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                                               <li><a href="https://2021.igem.org/Team:SCUT-China/Integrated">Integrated Human Practices</a></li>
 
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               <li style="font-size:26px;"><a class="a_nav">proposed implementation</a></li>
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               <li style="font-size:26px;"><a class="a_nav">Improve</a></li>
 
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               <li><a >Instructions to Stakeholders</a></li>
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               <li ><a>Background</a></li>
                <li><a >Project Proposed Implementation</a></li>
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              <li><a >Design </a></li>
                 <li><a >Safety points to Consider</a></li>
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                 <li><a >Result</a></li>
 
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                     <h2  class="content_text_h2">Instructions to Stakeholders</h2>
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                     <h2  class="content_text_h2">Overview</h2>
 
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                         <p  >      In Integrated Human Practices we analyze the project's stakeholders from a variety of perspectives. Because different groups have different requests, we provide recommendations for project-related content here.                  </p>
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                         <p  >      We wanted to find efficient promoter elements in yeast to help us achieve yield increase. So we tested the strength of 14 promoters from different metabolic pathways. And the experiments showed that the intensity of PDC1(BBa_K2365033) was the highest among them. Although the intensity of PDC1 is high in the early stage of fermentation compared to other promoters, it decreases significantly in the middle and late stages. (Fig.1) Therefore, we hope to construct a more stable promoter with high activity.                   </p>
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                      <h4 class="content_text_h2" style="font-size:18px;margin-top:20px;">For Claimant Stakeholders</h4>
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                        <p  >      The instructions for the subsequent products in the project will be easy to follow. Because we want our mosquito repellent products to be available to as many people as possible, it is likely that the product will be designed to be used in a way that references the common sprays used today. This will only require following the conventional methods of using mosquito repellent sprays, such as spraying evenly and applying to the skin surface and avoiding sensitive areas.                 </p>
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                        <p  >      Although there is still a long way to go before the project can be successfully implemented and produced to benefit the public, there are some practical ideas in the project design and subsequent industrialization ideas that may give new inspirations to takeholders.                  </p>
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                        <h4 class="content_text_h2" style="font-size:18px;margin-top:20px;">For Collaborator Stakeholde</h4>
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                        <h4 class="content_text_h2" style="font-size:16px;margin-top:18px;">Upstream Fermentation Engineering Researchers: Strategy Selection and Regulation of Modified Strains</h4>
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                        <h4 class="content_text_h2" style="font-size:14px;margin-top:14px;">UP Strategy (UAS Promoter Strategy)</h4>
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                        <p  style="width:70%;float:left;">      In our project, we realized that the transcriptional intensity and characteristics of UAS would be different after hybrid promoters constructed with different insertion sites in the promoter sequence. The difference in affinity with nucleosomes at different positions of the promoter sequence may also be different, and this may be one of the reasons why UAS inserts at different sites may lead to differences in regulatory strength. The UAS in the tightly bound part of the nucleosome may reduce the probability of recognition and binding to the transcription factors due to, for example, site-block. Therefore, we constructed hybrid promoters by combining different UAS and inserting them into the genome to different positions to obtain more stable production efficiency.<br>Based on the validation of the production capacity of our engineered strains, we believe that adding or modifying the UAS of promoters is a set of design ideas worth promoting. To better illustrate how the hybrid promoter modification approach of our project should be used, we propose the UP Strategy (UAS Promoter strategy) to guide the use of the stakeholders.
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                            <img style="margin-right:-30px;width:100%;" src="https://static.igem.org/mediawiki/parts/e/ee/T--SCUT_China--Implementation-UP_strategy_flow_chart.jpg">
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                        <p style="font-size:14px;text-align:center;color:#A5A8A6;">DFig.1 UP strategy flow chart</p>
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                        <p  >      See more instructions on the UP Strategy in the pdf below!</p>
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                        <p >      In realistic implementation, our UP Strategy will likely bring new ideas to stakeholders in these areas.<br><br>1. Based on the UP Strategy, you can add or remove such as UAS, URS, and others from the promoter. In this way, you can combine eukaryotic hybrid promoter elements with different characteristics, including but not limited to extending the duration of highly active transcripts, or customizing regulation in response to specific signaling factors. And this can be applied not only in fermentation engineering modification, we believe that UP Strategy can bring new options in other fields as well.<br><br>2. obtaining insertion sites that are more likely to be suitable for gene expression. In eukaryotic gene expression, not only the transcription factors will recognize and bind to DNA. Therefore, we believe that the nucleosome affinity analysis in the UP Strategy can be used to screen for suitable insertion sites in eukaryotic exogenous gene introduction studies. <br><br>3. further improve the UP Strategy and design a more efficient strategy. Although theoretically genes located at nucleosomal affinity sites are more likely to be expressed, our experimental investigations have shown that some of the results of the actual transformation are not as predicted. This suggests that there is still room for improvement in UPS. We also expect that subsequent researchers will carry out new analysis of the influencing factors or improve the algorithm to build a better UP Strategy.</p>
