ABSTRACT
A parametric study of the dispersed phase holdup, specific power consumption (P) and axial drop size distribution (ADSD) in a pulsed disc and doughnut column have been carried out with 30% Tri-Butyl Phosphate- 0.01 M nitric acid system. ‘P’ and holdup decreases with increasing percentage duty cycle and increases exponentially with increased pulsation. Whereas ‘P’ remains almost independent of total superficial velocity and phase flow ratio. At the top of the extraction section, the most uniform DSD have been observed. Subsequently, Unified empirical correlations have been developed over much wider range for predicting the holdup and Sauter mean diameter.
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Acknowledgements
The authors are grateful to Professor Dr J. B. Joshi, Emeritus Professor, Homi Bhabha National Institute, for his valuable guidance. The authors also express their sincere gratitude to Dr. M.L Singh, scientific officer, BARC, for helping them understand the techniques of linear regression. Dr. Joti Nath Sharma and Mr. Sukhdeep Singh, scientific officer, BARC, are humbly acknowledged for their valuable guidance in formatting the manuscript.
Disclosure statement
The authors declare no conflict of interest.
Correction Statement
This article has been republished with minor changes. These changes do not impact the academic content of the article.
Annexure-I.
Specific power consumption calculation:
Time =; where d.c = percentage duty cycle; f= frequency of pulsing (Hz)
Liquid mass in the extraction section = Volume of the extration section * Density of the mixed phase = πD2/4 *L * {ρdX + ρc(1–X)}= 3.14 * 0.25 * 0.0752 * 2 * {ρdX+ρc(1–X)} kg = 0.0088 * {ρdX+ρc(1–X)}kg
Specific power consumption= Pressure* W/kg;
The factor has been used to convert the pressure in PSI to Pascal.
Therefore, Specific power consumption= 1586.12* Pressure* W/kg