Difference between revisions of "Team:CCU Taiwan/Engineering"
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<p class="first">Sketch</p> | <p class="first">Sketch</p> | ||
| − | <p class="description">Fermenting→ Filtering→ Reacting→ Extraction→ Particle Manufacturing</p> | + | <div id="Line1" class="polaroid" style="display:inline-block"> |
| + | <img src="https://static.igem.org/mediawiki/2018/b/b0/T--CCU_Taiwan--LAI_ProductionLine.jpg" width="100%"> | ||
| + | <div class="container"> | ||
| + | <p>Figure1: Sketch of our designed production line.</p> | ||
| + | </div> | ||
| + | </div> | ||
| + | <p class="description">Process:Fermenting→ Filtering→ Reacting→ Extraction→ Particle Manufacturing</p> | ||
<br><p class="first">Devices</p> | <br><p class="first">Devices</p> | ||
<p class="description"><strong>1. Fermentation tank:</strong><br> | <p class="description"><strong>1. Fermentation tank:</strong><br> | ||
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<p class="description">Follow figures were complete design diagram of our production line</p> | <p class="description">Follow figures were complete design diagram of our production line</p> | ||
| − | <div id=" | + | <div id="Line2" class="polaroid" style="display:inline-block"> |
<img src="https://static.igem.org/mediawiki/2018/9/93/T--CCU_Taiwan--LAI_productionline.jpg" width="100%"> | <img src="https://static.igem.org/mediawiki/2018/9/93/T--CCU_Taiwan--LAI_productionline.jpg" width="100%"> | ||
<div class="container"> | <div class="container"> | ||
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<img src="https://static.igem.org/mediawiki/2018/3/32/T--CCU_Taiwan--LAI_production_fermentationtank.jpg" width="100%"> | <img src="https://static.igem.org/mediawiki/2018/3/32/T--CCU_Taiwan--LAI_production_fermentationtank.jpg" width="100%"> | ||
<div class="container"> | <div class="container"> | ||
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<img src="https://static.igem.org/mediawiki/2018/a/ad/T--CCU_Taiwan--LAI_production_filter.jpg" width="100%"> | <img src="https://static.igem.org/mediawiki/2018/a/ad/T--CCU_Taiwan--LAI_production_filter.jpg" width="100%"> | ||
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<img src="https://static.igem.org/mediawiki/2018/e/e7/T--CCU_Taiwan--LAI_production_reactiontank.jpg" width="100%"> | <img src="https://static.igem.org/mediawiki/2018/e/e7/T--CCU_Taiwan--LAI_production_reactiontank.jpg" width="100%"> | ||
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<img src="https://static.igem.org/mediawiki/2018/7/70/T--CCU_Taiwan--LAI_productionline_extrction.jpg" width="100%"> | <img src="https://static.igem.org/mediawiki/2018/7/70/T--CCU_Taiwan--LAI_productionline_extrction.jpg" width="100%"> | ||
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<img src="https://static.igem.org/mediawiki/2018/f/f5/T--CCU_Taiwan--LAI_production_pelletforming.jpg" width="100%"> | <img src="https://static.igem.org/mediawiki/2018/f/f5/T--CCU_Taiwan--LAI_production_pelletforming.jpg" width="100%"> | ||
<div class="container"> | <div class="container"> | ||
Revision as of 18:31, 17 October 2018
PRODUCTION LINE
Sketch
Figure1: Sketch of our designed production line.
Process:Fermenting→ Filtering→ Reacting→ Extraction→ Particle Manufacturing
Devices
1. Fermentation tank:
TFY-MS automatic mechanical stirring fermentation tank 50L
Working capacity: 65~75%
Product features: The fermentation tank adopts a mechanical stirring system, the stirrer speed can be adjusted continuously. The fermentation temperature, pH, dissolved oxygen and other parameters are automatically controlled, automatically recorded, stored, printed, and suitable for small test and pilot test of fermentation products.
2. Filtration device:
Use membrane filtration to prevent yeast from leaving the system.
3. Reaction tank
Reacted the enzyme with the monolignol, and added other essential material (buffer and H2O2). The capabilities are acid and alkali control, stirring, temperature control and pressure control.
Type: T.T-M.I-2000
Full capacity: 2000 L
Output: 15-50 kg / Hr
4. Low temperature concentration separation extraction system:
The device was filtered by membrane and separated by different molecular weight to separate different substances. Using this equipment, LIGGREEN would be extracted and purified.
Microfiltration membrane: MF Membrane 0.1~0.3um
Membrane area: 5m2
Diluted liquid volume: approximately 100 L / Hr
Temperature: up to 50° C
5. Extrusion granulation (Twin screw)
After heated material to the melting point, it was pumped (Liquid flowed out a tube and cut when it was cooled by air) to form particles, which made LIGREEN into a smaller particulates.
Type: TS 30
Output: 15-50 kg / Hr
Extruder: 7.5-18 kW
Design diagram
Follow figures were complete design diagram of our production line
Figure1: Design of our entire production line.
Figure2: Figure of the fermentation tank.
Figure3: Figure of the filtration device.
Figure4: Figure of the reaction tank.
Figure5: Figure of the low temperature concentration separation extraction system.
Figure6: Figure of the Extrusion granulation, and we would get production at last.