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                        <h4 class="content_text_h2" style="font-size:14px;margin-top:14px;">More and Better Hybrid promoters for <i>S. cerevisiae</i></h4>
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                        <div class="content_div_text">
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                          <p  >      In our wet lab, we proposed a new idea to improve the yield of late fermentation according to the carbon source response mechanism of S. cerevisiae promoter. By combining the UAS related to different glucose metabolism pathways, we modified the natural constituent promoters into those with inductivity, which can be activated by yeast “diauxic shift”, so that VS can be expressed at a higher level for a longer period of time without additional inducers. Through our design and engineering, we ended up with a stronger promoter, M8, and a series of promoters with different intensities (Table. 1). With the very exciting results, we got in touch with the technicians at QR Pharmaceuticals. QR Pharmaceuticals is the first company in China to set foot in the biological synthesis of Nootkatone, with rich experience. After effective communication, we have clearly understood the application significance of our idea in industrial production and how factories can learn from our idea in the future: <br>(1) Compared with wild-type PPDC1, the M8 promoter we finally obtained significantly increased the yield of Vlencene, Nootkatol, Nootkatone, which provided a new idea for companies wanting to obtain higher Nootkatone yield. <br>(2) Through different combinations of UAS from different promoters, a series of hybrid promoters with different intensities and a wide dynamic range of promoter libraries can be used for fine regulation of metabolic pathways in S. cerevisiae to improve the yield of target products. <br>(3) The hybrid promoter obtained by our engineering success can be activated by “diauxic Shift” in yeast growth to maintain a good ability of initiation transcription, that is, it has certain "inductivity"., and do not need to add inducers. There are two advantages: one is to reduce unnecessary costs, the other is to reduce the toxicity to cells, both of which are of great significance in the factory application. <br>(4) Technicians mentioned that in practical production, they often need to balance the relationship between fermentation time and yield. There are many considerations, such as avoiding costs caused by excessively long fermentation time. But if the fermentation time is too short, the yield may not reach the target. And frequent tank changes can also be costly. So we extended the duration of the promoter's high strength, making it easier for technicians to find a balance between input and output.
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                          <p style="font-size:14px;text-align:center;">Table1.  Promoters with Different Intensities.</p>
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                          <p style="font-size:14px;text-align:center;color:#A5A8A6;">(Promoter strength has been defined as the relative production of nootkatone from a promoter.)</p>
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                         <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.1 a) Fermentation results-genome level LEU2::P-VS-T; b) Time curve of Valencene; c) Glucose, Ethanol concentration and Valencene production.</p>
                         <h4 class="content_text_h2" style="font-size:16px;margin-top:18px;">Upstream Fermentation Engineering Researchers: Strategy Selection and Regulation of Modified Strains</h4>
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                        <div class="content_div_text">
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                            <p  >      Surface-enhanced Raman spectroscopy is an advanced technique for characterizing the reaction process. Fermentation processes commonly require real-time online monitoring to automate the control of some environmental parameters. Commonly, dissolved oxygen, pH, temperature, etc. are measured by electrodes. When the computer monitors excessive fluctuation of a certain index, which exceeds the set optimum range, the machine will automatically control the fermenter for acid-base adjustment and temperature adjustment of hot & cold-water flow to keep it within the set range.<br><br>However, during the interview with QR pharmaceuticals, we learned that in fermentation factories nowadays, except for the common pH and temperature parameters which are detected by electrodes, the values of reducing sugars need to be sampled offline and detected manually. By using surface-enhanced Raman spectroscopy, it is possible to measure online in real time and get more realistic and accurate curves, so that special cases can be detected and handled faster. <br><br>In the interview with QR pharmaceuticals, the other side also pointed out that there are new instrument technologies for measuring dissolved oxygen and carbon dioxide. However, from the cost and applicability of the spread may not be common enough and the application method may have a relatively large deviation, the engineers will prefer to use the electrode detection equipment that is already popular and widely used. <br><br>It means that the new reaction analysis equipment like Surface-enhanced Raman spectroscopy needs to be more utilized and popularized in the market before it can be practically applied in fermentation plants. The small and medium-sized plants or laboratories that are in a position to do so can try to adopt it before the equipment is updated faster.                           </p>
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                       <h2  class="content_text_h2">Project Proposed Implementation</h2>
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                       <h2  class="content_text_h2">Design</h2>
 
