Difference between revisions of "Team:UESTC-China/Demonstrate"

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             <table class="table table-hover">
 
             <table class="table table-hover">
                 <tr><td>No.</td><td> Vector </td><td>E.coli resistance </td><td>Vector map </td><td>Description</td></tr>
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                 <tr><td>No.</td><td> Vector </td><td>E. coli resistance</td><td> Description</td></tr>
                 <tr><td>1 </td><td>piGEM2018-Module004</td><td> Amp </td><td> </td><td>BBa_J23100-RBS-pelB+5D-Xyn10D-fae1A-RBS-pelB+5D-Xyl3A-RBS-pelB+5D-cex-RBS-pelB+5D-cenA-Ter</td></tr>
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                 <tr><td>1</td><td> piGEM2018-Module001</td><td> Amp </td><td>BBa_J23100-RBS-pelB+5D-Xyn10D-fae1A-RBS-pelB+5D-Xyl3A-RBS-pelB+5D-cex-RBS-pelB+5D-cenA-Ter</td></tr>
                 <tr><td>2 </td><td>piGEM2018-Module002 </td><td>Kan </td><td></td><td> Ter-Ter-RBS-Fdh-RBS-FRE_adhE-FRE_ackA-RBS-AtoB-RBS-AdhE2-RBS-Crt-RBS-Hbd-Ter</td></tr>
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                 <tr><td>2</td><td> piGEM2018-Module002 </td><td>Kan </td><td>Ter-Ter-RBS-Fdh-RBS-FRE_adhE-FRE_ackA-RBS-AtoB-RBS-AdhE2-RBS-Crt-RBS-Hbd-Ter</td></tr>
                 <tr><td>3 </td><td>piGEM2018-Module003 </td><td>Kan </td><td></td><td> BBa_J23100-RBS-FhlA-RBS-HydA-Ter</td></tr>
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                 <tr><td>3 </td><td>piGEM2018-Module003 </td><td>Kan </td><td>BBa_J23100-RBS-FhlA-RBS-HydA-</td></tr>
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         <div class="tu">Figure 1.&nbsp;The introduction of piGEM2018-Module001 to piGEM2018-Module003.</div>
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            Table 1.The introduction of piGEM2018-Module001 to piGEM2018-Module003.
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             Before DNA sequencing, those vectors were verified by restriction enzyme digestion. After electrophoresis analysis, the samples which contained all desired bands were selected and sent for sequencing. The sequencing results showed that all the above constructed vectors were successful. (Fig. 2)
 
             Before DNA sequencing, those vectors were verified by restriction enzyme digestion. After electrophoresis analysis, the samples which contained all desired bands were selected and sent for sequencing. The sequencing results showed that all the above constructed vectors were successful. (Fig. 2)
 
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/f/fe/T--UESTC-China--dem2.png" width="100%"></div>
 
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/f/fe/T--UESTC-China--dem2.png" width="100%"></div>
         <div class="tu">Figure 2.&nbsp; The image of agarose gel electrophoresis by double enzyme digestion.</div>
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         <div class="tu">
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            Figure 2.The image of agarose gel electrophoresis by double enzyme digestion.
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        </div>
 
         <div class="tu">(a)piGEM2018-Module001 (Line1,enzyme digested by EcoR32Ⅰ+NcoⅠ; Line2,enzyme digested by NcoIⅠ+XhoⅠ)</div>
 
         <div class="tu">(a)piGEM2018-Module001 (Line1,enzyme digested by EcoR32Ⅰ+NcoⅠ; Line2,enzyme digested by NcoIⅠ+XhoⅠ)</div>
 
         <div class="tu">(b) piGEM2018-Module002 (Line1,enzyme digested by PstⅠ+KpnⅠ; Line2,enzyme digested by HindⅢ+KpnⅠ)</div>
 
         <div class="tu">(b) piGEM2018-Module002 (Line1,enzyme digested by PstⅠ+KpnⅠ; Line2,enzyme digested by HindⅢ+KpnⅠ)</div>
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            Three pathway validation
 
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        <div class="smtitle">
 
 
             Straw degradation and glucose production
 
             Straw degradation and glucose production
 
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             Xylanase can decompose xylan to xylose, and the activity of xylanase can be estimated by detecting the concentration of xylose.
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             In order to verify whether E. coli BL21(DE3) with piGEM2018-Module001 has taken effect. We detect enzyme activity separately. (Fig. 3) Comparing with wild type, our E. coli carrying piGEM2018-Moudlu001 take effect. BL21(DE3) with piGEM2018-Module001 has the activity of ferulic acid esterase, xylanase and cellulase.
 
