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− | <a href="https://static.igem.org/mediawiki/2016/thumb/2/2c/T--Tianjin--experiment-1.jpg/1043px-T--Tianjin--experiment-1.jpg" data-lightbox="no" data-title="Fig.1 Division of work in bacteria consortium | + | <a href="https://static.igem.org/mediawiki/2016/thumb/2/2c/T--Tianjin--experiment-1.jpg/1043px-T--Tianjin--experiment-1.jpg" data-lightbox="no" data-title="Fig.1 Division of work in bacteria consortium"><img src="https://static.igem.org/mediawiki/2016/thumb/2/2c/T--Tianjin--experiment-1.jpg/1043px-T--Tianjin--experiment-1.jpg" width="100%"></a> |
− | <figcation>Fig.1 Division of work in bacteria consortium | + | <figcation>Fig.1 Division of work in bacteria consortium</figcaption> |
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Whereas, if our bacteria consortium want to achieve their aim, they must work in harmony, therefore, it is necessary find a appropriate environment where these bacteria can normally or supernormally work together. <br/><br/></p> | Whereas, if our bacteria consortium want to achieve their aim, they must work in harmony, therefore, it is necessary find a appropriate environment where these bacteria can normally or supernormally work together. <br/><br/></p> | ||
<p style="font-size:18px" id="ModificationofP.p1">Primarily, we try several kinds of medium and decide to use W medium in the end; next, we optimize culture conditions by change carbon source, nitrogen source and some ions, then, we check growing situations and conditions of the degrading PET, TPA and EG; eventually, 1we can find out a suitable culture condition to co-culture our bacteria consortium. | <p style="font-size:18px" id="ModificationofP.p1">Primarily, we try several kinds of medium and decide to use W medium in the end; next, we optimize culture conditions by change carbon source, nitrogen source and some ions, then, we check growing situations and conditions of the degrading PET, TPA and EG; eventually, 1we can find out a suitable culture condition to co-culture our bacteria consortium. | ||
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− | <a href="https://static.igem.org/mediawiki/2016/thumb/a/a4/T--Tianjin--experiment-2.jpg/1200px-T--Tianjin--experiment-2.jpg" data-lightbox="no" data-title="Fig.2 Idea about optimization of culture conditions | + | <a href="https://static.igem.org/mediawiki/2016/thumb/a/a4/T--Tianjin--experiment-2.jpg/1200px-T--Tianjin--experiment-2.jpg" data-lightbox="no" data-title="Fig.2 Idea about optimization of culture conditions"><img src="https://static.igem.org/mediawiki/2016/thumb/a/a4/T--Tianjin--experiment-2.jpg/1200px-T--Tianjin--experiment-2.jpg" width="100%"></a> |
− | <figcation>Fig.2 Idea about optimization of culture conditions | + | <figcation>Fig.2 Idea about optimization of culture conditions</figcaption> |
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<h3><b>2. Degradation of Ethylene Glycol | <h3><b>2. Degradation of Ethylene Glycol | ||
</b></h3> | </b></h3> | ||
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<h3><b id="ProductionofPHA">3. Production of Polyhydroxyalkanoate</b></h3> | <h3><b id="ProductionofPHA">3. Production of Polyhydroxyalkanoate</b></h3> | ||
− | <p style="font-size:18px"><i>Pseudomonas putida </i>is a natural producer of medium chain length polyhydroxyalkanoates (mcl-PHA), a polymeric precursor of bioplastics. A genome-based in silico model for <i>P. putida KT2440</i> metabolism was employed to identify potential genetic targets to be engineered for the improvement of mcl-PHA production using glucose as sole carbon source. Here, overproduction of pyruvate dehydrogenase subunit AcoA in the <i>P. putida KT2440</i> wild type led to an increase of PHA production. In controlled bioreactor batch fermentations PHA production was increased by 33% in