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                       <p >We want to contribute to the solution of nootkatone production challenges. Therefore, our team of microbial fermentation innovators should also consider more. We should extend our focus from the laboratory to the subsequent industrialization process. The conversion rate of university research results is not high, and many projects lack feasibility in production. This problem may be due to the fact that the upstream design does not take into account the subsequent processes.<br>Therefore, it is necessary to analyze and design the subsequent industrialization process to help us better transform the project into real productivity.<br>For a more detailed design process, see in Integrated Human Practices
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                       <p>     We determine that the large decrease in intensity before and after PDC1 may be due to the low activation of PDC1 in response to the carbon source at the late stage of fermentation.
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Different UASs on each promoter give it the ability to respond to different carbon sources [1]. Therefore, we can recombine the UASs from different promoters to change promoters, making them adapt for different carbon sources and activate production in the diauxic shift automatically.
 
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                       <div class="content_div_img Description_img">
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                      <p>      After design and experimental validation, we designed three more ideal hybrid UAS promoters, M2 (BBa_K3772039), M5 (BBa_K3772042), and M8 (BBa_K3772045), using PDC1p as a prototype.
                           <img src="https://static.igem.org/mediawiki/parts/9/95/T--SCUT_China--implementation-2.jpg">
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                      </p>
 +
                      <p>Hybrid UAS promoters M2, M5 and M8 were constructed by Over-lap PCR as shown in the Fig.2.
 +
                      </p>
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                       <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.2 Project Proposed Implementation</p>
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                       <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.2 Multi copy addition of UAS</p>
 
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                     <h2 class="content_text_h2">Safety points to Consider</h2>
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                     <h2 class="content_text_h2">Results</h2>
                    <div class="content_div_text">
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                       <p >     1. Industrial production process<br>Because our product nootkatone has been shown in animal studies to have a low potential for toxic effects in humans. Therefore, it is sufficient to use the usual protective measures in industrial processes. However, there are data that suggest a risk of sensitization of nootkatone at low purity levels, so try to avoid contact of the concentrated crude product with the skin before the isolation and purification process.
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                       <p>We next constructed hybrid UAS Promoter-VS-SAG1t expression cassettes (BBa_K3772060, BBa_K3772063 and BBa_K3772066) to compare the expression intensity of the hybrid promoters by the yield of valenece.                       </p>
 +
                      <p>According to the experimental results (Fig.3), the production of Valencene of PDC1p was 4.31mg/L and that of M2 was increased by 18.9% (5.13 mg/L) while M5 was being increased by 29.5% (5.58mg/L). Compared with M5, the Valencene yield of M8 increased by 27.0% (6.75 mg/L). Finally, the yield of Valencene controlled by the modified M8 mutant strain was increased by 56.6% (6.75 mg/L) compared with PDC1p.
 
