Experimental investigations of the parameters of the jet milk homogenizer with separate cream supply

Authors

DOI:

https://doi.org/10.15587/2312-8372.2017.103240

Keywords:

jet homogenizer, separate cream supply, cream supply channel, diameter of fat globules

Abstract

The jet milk homogenizer provides the cream supply in the right amount for normalization of the mixture, grinding of the fat globules and their uniform distribution in the volume of the milk plasma. In the process of technological audit, the following drawbacks are identified: lack of devices to maintain a constant temperature, low resolution of a digital camera and a microscope. In addition, it is necessary to investigate the nature of the influence of the flow and fat content of cream on the average size of fat globules.

In order to level out the identified drawbacks, it is planned to increase the time of the experiment in order to exclude the possible influence on the results at the initial and final stages of each experiment. In addition, at the next stage of the study, it is planned to determine the nature of the relationship between cream supply, fat content and average size of fat globules after homogenization.

The experimental studies of a jet milk homogenizer with a separate cream supply shows the values of the factors at which the grinding is carried out to the level of valve homogenizers. The average size of fat globules at a level of 0.85 microns is provided with a diameter of the cream supply channel equal to 0.6 mm and the distance of the central channel at the site of the maximal narrowing of 2 mm. It is determined that the nature of the relationship between the skim milk rate is the main factor of grinding and the average size of fat globules is directly proportional.

The nature of the relationship between decrease in the size of fat globules is determined as increase in skim milk rate, the nature of which can be explained by an increase in Weber's criterion. Its growth leads to an increase in the magnitude of the tangential stress, the extracted droplet in the ribbon-like body, which subsequently collapses into a large number of small elements. This confirms the hypothesis of destruction when creating the maximum phase rate difference realized in the design of a jet milk homogenizer with a separate cream supply.

Author Biographies

Alexandr Kovalyov, Tavria State Agrotechnological University, 18, B. Khmelnistskiy ave., Melitopol, Ukraine, 72312

Assistant

Department of Processing and Food Production Equipment

Kyrylo Samoichuk, Tavria State Agrotechnological University, 18, B. Khmelnistskiy ave., Melitopol, Ukraine, 72312

PhD, Associate Professor

Department of Processing and Food Production Equipment

Nadiya Palyanichka, Tavria State Agrotechnological University, 18, B. Khmelnistskiy ave., Melitopol, Ukraine, 72312

PhD, Associate Professor

Department of Processing and Food Production Equipment

Valentуna Verkholantseva, Tavria State Agrotechnological University, 18, B. Khmelnistskiy ave., Melitopol, Ukraine, 72312

PhD, Associate Professor

Department of Processing Equipment and Food Equipment

Valeriy Yanakov, Tavria State Agrotechnological University, 18, B. Khmelnistskiy ave., Melitopol, Ukraine, 72312

