Team:Manchester/Parts

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           <div class="title">             
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             <b>This year we submitted and characterised 3 BioBricks, one of which is an improvement of <a href="http://parts.igem.org/wiki/index.php?title=Part:BBa_K925000" target="_blank">BBa_K925000</a>!</b>
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<center><i>We used an existing BioBrick component with Constitutive promoter and RBS<br><br> (BBa_K608002) to express our BioBrick parts:</i></center><br>
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           <img src="https://static.igem.org/mediawiki/2013/1/1a/Expression_vectors.png" width="900" height="300"/>
<!--<p id="footer"><b>Figure 5. Overlay of structures from 1 ns FabA simulation. Images of overlaid from the following respective time points: 0 ps, 250 ps, 500 ps, 750 ps and 1000 ps with the following colours indicating each individual image: Green, Blue, Purple, Orange and Grey, respectively.  Both the N-Terminal and C-Terminal, are specified (Dotted Box), with a zoom in on each respective terminal at an angle appropriate to visualise the positions of the terminals.  
<!--<p id="footer"><b>Figure 5. Overlay of structures from 1 ns FabA simulation. Images of overlaid from the following respective time points: 0 ps, 250 ps, 500 ps, 750 ps and 1000 ps with the following colours indicating each individual image: Green, Blue, Purple, Orange and Grey, respectively.  Both the N-Terminal and C-Terminal, are specified (Dotted Box), with a zoom in on each respective terminal at an angle appropriate to visualise the positions of the terminals.  
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             <img src="https://static.igem.org/mediawiki/2013/3/3a/TestdigestfabulousA.png" width="500" height="850"/>
             <!--<p id="footer"><b>Figure 1. Two colour image of FabA homodimer with labelled N- and C-Termini (arrows)</b><br>-->
             <!--<p id="footer"><b>Figure 1. Two colour image of FabA homodimer with labelled N- and C-Termini (arrows)</b><br>-->
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             <p><b><a id="Q1">Introduction</a></b><br>
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             <p><b>Successful Expression of delta 9 and delta 12 desaturase, and FabA</b><br>
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Our model of the fatty acid biosynthesis pathways highlighted several key enzymes that could be altered to produce palm oil, including Delta 9, Delta 12 and FabA, which agrees with previous publications on these enzymes. Delta 9 and Delta 12 are involved in linear pathways, meaning that there are obvious reactants and products, so the overexpression of them can be measured directly via LC-MS and other techniques. However, FabA is a β-Hydroxydecanoyl Thiol Ester Dehydrase involved in a cyclic pathway<sup>[1]</sup> specifically the conversion of β-hydroxy acyl-ACP to Enol acyl-ACP as part of the fatty acid biosynthetic pathway<sup>[2]</sup>. Therefore characterising any specific change due to FabA overexpression will be challenging, as any products will automatically be involved in the proceeding stage of the cycle and it would therefore be difficult to determine the effect of overexpression. An alternative to measure the overexpression of FabA, would be through the addition of His-tags to either the N-terminal and or the C-terminal of FabA. However, depending on the structure of FabA, the addition of His-tags could potentially interfere with expression, protein folding, enzymatic functions and interactions<sup>[3][4][5][6][7]</sup>. Several studies including work by <sup>[5]</sup> and <sup>[6]</sup>, respectively showed that the addition of C-Terminus His-tags to proteins could interfere with enzyme activity and alter di-sulphide and therefore protein structure. These problems are particularly applicable to FabA, as it forms a homodimer, as shown by Leesong et al., 1996<sup>[1]</sup>. Therefore, the addition of His-tag could potentially interfere with the interaction domain and thus the formation of a homodimer, which would be consistent with several reports<sup>[4][5][6]</sup>.  To address this issue, we decided to perform a molecular dynamics simulation using the GROMACS software package<sup>[8]</sup> on a structure of FabA, determined by X-ray crystallography by Leesong et al., 1996<sup>[1]</sup>. This would allow for the trajectories of the N- and C-Termini of FabA over the course of the simulation to be studied, therefore allowing us to identify which terminal would be more suited for His-tag addition.
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<p>In order to characterise our biobricks, we made use of the standard parts found in the registry. By inserting the created biobricks BBa_K1027001 and BBa_K1027002 in to BBa_K608002 (a biobrick consisting of a ribosomal binding site and a constitutive promoter), we were able to create a new construct that expressed the delta 9 desaturase, delta 12 desaturase and FabA proteins. The constructs are shown above.</p>
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<p><b>Plates</b></p>