                       </p>
 
                       </p>
                       <p  >    2. product design<br>nootkatone has a certain degree of phytotoxicity, which can cause chlorosis or even necrosis of plant leaves. But because nootkatone has high volatility and is unstable under light and heat [1], its toxicity to the environment though is minimal. However, as a mosquito repellent that may be sprayed directly into the environment, it may form localized areas of high concentration in the environment and lead to poisoning of plants in the environment. The volatility and instability may also limit its effectiveness in the field of mosquito repellents that require long duration of action. Therefore, after searching the literature, we found that these risks and limitations can be greatly improved by encapsulating nootkatone.                      </p>
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                       <div class="content_div_img Description_img">
                      <p  >    The existing studies on nootkatone encapsulation technology are shown in Table.2.
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                           <img src="https://static.igem.org/mediawiki/parts/f/f2/T--SCUT_China--Improve-3.jpg">
The use of lignin for encapsulation not only reduces the phytotoxicity and slows down the volatilization of nootkatone, but even has a more significant killing effect on tick than raw materials.[2] In contrast, encapsulation with cydodexrins greatly affected the physical properties of nootkatone. cydodexrins- encapsulated nootkatone exhibited greater photothermal stability, and the encapsulated cydodexrins-encapsulated nootkatone has better water solubility [3], a property that would facilitate the preparation of safer mosquito repellents.                      </p>
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                       <p style="font-size:14px;text-align:center;color:#A5A8A6;">Table.2 nootkatone encapsulation technology<sup>[2,3]</sup></p>
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                       <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.3 The production of Valencene. a) Comparison of products between M1p, M2p and PDC1p; b) Comparison of products between M1-7p and PDC1p; c) Comparison of products between M5p and M8-10p; d) Comparison of products of all hybrid UAS Promoters in PDC1p.</p>
                      <p >    Different encapsulation systems need to be prepared in different ways. We expect that future products will be successfully converted to productivity, so whether the encapsulation method can be implemented in the factory is also a factor we should consider. <br><br>In an interview with Prof. Ye, who teaches bioreaction engineering at SCUT, we learned that the ultrasonic treatment used in the preparation of lignin-encapsulated nootkatone is only applicable to fermentation systems in small- or medium-scale plants, and that large-scale fermentation is not feasible. The freezing equipment used for the preparation of cydodexrins-encapsulated nootkatone can be used in any scale. Therefore, in future projects, we can choose the plant size or investigate other more suitable encapsulants and encapsulation methods.                     </p>
+
                      <p >    And to illustrate in more detail the characteristics of our highest transcriptional intensity hybrid UAS promoter M8, we compared the time curve and specific rate curve of Valencene production between the original PDC1p and the M8 promoter. <br>The results showed that the overall level of Valencene fermentation in M8 was higher than that in PDC1, and the yield of Valencene in M8 was significantly higher than that in PDC1 at the late stage of fermentation
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                      </p>
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                      <p style="font-size:14px;text-align:center;color:#A5A8A6;">(Fig.4), indicating that the transformation was effective.Fig.4 Time curve of Valencene between M8 and PDC1p.</p>
  
