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Suitable solvent inlet and outlet ports are located on two opposite sides of the sorbent layer.
In terms of desorption the model predicted both where desorption was occurring (solvent inlet, column, reboiler) and the total amount of CO2 desorbed.
The proposed procedure was able to control the extraction process under individual and simultaneous step disturbances in the initial content of oil in the solids and in the solvent inlet concentration.
An interface including a splitter and a make-up solvent inlet was found to be the best compromise and exhibited good detection sensitivity while maintaining more than 75% of the chromatographic efficiency.
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The ability to use unequal feed/anti-solvent inlet flowrates (in the Roughton vortex mixer) proved effective in controlling the batch CSD at 2% seed loading and constant feed composition.
We also discovered significant response differences with solvents, inlet temperatures, inlet liners, and OPAH stability not previously reported for this compound class.
Seeds of the stable β-form of LGA were produced using a reverse jet anti-solvent crystallisation process and introduced to the crystalliser immediately downstream of the growth solution inlet.
These models were implemented in programming software, where it was possible to obtain results, as variations in the length of pipe, type of solvent and inlet temperature.
3-MF vapor was generated by injecting liquid solvent into inlet air by means of a high-pressure piston pump (Gilson 302, Gilson, Villiers-le-bel, France).
Based on numerical simulations the impact of the two inlet solvent compositions is demonstrated in terms of the size and shape of regions of applicable flow-rates.
The effects of the main operating parameters (i.e., inlet CO2 loading, solvent concentration, liquid flow rate, CO2 partial pressure, inert gas flow rate, and liquid feed temperature) on KGav were investigated.
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CEO of Professional Science Editing for Scientists @ prosciediting.com