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Biomass Enhancement in Chlamydomonas reinhardtii using Steady C/N Ratio Microfluidic Perfusion Bioreactor, Vibrational Stress Priming, and Malate Synthase Expression : 미세유체 관류 배양기의 C/N 비율 유지, 진동 자극 프라이밍, 말릭산 합성 효소의 발현을 통한 Chlamydomonas reinhardtii의 생체량 증대

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dc.contributor.advisor전누리-
dc.contributor.author백상민-
dc.date.accessioned2018-11-12T00:54:28Z-
dc.date.available2018-11-12T00:54:28Z-
dc.date.issued2018-08-
dc.identifier.other000000151852-
dc.identifier.urihttps://hdl.handle.net/10371/143026-
dc.description학위논문 (박사)-- 서울대학교 대학원 : 공과대학 협동과정 바이오엔지니어링전공, 2018. 8. 전누리.-
dc.description.abstractMicroalgae, a photosynthetic microorganism, has recently attracted attention as an effective resource for both renewable energy and food security. This is because sequestration of more CO2 and composition of more nutrition than terrestrial plants help microalgae mitigate climate change and secure food shortage in the future. Therefore, efficient process operation on microalgae cultivation is of importance. In this dissertation, three strategies were developed and applied to enhance microalgal biomass productivity with less time and cost at large-scale.

The first one is cultivation with steady unbalanced C/N ratio. Microalgae-derived secondary metabolites include antioxidants (lutein, astaxanthin, etc) and neutral lipids (TAG), most of which are useful substances. These substances are produced in cells cultivated in a nutrient-depleted environment. In order to improve total productivity, increase in microalgal biomass should be accompanied well with increase in intracellular content. Thus, traditional nutrient depletion method can no longer be viable drastically constraining cellular growth. Recently, cultivation with unbalanced C/N ratio has been reported to increase biomass at a certain level simultaneously with TAG content increase. However, because batch process also has depleted nutrient over time, this method has the same limitations for enhancement of total products yield as traditional methods. In this study, continued supply of low concentrations of nutrients with the maintenance of unbalanced C/N ratio was proposed to enhance secondary metabolites production A microfluidic continuous perfusion system was designed and tested to culture microalgae, Chlamydomonas reinhardtii, under constant nutrient concentration slightly lower than normal condition with high C/N ratio. When cultured in 7.5%/7.5% of NH4+ /PO42-, C. reinhardtii showed a 2.4-fold increase in TAG production with a 3.5-fold increase in biomass compared to level obtained under an only NH4+ depleted condition. This is because nutrients continue to be supplied in small quantities without depletion of nutrients. Maintaining the unbalanced C/N ratio can improve the total TAG productivity by increasing the biomass.

The second is cellular stress response preparedness against turbulence in bioreactors. Turbulence agitates all the nutritional components for cellular proliferation. However, severe hydrodynamic shear fields by the turbulence decreases cell viability that detrimentally influence maximum yieldable biomass. Vibrational wave treatment has been used to increase proliferation of microalgae. When directly applied at large scale, however, it costs much setting up massive vibration generating system, and turbulence can offset positive effects of vibration on microalgae proliferation. Stress priming is the phenomenon that primed cells with activated stress response by milder stress can prepare themselves for harsh stress and exhibit greater survival rate. In this study, vibration pretreatment (between 10–30 Hz and 0.15–0.45 G) was used to prime the cells for enhanced biomass. When exposed to 10 Hz at 0.15 G for 72 h and inoculated in baffled flasks of large shear fields (0.292 Pa for the average wall shear force (aveWSF) and 184 s−1 for the average shear strain rate (aveSSR)), microalgae showed 27% increase in biomass as well as 39% increase in corresponding amount of heterologous protein (i.e. GFP-3HA). The level of TRP11 transcript was increased both at vibration treatment and at shaking cultivation. Ca2+-signaling pathway closely relates with stress response. In plants, calmodulin (CaM)-binding transcription factor (CAMTA) is involved in expression of CBF/CREB1 master transcriptional regulator under stressful conditions. Although Ca2+-signaling pathway in Chlamydomonas has not yet been studied in detail, our results show that stress primed microalgae with vibrations can lead to improved proliferation that results in increased biomass production at industrial scale bioprocesses.