 +
                      <p >    By analyzing Glucose, Ethanol concentration and Valencene production between M8 and PDC1 (Fig.5), we could find the difference in the activity of M8 and PDC1 during the consumption of different carbon sources.                      </p>
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                          <img src="https://static.igem.org/mediawiki/parts/a/ac/T--SCUT_China--HeP-10.jpg">
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                      </div>
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                      <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.5 Glucose, Ethanol concentration and Valencene production between M8p and PDC1p.</p>
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 +
                      <p >    During glucose consumption (0-15 h), there was no significant difference in Valencene Valencene production between M8p and PDC1p, while during the ethanol consumption phase (15-70 h), the Valencene production corresponding to M8p continued to rise with ethanol consumption, with significant growth, while PDC1p grew slowly.<br><br>The Fig.6 comparing the Valencene ratio production rate of M8 with that of PDC1 more visually reflects that the Valencene production rate of M8 is much higher than that of PDC1p at the late stage of fermentation (48h-72h).                    </p>
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                          <img src="https://static.igem.org/mediawiki/parts/a/aa/T--SCUT_China--HeP-11.jpg">
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                      </div>
 +
                      <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.6 Specific production rate of product.</p>
 +
 +
                      <p >    In order to verify that the increase of Valencene production is the results of the increase of mRNA at the transcription level, we conducted real-time quantitative PCR between M8 & PDC1. To be specific, we sampled the 9h and 26h fermentation broth to extract RNA from cells and reverse transcribed cDNA for qPCR verification, and the results (Fig.7) showed that the transcription level of M8 at the late fermentation (26h) was significantly higher than that of PDC1. These results indicated that the increase of Valencene production was due to the increased transcription level of Valencene synthase gene.                      </p>
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                          <img src="https://static.igem.org/mediawiki/parts/b/b1/T--SCUT_China--HeP-12.jpg">
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                      </div>
 +
                      <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.7 The differences of M8 & PDC1 in transcription level</p>
 +
 +
                      <p >    Finally, by transcribing Valencene synthase using the M8 promoter, the yield of Nootkatone synthesis with other enzymes showed a significant increase in the yield of Valencene, Nootkatol and total terpene compared to PDC1. (Fig.8)                      </p>
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                      </div>
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                      <p style="font-size:14px;text-align:center;color:#A5A8A6;">Fig.8 the yield of Valencene, Nootkatol and total terpene between M8p and PDC1p</p>
 +
 +
                      <p >    In summary, our improvement of BBa_K2365033 resulted in a significant increase in promoter activity of the improved parts M2 (BBa_K3772039), M5 (BBa_K3772042), and M8 (BBa_K3772045). And the M8 promoter was shown to have high activity even in the late stage of fermentation.                      </p>
 
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                     <h2  class="content_text_h2">References</h2>
 
                     <h2  class="content_text_h2">References</h2>
 
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                       <p>[1]National Center for Biotechnology Information (2021). PubChem Annotation Record for Nootkatone, Source: Hazardous Substances Data Bank (HSDB). Retrieved October 17, 2021 from https://pubchem.ncbi.nlm.nih.gov/source/hsdb/8272.    </p>
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                       <p>[1] Cao, L., et al., Two-stage transcriptional reprogramming in Saccharomyces cerevisiae for optimizing ethanol production from xylose. Metabolic Engineering, 2014. 24: p. 150-159.    </p>
                      <p>[2]Behle RW, Flor-Weiler LB, Bharadwaj A, Stafford KC 3rd. A formulation to encapsulate nootkatone for tick control. J Med Entomol. 2011;48(6):1120-1127. doi:10.1603/me10282 </p>
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                      <p>[3]Kfoury M, Landy D, Ruellan S, Auezova L, Greige-Gerges H, Fourmentin S. Nootkatone encapsulation by cyclodextrins: Effect on water solubility and photostability. Food Chem. 2017;236:41-48. doi:10.1016/j.foodchem.2016.12.086   </p>
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Revision as of 01:54, 22 October 2021


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Overview

We wanted to find efficient promoter elements in yeast to help us achieve yield increase. So we tested the strength of 14 promoters from different metabolic pathways. And the experiments showed that the intensity of PDC1(BBa_K2365033) was the highest among them. Although the intensity of PDC1 is high in the early stage of fermentation compared to other promoters, it decreases significantly in the middle and late stages. (Fig.1) Therefore, we hope to construct a more stable promoter with high activity.

Fig.1 a) Fermentation results-genome level LEU2::P-VS-T; b) Time curve of Valencene; c) Glucose, Ethanol concentration and Valencene production.

Design

We determine that the large decrease in intensity before and after PDC1 may be due to the low activation of PDC1 in response to the carbon source at the late stage of fermentation. Different UASs on each promoter give it the ability to respond to different carbon sources [1]. Therefore, we can recombine the UASs from different promoters to change promoters, making them adapt for different carbon sources and activate production in the diauxic shift automatically.

