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Development of an effective recovery plan can ensure provision of a number of practical recovery needs.
All the above indicates the practical recovery factor should be between the Darcy model and quasi-linear model.
The adsorption of specific metal ions is the important challenge for the practical recovery of metal ions.
A simple and practical recovery model using minerals, particle size and liberation and association was developed from these data, and various flowsheet configurations were simulated.
Furthermore, an optimisation analysis is carried out on the final design to optimise the process with a high NDMA rejection performance and the practical recovery rate by manipulating the operating conditions of the plant within specified constraints bounds.
These improvements in the recovery profile support hydrotherapy as a practical recovery strategy.
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Finally, economic analyses of a practical heat recovery system with nine heat recovery exchangers are proposed to estimate the saving of the fuel consumption.
Thus, voltage swells during the practical fault recovery change with transients and unbalances.
However, uncertainty is inherent during the process of the practical product recovery.
Finally, the conditions under which gas stripping is a practical product recovery method were established.
Finally, the optimization cases of a series-parallel system with practical heat recovery exchangers are studied.
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