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<p>Another piece of evidence suggesting that our constructs were successfully expressing our delta 9 desaturase and delta 12 desaturase enzymes was the size of the colonies grown on the plates. Pictures of the plates are shown below. On the far left is a control plate, with bacteria transformed with BBa_K608002 but with no gene inserted in front of the promoter. To the right of that are our delta 12 colonies. They are much smaller than the control, and even taking 20 hours to grow to that size as opposed to the usual 16 hours. We hypothesise that because delta 12 desaturase is a membrane-bound protein that the <i>E. coli</i> does not normally express, constitutively expressing it could inhibit the bacteria and slow growth. Compare this to FabA on the far right. Looking through the literature, we found that overexpression of FabA results in no significant difference in growth size or speed relative to the wild type strain (Luo et al, 2009). Compared to the control plate, we also found that the colonies grew normally.</p>
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<p><b>Gel Digests</b></p>
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<p>To confirm that our desired genes were in fact within the expression construct mentioned above, we carried out test digests of our ligated plasmids. Happily, when we ran our digests on an agarose gel, we saw all of the bands we would predict from the expected fragments. The gel pictures are on the right. <br>
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<b>delta 9 desaturase:</b> Cut with BamHI + EcoRV. Expected bands 1424 bp, 1262 bp, 99 bp.<br>
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<b>delta 12 desaturase:</b> Cut with BamHI, XbaI, PstI. Expected bands 2127 bp, 656 bp, 430 bp.<br>
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<b>FabA</b> Cut with EcoRV. Expected bands 1429 bp, 1115 bp. Cut with EcoRV, PstI. Expected bands 1153 bp, 1115 bp, 339 bp.<br></p>
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<p><b>Improvement of existing BioBrick</b></p>
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<p>Our biobrick BBa_K1027002 (<b>delta 12 desaturase</b>) is an improvement of the <a href="http://parts.igem.org/wiki/index.php?title=Part:BBa_K925000" target="_blank">BBa_K925000</a> biobrick created by the St Andrews team in 2012. We improved this biobrick from the ground up, starting by taking the protein sequence from <i>Synechocystis</i> sp. PCC 6803. This protein sequence was reverse translated and then codon optimised for expression in <i>E. coli</i>. We believe our redesigned biobrick has two features that the original biobrick does not. Firstly, the original biobrick could not be transformed by iGEM HQ, whereas we have managed successful transformation (as shown by the plate pictures). Next, the St. Andrews biobrick was cloned from cyanobacteria, and so is not optimised for expression in <i>E. coli</i>. As St. Andrews then went on to express their delta 12 desaturase biobrick in <i>E. coli</i> it follows that a sequence optimised for expression in this chassis, as ours was, would perform better than the sequence naturally found in cyanobacteria.</p>
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            <p id="footer"><b>LB-Agar (CmR) plates after 20h growth at 37&deg;C. Left: Control plate (transformed with empty vector BBa_K608002). Right: Transformed with delta 12 desaturase (note smaller colonies)</b><br>
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            <p id="footer"><b>LB-Agar (CmR) plates after 20h growth at 37&deg;C. Left: Control plate (transformed with empty vector BBa_K608002). Right: Transformed with FabA gene (note similar sized colonies)</b><br>
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             <p><b><a id="Q2">Installing GROMACS</a></b><br>
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             <p><b>Orbitrap LC-MS analysis</b><br>
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The Groningen Machine for Chemical Simulation (GROMACS) Version 4.5.5 [8], was installed on a MacBook Pro 2011 model, operating OS X 10.8.3, with a 4 GB 1333 MHz DDR3 memory, 2.3 GHz Intel Core i5 processor and a 320 GB SATA disk drive. Prior to installing GROMACS, “command line tools” were installed within Xcode, Version 4.6.1. GROMACS was installed to single precision, with the source file downloaded from www.gromacs.org/Downloads. In addition to GROMACS, the FFTW library, Version 3.3.3<sup>[9]</sup> was installed, with the source file downloaded from www.fftw.org/download.html.
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<p> Delta 9 desaturase and delta 12 desaturase enzymes were chosen because their products, when expressed in their host organism (<i>Synechocystis</i> sp. PCC 6803), convert stearic acid into <b>oleic acid</b>, and oleic acid into <b>linoleic acid</b> respectively. Therefore, we fed batches of transformed DH5-alpha with 2 different concentrations of exogenous fatty acid (0.1% and 0.5% stearic acid fed to the delta 9 desaturase batch, and 0.1% and 0.5% oleic acid fed to the delta 12 desaturase batch), left the cultures growing overnight and then harvested the cells.<br>
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<br>
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To analyse the metabolites extracted from both wild-type DH5-alpha and DH5-alpha expressing our delta 9 desaturase and delta 12 desaturase enzymes, we made use of the MIB’s in-house Orbitrap Liquid Chromatography - Mass Spectrometry (LC-MS). This technique was chosen because of its high mass accuracy and sensitivity. Upon analysing the most abundant metabolites extracted from our expression strains and comparing this data with the most abundant metabolites extracted from wild-type, it is apparent that a massive increase in linoleic acid (incorporated in phosphatidylethanolamines, PE) has occurred. This is demonstrated in the two figures directly below. The chromatograms produced for the delta 12 desaturase expression strains are also shown below. There is a clear difference between the wild-type <i>E. coli</i> fed with exogenous substrate compared with the <i>E. coli</i> strains expressing delta 12 desaturase. It is probable that the peak appearing around 7.9 min in the delta 12 desaturase strains is due to phospholipid incorporating <b>18:2 (9Z, 12Z) - linoleic acid</b>.