the acoA overexpressing wild type in comparison to <i>P. putida KT2440</i>. Transcriptome analyses of engineered PHA producing P. putida in comparison to its parental strains revealed the induction of genes encoding glucose 6-phosphate dehydrogenase and pyruvate dehydrogenase. In addition, NADPH seems to be quantitatively consumed for efficient PHA synthesis, since a direct relationship between low levels of NADPH and high concentrations of the biopolymer were observed. In contrast, intracellular levels of NADH were found increased in PHA producing organisms. Central metabolism of <i>P. putida KT2440</i> is shown right<sup>[4]</sup>.</p> | + | <p style="font-size:18px"><i>Pseudomonas putida </i>is a natural producer of medium chain length polyhydroxyalkanoates (mcl-PHA), a polymeric precursor of bioplastics. A genome-based in silico model for <i>P. putida KT2440</i> metabolism was employed to identify potential genetic targets to be engineered for the improvement of mcl-PHA production using glucose as sole carbon source. Here, overproduction of pyruvate dehydrogenase subunit AcoA in the <i>P. putida KT2440</i> wild type led to an increase of PHA production. In controlled bioreactor batch fermentations PHA production was increased by 33% in the acoA overexpressing wild type in comparison to <i>P. putida KT2440</i>.</p> |
+ | <p style="font-size:18px" id="AdvantagesofB.s"> | ||
+ | Transcriptome analyses of engineered PHA producing P. putida in comparison to its parental strains revealed the induction of genes encoding glucose 6-phosphate dehydrogenase and pyruvate dehydrogenase. In addition, NADPH seems to be quantitatively consumed for efficient PHA synthesis, since a direct relationship between low levels of NADPH and high concentrations of the biopolymer were observed. In contrast, intracellular levels of NADH were found increased in PHA producing organisms. Central metabolism of <i>P. putida KT2440</i> is shown right<sup>[4]</sup>.</p> | ||
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− | <h3><b | + | <h3><b >4. Advantages of <i>B. subtilis</i> strains |
</b></h3> | </b></h3> | ||
<p style="font-size:18px"id="EnhancedPromoter"><i>Bacillus subtilis</i> has an excellent secretion ability, displays fast growth, and is a nonpathogenic bacterium free of endotoxin <sup>[5] </sup>. It can, therefore, be used in food, enzyme, and pharmaceutical industries and can replace <i>Escherichia coli</i> for protein expression. Furthermore, the extracellular heterogeneous proteins secreted from <i>B. subtilis</i> are more convenient for recovery and purification in large-scale production during downstream processing <sup>[6] </sup>. </p> | <p style="font-size:18px"id="EnhancedPromoter"><i>Bacillus subtilis</i> has an excellent secretion ability, displays fast growth, and is a nonpathogenic bacterium free of endotoxin <sup>[5] </sup>. It can, therefore, be used in food, enzyme, and pharmaceutical industries and can replace <i>Escherichia coli</i> for protein expression. Furthermore, the extracellular heterogeneous proteins secreted from <i>B. subtilis</i> are more convenient for recovery and purification in large-scale production during downstream processing <sup>[6] </sup>. </p> | ||
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<h3><b>8. Lipid Recovery From Biomass</b></h3> | <h3><b>8. Lipid Recovery From Biomass</b></h3> | ||