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/b/b5/T--UESTC-China--dem3.png" width="100%"></div>
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        <div class="tu">
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            Figure 3. Enzyme activity detection. Module001: broken bacteria of BL21(DE3) with piGEM-Module001. WT: Broken bacteria of wild type.
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        <div class="tu">(a)The activity of xylanase. Using the changes of absorbance value under 540nm as an indicator of changes in xylose concentration.</div>
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        <div class="tu">(b)The activity of Ferulic Acid Esterase. Using the changes of absorbance value under 410nm as an indicator of changes in ferulic acid concentration.</div>
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        <div class="tu">(c) The activity of cellulase. Using filter paper assay method. [1]</div>
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        <div class="tu">(d) The activity of CenA. Using CMC assay method. [2]</div>
 
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             Firstly, for quantitative assay, standard curves of ranging from 0-60mg/L Xylose were measured (Fig. 3). Then, we test the activity of xylan. Comparing with wild type, our E. coli carrying piGEM2018-Moudlu001 takes effect. (Fig. 4)
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             Meanwhile, we also use GC-MS to detect ferulic acid. The ferulic acid production was monitored by periodically taking samples from the supernatant of E. coli carrying piGEM2018-Module001. The ferulic acid production was monitored using the method of gas chromatography by periodically taking samples from the supernatant of fermented liquid, and the internal standard is carvacrol [3]. Ferulic acid will decompose into 9 carbon compounds in the case of ferulic acid in gas chromatography with nitrogen as carrier gas [4]. Fig.4 shows that the peak of ferulic acid derivative increased within 20 hours while ferulic acid derivative was not found in sample of wild-type E. coli. Fig.5 demonstrate that our product is ferulic acid by GC-MS.
 
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/b/b5/T--UESTC-China--dem3.png" width="100%"></div>
 
        <div class="tu">Figure 3.&nbsp; The standard curve of Xylose.</div>
 
 
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/2f/T--UESTC-China--dem4.png" width="100%"></div>
 
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/2f/T--UESTC-China--dem4.png" width="100%"></div>
         <div class="tu">Figure 4.&nbsp;Two groups of different sample solutions were added. Namely, Module001: </div>
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         <div class="tu">
        <div class="tu">supernatant of piGEM-Module001. WT: supernatant of Wild Type. The strain BL21 (DE3) transformed with piGEM2018-Module001 was cultivated overnight and centrifuged to obtain the supernatant. The remaining bacteria were broken and broken products were obtained.1 ml xylan solution was added to 5 ml phosphate buffer solution (pH=6), incubated at 40 C for 5 min, and 1 ml sample solution was added. </div>
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            Figure 4, Chromatogram of Ferulic Acid derivatives and Internal Standard carvarol in supernatant of transgenic E. coli carrying piGEM2018-Module001 and wild-type E. coli. Samples were taken from reaction mixture at 0h, 24h.
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            Ferulic acid esterase can decompose ferulic acid p-nitrophenol ester to produce p-nitrophenol and ferulic acid. The changes of absorbance value under 410nm could be an indicator of changes in ferulic acid concentration. (Fig. 5)
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/a/af/T--UESTC-China--dem5.png" width="100%"></div>
 
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         <div class="tu">Figure 5.&nbsp; The strain BL21 (DE3) transformed with piGEM2018-Module001 and wild type were broken. DSMO solution of ferulic acid p-nitrophenol ester was added to phosphate buffer solution of 630 L pH=6.4 with a concentration of 400 L of 10 mmol/L. Heat preservation 5min at 40℃ and add 0.2ml sample solution. The initial OD were same. Gently mix and incubate 4h at 40 C, determine the final OD value and compare the difference. </div>
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         <div class="tu">
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            Figure 5, Mass spectrums of ferulic acid derivative. Sample was transgenic E. coli carrying piGEM2018-Module001 and taken from reaction mixture at 24h.
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        </div>
 
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             To fully determine that our plasmid has taken effect. We use GC-MS to detect ferulic acid. The ferulic acid production was monitored by periodically taking samples from the supernatant of E. coli carrying piGEM2018-Module001. GC-MS was used to detect the concentration of ferulic acid using the method reported in another paper [1]. Ferulic acid will undergo this reaction and decompose into 9 carbon compounds in the case of ferulic acid in gas chromatography with nitrogen as carrier gas (Fig. 6). Fig.7 is chromatograms of the supernatant samples, the peak of ferulic acid derivative was observed from samples of tobacco carrying piGEM2018-Module001 after 0h and 24h. Most importantly, the peak of ferulic acid derivative increased within 20 hours while ferulic acid derivative was not found in sample of wild-type E. coli. Fig.8 demonstrate that our product is ferulic acid by GC-MS.
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             To further find whether the cellulase had been expressed successfully in BL21 (DE3), the method of Congo Red assay was performed. The results are shown in Fig.6. The strains carrying piGEM2018-Module001 showed a zone of clearance created by hydrolysis of CMC showed that cellulase was successfully transcribed and translated by BL21(DE3). The empty vector control didn't show any zone of clearance around the colonies.
 