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             <p id="footer"><b>Figure 2. GROMACS Molecular Dynamics Simulation Workflow. The commands used at each step are included, with a brief description of their function</b><br>
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             <p id="footer"><b>The four most abundant metabolites extracted from <b>wild-type DH5-alpha</b>. Analysed using Orbitrap LC-MS. Note prominence of short-chain fatty acids. </b><br>
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             <p id="footer"><b>Figure 2. GROMACS Molecular Dynamics Simulation Workflow. The commands used at each step are included, with a brief description of their function</b><br>
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             <p id="footer"><b>The four most abundant metabolites extracted from our <b>delta 12 desaturase</b> expression strains. Analysed using Orbitrap LC-MS. Note prominence of C18:2 (9Z, 12Z) (linoleic acid). </b><br>
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              <p id="footer"><b>Above Left: Chromatograms obtained through Orbitrap LC-MS analysis.<br> Above Right: Workflow of how we went from samples to results<br>Below Left: Bar chart showing increase in linoleic acid when delta 12 desaturase is present<br>Below Right: Heat map showing metabolite abundances </b><br>
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            <p><b><a id="Q3">Behind the scenes of the Molecular Dynamics Simulations</a></b><br>
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For the simulations of FabA, a dimeric structure of FabA (PDB ID: 1MKB) derived by X-ray Diffraction, with a resolution of 2 Å from an E.Coli expression system by<sup>[1]</sup> was used.  
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            <img id="left" src="https://static.igem.org/mediawiki/2013/3/36/Delta12grapholeicacid.png" width="430" height="450"/>
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The molecular dynamics simulation was performed within the GROMACS package using version 4.5.5 [8], with the AMBER99SB force field<sup>[10]</sup>, the transferrable intermolecular potential 3P (TIP3P) water model<sup>[11]</sup> and the original crystal waters, from the X-Ray Crystallography with periodic boundary conditions. The methods for generating both topologies and parameters for G16bP are as described above. For all cases of the Protein in water, a protocol
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<p><b>Further analysis</b><br>
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The data obtained from the LC-MS was enormous. 2721 metabolites were detected in the samples, and so we filtered this down to the 43 fatty acids and phospholipids incorporating the compounds we were interested in (oleic acid and linoleic acid). A heat map was generated (seen above) showing the abundances of these 43 phospholipids and fatty acids in the 17 samples we run on the LC-MS. From this heatmap the diversity of detected compounds and high dynamic range can be seen. For the characterisation of our delta 12 desaturase BioBrick construct, a focus on the individual compounds of high intensity was necessary. An example of this can be seen in the bar chart above. Here you can see that, when fed with oleic acid (to a total w/v concentration of 0.1% and 0.5%), the amount of linoleic acid found within this representative phospholipid is much higher in the delta 12 desaturase expression strain than in the wild-type DH5-alpha strain. From this data we can confidently conclude that the delta 12 desaturase is converting the substrate oleic acid into the linoleic acid. Currently, the linoleic is incorporated into a phospholipid, but expression of the tesA gene (biobricked previously) would cleave the compound away to give free fatty acid. <br>
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<b>A work flow of the methods we used to get from sample to data analysis can be seen above.</b>
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              <p id="footer"><b>Atomic Force Microscopy pictures. Left: WT DH5-alpha. Right: DH5-alpha transformed with delta 12 desaturase expression plasmid.</b><br>
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<p><b>Atomic Force Microscopy</b><br>
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Whilst overexpression of the delta 12 desaturase led to a 4 fold increase in linoleic acid production incorporated in certain phospholipids, we had hypothesised that both overexpression of a non-native membrane protein and the resulting fatty acid composition changes would possibly alter <i>E. coli</i> membrane structure and potentially interfere growth and replication.  To address this, we performed Atomic Force Microscopy (AFM) on transformed wild-type and <i>E. coli</i> transformed with our delta 12 desaturase expression construct. From this we found that there was no significant difference in the membranes between the wild-type and delta 12 desaturase expression constructs.  From this we can conclude that overexpression of the non-native membrane bound delta 12 desaturase using our constitutive promoter system does not significantly alter the membranes. Therefore on an industrial scale the expression construct could be modified, such as by the addition of a stronger promoter sequence and RBS site or potentially using inducible expression systems, thus resulting in a greater production of linoleic acid.
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Latest revision as of 15:53, 28 October 2013