<p style="font-size:18px">The first goal of our research was to facilitate lipid recovery from biomass. The scientific community widespread disrupts the cyanobacterial cell envelope to achieve the goal. <sup>[10]</sup> (Seog JL et al. 1998)However, all these methods are not economical for large amounts of biomass or add additional cost and reduce the overall utility of the process. Our target is simply to make the cyanobacteria lyse at the appropriate time.</p> | <p style="font-size:18px">The first goal of our research was to facilitate lipid recovery from biomass. The scientific community widespread disrupts the cyanobacterial cell envelope to achieve the goal. <sup>[10]</sup> (Seog JL et al. 1998)However, all these methods are not economical for large amounts of biomass or add additional cost and reduce the overall utility of the process. Our target is simply to make the cyanobacteria lyse at the appropriate time.</p> | ||
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<h2><b id="ExperimentDesign">Experiment Design</b></h2> | <h2><b id="ExperimentDesign">Experiment Design</b></h2> | ||
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We cultivate each of them and the mixture of three in in modified W0 culture medium which changed the carbon source from glucose to sugar for amplification. Then we still did the same 4*3(bacteria liquid and six primer sequences) orthogonal test. Luckily, three bacteria mixed well after cultivating for 12 hours. The number is collected in Table 3. | We cultivate each of them and the mixture of three in in modified W0 culture medium which changed the carbon source from glucose to sugar for amplification. Then we still did the same 4*3(bacteria liquid and six primer sequences) orthogonal test. Luckily, three bacteria mixed well after cultivating for 12 hours. The number is collected in Table 3. | ||
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<h1 style="font-size:200%"><b id="ModificationofB.s">Modification of <i>Bacillus subtilis</i></b></h1> | <h1 style="font-size:200%"><b id="ModificationofB.s">Modification of <i>Bacillus subtilis</i></b></h1> | ||
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<a href="https://static.igem.org/mediawiki/2016/5/52/T--Tianjin--experiment-20.png" data-lightbox="no" data-title="Fig.11 the construction of pHP13-P43 plasmid in advance"><img src="https://static.igem.org/mediawiki/2016/5/52/T--Tianjin--experiment-20.png" width="100%"></a> | <a href="https://static.igem.org/mediawiki/2016/5/52/T--Tianjin--experiment-20.png" data-lightbox="no" data-title="Fig.11 the construction of pHP13-P43 plasmid in advance"><img src="https://static.igem.org/mediawiki/2016/5/52/T--Tianjin--experiment-20.png" width="100%"></a> | ||
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<figure id="BioactivityofPETaseandMHETase"> | <figure id="BioactivityofPETaseandMHETase"> | ||
− | <a href="https://static.igem.org/mediawiki/2016/4/4d/T--Tianjin--kucao4.png" data-lightbox="no" data-title="Fig.12 the construction of pHP13-P43 plasmid | + | <a href="https://static.igem.org/mediawiki/2016/4/4d/T--Tianjin--kucao4.png" data-lightbox="no" data-title="Fig.12 the construction of pHP13-P43-PETase/MHETase plasmid"><img src="https://static.igem.org/mediawiki/2016/4/4d/T--Tianjin--kucao4.png" width="100%"></a> |
− | <figcation>Fig.12 the construction of pHP13-P43 plasmid | + | <figcation>Fig.12 the construction of pHP13-P43-PETase/MHETase plasmid</figcaption> |
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− | <a href="https://static.igem.org/mediawiki/2016/1/1a/T--Tianjin--kucaofig18.png" data-lightbox="no" data-title="Fig.13 | + | <a href="https://static.igem.org/mediawiki/2016/1/1a/T--Tianjin--kucaofig18.png" data-lightbox="no" data-title="Fig.13.cultivation of wild <i>B.subtilis</i> and two recombinant one in LB culture medium"><img src="https://static.igem.org/mediawiki/2016/1/1a/T--Tianjin--kucaofig18.png" width="100%"></a> |
− | <figcation>Fig.13 | + | <figcation>Fig.13.cultivation of wild <i>B.subtilis</i> and two recombinant one in LB culture medium</figcaption> |
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− | <h1 style="font-size:200%"><b id="AControllableLipidProducer | + | <h1 style="font-size:200%"><b id="AControllableLipidProducer" >A Controllable Lipid Producer</b></h1> |
