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The various scenarios simulated in this work give an indication of how a future process for the integration of 2G and 1G ethanol production from sugar cane could be designed in order to achieve the lowest 2G ethanol production cost.
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They are believed to be important technologies for retrofitting existing processes and for incorporation into future processes for efficient and flexible (bio chemical production.
Future process studies designed for disentangling the role of momentum and buoyancy forcing in driving the ACC and MOC are proposed.
Recommendations for future process studies are provided.
Furthermore, the kinetics for SFILs in the esterification of geraniol were determined as the basis for future process design.
It includes two important parts, namely moving object extraction and shadow detection and removal, shown in Sections 2 and 3. Section 2 lays foundation for future process.
In general the model predicts the performance of the plant well (to within ±5%) and will be important for future process development, design and optimisation.
We also performed the recording of dynamic parameters and static voltage current characteristic was also recorded in order to model generator and chamber and use it for future process control.
From this we conclude, that TASTE not only offers an enormous degree of freedom for future process variations, but also will advance the patterning capabilities of current standard 3D micro- and nanofabrication methods.
The developed model and optimum conditions could be used for future process scale-up.
In this review we considered valorization options for cereals based biorefineries wastes while identifying their challenges and exploring the opportunities for future process.
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