Last but not at least, cellular metabolism itself could be additionally activated by malate. Malate has a close relation to biomass increase. High uptake of malate leads to biomass increase, reducing non-growth associated coefficient (maintenance energy). In addition, in plants, efficient distribution of intracellular malate to organelles was also elucidated to relate to biomass. Redox balance, especially in chloroplast, is carried out with reducing equivalents such as NADPH. Because its pool should be tightly regulated to maintain its capacity, intermediate metabolite, malate, play a role as an high potential energy carrier without disturbing reducing equivalents pool, and the malate is exported to other organelles. In this study, transgenic Chlamydomonas expressing malate synthase in chloroplast was developed. Stable expression of malate synthase enables malate production in chloroplast and distribution of more malate could be carried out in the transgenic cells. Transgenic Chlamydomonas under glyoxylate treatment showed 19% more increase in microalgal biomass than wild-type. By RNA analysis, the levels of malate dehydrogenase (MDH4) in TCA cycle, acetyl-CoA synthetase (ACS3), and isocitrate lyase (ICL1) and malate synthase (MAS1) of glyoxylate shunt, were significantly more expressed, which was consistent with reported metabolic flux analysis of heterotrophic cultivated cells. More meticulous analysis are necessary, but, in the transgenic microalgae with malate synthase overexpression, the metabolism is likely to more rely on energy production via TCA cycle and glyoxylate cycle than on photosynthesis, resulting in increase in microalgal biomass.
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dc.description.tableofcontentsCONTENTS

Abstract i

Contents vi

List of Figures x

List of Tables xii

List of Abbreviations xiii



Chapter 1. Research Background and Objective 1



Chapter 2. Literature Review 5



2.1 Earthcare with Sustainable Development Goals (SDGs) 6

2.1.1 Global Warming 6

2.1.2 Population Increase and Food Insecurity 7

2.1.3 Plant-Based Food for Sustainable Development Goals (SDGs) 7

2.2 Microalgae 10

2.2.1 Microalgae as Food Resource 10

2.2.2 Microalgae Cultivation Process 10

2.2.3 Chlamydomonas reinhardtii 15

2.3 Metabolic Engineering in Chlamydomonas reinhardtii 18

2.3.1 Advantageous Transgenic Microalgae over Other Chemotrophic Microbes 18

2.3.2 Chloroplast Transformation 19

2.3.3 Metabolic Engineering for Improving the Microalgal Biomass 30

2.3.3.1 Reduction of Antenna Size 30

2.3.3.2 NPQ (Non-Photochemical Quenching) Deactivation 30

2.3.3.3 Metabolism Manipulation 31

2.4 Mechanotransduction in Chlamydomonas reinhardtii and its Application 34

2.4.1 Ca2+ Signalling Mechanisms in Plants 34

2.4.2 Mechanotransduction in Chlamydomonas reinhardtii 37

2.4.3 Mechanical Stimulus for Biomass Increase 39

2.5 Triacylglycerol (TAG) Production in Chlamydomonas reinhardtii 41

2.5.1 Potential Triacylglycerol (TAG) Following Transesterification 41

2.5.2 Lipid Synthesis Molecular Mechanism 44

2.5.3 Genetic Engineering of Lipid Metabolism 48

2.5.4 Economic Triacylglycerol (TAG) Production 55



Chapter 3. Microfluidic Perfusion Bioreactor with Steady High C/N Ratio for Optimization of Microalgal Lipid Productivity 58



