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Metabolic engineering of polyploid Saccharomyces cerevisiae for production of ethanol and 2,3-butanediol : 대사공학적으로 재설계된 산업용 효모를 이용한 에탄올과 2,3-부탄다이올의 생산

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dc.contributor.advisor서진호-
dc.contributor.author이예지-
dc.date.accessioned2018-11-12T00:58:11Z-
dc.date.available2021-04-13T01:09:37Z-
dc.date.issued2018-08-
dc.identifier.other000000152361-
dc.identifier.urihttps://hdl.handle.net/10371/143183-
dc.description학위논문 (박사)-- 서울대학교 대학원 : 농업생명과학대학 농생명공학부, 2018. 8. 서진호.-
dc.description.abstractIndustrial polyploid Saccharomyces cerevisiae is a versatile yeast strain for large-scale fermentations due to rapid growth rate, high sugar consumption rate and high tolerance to ethanol and inhibitors. Despite these advantageous traits, however, industrial strains have not been widely used and studied as a host for genetic and metabolic engineering because of some drawbacks including aneuploidy or polyploidy, unstable mating-type and no auxotrophic markers. Generally, the desired phenotypes of industrial strains have been obtained through random mutagenesis or evolutionary adaptation rather than rational genetic engineering. This thesis has focused on using an industrial JHS200 strain as a host for metabolic engineering approaches in order to produce ethanol and 2,3-butanediol with high productivity and yield.

First of all, an industrial strain of S. cerevisiae JHS200 that was isolated from Korean Nuruk and identified to be a polyploidy (4n) was characterized for fermentation properties. The industrial JHS200 strain showed a higher maximum specific growth rate (0.547 hr-1) than haploid S. cerevisiae strains such as CEN.PK2-1D (0.452 hr-1), D452-2 (0.445 hr-1), L2612 (0.413 hr-1) and BY4742 (0.478 hr-1). In addition, the JHS200 exhibited superior properties in terms of sugar consumption rate, ethanol tolerance and resistance to fermentation inhibitors. For further metabolic engineering, the auxotrophic mutants of polyploidy JHS200 were constructed with the modified Clustered Regularly Interspaced Short Palindromic Repeats (CRISPR)-Cas9 genome editing tool. A stop codon (TAA) was introduced into the middle of each gene (URA3, TRP1, HIS3, LEU2) through a point mutation. Finally, four auxotrophic mutants of the polyploidy JHS200 (JHS200ura-, JHS200ura-trp-, JHS200ura-trp-his-, JHS200ura-trp-his-leu-) were constructed to possess single or multiple auxotrophic traits. The auxotrophic mutants kept the excellent fermentation properties without significant growth defects.

Second, in order to produce cellulosic ethanol, the xylose-assimilating pathway was introduced into the auxotrophic industrial strain. Plasmid pRS306_XYL123 harboring the genes coding for xylose reductase (XR), xylitol dehydrogenase (XDH) and xylulokinase (XK) from Scheffersomyces stipitis with strong and constitutive promoters was integrated into the JHS200ura-trp- strain, in which the URA3 and TRP1genes were previously disrupted. The resulting strain of JX123 produced 45.6 g/L ethanol with 0.73 g/L·hr of xylose consumption rate. As 7.25 g/L of xylitol accumulated as a major by-product in the JX123 strain, the heterologous noxE gene from Lactococcus lactis which reduces surplus intracellular NADH generated from the xylose metabolism was additionally introduced. As a result, the JX123_noxE strain expressing the noxE gene produced 47.0 g/L ethanol with decreased xylitol accumulation (2.26 g/L). Additionally, the JX123_noxE strain was successfully cultivated by using silver grass hydrolysates as a sole carbon source. It produced 55.5 g/L ethanol with 1.63 g/L·hr of productivity and 0.43 g/g of yield from lignocellulose hydrolysates. Even both furfural and HMF inhibitors were present in the hydrolysates, the engineered JX123_noxE industrial strain showed a high xylose consumption rate of 0.90 g/L·hr.