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− | <h3><b >1. Lysis genes(<i>13-19-15</i>)</b></h3> | + | <h3><b id="Lysisgenes">1. Lysis genes(<i>13-19-15</i>)</b></h3> |
− | <p style="font-size:18px">P22 gp13,P22 gp19 and P22 gp 15 are holins, endolysins and auxiliary lysis factors respectively. To construct the holin-endolysin lysis system, they should be connected together with defined sequence. First of all, we obtained the three lysis genes which were synthesized by GENEWIZ separately. Then we use PCR to amplify this part. TA cloning and ligation of Blunt-ended DNA on the T vector were our original idea.However, <i>19</i> and <i>15</i> were spliced via TA cloning according to our presumption. <i>13</i> and <i>19-15</i> were ligated PCR overlap extension method of Warrens et al.<sup>[19]</sup>( Warrens AN et al. 1997)</p> | + | <p style="font-size:18px">P22 gp13,P22 gp19 and P22 gp 15 are holins, endolysins and auxiliary lysis factors respectively. To construct the holin-endolysin lysis system, they should be connected together with defined sequence. First of all, we obtained the three lysis genes which were synthesized by GENEWIZ separately. <br/></p> |
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+ | <p style="font-size:18px" id="ANickelSensingSignalSystem"> | ||
+ | Then we use PCR to amplify this part. TA cloning and ligation of Blunt-ended DNA on the T vector were our original idea.However, <i>19</i> and <i>15</i> were spliced via TA cloning according to our presumption. <i>13</i> and <i>19-15</i> were ligated PCR overlap extension method of Warrens et al.<sup>[19]</sup>( Warrens AN et al. 1997)</p> | ||
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<a href="https://static.igem.org/mediawiki/2016/8/8e/Igem-6803-e3.png" data-lightbox="no" data-title="Fig.14 TA cloning and blunt end ligation"><img src="https://static.igem.org/mediawiki/2016/8/8e/Igem-6803-e3.png" width="100%"></a> | <a href="https://static.igem.org/mediawiki/2016/8/8e/Igem-6803-e3.png" data-lightbox="no" data-title="Fig.14 TA cloning and blunt end ligation"><img src="https://static.igem.org/mediawiki/2016/8/8e/Igem-6803-e3.png" width="100%"></a> | ||
<figcation>Fig.14 TA cloning and blunt end ligation</figcaption> | <figcation>Fig.14 TA cloning and blunt end ligation</figcaption> | ||
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<li><a class="topLink" href="#DegradationofEG">Degradation of EG</a></li> | <li><a class="topLink" href="#DegradationofEG">Degradation of EG</a></li> | ||
<li><a class="topLink" href="#ProductionofPHA">Production of PHA </a></li> | <li><a class="topLink" href="#ProductionofPHA">Production of PHA </a></li> | ||
+ | <li><a class="topLink" href="#AdvantagesofB.s">Advantages of B.s </a></li> | ||
<li><a class="topLink" href="#EnhancedPromoter">Enhanced Promoter-p43 </a></li> | <li><a class="topLink" href="#EnhancedPromoter">Enhanced Promoter-p43 </a></li> | ||
<li><a class="topLink" href="#TheCooperationofTwo">The Cooperation of Two Promoters</a></li> | <li><a class="topLink" href="#TheCooperationofTwo">The Cooperation of Two Promoters</a></li> | ||
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<li><a href="#">Experiment Design </a> | <li><a href="#">Experiment Design </a> | ||
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<li><a href="#">Optimization of Culture Conditions two </a> | <li><a href="#">Optimization of Culture Conditions two </a> |
Latest revision as of 14:55, 28 November 2016
Bacteria Consortium
Overview
After Yoshida and his co-workers found and isolated Ideonella sakaiensis 201-F6, which produced two enzymes to degrades PET, we kept very high interests at their works and also came up with many ordinary ideas to increase the efficiency of degradation reaction. Bacteria consortium is one of the most creative ideas.