3.1 Introduction 59

3.2 Materials and Methods 62

3.2.1 Fabrication of Microfluidic Perfusion Bioreactor 62

3.2.2 Microalgae Cultivation 63

3.2.3 Triacylglycerol (TAG) Staining and Fluorescent Microscopy 65

3.3 Results and Discussion 68

3.3.1 Characteristics of Microfluidic Perfusion Bioreactor 68

3.3.2 Synergetic Effect of Phosphate Depletion 71

3.3.3 Effect of Low Concentrations of NH4+ and PO42- 74

3.4 Conclusions 79



Chapter 4. Vibration-Induced Stress Priming During Seed Culture to Increase Microalgal Biomass in High Shear Field-Cultivation 80



4.1 Introduction 81

4.2 Materials and Methods 85

4.2.1 Microalgae Cultivation 85

4.2.2 Baffled Flask 86

4.2.3 RNA preparation and Analysis 86

4.2.4 CFD Simulation for the Shear Force Analysis 87

4.2.5 Construction of the GFP-expressing Strain 92

4.2.6 Sampling 93

4.2.6.1 Biomass Measurement 94

4.2.6.2 Protein preparation and Western Blot Analysis 94

4.3 Results and Discussion 96

4.3.1 Microalgal Stress Responses to Mechanical Stimulus with Vibrational Frequencies 96

4.3.2 Microalgal Stress Responses to Mechanical Stimulus with Vibrational Magnitudes 99

4.3.3 Shear Strain Rate (SSR) and Wall Shear Force (WSF) in Baffled Flasks 102

4.3.4 Priming Effects on Microalgal Biomass and Corresponding Productivity 106

4.4 Conclusions 112



Chapter 5. Chloroplastic Malate Synthase Expression for Microalgal Growth by Upregulating TCA cycle 113



5.1 Introduction 114

5.2 Materials and Methods 117

5.2.1 Construction of the Expression Vectors for the Transformations 117

5.2.1.1 Recombinant Plasmid for E.coli Transformation 117

5.2.1.2 Recombinant Plasmid for Chlamydomonas Chloroplast Transformation 117

5.2.2 Protein Purification 121

5.2.3 in vitro Malate Synthase Activity Test 123

5.2.4 Particle Bombardment 123

5.2.5 PCR for Screening Transformants 124

5.2.6 Southern Blot 124

5.2.7 Chloroplastic Malate Synthase Expression Test 125

5.2.8 Transgenic Microalgae Cultivation and Measurement of Cell Number and Biomass 125

5.2.9 RNA Preparation and Analysis 126

5.2.10 PAM (Pulse-Amplitude-Modifier) Measurement 126

5.3 Results and Discussion 128

5.3.1 in vitro Recombinant Malate Synthase Activity 128

5.3.2 Analysis of Chloroplast Transgenic Microalgae Expressing Malate Synthase 130

5.3.3 Malate Synthase Changes the Parameters of Microalgal Growth 137

5.3.4 Malate-related Transcripts Changes Under Glyoxylate Treatment 140

5.3.5 Acetate-related Transcripts Changes Under Glyoxylate Treatment 143

5.4 Conclusions 145



Chapter 6. Overall Conclusion 146



Bibliography 149

Abstract in Korean 166
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dc.language.isoen-
dc.publisher서울대학교 대학원-
dc.subject.ddc660.6-
dc.titleBiomass Enhancement in Chlamydomonas reinhardtii using Steady C/N Ratio Microfluidic Perfusion Bioreactor, Vibrational Stress Priming, and Malate Synthase Expression-
dc.title.alternative미세유체 관류 배양기의 C/N 비율 유지, 진동 자극 프라이밍, 말릭산 합성 효소의 발현을 통한 Chlamydomonas reinhardtii의 생체량 증대-
dc.typeThesis-
dc.contributor.AlternativeAuthorSang-Min Paik-
dc.description.degreeDoctor-
dc.contributor.affiliation공과대학 협동과정 바이오엔지니어링전공-
dc.date.awarded2018-08-
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