Comparative Study of the Optimized Hydrocyclones H13 and HCOT3 for Maximum Liquid Recovery

Article Preview

Abstract:

In industrial applications, it is very common to use multiple hydrocyclones in parallel to improve the separation. This equipment employs the centrifugal field to promote solid-liquid or liquid-liquid separation. In cases where there is interest in recovering the liquid phase by removing the maximum amount of dispersed phase (waste), such as in oil well drilling units and in water treatment systems, the employment of a hydrocyclone able to promote both the recovering liquid and the concentration of suspension is viable. This paper presents a comparison between two hydrocyclones considered concentrators, called H13 and HCOT3. The results obtained showed that both separators have a satisfactory capacity to concentrate aqueous suspensions, with the underflow-to-throughput ratio equivalent. The Euler number of HCOT3 hydrocyclone was 19% lower than that obtained for the H13 hydrocyclone. Moreover, the results showed that the HCOT3 has a total efficiency of separation 34% greater compared to H13.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

154-159

Citation:

Online since:

July 2017

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2017 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] L. Svarovsky: Solid-Liquid Separation. (Butterworth-Heinemann, fourth ed. Woburn MA, (2000).

Google Scholar

[2] D.O. Silva, L.G.M. Vieira, F.S. Lobato, M.A.S. Barrozo: Chem. Eng. Process. Process. Intensif. Vol. 61 (2012), p.1.

Google Scholar

[3] M.S. Oliveira, R.C. Guimarães, C.H. Ataide, M.A.S. Barrozo: Miner. Eng. Vol. 20 (2007), p.197.

Google Scholar

[4] M.A. Santos, R.C. Santana, F. Capponi, C.H. Ataide, M.A.S. Barrozo: Sep. Purif. Technol. Vol. 76 (2010), p.15.

Google Scholar

[5] E.B. Arruda, J.M.F. Façanha, L.N. Pires, A.J. Assis, M.A.S. Barrozo: Chem. Eng. Process. Vol. 48 (2009), p.1414.

Google Scholar

[6] D.C. Oliveira, C.A.K. Almeida, L.G.M. Vieira, J.J.R. Damasceno, M.A.S. Barrozo: Braz. J. Chem. Eng. Vol. 26 (2009), p.575.

Google Scholar

[7] L.G.M. Vieira, M.A.S. Barrozo, J. J. R. Damasceno: Materials Sci. Forum Vol. 416 (2003), p.317.

Google Scholar

[8] M.A.S. Barrozo, J.J.R. Damasceno, C.A. Silva Junior, L.G.M. Vieira: Sep. Purif. Technol. Vol. 28 (2007), p.282.

Google Scholar

[9] L.G.M. Vieira, M.A.S. Barrozo: Miner. Eng. Vol. 57 (2014), p.50.

Google Scholar

[10] L.G.M. Vieira, D. O. Silva, M.A.S. Barrozo: Sep. Sci. Technol. Vol. 48 (2013), p.2700.

Google Scholar

[11] L.G.M. Vieira, M.A.S. Barrozo, J.J.R. Damasceno: Braz. J. Chem. Eng. Vol. 22 (2005), p.143.

Google Scholar

[12] D.O. Silva, L.G.M. Vieira, F.S. Lobato, M.A.S. Barrozo: Sep. Sci. Technol. Vol. 48 (2013), p.1891.

Google Scholar

[13] C. Aldrich, F.D.L. Uahengo, M. Kistner: Miner. Eng. Vol. 70 (2015), p.14.

Google Scholar

[14] L.G.M. Vieira, J.J.R. Damasceno, M.A.S. Barrozo: Chem. Eng. Process. Vol. 49 (2010), p.460.

Google Scholar

[15] L.G.M. Vieira, B.C. Silvério, J.J.R. Damasceno, M.A. S Barrozo: Can. J. Chem. Eng. Vol. 89 (2011), p.655.

Google Scholar

[16] M.P.B. Martins, N.K.G. Silva, M.A.S. Barrozo, L.G.M. Vieira: XXXVI Congresso Brasileiro de Sistemas Particulados (ENEMP). Maceió, 20 a 23 de Outubro de 2013. Proceeding.. Maceió 2013. (AL).

Google Scholar

[17] K. Price, R. Storn: Dr. Dobb's Journal Vol. 22 (1997), p.18.

Google Scholar

[18] D.O. Silva, L.M. Tamiozzo, C.R. Duarte, V.V. Murata, M.A. S Barrozo: Technol. Vol. 29 (2011, p.286.

Google Scholar

[19] R. Storn, K. Price, J.A. Lampinen: Differential Evolution - A Practical Approach to Global Optimization. (Springer-Verlag Berlin, 2005).

Google Scholar