The development of sustainable replacements for fossil fuels has been spurred by concerns over global warming effects. Biofuels are typically produced through fermentation of edible crops, or forest or agricultural residues requiring cost-intensive pretreatment. An alternative is to use photosynthetic cyanobacteria to directly convert CO2 and sunlight into fuel. In this thesis, the cyanobacterium Synechocystis sp. PCC 6803 was genetically engineered to produce the biofuel n­-butanol. Several metabolic engineering strategies were explored with the aim to increase butanol titers and tolerance. In papers I-II, different driving forces for n-butanol production were evaluated. Expression of a phosphoketolase increased acetyl-CoA levels and subsequently butanol titers. Attempts to increase the NADH pool further improved titers to 100 mg/L in four days. In paper III, enzymes were co-localized onto a scaffold to aid intermediate channeling. The scaffold was tested on a farnesene and polyhydroxybutyrate (PHB) pathway in yeast and in E. coli, respectively, and could be extended to cyanobacteria. Enzyme co-localization increased farnesene titers by 120%. Additionally, fusion of scaffold-recognizing proteins to the enzymes improved farnesene and PHB production by 20% and 300%, respectively, even in the absence of scaffold. In paper IV, the gene repression technology CRISPRi was implemented in Synechocystis to enable parallel repression of multiple genes. CRISPRi allowed 50-95% repression of four genes simultaneously. The method will be valuable for repression of competing pathways to butanol synthesis. Butanol becomes toxic at high concentrations, impeding growth and thus limiting titers. In papers V-VI, butanol tolerance was increased by overexpressing a heat shock protein or a stress-related sigma factor. Taken together, this thesis demonstrates several strategies to improve butanol production from cyanobacteria. The strategies could ultimately be combined to increase titers further.

Biocatalysis involves the use of enzymes to perform stereo- and enantio-specific reactions. One of the reactions where biocatalysis is a valuable technology is oxidation of naphthalene to 1-naphthol using Toluene ortho-Monooxygenase (TOM) variant TmoA3 V106A, also known as TOM-Green. Whole-cell biocatalysis in a water-organic solvent biphasic system was used to minimize naphthalene and 1-naphthol toxicity, and to increase substrate loading. Recombinant Escherichia coli TG1 cells expressing TOM-Green were used for biphasic biocatalysis and lauryl acetate gave best results among the solvents tested. On a constant volume basis, 8 - fold improvement in 1-naphthol production was achieved using biphasic systems compared to biotransformation in aqueous medium. The organic phase was optimized by studying the effects of organic phase ratio and naphthalene concentration in the organic phase. The efficiency of biocatalysis was further improved by application of a solvent tolerant strain Pseudomonas putida S12. P. putida S12 is solvent tolerant owing to its two adaptive mechanisms: outer membrane modification and solvent extrusion using solvent resistant pump srpABC. P. putida S12, in addition to its tolerance to various organic solvents, showed better tolerance to naphthalene compared to E. coli TG1 strain expressing TOM-Green. Application of solvent tolerant P. putida S12 further improved 1-naphthol productivity by approximately 42%. Solvent tolerance of P. putida S12 was further analyzed by transferring its tolerance to a solvent sensitive E. coli strain by transfer of solvent resistant pump srpABC genes. Engineered E. coli strain bearing srpABC genes either in low-copy number plasmid or high-copy number plasmid grew in the presence of a saturated toluene concentration. Engineered E. coli strains were also more tolerant to toxic solvents, e. g., decanol and hexane, compared to the control E. coli strain without srpABC genes. The expression of solvent resistant pump genes was confirmed by Reverse Transcriptase PCR analysis. The main drawbacks of biocatalysis for production of chemicals were addressed and approaches to minimize the drawbacks have been presented. The production of 1-naphthol was significantly improved using biocatalysis in liquid-liquid biphasic systems.

京都大学 / 0048 / 新制・課程博士 / 博士(農学) / 甲第18326号 / 農博第2051号 / 新制||農||1022(附属図書館) / 学位論文||H26||N4833(農学部図書室) / 31184 / 京都大学大学院農学研究科応用生命科学専攻 / (主査)教授 植田 充美, 教授 喜多 恵子, 教授 栗原 達夫 / 学位規則第4条第1項該当 / Doctor of Agricultural Science / Kyoto University / DFAM