Third, the auxotrophic polyploidy strain (JHS200ura-trp-his-leu-, 4-JHS200) was used to produce 2,3-butanediol (2,3-BDO). In order to block the production of ethanol as a major metabolite, the genes coding for pyruvate decarboxylase (PDC) and alcohol dehydrogenase (ADH) were partially disrupted through the CRISPR-Cas9 method. To overcome the growth defect caused by complete deletion of all isozymes encoded by the PDC and ADH genes, a strategy of partial disruption of PDC1, PDC6 or ADH1 was employed to engineer the 4-JHS200 strain. The biosynthetic pathway of 2,3-BDO was introduced by transformation of plasmid p413_SDB harboring the genes coding for α-acetolactate synthase (alsS) and α-acetolactate decarboxylase (alsD) from Bacillus subtilis and 2,3-butanediol dehydrogenase (BDH1) from S. cerevisiae. And the heterologous NADH oxidase (noxE) from L. lactis was additionally expressed for modulating redox balance. The resulting strain of YG01_SDBN was able to produce 178.6 g/L of 2,3-BDO with a maximum productivity of 2.64 g/L·hr. In an optimized fermentation using cassava hydrolysates as carbon sources, 132.7 g/L of 2,3-BDO was produced with a productivity of 1.92 g/L·hr. On the other hand, glycerol accumulation in the 2,3-BDO-producing strains causes several problems such as low yield of 2,3-BDO and high cost of separation. To increase 2,3-BDO yield by elimination of glycerol accumulation, the genes coding for glycerol-3-phosphate dehydrogenase (GPD1 and GPD2) in the glycerol synthetic pathway were disrupted in the YG01_SDBN strain. As excess NADH was oxidized by NoxE with an aid of oxygen molecule in the host strain, the Gpd-deficient polyploid strain (YG01_SDBN_dGPD1GPD2) could be obtained without severe redox imbalance. The YG01_SDBN_dGPD1GPD2 strain lost a glycerol producing ability completely, and hence produced 151.5 g/L of 2,3-BDO with 0.41 g/g yield. Additionally, this strain could produce 120.6 g/L of 2,3-BDO with 0.42 g/g yield using the cassava hydrolysates. The maximum 2,3-BDO yield in this optimized fed-batch fermentations using cassava hydrolysates was comparable to those for engineered bacterial systems.

In conclusion, the polyploidy yeast of S. cerevisiae JHS200 was metabolically engineered by using the CRISPR-Cas9 genome editing tool. The engineered JHS200 variant with auxotrophic markers and various genes affecting metabolic phenotypes could produce ethanol and 2,3-BDO with high productivity, yield and concentration in optimized fed-batch fermentation processes. The engineered polyploid yeast strains could be used as a platform for economic production of valuable chemicals from various carbohydrate hydrolysates.
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dc.description.tableofcontentsCONTENTS