PhD, Senior Lecturer

Department of Processing and Food Production Equipment

References

  1. Fialkova, E. A. (2006). Gomogenizatsiia. Novyi vzgliad. St. Petersburg: GIORD, 392.
  2. Walstra, P., Wouters, J. T. M., Geurts, T. J. (2005). Homogenization. Dairy Science and Technology. Ed. 2. CRC Press, 279–298. doi:10.1201/9781420028010.ch9
  3. Pickering, C. J. D., Halliwell, N. A. (1984). Laser speckle photography and particle image velocimetry: photographic film noise. Applied Optics, 23 (17), 2961–2969. doi:10.1364/ao.23.002961
  4. Feigl, K., Megias-Alguacil, D., Fischer, P., Windhab, E. J. (2007). Simulation and experiments of droplet deformation and orientation in simple shear flow with surfactants. Chemical Engineering Science, 62 (12), 3242–3258. doi:10.1016/j.ces.2007.02.008
  5. Innings, F., Tragardh, C. (2005). Visualization of the Drop Deformation and Break-Up Process in a High Pressure Homogenizer. Chemical Engineering & Technology, 28 (8), 882–891. doi:10.1002/ceat.200500080
  6. Samoichuk, K. O. (2008). Obgruntuvannia parametriv ta rezhymiv roboty protytechiino-strumenevoho dysperhatora moloka. Donetsk, 20.
  7. Deinychenko, G., Samoichuk, K., Kovalyov, O. (2016). Constructions of jet mixing dispergators of milk fat phase. Pratsi Tavriiskoho derzhavnoho ahrotekhnolohichnoho universytetu, 16 (1), 219–228.
  8. Samoichuk, K., Kovalyov, O., Sultanova, V. (2015). The quality and the energy efficiency in a jet – mixing homogenization of milk process with the separated giving of creams. Pratsi Tavriiskoho derzhavnoho ahrotekhnolohichnoho universytetu, 15 (1), 241–249.
  9. Stankiewicz, A. I., Moulijn, J. A. (2000, January). Process Intensification: Transforming Chemical Engineering. Chemical Engineering Progress, 20–34.
  10. Glasgow, I., Aubry, N. (2003). Enhancement of microfluidic mixing using time pulsing. Lab Chip, 3 (2), 114–120. doi:10.1039/b302569a
  11. Kessler, H. G. (2002). Food and Bio Process Engineering Dairy Technology. Ed. 5. Germany, Munchen: Verlag A. Kessler (Publishing House A. Kessler), 694.
  12. Vankova, N., Tcholakova, S., Denkov, N. D., Ivanov, I. B., Vulchev, V. D., Danner, T. (2007). Emulsification in turbulent flow. Journal of Colloid and Interface Science, 312 (2), 363–380. doi:10.1016/j.jcis.2007.03.059
  13. In: Teknotext AB. (1995). Chapter 6.3. Homogenizers. Dairy Processing Handbook. Lund, Sweden: Tetra Pak Processing Systems AB, 115–122.
  14. Liao, Y., Lucas, D. (2009). A literature review of theoretical models for drop and bubble breakup in turbulent dispersions. Chemical Engineering Science, 64 (15), 3389–3406. doi:10.1016/j.ces.2009.04.026
  15. Bothe, D., Stemich, C., Warnecke, H.-J. (2006). Fluid mixing in a T-shaped micro-mixer. Chemical Engineering Science, 61 (9), 2950–2958. doi:10.1016/j.ces.2005.10.060
  16. Chung, C. K., Shih, T. R. (2007). Effect of geometry on fluid mixing of the rhombic micromixers. Microfluidics and Nanofluidics, 4 (5), 419–425. doi:10.1007/s10404-007-0197-9
  17. Cortes-Quiroz, C. A., Azarbadegan, A., Zangeneh, M. (2017). Effect of channel aspect ratio of 3-D T-mixer on flow patterns and convective mixing for a wide range of Reynolds number. Sensors and Actuators B: Chemical, 239, 1153–1176. doi:10.1016/j.snb.2016.08.116
  18. Fani, A., Camarri, S., Salvetti, M. V. (2013). Investigation of the steady engulfment regime in a three-dimensional T-mixer. Physics of Fluids, 25 (6), 064102. doi:10.1063/1.4809591
  19. Goullet, A., Glasgow, I., Aubry, N. (2006). Effects of microchannel geometry on pulsed flow mixing. Mechanics Research Communications, 33 (5), 739–746. doi:10.1016/j.mechrescom.2006.01.007
  20. Samoichuk, K. O., Kovalev, A. A., Bezditnyi, A. A. (2015). Modelirovanie protsessa struinoi gomogenizatsii moloka s razdel'noi podachei slivok. Vestnik MGUP, 2 (19), 69–76.

Published

2017-05-30

How to Cite

Kovalyov, A., Samoichuk, K., Palyanichka, N., Verkholantseva, V., & Yanakov, V. (2017). Experimental investigations of the parameters of the jet milk homogenizer with separate cream supply. Technology Audit and Production Reserves, 3(3(35), 33–38. https://doi.org/10.15587/2312-8372.2017.103240

Issue

Section

Food Production Technology: Original Research