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We submitted and sequenced three biobricks integral to our project. These can be found below:

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This year we submitted and characterised 3 BioBricks, one of which is an improvement of BBa_K925000!

We used an existing BioBrick component with Constitutive promoter and RBS

(BBa_K608002) to express our BioBrick parts:

Successful Expression of delta 9 and delta 12 desaturase, and FabA

In order to characterise our biobricks, we made use of the standard parts found in the registry. By inserting the created biobricks BBa_K1027001 and BBa_K1027002 in to BBa_K608002 (a biobrick consisting of a ribosomal binding site and a constitutive promoter), we were able to create a new construct that expressed the delta 9 desaturase, delta 12 desaturase and FabA proteins. The constructs are shown above.

Plates

Another piece of evidence suggesting that our constructs were successfully expressing our delta 9 desaturase and delta 12 desaturase enzymes was the size of the colonies grown on the plates. Pictures of the plates are shown below. On the far left is a control plate, with bacteria transformed with BBa_K608002 but with no gene inserted in front of the promoter. To the right of that are our delta 12 colonies. They are much smaller than the control, and even taking 20 hours to grow to that size as opposed to the usual 16 hours. We hypothesise that because delta 12 desaturase is a membrane-bound protein that the E. coli does not normally express, constitutively expressing it could inhibit the bacteria and slow growth. Compare this to FabA on the far right. Looking through the literature, we found that overexpression of FabA results in no significant difference in growth size or speed relative to the wild type strain (Luo et al, 2009). Compared to the control plate, we also found that the colonies grew normally.

Gel Digests

To confirm that our desired genes were in fact within the expression construct mentioned above, we carried out test digests of our ligated plasmids. Happily, when we ran our digests on an agarose gel, we saw all of the bands we would predict from the expected fragments. The gel pictures are on the right.
delta 9 desaturase: Cut with BamHI + EcoRV. Expected bands 1424 bp, 1262 bp, 99 bp.
delta 12 desaturase: Cut with BamHI, XbaI, PstI. Expected bands 2127 bp, 656 bp, 430 bp.
FabA Cut with EcoRV. Expected bands 1429 bp, 1115 bp. Cut with EcoRV, PstI. Expected bands 1153 bp, 1115 bp, 339 bp.


