| Literature DB >> 25103914 |
Ceyda Kasavi, Serpil Eraslan, Kazim Yalcin Arga, Ebru Toksoy Oner, Betul Kirdar1.
Abstract
BACKGROUND: Saccharomyces cerevisiae has been widely used for bio-ethanol production and development of rational genetic engineering strategies leading both to the improvement of productivity and ethanol tolerance is very important for cost-effective bio-ethanol production. Studies on the identification of the genes that are up- or down-regulated in the presence of ethanol indicated that the genes may be involved to protect the cells against ethanol stress, but not necessarily required for ethanol tolerance.Entities:
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Year: 2014 PMID: 25103914 PMCID: PMC4236716 DOI: 10.1186/s12918-014-0090-6
Source DB: PubMed Journal: BMC Syst Biol ISSN: 1752-0509
Core proteins of the network
| CTP synthase isozyme | [ | |
| Cysteine aminopeptidase | [ | |
| Endocytic protein | [ | |
| Elongase I (fatty acid elongation) | [ | |
| Trehalose-6-phosphate synthase | [ | |
| Transcriptional activator | [ | |
| 2-deoxyglucose-6-phosphate phosphatase | [ | |
| Cytoplasmic protein involved in halotolerance | [ | |
| Inositol-3-phosphate synthase | [ | |
| Delta(9) fatty acid desaturase | [ | |
| Cytochrome b5 | [ | |
| Repression of flocculation-related gene | [ | |
| Heat shock protein | [ | |
| Involved in RNA metabolism | [ |
Figure 1Schematic illustration of the network reconstruction algorithm, SPA.
Yeast strains used in this study
| ydr307wΔ/ydr307wΔ | BY4743; Mat a/α; his3Δ 1/his3Δ 1; leu2Δ 0/leu2Δ 0; lys2Δ 0/LYS2; MET15/met15Δ 0; ura3Δ 0/ura3Δ 0; YDR307w::kanMX4/YDR307w::kanMX4 |
| yhl042wΔ/yhl042wΔ | BY4743; Mat a/α; his3Δ 1/his3Δ 1; leu2Δ 0/leu2Δ 0; lys2Δ 0/LYS2; MET15/met15Δ 0; ura3Δ 0/ura3Δ 0; YHL042w::kanMX4/YHL042w::kanMX4 |
| ymr215wΔ/ymr215wΔ | BY4743; Mat a/α; his3Δ 1/his3Δ 1; leu2Δ 0/leu2Δ 0; lys2Δ 0/LYS2; MET15/ met15Δ 0; ura3Δ 0/ura3Δ 0; YMR215w::kanMX4/YMR215w::kanMX4 |
| ypl264cΔ/ypl264cΔ | BY4743; Mat a/α; his3Δ 1/his3Δ 1; leu2Δ 0/leu2Δ 0; lys2Δ 0/LYS2; MET15/ met15Δ 0; ura3Δ 0/ura3Δ 0; YPL264c::kanMX4/YPL264c::kanMX4 |
Figure 2Viability ofstrains after 8% (v/v) ethanol treatment. The error bars denote the standard deviations of the two biological and two technical replicates.
Comparison of fermentation parameters of strains
| Final DCW (g/L) | 5.462 | 5.458 | 5.457 |
| Max. ethanol conc. (g/L)* | 6.59 | 6.15 | 7.14 |
| Total glucose utilized (g/L) | 18.46 | 18.36 | 18.46 |
| μmax (h−1) | 0.453 | 0.454 | 0.451 |
| Yps (g ethanol/g glucose)* | 0.357 | 0.335 | 0.387 |
| Ypx (g ethanol/g biomass) | 1.207 | 1.127 | 1.308 |
(*) indicates significantly different (p-value < 0.005) fermentation parameters of mutants when compared to the wild type strain.
Figure 3Extracellular glucose and ethanol concentrations. Consumption of glucose (filled symbols) and production of ethanol (open symbols) by the wild type (■,□), ydr307wΔ/ydr307wΔ (●,○) and yhl042wΔ/yhl042wΔ (▲,Δ) strains.
Figure 4Heat map representation and enriched GO biological process terms. The heat map representation of the genes, which were significantly and differentially expressed in response to gene deletion; and the enriched GO biological process terms (p-value < 0.01) among the up- and down-regulated genes.
Figure 5Survival curves ofstrains. The error bars denote the standard deviations of the two biological and two technical replicates.