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/c/c7/T--UESTC-China--dem6.png" width="100%"></div>
 
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/c/c7/T--UESTC-China--dem6.png" width="100%"></div>
 
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         <div class="tu">
             Figure 6.&nbsp;Ferulic acid decomposition reaction in gas chromatography with nitrogen as carrier gas.
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             Figure 6, (a) CMC agar plate before staining with Congo Red. (b)CMC agar plate after staining with Congo Red. Module001: BL21(DE3) carrying piGEM2018-Module001(OD600=1, 3, 5 from left to right) Positive Control: Enzyme (concentration=0.2, 0.3, 0.4 mg/ml from left to right) Negative Control: BL21 (DE3) carrying empty vector control (OD600=1, 3, 5 from left to right)
 
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/21/T--UESTC-China--dem7.png" width="100%"></div>
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            Figure 7.&nbsp;Chromatogram of Ferulic Acid derivatives and Internal Standard carvarol in supernatant of transgenic E. coli carrying piGEM2018-Module001 and wild-type E. coli. Samples were taken from reaction mixture at 0h, 24h.
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/2c/T--UESTC-China--dem8.png" width="100%"></div>
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             Butanol production
             Figure 8.&nbsp;Mass spectrums of ferulic acid derivative. Sample was transgenic E. coli carrying piGEM2018-Module001 and taken from reaction mixture at 24h.
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             In order to find out if the cellulase had been expressed successfully in BL21 (DE3), the method of Congo Red assay was performed. Cellulase can cut CMC-Na into short chains. As Congo Red only binds to long chain polysaccharides CMC-Na but not short chain resulting in halo formation.
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             Work validation of multi-enzyme system in BL21(DE3) carrying piGEM2018-Module002. AtoB, Hbd, crt, ter and adhE2 catalyzed six-step reactions converting glucose to butanol. To test whether this multi-enzyme conversion system could work in our E. coli successfully or not, we detected the time production curve of butanol of BL21(DE3) carrying piGEM2018-Module002 under the anaerobic condition.
 
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/21/T--UESTC-China--dem7.png" width="100%"></div>
            The results are shown in Fig.9. The strains carrying piGEM2018-Module001 showed a zone of clearance created by hydrolysis of CMC showed that cellulase was successfully transcribed and translated by BL21(DE3). The empty vector control didn't show any zone of clearance around the colonies.
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/0/08/T--UESTC-China--dem9.png" width="100%"></div>
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         <div class="tu">
 
         <div class="tu">
             Figure 9.&nbsp;Line 1: BL21(DE3) carrying piGEM2018-Module001 (OD600=1, 3, 5 from left to right) Line 2: Positive control enzyme (concentration=0.2, 0.3, 0.4 mg/ml from left to right) Line 3: BL21(DE3) carrying empty vector control (OD600=1, 3, 5 from left to right)
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             Figure 7, Chromatogram of butanol and Internal iosbutanol of transgenic E. coli carrying piGEM2018-Module002 and wild-type E. coli. Samples were taken from reaction mixture at 0h, 24h.
 
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             To further detect the function of cellulase, we tested cellulase and cenA activity. Providing data for previously submitted parts ( BBa_K118022, BBa_K118022). Firstly, for quantitative assay, standard curves of ranging from 0-1000mg/L glucose were measured (Fig.10).
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             Besides, after a serious of butanol-production detection under different cultivating condition, we finally provided the necessary data for modeling. Then detecting the butanol production in 48h under the optimized conditions. (Fig. 8)And the final maximum yield of butanol is 0.37 g / L in 24 hours.
 
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/4/43/T--UESTC-China--dem10.png" width="100%"></div>
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/2c/T--UESTC-China--dem8.png" width="100%"></div>
 
         <div class="tu">
 
         <div class="tu">
             Figure 10.&nbsp;The standard curve of Glucose.
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             Figure 8, The butanol production curve at optimized conditions (temperature=34℃, initial OD=13, Initial pH=8)
 
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             We measured the release of reducing sugar from filter paper by the 3,5-dinitrosalicylic acid (DNS) method for the cellulase activity.
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             Furthermore, comparing with the production of butanol from other paper, our butanol production has reached a medium level. (Tab 1)
 
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             The total amount of reducing sugars was expressed as glucose equivalents according to a standard curve prepared with glucose in the range from 0 to 1000 mg/L−1.
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             <table class="table table-hover">
 +
                <tr><td>Source </td><td>butanol titer (g/L · h)</td><td> knocking other pathway</td></tr>
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                <tr><td>[7]</td><td> 0.012 g/L · h </td><td>No</td></tr>
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                <tr><td>Our Design</td><td> 0.018 g/L · h </td><td>No</td></tr>
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                <tr><td> [8]</td><td></td><td></td></tr>
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                <tr><td> [9]</td><td></td><td></td></tr>
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            </table>
 
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/d/d2/T--UESTC-China--dem11.png" width="100%"></div>
 
 
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             Figure 11.&nbsp;Reactions were carried out in 50 ml centrifuge tubes with 50 mg of filter paper (1 cm × 6 cm piece) in 1.0 ml potassium phosphate buffer (50mM, pH 7.0), plus 0.5 ml of the crude enzyme solution. Reaction mixtures were incubated at 40 °C for 3 h, enzyme action was interrupted by the addition of 3,5-dinitrosalisylic acid (DNS) reagent, which was used to quantify the total amount of reducing sugars. Reaction mixtures were then placed in a boiling water bath for 5 min, cooled to room temperature and diluted to 25 ml with water for the measurement of absorbance at 540 nm with a spectrophotometer.
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             Table 2, Comparing with relevant paper in butanol titer. All paper are using E. coli.
 
