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Przedmiotem badań, których wyniki przedstawiono w pracy, są zjawiska rozpadu i koalescencji wpływające na rozkład wielkości kropel. Rozważono dyspersje wytwarzane w mieszalnikach w warunkach przepływu burzliwego. W pierwszych rozdziałach pracy zaprezentowano sposób analizy układów rozproszonych w przestrzeni fazowej oraz przedstawiono opis mikrostruktury burzliwości. Przedyskutowano różnicę pomiędzy klasyczną teorią burzliwości Kołmogorowa opartą na uśrednionych statystycznie własnościach burzliwości i podejściem multifraktalnym uwzględniającym intermitentną naturę turbulencji. Zasadniczą część pracy stanowią rozdziały 4 i 5 poświęcone odpowiednio rozpadowi i koalescencji kropel. Każdy z nich zawiera krótki przegląd i dyskusję koncepcji modelowania rozważanego procesu oraz przedstawienie modeli własnych. Zaproponowane modele rozpadu i koalescencji kropel sformułowano przy użyciu formalizmu multifraktalnego. Zastosowane podejście pozwoliło uwzględnić różną aktywność wirów burzliwych o tej samej skali, a także w sposób naturalny wprowadzić do zależności na szybkość rozpadu, częstość zderzeń kropel i szybkość wypływu filmu fazy ciągłej spomiędzy kropel, wpływ dużych wirów energetycznych, a więc i wpływ skali układu. Prócz niehomogeniczności małej skali związanej z intermi-tencją wewnętrzną uwzględniono nierównomierny rozkład uśrednionych lokalnie parametrów burzliwości w mieszalniku. Zaproponowane modele rozpadu i koalescencji zweryfikowano doświadczalnie wykorzystując zarówno wyniki badań własnych, jak i zaczerpnięte z literatury. Przedstawiono zastosowania praktyczne sformułowanych modeli do przewidywania ewolucji rozkładów wielkości kropel w czasie i efektów powiększania skali układu. Zdefiniowano również indeksy dla inwersji faz.
The phenomena of breakup and coalescence, which affect the drop size distribution, are the core subject of investigations presented in this work. Liquid-liquid dispersion, created in stirred tanks, operating in a turbulent regime, are also considered. Initially, an analysis of dispersed systems in the phase space and a description of micro-structure of turbulence are presented. The differences between classical Kolmogorov theory, based on statistically averaged properties of turbulence, and the multifractal approach, taking into account the intermittent character of turbulence are discussed. Chapters 4 and 5 focus on droplet breakup and coalescence, respectively, which constitutes the main part of the work. A brief review and discussion of the modeling concepts of the process being considered, as well as a presentation of the author's own models, are contained in each of these chapters. The proposed models of drop breakup and coalescence were formulated with the use of multifractal formalism. Such an approach enables us to take into account different activity of turbulent eddies of the same scale, and to introduce the influence of large energetic eddies (and therefore influence of the system scale) on drop breakup rate, drop collision frequency and the rate of film drainage. Apart from small scale irregularity relating to the internal intermittency, the non-uniform distribution of locally averaged properties of turbulence in the tank were taken into account. The proposed models of drop breakup and coalescence were verified using both primary and secondary data. Practical applications of the formulated models to predict the time evolution of drop size distribution and the effects of scaling-up were presented. Phase inversion indices were also defined and these can be used in the analysis of the phase inversion process.
Rocznik
Tom
Strony
3--264
Opis fizyczny
Bibliogr. 354 poz., tab., rys., wykr.
Twórcy
autor
- Zakład Mechaniki Technicznej i Dynamiki Stosowanej, Wydział Inżynierii Chemicznej i Procesowej Politechniki Warszawskiej tel: 234 65 94, podgorsw@ichip.pw.edu.pl
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