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The steady state degrees of freedom of a base case design are optimized for a given C4 fresh feed processing rate (Mode I) and maximum production (Mode II).
At the end of the paper the results obtained from the simulation of a base case design are presented and discussed.
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In stage 1, the base case design is generated or selected from literature.
In the second, "design" stage, the processing route from the first stage is further developed and a base case design is established and analyzed.
At stages 1-2, the working scale is at the level of unit operations, where a base case design is identified and analyzed with respect to sustainability metrics.
In stage 2, the base case design is analysed in terms of economics, sustainability and LCA factors in order to identify process hot-spots that are translated into design targets.
At the first level (operation-scale) a conceptual base case design is synthesized through the sequencing of unit operations and subsequently analyzed for identifying process hot-spots using economic, life cycle and sustainability metrics.
In the second stage, the base-case design was analysed through economic evaluation and environmental impact analysis to identify the process "hot spots" and determine targets for improvement.
First, the base-case design was obtained, resulting in the production of ethylene glycol via two steps: ethylene oxidation synthesis followed by ethylene oxide hydration to produce ethylene glycol.
Previously, feasible base-case designs were established but were sub-optimal given the complexity of the model that included more than 200,000 equations.
The case design is based on the iconic Admirals' Cup collection that Corum has been pushing lately.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com