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            In addition, we measured the release of reducing sugar from CMC-Na with the 3,5-dinitrosalicylic acid (DNS) method for cenA activity. As shown in Fig 12, BL21(DE3) carrying piGEM2018-Module001 could decompose CMC-Na while wild-type couldn't, which proved that cenA could work successfully.
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/1/1c/T--UESTC-China--dem12.png" width="100%"></div>
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            Figure 12.&nbsp;The concentration of reducing sugar after 3 hours. Reaction proceeded in 50 mM potassium phosphate buffer (pH = 7.0) at 40°C. Module001: The crude enzyme solution obtained by ultrasonication of BL21(DE3) carrying is involved in the reaction. Wild Type: The crude enzyme solution obtained by ultrasonication of wild-type BL21(DE3) participated in the reaction. CMC-Na:The same amount of CMC-Na participated in the reaction as a control. Each data represents the mean value ± standard deviation from two independent experiments.
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         <div class="bigtitle">
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             Hydrogen production
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             Butanol production
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         <div class="zhengwen">
             Work validation of multi-enzyme system in BL21(DE3) carrying piGEM2018-Module002. AtoB,Hbd,crt,ter and adhE2 catalyzed six-step reactions converting glucose to butanol. To test whether this multi-enzyme conversion system could work in our E. coli successfully or not, we detected the time production curve of butanol of BL21(DE3) carrying piGEM2018-Module002 under the anaerobic condition. Significantly, the peak of butanol increased within 24 hours while it was not found in sample of wild-type BL23(DE3).(Fig.13)
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             To verify whether the piGEM-Module003 plasmid was working normally in E. coli DH5α. We set up an anaerobic fermentation unit. Because E. coli produces only carbon dioxide and hydrogen under anaerobic conditions, the removal of carbon dioxide theoretically allows us to produce relatively pure hydrogen. Then we test the collecting gas.
 
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/a/aa/T--UESTC-China--dem13.png" width="100%"></div>
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         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/0/08/T--UESTC-China--dem9.png" width="100%"></div>
 
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             Figure 13.&nbsp;Chromatogram of butanol and Internal iosbutanol of transgenic E. coli carrying piGEM2018-Module002 and wild-type E. coli. Samples were taken from reaction mixture at 0h, 24h.
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             Figure 9, Overall setup of the hydrogen collection device.
 
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             For quantitative assay, standard curves of butanol ranging from 1-5g/L were measured (Fig. 14). The butanol production was monitored using the method of gas chromatography by periodically taking samples from the supernatant of fermented liquid, and the internal standard is isobutanol. [2]
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             Then we test the collecting gas (Video 1). We can see from this video. The gas produced in turn a makes a sharp explosion when it meets the burning stick, while the gas produced in the wild makes the stick extinguish directly.
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                </object> 当前浏览器不支持 video直接播放,点击这里下载视频:
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                <a href="https://static.igem.org/mediawiki/2018/4/41/T--UESTC-China--jieshuo.mp4">Download Video</a>
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        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/6/67/T--UESTC-China--dem14.png" width="100%"></div>
 
 
         <div class="tu">
 
         <div class="tu">
             Figure 14.&nbsp;Standard curve of Butanol.
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             Video 1, The video of gas test. Sample were collected from DH5α with piGEM2018-Module003 and wild type after 48h, shaking with TB medium.
 
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         <div class="zhengwen">
 
         <div class="zhengwen">
             Furthermore, after a serious of butanol-production detection under different cultivating condition, we finally provided the necessary data for modeling. And detecting the butanol production in 48h under the optimized conditions. And the final maximum yield of butanol is 0.37 g / L.
+
             For quantitative assay, we measure hydrogen using gas chromatography under different cultivating condition to provide data for Modeling. Then detecting the butanol production in 48h under the optimized conditions. (Fig. 8)And the final maximum yield of hydrogen is xxx g / L in 48 hours.
 
         </div>
 
         </div>
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/b/ba/T--UESTC-China--dem15.png" width="100%"></div>
+
         <div class="chatu" style="padding:20px 10%;"><img src="10" width="100%"></div>
 
         <div class="tu">
 
         <div class="tu">
             Figure 15.&nbsp; The butanol production curve at optimized conditions (temperature=34℃, initial OD=13, Initial pH=8)
+
             Figure 10, Gas production of wild type DH5a and DH5a transfected into piGEM-Module 003 plasmid was measured in this gas collection unit for 36 hours.
        </div>
+
        <div class="smtitle">
+
            Hydrogen production
+
 
