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3 Turbulence : international journal

3 2005

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Optoelectronic measuring system for assessment of the annular two-phase gas-very viscous liquid flow

Witczak S., Czernek K.

Turbulence : international journal

2005

Vol. 11

25-33

The paper presents the results of tests and theoretical considerations on assessment of hydrodynamics of a cocurrent annular downward flow of a very viscous liquid and a gas in vertical pipes. Measurement methods have been presented; special attention was paid to the optoelectronic measuring system. Systematic of flow patterns has been discussed and some chosen quantities characterizing flowing liquid films of high viscosity have been described.

Investigations on film thickness of a very viscous liquid in its flow with gas

Czernek K., Witczak S.

Turbulence : international journal

2005

Vol. 11

247-249

The paper presents the results of tests and theoretical considerations concerning determination of the liquid film thickness under the cocurrent two-phase downward flow of gas and very viscous liquid. Influence of viscosity changes on undulation of the liquid film surface and changes of its thickness has been determined. Relationships for determination of the flowing liquid film thickness in the two-phase gas-liquid flows have been formulated.

Experimental investigation of a liquid film formed by impingement of an axisymmetric jet on a flat heated surface

Bykuć S.

Turbulence : international journal

2005

Vol. 11

235-237

The aim of the present work was to study experimentally hydrodynamic and heat transfer characteristics of the flow of a liquid film over a surface. A round jet of water impinging vertically on a horizontal plane forms a thin film flowing radially until the sudden increase of depth occurs (hydraulic jump). During the experiment, the temperature of the solid surface and liquid film thickness in the suhcritical region (downstream of the hydraulic jump) and supercritical region (upstream of the hydraulic jump) were measured. Radial film thickness and Nusselt number distributions were achieved. Experiments were performed for a range of flow rates between 0.3 and 0.8 I/min. The liquid film thickness upstream of the hydraulic jump was an order of magnitude smaller than that of the subcritical region. With the growth of the flow rate, the radius of the hydraulic jump and film thickness after the jump, increased. It was found that the local Nusselt number reached maximum near the stagnation region and decreases gradually with radius as the flow moves downstream with the biggest drop corresponding to the location of hydraulic jump. Downstream of the jump, Nu was approximately uniform. Higher Nusselt numbers were reached for higher flow rates. These differences for various flow rates were much bigger in the supercritical region than that in the subcritical one.