Continuous Melt Suspension Crystallization of Phosphoric Acid

Abstract

A continuous melt suspension crystallization process has been presented for the purification of the phosphoric acid in this study, which is performed in the cascade of a mixed suspension mixed product removal (MSMPR) crystallizer and a gravity wash column for the subsequent solid-liquid separation. Dynamic behavior in the crystallizer and role of reflux ration on the purification efficiency of column are studied in detail. A reasonable steady state with respect to the liquid phase is achieved after 2 to 3 hrs, which is followed by a solid-phase steady state in terms of the slurry density after 4 hrs. Reflux ratio is the effective parameter for separation and purification by the crystallization equipment from the influences of reflux ratio on the purity of product, the number of theoretical plates and the stability of the operations.

Share and Cite:

A. Chen, J. Zhu, B. Wu, K. Chen and L. Ji, "Continuous Melt Suspension Crystallization of Phosphoric Acid," Journal of Crystallization Process and Technology, Vol. 2 No. 3, 2012, pp. 111-116. doi: 10.4236/jcpt.2012.23014.

Conflicts of Interest

The authors declare no conflicts of interest.

References

[1] P. Becker, “Phosphates and Phosphoric Acid,” Marcel Decker Inc., New York, 1983.
[2] M. Feki, “Contribution to the phosphoric-acid purification of wet process by extraction with the methyl-isobutylcetone,” Ph.D. Thesis, University of Sciences, Tunis, 2001.
[3] R. Dhouib-Sahnoun, M. Feki and H.F. Ayedi, “Extractive purification of wet phosphoric acid with tributyl-phosphate: study of the impurities distribution,” J. de la Sciété de Tunisie, Vol. 8, 2000, pp. 873-885.
[4] A.M. Urtiaga, A. Alonso, I. Ortiz, J.A. Daoud and S.A. El-Reefy, “Comparison of liquid membrane processes for the removal of cadmium from wet phosphoric acid,” J. Membr. Sci., Vol. 164, No. 1, 2000, pp. 229-240.
[5] V. Kislik and A. Eyal, “Aqueous hybrid liquid membrane process for metal separation. Part II. Selectivity of metals separation from wet-process phosphoric acid,” J. Membr. Sci., Vol. 169, No. 1, 2000, pp. 133-146.
[6] J.F. McCullough, “Phosphoric acid purification: comparing the process choices,” Chem. Eng., Vol. 83, 1976, pp. 101-106.
[7] W.J. Huang, “Progress in the field of purifying wet-process phosphoric acid by solvent precipitation,” Chem. Eng. Prog., Vol. 6, 1997, pp. 39-43.
[8] Jian Zhu, “Preparation of electric-grade phosphoric acid by melt crystallization,” CN Patent No. 1843900, 2006.
[9] Hongyuan Wei and Leping Dang, “Purification of phosphoric acid by crystallization,” CN Patent No. 1730385, 2006.
[10] Kim Chul Ung and Koh Jae Cheon, “Purification method of phosphoric acid through layer crystallization including washing operation,” KR Patent No. 20060111282(A), 2006.
[11] Aaltonen, Jarmo and Sakari, “Process for production of phosphoric acid by crystallization of phosphoric acid hemihydrates,” WO Patent No. 00/59827, 2000.
[12] Yamazaki Yasuo, Tabei Seikichi and Negishi Kat-suyuki, “High purity phosphoric acid,” JP Patent No. 2000026111, 2000.
[13] Tadeusz K., Wiewiorowski, Phillip D. Mollere, Vivian C. Astley and David M.Dyer, “Phosphoric acid crystallization process,” US Patent No. 4655789, 1987.
[14] Hara Hisao, Yoshikawa Akihisa and Kubo Masao, “Production of highly purified phosphoric acid,” JP Patent No. 2225309, 1990.
[15] M. Matsuoka, T. Fukuda, Y. Takagi and H. Takiyama, “Purification of Organic Solid Solutions by Melt Crystallization: Comparison between Layer and Suspension Crystallization,” J. Cryst. Growth, Vol. 166, No. 1, 1996, pp. 1035-1039.
[16] Ana Paula Badan Ribeiro, Rodrigo Corrêa Basso and Renato Grimaldi, “Influence of chemical interesterification on thermal behavior, microstructure, polymorphism and crystallization properties of canola oil and fully hydrogenated cottonseed oil blends,” Food Res. Int., Vol. 42, No. 8, 2009, pp. 1153-1162.
[17] L. Svanberg, L. Ahrné, N. Lorén and E. Windhab, “Effect of sugar, cocoa particles and lecithin on cocoa butter crystallization in seeded and non-seeded chocolate model systems,” J. Food Eng., Vol. 104, No. 1, 2011, pp. 70-80.
[18] H. Miki, R. Fukunaga, Y. Asakuma, K. Maeda and K. Fukui, “Distribution of dye into KDP crystals in a continuous MSMPR crystallizer,” J. Sep. Purif. Technol., Vol. 43, No. 1, 2005, pp. 77-83.
[19] H. Miki, T. Terashima, Y. Asakuma, K. Maeda and K. Fukui, “Inclusion of mother liquor inside KDP crystals in a continuous MSMPR crystallizer,” J. Sep. Purif. Technol., Vol. 43, No.1, 2005, pp. 71-76.
[20] Y. Asakuma, T. Terashima, K. Maeda and K. Fukui, “Attrition behavior by micro-hardness parameter in suspension crystallization processes,” J. Powder Technol., Vol. 171, 2007, pp. 75-80.
[21] V.W. Uhl and J.B. Gray, “Mixing-Theory and Practice,” Academic Press, New York, 1966.
[22] M. Naga-shima, K. Takegami, H. Takiyama and M. Matsuoka, “Me-chanisms of purification of crystalline particles in an inclined column crystallizer,” Proceedings of the 14th International Symposium on Industrial Crystallization, Cambridge, 12-16 September 1999, pp. 1861-1871.

Copyright © 2024 by authors and Scientific Research Publishing Inc.

Creative Commons License

This work and the related PDF file are licensed under a Creative Commons Attribution 4.0 International License.