         </div>
 
         </div>
 
         <div class="zhengwen">
 
         <div class="zhengwen">
             First, in order to verify that the gene expressed the protein in E. coli, we performed SDS-PAGE on the DH5α bacterial solution containing piGEM-Module003 and the control bacterial solution. FhlA has a brighter band at 97.4 kDa and Hyda has a brighter band at 42 kDa.
+
             The theoretical maximum yield of facultative anaerobic bacteria is 2 moles H2 per mole of glucose. Based on the optimum reaction conditions for the modeling guidelines, we tested the hydrogen content and rate of production in the 40-hour anaerobic fermentation gas. The end result is x moles of hydrogen per gram of glucose.
        </div>
+
        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/b/b3/T--UESTC-China--dem16.png" width="100%"></div>
+
        <div class="tu">
+
            Figure 16.&nbsp; M: Marker, WT: wild type, Module 003: piGEM2018-003 in DH5α. All samples were obtained after breaking the cultivating E.coli DH5α for 4h at 37℃, 180rpm.
+
 
         </div>
 
         </div>
 
         <div class="zhengwen">
 
         <div class="zhengwen">
             Next, it was verified whether the piGEM-Module003 plasmid was working normally in Escherichia coli DH5α. We set up an anaerobic fermentation unit. Because E. coli produces only carbon dioxide and hydrogen under anaerobic conditions, the removal of carbon dioxide theoretically allows us to produce relatively pure hydrogen.
+
             <table>
 +
 
 +
            </table>
 
         </div>
 
         </div>
        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/f/fc/T--UESTC-China--dem17.png" width="100%"></div>
 
 
         <div class="tu">
 
         <div class="tu">
             Figure 17.&nbsp; The left side of the apparatus is a carbon dioxide generating apparatus, and carbon dioxide is produced by dropping a dilute hydrochloric acid into a flask containing CaCO3 under the separatory funnel. The middle part of the device is a bacterial liquid fermentation device consisting of a three-necked flask placed on a temperature-controlled magnetic stirrer. The magnetic stirrer can continuously stir the bacteria liquid and keep the temperature constant. The right side of the unit consists of two scrubbers and a sink. The first scrubber bottle is filled with a sodium hydroxide solution to remove carbon dioxide and hydrogen chloride gas from the mixed gas. In the second scrubber is a clarified lime water used to verify that the carbon dioxide gas has been removed. The final product gas is then collected using a drainage gas collection method in the water tank.
+
             Table 3, Comparing with relevant paper in hydrogen production. All paper are using E. coli.
 +
        </div>
 +
    </li>
 +
    <li>
 +
        <div class="bigtitle">
 +
            Validation of straw degradation and butanol production pathway
 
         </div>
 
         </div>
 
         <div class="zhengwen">
 
         <div class="zhengwen">
             Firstly, for quantitative assay, standard curves of ranging from 0-9ml hydrogen were measured (Fig. 17). Then, we measure hydrogen using gas chromatography. Fig.XX is chromatograms of the gas samples, the peak of hydrogen was observed from samples of DH5α carrying piGEM2018-Module003 after 0h and 24h. Most importantly, the peak of butanol increased within 24 hours while it was not found in sample of wild-type BL23(DE3).
+
             In the future, we will try to integrate the gene, which control butanol and hydrogen production. Therefore, our super E. coli could produce both butanol and hydrogen. [Fig. 11]
 
         </div>
 
         </div>
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/2/2e/T--UESTC-China--dem18.png" width="100%"></div>
+
         <div class="chatu" style="padding:20px 10%;"><img src="11" width="100%"></div>
 
         <div class="tu">
 
         <div class="tu">
             Figure 18.&nbsp; Standard curve of Hydrogen.
+
             Figure 11, awdawdawdwadaw
 
         </div>
 
         </div>
         <div class="zhengwen">
+
 
             We use gas chromatography (GC) to verify the gas produced by the fermentation unit. We injected three different gases, 5% hydrogen with 95% carbon dioxide, the gas produced by the DH5α fermentation of the piGEM-Module003 plasmid, and the gas after fermentation of the original DH5α strain. Fig
+
 
 +
 
 +
 
 +
 
 +
    </li>
 +
 
 +
 
 +
 
 +
    <li>
 +
         <div class="bigtitle">
 +
             Work going on
 
         </div>
 
         </div>
        <div class="chatu" style="padding:20px 10%;"><img src="19" width="100%"></div>
+
    </li>
         <div class="tu">
+
    <li>
             Figure 19.&nbsp;
+
         <div class="bigtitle">
 +
             All gene in one plasmid
 
         </div>
 
         </div>
 
         <div class="zhengwen">
 
         <div class="zhengwen">
             The theoretical maximum yield of facultative anaerobic bacteria is 2 moles H2 per mole of glucose. Based on the optimum reaction conditions for the modeling guidelines, we tested the hydrogen content and rate of production in the 40-hour anaerobic fermentation gas. The end result is x moles of hydrogen per gram of glucose.
+
             In the future, we will try to integrate the gene which control butanol and hydrogen production. Therefore, our super E. coli could produce both butanol and hydrogen.
 
