"
Team:Bielefeld-Germany/Results/S-Layer/Guide/3b
From 2011.igem.org
(→Expression of S-layer protein under control of T7 promoter in a bioreactor) |
|||
| (One intermediate revision not shown) | |||
| Line 1: | Line 1: | ||
{{Bielefeld_2011_Header}} | {{Bielefeld_2011_Header}} | ||
| - | + | <html><img src="https://static.igem.org/mediawiki/2011/2/28/Bielefeld-header-guide.png"/><p></p></html> | |
=<html><div style="line-height:1.2em;">Expression of S-layer protein under control of T7 promoter in a bioreactor</div></html>= | =<html><div style="line-height:1.2em;">Expression of S-layer protein under control of T7 promoter in a bioreactor</div></html>= | ||
| Line 25: | Line 25: | ||
The following figure shows the expression of an SgsE | luciferase S-layer fusion protein <partinfo>K525311</partinfo> in ''E. coli'' KRX in HSG medium with autoinduction sequencer as described above. Optical density, activity of the fused luciferase, dissolved oxygen and agitator speed are plotted against the cultivation time. | The following figure shows the expression of an SgsE | luciferase S-layer fusion protein <partinfo>K525311</partinfo> in ''E. coli'' KRX in HSG medium with autoinduction sequencer as described above. Optical density, activity of the fused luciferase, dissolved oxygen and agitator speed are plotted against the cultivation time. | ||
| - | [[Image:IGEM-Bielefeld2011-Cultivation311.jpg|650px|thumb|center|'''Fig. 1: Bioreactor cultivation of ''E. coli'' KRX expressing the fusion protein SgsE :: luciferase <partinfo>K525311</partinfo> under the control of a T7 / lac promoter. Induction with 1 mM IPTG and 0.2 % L-rhamnose after 4 h controlled by sequencer. Cultivation in [http://www.gmi-inc.com/BioEngineering-KLF-Small-Laboratory-Fermenter.html#product_desc Bioengineering KLF] bioreactor with 2.5 L [[Team:Bielefeld-Germany/Protocols/Materials#HSG_medium | HSG medium]] with 20 mg L<sup>-1</sup> chloramphenicol starting with OD<sub>600</sub> = 0.4. Dissolved oxygen was regulated to 60 % | + | [[Image:IGEM-Bielefeld2011-Cultivation311.jpg|650px|thumb|center|'''Fig. 1: Bioreactor cultivation of ''E. coli'' KRX expressing the fusion protein SgsE :: luciferase <partinfo>K525311</partinfo> under the control of a T7 / lac promoter. Induction with 1 mM IPTG and 0.2 % L-rhamnose after 4 h controlled by sequencer. Cultivation in [http://www.gmi-inc.com/BioEngineering-KLF-Small-Laboratory-Fermenter.html#product_desc Bioengineering KLF] bioreactor with 2.5 L [[Team:Bielefeld-Germany/Protocols/Materials#HSG_medium | HSG medium]] with 20 mg L<sup>-1</sup> chloramphenicol starting with OD<sub>600</sub> = 0.4. Dissolved oxygen was regulated to 60 % air saturation (controlled with stirrer cascade starting with 200 rpm) and the pH to 7.0 (controlled with 20 % phosphoric acid and 4 M NaOH). The dissolved oxygen sensor had to be recalibrated after about 140 min. ''']] |
Latest revision as of 02:46, 29 October 2011
Expression of S-layer protein under control of T7 promoter in a bioreactor
The expression of S-layer proteins is stressful for Escherichia coli. So using E. coli [http://www.promega.com/products/cloning-and-dna-markers/cloning-tools-and-competent-cells/bacterial-strains-and-competent-cells/single-step-_krx_-competent-cells/ KRX] to express genes under the control of a T7 promoter is an easy way to overexpress your proteins and seperate growth and production phase. This strain carries a T7 polymerase gene under the control of a rhamnose promoter in its genome and it is also optimized for cloning so you do not have to transform your plasmids after assembly in e.g. TOP10, isolate them and bring them in an expression strain like BL21(DE3) - you can go with a single transformation step from assembly to production.
The advantage of a bioreactor over shaking flasks is the possibility to control cultivation parameters like temperature, pH or dissolved oxygen (DO). When cultivating E. coli in shaking flasks the cells are often growing oxygen-limited because of a oxygen transmission rate (normally kLa = 40 - 80 h-1 in shaking flasks but up to 600 h-1 in a bioreactor). The production of acetate and lactate leads to a pH shift shaking flasks. In a bioreactor pH and DO is steady during the whole cultivation leading to higher growth rates and yields of biomass.
For our cultivations we used a [http://www.bioengineering-inc.com/standard-reactors.php?id=2.1 Bioengineering NLF22 7 L] or a [http://www.gmi-inc.com/BioEngineering-KLF-Small-Laboratory-Fermenter.html#product_desc Bioengineering KLF] with Bioengineering DCU and software. We implemented a sequencer which automatically pumped an inducer solution after 4 h cultivation time to start protein expression. Other parameters were:
- Medium: HSG medium with 20 mg L-1 chloramphenicol or 100 mg L-1 ampicillin
- Culture volume: 2.5 - 5 L
- Starting OD600: 0.1 - 0.4
- DO: 60 % air saturation (controlled with stirrer cascade starting with 200 rpm)
- pH: 7.0 (controlled with 20 % phosphoric acid and 4 M NaOH)
- Antifoam: BASF Pluronic PE-8100
- Induction solution: 0.2 % L-rhamnose and 1 mM IPTG
The use of the autoinduction sequencer enables a cultivation over night. The next morning the cells have to be harvested by centrifugation.
Now you have a lot of biomass which you have to disrupt - learn more about it!
The following figure shows the expression of an SgsE | luciferase S-layer fusion protein <partinfo>K525311</partinfo> in E. coli KRX in HSG medium with autoinduction sequencer as described above. Optical density, activity of the fused luciferase, dissolved oxygen and agitator speed are plotted against the cultivation time.
