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<p><h3><b></h3></b></p> | <p><h3><b></h3></b></p> | ||
− | <p> | + | <p>The optimisation potential of PHBV production is huge and as a result of our interaction with stakeholders, we developed a number of design requirements for our PHBV production process:</p> |
+ | <p>- Use of optimised and innovative processes, such as the use of glucose as carbon source instead of feeding propionic acid into the system.</p> | ||
+ | <p>- Use non-food crops and waste streams.</p> | ||
+ | <p>- Innovative and more cost and environmental friendly processes for separation and purification.</p> | ||
+ | <p>- Product design.</p> | ||
+ | <p>- Introduction of sustainable end-of life scenarios such as re-use and recycling.</p> | ||
+ | |||
+ | <p>After incorporating all these design requirements in our final process, the final aim of the team to produce PHBV from waste or industrial by-products. Additionally, we wanted to reduce the impacts of the downstream processing, which is costly environmentally (see our LCA). To demonstrate this we used:</p> | ||
+ | <p> - Bktb/phaCB operon</p> | ||
+ | <p> - Whisky pot ale as raw material</p> | ||
+ | <p> - Phasin and hemolysin secretion system</p> | ||
+ | <p> This section is intended to show how our parts and strategy were implemented and worked as a result of our stakeholders discussions and subsequent design.</p> | ||
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Revision as of 00:15, 18 October 2018