         </div>
 
         </div>
        <div class="chatu" style="padding:20px 10%;"><img src="20" width="100%"></div>
+
    </li>
         <div class="tu">
+
    <li>
             Figure 20.&nbsp;
+
         <div class="bigtitle">
 +
             Import resistance gene
 
         </div>
 
         </div>
 
         <div class="zhengwen">
 
         <div class="zhengwen">
             Now, let’s listen to the beautiful sound.
+
             During the production process, the accumulation of butanol will exert a great inhibitory effect on cell growth. Therefore, we will introduce the GroEL gene and GroES gene from clostridium acetone butanol to make E. coli heterologous expression of heat shock protein -- a molecular chaperone of GroESL, which has been shown to increase butanol production. Fig. 18 shows that GroESL have a good effect on butanol tolerance.
 
         </div>
 
         </div>
         video
+
         <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/1/1c/T--UESTC-China--dem12.png" width="100%"></div>
 +
        <div class="tu">Figure 12, After adding 0.3ml butanol in 30ml LB medium, the measurement of optical density (A600) deference between DH5α with GroESL and Negative Control in 24 hour.</div>
  
 
     </li>
 
     </li>
 
     <li>
 
     <li>
 
         <div class="bigtitle">
 
         <div class="bigtitle">
             Work going on
+
             Knock out relevant gene
 
         </div>
 
         </div>
 
         <div class="zhengwen">
 
         <div class="zhengwen">
             During the production process, the accumulation of butanol will exert a great inhibitory effect on cell growth. Therefore, we will introduce the GroEL gene and GroES gene from clostridium acetone butanol to make Escherichia coli heterologous expression of heat shock protein -- a molecular chaperone of GroESL, which has been shown to increase butanol production. Fig. 18 shows that GroESL have a good effect on butanol tolerance.
+
             Due to limitations of experimental conditions, we are not able to knock out competitive pathway. However, many by-products will produce in the process of butanol production, namely frdABCD for succinate, ldhA for lactate, pta-ack for acetate, and adhE for ethanol (Fig. ). If we could knock out these competitive pathway, then our butanol production will be greatly improved.
        </div>
+
        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/5/54/T--UESTC-China--dem21.png" width="100%"></div>
+
        <div class="tu">
+
            Figure 21.&nbsp; After adding 0.3ml butanol in 30ml LB medium, the measurement of optical density (A600) deference between DH5α with GroESL and Negative Control in 24 hour.
+
 
         </div>
 
         </div>
 +
        <div class="chatu" style="padding:20px 10%;"><img src="https://static.igem.org/mediawiki/2018/a/aa/T--UESTC-China--dem13.png" width="100%"></div>
 +
        <div class="tu">Figure 13, After adding 0.3ml butanol in 30ml LB medium, the measurement of optical density (A600) deference between DH5α with GroESL and Negative Control in 24 hour.</div>
 +
 +
 
     </li>
 
     </li>
 
     <li>
 
     <li>
Line 413: Line 446:
 
             References
 
             References
 
         </div>
 
         </div>
         <div class="zhengwen">[1]Fiddler, W., Parker, W. E., Wasserman, A. E., & Doerr, R. C. (1967). Thermal decomposition of ferulic acid. Journal of Agricultural and Food Chemistry, 15(5), 757-761.</div>
+
         <div class="zhengwen">
        <div class="zhengwen">[2] Atsumi, S., Cann, A. F., Connor, M. R., Shen, C. R., Smith, K. M., Brynildsen, M. P., ... & Liao, J. C. (2008). Metabolic engineering of Escherichia coli for 1-butanol production. Metabolic engineering, 10(6), 305-311.</div>
+
            <div>[1] Silveira, M. H. L., Rau, M., da Silva Bon, E. P., & Andreaus, J. (2012). A simple and fast method for the determination of endo-and exo-cellulase activity in cellulase preparations using filter paper. Enzyme and microbial technology, 51(5), 280-285.</div>
 +
            <div>[2] Wood, T. M., & Bhat, K. M. (1988). Methods for measuring cellulase activities. In Methods in enzymology (Vol. 160, pp. 87-112). Academic Press.</div>
 +
            <div>[3] http://en.cnki.com.cn/Article_en/CJFDTOTAL-SZGY200707082.htm</div>
 +
            <div>[4]Fiddler, W., Parker, W. E., Wasserman, A. E., & Doerr, R. C. (1967). Thermal decomposition of ferulic acid. Journal of Agricultural and Food Chemistry, 15(5), 757-761.</div>
 +
            <div>[5] Atsumi, S., Cann, A. F., Connor, M. R., Shen, C. R., Smith, K. M., Brynildsen, M. P., ... & Liao, J. C. (2008). Metabolic engineering of E. coli for 1-butanol production. Metabolic engineering, 10(6), 305-311.</div>
 +
        </div>
 +
 