The inspiration of this idea comes from nature and also learns from nature. Actually, bacteria never exist alone in our nature, they co-work and cooperate together to achieve an aim or live better in a special condition. Thinking from this point, we established a special bacteria consortium for this enzyme catalysis reaction.
1. Optimization of Culture Conditions
In order to improve efficiency of degrading PET, we are determined to co-culture Pseudomonas putida KT2440, Rhodococcus jostii RHA1 and Bacillus stubtilis 168 (or Bacillus stubtilis DB 104). In our bacteria consortium, work of degradation is divided several parts as follows:
1.Rhodococcus jostii RHA1 is responsible for degrading TPA (terephthalic acid) to remove substrate inhibition;
2. Pseudomonas putida KT2440 is responsible for degrading EG (ethylene glycol) to remove substrate inhibition, and contribute to produce degradable plastics PHA (polyhydroxyalkanoate).
3. Bacillus stubtilis 168 (or Bacillus stubtilis DB 104) is responsible for secreting PETase and MHETase as the main player of degrading PET.
Whereas, if our bacteria consortium want to achieve their aim, they must work in harmony, therefore, it is necessary find a appropriate environment where these bacteria can normally or supernormally work together.
Primarily, we try several kinds of medium and decide to use W medium in the end; next, we optimize culture conditions by change carbon source, nitrogen source and some ions, then, we check growing situations and conditions of the degrading PET, TPA and EG; eventually, 1we can find out a suitable culture condition to co-culture our bacteria consortium.
2. Modification of Pseudomonas putida KT2440
P.putida KT2440 is one of bacteria which can utilize ethylene glycol (EG) at a high speed and meanwhile produces mcl-PHA. In 1988, Lageveen and his co-workers first found mcl-PHA in P.putida KT2440. And then, the metabolism of producing PHA in P.putida KT2440 was reasearched, which found the gene AcoA was the key gene in the procedure. José Manuel Borrero-de Acuña and his co-workers improved the yield by 33% by overexpressing AcoA.
From Björn Mückschel’s works, Ethylene Glycol Metabolism by Pseudomonas putida was found. The key enzymes were identified by comparative proteomics. In P. putida JM37, tartronate semialdehyde synthase (Gcl), malate synthase (GlcB), and isocitrate lyase (AceA) were found to be induced in the presence of ethylene glycol or glyoxylic acid. Under the same conditions, strain KT2440 showed induction of AceA only.
From those studies, we decided to overexpress AcoA and AceA in P.putida KT2440 to help utilize EG as energy source for its growth.
3. Modification of Bacillus subtilis
After some attempt in E.coli and yeast, we look for a new type of host cells- B.subtilis for more secretion. In our experiment, the genes encoding two enzymes are for the first time expressed in S.cerevisiae. Increased yields of PETase and MHETase enzymes are achieved when B. subtilis strains 168 and DB104 (deficient in two and three extracellular proteases, respectively[1]) were transformed with the recombinant plasmid with the help of the enhanced promoter-p43.
4. A Controllable Lipid Producer
Cyanobacteria are excellent organisms for biofuel production. We thus have selected Cyanobacterium Synechocystis sp. PCC 6803 as the source of carbon in our mixed bacteria system. Our target is simply to make the cyanobacteria lyse at the appropriate time by transforming a plasmid contained three bacteriophage-derived lysis genes which were placed downstream of a nickel-inducible signal transduction system into the Synechocystis 6803.
In this part of our project, Cyanobacterium Synechocystis sp. PCC 6803 was selected as a model organism as the source of carbon in our mixed bacteria system. We simply to establish a cell wall disruption process which could make the cyanobacteria lyse at the appropriate time.
Theoretical Background
1. Degradation of Terephthalate
Rhodococcus sp. strain RHA1 is thought to be capable of degrading a wide range of aromatic compounds including terephthalate acid (TPA). in 2006, a reliable pathway consisting of Distinct ring cleavage dioxygenase systems and protocatechuate (PCA) pathway was come up with, and the proposed degradation pathway for TPA is shown as below[2].
