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The CFD analysis is made for both batch and continuous models whereas the previous authors carried out the analysis in batch model.
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Batch and continuous modes of treatment were studied.
Experiments performed using reactive distillation in batch and continuous modes, show significant recovery.
In addition, the removal of formaldehyde from water was investigated in both batch and continuous modes.
This occurs in processes that operate in batch, fed-batch, and continuous modes with slow flow rate.
This paper depicts the agglomeration of the particles using batch and continuous system through the mathematical modeling.
The catalytic process A→R along with surface poisoning P+⁎→P⁎ (⁎ is an active site) was modelled for batch and continuous reactors.
Model validation results demonstrate that both batch and continuous sludge settling processes could be accurately described by this model.
A detailed three-phase nonequilibrium (NEQ) dynamic model for simulating batch and continuous catalytic distillation (CD) processes has been developed.
This model enables the effect of temperature and current density to be predicted during both batch and continuous electrosynthesis.
The proposed three-parameter kinetic model describing the overall reaction with a variable mechanism was successfully applied to both batch and continuous reactions.
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