ArticleName |
Population balance of aluminate solution decomposition: physical modelling and model setup |
ArticleAuthorData |
RUSAL Engineering-Technical Center, Saint Petersburg, Russia:
V. O. Golubev, Head of the Mathematical Modelling Department, e-mail: Vladimir.Golubev2@rusal.com D. G. Chistyakov, Leading Engineer at the Mathematical Modelling Department, e-mail: Dmitriy.Chistiakov@rusal.com
Saint Petersburg Mining University, Saint Petersburg, Russia: V. N. Brichkin, Head of the Department of Metallurgy, e-mail: Brichkin_VN@pers.spmi.ru M. F. Postika, Undergraduate Student, e-mail: kafmet@spmi.ru |
Abstract |
Population balance modelling is the most developed technique for modelling the process of aluminate solution decomposition induced by aluminium hydroxide, and it is of great scientific and practical relevance. Through solving the population balance equation one can track how the process conditions influence the decomposition parameters, which include: degree of decomposition, solids in the slurry, alumina/caustic ratio, particle size distribution of the deposit, etc. Periodic and half-periodic experiments are applied to set up the functional relationships that dictate the growth rate, as well as the nucleation and granulation intensities in that equation. Using physical experiment and mathematical modelling, the authors demonstrate that agitation in a big lab reactor (5 litres) is far from being ideal and is characterized with significant fluctuations in the slurry density. This effect causes significant deviations from the population balance provisions and may affect the accuracy of predicted decomposition parameters. The authors conducted a laboratory study that looked at the decomposition process in an environment simulating the industrial regime of decomposing high-modulus aluminate solutions adopted by in-country plants that rely on Bayer process. The authors found a huge difference between the process in view and a layer-by-layer growth of the seed, a low relevance of the granulation stage and a high rate of secondary nucleation. A big discrepancy was found between the experimental data and the model analysis data at the initial stage of an hour-long decomposition process after the seed had been charged. Such discrepancy is due to an induction period. All the other simulation results proved to be acceptable in terms of accuracy. The method of physical modelling integrated with population balance modelling proved to be generally acceptable for experimental data description and analysis regardless of the original state of the system. At the same time the method requires further development so that it could produce consistent descriptions of all the stages and regimes of decomposition. This research was funded by the Russian Science Foundation under the Agreement No. 18-19-00577 dated April 26, 2018 on granting funds for basic and exploratory research. |
References |
1. Golubev V. O., Chistiakov D. G., Brichkin V. N., Litvinova T. E. Systems and aids mathematical modeling of the alumina refinery methods: problems and solutions. Non-ferrous Metals. 2019. No. 1. pp. 40–47. DOI: 10.17580/nfm.2019.01.07 2. Sweegers C., de Coninck H. C., Meekes H., van Enckevort W. J. P., Hiralal I. D. K., Rijkeboer A. Morphology, evolution and other characteristics of gibbsite crystals grown from pure and impure aqueous sodium aluminate solutions. Journal of Crystal Growth. 2001. Vol. 233. pp. 567–582. 3. Brichkin V. N., Kremcheeva D. A., Matveev V. A. The quantitative effect of the seed on the batch crystallization of chemical deposits. Zapiski Gornogo instituta. 2015. Vol. 211. pp. 64–70. 4. Prokopov I. V. The efficiency of recirculating alkali in alumina production. Tsvetnye Metally. 2017. No. 9. pp. 59–62. 5. Anisonyan K. G., Kopyev D. Yu., Olyunina T. V., Sadykhov G. B. Influence of Na2CO3 and CaCO3 additions on the aluminate slag formation during a single-stage reducing roasting of red mud. Non-ferrous Мetals. 2019. No. 1. DOI: 10.17580/nfm.2019.01.03 6. Dubovikov O. A., Brichkin V. N., Ris A. D., Sundurov A. V. Thermochemical activation of hydrated aluminosilicates and its importance for alumina production. Non-ferrous Мetals. 2018. No. 2. DOI: 10.17580/nfm.2018.02.02 7. Loginova I. V., Shoppert A. A., Kryuchkov E. Yu. Kinetics investigation and optimal parameters of alumina extraction during the Middle Timan bauxites leaching. Tsvetnye Metally. 2018. No. 1. pp. 63–68. DOI: 10.17580/tsm.2018.01.08 8. Ramkrishna D. Population balances. Theory and Applications to Particulate Systems in Engineering. London : Academic Press, 2000. 355 p. 9. Livk I., Ilievski D. A macroscopic agglomeration kernel model for gibbsite precipitation in turbulent and laminar flows. Chemical Engineering Science. 2007. Vol. 62. pp. 3787–3797. 10. Li T. S., Rohl A. L., Ilievski D. Modelling non-stationary precipitation systems: sources of error and their propagation. Chemical Engineering Science. 2000. Vol. 55. pp. 6037–6047. 11. Stoykov S., Margenov S. Scalable parallel implementation of shooting method for large-scale dynamical systems. Application to bridge components. Journal of Computational and Applied Mathematics. 2015. Vol. 293. pp. 223–231. 12. Litster J. D., Smit D. J., Hounslow M. J. Adjustable Discretized Population Balance for Growth and Aggregation. AlChE Journal. 1995. Vol. 41, No. 3. pp. 591–603. 13. Bramley A. S., Hounslow M. J., Ryall R. L. Aggregation during Precipitation from Solution: A Method for Extracting Rates from Experimental Data. Journal of Colloid and Interface Science. 1996. Vol. 183. pp. 155–165. 14. Nocedal J., Wright S. J. Numerical Optimization. Second Edition. Springer, Berlin : 2006. 664 p. 15. White E. T., Bateman S. H. Effect of caustic concentration on the growth rate of Al(OH)3 particles. Light Metals 1988 : Proceedings of the technical sessions presented by the TMS Aluminum Committee at the 177th TMS annual meeting. Phoenix,1988. pp. 157–162. 16. Misra C. The precipitation of Bayer aluminiumtrihydroxide. Ph.D. thesis, University of Queensland, Australia, 1970. 236 p. 17. Freij S. J., Parkinson G. M. Surface morphology and crystal growth mechanism of gibbsite in industrial Bayer liquors. Hydrometallurgy. 2005. Vol. 78. pp. 246–255. 18. Brichkin V. N., Kraslawski A. Isothermal transition of metastable aluminate solutions into the unstable region and its potential industrial application. Zapiski Gornogo instituta. 2016. Vol. 217. pp. 80–87. |