Hydrodynamic and kinetic processes of the mineral fertilizer granules encapsulating in the multistage device with suspended layer

Authors

DOI:

https://doi.org/10.15587/1729-4061.2016.84179

Keywords:

granulation, many-stage apparatus with the suspended layer, perforated shelf, organic suspension, entrainment

Abstract

One explained the possibility of reducing economic and environmental indicators in the production of mineral fertilizers by covering their surface with the protective coating (capsule), which creates additional resistance to mass transfer in the process of fertilizer dissolving. It is proved that the use of organic suspensions as a material for the capsule shell is very promising.

Using a many-stage countercurrent contact of a fluidizing agent and dispersed phase in the fluidized bed during the heat exchange process is a perspective way of reducing economic and energy costs. Therefore, in order to reduce the cost of processing wet materials and increase the uniformity of particle size distribution of the final product one offered to carry out the process of granules coating with organic substance in a many-stage shelf apparatus with the suspended layer.

One defined structural features of the shelf device classification section and experimentally established influence of the shelf length and degree of its perforation on the process of the fine fraction entrainment. Fine fraction entrainment is reducing with the increase of the shelf length. Also, pneumatic classification process of the material for the shelves with open area up to 5 % is more intense than for the shelves with open area of more than 15 %.

The kinetics of mineral granules enlargement during their encapsulation with organic suspension is experimentally and theoretically studied. It was found out that in the process of encapsulation the curve of particle size distribution has one typical maximum. It confirms the theory of uniform enlargement of granule surface, when organic substance is fixed on the particle surface in the form of a solid layer and no shearing of the granule coating takes place. It enables to obtain the complete organic shell (capsule) on the mineral granules surface.

One studied the transfer of material flows in the individual stages of the apparatus granulation section. A mathematical model of the granulation kinetics in the many-stage shelf apparatus, which takes into account changes of granules distribution density as to their sizes in each contact stage is developed. The resulting model is characterized by a cell structure in which the material flow is seen as divided into a number of series-connected zones, wherein different granulation modes are implemented.

Author Biographies

Mykola Yukhymenko, Sumy State University Rymskogo-Korsakova str., 2, Sumy, Ukraine, 40007

PhD, Associate Professor

Department of Processes and Equipment of Chemical and Petroleum-Refineries 

Ruslan Ostroga, Sumy State University Rymskogo-Korsakova str., 2, Sumy, Ukraine, 40007

PhD, Associate Professor

Department of Processes and Equipment of Chemical and Petroleum-Refineries 

Artem Artyukhov, Sumy State University Rymskogo-Korsakova str., 2, Sumy, Ukraine, 40007

