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Information Journal Paper

Title

MODELING OF MASS TRANSFER OF NON-SPHERICAL DROPS IN LIQUIDLIQUID EXTRACTION COLUMNS

Pages

  17-26

Abstract

 In this paper, mass transfer modeling of NON-SPHERICAL DROPS, when the drops are a segment of an ellipse, was carried out. Predicted results obtained by the new and Handlos-Baron models and experimental data were compared. The dimensions of the NON-SPHERICAL DROPS were optimized by using the experimental data. In this work, the Olney's model using Klee & Treybal drop terminal velocity correlations were utilized to model the hydrodynamics of the column. Mass transfer of the column was also modeled using forward mixing, and the required drop sizes were obtained from experimental data. 95% confidence limits in predicting the plug flow number of transfer units using Handlos-Baron and new model were calculated and the values of this parameter are 32.78% and 11.11% respectively.

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  • Cite

    APA: Copy

    BASTANI, D., PANAHI, MASOUD, & MOAZAMI, M.. (2009). MODELING OF MASS TRANSFER OF NON-SPHERICAL DROPS IN LIQUIDLIQUID EXTRACTION COLUMNS. PETROLEUM RESEARCH, 19(59), 17-26. SID. https://sid.ir/paper/114940/en

    Vancouver: Copy

    BASTANI D., PANAHI MASOUD, MOAZAMI M.. MODELING OF MASS TRANSFER OF NON-SPHERICAL DROPS IN LIQUIDLIQUID EXTRACTION COLUMNS. PETROLEUM RESEARCH[Internet]. 2009;19(59):17-26. Available from: https://sid.ir/paper/114940/en

    IEEE: Copy

    D. BASTANI, MASOUD PANAHI, and M. MOAZAMI, “MODELING OF MASS TRANSFER OF NON-SPHERICAL DROPS IN LIQUIDLIQUID EXTRACTION COLUMNS,” PETROLEUM RESEARCH, vol. 19, no. 59, pp. 17–26, 2009, [Online]. Available: https://sid.ir/paper/114940/en

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