Abstract
Vaporization process of single drops of pentane or furan in an aqueous glycerol has been studied photographically in the region where the geometrically simple configuration and rectilinear motion of vaporizing two-phase bubbles are realized. The instantaneous velocity of rise of two-phase bubbles agreed approximately with Stokes' theory in the range Re < 1. The liquid-liquid interfacial area takes almost a constant value slightly higher than the initial surface area of the liquid drop in the range below 10% of the vaporization ratio, and then reduces gradually. The vaporization does not bring an effective increase of heat transfer area.
Zusammenfassung
Der Verdampfungsvorgang einzelner Tropfen von Pentan und Furan in wässeriger Glyzerinlösung wurde photographisch in einem Bereich untersucht, in dem die geometrisch einfache Form und geradlinige Bewegung der verdampfenden zweiphasigen Blasen vorherrschen. Im Bereich Re < 1 stimmt die nichtstationäre Aufstiegsgeschwindigkeit der zweiphasigen Blasen mit der Stokes-Theorie überein. Die Grenzfläche flüssig-flüssig nimmt unterhalb einer 10 % igen Verdampfung einen fast konstanten Wert an, etwas höher als die ursprüngliche flüssige Tropfenoberfläche, und nimmt dann schrittweise ab. Die Verdampfung ergibt keine wirksame Erhöhung der wärmeübertragenden Oberfläche.
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Abbreviations
- A:
-
total surface area of two-phase bubble
- AL :
-
liquid-liquid interfacial area of two-phase bubble
- D:
-
equivalent spherical diameter of two-phase bubble
- Di :
-
initial drop diameter
- g:
-
acceleration of gravity
- L:
-
equivalent spherical diameter of horizontal cross section of upper column
- Ma :
-
mass of air
- Md :
-
mass of dispersed-phase component
- Mdl :
-
mass of dispersed-phase component in liquid phase
- Mdv :
-
mass of dispersed-phase component in vapor phase
- Re:
-
=UD/νc
- ΔT∞ :
-
nominal temperature difference
- U:
-
velocity of rise
- U∞ :
-
velocity of rise in infinite liquid medium
- β:
-
half opening angle of vapor phase in two-phase bubble
- μc :
-
viscosity of continuous-phase liquid
- μdl :
-
viscosity of dispersed-phase component in liquid phase
- μdv :
-
viscosity of dispersed-phase component in vapor phase
- νc :
-
kinematic viscosity of continuous-phase liquid
- ξ:
-
vaporization ratio
- ρa :
-
density of air
- ρc :
-
density of continuous-phase liquid
- ρdl :
-
density of dispersed-phase component in liquid phase
- ρdv :
-
density of dispersed-phase component in vapor phase
- σc :
-
surface tension of continuous-phase liquid
- σd :
-
surface tension of dispersed-phase liquid
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Tochitani, Y., Mori, Y.H. & Komotori, K. Vaporization of single liquid drops in an immiscible liquid Part I: Forms and motions of vaporizing drops. Warme- und Stoffubertragung 10, 51–59 (1977). https://doi.org/10.1007/BF02570666
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DOI: https://doi.org/10.1007/BF02570666