2. Degradation of Ethylene Glycol
By employing growth and bioconversion experiments, directed mutagenesis, and proteome analysis, it is found that Pseudomonas putida KT2440 does not grow within 2 days of incubation, compared to Pseudomonas putida JM37 which can grow rapidly under the same conditions. The key enzymes and specific differences between the two strains were identified by comparative proteomics. In P. putida JM37, tartronate semialdehyde synthase (Gcl), malate synthase (GlcB), and isocitrate lyase (AceA) were found to be induced in the presence of ethylene glycol or glyoxylic acid. Under the same conditions, strain KT2440 showed induction of AceA only. Postulated pathway for the metabolism of ethylene glycol in Pseudomonas putida strains KT2440 and JM37 is shown left[3].
3. Production of Polyhydroxyalkanoate
Pseudomonas putida is a natural producer of medium chain length polyhydroxyalkanoates (mcl-PHA), a polymeric precursor of bioplastics. A genome-based in silico model for P. putida KT2440 metabolism was employed to identify potential genetic targets to be engineered for the improvement of mcl-PHA production using glucose as sole carbon source. Here, overproduction of pyruvate dehydrogenase subunit AcoA in the P. putida KT2440 wild type led to an increase of PHA production. In controlled bioreactor batch fermentations PHA production was increased by 33% in the acoA overexpressing wild type in comparison to P. putida KT2440.
Transcriptome analyses of engineered PHA producing P. putida in comparison to its parental strains revealed the induction of genes encoding glucose 6-phosphate dehydrogenase and pyruvate dehydrogenase. In addition, NADPH seems to be quantitatively consumed for efficient PHA synthesis, since a direct relationship between low levels of NADPH and high concentrations of the biopolymer were observed. In contrast, intracellular levels of NADH were found increased in PHA producing organisms. Central metabolism of P. putida KT2440 is shown right[4].
4. Advantages of B. subtilis strains
Bacillus subtilis has an excellent secretion ability, displays fast growth, and is a nonpathogenic bacterium free of endotoxin [5] . It can, therefore, be used in food, enzyme, and pharmaceutical industries and can replace Escherichia coli for protein expression. Furthermore, the extracellular heterogeneous proteins secreted from B. subtilis are more convenient for recovery and purification in large-scale production during downstream processing [6] .
5. Enhanced Promoter-p43
In order to increase secretion, some enhanced promoters are necessary. However, native gene in a high-copy number plasmid was found to be unstable in B. subtilis[5] . To optimize the production and the stability of the expression vectors, both the promoter and the signal sequence of PETase were replaced by B. subtilis P43 promoter, a constitutively expressed promoter. This overcame the plasmid instability problem.
6. The Cooperation of Two Promoters-p43+psacB
Interestingly, the cooperation of two promoters in B. subtilis are easily found. For example, An endoglucanase from Bacillus akibai I-1 was successfully overexpressed in Bacillus subtilis 168 by the help of p43 promoter and the expression level of the recombinant enzyme was greatly enhanced by using the sucrose-inducible psacB promoter[7] .The construction of plasmid is in the Figure 1 . Thus, we are willing to try whether the combination of p43 and psacB can make a difference in the secretion of enzyme.
7. Lipid Producer
Photosynthetic microorganisms, including eukaryotic algae and cyanobacteria, are being optimized to overproduce numerous biofuel. According to previous data, algae accumulate large quantities of lipid as storage materials, but they do this when under stress and growing slowly. By contrast, cyanobacteria accumulate lipids in thylakoid membranes, which are associated with high levels of photosynthesis and a rapid growth rate. Thus, photo-synthetic bacteria have a natural advantage for producing lipids at a high rate. Furthermore, being prokaryotes can be improved by genetic manipulations much more readily than can eukaryotic algae. [8] Therefore, we decided to do something to make cyanobacteria ,the lipid producer, more appropriate for our project.
