Team,
The industrial liquid-liquid separators generally follows the stock's law. The sizing equations are well described in many resources e.g. Perry's & GPSA handbooks. However, I couldn't find a way to quantify the seperation improvement if an inlet device has been in the vessel (e.g. simple perforated pipe, baffle,...etc.
Are there empirical formulas to account for these inlet devices?
Your feedback is highly appreciated...
Regards,