Chapter 1



Literature review 1

1.1. Necessity of an industrial strain research 2

1.2. Significant features of industrial S. cerevisiae 5

1.3. Genetic manipulation of industrial S. cerevisiae 10

1.4. CRISPR-Cas9 genome editing in S. cerevisiae 16

1.5. Ethanol production in industrial S. cerevisiae 21

1.6. 2,3-Butanediol production from biomass 22

1.7. Objectives of the dissertation 24



Chapter 2



Identification of industrial S. cerevisiae JHS200 30

2.1. Summary 31

2.2. Introduction 32

2.3. Materials and method 33

2.4. Results and discussion 40

2.4.1. Species identification of the industrial strain by ITS region

sequencing 40

2.4.2. Determination of the mating type and ploidy of industrial strain JHS200 40

2.4.3. Characterization of fermentation parameters 42

2.4.3.1. Growth rate 42

2.4.3.2. High and low density of inoculum cell 43

2.4.3.3. Ethanol tolerance 45

2.4.3.4. Tolerance of the fermentation inhibitors from lignocellulosic

hydrolysates 46

2.5. Conclusions 48



Chapter 3



Genetic manipulation of polyploid JHS200 strain by CRISPR-Cas9 system 62

3.1. Summary 63

3.2. Introduction 65

3.3. Materials and method 70

3.4. Results and discussion 74

3.4.1. Construction of auxotrophic mutants 74

3.4.2. Fermentation of auxotrophic mutants 75

3.4.3. Maintenance of advantageous traits in auxotrophic mutants 76

3.5. Conclusions 78



Chapter 4



Bioethanol production from cellulosic hydrolysates by engineered

polyploid JHS200 strain 89

4.1. Summary 90

4.2. Introduction 91

4.3. Materials and methods 95

4.4. Results and discussion 101

4.4.1. Introduction of a xylose-assimilating pathway into the JHS200

strain 101

4.4.2. Optimization of xylose fermenting JHS200 to reduce xylitol 102

4.4.3. Cellulosic hydrolysates fermentation by engineered yeast strains

based on laboratory and industrial yeast strains 105

4.5. Conclusions 108



Chapter 5



Production of 2,3-butanediol by engineered industrial JHS200 strain 120

5.1. Summary 121

5.2. Introduction 123

5.3. Materials and methods 128

5.4. Results and discussion 136

5.4.1. Construction of the non-ethanologenic yeast strain 136

5.4.2. Introduction of 2,3-BDO pathway to non-ethanologenic yeast

strains 141

5.4.3. Relieve of cellular redox imbalance by over-expressed NADH

oxidase 143

5.4.4. Disruption of GPD1 and GPD2 for eliminating glycerol

accumulation 145

5.4.5. Development of cassava hydrolysate fermentation in a fermentor

148

5.5. Conclusions 152



CONCLUSIONS 175



References 180



국문 초록 206





LIST OF TABLES

Table 1-1. Ethanol production from biomass in the industrial S. cerevisiae wild-type or mutant strains. 25

Table 1-2. Microbial 2,3-butanediol production from industrial biomass 26

Table 2-1. Strains and primers used in Chapter 2 50

Table 2-2. Comparison of specific growth rates for yeast strains. Strains marked with asterisk are industrial yeast strains 51

Table 3-1. Strains and plasmids used in Chapter 3 80

Table 3-2. Primers used in this study. Bold and capital characters are restriction enzyme sites. 82

Table 4-1. Strains and plasmids used in Chapter 4 109

Table 4-2. Fermentation parameters of the genetically modified S. cerevisiae strains in bench-top fermentor with lignocellulose hydrolysates 110

Table 5-1. Strains and plasmids used in Chapter 5 155

Table 5-2. Primers used in Chapter 5 157

Table 5-3. Synthesis of the guideRNA-expressing cassettes used in Chapter 5 160

Table 5-4. Summary of the flask culture with the engineered industrial yeast strains 162

Table 5-5. Summary of fed-batch fermentations with the YP medium in a fermentor 163

Table 5-6. Summary of fed-batch fermentations with a cassava hydrolysate in a fermentor 164



LIST OF FIGURES

Figure 1-1. (A) Mechanisms of CRISPR-Cas9 system described by Type I, II and III (B) Cas9 protein interacted with guide RNA. 29

Figure 2-1. Identification of the industrial JHS200 strain. (A) Schematic diagram of ribosomal DNA showing the ITS (internal transcribed spacer) regions. The annealing sites for the universal primers (ITS1 and ITS4) are marked as arrows. (B) Phylogenetic tree of Saccharomyces genus including JHS200 strain. (C) Amplification of MAT locus in the JHS200, D452-2, BJ3505 strains by PCR 52

Figure 2-2. FACS analysis of (A) the industrial JHS200 strain and (B) the laboratory CEN.PK2-1D strain for ploidy determination. 54

Figure 2-3. Comparison of industrial and laboratory strains by cell growth. 55

Figure 2-4. Fermentation profiles of (A) JHS200 and (B) CEN.PK2-1D strains with high cell density of inoculum. (initial OD600=10) 56

Figure 2-5. Fermentation profiles of (A) JHS200 and (B) CEN.PK2-1D strains with very high concentration of glucose 57

Figure 2-6. Fermentation profiles of (A) JHS200 and (B) CEN.PK2-1D strains with low cell density of inoculum. (initial OD600=0.1) 58

Figure 2-7. Cell viability assay with the CEN.PK2-1D and JHS200 strains in (A) YP medium with 10 % ethanol and (B) YP medium with 15 % ethanol. 59

Figure 2-8. Fermentation profiles of (A) JHS200 and (B) CEN.PK2-1D strains with 100 g/L ethanol 60

Figure 2-9. Fermentation profiles of (A) JHS200 and (B) CEN.PK2-1D strains with 1.2 g/L furfural 61

Figure 3-1. Sequence alignment of auxotrophic mutants compared with reference sequences of S288C strain 84

Figure 3-2. Fermentation by a prototroph and auxotrophic mutants of the JHS200 strain in the YPD medium containing 50 g/L glucose
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dc.language.isoen-
dc.publisher서울대학교 대학원-
dc.subject.ddc630-
dc.titleMetabolic engineering of polyploid Saccharomyces cerevisiae for production of ethanol and 2,3-butanediol-
dc.title.alternative대사공학적으로 재설계된 산업용 효모를 이용한 에탄올과 2,3-부탄다이올의 생산-
dc.typeThesis-
dc.contributor.AlternativeAuthorLEE Ye-Gi-
dc.description.degreeDoctor-
dc.contributor.affiliation농업생명과학대학 농생명공학부-
dc.date.awarded2018-08-
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