Improvement of existing BioBrick

Our biobrick BBa_K1027002 (delta 12 desaturase) is an improvement of the BBa_K925000 biobrick created by the St Andrews team in 2012. We improved this biobrick from the ground up, starting by taking the protein sequence from Synechocystis sp. PCC 6803. This protein sequence was reverse translated and then codon optimised for expression in E. coli. We believe our redesigned biobrick has two features that the original biobrick does not. Firstly, the original biobrick could not be transformed by iGEM HQ, whereas we have managed successful transformation (as shown by the plate pictures). Next, the St. Andrews biobrick was cloned from cyanobacteria, and so is not optimised for expression in E. coli. As St. Andrews then went on to express their delta 12 desaturase biobrick in E. coli it follows that a sequence optimised for expression in this chassis, as ours was, would perform better than the sequence naturally found in cyanobacteria.

Orbitrap LC-MS analysis

Delta 9 desaturase and delta 12 desaturase enzymes were chosen because their products, when expressed in their host organism (Synechocystis sp. PCC 6803), convert stearic acid into oleic acid, and oleic acid into linoleic acid respectively. Therefore, we fed batches of transformed DH5-alpha with 2 different concentrations of exogenous fatty acid (0.1% and 0.5% stearic acid fed to the delta 9 desaturase batch, and 0.1% and 0.5% oleic acid fed to the delta 12 desaturase batch), left the cultures growing overnight and then harvested the cells.

To analyse the metabolites extracted from both wild-type DH5-alpha and DH5-alpha expressing our delta 9 desaturase and delta 12 desaturase enzymes, we made use of the MIB’s in-house Orbitrap Liquid Chromatography - Mass Spectrometry (LC-MS). This technique was chosen because of its high mass accuracy and sensitivity. Upon analysing the most abundant metabolites extracted from our expression strains and comparing this data with the most abundant metabolites extracted from wild-type, it is apparent that a massive increase in linoleic acid (incorporated in phosphatidylethanolamines, PE) has occurred. This is demonstrated in the two figures directly below. The chromatograms produced for the delta 12 desaturase expression strains are also shown below. There is a clear difference between the wild-type E. coli fed with exogenous substrate compared with the E. coli strains expressing delta 12 desaturase. It is probable that the peak appearing around 7.9 min in the delta 12 desaturase strains is due to phospholipid incorporating 18:2 (9Z, 12Z) - linoleic acid.

Further analysis
The data obtained from the LC-MS was enormous. 2721 metabolites were detected in the samples, and so we filtered this down to the 43 fatty acids and phospholipids incorporating the compounds we were interested in (oleic acid and linoleic acid). A heat map was generated (seen above) showing the abundances of these 43 phospholipids and fatty acids in the 17 samples we run on the LC-MS. From this heatmap the diversity of detected compounds and high dynamic range can be seen. For the characterisation of our delta 12 desaturase BioBrick construct, a focus on the individual compounds of high intensity was necessary. An example of this can be seen in the bar chart above. Here you can see that, when fed with oleic acid (to a total w/v concentration of 0.1% and 0.5%), the amount of linoleic acid found within this representative phospholipid is much higher in the delta 12 desaturase expression strain than in the wild-type DH5-alpha strain. From this data we can confidently conclude that the delta 12 desaturase is converting the substrate oleic acid into the linoleic acid. Currently, the linoleic is incorporated into a phospholipid, but expression of the tesA gene (biobricked previously) would cleave the compound away to give free fatty acid.

A work flow of the methods we used to get from sample to data analysis can be seen above.

Atomic Force Microscopy
Whilst overexpression of the delta 12 desaturase led to a 4 fold increase in linoleic acid production incorporated in certain phospholipids, we had hypothesised that both overexpression of a non-native membrane protein and the resulting fatty acid composition changes would possibly alter E. coli membrane structure and potentially interfere growth and replication. To address this, we performed Atomic Force Microscopy (AFM) on transformed wild-type and E. coli transformed with our delta 12 desaturase expression construct. From this we found that there was no significant difference in the membranes between the wild-type and delta 12 desaturase expression constructs. From this we can conclude that overexpression of the non-native membrane bound delta 12 desaturase using our constitutive promoter system does not significantly alter the membranes. Therefore on an industrial scale the expression construct could be modified, such as by the addition of a stronger promoter sequence and RBS site or potentially using inducible expression systems, thus resulting in a greater production of linoleic acid.

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