Journal of Applied Science and Engineering

Published by Tamkang University Press

1.30

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2.10

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Ho-Ming Yeh This email address is being protected from spambots. You need JavaScript enabled to view it.1 and Ching-Chun Hsu1

1Energy and Opto-Electronic Materials Research Center, Department of Chemical and Materials Engineering, Tamkang University, Tamsui, Taiwan 251, R.O.C.


 

Received: June 4, 2010
Accepted: December 9, 2010
Publication Date: June 1, 2011

Download Citation: ||https://doi.org/10.6180/jase.2011.14.2.08  


ABSTRACT


The expressions of mass transfer rate for membrane extraction through a rectangular module with external recycle have been derived under cocurrent-flow, countercurrent-flow and cross-flow operations based on the modified correction-factor analysis coupled with the mass balances. These expressions are explicit and the results can be readily calculated without using try-and-error method, which should be employed in the classical correction-factor analysis for designing heat and mass exchangers. For cross-flow operation, the correction factors are function of flow rate, mass-transfer area, distribution coefficient and overall mass-transfer coefficient, and some values of them are given graphically. Considerable improvement in mass transfer rate is achievable if the devices are operated with recycle, leading to increase the mass transfer coefficient.


Keywords: Membrane Extraction, Rectangular Module, Modified Correction Factor, Internal Recycle


REFERENCES


  1. [1] Treybal, R. E., “Liquid Extraction,” 2nd ed., McGraw-hill, New York, Chapter 11 (1963).
  2. [2] Lo, T. C. and Baird, M. H. I., “Lquid-Liguid Extraction” in M. Grayson (Ed.), Kirktothmer Encycloedia of Chemical Technology, Vol. 9, 3rd ed., Wiley, New York (1980).
  3. [3] Porter, M. C., Handbook of Industrial Membrane Technology, Noyes Publications, New Jersey, pp. 13, 175 (1990).
  4. [4] Kiani, A., Bhave, R. R. and Sirkar, K. K., “Solvent Extraction with Immobilized Interfaces in Microporous Membrane,” J. Membr. Sci., Vol. 20, p. 125 (1984).
  5. [5] Prasad, R., Kiani, A., Bhave, R. R. and Sirkar, K. K., “Further Studies on Solvent Extraction with Immobilized Interfaces in a Microporous Hydrophobic Membrane,” J. Membr. Sci., Vol. 26, p. 76 (1986).
  6. [6] Yang, M. C. and Cussler, E. L., “Designing HollowFiber Contractors,” AIChE J., Vol. 32, p. 1910 (1986).
  7. [7] Prasad, R. and Sirkar, K. K. “Dispersio-Free Solvent Extraction with Microporous Hollow-Fiber Modules,” AIChE J., Vol. 34, p. 177(1998).
  8. [8] Ding, H. and Cussler, E. L., “Fractional Extraction with Hollow Fibers with Hydrogelfilled Walls,” AIChE J., Vol. 37, p. 855 (1991).
  9. [9] Yeh, H. M., Peng, Y. Y. and Chen, Y. K., “Solvent Extraction through a Double-Pass Parallel-Plate Membrane Channel with Recycle,” J. Membr. Sci., Vol. 163, p. 177 (1999).
  10. [10] Yeh, M. H. and Chen, Y. K., “The Effect of Multipass Arrangement on the Performance in a Membrane Extraction of Fixed Configuration,” Chem. Eng. Sci., Vol. 55, p. 5873 (2001).
  11. [11] Yeh, H. M. and Hsu, Y. S., “Analysis of Membrane Extraction through Rectangular Mass Exchangers,” Chem. Eng. Sci., Vol. 54, p. 897 (1999).
  12. [12] Yeh, H. M., “Membrane Extraction in Rectangular Module with External Recycle,” J. Taiwan Inst. Chem. Engrs., Vol. 39, p. 679 (2008).
  13. [13] Bowman, R. A., Mueller, A. C. and Nagle, W. M., “Mean Temperature Difference in Design,” Trans. Am. Mech. Engrs., Vol. 62, p. 283 (1940).
  14. [14] Yeh, H. M., “Modified Correction-Factor Analysis of Solvent Extraction in Rectangular Membrane Modules,” J. Chinese Inst. Chem. Engrs., Vol. 38, p. 385 (2007).
  15. [15] Yeh, H. M. and Huang C. H., “Solvent Extration in Multipass Parallel-Flow Mass Exchangers of Microporous Hollow-Fiber Modules,” J. Membr. Sci., Vol. 103, p. 135 (1995).
  16. [16] Chen, Y. K., “The Influence of Aspect Ratio on Separation Performance in Flat-Plate Cross-Flow Membrane Extractors,” Master Thesis, Tamkang University, Tamsui, Taiwan (1999).
  17. [17] Yeh, H. M., “Effect of Reflux and Reflux-Barrier Location on Solvent Extraction through Cross-Flow Flat-Plate Membrane Modules with Internal Reflux,” J. Membr Sci., Vol. 269, p. 133 (2006).