Development of unified correlations for volumetric mass-transfer coefficient and effective interfacial area in bubble column reactors for various gas-liquid systems using support vector regression

Gandhi, Ankit B. ; Gupta, Prashant P. ; Joshi, Jyeshtharaj B. ; Jayaraman, Valadi K. ; Kulkarni, Bhaskar D. (2009) Development of unified correlations for volumetric mass-transfer coefficient and effective interfacial area in bubble column reactors for various gas-liquid systems using support vector regression Industrial & Engineering Chemistry Research, 48 (9). pp. 4216-4236. ISSN 0888-5885

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Official URL: http://pubs.acs.org/doi/abs/10.1021/ie8003489

Related URL: http://dx.doi.org/10.1021/ie8003489

Abstract

The objective of this study was to develop a unified correlation for the volumetric mass-transfer coefficient (kLa) and effective interfacial area (a) in bubble columns for various gas-liquid systems using support vector regression (SVR-) based modeling technique. From the data published in the open literature, 1600 data points from 27 open sources spanning the years 1965-2007 for kLa and 1330 data points from 28 open sources spanning the years 1968-2007 for a were collected. Generalized SVR-based models were developed for the relationship between kLa (and a) and each design and operating parameters such as column and sparger geometry, gas-liquid physical properties, operating temperature, pressure, superficial gas velocity, and so on. Further, these models for kLa and a are available online at http://www.esnips.com/web/UICT-NCL. The proposed generalized SVR-based correlations for kLa and a have prediction accuracies of 99.08% and 98.6% and average absolute relative errors (AAREs) of 7.12% and 5.01%, respectively. Also, the SVR-based correlation provided much improved predictions compared to those obtained using empirical correlations from the literature.

Item Type:Article
Source:Copyright of this article belongs to American Chemical Society.
ID Code:17438
Deposited On:16 Nov 2010 13:05
Last Modified:28 Jun 2012 05:52

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