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In this paper, thermal processing of starch slurry in a Couette-Taylor flow (CTF) apparatus was investigated. Gelatinized starch dispersion, after treatment in the CTF apparatus, was characterized using such parameters like starch granule diameters (or average diameter), starch granule swelling degree (quantifying the amount of water absorbed by starch granules) and concentration of dissolved starch. These parameters were affected mostly by the process temperature, although the impact of the axial flow or rotor rotation on them was also observed. Moreover, the analysis of results showed a relatively good correlation between these parameters, as well as, between those parameter and apparent viscosity of gelatinized starch dispersion. Meanwhile, the increase in the value of the apparent viscosity and in shear-tinning behaviour of dispersion was associated with the progress of starch processing in the CTF apparatus. Finally, the CTF apparatuses of different geometries were compared using numerical simulation of the process. The results of the simulation indicated that the apparatus scaling-up without increasing the width of the gap between cylinders results in higher mechanical energy consumption per unit of processed starch slurry.
Czasopismo
Rocznik
Tom
Strony
345--361
Opis fizyczny
Bibliogr. 17 poz., tab., rys.
Twórcy
autor
- Warsaw University of Technology, Faculty of Chemical and Process Engineering, ul. Waryńskiego 1, 00-645 Warszawa, Poland
autor
- University of Shizuoka, School of Food and Nutritional Science, 52-1 Yada, Suruga, Shizuoka 422- 8526, Japan
- Kobe University, Graduate School of Engineering, Department of Chemical Science and Engineering, 1-1 Rokkodai, Nada, Kobe 657-8501, Japan
autor
- Kobe University, Graduate School of Engineering, Department of Chemical Science and Engineering, 1-1 Rokkodai, Nada, Kobe 657-8501, Japan
autor
- Kobe University, Graduate School of Engineering, Department of Chemical Science and Engineering, 1-1 Rokkodai, Nada, Kobe 657-8501, Japan
Bibliografia
- 1. Baks T., Ngene I.S., Van Soest J.J.G., Janssen A.E.M., Boom R.M., 2007. Comparison of methods to determine the degree of gelatinisation for both high and low starch concentrations. Carbohydr. Polym., 67, 481–490. DOI: 10.1016/j.carbpol.2006.06.016.
- 2. Brandam C., Meyer X. M., Proth J., Strehaiano P., Pinguad H., 2003. A original kinetic model for the enzymatic hydrolysis of starch during mashing. Biochem. Eng. J., 13, 43-52. DOI: 10.1016/S1369-703X(02)00100-6.
- 3. Dłuska E., Markowska-Radomska A., 2010. Regimes of multiple mmulsions of W-1/O/W-2 and O-1/W/O-2 type in the continuous Couette-Taylor flow contactor. Chem. Eng. Technol., 33, 113-120. DOI: 10.1002/ceat.200900278.
- 4. Dłuska E., Hubacz R., 2000. Mass transfer in the two-phase helicoidal contactor. Inż. Chem. Proces., 21, 1, 103- 113.
- 5. Hellwig Z., 1998. Elementy rachunku prawdopodobieństwa i statystyki matematycznej. 13th edition, WNT, Warszawa.
- 6. Hubacz R., Buczyńska M., 2011. Starch gelatinisation in Couette-Taylor flow apparatus. Chem. Process Eng., 32, 267-279. DOI: 10.2478/v10176-011-0021-7.
- 7. Hubacz R., Ohmura N., Dluska E., 2013. Intensification of starch processing using apparatus with Couette–Taylor flow. J. Food Process Eng., 36, 6, 774-785. DOI: 10.1111/jfpe.12046.
- 8. Hubacz R., Masuda H., Horie T., Ohmura N., 2016. Starch granules swelling during gelatinization in Couette-Taylor flow apparatus. Proceedings of the 22nd of Chemical and Process Engineering. Spała, Poland, 5-9 September 2016, 435-444.
- 9. Lagarrigue S., Alvarez G., Cuvelier G., Flick D., 2008. Swelling kinetics of waxy maize and maize starches at high temperatures and heating rates. Carbohydr. Polym., 73, 148-155. DOI: 10.1016/j.carbpol.2007.11.018.
- 10. Malumba P., Jacquet N., Delimme G., Lefebvre F., Bera F., 2013. The swelling behaviour of wheat starch granules during isothermal and non-isothermal treatments. J. Food Eng., 114, 199-206. DOI: 10.1016/j.jfoodeng.2012.08.010.
- 11. Mayra Q.-P., Kim W.-S., 2015. Agglomeration of Ni-Rich hydroxide in reaction crystallization: Effect of Taylor vortex dimension and intensity. Cryst. Growth Des., 15, 1726-1734. DOI: 10.1021/cg501727v.
- 12. Masuda H., Horie T., Hubacz R., Ohmura N., 2013. Process intensification pf continuous starch hydrolysis with a Taylor-Couette flow reactor. Chem. Eng. Res. Des., 91,11, 2259-2264. DOI: 10.1016/j.cherd.2013.08.026.
- 13. Patel B. K., Seetharaman K., 2006. Effect of heating rate on starch granule morphology and size. Carbohydr. Polym., 65, 381-385. DOI: 10.1016/j.carbpol.2006.01.028.
- 14. Ramezani M., Kong B., Gao X., Olsen M.G., Vigil R.D., 2015. Experimental measurement of oxygen mass transfer and bubble size distribution in and air-water multiphase Taylor-Couette vortex bioreactor. Chem. Eng. J., 279, 286-296. DOI: 10.1016/j.cej.2015.05.007.
- 15. Rao M.A., Okechukwu P.E., Da Silva P.M.S., Oliveira J.C., 1997. Rheological behaviour of heated starch dispersions in excess water: role of starch granule. Carbohydr. Polym., 33, 273-283. DOI: 10.1016/S0144- 8617(97)00025-8.
- 16. Sakonidou E.P., Karapantsios T.D., Raphaelides S.N., 2003. Mass transfer limitations during starch gelatinization. Carbohydr. Polym., 53, 53-61. DOI: 10.1016/S0144-8617(03)00010-9.
- 17. Singh N., Singh S., Isono, N., Noda T., Singh A. M., 2009. Diversity in amylopectin structure, thermal and pasting properties of starches from wheat varieties/lines. Int. J. Bio Macromol. 45, 298-304. DOI: 10.1016/j.ijbiomac.2009.06.005.
Uwagi
PL
Opracowanie ze środków MNiSW w ramach umowy 812/P-DUN/2016 na działalność upowszechniającą naukę (zadania 2017)
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-380585ae-8867-4f78-ac14-acf4d592941b