After design and experimental validation, we designed three more ideal hybrid UAS promoters, M2 (BBa_K3772039), M5 (BBa_K3772042), and M8 (BBa_K3772045), using PDC1p as a prototype.

Hybrid UAS promoters M2, M5 and M8 were constructed by Over-lap PCR as shown in the Fig.2.

Fig.2 Multi copy addition of UAS

Results

We next constructed hybrid UAS Promoter-VS-SAG1t expression cassettes (BBa_K3772060, BBa_K3772063 and BBa_K3772066) to compare the expression intensity of the hybrid promoters by the yield of valenece.

According to the experimental results (Fig.3), the production of Valencene of PDC1p was 4.31mg/L and that of M2 was increased by 18.9% (5.13 mg/L) while M5 was being increased by 29.5% (5.58mg/L). Compared with M5, the Valencene yield of M8 increased by 27.0% (6.75 mg/L). Finally, the yield of Valencene controlled by the modified M8 mutant strain was increased by 56.6% (6.75 mg/L) compared with PDC1p.

Fig.3 The production of Valencene. a) Comparison of products between M1p, M2p and PDC1p; b) Comparison of products between M1-7p and PDC1p; c) Comparison of products between M5p and M8-10p; d) Comparison of products of all hybrid UAS Promoters in PDC1p.

And to illustrate in more detail the characteristics of our highest transcriptional intensity hybrid UAS promoter M8, we compared the time curve and specific rate curve of Valencene production between the original PDC1p and the M8 promoter.
The results showed that the overall level of Valencene fermentation in M8 was higher than that in PDC1, and the yield of Valencene in M8 was significantly higher than that in PDC1 at the late stage of fermentation

(Fig.4), indicating that the transformation was effective.Fig.4 Time curve of Valencene between M8 and PDC1p.

By analyzing Glucose, Ethanol concentration and Valencene production between M8 and PDC1 (Fig.5), we could find the difference in the activity of M8 and PDC1 during the consumption of different carbon sources.

Fig.5 Glucose, Ethanol concentration and Valencene production between M8p and PDC1p.

During glucose consumption (0-15 h), there was no significant difference in Valencene Valencene production between M8p and PDC1p, while during the ethanol consumption phase (15-70 h), the Valencene production corresponding to M8p continued to rise with ethanol consumption, with significant growth, while PDC1p grew slowly.

The Fig.6 comparing the Valencene ratio production rate of M8 with that of PDC1 more visually reflects that the Valencene production rate of M8 is much higher than that of PDC1p at the late stage of fermentation (48h-72h).

Fig.6 Specific production rate of product.

In order to verify that the increase of Valencene production is the results of the increase of mRNA at the transcription level, we conducted real-time quantitative PCR between M8 & PDC1. To be specific, we sampled the 9h and 26h fermentation broth to extract RNA from cells and reverse transcribed cDNA for qPCR verification, and the results (Fig.7) showed that the transcription level of M8 at the late fermentation (26h) was significantly higher than that of PDC1. These results indicated that the increase of Valencene production was due to the increased transcription level of Valencene synthase gene.

Fig.7 The differences of M8 & PDC1 in transcription level

Finally, by transcribing Valencene synthase using the M8 promoter, the yield of Nootkatone synthesis with other enzymes showed a significant increase in the yield of Valencene, Nootkatol and total terpene compared to PDC1. (Fig.8)

Fig.8 the yield of Valencene, Nootkatol and total terpene between M8p and PDC1p

In summary, our improvement of BBa_K2365033 resulted in a significant increase in promoter activity of the improved parts M2 (BBa_K3772039), M5 (BBa_K3772042), and M8 (BBa_K3772045). And the M8 promoter was shown to have high activity even in the late stage of fermentation.

References

[1] Cao, L., et al., Two-stage transcriptional reprogramming in Saccharomyces cerevisiae for optimizing ethanol production from xylose. Metabolic Engineering, 2014. 24: p. 150-159.