Synechococcus elongatus PCC7942 has larger capacity of lipid production than Synechocystis sp. PCC6803 but accumulates most of the product in the cell because of the imbalance of the rates of lipid production and secretion. Initially, we intended to do something to increase lipid secretion by knocking the wzt gene[9] (Akihiro Kato et al. 2016), however, Synechococcus elongatus PCC7942 wasn’t able to revive in two-week shaking cultivation. So we turned into Synechocystis sp.PCC 6803.
8. Lipid Recovery From Biomass
The first goal of our research was to facilitate lipid recovery from biomass. The scientific community widespread disrupts the cyanobacterial cell envelope to achieve the goal. [10] (Seog JL et al. 1998)However, all these methods are not economical for large amounts of biomass or add additional cost and reduce the overall utility of the process. Our target is simply to make the cyanobacteria lyse at the appropriate time.
We found that the cyanobacterial cell envelope is composed of 4 layers: the external surface layers ;the outer membrane; the polypeptidoglycan which is considerably thick, and the cytoplasmic membrane. [11] ( Hoiczyk E et al. 2000)To break up the peptidoglycan layer, we applied the holin-endolysin lysis strategy used by bacteriophages to exit bacterial cells[12] (Wang IN et al. 2000).Endolysins are peptidoglycan-degrading enzymes that attack the covalent linkages of the peptidoglycans that maintain the integrity of the cell wall. In addition to endolysins, some auxiliary lysis factors are involved in cleaving the oligopeptide linkages between the peptidoglycan and the outer membrane lipoprotein. Holins are small membrane proteins that produce nonspecific lesions (holes) in the cytoplasmic membrane from within, allow the endolysins and auxiliary lysis factors to gain access to the polypeptidoglycan layers, and trigger the lysis process. In this way, the cell wall is easy to break up.
9. Control The Lysis System
To control the appropriate time, a nickel sensing/responding signal system[13] (Garcia-Dominguez M et al. 2000) was used to control the timing of the expression of phage lysis genes in Synechocystis 6803.
Our strategy for achieving our target is to construct a expression vector pCPC3031-Ni-13-19-15 introduced the Salmonella phage P22 lysis cassette (13-19-15) with a Spectinomycin selection marker downstream of the promoter Pni, a nickel responding signal operon. Synechocystis 6803 with the pCPC3031-Ni-13-19-15 will lyse after Ni2+ addition.
Modification of Pseudomonas putida KT2440
1. Overexpression of AcoA and AceA in P.putida KT2440
AcoA and AceA are the crucial genes for production of PHA and utilization of EG, so overexpressing these two genes is beneficial to improve the efficiency of degradation reaction and accumulation of PHA. Based on this idea, we established a expression vector which can be used in P.putida KT2440.
Based on the shuttle plasmid pBBR1MCS-2, we established the overexpression vector. The target genes were obtained by colony PCR and were ligated to the plasmid by T4 DNA ligase. The target genes are leaded by a T3 promoter.
After we established the vector, we transformed it to competent cell of E.coli and amplified it.
2. Electroporation of P.putida KT2440
Procedure:
(1) 10 ml LB + 0.1 ml Overnight culture of P.putida KT2440;
(2) Centrifugation at 5000 rpm for 10 min at 4 degrees centigrade;
(3) Wash the precipitation (P.putida KT2440) with ice cold Elec-Buffer * 3;
(4) Re-suspend in 20 microliter Elec-Buffer;
(5) 4 microliter or 9 microliter suspension + 1 microliter of DNA(50 ng);
(6) Place 5 microliter or 10 microliter samples in Electrode Pin(5.6 mm diameter?) (50 microliter in Electrode Pin(1 mm diameter)?);
(7) Electroporation at 1.2 kV, 200 Ω, and 25 μF.