 
     </li>
 
     </li>
 
</ul>
 
</ul>

Revision as of 03:23, 16 October 2018

team

  • Pathway construction
    In order to express multiple enzymes in E. coli, we firstly did the codon-optimized of the enzymes. And then these genes were commercially synthesized. Finally, with the application of Gibson Assembly and Golden Gate strategy, we successfully introduced the target gene into different E. coli expression vector. (Fig. 1)
    No. Vector E. coli resistance Description
    1 piGEM2018-Module001 Amp BBa_J23100-RBS-pelB+5D-Xyn10D-fae1A-RBS-pelB+5D-Xyl3A-RBS-pelB+5D-cex-RBS-pelB+5D-cenA-Ter
    2 piGEM2018-Module002 Kan Ter-Ter-RBS-Fdh-RBS-FRE_adhE-FRE_ackA-RBS-AtoB-RBS-AdhE2-RBS-Crt-RBS-Hbd-Ter
    3 piGEM2018-Module003 Kan BBa_J23100-RBS-FhlA-RBS-HydA-
    Table 1.The introduction of piGEM2018-Module001 to piGEM2018-Module003.
    Before DNA sequencing, those vectors were verified by restriction enzyme digestion. After electrophoresis analysis, the samples which contained all desired bands were selected and sent for sequencing. The sequencing results showed that all the above constructed vectors were successful. (Fig. 2)
    Figure 2.The image of agarose gel electrophoresis by double enzyme digestion.
    (a)piGEM2018-Module001 (Line1,enzyme digested by EcoR32Ⅰ+NcoⅠ; Line2,enzyme digested by NcoIⅠ+XhoⅠ)
    (b) piGEM2018-Module002 (Line1,enzyme digested by PstⅠ+KpnⅠ; Line2,enzyme digested by HindⅢ+KpnⅠ)
    (c)piGEM2018-Module003 (Line1,enzyme digested by EcoRⅠ+NcoⅠ;Line2, enzyme digested by BamHⅠ+BglⅡ)
  • Straw degradation and glucose production
    In order to verify whether E. coli BL21(DE3) with piGEM2018-Module001 has taken effect. We detect enzyme activity separately. (Fig. 3) Comparing with wild type, our E. coli carrying piGEM2018-Moudlu001 take effect. BL21(DE3) with piGEM2018-Module001 has the activity of ferulic acid esterase, xylanase and cellulase.
    Figure 3. Enzyme activity detection. Module001: broken bacteria of BL21(DE3) with piGEM-Module001. WT: Broken bacteria of wild type.
    (a)The activity of xylanase. Using the changes of absorbance value under 540nm as an indicator of changes in xylose concentration.
    (b)The activity of Ferulic Acid Esterase. Using the changes of absorbance value under 410nm as an indicator of changes in ferulic acid concentration.
    (c) The activity of cellulase. Using filter paper assay method. [1]
    (d) The activity of CenA. Using CMC assay method. [2]
    Meanwhile, we also use GC-MS to detect ferulic acid. The ferulic acid production was monitored by periodically taking samples from the supernatant of E. coli carrying piGEM2018-Module001. The ferulic acid production was monitored using the method of gas chromatography by periodically taking samples from the supernatant of fermented liquid, and the internal standard is carvacrol [3]. Ferulic acid will decompose into 9 carbon compounds in the case of ferulic acid in gas chromatography with nitrogen as carrier gas [4]. Fig.4 shows that the peak of ferulic acid derivative increased within 20 hours while ferulic acid derivative was not found in sample of wild-type E. coli. Fig.5 demonstrate that our product is ferulic acid by GC-MS.
    Figure 4, Chromatogram of Ferulic Acid derivatives and Internal Standard carvarol in supernatant of transgenic E. coli carrying piGEM2018-Module001 and wild-type E. coli. Samples were taken from reaction mixture at 0h, 24h.
    Figure 5, Mass spectrums of ferulic acid derivative. Sample was transgenic E. coli carrying piGEM2018-Module001 and taken from reaction mixture at 24h.
    To further find whether the cellulase had been expressed successfully in BL21 (DE3), the method of Congo Red assay was performed. The results are shown in Fig.6. The strains carrying piGEM2018-Module001 showed a zone of clearance created by hydrolysis of CMC showed that cellulase was successfully transcribed and translated by BL21(DE3). The empty vector control didn't show any zone of clearance around the colonies.
    Figure 6, (a) CMC agar plate before staining with Congo Red. (b)CMC agar plate after staining with Congo Red. Module001: BL21(DE3) carrying piGEM2018-Module001(OD600=1, 3, 5 from left to right) Positive Control: Enzyme (concentration=0.2, 0.3, 0.4 mg/ml from left to right) Negative Control: BL21 (DE3) carrying empty vector control (OD600=1, 3, 5 from left to right)
  • Butanol production
    Work validation of multi-enzyme system in BL21(DE3) carrying piGEM2018-Module002. AtoB, Hbd, crt, ter and adhE2 catalyzed six-step reactions converting glucose to butanol. To test whether this multi-enzyme conversion system could work in our E. coli successfully or not, we detected the time production curve of butanol of BL21(DE3) carrying piGEM2018-Module002 under the anaerobic condition.
    Figure 7, Chromatogram of butanol and Internal iosbutanol of transgenic E. coli carrying piGEM2018-Module002 and wild-type E. coli. Samples were taken from reaction mixture at 0h, 24h.