PhD, Associate Professor

Department of Processes and Equipment of Chemical and Petroleum-Refineries 

References

  1. Jarchow, M. E., Liebman, M. (2012). Nitrogen fertilization increases diversity and productivity of prairie communities used for bioenergy. GCB Bioenergy, 5 (3), 281–289. doi: 10.1111/j.1757-1707.2012.01186.x
  2. Khiari, L., Parent, L. E. (2005). Phosphorus transformations in acid light-textured soils treated with dry swine manure. Canadian Journal of Soil Science, 85 (1), 75–87. doi: 10.4141/s03-049
  3. Ostroha, R. O., Yukhymenko, M. P., Mikhajlovskiy, Ya. E., Litvinenko, A. V. (2016). Technology of Producing Granular Fertilizers on the Organic Basis. Eastern-European Journal of Enterprise Technology, 1 (6 (79)), 19–26. doi: 10.15587/1729-4061.2016.60314
  4. Scialabba, N. E.-H., Müller-Lindenlauf, M. (2010). Organic agriculture and climate change. Renewable Agriculture and Food Systems, 25 (02), 158–169. doi: 10.1017/s1742170510000116
  5. Hu, X., Cunningham, J. C., Winstead, D. (2008). Study growth kinetics in fluidized bed granulation with at-line FBRM. International Journal of Pharmaceutics, 347 (1-2), 54–61. doi: 10.1016/j.ijpharm.2007.06.043
  6. Sheng, T. C., Sulaiman, S. A., Kumar, V. (2012). One-Dimensional Modeling of Hydrodynamics in a Swirling Fluidized Bed. International Journal of Mechanical & Mechatronics Engineering, 12 (6), 13–22.
  7. Gupta, S. K., Singhvi, I. J., Shirsat, M. K., Karwani, G., Agarwal, A., Aditi (2011). Microencapsulation techniques and its application in pharmaceutical. Asian Journal of Pharmaceutical Sciences and Clinical Research, 1 (3), 67–77.
  8. Saikh, M. A. (2013). A technical note on granulation technology: a way to optimise granules. International Journal of Pharmaceutical Sciences Review and Research, 4, 55–67.
  9. Grimmett, E. S. (1964). Kinetics of particle growth in the fluidized bed calcination process. AIChE Journal, 10 (5), 717–722. doi: 10.1002/aic.690100527
  10. Malovanyi, M. S., Nahurskyi, O. A., Bunko, V. Ya., Druziuk, V. M. (2012). Teplomasoobmin protsesu kapsuliuvannia mineralnykh dobryv vodnym rozchynom plivkoutvoriuiuchoi kompozytsii palyhorskit – meliasa. Visnyk Kremenchutskoho NU im. Mykhaila Ostrohradskoho, 2 (74), 117–120.
  11. Kornienko, Y., Sachok, R., Rayda, V., Tsepkalo, O. (2009). Mathematical modeling of continuous formation of multilayer humic-mineral solid composites. Chemistry & Chemical Technology, 4, 335–338.
  12. Caiyuan, Y., Tao, Q., Xizhong, W. (2004). Heat and mass transfer in process of fluidized bed spray granulation. Chinese Journal of Chemical Engineering, 16 (6), 836–839.
  13. Patel, P., Telange, D., Sharma, N. (2011). Comparison of Different Granulation Techniques for Lactose Monohydrate. International Journal of Pharmaceutical Sciences and Drug Research, 3, 222–225.
  14. Agrawal, R., Naveen, Y. (2011). Pharmaceutical Processing – A Review on Wet Granulation Technology. International Journal of Pharmaceutical Frontier Research, 1, 65–83.
  15. Sklabinskyi, V. I., Artyukhov, A. E. (2013). Opitno-promishlennoe vnedrenye protsessa poluchenyia porystoi ammyachnoi selytri v vykhrevikh hranuliatorakh. Naučnij vestnyk Nacyonaĺnoho hornoho unyversyteta, 6, 42–48.
  16. Artyukhov, A. E., Fursa, A. S., Moskalenko, K. V. (2015). Classification and Separation of Granules in Vortex Granulators. Chemical and Petroleum Engineering, 51 (5-6), 311–318. doi: 10.1007/s10556-015-0044-x
  17. Kaewklum, R., Kuprianov, V. I. (2010). Experimental studies on a novel swirling fluidized-bed combustor using an annular spiral air distributor. Fuel, 89 (1), 43–52. doi: 10.1016/j.fuel.2009.07.027
  18. Ashcraft, R. W., Heynderickx, G. J., Marin, G. B. (2012). Modeling fast biomass pyrolysis in a gas–solid vortex reactor. Chemical Engineering Journal, 207-208, 195–208. doi: 10.1016/j.cej.2012.06.048
  19. Khalatov, A. A. (2010). Heat transfer and hydrodynamics in the fields of mass forces. Journal of Engineering Physics and Thermophysics, 83 (4), 794–808. doi: 10.1007/s10891-010-0397-0
  20. Artyukhov, A. E., Sklabinskyi, V. I. (2015). Hydrodynamics of gas flow in small-sized vortex granulators in the production of nitrogen fertilizers. Chemistry & Chemical Technology, 9 (3), 337–342.
  21. Artyukhov, A. E., Voznyi, A. A. (2016). Thermodynamics of the vortex granulator's workspace: the impact on the structure of porous ammonium nitrate. Proc. Int. Conf. NAP–2016, 5 (2).
  22. Artyukhov, A. E. (2016). Kinetics of heating and drying of porous ammonium nitrate granules in the vortex granulator. Proc. Int. Conf. NAP–2016, 5 (2).
  23. Kaewklum, R., Kuprianov, V. I., Douglas, P. L. (2009). Hydrodynamics of air–sand flow in a conical swirling fluidized bed: A comparative study between tangential and axial air entries. Energy Conversion and Management, 50 (12), 2999–3006. doi: 10.1016/j.enconman.2009.07.019
  24. Volchkov, E. P., Dvornikov, N. A., Lukashov, V. V., Abdrakhmanov, R. K. (2013). Investigation of the flow in the vortex chamber with centrifugal fluidizing bed with and without combustion. Thermophysics and Aeromechanics, 20 (6), 663–668. doi: 10.1134/s0869864313060024
  25. Dvornikov, N. A., Belousov, P. P. (2011). Investigation of a fluidized bed in a vortex chamber. Journal of Applied Mechanics and Technical Physics, 52 (2), 206–211. doi: 10.1134/s0021894411020076
  26. Ostroha, R. O. (2014). Kinetyka kapsuliuvannia hranuliovanych mineraĺnych dobryv orhaničnoju obolonkoju. Visnyk NTU ChPI: Novi rišennia v sučasnych technolohijach, 7 (1050), 146–151.
  27. Yukhymenko, M. P., Vakal, S. V., Kononenko, M. P., Filonov, A. P. (2003). Aparaty zavisloho sharu. Teoretychni osnovy i rozrahunok. Sumy: Sobor, 304.

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Published

2016-12-20

How to Cite

Yukhymenko, M., Ostroga, R., & Artyukhov, A. (2016). Hydrodynamic and kinetic processes of the mineral fertilizer granules encapsulating in the multistage device with suspended layer. Eastern-European Journal of Enterprise Technologies, 6(6 (84), 22–28. https://doi.org/10.15587/1729-4061.2016.84179

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Section

Technology organic and inorganic substances