylating NAD⁺-dependent acetaldehyde dehydrogenase from Escherichia coli, was co-expressed in the aforementioned recombinant strain, a further increase in ethanol yield by 5.5 % and decrease in glycerol yield by 48 % were observed for the resultant recombinant strain GDMS1 when acetic acid was added into the medium prior to inoculation compared to the wild type. The process outlined in this study which enhances glycerol consumption and cofactor regulation in an industrial yeast is a promising metabolic engineering strategy to increase ethanol production by reducing the formation of glycerol.

Zhongpeng Guo

National Engineering Research Center of Cereal Fermentation and Food Biomanufacturing

Jiangnan University

Recent Advances in Methods for Analyzing Lipids and Fatty Acids