    Besides, after a serious of butanol-production detection under different cultivating condition, we finally provided the necessary data for modeling. Then detecting the butanol production in 48h under the optimized conditions. (Fig. 8)And the final maximum yield of butanol is 0.37 g / L in 24 hours.
    Figure 8, The butanol production curve at optimized conditions (temperature=34℃, initial OD=13, Initial pH=8)
    Furthermore, comparing with the production of butanol from other paper, our butanol production has reached a medium level. (Tab 1)
    Source butanol titer (g/L · h) knocking other pathway
    [7] 0.012 g/L · h No
    Our Design 0.018 g/L · h No
    [8]
    [9]
    Table 2, Comparing with relevant paper in butanol titer. All paper are using E. coli.
  • Hydrogen production
    To verify whether the piGEM-Module003 plasmid was working normally in E. coli DH5α. We set up an anaerobic fermentation unit. Because E. coli produces only carbon dioxide and hydrogen under anaerobic conditions, the removal of carbon dioxide theoretically allows us to produce relatively pure hydrogen. Then we test the collecting gas.
    Figure 9, Overall setup of the hydrogen collection device.
    Then we test the collecting gas (Video 1). We can see from this video. The gas produced in turn a makes a sharp explosion when it meets the burning stick, while the gas produced in the wild makes the stick extinguish directly.
    Video 1, The video of gas test. Sample were collected from DH5α with piGEM2018-Module003 and wild type after 48h, shaking with TB medium.
    For quantitative assay, we measure hydrogen using gas chromatography under different cultivating condition to provide data for Modeling. Then detecting the butanol production in 48h under the optimized conditions. (Fig. 8)And the final maximum yield of hydrogen is xxx g / L in 48 hours.
    Figure 10, Gas production of wild type DH5a and DH5a transfected into piGEM-Module 003 plasmid was measured in this gas collection unit for 36 hours.
    The theoretical maximum yield of facultative anaerobic bacteria is 2 moles H2 per mole of glucose. Based on the optimum reaction conditions for the modeling guidelines, we tested the hydrogen content and rate of production in the 40-hour anaerobic fermentation gas. The end result is x moles of hydrogen per gram of glucose.
    Table 3, Comparing with relevant paper in hydrogen production. All paper are using E. coli.
  • Validation of straw degradation and butanol production pathway
    In the future, we will try to integrate the gene, which control butanol and hydrogen production. Therefore, our super E. coli could produce both butanol and hydrogen. [Fig. 11]
    Figure 11, awdawdawdwadaw
  • Work going on
  • All gene in one plasmid
    In the future, we will try to integrate the gene which control butanol and hydrogen production. Therefore, our super E. coli could produce both butanol and hydrogen.
  • Import resistance gene
    During the production process, the accumulation of butanol will exert a great inhibitory effect on cell growth. Therefore, we will introduce the GroEL gene and GroES gene from clostridium acetone butanol to make E. coli heterologous expression of heat shock protein -- a molecular chaperone of GroESL, which has been shown to increase butanol production. Fig. 18 shows that GroESL have a good effect on butanol tolerance.
    Figure 12, After adding 0.3ml butanol in 30ml LB medium, the measurement of optical density (A600) deference between DH5α with GroESL and Negative Control in 24 hour.
  • Knock out relevant gene
    Due to limitations of experimental conditions, we are not able to knock out competitive pathway. However, many by-products will produce in the process of butanol production, namely frdABCD for succinate, ldhA for lactate, pta-ack for acetate, and adhE for ethanol (Fig. ). If we could knock out these competitive pathway, then our butanol production will be greatly improved.
    Figure 13, After adding 0.3ml butanol in 30ml LB medium, the measurement of optical density (A600) deference between DH5α with GroESL and Negative Control in 24 hour.
  • References
    [1] Silveira, M. H. L., Rau, M., da Silva Bon, E. P., & Andreaus, J. (2012). A simple and fast method for the determination of endo-and exo-cellulase activity in cellulase preparations using filter paper. Enzyme and microbial technology, 51(5), 280-285.
    [2] Wood, T. M., & Bhat, K. M. (1988). Methods for measuring cellulase activities. In Methods in enzymology (Vol. 160, pp. 87-112). Academic Press.
    [3] http://en.cnki.com.cn/Article_en/CJFDTOTAL-SZGY200707082.htm
    [4]Fiddler, W., Parker, W. E., Wasserman, A. E., & Doerr, R. C. (1967). Thermal decomposition of ferulic acid. Journal of Agricultural and Food Chemistry, 15(5), 757-761.
    [5] Atsumi, S., Cann, A. F., Connor, M. R., Shen, C. R., Smith, K. M., Brynildsen, M. P., ... & Liao, J. C. (2008). Metabolic engineering of E. coli for 1-butanol production. Metabolic engineering, 10(6), 305-311.
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