(8) Add 1-2 ml SOC Medium and culture at 30 degrees centigrade for 2 h
(9) Spread on selection plate (LB agar with Kanamycin)
P.S. Elec-Buffer is 10% Glycerol.
3. Detection of PHA in P.putida KT2440
Procedure:
(1) take a certain amount of bacteria in the extraction bottle, add 15mL chloroform for each 1g bacteria, and place the extraction bottle in a high-pressure reaction kettle at 100 degrees Centigrade to react for 4h.
(2) After cooling, filter.
(3) Slowly add 10 times the volume of ethanol, cooling and stirring.
(4) Place at 4 degrees centigrade over night.
(5) After pressure reduction and pressure filtration, dehydrate the PHA in vacuum drying oven for 24h, weigh and record.
Modification of Bacillus subtilis
1. Recombinant Plasmid Construction and Transformation
E.coli with gene of PETase and MHETase and vector of pHP13-p43 has been inoculated in tubes of LB culture. The plasmid is constructed in advance(Figure 13).
The Plasmids were isolated and enzyme digested using EcoR I and BamH I restriction enzyme. After gel extraction to get right band, construction of pHP13-p43 + PETase and pHP13-p43 + MHETase were caught out. The successfully constructed vectors, pHP13-p43 + PETase and pHP13-p43 + MHETase, were respectively transferred into E.coli and then E.coli were cultivated on chloramphenicol-containing LB plates to filter positive colony.(Figure 14) The positive colony of PETase and of MHETase were inoculated into tubes containing LB with chloramphenicol. Then well-constructed vectors were isolated. Vectors were respectively transferred into B.subtilis and then B.subtilis were cultivated on erythromycin-containing LB plates to filter positive colony. Above all, we got 2 strains of B.subtilis respectively secret PETase and MHETase.
2. Bioactivity of PETase and MHETase
In order to test the bioactivity of PETase and MHETase, we have two methods. First, we use hydrolysis of pNPA through degradation rate. We cultivated wild B.subtilis and recombinant one in modified LB culture medium, which add PNPA solution through filtering(pNPA has a very low solubility in water).
After some days, we take 1 ml bacteria liquid each and centrifuge them for 12000r/min. Then we take the supernatant and measure solution absorbance at 400 nm, which is an obvious absorption peak of p-nitrophenol. If there is an an obvious absorption peak at 400 nm, we prove the bioactivity of PETase and MHETase in B.subtilis.
Second, we make orthogonal test. We cultivated wild B.subtilis and two recombinant one in LB culture medium(Figure 15). We put PET in wild one and one of the recombinant B.subtilis. Then, we imitate of the first methods and measure solution absorbance at 260 and 240 nm , which is an obvious absorption peak of MHET and TPA.
A Controllable Lipid Producer
1. Lysis genes(13-19-15)
P22 gp13,P22 gp19 and P22 gp 15 are holins, endolysins and auxiliary lysis factors respectively. To construct the holin-endolysin lysis system, they should be connected together with defined sequence. First of all, we obtained the three lysis genes which were synthesized by GENEWIZ separately.
Then we use PCR to amplify this part. TA cloning and ligation of Blunt-ended DNA on the T vector were our original idea.However, 19 and 15 were spliced via TA cloning according to our presumption. 13 and 19-15 were ligated PCR overlap extension method of Warrens et al.[19]( Warrens AN et al. 1997)
2.A Nickel Sensing/Responding Signal System(pCPC3031-Ni)
Ni activates the transcription of downstream genes of Pni and positively autoregulates its own synthesis. The amount of mRNA increased about 20-fold within 4 h after Ni addition. First, Pni was cloned into pCPC3031 and was amplified by using PCR. Then we cut the plasmid with Nru I, after that the lysis genes, 13-19-15, were placed downstream of Pni. What’ more, we handed in the plasimids for sequencing, which confirmed its correctness.
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